2014
DOI: 10.1016/j.ijggc.2014.04.019
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Assessment of mass transfer correlations in rate-based modeling of a large-scale CO2 capture with MEA

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Cited by 30 publications
(14 citation statements)
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“…A review on several mass transfer correlations in packed columns has been performed in the literature. 15, 16 Razi, et al 17 have assessed these correlations in a rate-based model for CO 2 capture with a monoethanolamine (MEA) solution to show the uncertainty associated with using correlations in large-scale CO 2 capture plants. They concluded that the interactions among the transport parameters, mass transfer coefficients, effective interfacial areas and kinetics are too complex for the mass transfer correlations to be applied with a sufficient level of condence.…”
Section: Masoud Mofarahi Is a Fullmentioning
confidence: 99%
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“…A review on several mass transfer correlations in packed columns has been performed in the literature. 15, 16 Razi, et al 17 have assessed these correlations in a rate-based model for CO 2 capture with a monoethanolamine (MEA) solution to show the uncertainty associated with using correlations in large-scale CO 2 capture plants. They concluded that the interactions among the transport parameters, mass transfer coefficients, effective interfacial areas and kinetics are too complex for the mass transfer correlations to be applied with a sufficient level of condence.…”
Section: Masoud Mofarahi Is a Fullmentioning
confidence: 99%
“…They concluded that the interactions among the transport parameters, mass transfer coefficients, effective interfacial areas and kinetics are too complex for the mass transfer correlations to be applied with a sufficient level of condence. 17 So far, none of these reviews has provided a review of mass transfer performance in terms of the K GCO 2 a V parameter for CO 2 absorption into amine solutions in packed columns. In existing studies related to the K GCO 2 a V for CO 2 absorption at a laboratory scale, packed columns have been experimentally investigated for a large number of amine-based solvents across a range of operating parameters.…”
Section: Masoud Mofarahi Is a Fullmentioning
confidence: 99%
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“…Sensitivity analyses of several process variables on CO2 absorption have been performed recently (Kvamsdal and Hillestad, 2012;Ralph H. Weiland and Nathan A. Hatcher, 2011;Kale et al, 2013;Razi et al, 2013aRazi et al, , 2014. Neveux et al (Neveux et al, 2013) studied the contribution of water flux to the total heat transfer flux to the liquid in both absorber and stripper.…”
Section: Introductionmentioning
confidence: 99%
“…In the scale-up design for the absorber, correlations such as mass transfer and interfacial area should be carefully selected and validated against the pilot plant data. The simulation results using different correlations were found to differ widely (Razi et al, 2014). Since the CO2 stripper is operating at a high temperature, the predictions on CO2 recovery of rate-based and equilibrium-based models were found to be similar (Tobiesen et al, 2008;Plaza et al, 2010).…”
Section: Steady-state Modeling and Simulationsmentioning
confidence: 95%