2006
DOI: 10.1016/j.seppur.2006.04.003
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Selective absorption of H2S from gas mixtures into aqueous solutions of blended amines of methyldiethanolamine and 2-tertiarybutylamino-2-ethoxyethanol in a packed column

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Cited by 122 publications
(63 citation statements)
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“…The best H 2 S removal efficiency by pH of 11-13 was reported by Jian G. Lua et al 30) and Brettschneider et al 31) .…”
Section: Discussionmentioning
confidence: 85%
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“…The best H 2 S removal efficiency by pH of 11-13 was reported by Jian G. Lua et al 30) and Brettschneider et al 31) .…”
Section: Discussionmentioning
confidence: 85%
“…Generally, the venturi has a low to moderate removal efficiency for H 2 S that mainly relates to its low solubility. The effectiveness of the packed scrubber for removal of H 2 S has been proven by several studies [28][29][30][31][32] . The alkali mixtures of NaOH and NaOcl as absorption liquid has good efficiency for H 2 S removal in a packed scrubber 4) .…”
Section: Discussionmentioning
confidence: 99%
“…Currently, these unwanted gases are removed by absorption into physical or chemical solvents, absorption onto activated carbon, cryogenic distillation, or separation with solid and liquid membranes [2,3]. Gas-liquid absorption methods that use aqueous solutions of alkanolamines are extensively used to remove CO 2 and H 2 S from gaseous streams in the natural-gas, oil-refining, petroleum and synthetic-ammonia industries [4]. Primary, secondary, and tertiary amines such as monoethanolamine (MEA), diethanolamine (DEA), and N-methyldiethanolamine (MDEA), respectively, are the alkanolamine solvents used.…”
Section: Introductionmentioning
confidence: 99%
“…Absorption of acid gas into aqueous solutions of alkanolamines has been one preferred approach of the purification technologies in current industry. Commercially, alkanolamines for the approach are monoethanolamine (MEA), diethanolamine (DEA), diisopropanolamine (DIPA), methyldiethanolamine (MDEA), and 2-amino-2-methyl-L-propanol (AMP) [1]. In the industrial gas processing, there is an increasing interest in gas absorption processes for the selective removal of H 2 S from gas streams with a high ratio of CO 2 to H 2 S. One motivation for this processing route is to increase the H 2 S partial pressure in the regenerator off-gas to sulfur recovery unit.…”
Section: Introductionmentioning
confidence: 99%