Frontiers of Chemical Science and Engineering >
Pressure swing adsorption/membrane hybrid processes for hydrogen purification with a high recovery
Received date: 08 Dec 2015
Accepted date: 18 Jan 2016
Published date: 19 May 2016
Copyright
Hydrogen was recovered and purified from coal gasification-produced syngas using two kinds of hybrid processes: a pressure swing adsorption (PSA)-membrane system (a PSA unit followed by a membrane separation unit) and a membrane-PSA system (a membrane separation unit followed by a PSA unit). The PSA operational parameters were adjusted to control the product purity and the membrane operational parameters were adjusted to control the hydrogen recovery so that both a pure hydrogen product (>99.9%) and a high recovery (>90%) were obtained simultaneously. The hybrid hydrogen purification processes were simulated using HYSYS and the processes were evaluated in terms of hydrogen product purity and hydrogen recovery. For comparison, a PSA process and a membrane separation process were also used individually for hydrogen purification. Neither process alone produced high purity hydrogen with a high recovery. The PSA-membrane hybrid process produced hydrogen that was 99.98% pure with a recovery of 91.71%, whereas the membrane-PSA hybrid process produced hydrogen that was 99.99% pure with a recovery of 91.71%. The PSA-membrane hybrid process achieved higher total H2 recoveries than the membrane-PSA hybrid process under the same H2 recovery of membrane separation unit. Meanwhile, the membrane-PSA hybrid process achieved a higher total H2 recovery (97.06%) than PSA-membrane hybrid process (94.35%) at the same H2 concentration of PSA feed gas (62.57%).
Key words: hydrogen purification; PSA; membrane separation; hybrid process
Baojun Li , Gaohong He , Xiaobin Jiang , Yan Dai , Xuehua Ruan . Pressure swing adsorption/membrane hybrid processes for hydrogen purification with a high recovery[J]. Frontiers of Chemical Science and Engineering, 2016 , 10(2) : 255 -264 . DOI: 10.1007/s11705-016-1567-1
1 |
Towler G P, Mann R, Serriere A J, Gabaude C M. Refinery hydrogen management: Cost analysis of chemically-integrated facilities. Industrial & Engineering Chemistry Research, 1996, 35(7): 2378–2388
|
2 |
Alves J J, Towler G P. Analysis of refinery hydrogen distribution systems. Industrial & Engineering Chemistry Research, 2002, 41(23): 5759–5769
|
3 |
Liao Z, Wang J, Yang Y, Rong G. Integrating purifiers in refinery hydrogen networks: A retrofit case study. Journal of Cleaner Production, 2010, 18(3): 233–241
|
4 |
Qu G. Study on cost leadership strategy of hydrogen utilization in petroleum refining plants. Techno-Economics in Petrochemicals, 2007, 23(2): 19–22 (in Chinese)
|
5 |
Chen Y, Li P. Analysis of hydrocarcker’s operations in sinopec. Petroleum Refinery Engineering, 2007, 30(10): 1–4 (in Chinese)
|
6 |
LeValley T L, Richard A R, Fan M. The progress in water gas shift and steam reforming hydrogen production technologies—A review. International Journal of Hydrogen Energy, 2014, 39(30): 16983–17000
|
7 |
Liu B, Wang X L, Tang X L, Yang L Y, Sun C Y, Chen G J. Recovery of hydrogen from ammonia plant tail gas by absorption-hydration hybrid method. Chinese Journal of Chemical Engineering, 2011, 19(5): 784–791
|
8 |
Majlan E H, Daud W R W, Iyuke S E, Mohamad A B, Kadhum A A H, Mohammad A W, Takriff M S, Bahaman N. Hydrogen purification using compact pressure swing adsorption system for fuel cell. International Journal of Hydrogen Energy, 2009, 34(6): 2771–2777
|
9 |
Huang Q, Malekian A, Eić M. Optimization of PSA process for producing enriched hydrogen from plasma reactor gas. Separation and Purification Technology, 2008, 62(1): 22–31
|
10 |
Zhang D, Kodama A, Goto M, Hirose T. Recovery of trace hydrogen by cryogenic adsorption. Separation and Purification Technology, 2004, 35(2): 105–112
|
11 |
Huang L, Li G. The application on the actuality and development of pressure swing adsorption. Guangdong Chemical Industry, 2011, 38(215): 14–15 (in Chinese)
|
12 |
Gallucci F, Fernandez E, Corengia P, van Sint Annaland M. Recent advances on membranes and membrane reactors for hydrogen production. Chemical Engineering Science, 2013, 92: 40–66
|
13 |
Bernardo P, Drioli E, Golemme G. Membrane gas separation: A review/state of the art. Industrial & Engineering Chemistry Research, 2009, 48(10): 4638–4663
|
14 |
Chen W H, Lin C H, Lin Y L. Flow-field design for improving hydrogen recovery in a palladium membrane tube. Journal of Membrane Science, 2014, 472: 45–54
|
15 |
Favvas E P, Heliopoulos N S, Papageorgiou S K, Mitropoulos A C, Kapantaidakis G C, Kanellopoulos N K. Helium and hydrogen selective carbon hollow fiber membranes: The effect of pyrolysis isothermal time. Separation and Purification Technology, 2015, 142: 176–181
|
16 |
Sircar S, Waldron W E, Rao M B, Anand M. Hydrogen production by hybrid SMR-PSA-SSF membrane system. Separation and Purification Technology, 1999, 17(1): 11–20
|
17 |
Sircar S, Golden T C. Purification of hydrogen by pressure swing adsorption. Separation Science and Technology, 2000, 35(5): 667–687
|
18 |
Feng X, Pan C Y, Ivory J, Ghosh D. Integrated membrane/adsorption process for gas separation. Chemical Engineering Science, 1998, 53(9): 1689–1698
|
19 |
Esteves I A A C, Mota J P B. Simulation of a new hybrid membrane/pressure swing adsorption process for gas separation. Desalination, 2002, 148(1): 275–280
|
20 |
Esteves I A A C, Mota J P B. Gas separation by a novel hybrid membrane/pressure swing adsorption process. Industrial & Engineering Chemistry Research, 2007, 46(17): 5723–5733
|
21 |
Nikolić D D, Kikkinides E S. Modelling and optimization of hybrid PSA/membrane separation processes. Adsorption, 2015, 21(4): 283–305
|
23 |
Akinlabi C O, Gerogiorgis D I, Georgiadis M C, Pistikopoulos E N. Modelling, design and optimisation of a hybrid PSA-membrane gas separation process. Computer Aided Chemical Engineering, 2007, 24: 363–370
|
24 |
Naheiri T, Ludwig K A, Anand M, Rao M B, Sircar S. Scale-up of selective surface flow membrane for gas separation. Separation Science and Technology, 1997, 32(9): 1589–1602
|
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