Research Article
Mass Transfer Flux of CO2 into Methyldiethanolamine Solution in a Reactive-Absorption Process
Ahad Ghaemi,
Amir Hossein Behroozi,
Hossein Mashhadimoslem,
Corresponding Author
Ahad Ghaemi
Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran
Correspondence: Ahad Ghaemi ([email protected]), Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran.Search for more papers by this authorAmir Hossein Behroozi
Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran
Search for more papers by this authorHossein Mashhadimoslem
Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran
Search for more papers by this authorAhad Ghaemi,
Amir Hossein Behroozi,
Hossein Mashhadimoslem,
Corresponding Author
Ahad Ghaemi
Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran
Correspondence: Ahad Ghaemi ([email protected]), Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran.Search for more papers by this authorAmir Hossein Behroozi
Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran
Search for more papers by this authorHossein Mashhadimoslem
Iran University of Science and Technology, School of Chemical, Gas and Petroleum Engineering, Narmak, 16846 Tehran, Iran
Search for more papers by this authorAbstract
The mass transfer parameters of both gas and liquid phases affect the mass transfer flux of CO2 in absorption processes. In this study, an accurate correlation is proposed to calculate the CO2 mass transfer flux in an absorption-reactive process by methyldiethanolamine (MDEA) solution using the Buckingham π theorem. The various parameters include film parameter, CO2 loading, concentration ratio, partial-to-total pressure ratio, film thickness ratio, and diffusion ratio which are incorporated in the model. An average absolute relative error of 4.4 % for the calculation of mass transfer flux was stated.
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