H2S absorption at high pressure using hollow fibre membrane contactors

被引:28
作者
Faiz, Rami [1 ,2 ]
Li, K. [1 ]
Al-Marzouqi, M. [2 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn & Chem Technol, London SW7 2AZ, England
[2] UAE Univ, Chem & Petr Engn Dept, Al Ain, U Arab Emirates
关键词
H2S absorption; Membrane contactors; Mathematical modelling; High pressure; Pseudo wetting; CO2; ABSORPTION; CARBON-DIOXIDE; NATURAL-GAS; REMOVAL; MIXTURE; SEPARATION; SOLVENTS; CAPTURE;
D O I
10.1016/j.cep.2014.06.012
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this article, the removal of H2S from natural gas at high pressure using hollow fibre membrane contactors and water as the absorbent solvent was described and validated by a 2D comprehensive mathematical model. The modelling predictions were in a good agreement with the experimental data at low pressure of 1 bar under non-wetting conditions. However, the experimental behaviour at high pressure in the range of 10-50 bar was always lower than the modelling predictions. And thus, a sensitivity analysis was carried out to study the influence of gas, liquid, membrane diffusion and solubility coefficients of H2S at high pressure upon the modelling behaviour compared with the experimental trend. The modelling results confirmed that these parameters were still insensitive as the model predictions changed slightly with altering these coefficients. Conversely, membrane wetting was confirmed to be an important factor even for small ratios, i.e. pseudo-wetting (1-3%). The model was able to predict the absorption of H2S at higher pressures under 3% pseudo-wetting. Although the type of membranes used in this study was highly hydrophobic (ePTFE) and thus membrane wetting was not expected, pseudo-wetting phenomenon was confirmed to be an important factor at high pressure. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:33 / 42
页数:10
相关论文
共 33 条
[1]   Separation of CO2 from CH4 by using gas-liquid membrane contacting process [J].
Atchariyawut, Supakorn ;
Jiraratananon, Ratana ;
Wang, Rong .
JOURNAL OF MEMBRANE SCIENCE, 2007, 304 (1-2) :163-172
[2]  
Chapman S., 1970, The mathematical theory of non-uniform gases
[3]   Comparing the absorption performance of packed columns and membrane contactors [J].
deMontigny, D ;
Tontiwachwuthikul, P ;
Chakma, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (15) :5726-5732
[4]   Using polypropylene and polytetrafluoroethylene membranes in a membrane contactor for CO2 absorption [J].
deMontigny, David ;
Tontiwachwuthikul, Paitoon ;
Chakma, Amit .
JOURNAL OF MEMBRANE SCIENCE, 2006, 277 (1-2) :99-107
[5]   Modelling of cross-flow membrane contactors: Mass transfer with chemical reactions [J].
Dindore, VY ;
Brilman, DWF ;
Versteeg, GE .
JOURNAL OF MEMBRANE SCIENCE, 2005, 255 (1-2) :275-289
[6]   Hollow fiber membrane contactor as a gas-liquid model contactor [J].
Dindore, VY ;
Brilman, DWF ;
Versteeg, GE .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (02) :467-479
[7]   CO2 absorption at elevated pressures using a hollow fiber membrane contactor [J].
Dindore, VY ;
Brilman, DWF ;
Feron, PHM ;
Versteeg, GF .
JOURNAL OF MEMBRANE SCIENCE, 2004, 235 (1-2) :99-109
[8]   Membrane-solvent selection for CO2 removal using membrane gas-liquid contactors [J].
Dindore, VY ;
Brilman, DWF ;
Geuzebroek, FH ;
Versteeg, GF .
SEPARATION AND PURIFICATION TECHNOLOGY, 2004, 40 (02) :133-145
[9]  
Duan Z., 1996, CHEM GEOL, V130
[10]   Separation of Olefin/Paraffin Gas Mixtures Using Ceramic Hollow Fiber Membrane Contactors [J].
Faiz, Rami ;
Fallanza, Marcos ;
Ortiz, Inmaculada ;
Li, K. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (23) :7918-7929