Highly stable bilayer MFI zeolite membranes for high temperature hydrogen separation

Journal of Membrane Science

Volumn 450, Issue , 2014, Pages 425-432

  Wang, Haibing ^a   Dong, Xueliang ^a   Lin, Y S ^a  

^a Arizona State University   (United States)

Author keywords

Hydrogen separation; Long term stability; Microporous membranes; Stability; Water gas shift; Zeolite

Indexed keywords

HYDROGEN SEPARATION; INDUSTRIAL PROCESSS; INORGANIC MEMBRANES; LONG TERM STABILITY; MFI ZEOLITE MEMBRANES; MICRO POROUS MEMBRANES; THERMAL AND CHEMICAL STABILITIES; WATER GAS SHIFT (WGS) REACTION;

ALUMINA; BIOREACTORS; CARBON DIOXIDE; CATALYST SELECTIVITY; CATALYTIC CRACKING; CHEMICAL SHIFT; CONVERGENCE OF NUMERICAL METHODS; FISCHER-TROPSCH SYNTHESIS; HYDROGEN; HYDROGEN PRODUCTION; SEPARATION; VAPORS; WATER GAS SHIFT; ZEOLITES;

MEMBRANES;

ALUMINUM OXIDE; CARBON DIOXIDE; CARBON MONOXIDE; HYDROGEN; ZEOLITE; ZIRCONIUM OXIDE;

ARTICLE; BILAYER MEMBRANE; HIGH TEMPERATURE; MEMBRANE PERMEABILITY; MEMBRANE REACTOR; MEMBRANE STRUCTURE; PRIORITY JOURNAL;

EID: 84885907726     PISSN: 03767388     EISSN: 18733123     Source Type: Journal    
DOI: 10.1016/j.memsci.2013.08.030     Document Type: Article

References (43)

1. Lu G.Q., da Costa J.C.D., Duke M., Giessler S., Socolow R., Williams R.H., Kreutz T. Inorganic membranes for hydrogen production and purification: a critical review and perspective. J. Colloid Interface Sci. 2007, 314:589-603.
2. Tosti S., Basile A., Chiappetta G., Rizzello C., Violante V. Pd-Ag membrane reactors for water gas shift reaction. Chem. Eng. J. 2003, 93:23-30.
3. 2 catalyst. Int. J. Hydrogen Energy 2009, 34:2965-2971.
4. Basile A., Criscuoli A., Santella F., Drioli E. Membrane reactor for water gas shift reaction. Gas Sep. Purif. 1996, 10:243-254.
5. Augustine A.S., Ma Y.H., Kazantzis N.K. High pressure palladium membrane reactor for the high temperature water-gas shift reaction. Int. J. Hydrogen Energy 2011, 36:5350-5360.
6. Giessler S., Jordan L., da Costa J.C.D., Lu G.Q. Performance of hydrophobic and hydrophilic silica membrane reactors for the water gas shift reaction. Sep. Purif. Technol. 2003, 32:255-264.
7. Battersby S., Smart S., Ladewig B., Liu S., Duke M.C., Rudolph V., da Costa J.C.D. Hydrothermal stability of cobalt silica membranes in a water gas shift membrane reactor. Sep. Purif. Technol. 2009, 66:299-305.
8. 4 and water gas shift reaction. Appl. Catal. A: Gen. 2000, 196:65-72.
9. 3-δ under water gas shift reaction conditions. J. Electrochem. Soc. 2010, 157:B383-B387.
10. Tang Z., Kim S.J., Reddy G.K., Dong J., Smirniotis P. Modified zeolite membrane reactor for high temperature water gas shift reaction. J. Membr. Sci. 2010, 354:114-122.
11. Kim S.J., Xu Z., Reddy G.K., Smirniotis P., Dong J. Effect of pressure on high-temperature water gas shift reaction in microporous zeolite membrane reactor. Ind. Eng. Chem. Res. 2012, 51:1364-1375.
12. 2S on the performance of Pd and Pd/Cu composite membrane. J. Membr. Sci. 2010, 362:535-544.
13. 2S. J. Membr. Sci. 2005, 254:49-62.
14. Gade S.K., DeVoss S.J., Coulter K.E., Paglieri S.N., Alptekin G.O., Way J.D. Palladium-gold alloy membranes in mixed gas streams with hydrogen sulfide: effect of alloy content and fabrication technique. J. Membr. Sci. 2011, 378:35-41.
15. 2S at 350°C. J. Membr. Sci. 2010, 349:380-384.
16. Catalano J., Baschetti M.G., Sarti G.C. Influence of water vapor on hydrogen permeation through 2.5μm Pd-Ag membranes. Int. J. Hydrogen Energy 2011, 36:8658-8673.
17. Gao H., Lin Y.S., Li Y., Zhang B. Chemical stability and its improvement of palladium-based metallic membranes. Ind. Eng. Chem. Res. 2004, 43:6920-6930.
18. Flanagan T.B., Wang D., Shanahan K. The effect of CO on hydrogen permeation through Pd and through internally oxidized and un-oxidized Pd alloy membranes. Sep. Purif. Technol. 2011, 79:385-392.
19. Arstad B., Venvik H., Klette H., Walmsley J.C., Tucho W.M., Holmestad R., Holmen A., Bredesen R. Studies of self-supported 1.6μm Pd/23wt% Ag membranes during and after hydrogen production in a catalytic membrane reactor. Catal. Today 2006, 118:63-72.
20. Qi X., Lin Y.S. Electrical conduction and hydrogen permeation through mixed proton-electron conducting strontium cerate membranes. Solid State Ionics 2000, 130:149-156.
21. Cheng S., Gupta V.K., Lin Y.S. Synthesis and hydrogen permeation properties of thin proton-conducting ceramic membranes. Solid State Ionics 2005, 176:2653-2662.
22. Kniep J., Lin Y.S. Oxygen- and Hydrogen-Permeable Dense Ceramic Membranes, in Solid State Electrochemistry. I: Fundamentals, Materials and Their Applications 2011, 467-500. Springer, (Chapter 10). V.V. Kharton (Ed.).
23. Lin Y.S., Kumakiri I., Nair B.N., Alsyouri H. Microporous inorganic membranes. Sep. Purif. Methods 2002, 32:229-379.
24. Gu Y., Hacarlioglu P., Oyama S.T. Hydrothermally stable silica-alumina composite membranes for hydrogen separation. J. Membr. Sci. 2008, 310:28-37.
25. Gu Y., Oyama S.T. Permeation properties and hydrothermal stability of silica-titania membranes supported on porous alumina substrates. J. Membr. Sci. 2009, 345:267-275.
26. Nomura M., Ono K., Gopalakrishinan S., Sugawara T., Nakao S.I. Preparation of a stable silica membrane by a counter diffusion chemical vapor deposition method. J. Membr. Sci. 2005, 251:151-158.
27. Boffa V., Blank D.H.A., ten Elshof J.E. Hydrothermally stability of microporous silica and niobia-silica membranes. J. Membr. Sci. 2008, 319:256-263.
28. Akamatsu K., Nakane M., Sugawara T., Nakao S.I. Performance under thermal and hydrothermal condition of amorphous silica membrane prepared by chemical vapor deposition. AIChE J. 2009, 55:2197-2200.
29. Battersby S., Tasaki T., Smart S., Ladewig B., Liu S., Duke M., Rudolph V., da Costa J.C.D. Performance of cobalt silica membranes in gas mixture separation. J. Membr. Sci. 2009, 329:91-98.
30. Tsuru T., Igi R., Kanezashi M., Yoshioka T. Permeation properties of hydrogen and water vapor through porous silica membrane at high temperatures. AIChE J. 2011, 57:618-629.
31. Verweij H., Lin Y.S., Dong J. Microporous silica and zeolite membranes for hydrogen purification. MRS Bull. 2006, 31:756-764.
32. Dong J., Lin Y.S., Kanezashi M., Tang Z. Microporous inorganic membranes for high temperature hydrogen purification. J. Appl. Phys. 2008, 104:121301-121317.
33. Kanezashi M., Yada K., Yomohisa T., Tsuru T. Organic-inorganic hybrid silica membranes with controlled silica network size: preparation and gas permeation characteristics. J. Membr. Sci. 2010, 348:310-318.
34. Sea B.K., Watanabe M., Kusakabe K., Morooka S., Kim S.S. Formation of hydrogen permselective silica membrane for elevated temperature hydrogen recovery from a mixture containing steam. Gas Sep. Purif. 1996, 10:187-195.
35. Wang H., Lin Y.S. Synthesis and modification of ZSM-5/silicalite bilayer membrane with improved hydrogen separation performance. J. Membr. Sci. 2012, 396:128-137.
36. Khan A., Chen P., Boolchand P., Smirniotis P.G. Modified nano-crystalline ferrite for high temperature WGS membrane reactor applications. J. Catal. 2008, 253:91-104.
37. Kanezashi M., Lin Y.S. Gas permeation and diffusion characteristics of MFI-type zeolite membranes at high temperatures. J. Phys. Chem. C 2009, 113:3767-3774.
38. van de Graaf J.M., Kapteijn F., Moulijn J.A. Permeation of weakly adsorbing components through a silicalite-1 membrane. Chem. Eng. Sci. 1999, 54:1081-1092.
39. 4 permeation through MFI zeolite membranes. J. Membr. Sci. 1999, 160:115-125.
40. Algieri C., Bernardo P., Golemme G., Barbieri G., Drioli E. Permeation properties of a thin silicalite-1 (MFI) membrane. J. Membr. Sci. 2003, 222:181-190.
41. Wang H., Lin Y.S. Effects of water vapor on gas permeation and separation properties of MFI zeolite membranes at high temperature. AIChE J. 2012, 58:153-162.
42. Deng S.G., Lin Y.S. Sulfur dioxide sorption properties and thermal stability of hydrophobic zeolites. Ind. Eng. Chem. Res. 1995, 34:4063-4070.
43. Kanezashi M., O'Brien J., Lin Y.S. Thermal stability improvement of MFI-type zeolite membranes: effect of YSZ intermediate layer. Microporous Mesoporous Mater. 2007, 103:302-308.