Synthesis and Performance of Deca- Dodecasil 3 Rhombohedral (DDR)-Type Zeolite Membrane In CO2 Separation– A Review
Keywords:
Carbon dioxide separation, Natural gas, DDR membrane, Synthesis
Abstract
CO2 capture technologies including absorption, adsorption, and cryogenic distillation are reported. Conventional technologies for CO2 separation from natural gas have several disadvantages including high cost, high maintenance, occupy more space and consume high energy. Thus, membrane technology is introduced to separate CO2 due to their several advantages over conventional separation techniques. Inorganic membranes exhibit high thermal stability, chemical stability, permeability and selectivity for CO2 and CH4 separation as compared to other type of membranes. Zeolite membranes are potential for CO2 separation due to their characteristics such as, well define the pore structure and molecular sieving property. Among the zeolite membranes, DDR membranes exhibit highest selectivity for CO2 and CH4 separation. DDR membranes are synthesized by conventional hydrothermal and secondary growth methods. These methods required very long synthesis duration (25 days) due to extremely low nucleation and crystal growth rate of DDR zeolite. In this review, synthesis and performance of DDR membrane in CO2 separation from CH4 reported by various researchers are discussed. Challenges and upcoming guidelines related to the synthesis DDR membrane and performance of DDR membrane also included.References
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24. Gucuyener, C., Van dan Bergh, J., Joaristi, A.M., Magusin, P.C.M.M. Hensen, E.J.M., Gascon, J., and Kapteijn, F. (2011) Facile synthesis of the DD3R zeolite: performance in the adsorptive separation of buta-1,3-diene and but- 2-ene isomers. J. Mater. Chem, 21, 18386.
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27. Tomita, T., Nakayama, K., and Sakai, H. (2004) Gas separation characteristics of DDR type zeolite membrane. Microporous Mesoporous Mater, 68, 71.
28. Kuhn, J., Yajima, K., Tomita, T., Gross, J., and Kapteijn, F., (2008) Dehydration performance of a hydrophobic DD3R zeolite membrane. J. Membr. Sci,321,344.
29. Nakayama, K., Suzuki, K., Yoshida, M., Yajima, K., and Tomita, T. (2005) Method for preparing DDR type zeolite membrane, DDR type zeolite membrane, and composite DDR type zeolite membrane, and method for preparation thereof: US. Pat.20050229779 A1.
30. Bose, A., Sen, M., Pal, P., Das, J.K., and Das, N., (2014) Sonication mediated hydrothermal process – an efficient method for the rapid synthesis of DDR zeolite membranes. RSC Adv., 4, 19043.
31. Qi-Liang, Y., Sheng-Lai, Z., and Xiao, L., (2009) Synthesis of DDR-Type zeolite in fluoride medium. Chin. J. Inorg. Chem., 2, 002.
32. Uchikawa, T., Yajima, K., Nonaka, H., and Tomita, T., (2010) Method for production of DDR type zeolite membrane: US. Pat.2010/0144512 A1.
2. Scholes,C.A., Stevens,G.W., and Kentish, S. E., (2012) Membrane gas separation applications in natural gas processing. Fuel, 96, 15.
3. Zhang,Y., Sunarso,J., Liu,S., and Wang,R., (2013) Current status and development of membranes for CO2/CH4 separation - A review. Int J greenh gas con,12,84.
4. Yeo,Z.Y., Chew,T.L., Zhu,P.W., Mohamed,A.R., and Chai,S.P., (2012) Conventional processes and membrane technology for carbon dioxide removal from natural gas: A review. J. Nat. Gas Chem, 2, 282.
5. Olajire,A.A., (2010) CO2 capture and separation technologies for end-of- pipe applications – A review. Energ, 35, 2610.
6. Dortmundt, D., and Doshi, K., (1999) Recent developments in CO2 removal membrane technology. UOP LLC, Des Plaines, Illinois USA.
7. Pandey,P., and Chauhan,R.S., (2001) Membranes for gas separation. Prog. Polym. Sci, 26, 853.
8. Tavolaro, A., and Drioli, E., (1999) Zeolite Membranes. Adv. Mater. 11(12),975.
9. Ahmad, A.L., Jawad, Z.A., Low, S.C., and Zein, S.H.S. (2012). Prospect of mixed matrix membrane towards CO2 separation. J.Memb Sci Technol.,2,3.
10. Nasir, R., Mukhtar, H., Man, Z., and Mohshim, D.F. (2013) Material advancements in fabrication of mixed- matrix membranes. Chem. Eng. Technol., 36, 717.
11. Himeno, S., Tomita, T., Suzuki, K., Nakayama, K., Yajima K., and Yoshida, S., (2007) Synthesis and permeation properties of a DDR-Type zeolite membrane for separation of CO2/CH4 gaseous mixtures. Ind. Eng. Chem. Res, 46, 6989.
12. Caro, J., Noack, M., Kolsch, P., and Schafer,R., (2000) Review-Zeolite membranes state of their development and perspective. Microporous Mesoporous Mater.38,3.
13. Zhu, W., Hrabanek, P., Gora, L., Kapteijn, F.,and Moulijn, J.A., (2006) Role of adsorption in the permeation of CH4 and CO2 through a silicalite-1 membrane. Ind. Eng. Chem. Res. 45, 767.
14. Banihashemi, F., Pakizeh, M., and Ahmadpour,A., (2011) CO2 separation using PDMS/ZSM-5 zeolite composite membrane Sep Purif Technol 79 (3), 293.
15. Hasegawa,Y., Tanaka,T., Watanabe, K., Jeong,B-H., Kusakab, K., and Morooka, S., (2002) Separation of CO2-CH4 and CO2-N2 System using ion-exchanged FAU-type zeolite membranes with different Si/Al ratios. Korean Jr. Chem. Eng, 19, 309.
16. Kusakabe, K., Kuroda, T., Murata, A., and Morooka, S. (1997) Formation of a Y-type zeolite membrane on a porous α-alumina tube for gas separation. Ind. Eng. Chem. Res, 36,649.
17. Cui,Y., Kita, H., and Okamoto, K-I., (2004) Zeolite T membrane: preparation, characterization, pervaporation of water/organic liquid mixtures and acid stability. J. Membr. Sci, 236, 17.
18. Mirfendereski, M., Sadrzadeh, M., and Mohammadi, M., (2008) Effect of synthesis parameters on single gas permeation through T-type zeolite membranes. Int. J. Greenh Gas Con, 2, 531.
19. Venna, S.R., and Carreon, M.A., (2011) Amino-functionalized SAPO-34 membranes for CO2/CH4 and CO2/N2 separation. Langmuir, 27,2888.
20. Shekhawat, D., Luebke, D.R., and Pennline, H.W., (2003) A review of carbon dioxide selective membranes. US department of energy.
21. Chew, T.L., Ahmad, A.L., and Bhatia, S., (2011) Ba-SAPO-34 membrane synthesized from microwave heating and its performance for CO2/CH4 gas separation. Chem. Eng. J, 171, 1053.
22. van den Bergh, J., Zhu, W., Kapteijn, F., Moulijn, J.A., Yajima, K., Nakayama, K., Tomita, T., and Yoshida, S. (2006) Separation of CO2 and CH4 by a DDR membrane. Res. Chem. Intermed., 34,467.
23. Potapova, E., (2007) Synthesis and Characterization of DDR Type zeolite; Department of chemical engineering and geoscience: Lulea University of Technology, Lulea, Sweden.
24. Gucuyener, C., Van dan Bergh, J., Joaristi, A.M., Magusin, P.C.M.M. Hensen, E.J.M., Gascon, J., and Kapteijn, F. (2011) Facile synthesis of the DD3R zeolite: performance in the adsorptive separation of buta-1,3-diene and but- 2-ene isomers. J. Mater. Chem, 21, 18386.
25. Provenzano, J., (2011) A Study on the Hydrothermal Synthesis of the Zeolite DDR; Department of chemical engineering: University of Cincinnati. Cincinnati, United States
26. Momma, K., (2014) Clathrate compounds of silica, J. Phys. Condens. Matter 26,103203
27. Tomita, T., Nakayama, K., and Sakai, H. (2004) Gas separation characteristics of DDR type zeolite membrane. Microporous Mesoporous Mater, 68, 71.
28. Kuhn, J., Yajima, K., Tomita, T., Gross, J., and Kapteijn, F., (2008) Dehydration performance of a hydrophobic DD3R zeolite membrane. J. Membr. Sci,321,344.
29. Nakayama, K., Suzuki, K., Yoshida, M., Yajima, K., and Tomita, T. (2005) Method for preparing DDR type zeolite membrane, DDR type zeolite membrane, and composite DDR type zeolite membrane, and method for preparation thereof: US. Pat.20050229779 A1.
30. Bose, A., Sen, M., Pal, P., Das, J.K., and Das, N., (2014) Sonication mediated hydrothermal process – an efficient method for the rapid synthesis of DDR zeolite membranes. RSC Adv., 4, 19043.
31. Qi-Liang, Y., Sheng-Lai, Z., and Xiao, L., (2009) Synthesis of DDR-Type zeolite in fluoride medium. Chin. J. Inorg. Chem., 2, 002.
32. Uchikawa, T., Yajima, K., Nonaka, H., and Tomita, T., (2010) Method for production of DDR type zeolite membrane: US. Pat.2010/0144512 A1.
Published
2014-06-30
How to Cite
Mubashir, M., Fong, Y. Y., Keong, L. K., & Bin Sharrif, M. A. (2014). Synthesis and Performance of Deca- Dodecasil 3 Rhombohedral (DDR)-Type Zeolite Membrane In CO2 Separation– A Review. ASEAN Journal of Chemical Engineering, 14(2), 48-57. Retrieved from https://dev.journal.ugm.ac.id/v3/AJChE/article/view/8852
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