The chemical enhancement factors have been measured in a controlled environment for absorption and desorption mass transfer processes in aqueous 2.0 M MDEA solutions at temperatures of 298.15, 313.15, and 333.15 K and the loading of CO2 ranging from 0 to 0.8 in a batch-operated stirred tank reactor. At identical operating conditions, the chemical enhancement factor for absorption and desorption appears to be the same within the reported experimental uncertainty.In a continuous effort to describe the fundamentals of gas-liquid desorption processes [E.S. Hamborg, S.R.A. Kersten, G.F. Versteeg, Absorption and desorption mass transfer rates in non-reactive systems, Chem. Eng. J. 161(2010)191-195], it has been shown in the current work that a re...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
The mass transfer rates during CO2 absorption and desorption from N-methyl-2-pyrrolidone solutions w...
The chemical enhancement factors have been measured in a controlled environment for absorption and d...
The chemical enhancement factors have been measured in a controlled environment for absorption and d...
The forward and reverse kinetic rate parameters have been determined for CO2 absorption and desorpti...
The forward and reverse kinetic rate parameters have been determined for CO2 absorption and desorpti...
Liquid phase mass transfer coefficients have been measured in a controlled environment during gas ab...
In many chemical industrial processes, mass transfer across gas-liquid interfaces accompanied by che...
An absorption model has been developed which can be used to calculate rapidly absorption rates for t...
An absorption model has been developed which can be used to calculate rapidly absorption rates for t...
An absorption model has been developed which can be used to calculate rapidly absorption rates for t...
Abstract-An absorption model has been developed which can be used to calculate rapidly absorption ra...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
The mass transfer rates during CO2 absorption and desorption from N-methyl-2-pyrrolidone solutions w...
The chemical enhancement factors have been measured in a controlled environment for absorption and d...
The chemical enhancement factors have been measured in a controlled environment for absorption and d...
The forward and reverse kinetic rate parameters have been determined for CO2 absorption and desorpti...
The forward and reverse kinetic rate parameters have been determined for CO2 absorption and desorpti...
Liquid phase mass transfer coefficients have been measured in a controlled environment during gas ab...
In many chemical industrial processes, mass transfer across gas-liquid interfaces accompanied by che...
An absorption model has been developed which can be used to calculate rapidly absorption rates for t...
An absorption model has been developed which can be used to calculate rapidly absorption rates for t...
An absorption model has been developed which can be used to calculate rapidly absorption rates for t...
Abstract-An absorption model has been developed which can be used to calculate rapidly absorption ra...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
An absorption model to study gas–liquid mass transfer accompanied by reversible two-step reactions i...
The mass transfer rates during CO2 absorption and desorption from N-methyl-2-pyrrolidone solutions w...