aspen自带案例列表 - 图文

SYSOP15物性方法

SYSOP意为系统操作员，SYSOP15是基于ELECNRTL修改的适用于某些特定体系的物性方法。

This table shows electrolyte data packages, available in the ELECINS sub-directory, that use the SYSOP15M property method: Filename Electrolyte System

eh2ohc.bkp H2O - HCL (as Henry-comps) using ELECNRTL ehno3.bkp H2O - HNO3 using ELECNRTL enaoh.bkp H2O - NAOH using ELECNRTL eso4br.bkp H2O - H2SO4 - HBR using ELECNRTL ehbr.bkp ehi.bkp eh2so4.bkp ehclmg.bkp enaohs.bkp eso4cl.bkp ecauts.bkp ekoh.bkp ecaust.bkp ehcl.bkp ehclff.bkp ehclle.bkp eamp.bkp edea.bkp edga.bkp emdea.bkp pmdea.bkp emea.bkp ehotde.bkp ecl2.bkp enh3co.bkp enh3so.bkp esouro.bkp enh3h2.bkp ehotca.bkp enh3hc.bkp ebrine.bkp ebrinx.bkp H2O - HBR using ELECNRTL H2O - HI using ELECNRTL H2O - H2SO4 using ELECNRTL H2O - HCL - MGCL2 using ELECNRTL H2O - NAOH - SO2 using ELECNRTL H2O - H2SO4 - HCL using ELECNRTL

H2O - NAOH - NACL - NA2SO4 -NA2SO4.10H2O - NA2SO4.NAOH - NA2SO4.NAOH.NACL using ELECNRTL H2O - KOH using ELECNRTL

H2O - NAOH - NACL - NA2SO4 using ELECNRTL H2O - HCL (as solvent) using ELECNRTL

H2O - HCL (as Henry-comp, based on Fritz &Fuget) using ELECNRTL H2O - HCL (as solvent, recommend for LLE) using ELECNRTL H2O - amp - H2S - CO2 using ELECNRTL H2O - DEA - H2S - CO2 using ELECNRTL H2O - DGA - H2S - CO2 using ELECNRTL H2O - MDEA - CO2 - H2S using ELECNRTL

H2O - MDEA - CO2 - H2S (based on the 1997 paper of Posey & Rochelle) using ELECNRTL H2O - MEA - H2S - CO2 using ELECNRTL H2O - DEA - K2CO3 - H2S - CO2 using ELECNRTL H2O - CL2 - HCL using ELECNRTL H2O - NH3 - CO2 using ELECNRTL H2O - NH3 - SO2 using ELECNRTL

H2O - NH3 - H2S - CO2 - NAOH using ELECNRTL H2O - NH3 - H2S using ELECNRTL

H2O - K2CO3 - CO2 - KHCO3 using ELECNRTL withoutsalt precipitation H2O - NH3 - HCN using ELECNRTL H2O - CO2 - H2S - NACL using ELECNRTL

H2O - CO2 - H2S - NACL using ELECNRTL (extended Temperature range)

eclscr.bkp H2O - CL2 - CO2 - HCL - NAOH - NACL - NA2CO3 using ELECNRTL ekohx.bkp H2O - KOH (high concentration) using ELECNRTL ehf.bkp H2O - HF using ELECNRTL

ehotcb.bkp H2O - K2CO3 - CO2 - KHCO3 using ELECNRTL withsalt precipitation enh3po.bkp H2O - NH3 - H3PO4 - H2S using ELECNRTL esour.bkp H2O - NH3 - H2S - CO2 using ELECNRTL brine.bkp H2O - CO2 - H2S - NACL using SYSOP15 caust.bkp causts.bkp dea.bkp dga.bkp flue_g.bkp hna2co.bkp h2ohbr.bkp h2ohcl.bkp h2ohf.bkp h2ohi.bkp hotca.bkp hotcb.bkp hotdea.bkp kdea.bkp kmdea.bkp kmea.bkp keamp.bkp kedea.bkp kedga.bkp kemdea.bkp kemea.bkp mcl2.bkp mdea.bkp mea.bkp mh2so4.bkp mhbr.bkp mhcl.bkp H2O - NAOH - NACL - NA2SO4 using SYSOP15M

H2O - NAOH - NACL - NA2SO4 -NA2SO4.10H2O - NA2SO4.NAOH - NA2SO4.NAOH.NACL using SYSOP15M H2O - DEA - H2S - CO2 using SYSOP15M H2O - DGA - H2S - CO2 using SYSOP15M

H2O - N2 - O2 - CO2 - CO - SO2 - SO3 - NO - NO2 - HCL -HF - HNO3 - HNO2 - H2SO4 - H2SEO3 - HGCL2 - HG2CL2 – HG -C - SE - SEO2 - HG(OH)2 - CASO4*2H2O - CAF2 - CAO - CA(OH)2using ELECNRTL H2O - NA2CO3 - NA2CO3*10H2O - NA2CO3*7H2O - NA2CO3*H2O using ELECNRTL H2O - HBR using SYSOP15 H2O - HCL using SYSOP15 H2O - HF using SYSOP15 H2O - HI using SYSOP15

H2O - K2CO3 - CO2 using SYSOP15

H2O - K2CO3 - CO2 - KHCO3 using SYSOP15 H2O - DEA - K2CO3 - H2S - CO2 using SYSOP15M

H2O - DEA - H2S - CO2 using SYSOP15M with kinetic consideration H2O - MDEA - H2S - CO2 using SYSOP15M with kinetic consideration H2O - MEA - H2S - CO2 using SYSOP15M with kinetic consideration H2O - amp - H2S - CO2 using ELECNRTL with kinetic consideration H2O - DEA - H2S - CO2 using ELECNRTL with kinetic consideration H2O - DGA - H2S - CO2 using ELECNRTL with kinetic consideration H2O - MDEA - H2S - CO2 using ELECNRTL with kinetic consideration H2O - MEA - H2S - CO2 using ELECNRTL with kinetic consideration H2O - CL2 using SYSOP15

H2O - MDEA - H2S - CO2 using SYSOP15M H2O - MEA - H2S - CO2 using SYSOP15M H2O - H2SO4 using SYSOP15M H2O - HBR using SYSOP15M H2O - HCL using SYSOP15M

mhcl1.bkp H2O - HCL using SYSOP15M

mhclmg.bkp H2O - HCL - MGCL2 using SYSOP15M mhf.bkp H2O - HF using SYSOP15M

mhf2.bkp H2O - HF (to 100% HF) using ENRTL-HF which considers HF vapor phase association mhno3.bkp H2O - HNO3 using SYSOP15M

mnaoh.bkp H2O - NAOH using SYSOP15M (H5O3- is used instead of OH-) mnaoh1.bkp H2O - NAOH using SYSOP15M mso4br.bkp H2O - H2SO4 - HBR using SYSOP15M mso4cl.bkp H2O - H2SO4 - HCL using SYSOP15M naohso.bkp H2O - NAOH - SO2 using SYSOP15 nh3co2.bkp H2O - NH3 - CO2 using SYSOP15 nh3h2s.bkp H2O - NH3 - H2S using SYSOP15

nh3h2o.bkp H2O - NH3 (as a solvent to 100%) using ELECNRTL nh3hcn.bkp H2O - HCN using SYSOP15

nh3po4.bkp H2O - NH3 - H2S - H3PO4 using SYSOP15 nh3so2.bkp H2O - NH3 - SO2 using SYSOP15

pitz_1.bkp H2O - NAHCO3 - NA2SO4 - NACL - NAOH - NA2CO3*10H2O -NA2SO4*10H2O - NA2CO3*NAHCO3*2H2O - NA2CO3*7H2O -NA2CO3*H2O - KHCO3 - K2CO3 - K2SO4 - KHSO4 - KCL - KOH - K2CO3*1.5H2O - CACL2 - CASO4 - CA(OH)2 -ACL2*6H2O - CASO4*2H2O - CACL2*4H2O - MGCL2 - MGSO4 - MGCL2*6H2O - MGCL2*7H2O - MGCL2*H2O - MGSO4*6H2O - HCL -H2SO4 using PITZER

pitz_2.bkp H2O - NACL - KCL - CACL2 - CACL2*4H2O - CACL2*6H2O - BACL2 - BACL2*2H2O using PITZER

pitz_3.bkp H2O - NA2SO4 - NACL - NA2CO3*10H2O - NA2CA(SO4)2 - NA4CA(SO4)3*2H2O - NANO3 - K2SO4 - KCL - KNO3 - K2CA(SO4)2*H2O - CACL2 - CACL2*6H2O - CASO4*2H2O - 2(CASO4)*H2O - CACL2*4H2O - CA(NO3)2 - CA(NO3)2*4H2O using PITZER

pitz_4.bkp H2O - NACL - NA2SO4 - KCL - K2SO4 - CACL2 - CASO4 - MGCL2 - MGSO4 - CACL2*6H2O - MGCL2*6H2O - MGCL2*8H2O - MGCL2*12H2O - KMGCL3*6H2O - MG2CACL6*12H2O - NA2SO4*10H2O -MGSO4*6H2O - MGSO4*7H2O - K2MG(SO4)2*6H2O using PITZER pnh3co.bkp H2O - NH3 - CO2 using SYSOP16 pnh3h2.bkp H2O - NH3 - H2S using SYSOP16 pnh3so.bkp H2O - NH3 - SO2 using SYSOP16 psour.bkp H2O - NH3 - H2S - CO2 using SYSOP16 sour.bkp H2O - NH3 - H2S - CO2 using SYSOP15

souroh.bkp H2O - NH3 - H2S - CO2 - NAOH using SYSOP15

性质 ELECNRTL SYSOP15 PHIVMX03 RKS SYSOP15M PHIVMX03 RKS PHIVMX PHIVMX01 RK PHILMX PHILMXEL Henry's law and PHILMX34 Henry's law PHILMX39 Henry's law and andELECNRTL,1967 ELECNRTL,扩展ELECNRTL,扩展Antoine方程，真实ASMEsteam table，Antoine方程，RK,组成模型 真实组分模型 真实组分模型 HVMX HLMX HVMX01 RK HVMX00 Ideal Gas model ELECNRTL，水体系是真实组成 Ideal Gas model，包括压力影响 ELECNRTL，水体系是真实组成 Ideal Gas model，包括压力影响 ELECNRTL，水体系是真实组成 Ideal Gas model Clarke density HVMX00 HLMXELC ELECNRTL，mixed HLMX15A solvent体系是真实组成 GVMX01 RK GVMX00 HLMX15M ELECNRTL，mixed- solvent体系是真实组成 GVMX00 GVMX GLMX GLMXELC ELECNRTL，mixed GLMX15A solvent体系是真实组成 SVMX01 SLMXELC RK SVMX00 GLMX15M ELECNRTL，mixed- solvent体系是真实组成 SVMX00 SLMX15M ELECNRTL，mixed- solvent体系是真实组成 SVMX SLMX ELECNRTL，mixed SLMX15B solvent体系是真实组成 RK VVMX00 VVMX VLMX VVMX01 VVMX00 VLMX18A VLMXELC ELECNRTL，mixed VLMX18A solvent体系是真实组成 MUVMX MUVMX01 MULMX MULMX09 KVMX KLMX DVMX DLMX PHIV PHIL HV HL GV GL SV SL VV VL DL DV KVMX01 KLMX07 DVMX01 DLMX06 PHIV01 PHIL04 HV02 HL01 GV01 GL04 SV01 SL04 VV01 VL01 DL02 DV01 MUVMX01 MULMX09 KVMX01 KLMX07 DVMX01 DLMX06 PHIV00 PHIL04 HV00 HL00 GV00 GL00 SV00 SL00 VV00 VL01 DL02 DV01 MUVMX01 MULMX09 KVMX01 KLMX07 DVMX01 DLMX06 PHIV00 PHIL04 HV00 HL00 GV00 GL00 SV00 SL00 VV00 VL01 DL02 DV01 SIGLMX SIGLMX06 SIGLMX06 SIGLMX06 MUL MUV KV KL SIGL HSMX GSMX SSMX VSMX KSMX PHIS HS GS SS VS KS WSL HCSL

MUL01 MUV01 KV01 KL01 SIGL01 HSMX02 GSMX02 SSMX01 VSMX02 KSMX01 PHIS00 HS02 GS02 SS02 VS01 KS01 HCSOL01 MUL01 MUV01 KV00 KL01 SIGL01 HSMX02 GSMX02 SSMX01 VSMX02 KSMX01 PHIS00 HS02 GS02 SS02 VS01 KS01 HCSOL01 MUL01 MUV01 KV00 KL01 SIGL01 HSMX02 GSMX02 SSMX01 VSMX02 KSMX01 PHIS00 HS02 GS02 SS02 VS01 KS01 HCSOL01 PHISMX PHISMX00 PHISMX00 PHISMX00 WATSOL00 WATSOL00 WATSOL00

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