G.F. Versteeg

ORCID: 0000-0003-0448-9483
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Research Areas
  • Carbon Dioxide Capture Technologies
  • Phase Equilibria and Thermodynamics
  • Membrane Separation and Gas Transport
  • Catalytic Processes in Materials Science
  • Chemical and Physical Properties in Aqueous Solutions
  • Industrial Gas Emission Control
  • Thermodynamic properties of mixtures
  • Catalysts for Methane Reforming
  • Advanced Thermodynamics and Statistical Mechanics
  • Process Optimization and Integration
  • Fluid Dynamics and Mixing
  • Minerals Flotation and Separation Techniques
  • Membrane-based Ion Separation Techniques
  • Catalysis and Oxidation Reactions
  • Catalysis and Hydrodesulfurization Studies
  • Innovative Microfluidic and Catalytic Techniques Innovation
  • Hydrogen Storage and Materials
  • Heat and Mass Transfer in Porous Media
  • Ionic liquids properties and applications
  • Ammonia Synthesis and Nitrogen Reduction
  • Subcritical and Supercritical Water Processes
  • Extraction and Separation Processes
  • Thermal and Kinetic Analysis
  • Carbon dioxide utilization in catalysis
  • Refrigeration and Air Conditioning Technologies

University of Groningen
2008-2024

Practical Action
2009-2015

University of Twente
2000-2012

Clarkson University
2007-2008

Institut Français
2007

University of Mumbai
2002

North-West University
2001

AkzoNobel (Netherlands)
1999-2001

DSM (Netherlands)
1999

Universidad de Zaragoza
1992

ADVERTISEMENT RETURN TO ISSUEPREVArticleNEXTSolubility and diffusivity of acid gases (carbon dioxide, nitrous oxide) in aqueous alkanolamine solutionsGeert F. Versteeg Wim P. M. Van SwaaijCite this: J. Chem. Eng. Data 1988, 33, 1, 29–34Publication Date (Print):January 1988Publication History Published online1 May 2002Published inissue 1 January 1988https://pubs.acs.org/doi/10.1021/je00051a011https://doi.org/10.1021/je00051a011research-articleACS PublicationsRequest reuse permissionsArticle...

10.1021/je00051a011 article EN Journal of Chemical & Engineering Data 1988-01-01

10.1016/s1750-5836(07)00032-1 article EN International journal of greenhouse gas control 2007-03-29

10.1016/s1750-5836(06)00007-7 article EN International journal of greenhouse gas control 2007-03-08

Alkanolamine solutions are frequently used as solvent for the removal of acid compounds from industrial gases (Kohl and Riesenfeld, 1979). Depending on process requirements, e.g., selective H2S, CO2-bulk removal, several options alkanolamine based treating solvents with varying compositions solution have been proposed. In this paper an overview is presented mechanisms that proposed in literature kinetic data various reactions critically evaluated. Conclusions applicability restrictions...

10.1080/00986449608936450 article EN Chemical Engineering Communications 1996-02-01

ADVERTISEMENT RETURN TO ISSUEPREVArticleDiffusion coefficients of several aqueous alkanolamine solutionsErwin D. Snijder, Marcel J. M. te Riele, Geert F. Versteeg, and W. P. van SwaaijCite this: Chem. Eng. Data 1993, 38, 3, 475–480Publication Date (Print):July 1, 1993Publication History Published online1 May 2002Published inissue 1 July 1993https://pubs.acs.org/doi/10.1021/je00011a037https://doi.org/10.1021/je00011a037research-articleACS PublicationsRequest reuse permissionsArticle...

10.1021/je00011a037 article EN Journal of Chemical & Engineering Data 1993-07-01

Abstract The kinetics of the reaction between CO 2 and aqueous potassium salts taurine glycine was measured at 295 K in a stirred‐cell reactor with flat gas–liquid interface. For taurate solutions, temperature effect on 285 305 K. Unlike primary alkanolamines, partial order amino acid salt changes from one low concentration to approximately 1.5 concentrations as high 3,000 mol·m −3 . At concentrations, apparent rate constant (k app ) for glycinate is comparable values literature. In absence...

10.1002/aic.690490118 article EN AIChE Journal 2003-01-01

Abstract The reaction of CO 2 with TEA, DMMEA, and DEMEA has been studied at 293, 303, 318 333 K. All the kinetic experiments were carried out in a stirred cell reactor operated flat, smooth horizontal gas‐liquid interface. A numerical method, which describes mass transfer accompanied by reversible chemical reactions, applied to infer rate constants from experimental data. It is argued that contribution OH − observed may have overstimated most literature on tertiary amine kinetics as serious...

10.1002/aic.690361103 article EN AIChE Journal 1990-11-01

10.1016/s1750-5836(07)00015-1 article EN International journal of greenhouse gas control 2007-03-08

The dissociation constants of protonated 2-amino-2-ethyl-1,3-propanediol, 2-amino-2-methyl-1-propanol, diethylmonoethanolamine, diisopropanolamine, dimethylmonoethanolamine, monoethanolamine, 1-amino-2-propanol, methylmonoethanolamine, triethanolamine, and the first second piperazine hydroxyethylpiperazine have been determined by electromotive force measurements from (293 to 353) K. triethylamine with same technique 333) experimental results derived values standard state thermodynamic...

10.1021/je800897v article EN Journal of Chemical & Engineering Data 2009-03-10

10.1016/j.cherd.2008.07.014 article EN Process Safety and Environmental Protection 2008-10-24
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