eprintid: 6029
rev_number: 2
eprint_status: archive
userid: 1
dir: disk0/00/00/60/29
datestamp: 2023-11-09 16:17:46
lastmod: 2023-11-09 16:17:46
status_changed: 2023-11-09 16:04:37
type: article
metadata_visibility: show
creators_name: Abdul Halim, H.N.
creators_name: Shariff, A.M.
creators_name: Tan, L.S.
creators_name: Bustam, M.A.
title: Mass transfer performance of CO2 absorption from natural gas using monoethanolamine (MEA) in high pressure operations
ispublished: pub
keywords: Atmospheric pressure; Carbon dioxide; Ethanolamines; Flow of gases; Flow rate; Gases; Liquids; Mass transfer; Natural gas, Absorption columns; Absorption experiments; Absorption performance; High pressure operations; High-pressure condition; Liquid temperature; Mass transfer performance; Operating pressure, Gas absorption
note: cited By 27
abstract: Most carbon dioxide (CO2) absorption studies that use amine based solvents for fl ue gas treatments were conducted at atmospheric pressure. This study reports the absorption performance of monoethanolamine (MEA) for the removal of CO2 from natural gas (NG) at high pressure conditions. The absorption experiments were conducted in an absorption column packed with Sulzer metal gauze packing at 5.0 MPa operating pressure. The effects of gas flow rate (18.89-35.08 kmol/m2·h), liquid flow rate (1.81-4.51 m3/m2·h), MEA concentration (1.0-4.0 kmol/m3), and liquid temperature (27-45°C) on the mass transfer performance were evaluated in terms of CO2 removal () and overall volumetric mass transfer coeffi cient (KGav). From this study, the KGav was found to increase with increasing liquid flow rate and MEA concentration. However, the mass transfer performance was not a ffected by the total gas flow rate. The optimum condition for liquid temperature was found to be at 40°C. © 2015 American Chemical Society.
date: 2015
publisher: American Chemical Society
official_url: https://www.scopus.com/inward/record.uri?eid=2-s2.0-84922986432&doi=10.1021%2fie504024m&partnerID=40&md5=cb6ff7fd6becdd04a77d4a32583d7a27
id_number: 10.1021/ie504024m
full_text_status: none
publication: Industrial and Engineering Chemistry Research
volume: 54
number: 5
pagerange: 1675-1680
refereed: TRUE
issn: 08885885
citation:   Abdul Halim, H.N. and Shariff, A.M. and Tan, L.S. and Bustam, M.A.  (2015) Mass transfer performance of CO2 absorption from natural gas using monoethanolamine (MEA) in high pressure operations.  Industrial and Engineering Chemistry Research, 54 (5).  pp. 1675-1680.  ISSN 08885885