2014
DOI: 10.1016/j.egypro.2014.11.154
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Heat of Absorption of CO2 with Aqueous Solutions of MEA: New Experimental Data

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Cited by 61 publications
(36 citation statements)
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“…The same assumption has been used by several authors. 24,25,26 The amount of CO2 in the storage cylinder and the amount of unreacted CO2 in the gas phase in the reactor was calculated from the Peng Robinson equation of state. 27 Vapor-liquid equilibrium (VLE) results obtained in the apparatus at low CO2 pressures (<3 kPa) are considered inaccurate, since two almost equal numbers (with accuracy of 1.5 kPa) are subtracted from each other (total pressurepartial pressure of water and solvent).…”
Section: Heat Of Reaction ∆H Measurementsmentioning
confidence: 99%
“…The same assumption has been used by several authors. 24,25,26 The amount of CO2 in the storage cylinder and the amount of unreacted CO2 in the gas phase in the reactor was calculated from the Peng Robinson equation of state. 27 Vapor-liquid equilibrium (VLE) results obtained in the apparatus at low CO2 pressures (<3 kPa) are considered inaccurate, since two almost equal numbers (with accuracy of 1.5 kPa) are subtracted from each other (total pressurepartial pressure of water and solvent).…”
Section: Heat Of Reaction ∆H Measurementsmentioning
confidence: 99%
“…For primary amines, e.g. MEA, the heat of reaction is around 83-85 kJ/mol CO2 absorbed (Kim et al, 2014), equivalent of about 2 GJ/ton CO2 energy requirement in a post combustion CO2 capture process.…”
Section: Introductionmentioning
confidence: 99%
“…Differential with a small modification given in Kim et al 41 The experiments were initiated by evacuating the reactor to ~0.04 bar. Subsequently, around 1.1 -1.2L of amine solution was fed to the reactor, and the reactor was once again evacuated to degas the solution.…”
Section: Calorimetermentioning
confidence: 99%