package com.ruoyi.ngCalTools.model; public class GasProps { // corresponds to the control group in meter classes public int lStatus; // calculation status 计算状态 public boolean 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[] getAdMixtureD() { return adMixtureD; } public void setAdMixtureD(double[] adMixtureD) { this.adMixtureD = adMixtureD; } public int getlStatus() { return lStatus; } public void setlStatus(int lStatus) { this.lStatus = lStatus; } public boolean isbForceUpdate() { return bForceUpdate; } public void setbForceUpdate(boolean bForceUpdate) { this.bForceUpdate = bForceUpdate; } public double[] getAdMixture() { return adMixture; } public void setAdMixture(double[] adMixture) { this.adMixture = adMixture; } public double[] getAdMixtureV() { return adMixtureV; } public void setAdMixtureV(double[] adMixtureV) { this.adMixtureV = adMixtureV; } public int getdCbtj() { return dCbtj; } public void setdCbtj(int dCbtj) { this.dCbtj = dCbtj; } public double getdPb() { return dPb; } public void setdPb(double dPb) { this.dPb = dPb; } public double getdTb() { return dTb; } public void setdTb(double dTb) { this.dTb = dTb; } public double getdPf() { return dPf; } public void setdPf(double dPf) { this.dPf = dPf; } public double getdTf() { return dTf; } public void setdTf(double dTf) { this.dTf = dTf; } public double getdMrx() { return dMrx; } public void setdMrx(double dMrx) { this.dMrx = dMrx; } public double getdZb() { return dZb; } public void setdZb(double dZb) { this.dZb = dZb; } public double getdZf() { return dZf; } public void setdZf(double dZf) { this.dZf = dZf; } public double getdFpv() { return dFpv; } public void setdFpv(double dFpv) { this.dFpv = dFpv; } public double getdDb() { return dDb; } public void setdDb(double dDb) { this.dDb = dDb; } public double getdDf() { return dDf; } public void setdDf(double dDf) { this.dDf = dDf; } public double getdRhob() { return dRhob; } public void setdRhob(double dRhob) { this.dRhob = dRhob; } public double getdRhof() { return dRhof; } public void setdRhof(double dRhof) { this.dRhof = dRhof; } public double getdRD_Ideal() { return dRD_Ideal; } public void setdRD_Ideal(double dRD_Ideal) { this.dRD_Ideal = dRD_Ideal; } public double getdRD_Real() { return dRD_Real; } public void setdRD_Real(double dRD_Real) { this.dRD_Real = dRD_Real; } public double getdHo() { return dHo; } public void setdHo(double dHo) { this.dHo = dHo; } public double getdH() { return dH; } public void setdH(double dH) { this.dH = dH; } public double getdS() { return dS; } public void setdS(double dS) { this.dS = dS; } public double getdCpi() { return dCpi; } public void setdCpi(double dCpi) { this.dCpi = dCpi; } public double getdCp() { return dCp; } public void setdCp(double dCp) { this.dCp = dCp; } public double getdCv() { return dCv; } public void setdCv(double dCv) { this.dCv = dCv; } public double getDk() { return dk; } public void setDk(double dk) { this.dk = dk; } public double getdKappa() { return dKappa; } public void setdKappa(double dKappa) { this.dKappa = dKappa; } public double getdSOS() { return dSOS; } public void setdSOS(double dSOS) { this.dSOS = dSOS; } public double getdCstar() { return dCstar; } public void setdCstar(double dCstar) { this.dCstar = dCstar; } public double getdHhvMol() { return dHhvMol; } public void setdHhvMol(double dHhvMol) { this.dHhvMol = dHhvMol; } public double getdLhvMol() { return dLhvMol; } public void setdLhvMol(double dLhvMol) { this.dLhvMol = dLhvMol; } public double getdHhvv() { return dHhvv; } public void setdHhvv(double dHhvv) { this.dHhvv = dHhvv; } public double getdLhvv() { return dLhvv; } public void setdLhvv(double dLhvv) { this.dLhvv = dLhvv; } public double getdHhvm() { return dHhvm; } public void setdHhvm(double dHhvm) { this.dHhvm = dHhvm; } public double getdLhvm() { return dLhvm; } public void setdLhvm(double dLhvm) { this.dLhvm = dLhvm; } public double getdZb11062() { return dZb11062; } public void setdZb11062(double dZb11062) { this.dZb11062 = dZb11062; } public double getdRhob11062() { return dRhob11062; } public void setdRhob11062(double dRhob11062) { this.dRhob11062 = dRhob11062; } public double getdRhof11062() { return dRhof11062; } public void setdRhof11062(double dRhof11062) { this.dRhof11062 = dRhof11062; } public double getdRD_Ideal11062() { return dRD_Ideal11062; } public void setdRD_Ideal11062(double dRD_Ideal11062) { this.dRD_Ideal11062 = dRD_Ideal11062; } public double getdRD_Real11062() { return dRD_Real11062; } public void setdRD_Real11062(double dRD_Real11062) { this.dRD_Real11062 = dRD_Real11062; } public double getdWobbeIndex() { return dWobbeIndex; } public void setdWobbeIndex(double dWobbeIndex) { this.dWobbeIndex = dWobbeIndex; } public double getdPc() { return dPc; } public void setdPc(double dPc) { this.dPc = dPc; } public double getdTC() { return dTC; } public void setdTC(double dTC) { this.dTC = dTC; } public double getdBzsx() { return dBzsx; } public void setdBzsx(double dBzsx) { this.dBzsx = dBzsx; } public double getdBzxx() { return dBzxx; } public void setdBzxx(double dBzxx) { this.dBzxx = dBzxx; } public double getdTotalC() { return dTotalC; } public void setdTotalC(double dTotalC) { this.dTotalC = dTotalC; } public double getdC2() { return dC2; } public void setdC2(double dC2) { this.dC2 = dC2; } public double getdC2j() { return dC2j; } public void setdC2j(double dC2j) { this.dC2j = dC2j; } public double getdC3j() { return dC3j; } public void setdC3j(double dC3j) { this.dC3j = dC3j; } public double getdC4j() { return dC4j; } public void setdC4j(double dC4j) { this.dC4j = dC4j; } public double getdC5j() { return dC5j; } public void setdC5j(double dC5j) { this.dC5j = dC5j; } public double getdC6j() { return dC6j; } public void setdC6j(double dC6j) { this.dC6j = dC6j; } public double getdC3C4() { return dC3C4; } public void setdC3C4(double dC3C4) { this.dC3C4 = dC3C4; } public String getDngComponents() { return dngComponents; } public void setDngComponents(String dngComponents) { this.dngComponents = dngComponents; } 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 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 dPc; // 临界压力 public double dTC; // 临界温度 public double dBzsx; // 爆炸上限 public double dBzxx; // 爆炸下限 public double dTotalC; // 总炭含量 (kg/m3) public double dC2; // C2组分含量 (kg/m3) public double dC2j; // C2以上组分含量 (kg/m3) public double dC3j; // C3以上组分含量 (kg/m3) public double dC4j; // C4以上组分含量 (kg/m3) public double dC5j; // C5以上组分含量 (kg/m3) public double dC6j; // C6以上组分含量 (kg/m3) public double dC3C4; // C3C4组分含量 (kg/m3) public String dngComponents; //组分的组合字符串 从前端传过来 }