流量积算仪检定系统
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.vs/FlowInstegrationMeter/v16/.suo
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.vs/NGToolsPC/config/applicationhost.config
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.vs/NGToolsPC/config/applicationhost.config
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.vs/NGToolsPC/v15/.suo
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AGA8_10/Detail.cs
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AGA8_10/Detail.cs
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AGA8_10/FlowCal.cs
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AGA8_10/FlowCal.cs
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AGA8_10/GB11062.cs
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AGA8_10/GB11062.cs
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using System;
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using System.Collections.Generic;
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using System.Text;
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namespace NG_Tools
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{
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public class GB11062
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{
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int iNCC;// number of components
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int[] aiCID = new int[21];// component IDs
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double[] dXi = new double[21];// mole fraction of component i
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Detail ptDetail;
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public GB11062()
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{
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ptDetail = new Detail();
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for (int i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++) dXi[i] = 0;
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}// Detail()
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public void Run(ref NG_Cal.GasPropsSTRUCT ptAGA10)
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{
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int i;
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// Check for gas composition change
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ptAGA10.bForceUpdate = (ptAGA10.bForceUpdate || ptDetail.compositionchange(ref ptAGA10));
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// assign component IDs and values
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if (ptAGA10.bForceUpdate)
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{
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iNCC = -1;
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for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
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{
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if (ptAGA10.adMixture[i] > 0.0)
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{
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iNCC = iNCC + 1;
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aiCID[iNCC] = i;
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dXi[iNCC] = ptAGA10.adMixture[i];
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}
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}
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iNCC = iNCC + 1;
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//calculate composition dependent quantities; ported from original
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//FORTRAN functions paramdl() and chardl()
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GasPropsCal(ref ptAGA10);
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}
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}
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void GasPropsCal(ref NG_Cal.GasPropsSTRUCT ptAGA10)
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{
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double[] adTableMri = new double[NG_Cal.NUMBEROFCOMPONENTS] { 16.0430, 28.0135, 44.0100, 30.0700, 44.0970, 18.0153, 34.0820, 2.0159, 28.0100, 31.9988, 58.1230, 58.1230, 72.1500, 72.1500, 86.1770, 100.2040, 114.2310, 128.2580, 142.2850, 4.0026, 39.9480 };
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double[] adTablePc = new double[NG_Cal.NUMBEROFCOMPONENTS] { 4.604, 3.399, 7.382, 4.88, 4.249, 22.118, 9.005, 1.297, 3.499, 5.081, 3.648, 3.797, 3.381, 3.369, 3.012, 2.736, 2.486, 0, 0, 0.2275, 4.876 };
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double[] adTableTc = new double[NG_Cal.NUMBEROFCOMPONENTS] { 190.55, 126.1, 304.19, 305.43, 369.82, 647.3, 373.5, 33.2, 132.92, 154.7, 408.13, 425.16, 460.39, 469.6, 507.4, 540.2, 568.76, 0, 0, 5.2, 150.82 };
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double[] adTableBzsx = new double[NG_Cal.NUMBEROFCOMPONENTS] { 15, 0, 0, 13, 9.5, 0, 45.5, 74.2, 74.2, 0, 8.4, 8.4, 8.3, 8.3, 7.7, 7.0, 0, 0, 0, 0, 0 };
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double[] adTableBzxx = new double[NG_Cal.NUMBEROFCOMPONENTS] { 5.0, 0, 0, 2.9, 2.1, 0, 4.3, 4.0, 12.5, 0, 1.8, 1.8, 1.4, 1.4, 1.2, 1.0, 0.96, 0, 0, 0, 0 };
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double[,] adTableZn = new double[3, NG_Cal.NUMBEROFCOMPONENTS]
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{{0.9976,0.9995,0.9933,0.99,0.9789,0.93,0.99,1.0006,0.9993,0.999,0.958,0.9572,0.9377,0.918,0.892,0.83,0.742,0.613,0.434,1.0005,0.999},
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{0.998,0.9997,0.9944,0.9915,0.9821,0.945,0.99,1.0006,0.9995,0.9992,0.968,0.965,0.948,0.937,0.913,0.866,0.802,0.71,0.584,1.0005,0.9992},
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{0.9981,0.9997,0.9944,0.992,0.9834,0.952,0.99,1.0006,0.9996,0.9993,0.971,0.9682,0.953,0.945,0.919,0.876,0.817,0.735,0.623,1.0005,0.9993}};
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double[,] adTableSqrtbj = new double[3, NG_Cal.NUMBEROFCOMPONENTS]
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{{0.049,0.0224,0.0819,0.1,0.1453,0.2646,0.1,-0.004,0.0265,0.0316,0.2049,0.2069,0.251,0.2864,0.3286,0.4123,0.5079,0.6221,0.7523,0.0006,0.0316},
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{0.0447,0.0173,0.0748,0.0922,0.1338,0.2345,0.1,-0.0048,0.0224,0.0283,0.1789,0.1871,0.228,0.251,0.295,0.3661,0.445,0.5385,0.645,0.0002,0.0283},
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{0.0436,0.0173,0.0728,0.0894,0.1288,0.2191,0.1,-0.0051,0.02,0.0265,0.1703,0.1783,0.2168,0.2345,0.2846,0.3521,0.4278,0.5148,0.614,0,0.0265}};
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double[,] adTableHhvMol = new double[4, NG_Cal.NUMBEROFCOMPONENTS]
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{{892.97,0,0,1564.34,2224.01,45.074,562.94,286.63,282.8,0,2874.2,2883.82,3535.98,3542.89,4203.23,4862.87,5522.4,6182.91,6842.69,0,0},
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{891.56,0,0,1562.14,2221.1,44.433,562.38,286.15,282.91,0,2870.58,2879.76,3531.68,3538.6,4198.24,4857.18,5516.01,6175.82,6834.9,0,0},
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{891.09,0,0,1561.41,2220.13,44.224,562.19,285.99,282.95,0,2869.38,2878.57,3530.24,3537.17,4196.58,4855.29,5513.88,6173.46,6832.31,0,0},
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{890.63,0,0,1560.69,2219.17,44.016,562.01,285.83,282.98,0,2868.2,2877.4,3528.83,3535.77,4194.95,4853.43,5511.8,6171.15,6829.77,0,0}};
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double[,] adTableLhvMol = new double[4, NG_Cal.NUMBEROFCOMPONENTS]
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{{802.82,0,0,1429.12,2043.71,0,517.87,241.56,282.8,0,2648.83,2658.45,3265.54,3272.45,3887.71,4502.28,5116.73,5732.17,6346.88,0,0},
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{802.69,0,0,1428.84,2043.37,0,517.95,241.72,282.91,0,2648.42,2657.6,3265.08,3272,3887.21,4501.72,5116.11,5731.49,6346.14,0,0},
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{802.65,0,0,1428.74,2043.23,0,517.97,241.76,282.95,0,2648.26,2657.45,3264.89,3271.83,3887.01,4501.49,5115.87,5731.22,6345.85,0,0},
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{802.6,0,0,1428.64,2043.11,0,517.99,241.81,282.98,0,2648.12,2657.32,3264.73,3271.67,3886.84,4501.3,5115.66,5730.99,6345.59,0,0}};
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int i;
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double dMair = 28.9626;
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double dZair = 0;
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for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
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{
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if (ptAGA10.adMixture[i] != 0)
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{
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ptAGA10.Pc += adTablePc[i] * ptAGA10.adMixture[i];
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ptAGA10.TC += adTableTc[i] * ptAGA10.adMixture[i];
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if (adTableBzsx[i] != 0)
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{
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ptAGA10.Bzsx += ptAGA10.adMixture[i] / adTableBzsx[i];
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ptAGA10.Bzxx += ptAGA10.adMixture[i] / adTableBzxx[i];
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}
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if (i >= 10 & i <= 18)
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{
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ptAGA10.C4j += ptAGA10.adMixture[i] * adTableMri[i];
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}
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if (i >= 12 & i <= 18)
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{
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ptAGA10.C5j += ptAGA10.adMixture[i] * adTableMri[i];
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}
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if (i >= 14 & i <= 18)
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{
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ptAGA10.C6j += ptAGA10.adMixture[i] * adTableMri[i];
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}
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if (i == 3)
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{
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ptAGA10.C2 += ptAGA10.adMixture[i] * adTableMri[i];
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}
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switch (ptAGA10.dCbtj)
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{
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case 2:
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ptAGA10.dZb11062 += adTableSqrtbj[0, i] * ptAGA10.adMixture[i];
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dZair = 0.99941;
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break;
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case 1:
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ptAGA10.dZb11062 += adTableSqrtbj[1, i] * ptAGA10.adMixture[i];
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dZair = 0.99958;
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break;
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case 0:
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ptAGA10.dZb11062 += adTableSqrtbj[2, i] * ptAGA10.adMixture[i];
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dZair = 0.99963;
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break;
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}
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switch (ptAGA10.dCbtj_E)
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{
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case 0:
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ptAGA10.dHhvMol += adTableHhvMol[0, i] * ptAGA10.adMixture[i];
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ptAGA10.dLhvMol += adTableLhvMol[0, i] * ptAGA10.adMixture[i];
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break;
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case 1:
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ptAGA10.dHhvMol += adTableHhvMol[1, i] * ptAGA10.adMixture[i];
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ptAGA10.dLhvMol += adTableLhvMol[1, i] * ptAGA10.adMixture[i];
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break;
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case 2:
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ptAGA10.dHhvMol += adTableHhvMol[2, i] * ptAGA10.adMixture[i];
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ptAGA10.dLhvMol += adTableLhvMol[2, i] * ptAGA10.adMixture[i];
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break;
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case 3:
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ptAGA10.dHhvMol += adTableHhvMol[3, i] * ptAGA10.adMixture[i];
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ptAGA10.dLhvMol += adTableLhvMol[3, i] * ptAGA10.adMixture[i];
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break;
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}
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}
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}
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ptAGA10.Bzsx = ptAGA10.Bzsx == 0 ? 0 : 1 / ptAGA10.Bzsx;
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ptAGA10.Bzxx = ptAGA10.Bzxx == 0 ? 0 : 1 / ptAGA10.Bzxx;
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ptAGA10.dZb11062 = 1 - ptAGA10.dZb11062 * ptAGA10.dZb11062;
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ptAGA10.dHhvm = ptAGA10.dHhvMol / ptAGA10.dMrx;
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ptAGA10.dLhvm = ptAGA10.dLhvMol / ptAGA10.dMrx;
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ptAGA10.dHhvv = ptAGA10.dHhvMol * ptAGA10.dPb / ptAGA10.dTb / 8314.510 / ptAGA10.dZb11062;
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ptAGA10.dLhvv = ptAGA10.dLhvMol * ptAGA10.dPb / ptAGA10.dTb / 8314.510 / ptAGA10.dZb11062;
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ptAGA10.dRD_Ideal11062 = ptAGA10.dMrx / dMair;
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ptAGA10.dRD_Real11062 = ptAGA10.dRD_Ideal11062 * dZair / ptAGA10.dZb11062;
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ptAGA10.dRhob11062 = ptAGA10.dMrx * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.dRhof11062 = ptAGA10.dMrx * ptAGA10.dPf / 8314.51 / ptAGA10.dTf / ptAGA10.dZf;
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ptAGA10.dWobbeIndex = ptAGA10.dHhvv / Math.Sqrt(ptAGA10.dRD_Real11062);
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ptAGA10.C3j = ptAGA10.C4j + ptAGA10.adMixture[4] * adTableMri[4];
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ptAGA10.C2j = ptAGA10.C3j + ptAGA10.adMixture[3] * adTableMri[3];
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ptAGA10.C3C4 = ptAGA10.adMixture[4] * adTableMri[4] + ptAGA10.adMixture[10] * adTableMri[10] + ptAGA10.adMixture[11] * adTableMri[11];
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ptAGA10.TotalC = ptAGA10.C2j + ptAGA10.adMixture[0] * adTableMri[0];
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ptAGA10.TotalC = ptAGA10.TotalC * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.C2 = ptAGA10.C2 * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.C3C4 = ptAGA10.C3C4 * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.C2j = ptAGA10.C2j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.C3j = ptAGA10.C3j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.C4j = ptAGA10.C4j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.C5j = ptAGA10.C5j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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ptAGA10.C6j = ptAGA10.C6j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
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}
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}
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}
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530
AGA8_10/NG_Cal.cs
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530
AGA8_10/NG_Cal.cs
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using System;
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using System.Collections.Generic;
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using System.Runtime.InteropServices;
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using System.Text;
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namespace NG_Tools
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{
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public class NG_Cal
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{
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public const int NORMAL = 9000;
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public const int NG_Cal_INITIALIZED = 9001;
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public const int MEMORY_ALLOCATION_ERROR = 9002;
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public const int GENERAL_CALCULATION_FAILURE = 9003;
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public const int MAX_NUM_OF_ITERATIONS_EXCEEDED = 9004;
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public const int NEGATIVE_DENSITY_DERIVATIVE = 9005;
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public const int MAX_DENSITY_IN_BRAKET_EXCEEDED = 9006;
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/* number of components */
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public const int NUMBEROFCOMPONENTS = 21;
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/* maximum number of tries within search routines */
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public const int MAX_NUM_OF_ITERATIONS = 100;
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/* default tolerance limits */
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public const double P_CHG_TOL = 0.001; /* 0.001 Pa */
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public const double T_CHG_TOL = 0.001; /* 0.001 of a Kelvin */
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/* maximum allowable P & T */
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public const double P_MAX = 1.379e8; // maximum pressure (Pa) ~= 20,000 psi
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public const double P_MIN = 0.0; // maximum pressure = 0
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public const double T_MAX = 473.15; // maximum temperature (K) ~= 392 F
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public const double T_MIN = 143.0; // maximum temperature (K) ~= -200 F
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/* universal gas constant, in two configurations */
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public const double RGASKJ = 8.314510e-3; /* in kJ mol^-1 K^-1 */
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public const double RGAS = 8.314510; /* in J mol^-1 K^-1 */
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/* the main data structure used by this library */
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public struct GasPropsSTRUCT
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{ /* corresponds to the control group in meter classes */
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public int lStatus; /* calculation status 计算状态 */
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public bool bForceUpdate; /*执行全部计算的标志 signal to perform full calculation */
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public double[] adMixture; /*气体摩尔组成 Composition in mole fraction */
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public double[] adMixtureV; /*气体体积组成 Composition in mole fraction */
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public double[] adMixtureD; /*气体质量组成 Composition in mole fraction */
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public int dCbtj; //参比条件 101325 0,15,20
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public int dCbtj_E; //燃烧参比条件 101325 0,15,20
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public double dPb; /*参比压力 Contract base Pressure (Pa) */
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public double dTb; /* 参比温度Contract base temperature (K) */
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public double dPf; /*绝对压力 Absolute Pressure (Pa) */
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public double dTf; /*工况温度 Flowing temperature (K) */
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// basic output from AGA 8 Detail method
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public double dMrx; /*分子量 mixture molar mass */
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public double dZb; /* 标况压缩因子compressibility at contract base condition */
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public double dZf; /* 工况压缩因子compressibility at flowing condition */
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public double dFpv; /*超压缩系数 supercompressibility */
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public double dDb; /* 标况摩尔密度molar density at contract base conditions (moles/dm3) */
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public double dDf; /*工况摩尔密度 molar density at flowing conditions (moles/dm3) */
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public double dRhob; /* 标况质量密度mass density at contract base conditions (kg/m3) */
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public double dRhof; /*工况质量密度 mass density at flowing conditions (kg/m3) */
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public double dRD_Ideal; /* 理想气体的相对密度ideal gas relative density */
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public double dRD_Real; /* 真实气体的相对密度real gas relative density */
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// additional output
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public double dHo; /*理想气体的比焓 ideal gas specific enthalpy */
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public double dH; /*真实气体的焓 real gas specific enthalpy (J/kg) */
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public double dS; /* 真实气体的熵real gas specific entropy (J/kg-mol.K)*/
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||||
public double dCpi; /*理想气体定压热容 ideal gas constant pressure heat capacity (J/kg-mol.K)*/
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public double dCp; /* 定压热容real gas constant pressure heat capacity (J/kg-mol.K)*/
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public double dCv; /*定容积热容 real gas constant volume heat capacity (J/kg-mol.K)*/
|
||||
public double dk; /* 比热比ratio of specific heats */
|
||||
public double dKappa; /*等熵指数 isentropic exponent, denoted with Greek letter kappa */
|
||||
public double dSOS; /* 声速speed of sound (m/s) */
|
||||
public double dCstar; /*临界流函数 critical flow factor C* */
|
||||
|
||||
// 11062 输出
|
||||
|
||||
public double dHhvMol; //摩尔高位发热量
|
||||
public double dLhvMol; //摩尔低位发热量
|
||||
public double dHhvv; //体积高位发热量
|
||||
public double dLhvv; //体积低位发热量
|
||||
public double dHhvm; //质量高位发热量
|
||||
public double dLhvm; //质量地位发热量
|
||||
|
||||
public double dZb11062; //标况压缩因子
|
||||
public double dRhob11062; /* 标况质量密度mass density at contract base conditions (kg/m3) */
|
||||
public double dRhof11062; /*工况质量密度 mass density at flowing conditions (kg/m3) */
|
||||
public double dRD_Ideal11062; /* 理想气体的相对密度ideal gas relative density */
|
||||
public double dRD_Real11062; /* 真实气体的相对密度real gas relative density */
|
||||
public double dWobbeIndex; /* 真实气体的沃泊指数 */
|
||||
|
||||
|
||||
public double Pc; // '临界压力
|
||||
public double TC; /// '临界温度
|
||||
public double Bzsx; // '爆炸上限
|
||||
public double Bzxx; // '爆炸下限
|
||||
public double TotalC; // '总炭含量 (kg/m3)
|
||||
public double C2; // 'C2组分含量 (kg/m3)
|
||||
public double C2j; // 'C2以上组分含量 (kg/m3)
|
||||
public double C3j; // 'C3以上组分含量 (kg/m3)
|
||||
public double C4j; // 'C4以上组分含量 (kg/m3)
|
||||
public double C5j; // 'C5以上组分含量 (kg/m3)
|
||||
public double C6j; // 'C6以上组分含量 (kg/m3)
|
||||
public double C3C4; // 'C3C4组分含量 (kg/m3)
|
||||
|
||||
}
|
||||
public struct FlowParStruct //流量相关参数
|
||||
{
|
||||
//流量计算输入参数信息
|
||||
public int dFlowCalbz; //流量计算标准
|
||||
public int dZcalbz; //压缩因子计算标准
|
||||
public int dCbtj; //计量参比条件压力
|
||||
public double dPb_M; //计量参比条件压力
|
||||
public double dTb_M; //计量参比条件温度
|
||||
public double dPb_E; //燃烧参比条件压力
|
||||
public double dTb_E; //燃烧参比条件温度
|
||||
public double dPatm;//当地大气压
|
||||
public int dPatmUnit;//当地大气压单位
|
||||
public double[] dNG_Compents;//天然气组分
|
||||
|
||||
public int dMeterType;// 流量计类别
|
||||
public int dCoreType;//节流装置类型
|
||||
public int dPtmode; //取压方式
|
||||
public int dPipeType; // 管道类型
|
||||
public double dPipeD; //管道内径
|
||||
public int dLenUnit; //长度单位
|
||||
public double dPipeDtemp; //管道内径参考温度
|
||||
public int dPileDtempUint; //温度单位
|
||||
public int dPipeMaterial; //管道材料
|
||||
|
||||
public double dOrificeD; //孔板孔径
|
||||
public int dOrificeUnit; //长度单位
|
||||
public double dOrificeDtemp; //孔板内径参考温度
|
||||
public int dOrificeDtempUnit; //温度单位
|
||||
public int dOrificeMaterial; //孔板材料
|
||||
public int dOrificeSharpness; //锐利度系数计算方法
|
||||
public double dOrificeRk; //孔板入口圆弧半径
|
||||
public int dOrificeRkLenUint;//长度单位
|
||||
public double dPf;//输入压力
|
||||
public int dPfUnit;//压力单位
|
||||
public int dPfType; //压力类型
|
||||
public double dTf; //输入温度
|
||||
public int dTfUnit;//温度单位
|
||||
public double dDp; //输入差压
|
||||
public int dDpUnit; //压力单位
|
||||
public int dVFlowUnit; //体积流量单位
|
||||
public int dMFlowUnit; //'NG_Par(33) = ComboBox15.SelectedIndex '质量流量单位
|
||||
public int dEFlowUnit; //'NG_Par(34) = ComboBox16.SelectedIndex '能量流量单位
|
||||
public double dCd;//流出系数
|
||||
public double dCdCalMethod;//流出系数计算方法 0 检定证书 0回归公式
|
||||
public double dMeterFactor;//仪表系数
|
||||
public double dPulseNum;//脉冲数
|
||||
|
||||
public double dVFlowMax; //'NG_par(39)＝’最大体积流量
|
||||
public double dVFlowMin; //'NG_par(40)＝’最小体积流量
|
||||
public double dVFlowCon;//'NG_par(41)＝’常用流量
|
||||
public double dPfRangeMin; //'NG_par(42)＝’压力量程
|
||||
public double dPfRangeMax; //'NG_par(42)＝’压力量程
|
||||
public double dDpRangeMin; //'NG_par(43)＝’差压量程
|
||||
public double dDpRangeMax; //'NG_par(43)＝’差压量程
|
||||
public double dTfRangeMin; //'NG_par(44)＝’温度计量程
|
||||
public double dTfRangeMax; //'NG_par(44)＝’温度计量程
|
||||
|
||||
//流量计算输出参数
|
||||
public double dE; //'求渐近速度系数 E
|
||||
public double dFG; //'求相对密度系数 FG
|
||||
public double dFT; //'求流动温度系数 'FT
|
||||
public double dDViscosity; //'求动力粘度 dlnd
|
||||
public double dDExpCoefficient; //'求可膨胀系数
|
||||
public double dRnPipe; //'管道雷诺数
|
||||
public double dBk; //'孔板锐利度系数Bk
|
||||
public double dRoughNessPipe; //'管道粗糙度系数 Gme
|
||||
public double dCdCorrect; //'修正后的流出系数
|
||||
public double dCdNozell; //'喷嘴的流出系数
|
||||
public double dVFlowb;//'标况体积流量 m³、s
|
||||
public double dVFlowf; //'工况体积流量
|
||||
public double dMFlowb;//'标况质量流量
|
||||
public double dEFlowb;//'标况能量流量
|
||||
public double dVelocityFlow;//'管道内天然气流速
|
||||
public double dPressLost;//'压力损失
|
||||
public double dBeta;//'直径比
|
||||
public double dKappa;//'等熵指数
|
||||
|
||||
}
|
||||
|
||||
//public struct SqgyParStruct //输气工艺相关参数
|
||||
//{
|
||||
// public int dCalName; //计算项目
|
||||
// public int dPipleD; //管道内径mm
|
||||
// public int dPipleDw; //管道内径外径mm
|
||||
// public int dPipleBh; //管道壁厚 mm
|
||||
// public double dPipleTotalLength; //管道总长度 km
|
||||
// public double dPiplePointLength; //管道任意点长度 km
|
||||
// public double dPstart; //起点压力终点压力MPa
|
||||
// public double dPend; //终点压力MPa
|
||||
// public double dFlow; //输气能力
|
||||
// public double dRd;//相对密度
|
||||
// public double dZf;//压缩因子
|
||||
// public double[] dNG_Compents;//天然气组分
|
||||
|
||||
// public double dPavg;//管道平均压力
|
||||
// public double dPavgPoint;//管道任意点的平均压力
|
||||
|
||||
|
||||
//}
|
||||
|
||||
/* enumerations for tracking gas components */
|
||||
enum gascomp
|
||||
{
|
||||
XiC1 = 0, XiN2, XiCO2, XiC2, XiC3,
|
||||
XiH2O, XiH2S, XiH2, XiCO, XiO2, XiIC4, XiNC4,
|
||||
XiIC5, XiNC5, XiNC6, XiNC7, XiNC8, XiNC9, XiNC10, XiHe, XiAr
|
||||
};
|
||||
|
||||
|
||||
/* FUNCTION PROTOTYPES */
|
||||
/* prototypes for initialization */
|
||||
// int NG_Cal_Init(void) ; /* initialize library */
|
||||
// int NG_Cal_UnInit(void) ; /* un-initialize library */
|
||||
///* function prototype for basic VOS calculation */
|
||||
// double SOS(ref AGA10.GasPropsSTRUCT ) ;
|
||||
///* function prototype for a C* calculation */
|
||||
// double Crit(ref AGA10.GasPropsSTRUCT , double) ;
|
||||
|
||||
|
||||
|
||||
public Therm ptTherm;
|
||||
public Detail ptDetail;
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : NG_Cal_Init()
|
||||
* Arguments : void
|
||||
* Returns : int
|
||||
* Purpose : Initializes library; creates required objects
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public int NG_Cal_Init()
|
||||
{
|
||||
//create object for calculating density
|
||||
if (null == (ptDetail = new Detail()))
|
||||
{
|
||||
return MEMORY_ALLOCATION_ERROR;
|
||||
}
|
||||
|
||||
//create object for calculating thermodynamic properties
|
||||
if (null == (ptTherm = new Therm()))
|
||||
{
|
||||
return MEMORY_ALLOCATION_ERROR;
|
||||
}
|
||||
|
||||
return NG_Cal_INITIALIZED;
|
||||
|
||||
}// NG_Cal_Init
|
||||
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : NG_Cal_UnInit()
|
||||
* Arguments : void
|
||||
* Returns : int
|
||||
* Purpose : Un-initializes library; deletes objects
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public int NG_Cal_UnInit()
|
||||
{
|
||||
// delete the objects (if they exist)
|
||||
ptDetail = null;
|
||||
ptTherm = null;
|
||||
return 0;
|
||||
|
||||
}// NG_Cal_UnInit
|
||||
|
||||
|
||||
/**************************************************************************
|
||||
* Function : SOS()
|
||||
* Arguments : Pointers to external AGA10 data struct
|
||||
* Returns : double
|
||||
* Purpose : calculates speed of sound and other parameters
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public double SOS(ref GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
// check if library is ready; initialize if necessary
|
||||
if (null == ptDetail || null == ptTherm)
|
||||
{
|
||||
NG_Cal_UnInit();
|
||||
NG_Cal_Init();
|
||||
|
||||
}
|
||||
|
||||
switch (ptAGA10.dCbtj)
|
||||
{
|
||||
case 2:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 273.15;
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 288.15;
|
||||
break;
|
||||
case 0:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 293.15;
|
||||
break;
|
||||
}
|
||||
|
||||
|
||||
//Call function to calculate densities and thermodynamic properties
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
//the basic sound speed calculation doesn't calculate C*; initialize to zero
|
||||
ptAGA10.dCstar = 0.0;
|
||||
|
||||
//return the speed of sound to caller
|
||||
|
||||
return ptAGA10.dSOS;
|
||||
|
||||
}// VOS()
|
||||
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : Crit()
|
||||
* Arguments : Pointers to external AGA10 data struct, Detail and Therm
|
||||
* objects and a double precision float (gas velocity in plenum)
|
||||
* Returns : double
|
||||
* Purpose : calculates C*
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public double Crit(ref NG_Cal.GasPropsSTRUCT ptAGA10, double dPlenumVelocity)
|
||||
{
|
||||
//variables local to function
|
||||
double DH, DDH, S, H;
|
||||
double tolerance = 1.0;
|
||||
double R, P, T, Z;
|
||||
|
||||
int i;
|
||||
|
||||
//check objects for readiness; try to initialize if not
|
||||
if (null == ptDetail || null == ptTherm)
|
||||
{
|
||||
NG_Cal_UnInit();
|
||||
|
||||
if (NG_Cal_INITIALIZED != NG_Cal_Init())
|
||||
{
|
||||
|
||||
ptAGA10.lStatus = MEMORY_ALLOCATION_ERROR; return 0.0;
|
||||
|
||||
}
|
||||
}
|
||||
switch (ptAGA10.dCbtj)
|
||||
{
|
||||
case 2:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 273.15;
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 288.15;
|
||||
break;
|
||||
case 0:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 293.15;
|
||||
break;
|
||||
|
||||
|
||||
}
|
||||
//begin by calculating densities and thermodynamic properties
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
//DH is enthalpy change from plenum to throat; this is our initial guess
|
||||
|
||||
DH = (ptAGA10.dSOS * ptAGA10.dSOS - dPlenumVelocity * dPlenumVelocity) / 2.0;
|
||||
|
||||
//trap plenum conditions before we alter the data stucture's contents
|
||||
S = ptAGA10.dS;
|
||||
|
||||
H = ptAGA10.dH;
|
||||
|
||||
R = ptAGA10.dRhof;
|
||||
P = ptAGA10.dPf;
|
||||
Z = ptAGA10.dZf;
|
||||
T = ptAGA10.dTf;
|
||||
|
||||
//initialize delta of DH to an arbitrary value outside of
|
||||
|
||||
//convergence tolerance
|
||||
DDH = 10.0;
|
||||
|
||||
//Via simple repetition, search for a pressure, temperature and sound speed
|
||||
|
||||
//at a nozzle throat which provide constant enthalpy, given the entropy known
|
||||
//at the plenum. Abort if loop executes more than 100 times without convergence.
|
||||
for (i = 1; i < MAX_NUM_OF_ITERATIONS; i++)
|
||||
{
|
||||
|
||||
// calculate P and T to satisfy H and S
|
||||
ptTherm.HS_Mode(ref ptAGA10, ref ptDetail, H - DH, S, true);
|
||||
|
||||
//calculate new thermo, including SOS
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
//hold DH for tolerance check
|
||||
|
||||
DDH = DH;
|
||||
|
||||
// recalculate DH
|
||||
|
||||
DH = (ptAGA10.dSOS * ptAGA10.dSOS - dPlenumVelocity * dPlenumVelocity) / 2.0;
|
||||
|
||||
// end loop if tolerance reached
|
||||
|
||||
if (Math.Abs(DDH - DH) < tolerance) break;
|
||||
}
|
||||
|
||||
//C* is the real gas critical flow constant (not to be confused with Cperf or CRi)
|
||||
ptAGA10.dCstar = (ptAGA10.dRhof * ptAGA10.dSOS) / Math.Sqrt(R * P * Z);
|
||||
|
||||
//put the original plenum pressure and temperature back
|
||||
|
||||
ptAGA10.dPf = P;
|
||||
ptAGA10.dTf = T;
|
||||
|
||||
//restore fluid props to plenum conditions
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
GB11062 ptGB11062 = new GB11062();
|
||||
|
||||
ptGB11062.Run(ref ptAGA10);
|
||||
|
||||
//return the critical flow function to caller
|
||||
return ptAGA10.dCstar;
|
||||
|
||||
}// Crit()
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : Crit()
|
||||
* Arguments : Pointers to external AGA10 data struct, Detail and Therm
|
||||
* objects and a double precision float (gas velocity in plenum)
|
||||
* Returns : double
|
||||
* Purpose : calculates C*
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public double Zcal(ref NG_Cal.GasPropsSTRUCT ptAGA10, double dPlenumVelocity)
|
||||
{
|
||||
//variables local to function
|
||||
|
||||
|
||||
|
||||
//check objects for readiness; try to initialize if not
|
||||
if (null == ptDetail || null == ptTherm)
|
||||
{
|
||||
NG_Cal_UnInit();
|
||||
|
||||
if (NG_Cal_INITIALIZED != NG_Cal_Init())
|
||||
{
|
||||
|
||||
ptAGA10.lStatus = MEMORY_ALLOCATION_ERROR; return 0.0;
|
||||
|
||||
}
|
||||
}
|
||||
switch (ptAGA10.dCbtj)
|
||||
{
|
||||
case 2:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 273.15;
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 288.15;
|
||||
break;
|
||||
case 0:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 293.15;
|
||||
break;
|
||||
|
||||
|
||||
}
|
||||
//begin by calculating densities and thermodynamic properties
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
|
||||
GB11062 ptGB11062 = new GB11062();
|
||||
|
||||
ptGB11062.Run(ref ptAGA10);
|
||||
|
||||
//return the critical flow function to caller
|
||||
return ptAGA10.dZf;
|
||||
|
||||
}// Z()
|
||||
|
||||
/**************************************************************************
|
||||
* Function : Cperf()
|
||||
* Arguments : pointer to external AGA10 data struct
|
||||
* Returns : double
|
||||
* Purpose : calculates isentropic perfect gas critical flow function
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
double Cperf(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
|
||||
double k, root, exponent;
|
||||
|
||||
k = ptAGA10.dKappa; root = 2.0 / (k + 1.0);
|
||||
exponent = (k + 1.0) / (k - 1.0);
|
||||
|
||||
// isentropic perfect gas critical flow function C*i
|
||||
return (Math.Sqrt(k * Math.Pow(root, exponent)));
|
||||
|
||||
}// Cperf
|
||||
/**************************************************************************
|
||||
* Function : CRi()
|
||||
* Arguments : pointer to external AGA10 data struct
|
||||
* Returns : double
|
||||
* Purpose : calculates isentropic real gas critical flow function CRi
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
double CRi(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
return (Cperf(ref ptAGA10) / Math.Sqrt(ptAGA10.dZf));
|
||||
}// CRi()
|
||||
}
|
||||
}
|
||||
60
AGA8_10/NG_Cal.csproj
Normal file
60
AGA8_10/NG_Cal.csproj
Normal file
@ -0,0 +1,60 @@
|
||||
<?xml version="1.0" encoding="utf-8"?>
|
||||
<Project ToolsVersion="12.0" DefaultTargets="Build" xmlns="http://schemas.microsoft.com/developer/msbuild/2003">
|
||||
<Import Project="$(MSBuildExtensionsPath)\$(MSBuildToolsVersion)\Microsoft.Common.props" Condition="Exists('$(MSBuildExtensionsPath)\$(MSBuildToolsVersion)\Microsoft.Common.props')" />
|
||||
<PropertyGroup>
|
||||
<Configuration Condition=" '$(Configuration)' == '' ">Debug</Configuration>
|
||||
<Platform Condition=" '$(Platform)' == '' ">AnyCPU</Platform>
|
||||
<ProjectGuid>{186107A4-D8E6-46C1-A6CE-65E5C4F14C1B}</ProjectGuid>
|
||||
<OutputType>Library</OutputType>
|
||||
<AppDesignerFolder>Properties</AppDesignerFolder>
|
||||
<RootNamespace>NG_Cal</RootNamespace>
|
||||
<AssemblyName>NG_Cal</AssemblyName>
|
||||
<TargetFrameworkVersion>v4.0</TargetFrameworkVersion>
|
||||
<FileAlignment>512</FileAlignment>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition=" '$(Configuration)|$(Platform)' == 'Debug|AnyCPU' ">
|
||||
<DebugSymbols>true</DebugSymbols>
|
||||
<DebugType>full</DebugType>
|
||||
<Optimize>false</Optimize>
|
||||
<OutputPath>bin\Debug\</OutputPath>
|
||||
<DefineConstants>DEBUG;TRACE</DefineConstants>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<WarningLevel>4</WarningLevel>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition=" '$(Configuration)|$(Platform)' == 'Release|AnyCPU' ">
|
||||
<DebugType>pdbonly</DebugType>
|
||||
<Optimize>true</Optimize>
|
||||
<OutputPath>bin\Release\</OutputPath>
|
||||
<DefineConstants>TRACE</DefineConstants>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<WarningLevel>4</WarningLevel>
|
||||
</PropertyGroup>
|
||||
<ItemGroup>
|
||||
<Reference Include="System" />
|
||||
<Reference Include="System.Core" />
|
||||
<Reference Include="System.Drawing" />
|
||||
<Reference Include="System.Windows.Forms" />
|
||||
<Reference Include="System.Xml.Linq" />
|
||||
<Reference Include="System.Data.DataSetExtensions" />
|
||||
<Reference Include="Microsoft.CSharp" />
|
||||
<Reference Include="System.Data" />
|
||||
<Reference Include="System.Xml" />
|
||||
</ItemGroup>
|
||||
<ItemGroup>
|
||||
<Compile Include="FlowCal.cs" />
|
||||
<Compile Include="NG_Cal.cs" />
|
||||
<Compile Include="Detail.cs" />
|
||||
<Compile Include="GB11062.cs" />
|
||||
<Compile Include="Properties\AssemblyInfo.cs" />
|
||||
<Compile Include="Therm.cs" />
|
||||
<Compile Include="UnitConvert.cs" />
|
||||
</ItemGroup>
|
||||
<Import Project="$(MSBuildToolsPath)\Microsoft.CSharp.targets" />
|
||||
<!-- To modify your build process, add your task inside one of the targets below and uncomment it.
|
||||
Other similar extension points exist, see Microsoft.Common.targets.
|
||||
<Target Name="BeforeBuild">
|
||||
</Target>
|
||||
<Target Name="AfterBuild">
|
||||
</Target>
|
||||
-->
|
||||
</Project>
|
||||
BIN
AGA8_10/NG_TOOLS.snk
Normal file
BIN
AGA8_10/NG_TOOLS.snk
Normal file
Binary file not shown.
65
AGA8_10/NG_Tools.csproj
Normal file
65
AGA8_10/NG_Tools.csproj
Normal file
@ -0,0 +1,65 @@
|
||||
<?xml version="1.0" encoding="utf-8"?>
|
||||
<Project ToolsVersion="12.0" DefaultTargets="Build" xmlns="http://schemas.microsoft.com/developer/msbuild/2003">
|
||||
<Import Project="$(MSBuildExtensionsPath)\$(MSBuildToolsVersion)\Microsoft.Common.props" Condition="Exists('$(MSBuildExtensionsPath)\$(MSBuildToolsVersion)\Microsoft.Common.props')" />
|
||||
<PropertyGroup>
|
||||
<Configuration Condition=" '$(Configuration)' == '' ">Debug</Configuration>
|
||||
<Platform Condition=" '$(Platform)' == '' ">AnyCPU</Platform>
|
||||
<ProjectGuid>{186107A4-D8E6-46C1-A6CE-65E5C4F14C1B}</ProjectGuid>
|
||||
<OutputType>Library</OutputType>
|
||||
<AppDesignerFolder>Properties</AppDesignerFolder>
|
||||
<RootNamespace>NG_Tools</RootNamespace>
|
||||
<AssemblyName>NG_Tools</AssemblyName>
|
||||
<TargetFrameworkVersion>v2.0</TargetFrameworkVersion>
|
||||
<FileAlignment>512</FileAlignment>
|
||||
<TargetFrameworkProfile />
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition=" '$(Configuration)|$(Platform)' == 'Debug|AnyCPU' ">
|
||||
<DebugSymbols>true</DebugSymbols>
|
||||
<DebugType>full</DebugType>
|
||||
<Optimize>false</Optimize>
|
||||
<OutputPath>..\NGToolsPC\bin\x86\Debug\</OutputPath>
|
||||
<DefineConstants>DEBUG;TRACE</DefineConstants>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<WarningLevel>4</WarningLevel>
|
||||
<RegisterForComInterop>true</RegisterForComInterop>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition=" '$(Configuration)|$(Platform)' == 'Release|AnyCPU' ">
|
||||
<DebugType>pdbonly</DebugType>
|
||||
<Optimize>true</Optimize>
|
||||
<OutputPath>bin\Release\</OutputPath>
|
||||
<DefineConstants>TRACE</DefineConstants>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<WarningLevel>4</WarningLevel>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup>
|
||||
<SignAssembly>false</SignAssembly>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup>
|
||||
<AssemblyOriginatorKeyFile>
|
||||
</AssemblyOriginatorKeyFile>
|
||||
</PropertyGroup>
|
||||
<ItemGroup>
|
||||
<Reference Include="System" />
|
||||
<Reference Include="System.Drawing" />
|
||||
<Reference Include="System.Windows.Forms" />
|
||||
<Reference Include="System.Data" />
|
||||
<Reference Include="System.Xml" />
|
||||
</ItemGroup>
|
||||
<ItemGroup>
|
||||
<Compile Include="FlowCal.cs" />
|
||||
<Compile Include="NG_Cal.cs" />
|
||||
<Compile Include="Detail.cs" />
|
||||
<Compile Include="GB11062.cs" />
|
||||
<Compile Include="Properties\AssemblyInfo.cs" />
|
||||
<Compile Include="Therm.cs" />
|
||||
<Compile Include="UnitConvert.cs" />
|
||||
</ItemGroup>
|
||||
<Import Project="$(MSBuildToolsPath)\Microsoft.CSharp.targets" />
|
||||
<!-- To modify your build process, add your task inside one of the targets below and uncomment it.
|
||||
Other similar extension points exist, see Microsoft.Common.targets.
|
||||
<Target Name="BeforeBuild">
|
||||
</Target>
|
||||
<Target Name="AfterBuild">
|
||||
</Target>
|
||||
-->
|
||||
</Project>
|
||||
36
AGA8_10/Properties/AssemblyInfo.cs
Normal file
36
AGA8_10/Properties/AssemblyInfo.cs
Normal file
@ -0,0 +1,36 @@
|
||||
using System.Reflection;
|
||||
using System.Runtime.CompilerServices;
|
||||
using System.Runtime.InteropServices;
|
||||
|
||||
// 有关程序集的常规信息通过以下
|
||||
// 特性集控制。更改这些特性值可修改
|
||||
// 与程序集关联的信息。
|
||||
[assembly: AssemblyTitle("NG_Tools")]
|
||||
[assembly: AssemblyDescription("")]
|
||||
[assembly: AssemblyConfiguration("")]
|
||||
[assembly: AssemblyCompany("")]
|
||||
[assembly: AssemblyProduct("NG_Tools")]
|
||||
[assembly: AssemblyCopyright("Copyright © 2017 廖德云 ldeyun@163.com")]
|
||||
[assembly: AssemblyTrademark("")]
|
||||
[assembly: AssemblyCulture("")]
|
||||
|
||||
// 将 ComVisible 设置为 false 使此程序集中的类型
|
||||
// 对 COM 组件不可见。 如果需要从 COM 访问此程序集中的类型，
|
||||
// 则将该类型上的 ComVisible 特性设置为 true。
|
||||
[assembly: ComVisible(false)]
|
||||
|
||||
// 如果此项目向 COM 公开，则下列 GUID 用于类型库的 ID
|
||||
[assembly: Guid("7f6505ae-7989-41df-9888-b7b7c2e4ed67")]
|
||||
|
||||
// 程序集的版本信息由下面四个值组成:
|
||||
//
|
||||
// 主版本
|
||||
// 次版本
|
||||
// 生成号
|
||||
// 修订号
|
||||
//
|
||||
// 可以指定所有这些值，也可以使用“生成号”和“修订号”的默认值，
|
||||
// 方法是按如下所示使用“*”:
|
||||
// [assembly: AssemblyVersion("1.0.*")]
|
||||
[assembly: AssemblyVersion("1.0.0.0")]
|
||||
[assembly: AssemblyFileVersion("1.0.0.0")]
|
||||
534
AGA8_10/Therm.cs
Normal file
534
AGA8_10/Therm.cs
Normal file
@ -0,0 +1,534 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
|
||||
using System.Text;
|
||||
namespace NG_Tools
|
||||
{
|
||||
public class Therm
|
||||
{
|
||||
// member data
|
||||
//double dT;// current temperature, in Kelvins
|
||||
//double dP;// current pressure, in Pascals
|
||||
//double dD;// molar density, in moles/dm3
|
||||
//double dRho;// mass density, in kg/m3
|
||||
double dPdD;// partial deriv of P wrt D
|
||||
double dPdT;// partial deriv of P wrt T
|
||||
double dSi;// ideal gas specific entropy, kJ/kg.K
|
||||
double dTold;// temperature previously used
|
||||
double dMrxold;// mixture molar mass previously used
|
||||
double[] GK_root = new double[5] { 0.14887433898163121088, 0.43339539412924719080, 0.67940956829902440263, 0.86506336668898451073, 0.97390652851717172008 };
|
||||
double[] GK_weight = new double[5] { 0.29552422471475286217, 0.26926671930999634918, 0.21908636251598204295, 0.14945134915058059038, 0.066671344308688137179 };
|
||||
//set the number of points for quadrature
|
||||
int GK_points = 5;
|
||||
//equation constants for ideal gas heat capacity, enthalpy and entropy
|
||||
double[,] ThermConstants = new double[21, 11] {{-29776.4, 7.95454, 43.9417, 1037.09, 1.56373, 813.205, -24.9027, 1019.98,-10.1601, 1070.14,-20.0615},
|
||||
{-3495.34, 6.95587, 0.272892, 662.738,-0.291318,-680.562, 1.78980, 1740.06, 0.0, 100.0, 4.49823},
|
||||
{ 20.7307, 6.96237, 2.68645, 500.371,-2.56429,-530.443, 3.91921, 500.198, 2.13290, 2197.22, 5.81381},
|
||||
{-37524.4, 7.98139, 24.3668, 752.320, 3.53990, 272.846, 8.44724, 1020.13,-13.2732, 869.510,-22.4010},
|
||||
{-56072.1, 8.14319,37.0629,735.402,9.38159,247.190,13.4556, 1454.78,-11.7342, 984.518,-24.0426},
|
||||
{-13773.1, 7.97183, 6.27078,2572.63,2.05010,1156.72,0.0,100.0,0.0,100.0,-3.24989},
|
||||
{-10085.4, 7.94680,-0.08380,433.801,2.85539, 843.792,6.31595, 1481.43,-2.88457, 1102.23,-0.51551},
|
||||
{-5565.60, 6.66789, 2.33458,2584.98,.749019, 559.656,0.0,100.0,0.0,100.0,-7.94821},
|
||||
{-2753.49, 6.95854, 2.02441,1541.22,.096774, 3674.81,0.0,100.0,0.0,100.0,6.23387},
|
||||
{-3497.45, 6.96302, 2.40013, 2522.05, 2.21752, 1154.15, 0.0,100.0,0.0,100.0,9.19749},
|
||||
{-72387.0, 17.8143, 58.2062, 1787.39, 40.7621, 808.645, 0.0,100.0,0.0,100.0,-44.1341},
|
||||
{-72674.8, 18.6383, 57.4178, 1792.73, 38.6599, 814.151, 0.0,100.0,0.0,100.0,-46.1938},
|
||||
{-91505.5, 21.3861, 74.3410, 1701.58, 47.0587, 775.899, 0.0,100.0,0.0,100.0,-60.2474},
|
||||
{-83845.2, 22.5012, 69.5789, 1719.58, 46.2164, 802.174, 0.0,100.0,0.0,100.0,-62.2197},
|
||||
{-94982.5, 26.6225, 80.3819, 1718.49, 55.6598, 802.069, 0.0,100.0,0.0,100.0,-77.5366},
|
||||
{-103353.0, 30.4029, 90.6941, 1669.32, 63.2028, 786.001, 0.0,100.0,0.0,100.0,-92.0164},
|
||||
{-109674.0, 34.0847, 100.253, 1611.55, 69.7675, 768.847, 0.0,100.0,0.0,100.0,-106.149},
|
||||
{-122599.0, 38.5014, 111.446, 1646.48, 80.5015, 781.588, 0.0,100.0,0.0,100.0,-122.444},
|
||||
{-133564.0, 42.7143, 122.173, 1654.85, 90.2255, 785.564, 0.0,100.0,0.0,100.0,-138.006},
|
||||
{0.0,4.9680,0.0,100.0,0.0,100.0,0.0,100.0,0.0,100.0,0.0},
|
||||
{0.0,4.9680,0.0,100.0,0.0,100.0,0.0,100.0,0.0,100.0,0.0}};
|
||||
// enumerations for indexing of coefficients
|
||||
//public enum CoefficientList { coefA = 0, coefB, coefC, coefD, coefE, coefF, coefG, coefH, coefI, coefJ, coefK } ;
|
||||
public int coefA = 0;
|
||||
public int coefB = 1;
|
||||
public int coefC = 2;
|
||||
public int coefD = 3;
|
||||
public int coefE = 4;
|
||||
public int coefF = 5;
|
||||
public int coefG = 6;
|
||||
public int coefH = 7;
|
||||
public int coefI = 8;
|
||||
public int coefJ = 9;
|
||||
public int coefK = 10;
|
||||
// conversion constant for thermochemical calories to Joules: 1 cal(IT) = 4.1840 J
|
||||
const double CalTH = 4.1840;
|
||||
public Therm()
|
||||
{
|
||||
// initialize 3 history-sensitive variables
|
||||
dSi = 0.0;
|
||||
dTold = 0.0;
|
||||
dMrxold = 0.0;
|
||||
}//Therm()
|
||||
/**************************************************************************
|
||||
*Function:Math.Coth()
|
||||
*Arguments:double
|
||||
*Returns:double
|
||||
*Purpose:calculate hyperbolic cotangent; used in Ho calculations
|
||||
*Revisions:
|
||||
*Notes:Not a Therm object class member, just a utility for this
|
||||
*file. The C++ language has no intrinsic support for
|
||||
*hyperbolic cotangent
|
||||
**************************************************************************/
|
||||
double coth(double x)
|
||||
{
|
||||
return Math.Cosh(x) / Math.Sinh(x);
|
||||
}// Math.Coth()
|
||||
/**************************************************************************
|
||||
*Function:Run()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:void
|
||||
*Purpose:overall execution control; top level math for SOS and k
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
public void Run(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
//local variables
|
||||
double c, x, y, z;
|
||||
//first run basic set of functions within AGA 8 (1994) Detail Method
|
||||
ptD.Run(ref ptAGA10);
|
||||
//find first partial derivative of Z wrt D
|
||||
ptD.dZdD(ptAGA10.dDf);
|
||||
//find real gas cv, cp, specific enthalpy and entropy
|
||||
CprCvrHS(ref ptAGA10, ref ptD);
|
||||
//ratio of real gas specific heats
|
||||
ptAGA10.dk = ptAGA10.dCp / ptAGA10.dCv;
|
||||
//solve c in three steps, for clarity and ease of debugging
|
||||
x = ptAGA10.dk * NG_Cal.RGAS * 1000.0 * ptAGA10.dTf;
|
||||
y = ptAGA10.dMrx;
|
||||
z = ptAGA10.dZf + ptAGA10.dDf * ptD.ddZdD;
|
||||
//calculate c, which is SOS^2
|
||||
c = (x / y) * z;
|
||||
//speed of sound
|
||||
ptAGA10.dSOS = Math.Sqrt(c);
|
||||
//calculate the real gas isentropic exponent
|
||||
//using expression functionally equivalent to Equation 3.2
|
||||
ptAGA10.dKappa = (c * ptAGA10.dRhof) / ptAGA10.dPf;
|
||||
return;
|
||||
}//Run()
|
||||
/**************************************************************************
|
||||
*Function:CpiMolar()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT
|
||||
*Returns:double
|
||||
*Purpose:Calculate constant pressure ideal gas molar heat capacity
|
||||
*in (J/mol-K), applying eqns from Aly, Lee, McFall
|
||||
*Notes:For continuity, the original constants and eqn's have been
|
||||
*retained. Conversion from thermochemical calories(th) to
|
||||
*Joules is applied after the primary calculations are complete.
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double CpiMolar(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
double Cp = 0.0;
|
||||
double Cpx;
|
||||
double DT, FT, HT, JT;
|
||||
double Dx, Fx, Hx, Jx;
|
||||
double T;
|
||||
int i;
|
||||
//to maximize readability of this section, use intermediate variable T
|
||||
T = ptAGA10.dTf;
|
||||
//calculate heat capacity for each component
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
//skip species whose concentration is zero
|
||||
if (ptAGA10.adMixture[i] <= 0.0) continue;
|
||||
//initialize Cp of species to zero
|
||||
Cpx = 0.0;
|
||||
// calculate species intermediate terms
|
||||
DT = ThermConstants[i, coefD] / T;
|
||||
FT = ThermConstants[i, coefF] / T;
|
||||
HT = ThermConstants[i, coefH] / T;
|
||||
JT = ThermConstants[i, coefJ] / T;
|
||||
// use intermediate terms to avoid redundant calcs
|
||||
Dx = DT / Math.Sinh(DT);
|
||||
Fx = FT / Math.Cosh(FT);
|
||||
Hx = HT / Math.Sinh(HT);
|
||||
Jx = JT / Math.Cosh(JT);
|
||||
Cpx += ThermConstants[i, coefB];
|
||||
Cpx += ThermConstants[i, coefC] * Dx * Dx;
|
||||
Cpx += ThermConstants[i, coefE] * Fx * Fx;
|
||||
Cpx += ThermConstants[i, coefG] * Hx * Hx;
|
||||
Cpx += ThermConstants[i, coefI] * Jx * Jx;
|
||||
//use current mole fraction to weight the contribution
|
||||
Cpx *= ptAGA10.adMixture[i];
|
||||
//add this contribution to the sum
|
||||
Cp += Cpx;
|
||||
}
|
||||
// convert from cal(th)/mol-K to J/mol-K
|
||||
Cp *= CalTH;
|
||||
return Cp;
|
||||
}//CpiMolar()
|
||||
/**************************************************************************
|
||||
*Function:Ho()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT
|
||||
*Returns:double
|
||||
*Purpose:Calculate ideal gas specific enthalpy (J/kg)
|
||||
*Notes:For continuity, the original constants and eqn's have been
|
||||
*retained. Conversion from thermochemical calories(th) to
|
||||
*Joules is applied after the primary calculations are complete.
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double Ho(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
double H = 0.0; double Hx;
|
||||
double DT, FT, HT, JT;
|
||||
double cothDT, tanhFT, cothHT, tanhJT; double T;
|
||||
int i;
|
||||
// to maximize readability of this section, use intermediate variable T
|
||||
T = ptAGA10.dTf;
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
// skip species whose concentration is zero
|
||||
if (ptAGA10.adMixture[i] <= 0.0) continue;
|
||||
Hx = 0.0;
|
||||
// calculate species intermediate terms
|
||||
DT = ThermConstants[i, coefD] / T;
|
||||
FT = ThermConstants[i, coefF] / T; HT = ThermConstants[i, coefH] / T; JT = ThermConstants[i, coefJ] / T;
|
||||
cothDT = coth(DT); tanhFT = Math.Tanh(FT); cothHT = coth(HT); tanhJT = Math.Tanh(JT);
|
||||
Hx += ThermConstants[i, coefA];
|
||||
Hx += ThermConstants[i, coefB] * T;
|
||||
Hx += ThermConstants[i, coefC] * ThermConstants[i, coefD] * cothDT;
|
||||
Hx -= ThermConstants[i, coefE] * ThermConstants[i, coefF] * tanhFT;
|
||||
Hx += ThermConstants[i, coefG] * ThermConstants[i, coefH] * cothHT;
|
||||
Hx -= ThermConstants[i, coefI] * ThermConstants[i, coefJ] * tanhJT;
|
||||
//use current mole fraction to weight the contribution
|
||||
Hx *= ptAGA10.adMixture[i];
|
||||
//add this contribution to the sum
|
||||
H += Hx;
|
||||
}
|
||||
//convert from cal(th)/g-mol to kJ/kg-mol
|
||||
H *= CalTH;
|
||||
//convert from kJ/kg-mol to J/kg
|
||||
H /= ptAGA10.dMrx;
|
||||
// return in J/kg
|
||||
return H * 1.0e3;
|
||||
}
|
||||
// Ho()
|
||||
/**************************************************************************
|
||||
*Function:So()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT
|
||||
*Returns:double
|
||||
*Purpose:ideal gas specific entropy (J/kg-K)
|
||||
*Notes:For continuity, the original constants and eqn's have been
|
||||
*retained. Conversion from thermochemical calories(th) to
|
||||
*Joules is applied after the primary calculations are complete.
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double So(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
double S = 0.0; double Sx;
|
||||
double DT, FT, HT, JT;
|
||||
double cothDT, tanhFT, cothHT, tanhJT; double sinhDT, coshFT, sinhHT, coshJT; double T;
|
||||
int i;
|
||||
// to improve readability of this section, use intermediate variable T
|
||||
T = ptAGA10.dTf;
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
// skip species whose concentration is zero
|
||||
if (ptAGA10.adMixture[i] <= 0.0) continue;
|
||||
Sx = 0.0;
|
||||
// calculate species intermediate terms
|
||||
DT = ThermConstants[i, coefD] / T;
|
||||
FT = ThermConstants[i, coefF] / T;
|
||||
HT = ThermConstants[i, coefH] / T;
|
||||
JT = ThermConstants[i, coefJ] / T;
|
||||
cothDT = coth(DT); tanhFT = Math.Tanh(FT); cothHT = coth(HT);
|
||||
tanhJT = Math.Tanh(JT);
|
||||
sinhDT = Math.Sinh(DT); coshFT = Math.Cosh(FT); sinhHT = Math.Sinh(HT); coshJT = Math.Cosh(JT);
|
||||
Sx += ThermConstants[i, coefK];
|
||||
Sx += ThermConstants[i, coefB] * Math.Log(T);
|
||||
Sx += ThermConstants[i, coefC] * (DT * cothDT - Math.Log(sinhDT));
|
||||
Sx -= ThermConstants[i, coefE] * (FT * tanhFT - Math.Log(coshFT));
|
||||
Sx += ThermConstants[i, coefG] * (HT * cothHT - Math.Log(sinhHT));
|
||||
Sx -= ThermConstants[i, coefI] * (JT * tanhJT - Math.Log(coshJT));
|
||||
//use current mole fraction to weight the contribution
|
||||
Sx *= ptAGA10.adMixture[i];
|
||||
//add this contribution to the sum
|
||||
S += Sx;
|
||||
}
|
||||
//convert cal(th)/mol-K basis to to kJ/kg mol-K
|
||||
S *= CalTH;
|
||||
//convert from kJ/kg mol-K to kJ/kg-K
|
||||
S /= ptAGA10.dMrx;
|
||||
// return in J/kg-K
|
||||
return S * 1.0e3;
|
||||
}//So()
|
||||
/**************************************************************************
|
||||
*Function:CprCvrHS()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:void
|
||||
*Purpose:reasonably efficient group calculation of Cp, Cv, H and S
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
void CprCvrHS(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
double Cvinc, Cvr, Cpr;
|
||||
double Hinc;
|
||||
double Sinc;
|
||||
double Smixing;
|
||||
double Cp, Si;
|
||||
double a, b, x;
|
||||
int i;
|
||||
//initialize integrals to zero
|
||||
Cvinc = 0.0;
|
||||
Hinc = 0.0;
|
||||
Sinc = 0.0;
|
||||
//initialize entropy of mixing
|
||||
Smixing = 0.0;
|
||||
//find ideal gas Cp
|
||||
Cp = CpiMolar(ref ptAGA10);
|
||||
//find ideal gas enthalpy
|
||||
ptAGA10.dHo = Ho(ref ptAGA10);
|
||||
//find ideal gas entropy
|
||||
Si = So(ref ptAGA10);
|
||||
//calculate ideal gas specific heat capacity at constant pressure in J/kgK
|
||||
ptAGA10.dCpi = (Cp * 1000.0) / ptAGA10.dMrx;
|
||||
//integrate partial derivatives from D=0 to D=D, applying Gauss-Kronrod quadrature
|
||||
for (i = 0; i < GK_points; i++)
|
||||
{
|
||||
// set calculation point at + abscissa
|
||||
x = ptAGA10.dDf * (1.0 + GK_root[i]) / 2.0;
|
||||
//get Z at D
|
||||
ptD.zdetail(x);
|
||||
ptD.dZdT(x);
|
||||
ptD.d2ZdT2(x);
|
||||
//gather contributions at + abscissa; applying weighting factor
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x;
|
||||
Cvinc += GK_weight[i] * (2.0 * ptD.ddZdT + ptAGA10.dTf * ptD.dd2ZdT2) / x;
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
//set calculation point at - abscissa
|
||||
x = ptAGA10.dDf * (1.0 - GK_root[i]) / 2.0;
|
||||
//get Z at D
|
||||
ptD.zdetail(x);
|
||||
//calculate 1st and 2nd partial derivatives of Z wrt T
|
||||
ptD.dZdT(x);
|
||||
ptD.d2ZdT2(x);
|
||||
//gather contributions at - abscissa; applying weighting factor
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x;
|
||||
Cvinc += GK_weight[i] * (2.0 * ptD.ddZdT + ptAGA10.dTf * ptD.dd2ZdT2) / x;
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
}
|
||||
//return Z and partial derivatives to full molar density
|
||||
ptD.zdetail(ptAGA10.dDf);
|
||||
ptD.dZdT(ptAGA10.dDf);
|
||||
ptD.d2ZdT2(ptAGA10.dDf);
|
||||
//complete Cv molar
|
||||
Cvr = Cp - NG_Cal.RGAS * (1.0 + ptAGA10.dTf * Cvinc * 0.5 * ptAGA10.dDf);
|
||||
//intermediate values for Cp, containing 2 partial derivatives
|
||||
a = (ptAGA10.dZf + ptAGA10.dTf * ptD.ddZdT);
|
||||
b = (ptAGA10.dZf + ptAGA10.dDf * ptD.ddZdD);
|
||||
//calculate dPdT, the partial derivative of P wrt T, at D
|
||||
dPdT = NG_Cal.RGAS * ptAGA10.dDf * a;
|
||||
//calculate dPdD, the partial derivative of P wrt D, at T
|
||||
dPdD = NG_Cal.RGAS * ptAGA10.dTf * b;
|
||||
//equation completing molar Cp, cancelling appropriate terms
|
||||
Cpr = Cvr + NG_Cal.RGAS * ((a * a) / b);
|
||||
//change from molar to mass basis
|
||||
Cpr /= ptAGA10.dMrx;
|
||||
Cvr /= ptAGA10.dMrx;
|
||||
// write to the data stucture
|
||||
ptAGA10.dCv = Cvr * 1000.0; // convert from joules/kgK to kilojoules/kgK
|
||||
ptAGA10.dCp = Cpr * 1000.0;
|
||||
// calculate specific enthalpy
|
||||
ptAGA10.dH = ptAGA10.dHo + 1000.0 * NG_Cal.RGAS * ptAGA10.dTf * (ptAGA10.dZf - 1.0 - ptAGA10.dTf * Hinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
// calculate entropy of mixing
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
if (ptAGA10.adMixture[i] != 0) Smixing += ptAGA10.adMixture[i] * Math.Log(ptAGA10.adMixture[i]);
|
||||
}
|
||||
Smixing *= NG_Cal.RGAS;
|
||||
// calculate specific entropy
|
||||
ptAGA10.dS = Si - Smixing - 1000.0 * NG_Cal.RGAS * (Math.Log(ptAGA10.dPf / 101325.0) - Math.Log(ptAGA10.dZf) + Sinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
return;
|
||||
}//CprCvrHS()
|
||||
/**************************************************************************
|
||||
*Function:HS_Mode()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *, double, double, bool
|
||||
*Returns:void
|
||||
*Purpose:Calculates a pressure & temperature from known enthalpy & entropy,
|
||||
*with or without prior estimates.This function has a role in the
|
||||
*calculation of C*.
|
||||
*Solution based on a doubly-nested trial & error algorithm and Newton's
|
||||
*method.
|
||||
*
|
||||
*For illustrative purpose, two approaches are supported by this example.
|
||||
*If you are starting without advance knowledge of P & T, set the input parm
|
||||
*bGuess to false, thus specifying a conservative search approach.
|
||||
*If, however, you have a basis for guessing P & T (plenum conditions of a
|
||||
*critical flow nozzle, for example) set P & T via GasPropsSTRUCT and set
|
||||
*bGuess = true. The initial guess allows the search function to be more
|
||||
*aggressive and, typically, faster.
|
||||
*
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
public void HS_Mode(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD, double H, double S, bool bGuess)
|
||||
{
|
||||
double s0, s1, s2, t0, t1, t2, tmin, tmax; double h0, h1, h2, p0, p1, p2, px, pmin, pmax; double delta1, delta2;
|
||||
double tolerance = 0.001;// convergence tolerance (used for both H and S searches)
|
||||
int i, j;
|
||||
//s0and h0 are our real gas reference points
|
||||
s0 = S;
|
||||
h0 = H;
|
||||
//calling function specifies whether search parameters are supplied thru ptAGA10 or unknown
|
||||
if (bGuess)
|
||||
{
|
||||
t1 = ptAGA10.dTf; px = ptAGA10.dPf; pmax = px * 2.0; pmin = px * 0.1;
|
||||
tmax = t1 * 1.5; tmin = t1 * 0.67;
|
||||
}
|
||||
else// use arbitrary, generic limits
|
||||
{
|
||||
t1 = 273.15;
|
||||
px = 1013250.0; // 10 atmospheres
|
||||
pmax = NG_Cal.P_MAX;
|
||||
pmin = 10000.0; // 10 kPa
|
||||
tmax = NG_Cal.T_MAX;
|
||||
tmin = NG_Cal.T_MIN;
|
||||
}
|
||||
// set the temperature differential
|
||||
t2 = t1 + 10.0;
|
||||
///////////////////////////////////////////
|
||||
//begin double trial-and-error, searching for T & P
|
||||
//run the calculation with initial guesses
|
||||
ptD.Run(ref ptAGA10);
|
||||
//h1 is difference between h given and h@Tf, Pf
|
||||
h1 = this.H(ref ptAGA10, ref ptD) - h0;
|
||||
//outer loop: search for a t2 which will satisfy constant enthalpy
|
||||
for (i = 0; i < NG_Cal.MAX_NUM_OF_ITERATIONS; i++)
|
||||
{
|
||||
ptAGA10.dTf = t2;
|
||||
p1 = px;// reset one bracket
|
||||
p2 = px * 0.1;// set other bracket to 0.1x the upper bracket
|
||||
ptAGA10.dPf = p1;
|
||||
ptD.Run(ref ptAGA10);
|
||||
s1 = this.S(ref ptAGA10, ref ptD) - s0;
|
||||
//inside loop: search for a p2 which will satisfy constant entropy
|
||||
for (j = 0; j < NG_Cal.MAX_NUM_OF_ITERATIONS; j++)
|
||||
{
|
||||
ptAGA10.dPf = p2; ptD.Run(ref ptAGA10);
|
||||
s2 = this.S(ref ptAGA10, ref ptD) - s0;
|
||||
//calculate our proportional change
|
||||
delta2 = Math.Abs(s1 - s2) / s0; // close enough?
|
||||
if (delta2 < tolerance) break;
|
||||
//revise our estimate to p2
|
||||
p0 = p2;
|
||||
p2 = (p1 * s2 - p2 * s1) / (s2 - s1);
|
||||
//check for negative pressure and clamp to pmin for safety
|
||||
if (p2 <= pmin)
|
||||
{
|
||||
p2 = pmin;
|
||||
}
|
||||
//check if we've created an unrealistic pressure
|
||||
if (p2 >= pmax) p2 = pmax; // swap values
|
||||
p1 = p0;
|
||||
s1 = s2;
|
||||
}
|
||||
// check for failure to converge
|
||||
if (j >= NG_Cal.MAX_NUM_OF_ITERATIONS) ptAGA10.lStatus = NG_Cal.MAX_NUM_OF_ITERATIONS_EXCEEDED;
|
||||
//calc enthalpy at guessed P & current iter T
|
||||
h2 = this.H(ref ptAGA10, ref ptD) - h0;
|
||||
//calculate our proportional change
|
||||
delta1 = Math.Abs(h1 - h2) / h0;
|
||||
// close enough?
|
||||
if (delta1 < tolerance && i > 0) break;
|
||||
//revise our estimate to t2
|
||||
t0 = t2;
|
||||
t2 = (t1 * h2 - t2 * h1) / (h2 - h1);
|
||||
//check if we've created an unrealistic temperature
|
||||
if (t2 >= tmax) t2 = tmax;
|
||||
//revise t2, if necessary
|
||||
if (t2 <= tmin)
|
||||
{
|
||||
t2 = t0 + 10.0;
|
||||
ptAGA10.dTf = t2; ptD.Run(ref ptAGA10);
|
||||
h2 = this.H(ref ptAGA10, ref ptD) - h0;
|
||||
}
|
||||
t1 = t0;
|
||||
h1 = h2;
|
||||
}
|
||||
// check for failure to converge
|
||||
if (i >= NG_Cal.MAX_NUM_OF_ITERATIONS) ptAGA10.lStatus = NG_Cal.MAX_NUM_OF_ITERATIONS_EXCEEDED;
|
||||
}//HS_Mode()
|
||||
/**************************************************************************
|
||||
*Function:H()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:double
|
||||
*Purpose:real gas specific enthalpy
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double H(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
double Hinc; double x; int i;
|
||||
//initialize integral
|
||||
Hinc = 0.0;
|
||||
//find ideal gas enthalpy
|
||||
ptAGA10.dHo = Ho(ref ptAGA10);
|
||||
//integrate partial derivatives from D=0 to D=D, applying Gauss-Kronrod quadrature
|
||||
for (i = 0; i < GK_points; i++)
|
||||
{
|
||||
//calculate 1st and 2nd partial derivatives of Z wrt T
|
||||
x = ptAGA10.dDf * (1.0 + GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x);
|
||||
ptD.d2ZdT2(x);
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x; if (i == 10) break;
|
||||
x = ptAGA10.dDf * (1.0 - GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x); ptD.d2ZdT2(x);
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x;
|
||||
}
|
||||
ptD.zdetail(ptAGA10.dDf); ptD.dZdT(ptAGA10.dDf); ptD.d2ZdT2(ptAGA10.dDf);
|
||||
// calculate specific enthalpy
|
||||
ptAGA10.dH = ptAGA10.dHo + 1000.0 * NG_Cal.RGAS * ptAGA10.dTf *
|
||||
(ptAGA10.dZf - 1.0 - ptAGA10.dTf * Hinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
return (ptAGA10.dH);
|
||||
} // H()
|
||||
/**************************************************************************
|
||||
*Function:S()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:double
|
||||
*Purpose:real gas specific entropy
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double S(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
double Sinc; double Smixing; double x;
|
||||
int i;
|
||||
//initialize integral
|
||||
Sinc = 0.0;
|
||||
//initialize entropy of mixing
|
||||
Smixing = 0.0;
|
||||
//integrate partial derivatives from D=0 to D=D, applying Gauss-Kronrod quadrature
|
||||
for (i = 0; i < GK_points; i++)
|
||||
{
|
||||
//calculate 1st and 2nd partial derivatives of Z wrt T
|
||||
x = ptAGA10.dDf * (1.0 + GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x); ptD.d2ZdT2(x);
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
if (i == 10) break;
|
||||
x = ptAGA10.dDf * (1.0 - GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x); ptD.d2ZdT2(x);
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
}
|
||||
//reset Z and partial deivatives dZdT and d2ZdT2
|
||||
ptD.zdetail(ptAGA10.dDf);
|
||||
ptD.dZdT(ptAGA10.dDf);
|
||||
ptD.d2ZdT2(ptAGA10.dDf);
|
||||
//find ideal gas entropy, but only if temperature or composition have changed
|
||||
if (ptAGA10.dTf != dTold || ptAGA10.dMrx != dMrxold)
|
||||
{
|
||||
dSi = So(ref ptAGA10); dTold = ptAGA10.dTf; dMrxold = ptAGA10.dMrx;
|
||||
}
|
||||
//calculate entropy of mixing
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
if (ptAGA10.adMixture[i] != 0) Smixing += ptAGA10.adMixture[i] * Math.Log(ptAGA10.adMixture[i]);
|
||||
}
|
||||
Smixing *= NG_Cal.RGAS;
|
||||
// calculate specific entropy
|
||||
ptAGA10.dS = dSi - Smixing - 1000.0 * NG_Cal.RGAS * (Math.Log(ptAGA10.dPf / 101325.0) - Math.Log(ptAGA10.dZf) + Sinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
return (ptAGA10.dS);
|
||||
} // S()
|
||||
}
|
||||
}
|
||||
407
AGA8_10/UnitConvert.cs
Normal file
407
AGA8_10/UnitConvert.cs
Normal file
@ -0,0 +1,407 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
|
||||
using System.Text;
|
||||
|
||||
namespace NG_Tools
|
||||
{
|
||||
public class UnitConvert
|
||||
{
|
||||
public double Converter(string UnitName, double oldValue, int oldunit, int newunit, int Xsdws)
|
||||
{
|
||||
double returnValue = 0;
|
||||
//On Error Resume Next VBConversions Warning: On Error Resume Next not supported in C#
|
||||
//Dim strUnit() As String
|
||||
double[] dataUnit = new double[] { 0 };
|
||||
|
||||
//ReDim strUnit(UnitNum)
|
||||
//RereDim dataUnit(UnitNum)
|
||||
switch (UnitName)
|
||||
{
|
||||
case "tj":
|
||||
|
||||
dataUnit = new double[8];
|
||||
|
||||
|
||||
//strUnit(0) = "立方米(m3)"
|
||||
//strUnit(1) = "升(L, dm3)"
|
||||
//strUnit(2) = "立方厘米(cm3, ml, c.c)"
|
||||
//strUnit(3) = "立方英尺(ft3)"
|
||||
//strUnit(4) = "立方英寸(in3)"
|
||||
//strUnit(5) = "英加仑(UKgal)"
|
||||
//strUnit(6) = "美加仑(U.Sgal)"
|
||||
//strUnit(7) = "美油桶(USbbl)"
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 1000;
|
||||
dataUnit[2] = 1000000;
|
||||
dataUnit[3] = 35.3147;
|
||||
dataUnit[4] = 61023.7;
|
||||
dataUnit[5] = 219.969;
|
||||
dataUnit[6] = 264.172;
|
||||
dataUnit[7] = 6.28994;
|
||||
break;
|
||||
|
||||
case "zl":
|
||||
|
||||
//strUnit(0) = "千克(公斤)(kg)"
|
||||
//strUnit(1) = "克(g)"
|
||||
//strUnit(2) = "毫克(mg)"
|
||||
//strUnit(3) = "吨(t)"
|
||||
//strUnit(4) = "英吨(长吨)(UKton)"
|
||||
//strUnit(5) = "美吨(短吨)(U.Ston)"
|
||||
//strUnit(6) = "磅(lb)"
|
||||
//strUnit(7) = "盎司(oz)"
|
||||
dataUnit = new double[8]; //As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 1000;
|
||||
dataUnit[2] = 1000000;
|
||||
dataUnit[3] = 0.001;
|
||||
dataUnit[4] = 0.000984207;
|
||||
dataUnit[5] = 0.00110231;
|
||||
dataUnit[6] = 2.20462;
|
||||
dataUnit[7] = 35.274;
|
||||
break;
|
||||
case "rl":
|
||||
//strUnit(0) = "焦耳(J)"
|
||||
//strUnit(1) = "马力小时(Hp·h)"
|
||||
//strUnit(2) = "公斤力·米(kgf·m)"
|
||||
//strUnit(3) = "升·大气压(L·atm)"
|
||||
//strUnit(4) = "尔格(erg)"
|
||||
//strUnit(5) = "千卡(kacl)"
|
||||
//strUnit(6) = "千瓦小时(kW·h)"
|
||||
//strUnit(7) = "英马力小时(UKHp·h)"
|
||||
//strUnit(8) = "英尺·磅力(ft·lbf)"
|
||||
//strUnit(9) = "英热单位(BTU)"
|
||||
dataUnit = new double[10]; // As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 0.000000377672;
|
||||
dataUnit[2] = 0.101972;
|
||||
dataUnit[3] = 0.00986923;
|
||||
dataUnit[4] = 107;
|
||||
dataUnit[5] = 0.000238846;
|
||||
dataUnit[6] = 0.000000277778;
|
||||
dataUnit[7] = 0.000000372506;
|
||||
dataUnit[8] = 0.737562;
|
||||
dataUnit[9] = 0.000947813;
|
||||
break;
|
||||
|
||||
|
||||
case "nlll":
|
||||
//strUnit(0) = "兆焦/秒(MJ/s)"
|
||||
//strUnit(1) = "兆焦/小时(MJ/h)"
|
||||
//strUnit(2) = "兆焦/天(MJ/d)"
|
||||
//strUnit(3) = "千卡/秒(kcal/s)"
|
||||
//strUnit(4) = "千卡/小时(kcal/h)"
|
||||
//strUnit(5) = "英热单位/秒(BTU/s)"
|
||||
//strUnit(6) = "英热单位/小时(BTU/h)"
|
||||
|
||||
dataUnit = new double[7]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 3600;
|
||||
dataUnit[2] = 86400;
|
||||
dataUnit[3] = 238.846;
|
||||
dataUnit[4] = 859845.6;
|
||||
dataUnit[5] = 947.813;
|
||||
dataUnit[6] = 3412126.8;
|
||||
break;
|
||||
|
||||
case "zlll":
|
||||
|
||||
//strUnit(0) = "千克(公斤)/秒(kg/s)"
|
||||
//strUnit(1) = "千克(公斤)/分(kg/Min)"
|
||||
//strUnit(2) = "千克(公斤)/时(kg/h)"
|
||||
//strUnit(3) = "磅/秒(lb/s)"
|
||||
//strUnit(4) = "磅/分(lb/Min)"
|
||||
//strUnit(5) = "磅/时(lb/h)"
|
||||
//strUnit(6) = "吨/时(t/h)"
|
||||
//strUnit(7) = "英吨(长吨)/时(UKton/h)"
|
||||
//strUnit(8) = "美吨(短吨)/小时(U.Ston/h)"
|
||||
|
||||
dataUnit = new double[9]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 60;
|
||||
dataUnit[2] = 3600;
|
||||
dataUnit[3] = 2.20462;
|
||||
dataUnit[4] = 132.2772;
|
||||
dataUnit[5] = 7936.632;
|
||||
dataUnit[6] = 3.6;
|
||||
dataUnit[7] = 3.543145;
|
||||
dataUnit[8] = 3.968316;
|
||||
break;
|
||||
case "tjll":
|
||||
//strUnit(0) = "立方米/秒(m3/s)"
|
||||
//strUnit(1) = "万立方米/天(m3/d)"
|
||||
//strUnit(1) = "立方米/时(m3/h)"
|
||||
//strUnit(2) = "立方米/分(m3/Min)"
|
||||
//strUnit(3) = "升/时(L/h)"
|
||||
//strUnit(4) = "升/分(L/Min)"
|
||||
//strUnit(5) = "升/秒(L/s)"
|
||||
//strUnit(6) = "立方英尺/时(ft3/h)"
|
||||
//strUnit(7) = "立方英尺/分(ft3/Min)"
|
||||
//strUnit(8) = "立方英尺/秒(ft3/s)"
|
||||
//strUnit(9) = "立方英尺/秒(ft3/s)"
|
||||
//strUnit(10) = "立方英尺/天(ft3/d)"
|
||||
|
||||
//strUnit(11) = "英加仑/秒(UKgal/s)"
|
||||
//strUnit(12) = "美加仑/秒(U.Sgal/s)"
|
||||
//strUnit(13) = "美油桶/秒(USbbl/s)"
|
||||
|
||||
|
||||
dataUnit = new double[13]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 8.64;
|
||||
dataUnit[2] = 3600;
|
||||
dataUnit[3] = 60;
|
||||
dataUnit[4] = 3600000;
|
||||
dataUnit[5] = 60000;
|
||||
dataUnit[6] = 1000;
|
||||
dataUnit[7] = 127132.92;
|
||||
dataUnit[8] = 2118.882;
|
||||
dataUnit[9] = 0.0245240972222222;
|
||||
dataUnit[10] = 35.3147;
|
||||
dataUnit[11] = 219.969;
|
||||
dataUnit[12] = 264.172;
|
||||
|
||||
break;
|
||||
|
||||
|
||||
case "yl":
|
||||
//strUnit(0) = "帕(Pa)"
|
||||
//strUnit(1) = "千帕(kPa)"
|
||||
//strUnit(2) = "兆帕(Mpa)"
|
||||
//strUnit(3) = "标准大气压(atm)"
|
||||
//strUnit(4) = "毫巴(mbar)"
|
||||
//strUnit(5) = "巴(bar)"
|
||||
//strUnit(6) = "千克力/平方米(kgf/m2)"
|
||||
//strUnit(7) = "千克力/平方厘米(kgf/cm2)"
|
||||
//strUnit(8) = "毫米汞柱(mmHg)"
|
||||
//strUnit(9) = "毫米水柱4℃(mmH2O)"
|
||||
//strUnit(10) = "磅/平方英寸(psi)"
|
||||
|
||||
dataUnit = new double[11]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 0.001;
|
||||
dataUnit[2] = 0.000001;
|
||||
dataUnit[3] = 0.00000986923266716013;
|
||||
dataUnit[4] = 0.01;
|
||||
dataUnit[5] = 0.00001;
|
||||
dataUnit[6] = 0.101971621;
|
||||
dataUnit[7] = 0.0000101972;
|
||||
dataUnit[8] = 0.007500638;
|
||||
dataUnit[9] = 0.101972;
|
||||
dataUnit[10] = 0.000145038;
|
||||
break;
|
||||
|
||||
case "wd":
|
||||
switch (newunit)
|
||||
{
|
||||
case 0:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
case 1: //K->℃
|
||||
returnValue = oldValue - 273.15;
|
||||
break;
|
||||
case 2: //F->℃
|
||||
returnValue = (oldValue - 32) / 1.8;
|
||||
break;
|
||||
case 3: //R->℃
|
||||
returnValue = oldValue / 1.8 - 273.15;
|
||||
break;
|
||||
}
|
||||
break;
|
||||
case 1:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0: //℃->K
|
||||
returnValue = oldValue + 273.15;
|
||||
break;
|
||||
case 1:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
case 2: //F->K
|
||||
returnValue = (oldValue - 32) / 1.8 + 273.15;
|
||||
break;
|
||||
case 3: //R->K
|
||||
returnValue = oldValue / 1.8;
|
||||
break;
|
||||
}
|
||||
break;
|
||||
case 2:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0: //C->F
|
||||
returnValue = oldValue * 1.8 + 32;
|
||||
break;
|
||||
case 1: //k->f
|
||||
returnValue = (oldValue - 273.15) * 1.8 + 32;
|
||||
break;
|
||||
case 2:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
case 3: //R->F
|
||||
returnValue = oldValue - 273.15 * 1.8 + 32;
|
||||
break;
|
||||
|
||||
}
|
||||
break;
|
||||
case 3:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0: //C->R
|
||||
returnValue = (oldValue + 273.15) * 1.8;
|
||||
break;
|
||||
case 1: //K->R
|
||||
returnValue = oldValue * 1.8;
|
||||
break;
|
||||
case 2: //F->R
|
||||
returnValue = (oldValue - 32) + 273.15 * 1.8;
|
||||
break;
|
||||
case 3:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
}
|
||||
break;
|
||||
default:
|
||||
break;
|
||||
}
|
||||
return returnValue;
|
||||
case "cd":
|
||||
//米(m)
|
||||
//分米(dm)
|
||||
//厘米(cm)
|
||||
//毫米(mm)
|
||||
//英尺(ft)
|
||||
//英寸(in)
|
||||
//英里(mile)
|
||||
//英寻(fm)
|
||||
//海里(nmile)
|
||||
//埃(a)
|
||||
//码(yd)
|
||||
//密尔(mil)
|
||||
//杆<(rad)
|
||||
|
||||
dataUnit = new double[14]; //As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 10;
|
||||
dataUnit[2] = 100;
|
||||
dataUnit[3] = 1000;
|
||||
dataUnit[5] = 3.28038;
|
||||
dataUnit[4] = 39.3700787401575;
|
||||
dataUnit[6] = 0.001;
|
||||
dataUnit[7] = 0.000621504039776259;
|
||||
dataUnit[8] = 0.546746856205577;
|
||||
dataUnit[9] = 0.000539956803455;
|
||||
dataUnit[10] = 10000000000.0D;
|
||||
dataUnit[11] = 1.093613;
|
||||
dataUnit[12] = 39370.0787401575;
|
||||
dataUnit[13] = 0.198838781515947;
|
||||
break;
|
||||
|
||||
case "mj":
|
||||
|
||||
|
||||
//平方米m2
|
||||
//平方分米dm2
|
||||
//平方厘米cm2
|
||||
//平方毫米mm2
|
||||
//平方英尺ft2
|
||||
//平方英寸in2
|
||||
//平方公里km2
|
||||
//公顷ha
|
||||
//公亩are
|
||||
//英亩acre
|
||||
//平方英里sq -mile
|
||||
//平方码yd2
|
||||
|
||||
dataUnit = new double[12]; //As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 100;
|
||||
dataUnit[2] = 10000;
|
||||
dataUnit[3] = 1000000;
|
||||
dataUnit[4] = 10.7608929444;
|
||||
dataUnit[5] = 1550.0031;
|
||||
dataUnit[6] = 0.000001;
|
||||
dataUnit[7] = 0.0001;
|
||||
dataUnit[8] = 0.01;
|
||||
dataUnit[9] = 0.0002471;
|
||||
dataUnit[10] = 0.000000386102158;
|
||||
dataUnit[11] = 1.19599;
|
||||
break;
|
||||
//小时
|
||||
//分钟
|
||||
//天
|
||||
//秒
|
||||
|
||||
case "sj":
|
||||
dataUnit = new double[4]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 60;
|
||||
dataUnit[2] = 0.0416666666666667;
|
||||
dataUnit[3] = 3600;
|
||||
break;
|
||||
|
||||
|
||||
|
||||
case "sd":
|
||||
break;
|
||||
//米每秒
|
||||
//厘米每秒
|
||||
//
|
||||
}
|
||||
if (newunit == oldunit)
|
||||
{
|
||||
return oldValue;
|
||||
|
||||
}
|
||||
return SsWr(oldValue * dataUnit[newunit] / dataUnit[oldunit], Xsdws);
|
||||
|
||||
}
|
||||
|
||||
private double SsWr(double value, int weishu)
|
||||
{
|
||||
long tempValue = 0;
|
||||
double SorR = 0;
|
||||
try
|
||||
{
|
||||
tempValue = (long)(value * Math.Pow(10, weishu));
|
||||
|
||||
SorR = System.Convert.ToInt32((value * Math.Pow(10, weishu) - tempValue) * 10);
|
||||
if (SorR >= 5)
|
||||
{
|
||||
tempValue++;
|
||||
}
|
||||
return tempValue / Math.Pow(10, weishu);
|
||||
}
|
||||
catch
|
||||
{
|
||||
|
||||
return value;
|
||||
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
|
||||
|
||||
|
||||
|
||||
|
||||
}
|
||||
}
|
||||
BIN
AGA8_10/bin/Debug/NG_Tools.dll
Normal file
BIN
AGA8_10/bin/Debug/NG_Tools.dll
Normal file
Binary file not shown.
BIN
AGA8_10/bin/Debug/NG_Tools.pdb
Normal file
BIN
AGA8_10/bin/Debug/NG_Tools.pdb
Normal file
Binary file not shown.
BIN
AGA8_10/bin/Release/NG_Tools.dll
Normal file
BIN
AGA8_10/bin/Release/NG_Tools.dll
Normal file
Binary file not shown.
BIN
AGA8_10/bin/Release/NG_Tools.pdb
Normal file
BIN
AGA8_10/bin/Release/NG_Tools.pdb
Normal file
Binary file not shown.
10
AGA8_10/obj/Debug/AGA8_10.csproj.FileListAbsolute.txt
Normal file
10
AGA8_10/obj/Debug/AGA8_10.csproj.FileListAbsolute.txt
Normal file
@ -0,0 +1,10 @@
|
||||
e:\ldy\documents\visual studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\AGA8_10.csprojResolveAssemblyReference.cache
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\obj\Debug\AGA8_10.csprojResolveAssemblyReference.cache
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\AGA8_10.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\AGA8_10.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\AGA8_10.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\AGA8_10.pdb
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Cal.dll
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Cal.pdb
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Cal.dll
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Cal.pdb
|
||||
BIN
AGA8_10/obj/Debug/AGA8_10.csprojResolveAssemblyReference.cache
Normal file
BIN
AGA8_10/obj/Debug/AGA8_10.csprojResolveAssemblyReference.cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/DesignTimeResolveAssemblyReferences.cache
Normal file
BIN
AGA8_10/obj/Debug/DesignTimeResolveAssemblyReferences.cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/DesignTimeResolveAssemblyReferencesInput.cache
Normal file
BIN
AGA8_10/obj/Debug/DesignTimeResolveAssemblyReferencesInput.cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Cal.VerifiSys.resources
Normal file
BIN
AGA8_10/obj/Debug/NG_Cal.VerifiSys.resources
Normal file
Binary file not shown.
13
AGA8_10/obj/Debug/NG_Cal.csproj.FileListAbsolute.txt
Normal file
13
AGA8_10/obj/Debug/NG_Cal.csproj.FileListAbsolute.txt
Normal file
@ -0,0 +1,13 @@
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Cal.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Cal.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Cal.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Cal.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Cal.csprojResolveAssemblyReference.cache
|
||||
E:\ldy\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Cal.dll
|
||||
E:\ldy\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Cal.pdb
|
||||
E:\ldy\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Cal.dll
|
||||
E:\ldy\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Cal.pdb
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
BIN
AGA8_10/obj/Debug/NG_Cal.csproj.GenerateResource.Cache
Normal file
BIN
AGA8_10/obj/Debug/NG_Cal.csproj.GenerateResource.Cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Cal.csprojResolveAssemblyReference.cache
Normal file
BIN
AGA8_10/obj/Debug/NG_Cal.csprojResolveAssemblyReference.cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Cal.dll
Normal file
BIN
AGA8_10/obj/Debug/NG_Cal.dll
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Cal.pdb
Normal file
BIN
AGA8_10/obj/Debug/NG_Cal.pdb
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Tools-副本20210207075021.dll
Normal file
BIN
AGA8_10/obj/Debug/NG_Tools-副本20210207075021.dll
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Tools-副本20210207075022.pdb
Normal file
BIN
AGA8_10/obj/Debug/NG_Tools-副本20210207075022.pdb
Normal file
Binary file not shown.
@ -0,0 +1 @@
|
||||
f7356ac4a88e5f88d3562e5b4a2aa538eab6c652
|
||||
@ -0,0 +1 @@
|
||||
aa7b8fa9bf6992e64b927598d7523274d516d83e
|
||||
74
AGA8_10/obj/Debug/NG_Tools.csproj.FileListAbsolute.txt
Normal file
74
AGA8_10/obj/Debug/NG_Tools.csproj.FileListAbsolute.txt
Normal file
@ -0,0 +1,74 @@
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
E:\My Documents\Desktop\AGA8_10\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Tools.tlb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
C:\Users\Intouch\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
C:\Users\Intouch\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
C:\Users\Intouch\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\bin\Debug\NG_Tools.tlb
|
||||
C:\Users\Intouch\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
C:\Users\Intouch\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\AGA8_10\AGA8_10\obj\Debug\NG_Tools.csprojResolveAssemblyReference.cache
|
||||
C:\Users\ldeyu\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
C:\Users\ldeyu\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
C:\Users\ldeyu\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Debug\NG_Tools.tlb
|
||||
C:\Users\ldeyu\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
C:\Users\ldeyu\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
C:\Users\ldeyu\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Debug\NG_Tools.tlb
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.tlb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.tlb
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.pdb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGTools\AGA8_10\bin\Debug\NG_Tools.tlb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.csproj.CoreCompileInputs.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGTools\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
E:\My Document\Documents\Visual Studio 2019\Projects\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.dll
|
||||
E:\My Document\Documents\Visual Studio 2019\Projects\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.pdb
|
||||
E:\My Document\Documents\Visual Studio 2019\Projects\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.tlb
|
||||
E:\My Document\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.csproj.CoreCompileInputs.cache
|
||||
E:\My Document\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
E:\My Document\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
E:\My Document\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC(3)\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC(3)\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.pdb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC(3)\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.tlb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC(3)\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC(3)\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.csproj.CoreCompileInputs.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC(3)\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC(3)\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.pdb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC\NGToolsPC\bin\x86\Debug\NG_Tools.tlb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.csproj.CoreCompileInputs.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\NGToolsPC\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\FlowInstegrationMeter\NGToolsPC\bin\x86\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\FlowInstegrationMeter\NGToolsPC\bin\x86\Debug\NG_Tools.pdb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\FlowInstegrationMeter\NGToolsPC\bin\x86\Debug\NG_Tools.tlb
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\FlowInstegrationMeter\AGA8_10\obj\Debug\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\FlowInstegrationMeter\AGA8_10\obj\Debug\NG_Tools.csproj.CoreCompileInputs.cache
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\FlowInstegrationMeter\AGA8_10\obj\Debug\NG_Tools.dll
|
||||
D:\My Documents\Documents\Visual Studio 2019\Projects\FlowInstegrationMeter\AGA8_10\obj\Debug\NG_Tools.pdb
|
||||
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Tools.csprojAssemblyReference.cache
Normal file
BIN
AGA8_10/obj/Debug/NG_Tools.csprojAssemblyReference.cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Tools.csprojResolveAssemblyReference.cache
Normal file
BIN
AGA8_10/obj/Debug/NG_Tools.csprojResolveAssemblyReference.cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Tools.dll
Normal file
BIN
AGA8_10/obj/Debug/NG_Tools.dll
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Debug/NG_Tools.pdb
Normal file
BIN
AGA8_10/obj/Debug/NG_Tools.pdb
Normal file
Binary file not shown.
BIN
AGA8_10/obj/NG_Tools.csproj.UnmanagedRegistration.cache
Normal file
BIN
AGA8_10/obj/NG_Tools.csproj.UnmanagedRegistration.cache
Normal file
Binary file not shown.
Binary file not shown.
@ -0,0 +1 @@
|
||||
ac7dff52d59b5a0ed089bc9959ede1638673797d
|
||||
15
AGA8_10/obj/Release/NG_Tools.csproj.FileListAbsolute.txt
Normal file
15
AGA8_10/obj/Release/NG_Tools.csproj.FileListAbsolute.txt
Normal file
@ -0,0 +1,15 @@
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Release\NG_Tools.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Release\NG_Tools.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Release\NG_Tools.dll
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Release\NG_Tools.pdb
|
||||
E:\ldy\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Release\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Release\NG_Tools.dll
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\bin\Release\NG_Tools.pdb
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Release\NG_Tools.csprojAssemblyReference.cache
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Release\NG_Tools.dll
|
||||
D:\MyDocument\Documents\Visual Studio 2019\projects\NGTools\AGA8_10\obj\Release\NG_Tools.pdb
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Release\NG_Tools.dll
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\bin\Release\NG_Tools.pdb
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Release\NG_Tools.csprojAssemblyReference.cache
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Release\NG_Tools.dll
|
||||
E:\My Documents\Documents\Visual Studio 2013\Projects\NGTools\AGA8_10\obj\Release\NG_Tools.pdb
|
||||
BIN
AGA8_10/obj/Release/NG_Tools.csprojAssemblyReference.cache
Normal file
BIN
AGA8_10/obj/Release/NG_Tools.csprojAssemblyReference.cache
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Release/NG_Tools.dll
Normal file
BIN
AGA8_10/obj/Release/NG_Tools.dll
Normal file
Binary file not shown.
BIN
AGA8_10/obj/Release/NG_Tools.pdb
Normal file
BIN
AGA8_10/obj/Release/NG_Tools.pdb
Normal file
Binary file not shown.
31
NGToolsPC.sln
Normal file
31
NGToolsPC.sln
Normal file
@ -0,0 +1,31 @@
|
||||
|
||||
Microsoft Visual Studio Solution File, Format Version 12.00
|
||||
# Visual Studio 15
|
||||
VisualStudioVersion = 15.0.28307.1321
|
||||
MinimumVisualStudioVersion = 10.0.40219.1
|
||||
Project("{FAE04EC0-301F-11D3-BF4B-00C04F79EFBC}") = "NGToolsPC", "NGToolsPC\NGToolsPC.csproj", "{7A3AD680-49E7-4498-8565-38F69C2F7413}"
|
||||
EndProject
|
||||
Global
|
||||
GlobalSection(SolutionConfigurationPlatforms) = preSolution
|
||||
Debug|Any CPU = Debug|Any CPU
|
||||
Debug|x86 = Debug|x86
|
||||
Release|Any CPU = Release|Any CPU
|
||||
Release|x86 = Release|x86
|
||||
EndGlobalSection
|
||||
GlobalSection(ProjectConfigurationPlatforms) = postSolution
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Debug|Any CPU.ActiveCfg = Debug|Any CPU
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Debug|Any CPU.Build.0 = Debug|Any CPU
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Debug|x86.ActiveCfg = Debug|x86
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Debug|x86.Build.0 = Debug|x86
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Release|Any CPU.ActiveCfg = Release|Any CPU
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Release|Any CPU.Build.0 = Release|Any CPU
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Release|x86.ActiveCfg = Release|x86
|
||||
{7A3AD680-49E7-4498-8565-38F69C2F7413}.Release|x86.Build.0 = Release|x86
|
||||
EndGlobalSection
|
||||
GlobalSection(SolutionProperties) = preSolution
|
||||
HideSolutionNode = FALSE
|
||||
EndGlobalSection
|
||||
GlobalSection(ExtensibilityGlobals) = postSolution
|
||||
SolutionGuid = {EC16CC88-BCFE-478A-B817-46F885B5BC17}
|
||||
EndGlobalSection
|
||||
EndGlobal
|
||||
BIN
NGToolsPC/.vs/NGToolsPC/v15/.suo
Normal file
BIN
NGToolsPC/.vs/NGToolsPC/v15/.suo
Normal file
Binary file not shown.
0
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/db.lock
Normal file
0
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/db.lock
Normal file
BIN
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/storage.ide
Normal file
BIN
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/storage.ide
Normal file
Binary file not shown.
BIN
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/storage.ide-shm
Normal file
BIN
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/storage.ide-shm
Normal file
Binary file not shown.
BIN
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/storage.ide-wal
Normal file
BIN
NGToolsPC/.vs/NGToolsPC/v15/Server/sqlite3/storage.ide-wal
Normal file
Binary file not shown.
42
NGToolsPC/.vscode/launch.json
vendored
Normal file
42
NGToolsPC/.vscode/launch.json
vendored
Normal file
@ -0,0 +1,42 @@
|
||||
{
|
||||
// 使用 IntelliSense 了解相关属性。
|
||||
// 悬停以查看现有属性的描述。
|
||||
// 欲了解更多信息，请访问: https://go.microsoft.com/fwlink/?linkid=830387
|
||||
"version": "0.2.0",
|
||||
"configurations": [
|
||||
{
|
||||
"name": ".NET Core Launch (console)",
|
||||
"type": "coreclr",
|
||||
"request": "launch",
|
||||
"WARNING01": "*********************************************************************************",
|
||||
"WARNING02": "The C# extension was unable to automatically decode projects in the current",
|
||||
"WARNING03": "workspace to create a runnable launch.json file. A template launch.json file has",
|
||||
"WARNING04": "been created as a placeholder.",
|
||||
"WARNING05": "",
|
||||
"WARNING06": "If OmniSharp is currently unable to load your project, you can attempt to resolve",
|
||||
"WARNING07": "this by restoring any missing project dependencies (example: run 'dotnet restore')",
|
||||
"WARNING08": "and by fixing any reported errors from building the projects in your workspace.",
|
||||
"WARNING09": "If this allows OmniSharp to now load your project then --",
|
||||
"WARNING10": " * Delete this file",
|
||||
"WARNING11": " * Open the Visual Studio Code command palette (View->Command Palette)",
|
||||
"WARNING12": " * run the command: '.NET: Generate Assets for Build and Debug'.",
|
||||
"WARNING13": "",
|
||||
"WARNING14": "If your project requires a more complex launch configuration, you may wish to delete",
|
||||
"WARNING15": "this configuration and pick a different template using the 'Add Configuration...'",
|
||||
"WARNING16": "button at the bottom of this file.",
|
||||
"WARNING17": "*********************************************************************************",
|
||||
"preLaunchTask": "build",
|
||||
"program": "${workspaceFolder}/bin/Debug/<insert-target-framework-here>/<insert-project-name-here>.dll",
|
||||
"args": [],
|
||||
"cwd": "${workspaceFolder}",
|
||||
"console": "internalConsole",
|
||||
"stopAtEntry": false
|
||||
},
|
||||
{
|
||||
"name": ".NET Core Attach",
|
||||
"type": "coreclr",
|
||||
"request": "attach",
|
||||
"processId": "${command:pickProcess}"
|
||||
}
|
||||
]
|
||||
}
|
||||
199
NGToolsPC/AboutBox1.Designer.cs
generated
Normal file
199
NGToolsPC/AboutBox1.Designer.cs
generated
Normal file
@ -0,0 +1,199 @@
|
||||
namespace NGToolsPC
|
||||
{
|
||||
partial class AboutBox1
|
||||
{
|
||||
/// <summary>
|
||||
/// 必需的设计器变量。
|
||||
/// </summary>
|
||||
private System.ComponentModel.IContainer components = null;
|
||||
|
||||
/// <summary>
|
||||
/// 清理所有正在使用的资源。
|
||||
/// </summary>
|
||||
protected override void Dispose(bool disposing)
|
||||
{
|
||||
if (disposing && (components != null))
|
||||
{
|
||||
components.Dispose();
|
||||
}
|
||||
base.Dispose(disposing);
|
||||
}
|
||||
|
||||
#region Windows 窗体设计器生成的代码
|
||||
|
||||
/// <summary>
|
||||
/// 设计器支持所需的方法 - 不要修改
|
||||
/// 使用代码编辑器修改此方法的内容。
|
||||
/// </summary>
|
||||
private void InitializeComponent()
|
||||
{
|
||||
System.ComponentModel.ComponentResourceManager resources = new System.ComponentModel.ComponentResourceManager(typeof(AboutBox1));
|
||||
this.tableLayoutPanel = new System.Windows.Forms.TableLayoutPanel();
|
||||
this.logoPictureBox = new System.Windows.Forms.PictureBox();
|
||||
this.labelProductName = new System.Windows.Forms.Label();
|
||||
this.labelVersion = new System.Windows.Forms.Label();
|
||||
this.labelCopyright = new System.Windows.Forms.Label();
|
||||
this.labelCompanyName = new System.Windows.Forms.Label();
|
||||
this.textBoxDescription = new System.Windows.Forms.TextBox();
|
||||
this.okButton = new System.Windows.Forms.Button();
|
||||
this.textBox1 = new System.Windows.Forms.TextBox();
|
||||
this.tableLayoutPanel.SuspendLayout();
|
||||
((System.ComponentModel.ISupportInitialize)(this.logoPictureBox)).BeginInit();
|
||||
this.SuspendLayout();
|
||||
//
|
||||
// tableLayoutPanel
|
||||
//
|
||||
this.tableLayoutPanel.ColumnCount = 2;
|
||||
this.tableLayoutPanel.ColumnStyles.Add(new System.Windows.Forms.ColumnStyle(System.Windows.Forms.SizeType.Percent, 33F));
|
||||
this.tableLayoutPanel.ColumnStyles.Add(new System.Windows.Forms.ColumnStyle(System.Windows.Forms.SizeType.Percent, 67F));
|
||||
this.tableLayoutPanel.Controls.Add(this.logoPictureBox, 0, 0);
|
||||
this.tableLayoutPanel.Controls.Add(this.labelProductName, 1, 0);
|
||||
this.tableLayoutPanel.Controls.Add(this.labelVersion, 1, 1);
|
||||
this.tableLayoutPanel.Controls.Add(this.labelCopyright, 1, 2);
|
||||
this.tableLayoutPanel.Controls.Add(this.labelCompanyName, 1, 3);
|
||||
this.tableLayoutPanel.Controls.Add(this.textBoxDescription, 1, 4);
|
||||
this.tableLayoutPanel.Controls.Add(this.okButton, 1, 5);
|
||||
this.tableLayoutPanel.Controls.Add(this.textBox1, 1, 6);
|
||||
this.tableLayoutPanel.Dock = System.Windows.Forms.DockStyle.Fill;
|
||||
this.tableLayoutPanel.Location = new System.Drawing.Point(9, 8);
|
||||
this.tableLayoutPanel.Name = "tableLayoutPanel";
|
||||
this.tableLayoutPanel.RowCount = 7;
|
||||
this.tableLayoutPanel.RowStyles.Add(new System.Windows.Forms.RowStyle(System.Windows.Forms.SizeType.Percent, 10F));
|
||||
this.tableLayoutPanel.RowStyles.Add(new System.Windows.Forms.RowStyle(System.Windows.Forms.SizeType.Percent, 10F));
|
||||
this.tableLayoutPanel.RowStyles.Add(new System.Windows.Forms.RowStyle(System.Windows.Forms.SizeType.Percent, 10F));
|
||||
this.tableLayoutPanel.RowStyles.Add(new System.Windows.Forms.RowStyle(System.Windows.Forms.SizeType.Percent, 10F));
|
||||
this.tableLayoutPanel.RowStyles.Add(new System.Windows.Forms.RowStyle(System.Windows.Forms.SizeType.Percent, 50F));
|
||||
this.tableLayoutPanel.RowStyles.Add(new System.Windows.Forms.RowStyle(System.Windows.Forms.SizeType.Percent, 10F));
|
||||
this.tableLayoutPanel.RowStyles.Add(new System.Windows.Forms.RowStyle(System.Windows.Forms.SizeType.Absolute, 20F));
|
||||
this.tableLayoutPanel.Size = new System.Drawing.Size(658, 285);
|
||||
this.tableLayoutPanel.TabIndex = 0;
|
||||
//
|
||||
// logoPictureBox
|
||||
//
|
||||
this.logoPictureBox.Dock = System.Windows.Forms.DockStyle.Fill;
|
||||
this.logoPictureBox.Image = ((System.Drawing.Image)(resources.GetObject("logoPictureBox.Image")));
|
||||
this.logoPictureBox.InitialImage = ((System.Drawing.Image)(resources.GetObject("logoPictureBox.InitialImage")));
|
||||
this.logoPictureBox.Location = new System.Drawing.Point(3, 3);
|
||||
this.logoPictureBox.Name = "logoPictureBox";
|
||||
this.tableLayoutPanel.SetRowSpan(this.logoPictureBox, 7);
|
||||
this.logoPictureBox.Size = new System.Drawing.Size(211, 279);
|
||||
this.logoPictureBox.SizeMode = System.Windows.Forms.PictureBoxSizeMode.StretchImage;
|
||||
this.logoPictureBox.TabIndex = 12;
|
||||
this.logoPictureBox.TabStop = false;
|
||||
//
|
||||
// labelProductName
|
||||
//
|
||||
this.labelProductName.Dock = System.Windows.Forms.DockStyle.Fill;
|
||||
this.labelProductName.Location = new System.Drawing.Point(223, 0);
|
||||
this.labelProductName.Margin = new System.Windows.Forms.Padding(6, 0, 3, 0);
|
||||
this.labelProductName.MaximumSize = new System.Drawing.Size(0, 16);
|
||||
this.labelProductName.Name = "labelProductName";
|
||||
this.labelProductName.Size = new System.Drawing.Size(432, 16);
|
||||
this.labelProductName.TabIndex = 19;
|
||||
this.labelProductName.Text = "产品名称";
|
||||
this.labelProductName.TextAlign = System.Drawing.ContentAlignment.MiddleLeft;
|
||||
//
|
||||
// labelVersion
|
||||
//
|
||||
this.labelVersion.Dock = System.Windows.Forms.DockStyle.Fill;
|
||||
this.labelVersion.Location = new System.Drawing.Point(223, 26);
|
||||
this.labelVersion.Margin = new System.Windows.Forms.Padding(6, 0, 3, 0);
|
||||
this.labelVersion.MaximumSize = new System.Drawing.Size(0, 16);
|
||||
this.labelVersion.Name = "labelVersion";
|
||||
this.labelVersion.Size = new System.Drawing.Size(432, 16);
|
||||
this.labelVersion.TabIndex = 0;
|
||||
this.labelVersion.Text = "版本";
|
||||
this.labelVersion.TextAlign = System.Drawing.ContentAlignment.MiddleLeft;
|
||||
//
|
||||
// labelCopyright
|
||||
//
|
||||
this.labelCopyright.Dock = System.Windows.Forms.DockStyle.Fill;
|
||||
this.labelCopyright.Location = new System.Drawing.Point(223, 52);
|
||||
this.labelCopyright.Margin = new System.Windows.Forms.Padding(6, 0, 3, 0);
|
||||
this.labelCopyright.MaximumSize = new System.Drawing.Size(0, 16);
|
||||
this.labelCopyright.Name = "labelCopyright";
|
||||
this.labelCopyright.Size = new System.Drawing.Size(432, 16);
|
||||
this.labelCopyright.TabIndex = 21;
|
||||
this.labelCopyright.Text = "版权";
|
||||
this.labelCopyright.TextAlign = System.Drawing.ContentAlignment.MiddleLeft;
|
||||
//
|
||||
// labelCompanyName
|
||||
//
|
||||
this.labelCompanyName.Dock = System.Windows.Forms.DockStyle.Fill;
|
||||
this.labelCompanyName.Location = new System.Drawing.Point(223, 78);
|
||||
this.labelCompanyName.Margin = new System.Windows.Forms.Padding(6, 0, 3, 0);
|
||||
this.labelCompanyName.MaximumSize = new System.Drawing.Size(0, 16);
|
||||
this.labelCompanyName.Name = "labelCompanyName";
|
||||
this.labelCompanyName.Size = new System.Drawing.Size(432, 16);
|
||||
this.labelCompanyName.TabIndex = 22;
|
||||
this.labelCompanyName.Text = "公司名称";
|
||||
this.labelCompanyName.TextAlign = System.Drawing.ContentAlignment.MiddleLeft;
|
||||
//
|
||||
// textBoxDescription
|
||||
//
|
||||
this.textBoxDescription.Dock = System.Windows.Forms.DockStyle.Fill;
|
||||
this.textBoxDescription.Location = new System.Drawing.Point(223, 107);
|
||||
this.textBoxDescription.Margin = new System.Windows.Forms.Padding(6, 3, 3, 3);
|
||||
this.textBoxDescription.Multiline = true;
|
||||
this.textBoxDescription.Name = "textBoxDescription";
|
||||
this.textBoxDescription.ReadOnly = true;
|
||||
this.textBoxDescription.ScrollBars = System.Windows.Forms.ScrollBars.Both;
|
||||
this.textBoxDescription.Size = new System.Drawing.Size(432, 126);
|
||||
this.textBoxDescription.TabIndex = 23;
|
||||
this.textBoxDescription.TabStop = false;
|
||||
this.textBoxDescription.Text = resources.GetString("textBoxDescription.Text");
|
||||
//
|
||||
// okButton
|
||||
//
|
||||
this.okButton.Anchor = ((System.Windows.Forms.AnchorStyles)((System.Windows.Forms.AnchorStyles.Bottom | System.Windows.Forms.AnchorStyles.Right)));
|
||||
this.okButton.DialogResult = System.Windows.Forms.DialogResult.Cancel;
|
||||
this.okButton.Location = new System.Drawing.Point(580, 239);
|
||||
this.okButton.Name = "okButton";
|
||||
this.okButton.Size = new System.Drawing.Size(75, 20);
|
||||
this.okButton.TabIndex = 24;
|
||||
this.okButton.Text = "确定(&O)";
|
||||
//
|
||||
// textBox1
|
||||
//
|
||||
this.textBox1.Location = new System.Drawing.Point(220, 265);
|
||||
this.textBox1.Name = "textBox1";
|
||||
this.textBox1.Size = new System.Drawing.Size(435, 21);
|
||||
this.textBox1.TabIndex = 25;
|
||||
//
|
||||
// AboutBox1
|
||||
//
|
||||
this.AcceptButton = this.okButton;
|
||||
this.AutoScaleDimensions = new System.Drawing.SizeF(6F, 12F);
|
||||
this.AutoScaleMode = System.Windows.Forms.AutoScaleMode.Font;
|
||||
this.ClientSize = new System.Drawing.Size(676, 301);
|
||||
this.Controls.Add(this.tableLayoutPanel);
|
||||
this.FormBorderStyle = System.Windows.Forms.FormBorderStyle.FixedDialog;
|
||||
this.MaximizeBox = false;
|
||||
this.MinimizeBox = false;
|
||||
this.Name = "AboutBox1";
|
||||
this.Padding = new System.Windows.Forms.Padding(9, 8, 9, 8);
|
||||
this.ShowIcon = false;
|
||||
this.ShowInTaskbar = false;
|
||||
this.StartPosition = System.Windows.Forms.FormStartPosition.CenterParent;
|
||||
this.Text = "关于";
|
||||
this.Load += new System.EventHandler(this.AboutBox1_Load);
|
||||
this.tableLayoutPanel.ResumeLayout(false);
|
||||
this.tableLayoutPanel.PerformLayout();
|
||||
((System.ComponentModel.ISupportInitialize)(this.logoPictureBox)).EndInit();
|
||||
this.ResumeLayout(false);
|
||||
|
||||
}
|
||||
|
||||
#endregion
|
||||
|
||||
private System.Windows.Forms.TableLayoutPanel tableLayoutPanel;
|
||||
private System.Windows.Forms.PictureBox logoPictureBox;
|
||||
private System.Windows.Forms.Label labelProductName;
|
||||
private System.Windows.Forms.Label labelVersion;
|
||||
private System.Windows.Forms.Label labelCopyright;
|
||||
private System.Windows.Forms.Label labelCompanyName;
|
||||
private System.Windows.Forms.TextBox textBoxDescription;
|
||||
private System.Windows.Forms.Button okButton;
|
||||
private System.Windows.Forms.TextBox textBox1;
|
||||
}
|
||||
}
|
||||
113
NGToolsPC/AboutBox1.cs
Normal file
113
NGToolsPC/AboutBox1.cs
Normal file
@ -0,0 +1,113 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
using System.ComponentModel;
|
||||
using System.Drawing;
|
||||
using System.Linq;
|
||||
using System.Reflection;
|
||||
using System.Windows.Forms;
|
||||
|
||||
namespace NGToolsPC
|
||||
{
|
||||
partial class AboutBox1 : Form
|
||||
{
|
||||
public AboutBox1()
|
||||
{
|
||||
InitializeComponent();
|
||||
this.Text = String.Format("关于 {0}", AssemblyTitle);
|
||||
this.labelProductName.Text = AssemblyProduct;
|
||||
this.labelVersion.Text = String.Format("版本 {0}", AssemblyVersion);
|
||||
this.labelCopyright.Text = AssemblyCopyright;
|
||||
this.labelCompanyName.Text = AssemblyCompany;
|
||||
//this.textBoxDescription.Text = AssemblyDescription;
|
||||
}
|
||||
|
||||
#region 程序集特性访问器
|
||||
|
||||
public string AssemblyTitle
|
||||
{
|
||||
get
|
||||
{
|
||||
object[] attributes = Assembly.GetExecutingAssembly().GetCustomAttributes(typeof(AssemblyTitleAttribute), false);
|
||||
if (attributes.Length > 0)
|
||||
{
|
||||
AssemblyTitleAttribute titleAttribute = (AssemblyTitleAttribute)attributes[0];
|
||||
if (titleAttribute.Title != "")
|
||||
{
|
||||
return titleAttribute.Title;
|
||||
}
|
||||
}
|
||||
return System.IO.Path.GetFileNameWithoutExtension(Assembly.GetExecutingAssembly().CodeBase);
|
||||
}
|
||||
}
|
||||
|
||||
public string AssemblyVersion
|
||||
{
|
||||
get
|
||||
{
|
||||
return Assembly.GetExecutingAssembly().GetName().Version.ToString();
|
||||
}
|
||||
}
|
||||
|
||||
public string AssemblyDescription
|
||||
{
|
||||
get
|
||||
{
|
||||
object[] attributes = Assembly.GetExecutingAssembly().GetCustomAttributes(typeof(AssemblyDescriptionAttribute), false);
|
||||
if (attributes.Length == 0)
|
||||
{
|
||||
return "";
|
||||
}
|
||||
return ((AssemblyDescriptionAttribute)attributes[0]).Description;
|
||||
}
|
||||
}
|
||||
|
||||
public string AssemblyProduct
|
||||
{
|
||||
get
|
||||
{
|
||||
object[] attributes = Assembly.GetExecutingAssembly().GetCustomAttributes(typeof(AssemblyProductAttribute), false);
|
||||
if (attributes.Length == 0)
|
||||
{
|
||||
return "";
|
||||
}
|
||||
return ((AssemblyProductAttribute)attributes[0]).Product;
|
||||
}
|
||||
}
|
||||
|
||||
public string AssemblyCopyright
|
||||
{
|
||||
get
|
||||
{
|
||||
object[] attributes = Assembly.GetExecutingAssembly().GetCustomAttributes(typeof(AssemblyCopyrightAttribute), false);
|
||||
if (attributes.Length == 0)
|
||||
{
|
||||
return "";
|
||||
}
|
||||
return ((AssemblyCopyrightAttribute)attributes[0]).Copyright;
|
||||
}
|
||||
}
|
||||
|
||||
public string AssemblyCompany
|
||||
{
|
||||
get
|
||||
{
|
||||
object[] attributes = Assembly.GetExecutingAssembly().GetCustomAttributes(typeof(AssemblyCompanyAttribute), false);
|
||||
if (attributes.Length == 0)
|
||||
{
|
||||
return "";
|
||||
}
|
||||
return ((AssemblyCompanyAttribute)attributes[0]).Company;
|
||||
}
|
||||
}
|
||||
#endregion
|
||||
|
||||
private void AboutBox1_Load(object sender, EventArgs e)
|
||||
{
|
||||
MachineInfo info = new MachineInfo();
|
||||
string strCpu = info.GetCPUSerialNumber();
|
||||
string strDisk = info.GetHardDiskSerialNumber();
|
||||
|
||||
this.textBox1.Text ="机器码："+ strCpu + "@" + strDisk;
|
||||
}
|
||||
}
|
||||
}
|
||||
4200
NGToolsPC/AboutBox1.resx
Normal file
4200
NGToolsPC/AboutBox1.resx
Normal file
File diff suppressed because it is too large
Load Diff
1250
NGToolsPC/Detail.cs
Normal file
1250
NGToolsPC/Detail.cs
Normal file
File diff suppressed because it is too large
Load Diff
1826
NGToolsPC/FlowCal-副本20210318074607.cs
Normal file
1826
NGToolsPC/FlowCal-副本20210318074607.cs
Normal file
File diff suppressed because it is too large
Load Diff
1826
NGToolsPC/FlowCal.cs
Normal file
1826
NGToolsPC/FlowCal.cs
Normal file
File diff suppressed because it is too large
Load Diff
11
NGToolsPC/FlowCalGB2624.cs
Normal file
11
NGToolsPC/FlowCalGB2624.cs
Normal file
@ -0,0 +1,11 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
using System.Linq;
|
||||
using System.Text;
|
||||
|
||||
namespace NGToolsPC
|
||||
{
|
||||
class FlowCalGB2624
|
||||
{
|
||||
}
|
||||
}
|
||||
179
NGToolsPC/GB11062.cs
Normal file
179
NGToolsPC/GB11062.cs
Normal file
@ -0,0 +1,179 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
using System.Text;
|
||||
|
||||
namespace NG_Tools
|
||||
{
|
||||
public class GB11062
|
||||
{
|
||||
|
||||
int iNCC;// number of components
|
||||
int[] aiCID = new int[21];// component IDs
|
||||
double[] dXi = new double[21];// mole fraction of component i
|
||||
Detail ptDetail;
|
||||
public GB11062()
|
||||
{
|
||||
|
||||
ptDetail = new Detail();
|
||||
for (int i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++) dXi[i] = 0;
|
||||
|
||||
|
||||
}// Detail()
|
||||
public void Run(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
int i;
|
||||
// Check for gas composition change
|
||||
ptAGA10.bForceUpdate = (ptAGA10.bForceUpdate || ptDetail.compositionchange(ref ptAGA10));
|
||||
// assign component IDs and values
|
||||
if (ptAGA10.bForceUpdate)
|
||||
{
|
||||
iNCC = -1;
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
if (ptAGA10.adMixture[i] > 0.0)
|
||||
{
|
||||
iNCC = iNCC + 1;
|
||||
aiCID[iNCC] = i;
|
||||
dXi[iNCC] = ptAGA10.adMixture[i];
|
||||
}
|
||||
}
|
||||
iNCC = iNCC + 1;
|
||||
//calculate composition dependent quantities; ported from original
|
||||
//FORTRAN functions paramdl() and chardl()
|
||||
GasPropsCal(ref ptAGA10);
|
||||
}
|
||||
}
|
||||
|
||||
void GasPropsCal(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
double[] adTableMri = new double[NG_Cal.NUMBEROFCOMPONENTS] { 16.0430, 28.0135, 44.0100, 30.0700, 44.0970, 18.0153, 34.0820, 2.0159, 28.0100, 31.9988, 58.1230, 58.1230, 72.1500, 72.1500, 86.1770, 100.2040, 114.2310, 128.2580, 142.2850, 4.0026, 39.9480 };
|
||||
double[] adTablePc = new double[NG_Cal.NUMBEROFCOMPONENTS] { 4.604, 3.399, 7.382, 4.88, 4.249, 22.118, 9.005, 1.297, 3.499, 5.081, 3.648, 3.797, 3.381, 3.369, 3.012, 2.736, 2.486, 0, 0, 0.2275, 4.876 };
|
||||
double[] adTableTc = new double[NG_Cal.NUMBEROFCOMPONENTS] { 190.55, 126.1, 304.19, 305.43, 369.82, 647.3, 373.5, 33.2, 132.92, 154.7, 408.13, 425.16, 460.39, 469.6, 507.4, 540.2, 568.76, 0, 0, 5.2, 150.82 };
|
||||
double[] adTableBzsx = new double[NG_Cal.NUMBEROFCOMPONENTS] { 15, 0, 0, 13, 9.5, 0, 45.5, 74.2, 74.2, 0, 8.4, 8.4, 8.3, 8.3, 7.7, 7.0, 0, 0, 0, 0, 0 };
|
||||
double[] adTableBzxx = new double[NG_Cal.NUMBEROFCOMPONENTS] { 5.0, 0, 0, 2.9, 2.1, 0, 4.3, 4.0, 12.5, 0, 1.8, 1.8, 1.4, 1.4, 1.2, 1.0, 0.96, 0, 0, 0, 0 };
|
||||
double[,] adTableZn = new double[3, NG_Cal.NUMBEROFCOMPONENTS]
|
||||
{{0.9976,0.9995,0.9933,0.99,0.9789,0.93,0.99,1.0006,0.9993,0.999,0.958,0.9572,0.9377,0.918,0.892,0.83,0.742,0.613,0.434,1.0005,0.999},
|
||||
{0.998,0.9997,0.9944,0.9915,0.9821,0.945,0.99,1.0006,0.9995,0.9992,0.968,0.965,0.948,0.937,0.913,0.866,0.802,0.71,0.584,1.0005,0.9992},
|
||||
{0.9981,0.9997,0.9944,0.992,0.9834,0.952,0.99,1.0006,0.9996,0.9993,0.971,0.9682,0.953,0.945,0.919,0.876,0.817,0.735,0.623,1.0005,0.9993}};
|
||||
double[,] adTableSqrtbj = new double[3, NG_Cal.NUMBEROFCOMPONENTS]
|
||||
{{0.049,0.0224,0.0819,0.1,0.1453,0.2646,0.1,-0.004,0.0265,0.0316,0.2049,0.2069,0.251,0.2864,0.3286,0.4123,0.5079,0.6221,0.7523,0.0006,0.0316},
|
||||
{0.0447,0.0173,0.0748,0.0922,0.1338,0.2345,0.1,-0.0048,0.0224,0.0283,0.1789,0.1871,0.228,0.251,0.295,0.3661,0.445,0.5385,0.645,0.0002,0.0283},
|
||||
{0.0436,0.0173,0.0728,0.0894,0.1288,0.2191,0.1,-0.0051,0.02,0.0265,0.1703,0.1783,0.2168,0.2345,0.2846,0.3521,0.4278,0.5148,0.614,0,0.0265}};
|
||||
double[,] adTableHhvMol = new double[4, NG_Cal.NUMBEROFCOMPONENTS]
|
||||
{{892.97,0,0,1564.34,2224.01,45.074,562.94,286.63,282.8,0,2874.2,2883.82,3535.98,3542.89,4203.23,4862.87,5522.4,6182.91,6842.69,0,0},
|
||||
{891.56,0,0,1562.14,2221.1,44.433,562.38,286.15,282.91,0,2870.58,2879.76,3531.68,3538.6,4198.24,4857.18,5516.01,6175.82,6834.9,0,0},
|
||||
{891.09,0,0,1561.41,2220.13,44.224,562.19,285.99,282.95,0,2869.38,2878.57,3530.24,3537.17,4196.58,4855.29,5513.88,6173.46,6832.31,0,0},
|
||||
{890.63,0,0,1560.69,2219.17,44.016,562.01,285.83,282.98,0,2868.2,2877.4,3528.83,3535.77,4194.95,4853.43,5511.8,6171.15,6829.77,0,0}};
|
||||
double[,] adTableLhvMol = new double[4, NG_Cal.NUMBEROFCOMPONENTS]
|
||||
{{802.82,0,0,1429.12,2043.71,0,517.87,241.56,282.8,0,2648.83,2658.45,3265.54,3272.45,3887.71,4502.28,5116.73,5732.17,6346.88,0,0},
|
||||
{802.69,0,0,1428.84,2043.37,0,517.95,241.72,282.91,0,2648.42,2657.6,3265.08,3272,3887.21,4501.72,5116.11,5731.49,6346.14,0,0},
|
||||
{802.65,0,0,1428.74,2043.23,0,517.97,241.76,282.95,0,2648.26,2657.45,3264.89,3271.83,3887.01,4501.49,5115.87,5731.22,6345.85,0,0},
|
||||
{802.6,0,0,1428.64,2043.11,0,517.99,241.81,282.98,0,2648.12,2657.32,3264.73,3271.67,3886.84,4501.3,5115.66,5730.99,6345.59,0,0}};
|
||||
|
||||
int i;
|
||||
|
||||
double dMair = 28.9626;
|
||||
double dZair = 0;
|
||||
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
if (ptAGA10.adMixture[i] != 0)
|
||||
{
|
||||
ptAGA10.Pc += adTablePc[i] * ptAGA10.adMixture[i];
|
||||
ptAGA10.TC += adTableTc[i] * ptAGA10.adMixture[i];
|
||||
if (adTableBzsx[i] != 0)
|
||||
{
|
||||
ptAGA10.Bzsx += ptAGA10.adMixture[i] / adTableBzsx[i];
|
||||
ptAGA10.Bzxx += ptAGA10.adMixture[i] / adTableBzxx[i];
|
||||
}
|
||||
|
||||
if (i >= 10 & i <= 18)
|
||||
{
|
||||
ptAGA10.C4j += ptAGA10.adMixture[i] * adTableMri[i];
|
||||
}
|
||||
if (i >= 12 & i <= 18)
|
||||
{
|
||||
ptAGA10.C5j += ptAGA10.adMixture[i] * adTableMri[i];
|
||||
}
|
||||
if (i >= 14 & i <= 18)
|
||||
{
|
||||
ptAGA10.C6j += ptAGA10.adMixture[i] * adTableMri[i];
|
||||
}
|
||||
if (i == 3)
|
||||
{
|
||||
ptAGA10.C2 += ptAGA10.adMixture[i] * adTableMri[i];
|
||||
}
|
||||
|
||||
switch (ptAGA10.dCbtj)
|
||||
{
|
||||
case 2:
|
||||
ptAGA10.dZb11062 += adTableSqrtbj[0, i] * ptAGA10.adMixture[i];
|
||||
dZair = 0.99941;
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dZb11062 += adTableSqrtbj[1, i] * ptAGA10.adMixture[i];
|
||||
|
||||
dZair = 0.99958;
|
||||
break;
|
||||
case 0:
|
||||
ptAGA10.dZb11062 += adTableSqrtbj[2, i] * ptAGA10.adMixture[i];
|
||||
|
||||
dZair = 0.99963;
|
||||
break;
|
||||
}
|
||||
|
||||
switch (ptAGA10.dCbtj_E)
|
||||
{
|
||||
case 0:
|
||||
|
||||
ptAGA10.dHhvMol += adTableHhvMol[0, i] * ptAGA10.adMixture[i];
|
||||
ptAGA10.dLhvMol += adTableLhvMol[0, i] * ptAGA10.adMixture[i];
|
||||
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dHhvMol += adTableHhvMol[1, i] * ptAGA10.adMixture[i];
|
||||
ptAGA10.dLhvMol += adTableLhvMol[1, i] * ptAGA10.adMixture[i];
|
||||
break;
|
||||
case 2:
|
||||
ptAGA10.dHhvMol += adTableHhvMol[2, i] * ptAGA10.adMixture[i];
|
||||
ptAGA10.dLhvMol += adTableLhvMol[2, i] * ptAGA10.adMixture[i];
|
||||
break;
|
||||
case 3:
|
||||
ptAGA10.dHhvMol += adTableHhvMol[3, i] * ptAGA10.adMixture[i];
|
||||
ptAGA10.dLhvMol += adTableLhvMol[3, i] * ptAGA10.adMixture[i];
|
||||
break;
|
||||
}
|
||||
}
|
||||
}
|
||||
ptAGA10.Bzsx = ptAGA10.Bzsx == 0 ? 0 : 1 / ptAGA10.Bzsx;
|
||||
ptAGA10.Bzxx = ptAGA10.Bzxx == 0 ? 0 : 1 / ptAGA10.Bzxx;
|
||||
|
||||
|
||||
ptAGA10.dZb11062 = 1 - ptAGA10.dZb11062 * ptAGA10.dZb11062;
|
||||
ptAGA10.dHhvm = ptAGA10.dHhvMol / ptAGA10.dMrx;
|
||||
ptAGA10.dLhvm = ptAGA10.dLhvMol / ptAGA10.dMrx;
|
||||
ptAGA10.dHhvv = ptAGA10.dHhvMol * ptAGA10.dPb / ptAGA10.dTb / 8314.510 / ptAGA10.dZb11062;
|
||||
ptAGA10.dLhvv = ptAGA10.dLhvMol * ptAGA10.dPb / ptAGA10.dTb / 8314.510 / ptAGA10.dZb11062;
|
||||
ptAGA10.dRD_Ideal11062 = ptAGA10.dMrx / dMair;
|
||||
ptAGA10.dRD_Real11062 = ptAGA10.dRD_Ideal11062 * dZair / ptAGA10.dZb11062;
|
||||
|
||||
ptAGA10.dRhob11062 = ptAGA10.dMrx * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.dRhof11062 = ptAGA10.dMrx * ptAGA10.dPf / 8314.51 / ptAGA10.dTf / ptAGA10.dZf;
|
||||
ptAGA10.dWobbeIndex = ptAGA10.dHhvv / Math.Sqrt(ptAGA10.dRD_Real11062);
|
||||
ptAGA10.C3j = ptAGA10.C4j + ptAGA10.adMixture[4] * adTableMri[4];
|
||||
ptAGA10.C2j = ptAGA10.C3j + ptAGA10.adMixture[3] * adTableMri[3];
|
||||
ptAGA10.C3C4 = ptAGA10.adMixture[4] * adTableMri[4] + ptAGA10.adMixture[10] * adTableMri[10] + ptAGA10.adMixture[11] * adTableMri[11];
|
||||
ptAGA10.TotalC = ptAGA10.C2j + ptAGA10.adMixture[0] * adTableMri[0];
|
||||
|
||||
ptAGA10.TotalC = ptAGA10.TotalC * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.C2 = ptAGA10.C2 * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.C3C4 = ptAGA10.C3C4 * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.C2j = ptAGA10.C2j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.C3j = ptAGA10.C3j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.C4j = ptAGA10.C4j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.C5j = ptAGA10.C5j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
ptAGA10.C6j = ptAGA10.C6j * ptAGA10.dPb / 8314.51 / ptAGA10.dTb / ptAGA10.dZb11062;
|
||||
|
||||
}
|
||||
}
|
||||
}
|
||||
242
NGToolsPC/NGToolsPC.csproj
Normal file
242
NGToolsPC/NGToolsPC.csproj
Normal file
@ -0,0 +1,242 @@
|
||||
<?xml version="1.0" encoding="utf-8"?>
|
||||
<Project ToolsVersion="15.0" xmlns="http://schemas.microsoft.com/developer/msbuild/2003">
|
||||
<Import Project="$(MSBuildExtensionsPath)\$(MSBuildToolsVersion)\Microsoft.Common.props" Condition="Exists('$(MSBuildExtensionsPath)\$(MSBuildToolsVersion)\Microsoft.Common.props')" />
|
||||
<PropertyGroup>
|
||||
<Configuration Condition=" '$(Configuration)' == '' ">Debug</Configuration>
|
||||
<Platform Condition=" '$(Platform)' == '' ">AnyCPU</Platform>
|
||||
<ProjectGuid>{7A3AD680-49E7-4498-8565-38F69C2F7413}</ProjectGuid>
|
||||
<OutputType>WinExe</OutputType>
|
||||
<RootNamespace>NGToolsPC</RootNamespace>
|
||||
<AssemblyName>NGToolsPC</AssemblyName>
|
||||
<TargetFrameworkVersion>v4.0</TargetFrameworkVersion>
|
||||
<FileAlignment>512</FileAlignment>
|
||||
<Deterministic>true</Deterministic>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition=" '$(Configuration)|$(Platform)' == 'Debug|AnyCPU' ">
|
||||
<PlatformTarget>AnyCPU</PlatformTarget>
|
||||
<DebugSymbols>true</DebugSymbols>
|
||||
<DebugType>full</DebugType>
|
||||
<Optimize>false</Optimize>
|
||||
<OutputPath>bin\Debug\</OutputPath>
|
||||
<DefineConstants>DEBUG;TRACE</DefineConstants>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<WarningLevel>4</WarningLevel>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition=" '$(Configuration)|$(Platform)' == 'Release|AnyCPU' ">
|
||||
<PlatformTarget>AnyCPU</PlatformTarget>
|
||||
<DebugType>pdbonly</DebugType>
|
||||
<Optimize>true</Optimize>
|
||||
<OutputPath>bin\Release\</OutputPath>
|
||||
<DefineConstants>TRACE</DefineConstants>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<WarningLevel>4</WarningLevel>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition="'$(Configuration)|$(Platform)' == 'Debug|x86'">
|
||||
<DebugSymbols>true</DebugSymbols>
|
||||
<OutputPath>bin\x86\Debug\</OutputPath>
|
||||
<DefineConstants>DEBUG;TRACE</DefineConstants>
|
||||
<DebugType>full</DebugType>
|
||||
<PlatformTarget>x86</PlatformTarget>
|
||||
<LangVersion>7.3</LangVersion>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<CodeAnalysisRuleSet>MinimumRecommendedRules.ruleset</CodeAnalysisRuleSet>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup Condition="'$(Configuration)|$(Platform)' == 'Release|x86'">
|
||||
<OutputPath>bin\x86\Release\</OutputPath>
|
||||
<DefineConstants>TRACE</DefineConstants>
|
||||
<Optimize>true</Optimize>
|
||||
<DebugType>pdbonly</DebugType>
|
||||
<PlatformTarget>x86</PlatformTarget>
|
||||
<LangVersion>7.3</LangVersion>
|
||||
<ErrorReport>prompt</ErrorReport>
|
||||
<CodeAnalysisRuleSet>MinimumRecommendedRules.ruleset</CodeAnalysisRuleSet>
|
||||
</PropertyGroup>
|
||||
<PropertyGroup>
|
||||
<StartupObject>
|
||||
</StartupObject>
|
||||
</PropertyGroup>
|
||||
<ItemGroup>
|
||||
<Reference Include="AxInterop.DSOFramer, Version=2.3.0.0, Culture=neutral, processorArchitecture=MSIL">
|
||||
<SpecificVersion>False</SpecificVersion>
|
||||
<HintPath>bin\x86\Debug\AxInterop.DSOFramer.dll</HintPath>
|
||||
</Reference>
|
||||
<Reference Include="hasp_net_windows, Version=7.9.22426.60000, Culture=neutral, PublicKeyToken=56120be447701319, processorArchitecture=MSIL">
|
||||
<SpecificVersion>False</SpecificVersion>
|
||||
<HintPath>..\..\..\..\Gemalto\Sentinel LDK 7.10\API\Runtime\DotNet\hasp_net_windows.dll</HintPath>
|
||||
</Reference>
|
||||
<Reference Include="Microsoft.VisualBasic" />
|
||||
<Reference Include="NG_OCX, Version=1.0.4263.31079, Culture=neutral, processorArchitecture=MSIL">
|
||||
<SpecificVersion>False</SpecificVersion>
|
||||
<HintPath>bin\x86\Debug\NG_OCX.dll</HintPath>
|
||||
</Reference>
|
||||
<Reference Include="NPOI, Version=2.2.1.0, Culture=neutral, PublicKeyToken=0df73ec7942b34e1, processorArchitecture=MSIL">
|
||||
<SpecificVersion>False</SpecificVersion>
|
||||
<HintPath>bin\x86\Debug\NPOI.dll</HintPath>
|
||||
</Reference>
|
||||
<Reference Include="NPOI.OOXML, Version=2.2.1.0, Culture=neutral, PublicKeyToken=0df73ec7942b34e1, processorArchitecture=MSIL">
|
||||
<SpecificVersion>False</SpecificVersion>
|
||||
<HintPath>bin\x86\Debug\NPOI.OOXML.dll</HintPath>
|
||||
</Reference>
|
||||
<Reference Include="NPOI.OpenXml4Net, Version=2.2.1.0, Culture=neutral, PublicKeyToken=0df73ec7942b34e1, processorArchitecture=MSIL">
|
||||
<SpecificVersion>False</SpecificVersion>
|
||||
<HintPath>bin\x86\Debug\NPOI.OpenXml4Net.dll</HintPath>
|
||||
</Reference>
|
||||
<Reference Include="NPOI.OpenXmlFormats, Version=2.2.1.0, Culture=neutral, PublicKeyToken=0df73ec7942b34e1, processorArchitecture=MSIL">
|
||||
<SpecificVersion>False</SpecificVersion>
|
||||
<HintPath>bin\x86\Debug\NPOI.OpenXmlFormats.dll</HintPath>
|
||||
</Reference>
|
||||
<Reference Include="System" />
|
||||
<Reference Include="System.Core" />
|
||||
<Reference Include="System.Management" />
|
||||
<Reference Include="System.Runtime.Serialization" />
|
||||
<Reference Include="System.Web.Extensions" />
|
||||
<Reference Include="System.Xml.Linq" />
|
||||
<Reference Include="System.Data.DataSetExtensions" />
|
||||
<Reference Include="Microsoft.CSharp" />
|
||||
<Reference Include="System.Data" />
|
||||
<Reference Include="System.Deployment" />
|
||||
<Reference Include="System.Drawing" />
|
||||
<Reference Include="System.Windows.Forms" />
|
||||
<Reference Include="System.Xml" />
|
||||
</ItemGroup>
|
||||
<ItemGroup>
|
||||
<Compile Include="AboutBox1.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="AboutBox1.Designer.cs">
|
||||
<DependentUpon>AboutBox1.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="Detail.cs" />
|
||||
<Compile Include="FlowCal.cs" />
|
||||
<Compile Include="frmAddJld.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="frmAddJld.Designer.cs">
|
||||
<DependentUpon>frmAddJld.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="frmInputNGCom.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="frmInputNGCom.Designer.cs">
|
||||
<DependentUpon>frmInputNGCom.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="frmJdygl.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="frmJdygl.Designer.cs">
|
||||
<DependentUpon>frmJdygl.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="frmLogin.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="frmLogin.Designer.cs">
|
||||
<DependentUpon>frmLogin.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="frmNgTools.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="frmNgTools.Designer.cs">
|
||||
<DependentUpon>frmNgTools.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="frmPrint.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="frmPrint.Designer.cs">
|
||||
<DependentUpon>frmPrint.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="frmZjcs.cs">
|
||||
<SubType>Form</SubType>
|
||||
</Compile>
|
||||
<Compile Include="frmZjcs.Designer.cs">
|
||||
<DependentUpon>frmZjcs.cs</DependentUpon>
|
||||
</Compile>
|
||||
<Compile Include="GB11062.cs" />
|
||||
<Compile Include="mldPublic.cs" />
|
||||
<Compile Include="NG_Cal.cs" />
|
||||
<Compile Include="Program.cs" />
|
||||
<Compile Include="Properties\AssemblyInfo.cs" />
|
||||
<Compile Include="Therm.cs" />
|
||||
<Compile Include="UnitConvert.cs" />
|
||||
<EmbeddedResource Include="AboutBox1.resx">
|
||||
<DependentUpon>AboutBox1.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="frmAddJld.resx">
|
||||
<DependentUpon>frmAddJld.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="frmInputNGCom.resx">
|
||||
<DependentUpon>frmInputNGCom.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="frmJdygl.resx">
|
||||
<DependentUpon>frmJdygl.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="frmLogin.resx">
|
||||
<DependentUpon>frmLogin.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="frmNgTools.resx">
|
||||
<DependentUpon>frmNgTools.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="frmPrint.resx">
|
||||
<DependentUpon>frmPrint.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="frmZjcs.resx">
|
||||
<DependentUpon>frmZjcs.cs</DependentUpon>
|
||||
</EmbeddedResource>
|
||||
<EmbeddedResource Include="Properties\Resources.resx">
|
||||
<Generator>ResXFileCodeGenerator</Generator>
|
||||
<LastGenOutput>Resources.Designer.cs</LastGenOutput>
|
||||
<SubType>Designer</SubType>
|
||||
</EmbeddedResource>
|
||||
<Compile Include="Properties\Resources.Designer.cs">
|
||||
<AutoGen>True</AutoGen>
|
||||
<DependentUpon>Resources.resx</DependentUpon>
|
||||
</Compile>
|
||||
<None Include="app.config" />
|
||||
<None Include="Properties\Settings.settings">
|
||||
<Generator>SettingsSingleFileGenerator</Generator>
|
||||
<LastGenOutput>Settings.Designer.cs</LastGenOutput>
|
||||
</None>
|
||||
<Compile Include="Properties\Settings.Designer.cs">
|
||||
<AutoGen>True</AutoGen>
|
||||
<DependentUpon>Settings.settings</DependentUpon>
|
||||
<DesignTimeSharedInput>True</DesignTimeSharedInput>
|
||||
</Compile>
|
||||
</ItemGroup>
|
||||
<ItemGroup>
|
||||
<COMReference Include="ADODB">
|
||||
<Guid>{2A75196C-D9EB-4129-B803-931327F72D5C}</Guid>
|
||||
<VersionMajor>2</VersionMajor>
|
||||
<VersionMinor>8</VersionMinor>
|
||||
<Lcid>0</Lcid>
|
||||
<WrapperTool>tlbimp</WrapperTool>
|
||||
<Isolated>False</Isolated>
|
||||
<EmbedInteropTypes>True</EmbedInteropTypes>
|
||||
</COMReference>
|
||||
<COMReference Include="AxDSOFramer">
|
||||
<Guid>{00460180-9E5E-11D5-B7C8-B8269041DD57}</Guid>
|
||||
<VersionMajor>2</VersionMajor>
|
||||
<VersionMinor>3</VersionMinor>
|
||||
<Lcid>0</Lcid>
|
||||
<WrapperTool>aximp</WrapperTool>
|
||||
<Isolated>False</Isolated>
|
||||
</COMReference>
|
||||
<COMReference Include="DSOFramer">
|
||||
<Guid>{00460180-9E5E-11D5-B7C8-B8269041DD57}</Guid>
|
||||
<VersionMajor>2</VersionMajor>
|
||||
<VersionMinor>3</VersionMinor>
|
||||
<Lcid>0</Lcid>
|
||||
<WrapperTool>tlbimp</WrapperTool>
|
||||
<Isolated>False</Isolated>
|
||||
<EmbedInteropTypes>True</EmbedInteropTypes>
|
||||
</COMReference>
|
||||
<COMReference Include="stdole">
|
||||
<Guid>{00020430-0000-0000-C000-000000000046}</Guid>
|
||||
<VersionMajor>2</VersionMajor>
|
||||
<VersionMinor>0</VersionMinor>
|
||||
<Lcid>0</Lcid>
|
||||
<WrapperTool>primary</WrapperTool>
|
||||
<Isolated>False</Isolated>
|
||||
<EmbedInteropTypes>True</EmbedInteropTypes>
|
||||
</COMReference>
|
||||
</ItemGroup>
|
||||
<Import Project="$(MSBuildToolsPath)\Microsoft.CSharp.targets" />
|
||||
</Project>
|
||||
13
NGToolsPC/NGToolsPC.csproj.user
Normal file
13
NGToolsPC/NGToolsPC.csproj.user
Normal file
@ -0,0 +1,13 @@
|
||||
<?xml version="1.0" encoding="utf-8"?>
|
||||
<Project ToolsVersion="Current" xmlns="http://schemas.microsoft.com/developer/msbuild/2003">
|
||||
<PropertyGroup>
|
||||
<PublishUrlHistory>publish\</PublishUrlHistory>
|
||||
<InstallUrlHistory />
|
||||
<SupportUrlHistory />
|
||||
<UpdateUrlHistory />
|
||||
<BootstrapperUrlHistory />
|
||||
<ErrorReportUrlHistory />
|
||||
<FallbackCulture>zh-CN</FallbackCulture>
|
||||
<VerifyUploadedFiles>false</VerifyUploadedFiles>
|
||||
</PropertyGroup>
|
||||
</Project>
|
||||
530
NGToolsPC/NG_Cal.cs
Normal file
530
NGToolsPC/NG_Cal.cs
Normal file
@ -0,0 +1,530 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
|
||||
using System.Runtime.InteropServices;
|
||||
using System.Text;
|
||||
|
||||
namespace NG_Tools
|
||||
{
|
||||
public class NG_Cal
|
||||
{
|
||||
public const int NORMAL = 9000;
|
||||
public const int NG_Cal_INITIALIZED = 9001;
|
||||
public const int MEMORY_ALLOCATION_ERROR = 9002;
|
||||
public const int GENERAL_CALCULATION_FAILURE = 9003;
|
||||
public const int MAX_NUM_OF_ITERATIONS_EXCEEDED = 9004;
|
||||
public const int NEGATIVE_DENSITY_DERIVATIVE = 9005;
|
||||
public const int MAX_DENSITY_IN_BRAKET_EXCEEDED = 9006;
|
||||
/* number of components */
|
||||
public const int NUMBEROFCOMPONENTS = 21;
|
||||
/* maximum number of tries within search routines */
|
||||
public const int MAX_NUM_OF_ITERATIONS = 100;
|
||||
/* default tolerance limits */
|
||||
public const double P_CHG_TOL = 0.001; /* 0.001 Pa */
|
||||
public const double T_CHG_TOL = 0.001; /* 0.001 of a Kelvin */
|
||||
/* maximum allowable P & T */
|
||||
public const double P_MAX = 1.379e8; // maximum pressure (Pa) ~= 20,000 psi
|
||||
public const double P_MIN = 0.0; // maximum pressure = 0
|
||||
public const double T_MAX = 473.15; // maximum temperature (K) ~= 392 F
|
||||
public const double T_MIN = 143.0; // maximum temperature (K) ~= -200 F
|
||||
/* universal gas constant, in two configurations */
|
||||
public const double RGASKJ = 8.314510e-3; /* in kJ mol^-1 K^-1 */
|
||||
public const double RGAS = 8.314510; /* in J mol^-1 K^-1 */
|
||||
/* the main data structure used by this library */
|
||||
public struct GasPropsSTRUCT
|
||||
{ /* corresponds to the control group in meter classes */
|
||||
|
||||
public int lStatus; /* calculation status 计算状态 */
|
||||
public bool bForceUpdate; /*执行全部计算的标志 signal to perform full calculation */
|
||||
public double[] adMixture; /*气体摩尔组成 Composition in mole fraction */
|
||||
public double[] adMixtureV; /*气体体积组成 Composition in mole fraction */
|
||||
public double[] adMixtureD; /*气体质量组成 Composition in mole fraction */
|
||||
public int dCbtj; //参比条件 101325 0,15,20
|
||||
public int dCbtj_E; //燃烧参比条件 101325 0,15,20
|
||||
|
||||
public double dPb; /*参比压力 Contract base Pressure (Pa) */
|
||||
public double dTb; /* 参比温度Contract base temperature (K) */
|
||||
public double dPf; /*绝对压力 Absolute Pressure (Pa) */
|
||||
public double dTf; /*工况温度 Flowing temperature (K) */
|
||||
|
||||
|
||||
// basic output from AGA 8 Detail method
|
||||
public double dMrx; /*分子量 mixture molar mass */
|
||||
public double dZb; /* 标况压缩因子compressibility at contract base condition */
|
||||
public double dZf; /* 工况压缩因子compressibility at flowing condition */
|
||||
public double dFpv; /*超压缩系数 supercompressibility */
|
||||
public double dDb; /* 标况摩尔密度molar density at contract base conditions (moles/dm3) */
|
||||
public double dDf; /*工况摩尔密度 molar density at flowing conditions (moles/dm3) */
|
||||
public double dRhob; /* 标况质量密度mass density at contract base conditions (kg/m3) */
|
||||
public double dRhof; /*工况质量密度 mass density at flowing conditions (kg/m3) */
|
||||
public double dRD_Ideal; /* 理想气体的相对密度ideal gas relative density */
|
||||
public double dRD_Real; /* 真实气体的相对密度real gas relative density */
|
||||
// additional output
|
||||
public double dHo; /*理想气体的比焓 ideal gas specific enthalpy */
|
||||
public double dH; /*真实气体的焓 real gas specific enthalpy (J/kg) */
|
||||
public double dS; /* 真实气体的熵real gas specific entropy (J/kg-mol.K)*/
|
||||
public double dCpi; /*理想气体定压热容 ideal gas constant pressure heat capacity (J/kg-mol.K)*/
|
||||
public double dCp; /* 定压热容real gas constant pressure heat capacity (J/kg-mol.K)*/
|
||||
public double dCv; /*定容积热容 real gas constant volume heat capacity (J/kg-mol.K)*/
|
||||
public double dk; /* 比热比ratio of specific heats */
|
||||
public double dKappa; /*等熵指数 isentropic exponent, denoted with Greek letter kappa */
|
||||
public double dSOS; /* 声速speed of sound (m/s) */
|
||||
public double dCstar; /*临界流函数 critical flow factor C* */
|
||||
|
||||
// 11062 输出
|
||||
|
||||
public double dHhvMol; //摩尔高位发热量
|
||||
public double dLhvMol; //摩尔低位发热量
|
||||
public double dHhvv; //体积高位发热量
|
||||
public double dLhvv; //体积低位发热量
|
||||
public double dHhvm; //质量高位发热量
|
||||
public double dLhvm; //质量地位发热量
|
||||
|
||||
public double dZb11062; //标况压缩因子
|
||||
public double dRhob11062; /* 标况质量密度mass density at contract base conditions (kg/m3) */
|
||||
public double dRhof11062; /*工况质量密度 mass density at flowing conditions (kg/m3) */
|
||||
public double dRD_Ideal11062; /* 理想气体的相对密度ideal gas relative density */
|
||||
public double dRD_Real11062; /* 真实气体的相对密度real gas relative density */
|
||||
public double dWobbeIndex; /* 真实气体的沃泊指数 */
|
||||
|
||||
|
||||
public double Pc; // '临界压力
|
||||
public double TC; /// '临界温度
|
||||
public double Bzsx; // '爆炸上限
|
||||
public double Bzxx; // '爆炸下限
|
||||
public double TotalC; // '总炭含量 (kg/m3)
|
||||
public double C2; // 'C2组分含量 (kg/m3)
|
||||
public double C2j; // 'C2以上组分含量 (kg/m3)
|
||||
public double C3j; // 'C3以上组分含量 (kg/m3)
|
||||
public double C4j; // 'C4以上组分含量 (kg/m3)
|
||||
public double C5j; // 'C5以上组分含量 (kg/m3)
|
||||
public double C6j; // 'C6以上组分含量 (kg/m3)
|
||||
public double C3C4; // 'C3C4组分含量 (kg/m3)
|
||||
|
||||
}
|
||||
public struct FlowParStruct //流量相关参数
|
||||
{
|
||||
//流量计算输入参数信息
|
||||
public int dFlowCalbz; //流量计算标准
|
||||
public int dZcalbz; //压缩因子计算标准
|
||||
public int dCbtj; //计量参比条件压力
|
||||
public double dPb_M; //计量参比条件压力
|
||||
public double dTb_M; //计量参比条件温度
|
||||
public double dPb_E; //燃烧参比条件压力
|
||||
public double dTb_E; //燃烧参比条件温度
|
||||
public double dPatm;//当地大气压
|
||||
public int dPatmUnit;//当地大气压单位
|
||||
public double[] dNG_Compents;//天然气组分
|
||||
|
||||
public int dMeterType;// 流量计类别
|
||||
public int dCoreType;//节流装置类型
|
||||
public int dPtmode; //取压方式
|
||||
public int dPipeType; // 管道类型
|
||||
public double dPipeD; //管道内径
|
||||
public int dLenUnit; //长度单位
|
||||
public double dPipeDtemp; //管道内径参考温度
|
||||
public int dPileDtempUint; //温度单位
|
||||
public int dPipeMaterial; //管道材料
|
||||
|
||||
public double dOrificeD; //孔板孔径
|
||||
public int dOrificeUnit; //长度单位
|
||||
public double dOrificeDtemp; //孔板内径参考温度
|
||||
public int dOrificeDtempUnit; //温度单位
|
||||
public int dOrificeMaterial; //孔板材料
|
||||
public int dOrificeSharpness; //锐利度系数计算方法
|
||||
public double dOrificeRk; //孔板入口圆弧半径
|
||||
public int dOrificeRkLenUint;//长度单位
|
||||
public double dPf;//输入压力
|
||||
public int dPfUnit;//压力单位
|
||||
public int dPfType; //压力类型
|
||||
public double dTf; //输入温度
|
||||
public int dTfUnit;//温度单位
|
||||
public double dDp; //输入差压
|
||||
public int dDpUnit; //压力单位
|
||||
public int dVFlowUnit; //体积流量单位
|
||||
public int dMFlowUnit; //'NG_Par(33) = ComboBox15.SelectedIndex '质量流量单位
|
||||
public int dEFlowUnit; //'NG_Par(34) = ComboBox16.SelectedIndex '能量流量单位
|
||||
public double dCd;//流出系数
|
||||
public double dCdCalMethod;//流出系数计算方法 0 检定证书 0回归公式
|
||||
public double dMeterFactor;//仪表系数
|
||||
public double dPulseNum;//脉冲数
|
||||
|
||||
public double dVFlowMax; //'NG_par(39)＝’最大体积流量
|
||||
public double dVFlowMin; //'NG_par(40)＝’最小体积流量
|
||||
public double dVFlowCon;//'NG_par(41)＝’常用流量
|
||||
public double dPfRangeMin; //'NG_par(42)＝’压力量程
|
||||
public double dPfRangeMax; //'NG_par(42)＝’压力量程
|
||||
public double dDpRangeMin; //'NG_par(43)＝’差压量程
|
||||
public double dDpRangeMax; //'NG_par(43)＝’差压量程
|
||||
public double dTfRangeMin; //'NG_par(44)＝’温度计量程
|
||||
public double dTfRangeMax; //'NG_par(44)＝’温度计量程
|
||||
|
||||
//流量计算输出参数
|
||||
public double dE; //'求渐近速度系数 E
|
||||
public double dFG; //'求相对密度系数 FG
|
||||
public double dFT; //'求流动温度系数 'FT
|
||||
public double dDViscosity; //'求动力粘度 dlnd
|
||||
public double dDExpCoefficient; //'求可膨胀系数
|
||||
public double dRnPipe; //'管道雷诺数
|
||||
public double dBk; //'孔板锐利度系数Bk
|
||||
public double dRoughNessPipe; //'管道粗糙度系数 Gme
|
||||
public double dCdCorrect; //'修正后的流出系数
|
||||
public double dCdNozell; //'喷嘴的流出系数
|
||||
public double dVFlowb;//'标况体积流量 m³、s
|
||||
public double dVFlowf; //'工况体积流量
|
||||
public double dMFlowb;//'标况质量流量
|
||||
public double dEFlowb;//'标况能量流量
|
||||
public double dVelocityFlow;//'管道内天然气流速
|
||||
public double dPressLost;//'压力损失
|
||||
public double dBeta;//'直径比
|
||||
public double dKappa;//'等熵指数
|
||||
|
||||
}
|
||||
|
||||
//public struct SqgyParStruct //输气工艺相关参数
|
||||
//{
|
||||
// public int dCalName; //计算项目
|
||||
// public int dPipleD; //管道内径mm
|
||||
// public int dPipleDw; //管道内径外径mm
|
||||
// public int dPipleBh; //管道壁厚 mm
|
||||
// public double dPipleTotalLength; //管道总长度 km
|
||||
// public double dPiplePointLength; //管道任意点长度 km
|
||||
// public double dPstart; //起点压力终点压力MPa
|
||||
// public double dPend; //终点压力MPa
|
||||
// public double dFlow; //输气能力
|
||||
// public double dRd;//相对密度
|
||||
// public double dZf;//压缩因子
|
||||
// public double[] dNG_Compents;//天然气组分
|
||||
|
||||
// public double dPavg;//管道平均压力
|
||||
// public double dPavgPoint;//管道任意点的平均压力
|
||||
|
||||
|
||||
//}
|
||||
|
||||
/* enumerations for tracking gas components */
|
||||
enum gascomp
|
||||
{
|
||||
XiC1 = 0, XiN2, XiCO2, XiC2, XiC3,
|
||||
XiH2O, XiH2S, XiH2, XiCO, XiO2, XiIC4, XiNC4,
|
||||
XiIC5, XiNC5, XiNC6, XiNC7, XiNC8, XiNC9, XiNC10, XiHe, XiAr
|
||||
};
|
||||
|
||||
|
||||
/* FUNCTION PROTOTYPES */
|
||||
/* prototypes for initialization */
|
||||
// int NG_Cal_Init(void) ; /* initialize library */
|
||||
// int NG_Cal_UnInit(void) ; /* un-initialize library */
|
||||
///* function prototype for basic VOS calculation */
|
||||
// double SOS(ref AGA10.GasPropsSTRUCT ) ;
|
||||
///* function prototype for a C* calculation */
|
||||
// double Crit(ref AGA10.GasPropsSTRUCT , double) ;
|
||||
|
||||
|
||||
|
||||
public Therm ptTherm;
|
||||
public Detail ptDetail;
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : NG_Cal_Init()
|
||||
* Arguments : void
|
||||
* Returns : int
|
||||
* Purpose : Initializes library; creates required objects
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public int NG_Cal_Init()
|
||||
{
|
||||
//create object for calculating density
|
||||
if (null == (ptDetail = new Detail()))
|
||||
{
|
||||
return MEMORY_ALLOCATION_ERROR;
|
||||
}
|
||||
|
||||
//create object for calculating thermodynamic properties
|
||||
if (null == (ptTherm = new Therm()))
|
||||
{
|
||||
return MEMORY_ALLOCATION_ERROR;
|
||||
}
|
||||
|
||||
return NG_Cal_INITIALIZED;
|
||||
|
||||
}// NG_Cal_Init
|
||||
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : NG_Cal_UnInit()
|
||||
* Arguments : void
|
||||
* Returns : int
|
||||
* Purpose : Un-initializes library; deletes objects
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public int NG_Cal_UnInit()
|
||||
{
|
||||
// delete the objects (if they exist)
|
||||
ptDetail = null;
|
||||
ptTherm = null;
|
||||
return 0;
|
||||
|
||||
}// NG_Cal_UnInit
|
||||
|
||||
|
||||
/**************************************************************************
|
||||
* Function : SOS()
|
||||
* Arguments : Pointers to external AGA10 data struct
|
||||
* Returns : double
|
||||
* Purpose : calculates speed of sound and other parameters
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public double SOS(ref GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
// check if library is ready; initialize if necessary
|
||||
if (null == ptDetail || null == ptTherm)
|
||||
{
|
||||
NG_Cal_UnInit();
|
||||
NG_Cal_Init();
|
||||
|
||||
}
|
||||
|
||||
switch (ptAGA10.dCbtj)
|
||||
{
|
||||
case 2:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 273.15;
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 288.15;
|
||||
break;
|
||||
case 0:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 293.15;
|
||||
break;
|
||||
}
|
||||
|
||||
|
||||
//Call function to calculate densities and thermodynamic properties
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
//the basic sound speed calculation doesn't calculate C*; initialize to zero
|
||||
ptAGA10.dCstar = 0.0;
|
||||
|
||||
//return the speed of sound to caller
|
||||
|
||||
return ptAGA10.dSOS;
|
||||
|
||||
}// VOS()
|
||||
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : Crit()
|
||||
* Arguments : Pointers to external AGA10 data struct, Detail and Therm
|
||||
* objects and a double precision float (gas velocity in plenum)
|
||||
* Returns : double
|
||||
* Purpose : calculates C*
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public double Crit(ref NG_Cal.GasPropsSTRUCT ptAGA10, double dPlenumVelocity)
|
||||
{
|
||||
//variables local to function
|
||||
double DH, DDH, S, H;
|
||||
double tolerance = 1.0;
|
||||
double R, P, T, Z;
|
||||
|
||||
int i;
|
||||
|
||||
//check objects for readiness; try to initialize if not
|
||||
if (null == ptDetail || null == ptTherm)
|
||||
{
|
||||
NG_Cal_UnInit();
|
||||
|
||||
if (NG_Cal_INITIALIZED != NG_Cal_Init())
|
||||
{
|
||||
|
||||
ptAGA10.lStatus = MEMORY_ALLOCATION_ERROR; return 0.0;
|
||||
|
||||
}
|
||||
}
|
||||
switch (ptAGA10.dCbtj)
|
||||
{
|
||||
case 2:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 273.15;
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 288.15;
|
||||
break;
|
||||
case 0:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 293.15;
|
||||
break;
|
||||
|
||||
|
||||
}
|
||||
//begin by calculating densities and thermodynamic properties
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
//DH is enthalpy change from plenum to throat; this is our initial guess
|
||||
|
||||
DH = (ptAGA10.dSOS * ptAGA10.dSOS - dPlenumVelocity * dPlenumVelocity) / 2.0;
|
||||
|
||||
//trap plenum conditions before we alter the data stucture's contents
|
||||
S = ptAGA10.dS;
|
||||
|
||||
H = ptAGA10.dH;
|
||||
|
||||
R = ptAGA10.dRhof;
|
||||
P = ptAGA10.dPf;
|
||||
Z = ptAGA10.dZf;
|
||||
T = ptAGA10.dTf;
|
||||
|
||||
//initialize delta of DH to an arbitrary value outside of
|
||||
|
||||
//convergence tolerance
|
||||
DDH = 10.0;
|
||||
|
||||
//Via simple repetition, search for a pressure, temperature and sound speed
|
||||
|
||||
//at a nozzle throat which provide constant enthalpy, given the entropy known
|
||||
//at the plenum. Abort if loop executes more than 100 times without convergence.
|
||||
for (i = 1; i < MAX_NUM_OF_ITERATIONS; i++)
|
||||
{
|
||||
|
||||
// calculate P and T to satisfy H and S
|
||||
ptTherm.HS_Mode(ref ptAGA10, ref ptDetail, H - DH, S, true);
|
||||
|
||||
//calculate new thermo, including SOS
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
//hold DH for tolerance check
|
||||
|
||||
DDH = DH;
|
||||
|
||||
// recalculate DH
|
||||
|
||||
DH = (ptAGA10.dSOS * ptAGA10.dSOS - dPlenumVelocity * dPlenumVelocity) / 2.0;
|
||||
|
||||
// end loop if tolerance reached
|
||||
|
||||
if (Math.Abs(DDH - DH) < tolerance) break;
|
||||
}
|
||||
|
||||
//C* is the real gas critical flow constant (not to be confused with Cperf or CRi)
|
||||
ptAGA10.dCstar = (ptAGA10.dRhof * ptAGA10.dSOS) / Math.Sqrt(R * P * Z);
|
||||
|
||||
//put the original plenum pressure and temperature back
|
||||
|
||||
ptAGA10.dPf = P;
|
||||
ptAGA10.dTf = T;
|
||||
|
||||
//restore fluid props to plenum conditions
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
GB11062 ptGB11062 = new GB11062();
|
||||
|
||||
ptGB11062.Run(ref ptAGA10);
|
||||
|
||||
//return the critical flow function to caller
|
||||
return ptAGA10.dCstar;
|
||||
|
||||
}// Crit()
|
||||
|
||||
/**************************************************************************
|
||||
|
||||
* Function : Crit()
|
||||
* Arguments : Pointers to external AGA10 data struct, Detail and Therm
|
||||
* objects and a double precision float (gas velocity in plenum)
|
||||
* Returns : double
|
||||
* Purpose : calculates C*
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
public double Zcal(ref NG_Cal.GasPropsSTRUCT ptAGA10, double dPlenumVelocity)
|
||||
{
|
||||
//variables local to function
|
||||
|
||||
|
||||
|
||||
//check objects for readiness; try to initialize if not
|
||||
if (null == ptDetail || null == ptTherm)
|
||||
{
|
||||
NG_Cal_UnInit();
|
||||
|
||||
if (NG_Cal_INITIALIZED != NG_Cal_Init())
|
||||
{
|
||||
|
||||
ptAGA10.lStatus = MEMORY_ALLOCATION_ERROR; return 0.0;
|
||||
|
||||
}
|
||||
}
|
||||
switch (ptAGA10.dCbtj)
|
||||
{
|
||||
case 2:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 273.15;
|
||||
break;
|
||||
case 1:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 288.15;
|
||||
break;
|
||||
case 0:
|
||||
ptAGA10.dPb = 101325;
|
||||
ptAGA10.dTb = 293.15;
|
||||
break;
|
||||
|
||||
|
||||
}
|
||||
//begin by calculating densities and thermodynamic properties
|
||||
ptTherm.Run(ref ptAGA10, ref ptDetail);
|
||||
|
||||
|
||||
GB11062 ptGB11062 = new GB11062();
|
||||
|
||||
ptGB11062.Run(ref ptAGA10);
|
||||
|
||||
//return the critical flow function to caller
|
||||
return ptAGA10.dZf;
|
||||
|
||||
}// Z()
|
||||
|
||||
/**************************************************************************
|
||||
* Function : Cperf()
|
||||
* Arguments : pointer to external AGA10 data struct
|
||||
* Returns : double
|
||||
* Purpose : calculates isentropic perfect gas critical flow function
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
double Cperf(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
|
||||
double k, root, exponent;
|
||||
|
||||
k = ptAGA10.dKappa; root = 2.0 / (k + 1.0);
|
||||
exponent = (k + 1.0) / (k - 1.0);
|
||||
|
||||
// isentropic perfect gas critical flow function C*i
|
||||
return (Math.Sqrt(k * Math.Pow(root, exponent)));
|
||||
|
||||
}// Cperf
|
||||
/**************************************************************************
|
||||
* Function : CRi()
|
||||
* Arguments : pointer to external AGA10 data struct
|
||||
* Returns : double
|
||||
* Purpose : calculates isentropic real gas critical flow function CRi
|
||||
* Revisions :
|
||||
**************************************************************************/
|
||||
|
||||
double CRi(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
return (Cperf(ref ptAGA10) / Math.Sqrt(ptAGA10.dZf));
|
||||
}// CRi()
|
||||
}
|
||||
}
|
||||
39
NGToolsPC/Program.cs
Normal file
39
NGToolsPC/Program.cs
Normal file
@ -0,0 +1,39 @@
|
||||
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
using System.Linq;
|
||||
using System.Windows.Forms;
|
||||
|
||||
namespace NGToolsPC
|
||||
{
|
||||
static class Program
|
||||
{
|
||||
/// <summary>
|
||||
/// 应用程序的主入口点。
|
||||
/// </summary>
|
||||
[STAThread]
|
||||
static void Main()
|
||||
{
|
||||
Application.EnableVisualStyles();
|
||||
Application.SetCompatibleTextRenderingDefault(false);
|
||||
|
||||
|
||||
|
||||
|
||||
bool createdNew;//返回是否赋予了使用线程的互斥体初始所属权
|
||||
System.Threading.Mutex instance = new System.Threading.Mutex(true, "MutexName", out createdNew); //同步基元变量
|
||||
if (createdNew) //赋予了线程初始所属权，也就是首次使用互斥体
|
||||
{
|
||||
Application.Run(new frmNgTools());
|
||||
instance.ReleaseMutex();
|
||||
}
|
||||
else
|
||||
{
|
||||
MessageBox.Show("已经有一个程序已经在运行，请不要同时运行多个程序！", "系统提示", MessageBoxButtons.OK, MessageBoxIcon.Error);
|
||||
Application.Exit();
|
||||
}
|
||||
|
||||
|
||||
}
|
||||
}
|
||||
}
|
||||
36
NGToolsPC/Properties/AssemblyInfo.cs
Normal file
36
NGToolsPC/Properties/AssemblyInfo.cs
Normal file
@ -0,0 +1,36 @@
|
||||
using System.Reflection;
|
||||
using System.Runtime.CompilerServices;
|
||||
using System.Runtime.InteropServices;
|
||||
|
||||
// 有关程序集的一般信息由以下
|
||||
// 控制。更改这些特性值可修改
|
||||
// 与程序集关联的信息。
|
||||
[assembly: AssemblyTitle("流量积算仪检定系统（天然气）")]
|
||||
[assembly: AssemblyDescription("说明：为用户提供天然气相关参数计算。计算标准采用GB/T11062 GB/T17747和GB/T 21446等标准算法，计算孔板流量及天然气的物性参数。")]
|
||||
[assembly: AssemblyConfiguration("")]
|
||||
[assembly: AssemblyCompany("")]
|
||||
[assembly: AssemblyProduct("流量积算仪检定系统（天然气）")]
|
||||
[assembly: AssemblyCopyright("Copyright © 2021")]
|
||||
[assembly: AssemblyTrademark("")]
|
||||
[assembly: AssemblyCulture("")]
|
||||
|
||||
// 将 ComVisible 设置为 false 会使此程序集中的类型
|
||||
//对 COM 组件不可见。如果需要从 COM 访问此程序集中的类型
|
||||
//请将此类型的 ComVisible 特性设置为 true。
|
||||
[assembly: ComVisible(false)]
|
||||
|
||||
// 如果此项目向 COM 公开，则下列 GUID 用于类型库的 ID
|
||||
[assembly: Guid("7a3ad680-49e7-4498-8565-38f69c2f7413")]
|
||||
|
||||
// 程序集的版本信息由下列四个值组成:
|
||||
//
|
||||
// 主版本
|
||||
// 次版本
|
||||
// 生成号
|
||||
// 修订号
|
||||
//
|
||||
//可以指定所有这些值，也可以使用“生成号”和“修订号”的默认值
|
||||
//通过使用 "*"，如下所示:
|
||||
// [assembly: AssemblyVersion("1.0.*")]
|
||||
[assembly: AssemblyVersion("1.0.0.0")]
|
||||
[assembly: AssemblyFileVersion("1.0.0.0")]
|
||||
71
NGToolsPC/Properties/Resources.Designer.cs
generated
Normal file
71
NGToolsPC/Properties/Resources.Designer.cs
generated
Normal file
@ -0,0 +1,71 @@
|
||||
//------------------------------------------------------------------------------
|
||||
// <auto-generated>
|
||||
// 此代码由工具生成。
|
||||
// 运行时版本: 4.0.30319.42000
|
||||
//
|
||||
// 对此文件的更改可能导致不正确的行为，如果
|
||||
// 重新生成代码，则所做更改将丢失。
|
||||
// </auto-generated>
|
||||
//------------------------------------------------------------------------------
|
||||
|
||||
namespace NGToolsPC.Properties
|
||||
{
|
||||
|
||||
|
||||
/// <summary>
|
||||
/// 强类型资源类，用于查找本地化字符串等。
|
||||
/// </summary>
|
||||
// 此类是由 StronglyTypedResourceBuilder
|
||||
// 类通过类似于 ResGen 或 Visual Studio 的工具自动生成的。
|
||||
// 若要添加或删除成员，请编辑 .ResX 文件，然后重新运行 ResGen
|
||||
// (以 /str 作为命令选项)，或重新生成 VS 项目。
|
||||
[global::System.CodeDom.Compiler.GeneratedCodeAttribute("System.Resources.Tools.StronglyTypedResourceBuilder", "4.0.0.0")]
|
||||
[global::System.Diagnostics.DebuggerNonUserCodeAttribute()]
|
||||
[global::System.Runtime.CompilerServices.CompilerGeneratedAttribute()]
|
||||
internal class Resources
|
||||
{
|
||||
|
||||
private static global::System.Resources.ResourceManager resourceMan;
|
||||
|
||||
private static global::System.Globalization.CultureInfo resourceCulture;
|
||||
|
||||
[global::System.Diagnostics.CodeAnalysis.SuppressMessageAttribute("Microsoft.Performance", "CA1811:AvoidUncalledPrivateCode")]
|
||||
internal Resources()
|
||||
{
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 返回此类使用的缓存 ResourceManager 实例。
|
||||
/// </summary>
|
||||
[global::System.ComponentModel.EditorBrowsableAttribute(global::System.ComponentModel.EditorBrowsableState.Advanced)]
|
||||
internal static global::System.Resources.ResourceManager ResourceManager
|
||||
{
|
||||
get
|
||||
{
|
||||
if ((resourceMan == null))
|
||||
{
|
||||
global::System.Resources.ResourceManager temp = new global::System.Resources.ResourceManager("NGToolsPC.Properties.Resources", typeof(Resources).Assembly);
|
||||
resourceMan = temp;
|
||||
}
|
||||
return resourceMan;
|
||||
}
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 覆盖当前线程的 CurrentUICulture 属性
|
||||
/// 使用此强类型的资源类的资源查找。
|
||||
/// </summary>
|
||||
[global::System.ComponentModel.EditorBrowsableAttribute(global::System.ComponentModel.EditorBrowsableState.Advanced)]
|
||||
internal static global::System.Globalization.CultureInfo Culture
|
||||
{
|
||||
get
|
||||
{
|
||||
return resourceCulture;
|
||||
}
|
||||
set
|
||||
{
|
||||
resourceCulture = value;
|
||||
}
|
||||
}
|
||||
}
|
||||
}
|
||||
117
NGToolsPC/Properties/Resources.resx
Normal file
117
NGToolsPC/Properties/Resources.resx
Normal file
@ -0,0 +1,117 @@
|
||||
<?xml version="1.0" encoding="utf-8"?>
|
||||
<root>
|
||||
<!--
|
||||
Microsoft ResX Schema
|
||||
|
||||
Version 2.0
|
||||
|
||||
The primary goals of this format is to allow a simple XML format
|
||||
that is mostly human readable. The generation and parsing of the
|
||||
various data types are done through the TypeConverter classes
|
||||
associated with the data types.
|
||||
|
||||
Example:
|
||||
|
||||
... ado.net/XML headers & schema ...
|
||||
<resheader name="resmimetype">text/microsoft-resx</resheader>
|
||||
<resheader name="version">2.0</resheader>
|
||||
<resheader name="reader">System.Resources.ResXResourceReader, System.Windows.Forms, ...</resheader>
|
||||
<resheader name="writer">System.Resources.ResXResourceWriter, System.Windows.Forms, ...</resheader>
|
||||
<data name="Name1"><value>this is my long string</value><comment>this is a comment</comment></data>
|
||||
<data name="Color1" type="System.Drawing.Color, System.Drawing">Blue</data>
|
||||
<data name="Bitmap1" mimetype="application/x-microsoft.net.object.binary.base64">
|
||||
<value>[base64 mime encoded serialized .NET Framework object]</value>
|
||||
</data>
|
||||
<data name="Icon1" type="System.Drawing.Icon, System.Drawing" mimetype="application/x-microsoft.net.object.bytearray.base64">
|
||||
<value>[base64 mime encoded string representing a byte array form of the .NET Framework object]</value>
|
||||
<comment>This is a comment</comment>
|
||||
</data>
|
||||
|
||||
There are any number of "resheader" rows that contain simple
|
||||
name/value pairs.
|
||||
|
||||
Each data row contains a name, and value. The row also contains a
|
||||
type or mimetype. Type corresponds to a .NET class that support
|
||||
text/value conversion through the TypeConverter architecture.
|
||||
Classes that don't support this are serialized and stored with the
|
||||
mimetype set.
|
||||
|
||||
The mimetype is used for serialized objects, and tells the
|
||||
ResXResourceReader how to depersist the object. This is currently not
|
||||
extensible. For a given mimetype the value must be set accordingly:
|
||||
|
||||
Note - application/x-microsoft.net.object.binary.base64 is the format
|
||||
that the ResXResourceWriter will generate, however the reader can
|
||||
read any of the formats listed below.
|
||||
|
||||
mimetype: application/x-microsoft.net.object.binary.base64
|
||||
value : The object must be serialized with
|
||||
: System.Serialization.Formatters.Binary.BinaryFormatter
|
||||
: and then encoded with base64 encoding.
|
||||
|
||||
mimetype: application/x-microsoft.net.object.soap.base64
|
||||
value : The object must be serialized with
|
||||
: System.Runtime.Serialization.Formatters.Soap.SoapFormatter
|
||||
: and then encoded with base64 encoding.
|
||||
|
||||
mimetype: application/x-microsoft.net.object.bytearray.base64
|
||||
value : The object must be serialized into a byte array
|
||||
: using a System.ComponentModel.TypeConverter
|
||||
: and then encoded with base64 encoding.
|
||||
-->
|
||||
<xsd:schema id="root" xmlns="" xmlns:xsd="http://www.w3.org/2001/XMLSchema" xmlns:msdata="urn:schemas-microsoft-com:xml-msdata">
|
||||
<xsd:element name="root" msdata:IsDataSet="true">
|
||||
<xsd:complexType>
|
||||
<xsd:choice maxOccurs="unbounded">
|
||||
<xsd:element name="metadata">
|
||||
<xsd:complexType>
|
||||
<xsd:sequence>
|
||||
<xsd:element name="value" type="xsd:string" minOccurs="0" />
|
||||
</xsd:sequence>
|
||||
<xsd:attribute name="name" type="xsd:string" />
|
||||
<xsd:attribute name="type" type="xsd:string" />
|
||||
<xsd:attribute name="mimetype" type="xsd:string" />
|
||||
</xsd:complexType>
|
||||
</xsd:element>
|
||||
<xsd:element name="assembly">
|
||||
<xsd:complexType>
|
||||
<xsd:attribute name="alias" type="xsd:string" />
|
||||
<xsd:attribute name="name" type="xsd:string" />
|
||||
</xsd:complexType>
|
||||
</xsd:element>
|
||||
<xsd:element name="data">
|
||||
<xsd:complexType>
|
||||
<xsd:sequence>
|
||||
<xsd:element name="value" type="xsd:string" minOccurs="0" msdata:Ordinal="1" />
|
||||
<xsd:element name="comment" type="xsd:string" minOccurs="0" msdata:Ordinal="2" />
|
||||
</xsd:sequence>
|
||||
<xsd:attribute name="name" type="xsd:string" msdata:Ordinal="1" />
|
||||
<xsd:attribute name="type" type="xsd:string" msdata:Ordinal="3" />
|
||||
<xsd:attribute name="mimetype" type="xsd:string" msdata:Ordinal="4" />
|
||||
</xsd:complexType>
|
||||
</xsd:element>
|
||||
<xsd:element name="resheader">
|
||||
<xsd:complexType>
|
||||
<xsd:sequence>
|
||||
<xsd:element name="value" type="xsd:string" minOccurs="0" msdata:Ordinal="1" />
|
||||
</xsd:sequence>
|
||||
<xsd:attribute name="name" type="xsd:string" use="required" />
|
||||
</xsd:complexType>
|
||||
</xsd:element>
|
||||
</xsd:choice>
|
||||
</xsd:complexType>
|
||||
</xsd:element>
|
||||
</xsd:schema>
|
||||
<resheader name="resmimetype">
|
||||
<value>text/microsoft-resx</value>
|
||||
</resheader>
|
||||
<resheader name="version">
|
||||
<value>2.0</value>
|
||||
</resheader>
|
||||
<resheader name="reader">
|
||||
<value>System.Resources.ResXResourceReader, System.Windows.Forms, Version=2.0.0.0, Culture=neutral, PublicKeyToken=b77a5c561934e089</value>
|
||||
</resheader>
|
||||
<resheader name="writer">
|
||||
<value>System.Resources.ResXResourceWriter, System.Windows.Forms, Version=2.0.0.0, Culture=neutral, PublicKeyToken=b77a5c561934e089</value>
|
||||
</resheader>
|
||||
</root>
|
||||
36
NGToolsPC/Properties/Settings.Designer.cs
generated
Normal file
36
NGToolsPC/Properties/Settings.Designer.cs
generated
Normal file
@ -0,0 +1,36 @@
|
||||
//------------------------------------------------------------------------------
|
||||
// <auto-generated>
|
||||
// 此代码由工具生成。
|
||||
// 运行时版本:4.0.30319.42000
|
||||
//
|
||||
// 对此文件的更改可能会导致不正确的行为，并且如果
|
||||
// 重新生成代码，这些更改将会丢失。
|
||||
// </auto-generated>
|
||||
//------------------------------------------------------------------------------
|
||||
|
||||
namespace NGToolsPC.Properties {
|
||||
|
||||
|
||||
[global::System.Runtime.CompilerServices.CompilerGeneratedAttribute()]
|
||||
[global::System.CodeDom.Compiler.GeneratedCodeAttribute("Microsoft.VisualStudio.Editors.SettingsDesigner.SettingsSingleFileGenerator", "16.5.0.0")]
|
||||
internal sealed partial class Settings : global::System.Configuration.ApplicationSettingsBase {
|
||||
|
||||
private static Settings defaultInstance = ((Settings)(global::System.Configuration.ApplicationSettingsBase.Synchronized(new Settings())));
|
||||
|
||||
public static Settings Default {
|
||||
get {
|
||||
return defaultInstance;
|
||||
}
|
||||
}
|
||||
|
||||
[global::System.Configuration.ApplicationScopedSettingAttribute()]
|
||||
[global::System.Diagnostics.DebuggerNonUserCodeAttribute()]
|
||||
[global::System.Configuration.SpecialSettingAttribute(global::System.Configuration.SpecialSetting.ConnectionString)]
|
||||
[global::System.Configuration.DefaultSettingValueAttribute("Provider=Microsoft.Jet.OLEDB.4.0;Data Source=|DataDirectory|\\NGDATA.mdb")]
|
||||
public string NGDATAConnectionString {
|
||||
get {
|
||||
return ((string)(this["NGDATAConnectionString"]));
|
||||
}
|
||||
}
|
||||
}
|
||||
}
|
||||
14
NGToolsPC/Properties/Settings.settings
Normal file
14
NGToolsPC/Properties/Settings.settings
Normal file
@ -0,0 +1,14 @@
|
||||
<?xml version='1.0' encoding='utf-8'?>
|
||||
<SettingsFile xmlns="http://schemas.microsoft.com/VisualStudio/2004/01/settings" CurrentProfile="(Default)" GeneratedClassNamespace="NGToolsPC.Properties" GeneratedClassName="Settings">
|
||||
<Profiles />
|
||||
<Settings>
|
||||
<Setting Name="NGDATAConnectionString" Type="(Connection string)" Scope="Application">
|
||||
<DesignTimeValue Profile="(Default)"><?xml version="1.0" encoding="utf-16"?>
|
||||
<SerializableConnectionString xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:xsd="http://www.w3.org/2001/XMLSchema">
|
||||
<ConnectionString>Provider=Microsoft.Jet.OLEDB.4.0;Data Source=|DataDirectory|\NGDATA.mdb</ConnectionString>
|
||||
<ProviderName>System.Data.OleDb</ProviderName>
|
||||
</SerializableConnectionString></DesignTimeValue>
|
||||
<Value Profile="(Default)">Provider=Microsoft.Jet.OLEDB.4.0;Data Source=|DataDirectory|\NGDATA.mdb</Value>
|
||||
</Setting>
|
||||
</Settings>
|
||||
</SettingsFile>
|
||||
534
NGToolsPC/Therm.cs
Normal file
534
NGToolsPC/Therm.cs
Normal file
@ -0,0 +1,534 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
|
||||
using System.Text;
|
||||
namespace NG_Tools
|
||||
{
|
||||
public class Therm
|
||||
{
|
||||
// member data
|
||||
//double dT;// current temperature, in Kelvins
|
||||
//double dP;// current pressure, in Pascals
|
||||
//double dD;// molar density, in moles/dm3
|
||||
//double dRho;// mass density, in kg/m3
|
||||
double dPdD;// partial deriv of P wrt D
|
||||
double dPdT;// partial deriv of P wrt T
|
||||
double dSi;// ideal gas specific entropy, kJ/kg.K
|
||||
double dTold;// temperature previously used
|
||||
double dMrxold;// mixture molar mass previously used
|
||||
double[] GK_root = new double[5] { 0.14887433898163121088, 0.43339539412924719080, 0.67940956829902440263, 0.86506336668898451073, 0.97390652851717172008 };
|
||||
double[] GK_weight = new double[5] { 0.29552422471475286217, 0.26926671930999634918, 0.21908636251598204295, 0.14945134915058059038, 0.066671344308688137179 };
|
||||
//set the number of points for quadrature
|
||||
int GK_points = 5;
|
||||
//equation constants for ideal gas heat capacity, enthalpy and entropy
|
||||
double[,] ThermConstants = new double[21, 11] {{-29776.4, 7.95454, 43.9417, 1037.09, 1.56373, 813.205, -24.9027, 1019.98,-10.1601, 1070.14,-20.0615},
|
||||
{-3495.34, 6.95587, 0.272892, 662.738,-0.291318,-680.562, 1.78980, 1740.06, 0.0, 100.0, 4.49823},
|
||||
{ 20.7307, 6.96237, 2.68645, 500.371,-2.56429,-530.443, 3.91921, 500.198, 2.13290, 2197.22, 5.81381},
|
||||
{-37524.4, 7.98139, 24.3668, 752.320, 3.53990, 272.846, 8.44724, 1020.13,-13.2732, 869.510,-22.4010},
|
||||
{-56072.1, 8.14319,37.0629,735.402,9.38159,247.190,13.4556, 1454.78,-11.7342, 984.518,-24.0426},
|
||||
{-13773.1, 7.97183, 6.27078,2572.63,2.05010,1156.72,0.0,100.0,0.0,100.0,-3.24989},
|
||||
{-10085.4, 7.94680,-0.08380,433.801,2.85539, 843.792,6.31595, 1481.43,-2.88457, 1102.23,-0.51551},
|
||||
{-5565.60, 6.66789, 2.33458,2584.98,.749019, 559.656,0.0,100.0,0.0,100.0,-7.94821},
|
||||
{-2753.49, 6.95854, 2.02441,1541.22,.096774, 3674.81,0.0,100.0,0.0,100.0,6.23387},
|
||||
{-3497.45, 6.96302, 2.40013, 2522.05, 2.21752, 1154.15, 0.0,100.0,0.0,100.0,9.19749},
|
||||
{-72387.0, 17.8143, 58.2062, 1787.39, 40.7621, 808.645, 0.0,100.0,0.0,100.0,-44.1341},
|
||||
{-72674.8, 18.6383, 57.4178, 1792.73, 38.6599, 814.151, 0.0,100.0,0.0,100.0,-46.1938},
|
||||
{-91505.5, 21.3861, 74.3410, 1701.58, 47.0587, 775.899, 0.0,100.0,0.0,100.0,-60.2474},
|
||||
{-83845.2, 22.5012, 69.5789, 1719.58, 46.2164, 802.174, 0.0,100.0,0.0,100.0,-62.2197},
|
||||
{-94982.5, 26.6225, 80.3819, 1718.49, 55.6598, 802.069, 0.0,100.0,0.0,100.0,-77.5366},
|
||||
{-103353.0, 30.4029, 90.6941, 1669.32, 63.2028, 786.001, 0.0,100.0,0.0,100.0,-92.0164},
|
||||
{-109674.0, 34.0847, 100.253, 1611.55, 69.7675, 768.847, 0.0,100.0,0.0,100.0,-106.149},
|
||||
{-122599.0, 38.5014, 111.446, 1646.48, 80.5015, 781.588, 0.0,100.0,0.0,100.0,-122.444},
|
||||
{-133564.0, 42.7143, 122.173, 1654.85, 90.2255, 785.564, 0.0,100.0,0.0,100.0,-138.006},
|
||||
{0.0,4.9680,0.0,100.0,0.0,100.0,0.0,100.0,0.0,100.0,0.0},
|
||||
{0.0,4.9680,0.0,100.0,0.0,100.0,0.0,100.0,0.0,100.0,0.0}};
|
||||
// enumerations for indexing of coefficients
|
||||
//public enum CoefficientList { coefA = 0, coefB, coefC, coefD, coefE, coefF, coefG, coefH, coefI, coefJ, coefK } ;
|
||||
public int coefA = 0;
|
||||
public int coefB = 1;
|
||||
public int coefC = 2;
|
||||
public int coefD = 3;
|
||||
public int coefE = 4;
|
||||
public int coefF = 5;
|
||||
public int coefG = 6;
|
||||
public int coefH = 7;
|
||||
public int coefI = 8;
|
||||
public int coefJ = 9;
|
||||
public int coefK = 10;
|
||||
// conversion constant for thermochemical calories to Joules: 1 cal(IT) = 4.1840 J
|
||||
const double CalTH = 4.1840;
|
||||
public Therm()
|
||||
{
|
||||
// initialize 3 history-sensitive variables
|
||||
dSi = 0.0;
|
||||
dTold = 0.0;
|
||||
dMrxold = 0.0;
|
||||
}//Therm()
|
||||
/**************************************************************************
|
||||
*Function:Math.Coth()
|
||||
*Arguments:double
|
||||
*Returns:double
|
||||
*Purpose:calculate hyperbolic cotangent; used in Ho calculations
|
||||
*Revisions:
|
||||
*Notes:Not a Therm object class member, just a utility for this
|
||||
*file. The C++ language has no intrinsic support for
|
||||
*hyperbolic cotangent
|
||||
**************************************************************************/
|
||||
double coth(double x)
|
||||
{
|
||||
return Math.Cosh(x) / Math.Sinh(x);
|
||||
}// Math.Coth()
|
||||
/**************************************************************************
|
||||
*Function:Run()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:void
|
||||
*Purpose:overall execution control; top level math for SOS and k
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
public void Run(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
//local variables
|
||||
double c, x, y, z;
|
||||
//first run basic set of functions within AGA 8 (1994) Detail Method
|
||||
ptD.Run(ref ptAGA10);
|
||||
//find first partial derivative of Z wrt D
|
||||
ptD.dZdD(ptAGA10.dDf);
|
||||
//find real gas cv, cp, specific enthalpy and entropy
|
||||
CprCvrHS(ref ptAGA10, ref ptD);
|
||||
//ratio of real gas specific heats
|
||||
ptAGA10.dk = ptAGA10.dCp / ptAGA10.dCv;
|
||||
//solve c in three steps, for clarity and ease of debugging
|
||||
x = ptAGA10.dk * NG_Cal.RGAS * 1000.0 * ptAGA10.dTf;
|
||||
y = ptAGA10.dMrx;
|
||||
z = ptAGA10.dZf + ptAGA10.dDf * ptD.ddZdD;
|
||||
//calculate c, which is SOS^2
|
||||
c = (x / y) * z;
|
||||
//speed of sound
|
||||
ptAGA10.dSOS = Math.Sqrt(c);
|
||||
//calculate the real gas isentropic exponent
|
||||
//using expression functionally equivalent to Equation 3.2
|
||||
ptAGA10.dKappa = (c * ptAGA10.dRhof) / ptAGA10.dPf;
|
||||
return;
|
||||
}//Run()
|
||||
/**************************************************************************
|
||||
*Function:CpiMolar()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT
|
||||
*Returns:double
|
||||
*Purpose:Calculate constant pressure ideal gas molar heat capacity
|
||||
*in (J/mol-K), applying eqns from Aly, Lee, McFall
|
||||
*Notes:For continuity, the original constants and eqn's have been
|
||||
*retained. Conversion from thermochemical calories(th) to
|
||||
*Joules is applied after the primary calculations are complete.
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double CpiMolar(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
double Cp = 0.0;
|
||||
double Cpx;
|
||||
double DT, FT, HT, JT;
|
||||
double Dx, Fx, Hx, Jx;
|
||||
double T;
|
||||
int i;
|
||||
//to maximize readability of this section, use intermediate variable T
|
||||
T = ptAGA10.dTf;
|
||||
//calculate heat capacity for each component
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
//skip species whose concentration is zero
|
||||
if (ptAGA10.adMixture[i] <= 0.0) continue;
|
||||
//initialize Cp of species to zero
|
||||
Cpx = 0.0;
|
||||
// calculate species intermediate terms
|
||||
DT = ThermConstants[i, coefD] / T;
|
||||
FT = ThermConstants[i, coefF] / T;
|
||||
HT = ThermConstants[i, coefH] / T;
|
||||
JT = ThermConstants[i, coefJ] / T;
|
||||
// use intermediate terms to avoid redundant calcs
|
||||
Dx = DT / Math.Sinh(DT);
|
||||
Fx = FT / Math.Cosh(FT);
|
||||
Hx = HT / Math.Sinh(HT);
|
||||
Jx = JT / Math.Cosh(JT);
|
||||
Cpx += ThermConstants[i, coefB];
|
||||
Cpx += ThermConstants[i, coefC] * Dx * Dx;
|
||||
Cpx += ThermConstants[i, coefE] * Fx * Fx;
|
||||
Cpx += ThermConstants[i, coefG] * Hx * Hx;
|
||||
Cpx += ThermConstants[i, coefI] * Jx * Jx;
|
||||
//use current mole fraction to weight the contribution
|
||||
Cpx *= ptAGA10.adMixture[i];
|
||||
//add this contribution to the sum
|
||||
Cp += Cpx;
|
||||
}
|
||||
// convert from cal(th)/mol-K to J/mol-K
|
||||
Cp *= CalTH;
|
||||
return Cp;
|
||||
}//CpiMolar()
|
||||
/**************************************************************************
|
||||
*Function:Ho()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT
|
||||
*Returns:double
|
||||
*Purpose:Calculate ideal gas specific enthalpy (J/kg)
|
||||
*Notes:For continuity, the original constants and eqn's have been
|
||||
*retained. Conversion from thermochemical calories(th) to
|
||||
*Joules is applied after the primary calculations are complete.
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double Ho(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
double H = 0.0; double Hx;
|
||||
double DT, FT, HT, JT;
|
||||
double cothDT, tanhFT, cothHT, tanhJT; double T;
|
||||
int i;
|
||||
// to maximize readability of this section, use intermediate variable T
|
||||
T = ptAGA10.dTf;
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
// skip species whose concentration is zero
|
||||
if (ptAGA10.adMixture[i] <= 0.0) continue;
|
||||
Hx = 0.0;
|
||||
// calculate species intermediate terms
|
||||
DT = ThermConstants[i, coefD] / T;
|
||||
FT = ThermConstants[i, coefF] / T; HT = ThermConstants[i, coefH] / T; JT = ThermConstants[i, coefJ] / T;
|
||||
cothDT = coth(DT); tanhFT = Math.Tanh(FT); cothHT = coth(HT); tanhJT = Math.Tanh(JT);
|
||||
Hx += ThermConstants[i, coefA];
|
||||
Hx += ThermConstants[i, coefB] * T;
|
||||
Hx += ThermConstants[i, coefC] * ThermConstants[i, coefD] * cothDT;
|
||||
Hx -= ThermConstants[i, coefE] * ThermConstants[i, coefF] * tanhFT;
|
||||
Hx += ThermConstants[i, coefG] * ThermConstants[i, coefH] * cothHT;
|
||||
Hx -= ThermConstants[i, coefI] * ThermConstants[i, coefJ] * tanhJT;
|
||||
//use current mole fraction to weight the contribution
|
||||
Hx *= ptAGA10.adMixture[i];
|
||||
//add this contribution to the sum
|
||||
H += Hx;
|
||||
}
|
||||
//convert from cal(th)/g-mol to kJ/kg-mol
|
||||
H *= CalTH;
|
||||
//convert from kJ/kg-mol to J/kg
|
||||
H /= ptAGA10.dMrx;
|
||||
// return in J/kg
|
||||
return H * 1.0e3;
|
||||
}
|
||||
// Ho()
|
||||
/**************************************************************************
|
||||
*Function:So()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT
|
||||
*Returns:double
|
||||
*Purpose:ideal gas specific entropy (J/kg-K)
|
||||
*Notes:For continuity, the original constants and eqn's have been
|
||||
*retained. Conversion from thermochemical calories(th) to
|
||||
*Joules is applied after the primary calculations are complete.
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double So(ref NG_Cal.GasPropsSTRUCT ptAGA10)
|
||||
{
|
||||
double S = 0.0; double Sx;
|
||||
double DT, FT, HT, JT;
|
||||
double cothDT, tanhFT, cothHT, tanhJT; double sinhDT, coshFT, sinhHT, coshJT; double T;
|
||||
int i;
|
||||
// to improve readability of this section, use intermediate variable T
|
||||
T = ptAGA10.dTf;
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
// skip species whose concentration is zero
|
||||
if (ptAGA10.adMixture[i] <= 0.0) continue;
|
||||
Sx = 0.0;
|
||||
// calculate species intermediate terms
|
||||
DT = ThermConstants[i, coefD] / T;
|
||||
FT = ThermConstants[i, coefF] / T;
|
||||
HT = ThermConstants[i, coefH] / T;
|
||||
JT = ThermConstants[i, coefJ] / T;
|
||||
cothDT = coth(DT); tanhFT = Math.Tanh(FT); cothHT = coth(HT);
|
||||
tanhJT = Math.Tanh(JT);
|
||||
sinhDT = Math.Sinh(DT); coshFT = Math.Cosh(FT); sinhHT = Math.Sinh(HT); coshJT = Math.Cosh(JT);
|
||||
Sx += ThermConstants[i, coefK];
|
||||
Sx += ThermConstants[i, coefB] * Math.Log(T);
|
||||
Sx += ThermConstants[i, coefC] * (DT * cothDT - Math.Log(sinhDT));
|
||||
Sx -= ThermConstants[i, coefE] * (FT * tanhFT - Math.Log(coshFT));
|
||||
Sx += ThermConstants[i, coefG] * (HT * cothHT - Math.Log(sinhHT));
|
||||
Sx -= ThermConstants[i, coefI] * (JT * tanhJT - Math.Log(coshJT));
|
||||
//use current mole fraction to weight the contribution
|
||||
Sx *= ptAGA10.adMixture[i];
|
||||
//add this contribution to the sum
|
||||
S += Sx;
|
||||
}
|
||||
//convert cal(th)/mol-K basis to to kJ/kg mol-K
|
||||
S *= CalTH;
|
||||
//convert from kJ/kg mol-K to kJ/kg-K
|
||||
S /= ptAGA10.dMrx;
|
||||
// return in J/kg-K
|
||||
return S * 1.0e3;
|
||||
}//So()
|
||||
/**************************************************************************
|
||||
*Function:CprCvrHS()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:void
|
||||
*Purpose:reasonably efficient group calculation of Cp, Cv, H and S
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
void CprCvrHS(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
double Cvinc, Cvr, Cpr;
|
||||
double Hinc;
|
||||
double Sinc;
|
||||
double Smixing;
|
||||
double Cp, Si;
|
||||
double a, b, x;
|
||||
int i;
|
||||
//initialize integrals to zero
|
||||
Cvinc = 0.0;
|
||||
Hinc = 0.0;
|
||||
Sinc = 0.0;
|
||||
//initialize entropy of mixing
|
||||
Smixing = 0.0;
|
||||
//find ideal gas Cp
|
||||
Cp = CpiMolar(ref ptAGA10);
|
||||
//find ideal gas enthalpy
|
||||
ptAGA10.dHo = Ho(ref ptAGA10);
|
||||
//find ideal gas entropy
|
||||
Si = So(ref ptAGA10);
|
||||
//calculate ideal gas specific heat capacity at constant pressure in J/kgK
|
||||
ptAGA10.dCpi = (Cp * 1000.0) / ptAGA10.dMrx;
|
||||
//integrate partial derivatives from D=0 to D=D, applying Gauss-Kronrod quadrature
|
||||
for (i = 0; i < GK_points; i++)
|
||||
{
|
||||
// set calculation point at + abscissa
|
||||
x = ptAGA10.dDf * (1.0 + GK_root[i]) / 2.0;
|
||||
//get Z at D
|
||||
ptD.zdetail(x);
|
||||
ptD.dZdT(x);
|
||||
ptD.d2ZdT2(x);
|
||||
//gather contributions at + abscissa; applying weighting factor
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x;
|
||||
Cvinc += GK_weight[i] * (2.0 * ptD.ddZdT + ptAGA10.dTf * ptD.dd2ZdT2) / x;
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
//set calculation point at - abscissa
|
||||
x = ptAGA10.dDf * (1.0 - GK_root[i]) / 2.0;
|
||||
//get Z at D
|
||||
ptD.zdetail(x);
|
||||
//calculate 1st and 2nd partial derivatives of Z wrt T
|
||||
ptD.dZdT(x);
|
||||
ptD.d2ZdT2(x);
|
||||
//gather contributions at - abscissa; applying weighting factor
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x;
|
||||
Cvinc += GK_weight[i] * (2.0 * ptD.ddZdT + ptAGA10.dTf * ptD.dd2ZdT2) / x;
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
}
|
||||
//return Z and partial derivatives to full molar density
|
||||
ptD.zdetail(ptAGA10.dDf);
|
||||
ptD.dZdT(ptAGA10.dDf);
|
||||
ptD.d2ZdT2(ptAGA10.dDf);
|
||||
//complete Cv molar
|
||||
Cvr = Cp - NG_Cal.RGAS * (1.0 + ptAGA10.dTf * Cvinc * 0.5 * ptAGA10.dDf);
|
||||
//intermediate values for Cp, containing 2 partial derivatives
|
||||
a = (ptAGA10.dZf + ptAGA10.dTf * ptD.ddZdT);
|
||||
b = (ptAGA10.dZf + ptAGA10.dDf * ptD.ddZdD);
|
||||
//calculate dPdT, the partial derivative of P wrt T, at D
|
||||
dPdT = NG_Cal.RGAS * ptAGA10.dDf * a;
|
||||
//calculate dPdD, the partial derivative of P wrt D, at T
|
||||
dPdD = NG_Cal.RGAS * ptAGA10.dTf * b;
|
||||
//equation completing molar Cp, cancelling appropriate terms
|
||||
Cpr = Cvr + NG_Cal.RGAS * ((a * a) / b);
|
||||
//change from molar to mass basis
|
||||
Cpr /= ptAGA10.dMrx;
|
||||
Cvr /= ptAGA10.dMrx;
|
||||
// write to the data stucture
|
||||
ptAGA10.dCv = Cvr * 1000.0; // convert from joules/kgK to kilojoules/kgK
|
||||
ptAGA10.dCp = Cpr * 1000.0;
|
||||
// calculate specific enthalpy
|
||||
ptAGA10.dH = ptAGA10.dHo + 1000.0 * NG_Cal.RGAS * ptAGA10.dTf * (ptAGA10.dZf - 1.0 - ptAGA10.dTf * Hinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
// calculate entropy of mixing
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
if (ptAGA10.adMixture[i] != 0) Smixing += ptAGA10.adMixture[i] * Math.Log(ptAGA10.adMixture[i]);
|
||||
}
|
||||
Smixing *= NG_Cal.RGAS;
|
||||
// calculate specific entropy
|
||||
ptAGA10.dS = Si - Smixing - 1000.0 * NG_Cal.RGAS * (Math.Log(ptAGA10.dPf / 101325.0) - Math.Log(ptAGA10.dZf) + Sinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
return;
|
||||
}//CprCvrHS()
|
||||
/**************************************************************************
|
||||
*Function:HS_Mode()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *, double, double, bool
|
||||
*Returns:void
|
||||
*Purpose:Calculates a pressure & temperature from known enthalpy & entropy,
|
||||
*with or without prior estimates.This function has a role in the
|
||||
*calculation of C*.
|
||||
*Solution based on a doubly-nested trial & error algorithm and Newton's
|
||||
*method.
|
||||
*
|
||||
*For illustrative purpose, two approaches are supported by this example.
|
||||
*If you are starting without advance knowledge of P & T, set the input parm
|
||||
*bGuess to false, thus specifying a conservative search approach.
|
||||
*If, however, you have a basis for guessing P & T (plenum conditions of a
|
||||
*critical flow nozzle, for example) set P & T via GasPropsSTRUCT and set
|
||||
*bGuess = true. The initial guess allows the search function to be more
|
||||
*aggressive and, typically, faster.
|
||||
*
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
public void HS_Mode(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD, double H, double S, bool bGuess)
|
||||
{
|
||||
double s0, s1, s2, t0, t1, t2, tmin, tmax; double h0, h1, h2, p0, p1, p2, px, pmin, pmax; double delta1, delta2;
|
||||
double tolerance = 0.001;// convergence tolerance (used for both H and S searches)
|
||||
int i, j;
|
||||
//s0and h0 are our real gas reference points
|
||||
s0 = S;
|
||||
h0 = H;
|
||||
//calling function specifies whether search parameters are supplied thru ptAGA10 or unknown
|
||||
if (bGuess)
|
||||
{
|
||||
t1 = ptAGA10.dTf; px = ptAGA10.dPf; pmax = px * 2.0; pmin = px * 0.1;
|
||||
tmax = t1 * 1.5; tmin = t1 * 0.67;
|
||||
}
|
||||
else// use arbitrary, generic limits
|
||||
{
|
||||
t1 = 273.15;
|
||||
px = 1013250.0; // 10 atmospheres
|
||||
pmax = NG_Cal.P_MAX;
|
||||
pmin = 10000.0; // 10 kPa
|
||||
tmax = NG_Cal.T_MAX;
|
||||
tmin = NG_Cal.T_MIN;
|
||||
}
|
||||
// set the temperature differential
|
||||
t2 = t1 + 10.0;
|
||||
///////////////////////////////////////////
|
||||
//begin double trial-and-error, searching for T & P
|
||||
//run the calculation with initial guesses
|
||||
ptD.Run(ref ptAGA10);
|
||||
//h1 is difference between h given and h@Tf, Pf
|
||||
h1 = this.H(ref ptAGA10, ref ptD) - h0;
|
||||
//outer loop: search for a t2 which will satisfy constant enthalpy
|
||||
for (i = 0; i < NG_Cal.MAX_NUM_OF_ITERATIONS; i++)
|
||||
{
|
||||
ptAGA10.dTf = t2;
|
||||
p1 = px;// reset one bracket
|
||||
p2 = px * 0.1;// set other bracket to 0.1x the upper bracket
|
||||
ptAGA10.dPf = p1;
|
||||
ptD.Run(ref ptAGA10);
|
||||
s1 = this.S(ref ptAGA10, ref ptD) - s0;
|
||||
//inside loop: search for a p2 which will satisfy constant entropy
|
||||
for (j = 0; j < NG_Cal.MAX_NUM_OF_ITERATIONS; j++)
|
||||
{
|
||||
ptAGA10.dPf = p2; ptD.Run(ref ptAGA10);
|
||||
s2 = this.S(ref ptAGA10, ref ptD) - s0;
|
||||
//calculate our proportional change
|
||||
delta2 = Math.Abs(s1 - s2) / s0; // close enough?
|
||||
if (delta2 < tolerance) break;
|
||||
//revise our estimate to p2
|
||||
p0 = p2;
|
||||
p2 = (p1 * s2 - p2 * s1) / (s2 - s1);
|
||||
//check for negative pressure and clamp to pmin for safety
|
||||
if (p2 <= pmin)
|
||||
{
|
||||
p2 = pmin;
|
||||
}
|
||||
//check if we've created an unrealistic pressure
|
||||
if (p2 >= pmax) p2 = pmax; // swap values
|
||||
p1 = p0;
|
||||
s1 = s2;
|
||||
}
|
||||
// check for failure to converge
|
||||
if (j >= NG_Cal.MAX_NUM_OF_ITERATIONS) ptAGA10.lStatus = NG_Cal.MAX_NUM_OF_ITERATIONS_EXCEEDED;
|
||||
//calc enthalpy at guessed P & current iter T
|
||||
h2 = this.H(ref ptAGA10, ref ptD) - h0;
|
||||
//calculate our proportional change
|
||||
delta1 = Math.Abs(h1 - h2) / h0;
|
||||
// close enough?
|
||||
if (delta1 < tolerance && i > 0) break;
|
||||
//revise our estimate to t2
|
||||
t0 = t2;
|
||||
t2 = (t1 * h2 - t2 * h1) / (h2 - h1);
|
||||
//check if we've created an unrealistic temperature
|
||||
if (t2 >= tmax) t2 = tmax;
|
||||
//revise t2, if necessary
|
||||
if (t2 <= tmin)
|
||||
{
|
||||
t2 = t0 + 10.0;
|
||||
ptAGA10.dTf = t2; ptD.Run(ref ptAGA10);
|
||||
h2 = this.H(ref ptAGA10, ref ptD) - h0;
|
||||
}
|
||||
t1 = t0;
|
||||
h1 = h2;
|
||||
}
|
||||
// check for failure to converge
|
||||
if (i >= NG_Cal.MAX_NUM_OF_ITERATIONS) ptAGA10.lStatus = NG_Cal.MAX_NUM_OF_ITERATIONS_EXCEEDED;
|
||||
}//HS_Mode()
|
||||
/**************************************************************************
|
||||
*Function:H()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:double
|
||||
*Purpose:real gas specific enthalpy
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double H(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
double Hinc; double x; int i;
|
||||
//initialize integral
|
||||
Hinc = 0.0;
|
||||
//find ideal gas enthalpy
|
||||
ptAGA10.dHo = Ho(ref ptAGA10);
|
||||
//integrate partial derivatives from D=0 to D=D, applying Gauss-Kronrod quadrature
|
||||
for (i = 0; i < GK_points; i++)
|
||||
{
|
||||
//calculate 1st and 2nd partial derivatives of Z wrt T
|
||||
x = ptAGA10.dDf * (1.0 + GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x);
|
||||
ptD.d2ZdT2(x);
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x; if (i == 10) break;
|
||||
x = ptAGA10.dDf * (1.0 - GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x); ptD.d2ZdT2(x);
|
||||
Hinc += GK_weight[i] * ptD.ddZdT / x;
|
||||
}
|
||||
ptD.zdetail(ptAGA10.dDf); ptD.dZdT(ptAGA10.dDf); ptD.d2ZdT2(ptAGA10.dDf);
|
||||
// calculate specific enthalpy
|
||||
ptAGA10.dH = ptAGA10.dHo + 1000.0 * NG_Cal.RGAS * ptAGA10.dTf *
|
||||
(ptAGA10.dZf - 1.0 - ptAGA10.dTf * Hinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
return (ptAGA10.dH);
|
||||
} // H()
|
||||
/**************************************************************************
|
||||
*Function:S()
|
||||
*Arguments:ref AGA10.GasPropsSTRUCT , Detail *
|
||||
*Returns:double
|
||||
*Purpose:real gas specific entropy
|
||||
*Revisions:
|
||||
**************************************************************************/
|
||||
double S(ref NG_Cal.GasPropsSTRUCT ptAGA10, ref Detail ptD)
|
||||
{
|
||||
double Sinc; double Smixing; double x;
|
||||
int i;
|
||||
//initialize integral
|
||||
Sinc = 0.0;
|
||||
//initialize entropy of mixing
|
||||
Smixing = 0.0;
|
||||
//integrate partial derivatives from D=0 to D=D, applying Gauss-Kronrod quadrature
|
||||
for (i = 0; i < GK_points; i++)
|
||||
{
|
||||
//calculate 1st and 2nd partial derivatives of Z wrt T
|
||||
x = ptAGA10.dDf * (1.0 + GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x); ptD.d2ZdT2(x);
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
if (i == 10) break;
|
||||
x = ptAGA10.dDf * (1.0 - GK_root[i]) / 2.0; ptD.zdetail(x);
|
||||
ptD.dZdT(x); ptD.d2ZdT2(x);
|
||||
Sinc += GK_weight[i] * (ptD.dZ + ptAGA10.dTf * ptD.ddZdT - 1.0) / x;
|
||||
}
|
||||
//reset Z and partial deivatives dZdT and d2ZdT2
|
||||
ptD.zdetail(ptAGA10.dDf);
|
||||
ptD.dZdT(ptAGA10.dDf);
|
||||
ptD.d2ZdT2(ptAGA10.dDf);
|
||||
//find ideal gas entropy, but only if temperature or composition have changed
|
||||
if (ptAGA10.dTf != dTold || ptAGA10.dMrx != dMrxold)
|
||||
{
|
||||
dSi = So(ref ptAGA10); dTold = ptAGA10.dTf; dMrxold = ptAGA10.dMrx;
|
||||
}
|
||||
//calculate entropy of mixing
|
||||
for (i = 0; i < NG_Cal.NUMBEROFCOMPONENTS; i++)
|
||||
{
|
||||
if (ptAGA10.adMixture[i] != 0) Smixing += ptAGA10.adMixture[i] * Math.Log(ptAGA10.adMixture[i]);
|
||||
}
|
||||
Smixing *= NG_Cal.RGAS;
|
||||
// calculate specific entropy
|
||||
ptAGA10.dS = dSi - Smixing - 1000.0 * NG_Cal.RGAS * (Math.Log(ptAGA10.dPf / 101325.0) - Math.Log(ptAGA10.dZf) + Sinc * 0.5 * ptAGA10.dDf) / ptAGA10.dMrx;
|
||||
return (ptAGA10.dS);
|
||||
} // S()
|
||||
}
|
||||
}
|
||||
407
NGToolsPC/UnitConvert.cs
Normal file
407
NGToolsPC/UnitConvert.cs
Normal file
@ -0,0 +1,407 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
|
||||
using System.Text;
|
||||
|
||||
namespace NG_Tools
|
||||
{
|
||||
public class UnitConvert
|
||||
{
|
||||
public double Converter(string UnitName, double oldValue, int oldunit, int newunit, int Xsdws)
|
||||
{
|
||||
double returnValue = 0;
|
||||
//On Error Resume Next VBConversions Warning: On Error Resume Next not supported in C#
|
||||
//Dim strUnit() As String
|
||||
double[] dataUnit = new double[] { 0 };
|
||||
|
||||
//ReDim strUnit(UnitNum)
|
||||
//RereDim dataUnit(UnitNum)
|
||||
switch (UnitName)
|
||||
{
|
||||
case "tj":
|
||||
|
||||
dataUnit = new double[8];
|
||||
|
||||
|
||||
//strUnit(0) = "立方米(m3)"
|
||||
//strUnit(1) = "升(L, dm3)"
|
||||
//strUnit(2) = "立方厘米(cm3, ml, c.c)"
|
||||
//strUnit(3) = "立方英尺(ft3)"
|
||||
//strUnit(4) = "立方英寸(in3)"
|
||||
//strUnit(5) = "英加仑(UKgal)"
|
||||
//strUnit(6) = "美加仑(U.Sgal)"
|
||||
//strUnit(7) = "美油桶(USbbl)"
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 1000;
|
||||
dataUnit[2] = 1000000;
|
||||
dataUnit[3] = 35.3147;
|
||||
dataUnit[4] = 61023.7;
|
||||
dataUnit[5] = 219.969;
|
||||
dataUnit[6] = 264.172;
|
||||
dataUnit[7] = 6.28994;
|
||||
break;
|
||||
|
||||
case "zl":
|
||||
|
||||
//strUnit(0) = "千克(公斤)(kg)"
|
||||
//strUnit(1) = "克(g)"
|
||||
//strUnit(2) = "毫克(mg)"
|
||||
//strUnit(3) = "吨(t)"
|
||||
//strUnit(4) = "英吨(长吨)(UKton)"
|
||||
//strUnit(5) = "美吨(短吨)(U.Ston)"
|
||||
//strUnit(6) = "磅(lb)"
|
||||
//strUnit(7) = "盎司(oz)"
|
||||
dataUnit = new double[8]; //As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 1000;
|
||||
dataUnit[2] = 1000000;
|
||||
dataUnit[3] = 0.001;
|
||||
dataUnit[4] = 0.000984207;
|
||||
dataUnit[5] = 0.00110231;
|
||||
dataUnit[6] = 2.20462;
|
||||
dataUnit[7] = 35.274;
|
||||
break;
|
||||
case "rl":
|
||||
//strUnit(0) = "焦耳(J)"
|
||||
//strUnit(1) = "马力小时(Hp·h)"
|
||||
//strUnit(2) = "公斤力·米(kgf·m)"
|
||||
//strUnit(3) = "升·大气压(L·atm)"
|
||||
//strUnit(4) = "尔格(erg)"
|
||||
//strUnit(5) = "千卡(kacl)"
|
||||
//strUnit(6) = "千瓦小时(kW·h)"
|
||||
//strUnit(7) = "英马力小时(UKHp·h)"
|
||||
//strUnit(8) = "英尺·磅力(ft·lbf)"
|
||||
//strUnit(9) = "英热单位(BTU)"
|
||||
dataUnit = new double[10]; // As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 0.000000377672;
|
||||
dataUnit[2] = 0.101972;
|
||||
dataUnit[3] = 0.00986923;
|
||||
dataUnit[4] = 107;
|
||||
dataUnit[5] = 0.000238846;
|
||||
dataUnit[6] = 0.000000277778;
|
||||
dataUnit[7] = 0.000000372506;
|
||||
dataUnit[8] = 0.737562;
|
||||
dataUnit[9] = 0.000947813;
|
||||
break;
|
||||
|
||||
|
||||
case "nlll":
|
||||
//strUnit(0) = "兆焦/秒(MJ/s)"
|
||||
//strUnit(1) = "兆焦/小时(MJ/h)"
|
||||
//strUnit(2) = "兆焦/天(MJ/d)"
|
||||
//strUnit(3) = "千卡/秒(kcal/s)"
|
||||
//strUnit(4) = "千卡/小时(kcal/h)"
|
||||
//strUnit(5) = "英热单位/秒(BTU/s)"
|
||||
//strUnit(6) = "英热单位/小时(BTU/h)"
|
||||
|
||||
dataUnit = new double[7]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 3600;
|
||||
dataUnit[2] = 86400;
|
||||
dataUnit[3] = 238.846;
|
||||
dataUnit[4] = 859845.6;
|
||||
dataUnit[5] = 947.813;
|
||||
dataUnit[6] = 3412126.8;
|
||||
break;
|
||||
|
||||
case "zlll":
|
||||
|
||||
//strUnit(0) = "千克(公斤)/秒(kg/s)"
|
||||
//strUnit(1) = "千克(公斤)/分(kg/Min)"
|
||||
//strUnit(2) = "千克(公斤)/时(kg/h)"
|
||||
//strUnit(3) = "磅/秒(lb/s)"
|
||||
//strUnit(4) = "磅/分(lb/Min)"
|
||||
//strUnit(5) = "磅/时(lb/h)"
|
||||
//strUnit(6) = "吨/时(t/h)"
|
||||
//strUnit(7) = "英吨(长吨)/时(UKton/h)"
|
||||
//strUnit(8) = "美吨(短吨)/小时(U.Ston/h)"
|
||||
|
||||
dataUnit = new double[9]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 60;
|
||||
dataUnit[2] = 3600;
|
||||
dataUnit[3] = 2.20462;
|
||||
dataUnit[4] = 132.2772;
|
||||
dataUnit[5] = 7936.632;
|
||||
dataUnit[6] = 3.6;
|
||||
dataUnit[7] = 3.543145;
|
||||
dataUnit[8] = 3.968316;
|
||||
break;
|
||||
case "tjll":
|
||||
//strUnit(0) = "立方米/秒(m3/s)"
|
||||
//strUnit(1) = "万立方米/天(m3/d)"
|
||||
//strUnit(1) = "立方米/时(m3/h)"
|
||||
//strUnit(2) = "立方米/分(m3/Min)"
|
||||
//strUnit(3) = "升/时(L/h)"
|
||||
//strUnit(4) = "升/分(L/Min)"
|
||||
//strUnit(5) = "升/秒(L/s)"
|
||||
//strUnit(6) = "立方英尺/时(ft3/h)"
|
||||
//strUnit(7) = "立方英尺/分(ft3/Min)"
|
||||
//strUnit(8) = "立方英尺/秒(ft3/s)"
|
||||
//strUnit(9) = "立方英尺/秒(ft3/s)"
|
||||
//strUnit(10) = "立方英尺/天(ft3/d)"
|
||||
|
||||
//strUnit(11) = "英加仑/秒(UKgal/s)"
|
||||
//strUnit(12) = "美加仑/秒(U.Sgal/s)"
|
||||
//strUnit(13) = "美油桶/秒(USbbl/s)"
|
||||
|
||||
|
||||
dataUnit = new double[13]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 8.64;
|
||||
dataUnit[2] = 3600;
|
||||
dataUnit[3] = 60;
|
||||
dataUnit[4] = 3600000;
|
||||
dataUnit[5] = 60000;
|
||||
dataUnit[6] = 1000;
|
||||
dataUnit[7] = 127132.92;
|
||||
dataUnit[8] = 2118.882;
|
||||
dataUnit[9] = 0.0245240972222222;
|
||||
dataUnit[10] = 35.3147;
|
||||
dataUnit[11] = 219.969;
|
||||
dataUnit[12] = 264.172;
|
||||
|
||||
break;
|
||||
|
||||
|
||||
case "yl":
|
||||
//strUnit(0) = "帕(Pa)"
|
||||
//strUnit(1) = "千帕(kPa)"
|
||||
//strUnit(2) = "兆帕(Mpa)"
|
||||
//strUnit(3) = "标准大气压(atm)"
|
||||
//strUnit(4) = "毫巴(mbar)"
|
||||
//strUnit(5) = "巴(bar)"
|
||||
//strUnit(6) = "千克力/平方米(kgf/m2)"
|
||||
//strUnit(7) = "千克力/平方厘米(kgf/cm2)"
|
||||
//strUnit(8) = "毫米汞柱(mmHg)"
|
||||
//strUnit(9) = "毫米水柱4℃(mmH2O)"
|
||||
//strUnit(10) = "磅/平方英寸(psi)"
|
||||
|
||||
dataUnit = new double[11]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 0.001;
|
||||
dataUnit[2] = 0.000001;
|
||||
dataUnit[3] = 0.00000986923266716013;
|
||||
dataUnit[4] = 0.01;
|
||||
dataUnit[5] = 0.00001;
|
||||
dataUnit[6] = 0.101971621;
|
||||
dataUnit[7] = 0.0000101972;
|
||||
dataUnit[8] = 0.007500638;
|
||||
dataUnit[9] = 0.101972;
|
||||
dataUnit[10] = 0.000145038;
|
||||
break;
|
||||
|
||||
case "wd":
|
||||
switch (newunit)
|
||||
{
|
||||
case 0:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
case 1: //K->℃
|
||||
returnValue = oldValue - 273.15;
|
||||
break;
|
||||
case 2: //F->℃
|
||||
returnValue = (oldValue - 32) / 1.8;
|
||||
break;
|
||||
case 3: //R->℃
|
||||
returnValue = oldValue / 1.8 - 273.15;
|
||||
break;
|
||||
}
|
||||
break;
|
||||
case 1:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0: //℃->K
|
||||
returnValue = oldValue + 273.15;
|
||||
break;
|
||||
case 1:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
case 2: //F->K
|
||||
returnValue = (oldValue - 32) / 1.8 + 273.15;
|
||||
break;
|
||||
case 3: //R->K
|
||||
returnValue = oldValue / 1.8;
|
||||
break;
|
||||
}
|
||||
break;
|
||||
case 2:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0: //C->F
|
||||
returnValue = oldValue * 1.8 + 32;
|
||||
break;
|
||||
case 1: //k->f
|
||||
returnValue = (oldValue - 273.15) * 1.8 + 32;
|
||||
break;
|
||||
case 2:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
case 3: //R->F
|
||||
returnValue = oldValue - 273.15 * 1.8 + 32;
|
||||
break;
|
||||
|
||||
}
|
||||
break;
|
||||
case 3:
|
||||
switch (oldunit)
|
||||
{
|
||||
case 0: //C->R
|
||||
returnValue = (oldValue + 273.15) * 1.8;
|
||||
break;
|
||||
case 1: //K->R
|
||||
returnValue = oldValue * 1.8;
|
||||
break;
|
||||
case 2: //F->R
|
||||
returnValue = (oldValue - 32) + 273.15 * 1.8;
|
||||
break;
|
||||
case 3:
|
||||
returnValue = oldValue;
|
||||
break;
|
||||
}
|
||||
break;
|
||||
default:
|
||||
break;
|
||||
}
|
||||
return returnValue;
|
||||
case "cd":
|
||||
//米(m)
|
||||
//分米(dm)
|
||||
//厘米(cm)
|
||||
//毫米(mm)
|
||||
//英尺(ft)
|
||||
//英寸(in)
|
||||
//英里(mile)
|
||||
//英寻(fm)
|
||||
//海里(nmile)
|
||||
//埃(a)
|
||||
//码(yd)
|
||||
//密尔(mil)
|
||||
//杆<(rad)
|
||||
|
||||
dataUnit = new double[14]; //As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 10;
|
||||
dataUnit[2] = 100;
|
||||
dataUnit[3] = 1000;
|
||||
dataUnit[5] = 3.28038;
|
||||
dataUnit[4] = 39.3700787401575;
|
||||
dataUnit[6] = 0.001;
|
||||
dataUnit[7] = 0.000621504039776259;
|
||||
dataUnit[8] = 0.546746856205577;
|
||||
dataUnit[9] = 0.000539956803455;
|
||||
dataUnit[10] = 10000000000.0D;
|
||||
dataUnit[11] = 1.093613;
|
||||
dataUnit[12] = 39370.0787401575;
|
||||
dataUnit[13] = 0.198838781515947;
|
||||
break;
|
||||
|
||||
case "mj":
|
||||
|
||||
|
||||
//平方米m2
|
||||
//平方分米dm2
|
||||
//平方厘米cm2
|
||||
//平方毫米mm2
|
||||
//平方英尺ft2
|
||||
//平方英寸in2
|
||||
//平方公里km2
|
||||
//公顷ha
|
||||
//公亩are
|
||||
//英亩acre
|
||||
//平方英里sq -mile
|
||||
//平方码yd2
|
||||
|
||||
dataUnit = new double[12]; //As Double
|
||||
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 100;
|
||||
dataUnit[2] = 10000;
|
||||
dataUnit[3] = 1000000;
|
||||
dataUnit[4] = 10.7608929444;
|
||||
dataUnit[5] = 1550.0031;
|
||||
dataUnit[6] = 0.000001;
|
||||
dataUnit[7] = 0.0001;
|
||||
dataUnit[8] = 0.01;
|
||||
dataUnit[9] = 0.0002471;
|
||||
dataUnit[10] = 0.000000386102158;
|
||||
dataUnit[11] = 1.19599;
|
||||
break;
|
||||
//小时
|
||||
//分钟
|
||||
//天
|
||||
//秒
|
||||
|
||||
case "sj":
|
||||
dataUnit = new double[4]; //As Double
|
||||
|
||||
dataUnit[0] = 1;
|
||||
dataUnit[1] = 60;
|
||||
dataUnit[2] = 0.0416666666666667;
|
||||
dataUnit[3] = 3600;
|
||||
break;
|
||||
|
||||
|
||||
|
||||
case "sd":
|
||||
break;
|
||||
//米每秒
|
||||
//厘米每秒
|
||||
//
|
||||
}
|
||||
if (newunit == oldunit)
|
||||
{
|
||||
return oldValue;
|
||||
|
||||
}
|
||||
return SsWr(oldValue * dataUnit[newunit] / dataUnit[oldunit], Xsdws);
|
||||
|
||||
}
|
||||
|
||||
private double SsWr(double value, int weishu)
|
||||
{
|
||||
long tempValue = 0;
|
||||
double SorR = 0;
|
||||
try
|
||||
{
|
||||
tempValue = (long)(value * Math.Pow(10, weishu));
|
||||
|
||||
SorR = System.Convert.ToInt32((value * Math.Pow(10, weishu) - tempValue) * 10);
|
||||
if (SorR >= 5)
|
||||
{
|
||||
tempValue++;
|
||||
}
|
||||
return tempValue / Math.Pow(10, weishu);
|
||||
}
|
||||
catch
|
||||
{
|
||||
|
||||
return value;
|
||||
|
||||
}
|
||||
}
|
||||
|
||||
|
||||
|
||||
|
||||
|
||||
|
||||
|
||||
}
|
||||
}
|
||||
578
NGToolsPC/XMLHelper.cs
Normal file
578
NGToolsPC/XMLHelper.cs
Normal file
@ -0,0 +1,578 @@
|
||||
using System;
|
||||
using System.Collections.Generic;
|
||||
using System.Linq;
|
||||
using System.Text;
|
||||
using System.Xml;
|
||||
|
||||
namespace NGToolsPC
|
||||
{
|
||||
|
||||
/// <summary>
|
||||
/// XMLHelper XML文档操作管理器
|
||||
/// </summary>
|
||||
public class XMLHelper
|
||||
{
|
||||
public XMLHelper()
|
||||
{
|
||||
//
|
||||
// TODO: 在此处添加构造函数逻辑
|
||||
//
|
||||
}
|
||||
|
||||
|
||||
#region XML文档节点查询和读取
|
||||
/// <summary>
|
||||
/// 选择匹配XPath表达式的第一个节点XmlNode.
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名")</param>
|
||||
/// <returns>返回XmlNode</returns>
|
||||
public static XmlNode GetXmlNodeByXpath(string xmlFileName, string xpath)
|
||||
{
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
return xmlNode;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
return null;
|
||||
//throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 选择匹配XPath表达式的节点列表XmlNodeList.
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名")</param>
|
||||
/// <returns>返回XmlNodeList</returns>
|
||||
public static XmlNodeList GetXmlNodeListByXpath(string xmlFileName, string xpath)
|
||||
{
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNodeList xmlNodeList = xmlDoc.SelectNodes(xpath);
|
||||
return xmlNodeList;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
return null;
|
||||
//throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 选择匹配XPath表达式的第一个节点的匹配xmlAttributeName的属性XmlAttribute.
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="xmlAttributeName">要匹配xmlAttributeName的属性名称</param>
|
||||
/// <returns>返回xmlAttributeName</returns>
|
||||
public static XmlAttribute GetXmlAttribute(string xmlFileName, string xpath, string xmlAttributeName)
|
||||
{
|
||||
string content = string.Empty;
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
XmlAttribute xmlAttribute = null;
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
if (xmlNode.Attributes.Count > 0)
|
||||
{
|
||||
xmlAttribute = xmlNode.Attributes[xmlAttributeName];
|
||||
}
|
||||
}
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return xmlAttribute;
|
||||
}
|
||||
/// <summary>
|
||||
/// 选择匹配XPath表达式的第一个节点的匹配xmlAttributeName的属性XmlAttribute.
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="name">要匹配xmlAttributeName的属性的子节点名称</param>
|
||||
/// <param name="xmlAttributeName">要匹配xmlAttributeName的属性名称</param>
|
||||
/// <param name="xmlAttributeValues">要匹配xmlAttributeName的属性值</param>
|
||||
/// <returns>返回xmlAttributeName的属性的子节点名称InnerText</returns>
|
||||
public static string GetXmlByAttribute(string xmlFileName, string xpath, string name, string xmlAttributeName, string xmlAttributeValues)
|
||||
{
|
||||
string content = string.Empty;
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
//主要
|
||||
XmlNodeList xlist = xmlDoc.SelectNodes(xpath);
|
||||
XmlNode xmlNode = xlist.Cast<XmlNode>().Where(o => o.Attributes.Cast<XmlAttribute>().FirstOrDefault(a => a.Name == xmlAttributeName && a.Value == xmlAttributeValues) != null).FirstOrDefault();
|
||||
|
||||
//XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
foreach (XmlNode node in xmlNode.ChildNodes)
|
||||
{
|
||||
if (node.Name.ToLower() == name.ToLower())
|
||||
{
|
||||
//存在此节点则返回InnerText
|
||||
content = node.InnerText;
|
||||
break;
|
||||
}
|
||||
}
|
||||
}
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return content;
|
||||
}
|
||||
/// <summary>
|
||||
/// 选择匹配XPath表达式的第一个节点的匹配xmlAttributeName的属性XmlAttribute.
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName"></param>
|
||||
/// <param name="xpath"></param>
|
||||
/// <param name="xmlAttributeName">要匹配xmlAttributeName的属性名称</param>
|
||||
/// <param name="xmlAttributeValues">要匹配xmlAttributeName的属性值</param>
|
||||
/// <returns>返回节点InnerText</returns>
|
||||
public static string GetXmlByAttribute(string xmlFileName, string xpath, string xmlAttributeName, string xmlAttributeValues)
|
||||
{
|
||||
string content = string.Empty;
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
//主要
|
||||
XmlNodeList xlist = xmlDoc.SelectNodes(xpath);
|
||||
XmlNode xmlNode = xlist.Cast<XmlNode>().Where(o => o.Attributes.Cast<XmlAttribute>().FirstOrDefault(a => a.Name == xmlAttributeName && a.Value == xmlAttributeValues) != null).FirstOrDefault();
|
||||
|
||||
//XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
content = xmlNode.InnerText;
|
||||
}
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return content;
|
||||
}
|
||||
#endregion
|
||||
|
||||
#region XML文档创建和节点或属性的添加、修改
|
||||
/// <summary>
|
||||
/// 创建一个XML文档
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="rootNodeName">XML文档根节点名称(须指定一个根节点名称)</param>
|
||||
/// <param name="version">XML文档版本号(必须为:"1.0")</param>
|
||||
/// <param name="encoding">XML文档编码方式</param>
|
||||
/// <param name="standalone">该值必须是"yes"或"no",如果为null,Save方法不在XML声明上写出独立属性</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool CreateXmlDocument(string xmlFileName, string rootNodeName, string version, string encoding, string standalone)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
try
|
||||
{
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
XmlDeclaration xmlDeclaration = xmlDoc.CreateXmlDeclaration(version, encoding, standalone);
|
||||
XmlNode root = xmlDoc.CreateElement(rootNodeName);
|
||||
xmlDoc.AppendChild(xmlDeclaration);
|
||||
xmlDoc.AppendChild(root);
|
||||
xmlDoc.Save(xmlFileName);
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 依据匹配XPath表达式的第一个节点来创建它的子节点(如果此节点已存在则追加一个新的同名节点
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="xmlNodeName">要匹配xmlNodeName的节点名称</param>
|
||||
/// <param name="innerText">节点文本值</param>
|
||||
/// <param name="xmlAttributeName">要匹配xmlAttributeName的属性名称</param>
|
||||
/// <param name="value">属性值</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool CreateXmlNodeByXPath(string xmlFileName, string xpath, string xmlNodeName, string innerText, string xmlAttributeName, string value)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//存不存在此节点都创建
|
||||
XmlElement subElement = xmlDoc.CreateElement(xmlNodeName);
|
||||
subElement.InnerXml = innerText;
|
||||
|
||||
//如果属性和值参数都不为空则在此新节点上新增属性
|
||||
if (!string.IsNullOrEmpty(xmlAttributeName) && !string.IsNullOrEmpty(value))
|
||||
{
|
||||
XmlAttribute xmlAttribute = xmlDoc.CreateAttribute(xmlAttributeName);
|
||||
xmlAttribute.Value = value;
|
||||
subElement.Attributes.Append(xmlAttribute);
|
||||
}
|
||||
|
||||
xmlNode.AppendChild(subElement);
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 依据匹配XPath表达式的第一个节点来创建或更新它的子节点(如果节点存在则更新,不存在则创建)
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="xmlNodeName">要匹配xmlNodeName的节点名称</param>
|
||||
/// <param name="innerText">节点文本值</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool CreateOrUpdateXmlNodeByXPath(string xmlFileName, string xpath, string xmlNodeName, string innerText)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
bool isExistsNode = false;//标识节点是否存在
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
//XmlNodeList xlist = xmlDoc.SelectNodes(xpath);
|
||||
//XmlNode xmlNode = xlist.Cast<XmlNode>().Where(o => o.InnerText == innerText).FirstOrDefault();
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//遍历xpath节点下的所有子节点
|
||||
foreach (XmlNode node in xmlNode.ChildNodes)
|
||||
{
|
||||
//XmlAttribute att = node.Attributes.Cast<XmlAttribute>().Where(o => o.Name == innerText).FirstOrDefault();
|
||||
if (node.Name.ToLower() == xmlNodeName.ToLower())
|
||||
{
|
||||
//存在此节点则更新
|
||||
node.InnerXml = innerText;
|
||||
isExistsNode = true;
|
||||
break;
|
||||
}
|
||||
}
|
||||
if (!isExistsNode)
|
||||
{
|
||||
//不存在此节点则创建
|
||||
XmlElement subElement = xmlDoc.CreateElement(xmlNodeName);
|
||||
subElement.InnerXml = innerText;
|
||||
xmlNode.AppendChild(subElement);
|
||||
}
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 依据匹配XPath表达式的第一个节点来创建或更新它的子节点(如果节点存在则更新,不存在则创建)
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="xmlNodeName">要匹配xmlNodeName的节点名称</param>
|
||||
/// <param name="innerText">节点文本值</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool CreateOrUpdateXmlNodeByXPath(string xmlFileName, string xpath, string xmlNodeName, string innerText, string XmlAttributeName, string XmlAttributeValues)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
bool isExistsNode = false;//标识节点是否存在
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//遍历xpath节点下的所有子节点
|
||||
foreach (XmlNode node in xmlNode.ChildNodes)
|
||||
{
|
||||
XmlAttribute att = node.Attributes.Cast<XmlAttribute>().Where(o => o.Name == XmlAttributeName && o.Value == XmlAttributeValues).FirstOrDefault();
|
||||
if (att != null && node.Name.ToLower() == xmlNodeName.ToLower())
|
||||
{
|
||||
//存在此节点则更新
|
||||
node.InnerXml = innerText;
|
||||
isExistsNode = true;
|
||||
#region //遍历xpath节点中的所有属性
|
||||
bool isExistsAttribute = false;
|
||||
foreach (XmlAttribute attribute in node.Attributes)
|
||||
{
|
||||
if (attribute.Name.ToLower() == XmlAttributeName.ToLower())
|
||||
{
|
||||
//节点中存在此属性则更新
|
||||
attribute.Value = XmlAttributeValues;
|
||||
isExistsAttribute = true;
|
||||
break;
|
||||
}
|
||||
}
|
||||
if (!isExistsAttribute)
|
||||
{
|
||||
//节点中不存在此属性则创建
|
||||
XmlAttribute xmlAttribute = xmlDoc.CreateAttribute(XmlAttributeName);
|
||||
xmlAttribute.Value = XmlAttributeValues;
|
||||
node.Attributes.Append(xmlAttribute);
|
||||
}
|
||||
#endregion
|
||||
break;
|
||||
}
|
||||
}
|
||||
if (!isExistsNode)
|
||||
{
|
||||
//不存在此节点则创建
|
||||
XmlElement subElement = xmlDoc.CreateElement(xmlNodeName);
|
||||
subElement.InnerXml = innerText;
|
||||
|
||||
XmlAttribute xmlAttribute = xmlDoc.CreateAttribute(XmlAttributeName);
|
||||
xmlAttribute.Value = XmlAttributeValues;
|
||||
subElement.Attributes.Append(xmlAttribute);
|
||||
xmlNode.AppendChild(subElement);
|
||||
}
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 依据匹配XPath表达式的第一个节点来创建或更新它的子节点(如果节点存在则更新,不存在则创建)
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="xmlNodeName">要匹配xmlNodeName的节点名称</param>
|
||||
/// <param name="innerText">节点文本值</param>
|
||||
/// <param name="parentinnerText">指定父节点文本值</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool CreateOrUpdateXmlNodeByXPath(string xmlFileName, string xpath, string xmlNodeName, string innerText, string parentAttributevalues)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
bool isExistsNode = false;//标识节点是否存在
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNodeList xlist = xmlDoc.SelectNodes(xpath);
|
||||
//主要
|
||||
XmlNode xmlNode = xlist.Cast<XmlNode>().Where(o => o.Attributes.Cast<XmlAttribute>().FirstOrDefault(a => a.Name == "Name" && a.Value == parentAttributevalues) != null).FirstOrDefault();
|
||||
//XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//遍历xpath节点下的所有子节点
|
||||
foreach (XmlNode node in xmlNode.ChildNodes)
|
||||
{
|
||||
if (node.Name.ToLower() == xmlNodeName.ToLower())
|
||||
{
|
||||
//存在此节点则更新
|
||||
node.InnerXml = innerText;
|
||||
isExistsNode = true;
|
||||
break;
|
||||
}
|
||||
}
|
||||
if (!isExistsNode)
|
||||
{
|
||||
//不存在此节点则创建
|
||||
XmlElement subElement = xmlDoc.CreateElement(xmlNodeName);
|
||||
subElement.InnerXml = innerText;
|
||||
xmlNode.AppendChild(subElement);
|
||||
}
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 依据匹配XPath表达式的第一个节点来创建或更新它的属性(如果属性存在则更新,不存在则创建)
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="xmlAttributeName">要匹配xmlAttributeName的属性名称</param>
|
||||
/// <param name="value">属性值</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool CreateOrUpdateXmlAttributeByXPath(string xmlFileName, string xpath, string xmlAttributeName, string value)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
bool isExistsAttribute = false;//标识属性是否存在
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//遍历xpath节点中的所有属性
|
||||
foreach (XmlAttribute attribute in xmlNode.Attributes)
|
||||
{
|
||||
if (attribute.Name.ToLower() == xmlAttributeName.ToLower())
|
||||
{
|
||||
//节点中存在此属性则更新
|
||||
attribute.Value = value;
|
||||
isExistsAttribute = true;
|
||||
break;
|
||||
}
|
||||
}
|
||||
if (!isExistsAttribute)
|
||||
{
|
||||
//节点中不存在此属性则创建
|
||||
XmlAttribute xmlAttribute = xmlDoc.CreateAttribute(xmlAttributeName);
|
||||
xmlAttribute.Value = value;
|
||||
xmlNode.Attributes.Append(xmlAttribute);
|
||||
}
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
#endregion
|
||||
|
||||
#region XML文档节点或属性的删除
|
||||
/// <summary>
|
||||
/// 删除匹配XPath表达式的第一个节点(节点中的子元素同时会被删除)
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool DeleteXmlNodeByXPath(string xmlFileName, string xpath)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//删除节点
|
||||
xmlNode.ParentNode.RemoveChild(xmlNode);
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 删除匹配XPath表达式的第一个节点中的匹配参数xmlAttributeName的属性
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <param name="xmlAttributeName">要删除的xmlAttributeName的属性名称</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool DeleteXmlAttributeByXPath(string xmlFileName, string xpath, string xmlAttributeName)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
bool isExistsAttribute = false;
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
XmlAttribute xmlAttribute = null;
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//遍历xpath节点中的所有属性
|
||||
foreach (XmlAttribute attribute in xmlNode.Attributes)
|
||||
{
|
||||
if (attribute.Name.ToLower() == xmlAttributeName.ToLower())
|
||||
{
|
||||
//节点中存在此属性
|
||||
xmlAttribute = attribute;
|
||||
isExistsAttribute = true;
|
||||
break;
|
||||
}
|
||||
}
|
||||
if (isExistsAttribute)
|
||||
{
|
||||
//删除节点中的属性
|
||||
xmlNode.Attributes.Remove(xmlAttribute);
|
||||
}
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
|
||||
/// <summary>
|
||||
/// 删除匹配XPath表达式的第一个节点中的所有属性
|
||||
/// </summary>
|
||||
/// <param name="xmlFileName">XML文档完全文件名(包含物理路径)</param>
|
||||
/// <param name="xpath">要匹配的XPath表达式(例如:"//节点名//子节点名</param>
|
||||
/// <returns>成功返回true,失败返回false</returns>
|
||||
public static bool DeleteAllXmlAttributeByXPath(string xmlFileName, string xpath)
|
||||
{
|
||||
bool isSuccess = false;
|
||||
XmlDocument xmlDoc = new XmlDocument();
|
||||
try
|
||||
{
|
||||
xmlDoc.Load(xmlFileName); //加载XML文档
|
||||
XmlNode xmlNode = xmlDoc.SelectSingleNode(xpath);
|
||||
if (xmlNode != null)
|
||||
{
|
||||
//遍历xpath节点中的所有属性
|
||||
xmlNode.Attributes.RemoveAll();
|
||||
}
|
||||
xmlDoc.Save(xmlFileName); //保存到XML文档
|
||||
isSuccess = true;
|
||||
}
|
||||
catch (Exception ex)
|
||||
{
|
||||
throw ex; //这里可以定义你自己的异常处理
|
||||
}
|
||||
return isSuccess;
|
||||
}
|
||||
#endregion
|
||||
|
||||
}
|
||||
}
|
||||
10
NGToolsPC/app.config
Normal file
10
NGToolsPC/app.config
Normal file
@ -0,0 +1,10 @@
|
||||
<?xml version="1.0" encoding="utf-8" ?>
|
||||
<configuration>
|
||||
<configSections>
|
||||
</configSections>
|
||||
<connectionStrings>
|
||||
<add name="NGToolsPC.Properties.Settings.NGDATAConnectionString"
|
||||
connectionString="Provider=Microsoft.Jet.OLEDB.4.0;Data Source=|DataDirectory|\NGDATA.mdb"
|
||||
providerName="System.Data.OleDb" />
|
||||
</connectionStrings>
|
||||
</configuration>
|
||||
BIN
NGToolsPC/bin/Debug/AxInterop.DSOFramer.dll
Normal file
BIN
NGToolsPC/bin/Debug/AxInterop.DSOFramer.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/Interop.DSOFramer-副本20210318074609.dll
Normal file
BIN
NGToolsPC/bin/Debug/Interop.DSOFramer-副本20210318074609.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/Interop.DSOFramer.dll
Normal file
BIN
NGToolsPC/bin/Debug/Interop.DSOFramer.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NGDATA.mdb
Normal file
BIN
NGToolsPC/bin/Debug/NGDATA.mdb
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NGToolsPC-副本20210318074609.exe
Normal file
BIN
NGToolsPC/bin/Debug/NGToolsPC-副本20210318074609.exe
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NGToolsPC-副本20210318074609.pdb
Normal file
BIN
NGToolsPC/bin/Debug/NGToolsPC-副本20210318074609.pdb
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NGToolsPC.exe
Normal file
BIN
NGToolsPC/bin/Debug/NGToolsPC.exe
Normal file
Binary file not shown.
10
NGToolsPC/bin/Debug/NGToolsPC.exe.config
Normal file
10
NGToolsPC/bin/Debug/NGToolsPC.exe.config
Normal file
@ -0,0 +1,10 @@
|
||||
<?xml version="1.0" encoding="utf-8" ?>
|
||||
<configuration>
|
||||
<configSections>
|
||||
</configSections>
|
||||
<connectionStrings>
|
||||
<add name="NGToolsPC.Properties.Settings.NGDATAConnectionString"
|
||||
connectionString="Provider=Microsoft.Jet.OLEDB.4.0;Data Source=|DataDirectory|\NGDATA.mdb"
|
||||
providerName="System.Data.OleDb" />
|
||||
</connectionStrings>
|
||||
</configuration>
|
||||
BIN
NGToolsPC/bin/Debug/NGToolsPC.pdb
Normal file
BIN
NGToolsPC/bin/Debug/NGToolsPC.pdb
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NG_OCX.dll
Normal file
BIN
NGToolsPC/bin/Debug/NG_OCX.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NG_Tools.dll
Normal file
BIN
NGToolsPC/bin/Debug/NG_Tools.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NG_Tools.pdb
Normal file
BIN
NGToolsPC/bin/Debug/NG_Tools.pdb
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NPOI.OOXML.dll
Normal file
BIN
NGToolsPC/bin/Debug/NPOI.OOXML.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NPOI.OpenXml4Net.dll
Normal file
BIN
NGToolsPC/bin/Debug/NPOI.OpenXml4Net.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NPOI.OpenXmlFormats.dll
Normal file
BIN
NGToolsPC/bin/Debug/NPOI.OpenXmlFormats.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/NPOI.dll
Normal file
BIN
NGToolsPC/bin/Debug/NPOI.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/SoftDogInstdrv.exe
Normal file
BIN
NGToolsPC/bin/Debug/SoftDogInstdrv.exe
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/SoftDogSetup.dll
Normal file
BIN
NGToolsPC/bin/Debug/SoftDogSetup.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/Debug/stdole.dll
Normal file
BIN
NGToolsPC/bin/Debug/stdole.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/x86/Debug/AxInterop.DSOFramer-副本20210318074613.dll
Normal file
BIN
NGToolsPC/bin/x86/Debug/AxInterop.DSOFramer-副本20210318074613.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/x86/Debug/AxInterop.DSOFramer.dll
Normal file
BIN
NGToolsPC/bin/x86/Debug/AxInterop.DSOFramer.dll
Normal file
Binary file not shown.
BIN
NGToolsPC/bin/x86/Debug/CalResult/报表20210216113538.xls
Normal file
BIN
NGToolsPC/bin/x86/Debug/CalResult/报表20210216113538.xls
Normal file
Binary file not shown.
Some files were not shown because too many files have changed in this diff Show More
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Reference in New Issue
Block a user