Aspen Plus V8.4=================This file contains information about the physical property data packages available in Aspen Plus. Read this file if you are interested in using the specialized data packages from the User Interface.The data packages are delivered as backup files within the Aspen Plus User Interface directory structure in a sub-directory called datapkg.The following backup files are available in the datapkg sub-directory:Filename Data Package-------- --------------------------ethylene.bkp Property method: SR-POLAR Pure component parameters were evaluated using data for vapor pressure, liquid heat capacity and liquid density. Binary parameters were evaluated from VLE and LLE data.flue_gas.bkp For flue-gas purification process. Apparent components: 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*2W, CaF2, CAO, CA(OH)2 Henry-components:CO CO2 SO2 HCl O2 N2 NO HA Property method: ELECNRTL Temperature: 0 - 100 Cformaldehyde.bkp H2O-CH4O-CH2O Property method: UNIFAC Temperature: 0 - 100 C Pressure: 0 - 3 bar Formaldehyde Concentration (mole fraction): 0 - 0.6glycols.bkp This data package is provided as a starting point to build simulation for TEG (or other Glycols) dehydration study. The Schwartzentruber-Renon equation of state (SR-POLAR) is used for this application because it is well suited for high-pressure non-ideal systems. Binary interaction parameters are included in this data package to accurately model the mixtures of components commonly found in gas processing.keamp.bkp H2O-AMP-H2S-CO2 Property method: ELECNRTL with kinetic consideration Temperature: 40 - 100 C AMP Concentration from 2.47 to 4.44 molality CO2 Loading: up to 1.715 (mol CO2/mol AMP at 40 C)kedea.bkp H2O-DEA-H2S-CO2 Property method: ELECNRTL with kinetic consideration Temperature: up to 140 C DEA Concentration up to 30 wt.%kedga.bkp H2O-DGA-H2S-CO2 Property method: ELECNRTL with kinetic consideration Temperature: up to 100 C DGA Concentration up to 65 wt.%kemdea.bkp H2O-MDEA-H2S-CO2 Property method: ELECNRTL with kinetic consideration Temperature: 25 - 120 C Pressure up to 64.8 atm for CO2 MDEA Concentration from 11.72 to 51.40 wt.% kemea.bkp H2O-MEA-H2S-CO2 Property method: ELECNRTL with kinetic consideration Temperature: up to 120 C MEA Concentration up to 50 wt.%methylamine.bkp This data package was developed for simulating methylamines process. Components included are: ammonia, water, methanol, monomethylamine, dimethylamine and trimethylamine. The model used for representing VLE data is the SR-POLARequation-of-state. High pressure VLE data for NH3-H2O and methanol-water were used in the regression. Pure component parameters were evaluated using liquid density, heat capacity and vapor pressure data.pitzer_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- CACl2*6H2O- CASO4*2H2O- CACl2*4H2O- MGCl2- MGSO4- MGCl2*6H2O- MGCl2*7H2O- MGCl2*H2O- MGSO4*6H2O- HCl- H2SO4 Property method: PITZER Temperature: around 25Cpitzer_2.bkp H2O- NACl- KCl- CACl2- CACL2*4H2O- CACL2*6H2O- BACL2- BACL2*2H2O Property method: PITZER Temperature: up to 200 C Pressure equilibrium only to 1 atmpitzer_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 Property method: PITZER Temperature: 0 - 250 Cpitzer_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 Property method: PITZER Temperature: -60 - 25 C pmdea.bkp H2O-MDEA-H2S-CO2 Property method: ELECNRTL Temperature: 25 - 120 C Pressure up to 64.8 atm for CO2 MDEA Concentration from 11.72 to 51.40 wt% hno3.bkp H2O-HNO3 Property method: ELECNRTL Temperature: 0 - 120 C HNO3 Concentration up to 100 wt%