Hydrate temperature depression of MEG solutions at concentrations up to 60wt%. Experimental data and simulation results
Authors:
- Pål V. HemmingsenPHPål V. Hemmingsen
- Roderick BurgassRBRoderick Burgass
- Karen Schou PedersenKPKaren Schou Pedersen
- Keijo KinnariKKKeijo Kinnari
- Henrik SørensenHSHenrik Sørensen
- 1 August 2011
- journal article
- Published by Elsevier in Fluid Phase Equilibria
- Vol. 307 (2) , 175-179
Abstract
No abstract availableKeywords
This publication has 15 references indexed in Scilit:
- Experimental and thermodynamic modelling of systems containing water and ethylene glycol: Application to flow assurance and gas processingFluid Phase Equilibria, 2009
- Experimental and modeling studies on the hydrate formation of CO2 and CO2-rich gas mixturesChemical Engineering Journal, 2000
- Measurements and Predictions of Hydrate Equilibrium ConditionsAnnals of the New York Academy of Sciences, 2000
- Phase equilibrium calculations for unprocessed well streams containing hydrate inhibitorsFluid Phase Equilibria, 1996
- Measurement of the critical properties of thermally unstable substances and mixtures by the pulse-heating methodThe Journal of Chemical Thermodynamics, 1993
- A combined soave-redlich-kwong and NRTL equation for calculating the distribution of methanol between water and hydrocarbon phasesFluid Phase Equilibria, 1993
- Hydrate formation and inhibition in gas condensate and hydrocarbon liquid systemsFluid Phase Equilibria, 1987
- New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixturesFluid Phase Equilibria, 1979
- A New Two-Constant Equation of StateIndustrial & Engineering Chemistry Fundamentals, 1976
- Equilibrium constants from a modified Redlich-Kwong equation of stateChemical Engineering Science, 1972