Application of Liquid State Models for the Time Efficient Phase Equilibrium Calculation of Supercritical CO2 and H2O at High Temperatures and Pressures

Author： Islam Akand   Carlson Eric  

Publisher： Springer Publishing Company

ISSN： 0095-9782

Source： Journal of Solution Chemistry, Vol.42, Iss.8, 2013-09, pp. : 1641-1653

Disclaimer: Any content in publications that violate the sovereignty, the constitution or regulations of the PRC is not accepted or approved by CNPIEC.

Previous Menu Next

Abstract

Related content

Liquid-liquid and liquid-liquid-solid equilibrium in Na 2 CO 3 -PEG-H 2 O

By Taboada M.E.   Asenjo J.A.   Andrews B.A.  

Fluid Phase Equilibria, Vol. 180, Iss. 1, 2001-04 ,pp. : 273-280

Elsevier

Access to resources Recommend Favorite

(Liquid + liquid) phase equilibria at high pressures Pressure-limited closed-loop behaviour of { xc -(CH 2 ) 4 O + (1 - x )H 2 O} and the effect of dissolved ammonium sulfate

By Wallbruch A.   Schneider G.M.  

Journal of Chemical Thermodynamics, Vol. 27, Iss. 4, 1995-04 ,pp. : 377-382

Academic Press

Access to resources Recommend Favorite

EFFECTS OF H2O AND CO2 DILUTION ON THE CATALYTIC AND GAS-PHASE COMBUSTION OF METHANE OVER PLATINUM AT ELEVATED PRESSURES

By  

Combustion Science and Technology, Vol. 179, Iss. 3, 2007-03 ,pp. : 553-600

Taylor & Francis Ltd

Access to resources Recommend Favorite

Modelling of the equilibrium properties of the system H 3 PO 4 -H 2 O: representation of VLE and liquid phase composition

By Cherif M.   Mgaidi A.   Ammar M.N.   Abderrabba M.   Furst W.  

Fluid Phase Equilibria, Vol. 175, Iss. 1, 2000-10 ,pp. : 197-212

Elsevier

Access to resources Recommend Favorite

Vapor-liquid equilibrium data for the CO 2 + 1,1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa

By Valtz A.   Coquelet C.   Baba-Ahmed A.   Richon D.  

Fluid Phase Equilibria, Vol. 207, Iss. 1, 2003-05 ,pp. : 53-67

Elsevier

Access to resources Recommend Favorite