流化床反应器Aspen plus模拟数据.doc

VLSTDAPI standard liquid molar volume0.0556062cum/kmol1.43E-05ZCCritical compressibility factor0.24630.0257PCCritical pressure8163768.5N/sqm692274.3TCCritical temperature719.34K5.01VCCritical volume0.1805cum/kmol-0.0109FREEZEPTFreeze point temperature259.7KDGFORMGibbs energy of formation (ideal gas)-298034387.4J/kmol3795396.7DHFORMHeat of formation (ideal gas)-388938472.6J/kmol2889694.5HFUSHeat of fusion11623150J/kmol12552MWMolecular weight62.068TBNormal boiling point470.6473K0.0525OMEGAPitzer acentric factor0.51814DELTASolubility parameter 25 C33756.4(J/cum)*.517115.7SGSpecific gravity1.1173550.000288CPIALEETDE Aly-Lee ideal gas Cp+J/kmol-K65519.69J/kmol-K157464.7J/kmol-K1665.44K113063.8J/kmol-K771.9435K0Unitless8.31447J/mol-K298K1000KMULNVETDE equation for liquid viscosity+N-sec/sqm-13.06623Unitless4033.58K-1116747K*2212612800K*3259.26K719.3373KDNLEXSATTDE expansion for liquid molar density+kg/cum13.68103kmol/cum3.106776kmol/cum-3.887829kmol/cum2.53471kmol/cum0kmol/cum0kmol/cum0kmol/cum719.3373K6Unitless259.26K719.3373KWAGNER25TDE Wagner 25 liquid vapor pressure+N/sqm-8.332095Unitless2.034673Unitless-5.615515Unitless-1.992714Unitless15.91522Unitless719.3373K259.26K719.3373KDHVLTDEWTDE Watson equation for heat of vaporization+J/kmol18.16271Unitless0.1262906Unitless0.4476227Unitless-0.1328732Unitless719.3373K4Unitless259.26K719.3373KSIGTDEWTDE Watson equation for liquid-gas surface tension+N/m-2.652948Unitless0.7168643Unitless2.349106E-09Unitless-2.699177E-09Unitless719.3373K4Unitless259.26K719.3373KCPLTMLPOThermoML polynomials for liquid Cp+J/kmol-K1043208J/kmol-K-6208.457J/kmol-K*210.51548J/kmol-K*30J/kmol-K*40J/kmol-K*55Unitless259.26K462.9607KKLTMLPOThermoML polynomials for liquid thermal conductivity+Watt/m-K0.279772Watt/m-K-6.966482E-05Watt/m-K*20Watt/m-K*30Watt/m-K*44Unitless273.0001K640KCPSTMLPOThermoML polynomials for solid Cp+J/kmol-K87373.88J/kmol-K-2059.783J/kmol-K*227.62369J/kmol-K*3-0.1379473J/kmol-K*40.0002469359J/kmol-K*55Unitless80K259.7KKVTMLPOThermoML polynomials for vapor thermal conductivity+Watt/m-K-0.007076243Watt/m-K3.625601E-05Watt/m-K*29.766584E-08Watt/m-K*3-3.692773E-11Watt/m-K*44Unitless480K1070KMUVTMLPOThermoML polynomials for vapor viscosity+N-sec/sqm-7.311253E-07N-sec/sqm2.957528E-08N-sec/sqm-K-1.049657E-12N-sec/sqm-K*2-1.382646E-15N-sec/sqm-K*34Unitless480K1070KTPTTriple point temperature259.7K1.62FAMILYCompound family namePOLYOLSSUB FAMILYCompound sub family namealiphatic glycolsVLSTDAPI standard liquid molar volume0.080533cum/kmol0.000206ZCCritical compressibility factor0.27850.0177PCCritical pressure4593695.6N/sqm64474.9TCCritical temperature364.946K0.259VCCritical volume0.1839cum/kmol-0.0114MUPDipole moment1.2649E-25(J*cum)*.5FREEZEPTFreeze point temperature87.85KDGFORMGibbs energy of formation (ideal gas)59952907.2J/kmol1967223.2DHFORMHeat of formation (ideal gas)17454000J/kmol1172000HFUSHeat of fusion3002871.6J/kmol5301.8MWMolecular weight42.08TBNormal boiling point225.525K0.124OMEGAPitzer acentric factor0.14158DELTASolubility parameter 25 C11860.3(J/cum)*.55300.6SGSpecific gravity0.523050.00134CPIALEETDE Aly-Lee ideal gas Cp+J/kmol-K33865.96J/kmol-K162245.8J/kmol-K1164.658K65604.97J/kmol-K401.9671K0Unitless8.31447J/mol-K50K3000KCPLTDECSTDE equation for liquid Cp+J/kmol-K122104.8J/kmol-K-620.6829J/kmol-K*22.708691J/kmol-K*3-0.003604033J/kmol-K*45231.685J/kmol-K364.9457K4Unitless87.85K357.6468KMULNVETDE equation for liquid viscosity+N-sec/sqm-13.60359Unitless1831.598K-203514.6K*210212110K*387.85K364.9457KDNLEXSATTDE expansion for liquid molar density+kg/cum10.27348kmol/cum5.967218kmol/cum-5.722345kmol/cum4.951059kmol/cum0kmol/cum0kmol/cum0kmol/cum364.9457K6Unitless87.85K364.9457KWAGNER25TDE Wagner 25 liquid vapor pressure+N/sqm-6.492461Unitless0.9967976Unitless-1.010451Unitless-2.571251Unitless15.3402Unitless364.9457K87.85K364.9457KDHVLTDEWTDE Watson equation for heat of vaporization+J/kmol17.25187Unitless1.165803Unitless-1.459517Unitless0.7331973Unitless364.9457K4Unitless87.85K364.9457KSIGTDEWTDE Watson equation for liquid-gas surface tension+N/m-2.898065Unitless1.239623Unitless-7.614463E-10Unitless8.870249E-10Unitless364.9457K4Unitless87.85K364.9457KKLTMLPOThermoML polynomials for liquid thermal conductivity+Watt/m-K0.1768823Watt/m-K-0.000101222Watt/m-K*2-5.515645E-07Watt/m-K*30Watt/m-K*44Unitless90K320KCPSTMLPOThermoML polynomials for solid Cp+J/kmol-K-19146.58J/kmol-K1732.553J/kmol-K*2-16.44506J/kmol-K*30.07660665J/kmol-K*40J/kmol-K*55Unitless20K87.85KKVTMLPOThermoML polynomials for vapor thermal conductivity+Watt/m-K-0.007460532Watt/m-K6.007474E-05Watt/m-K*28.086096E-08Watt/m-K*30Watt/m-K*44Unitless230K623.1087KMUVTMLPOThermoML polynomials for vapor viscosity+N-sec/sqm-6.33037E-07N-sec/sqm3.402028E-08N-sec/sqm-K-8.379171E-12N-sec/sqm-K*20N-sec/sqm-K*34Unitless230K540KTPTTriple point temperature87.85K0.0196FAMILYCompound family name1-ALKENESSUB FAMILYCompound sub family nameVLSTDAPI standard liquid molar volume0.080533cum/kmol0.000206ZCCritical compressibility factor0.27850.0177PCCritical pressure4593695.6N/sqm64474.9TCCritical temperature364.946K0.259VCCritical volume0.1839cum/kmol-0.0114MUPDipole moment1.2649E-25(J*cum)*.5FREEZEPTFreeze point temperature87.85KDGFORMGibbs energy of formation (ideal gas)59952907.2J/kmol1967223.2DHFORMHeat of formation (ideal gas)17454000J/kmol1172000HFUSHeat of fusion3002871.6J/kmol5301.8MWMolecular weight42.08TBNormal boiling point225.525K0.124OMEGAPitzer acentric factor0.14158DELTASolubility parameter 25 C11860.3(J/cum)*.55300.6SGSpecific gravity0.523050.00134CPIALEETDE Aly-Lee ideal gas Cp+J/kmol-K33865.96J/kmol-K162245.8J/kmol-K1164.658K65604.97J/kmol-K401.9671K0Unitless8.31447J/mol-K50K3000KCPLTDECSTDE equation for liquid Cp+J/kmol-K122104.8J/kmol-K-620.6829J/kmol-K*22.708691J/kmol-K*3-0.003604033J/kmol-K*45231.685J/kmol-K364.9457K4Unitless87.85K357.6468KMULNVETDE equation for liquid viscosity+N-sec/sqm-13.60359Unitless1831.598K-203514.6K*210212110K*387.85K364.9457KDNLEXSATTDE expansion for liquid molar density+kg/cum10.27348kmol/cum5.967218kmol/cum-5.722345kmol/cum4.951059kmol/cum0kmol/cum0kmol/cum0kmol/cum364.9457K6Unitless87.85K364.9457KWAGNER25TDE Wagner 25 liquid vapor pressure+N/sqm-6.492461Unitless0.9967976Unitless-1.010451Unitless-2.571251Unitless15.3402Unitless364.9457K87.85K364.9457KDHVLTDEWTDE Watson equation for heat of vaporization+J/kmol17.25187Unitless1.165803Unitless-1.459517Unitless0.7331973Unitless364.9457K4Unitless87.85K364.9457KSIGTDEWTDE Watson equation for liquid-gas surface tension+N/m-2.898065Unitless1.239623Unitless-7.614463E-10Unitless8.870249E-10Unitless364.9457K4Unitless87.85K364.9457KKLTMLP