Selective H2S removal by nonaqueous methyldiethanolamine solutions in an experimental apparatus

Industrial and Engineering Chemistry Research

Volumn 41, Issue 12, 2002, Pages 2953-2956

  Xu, Hong Jian ^a   Zhang, Cheng Fang ^a   Zheng, Zhi Sheng ^a  

^a EAST CHINA UNIVERSITY OF SCIENCE AND TECHNOLOGY   (China)

Author keywords

[No Author keywords available]

Indexed keywords

ABSORPTION; AMINES; COMPUTER SIMULATION; HEATING; HYDROGEN SULFIDE; REMOVAL;

OPERATING CONDITIONS;

CHEMICAL ENGINEERING;

DIETHYLENE GLYCOL; ETHANOLAMINE DERIVATIVE; ETHYLENE GLYCOL; HYDROGEN SULFIDE; METHYLDIETHANOLAMINE; PYRROLIDINE DERIVATIVE; UNCLASSIFIED DRUG;

CIRCULATION; FLUID FLOW; GAS-LIQUID SEPARATION; HYDROGEN SULFIDE; REMOVAL; WATER TREATMENT;

ABSORPTION; APPARATUS; ARTICLE; DESULFURIZATION; FLOW RATE; HEATING; SIMULATION; TEMPERATURE; WATER CONTENT;

EID: 0037066919     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie0109253     Document Type: Article

References (11)

1. 2S selectively
2. 2S
3. Gas plant converts amine unit to MDEA-based solvent
4. 2 selectivity
5. Reactions of carbon dioxide and hydrogen sulfide with some alkanolamines
6. Sweetening of sour natural gases by mixed-solvent absorption: Solubility of ethane, carbon dioxide, and hydrogen sulfide in mixtures of physical and chemical solvents
7. 2S removal
8. 2 removal and optimum concentration of MDEA aqueous solution
9. Methyldiethanolamine degradation - Mechanism and kinetics
10. 2 into aqueous solutions of methyldiethanolamine
11. Densities and viscosities for binary mixtures of N-meth-yldiethanolamine + triethylene glycol monomethyl ether from 25°C to 70°C and N-methyldiethanolamine + ethanol mixtures at 40°C