Green Hydrogen Separation from Nitrogen by Mixed-Matrix Membranes Consisting of Nanosized Sodalite Crystals

被引:29
作者
Yang, Ge [1 ]
Guo, Hailing [1 ]
Kang, Zixi [2 ]
Zhao, Lei [1 ]
Feng, Shou [2 ]
Jiao, Feng [1 ]
Mintova, Svetlana [1 ,3 ]
机构
[1] China Univ Petr East China, CNPC, Key Lab Catalysis, State Key Lab Heavy Oil Proc, Qingdao 266555, Shandong, Peoples R China
[2] China Univ Petr East China, Coll Sci, Qingdao 266580, Shandong, Peoples R China
[3] Normandie Univ, CNRS, UNICAEN, ENSICAEN,LCS, 6 Blvd Marechal Juin, F-14050 Caen, France
基金
中国国家自然科学基金;
关键词
gas separation; hydrogen; mixed-matrix membranes; nitrogen; sodalite; GAS SEPARATION; HYDROTHERMAL SYNTHESIS; POLYIMIDE; PURIFICATION; CO2; PERFORMANCE; ZEOLITES; METHANE;
D O I
10.1002/cssc.201802577
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Nanosized sodalite (Nano-SOD) crystals were used as active filler to prepare mixed-matrix membranes (MMMs) for promoting the H-2/N-2 gas-separation performance. The Nano-SOD crystals with extremely small crystallites (40-50 nm) were synthesized from a colloidal suspension free of organic structural directing agent and uniformly dispersed in the polyetherimide (PEI) matrix. The Nano-SOD filler with a suitable aperture size (2.8 angstrom) allowed only H-2 molecules to pass through and rejected the N-2, thus improving the selectivity of the membranes. The high dispersion of Nano-SOD crystals in the polymer matrix and the interactions between the inorganic and organic phases greatly improved the membrane separation performance and minimized interfacial holes. The MMMs showed a high H-2 permeability (approximate to 7155.1Barrer at 25 degrees C under atmospheric pressure) and an ideal H-2/N-2 selectivity factor of approximately 16.9 in a single gas test. Moreover, in a gas mixture (H-2/N-2, 25-100 degrees C), the selectivity factor increased significantly to approximately 30.9. The high stability of the MMMs, which consist of highly dispersed Nano-SOD crystals in a PEI matrix for H-2/N-2 separation (6weeks continuous test), makes them an important material for ammonia synthesis applications that require and also release a large amount of H-2.
引用
收藏
页码:4529 / 4537
页数:9
相关论文
共 41 条
[1]   Hydrogen membrane separation techniques [J].
Adhikari, S ;
Fernando, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (03) :875-881
[2]   The effects of aminosilane grafting on NaY zeolite-Matrimid®5218 mixed matrix membranes for CO2/CH4 separation [J].
Amooghin, Abtin Ebadi ;
Omidkhah, Mohammadreza ;
Kargari, Ali .
JOURNAL OF MEMBRANE SCIENCE, 2015, 490 :364-379
[3]  
Awala H, 2015, NAT MATER, V14, P447, DOI [10.1038/nmat4173, 10.1038/NMAT4173]
[4]   Polymeric mixed matrix membranes containing zeolites as a filler for gas separation applications: A review [J].
Bastani, Dariush ;
Esmaeili, Nazila ;
Asadollahi, Mahdieh .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2013, 19 (02) :375-393
[5]   SYNTHESIS AND STRUCTURE OF SULFIDE ALUMINATE SODALITES [J].
BRENCHLEY, ME ;
WELLER, MT .
JOURNAL OF MATERIALS CHEMISTRY, 1992, 2 (10) :1003-1005
[6]   Gas Separation Properties of Polyimide-Zeolite Mixed Matrix Membranes [J].
Chaidou, C. I. ;
Pantoleontos, G. ;
Koutsonikolas, D. E. ;
Kaldis, S. P. ;
Sakellaropoulos, G. P. .
SEPARATION SCIENCE AND TECHNOLOGY, 2012, 47 (07) :950-962
[7]   Synthesis and characterization of poly (ethylene oxide) containing copolyimides for hydrogen purification [J].
Chen, Hangzheng ;
Xiao, Youchang ;
Chung, Tai-Shung .
POLYMER, 2010, 51 (18) :4077-4086
[8]   A SIMPLE-MODEL FOR A WATER-GAS SHIFT MEMBRANE REACTOR [J].
DAMLE, AS ;
GANGWAL, SK ;
VENKATARAMAN, VK .
GAS SEPARATION & PURIFICATION, 1994, 8 (02) :101-106
[9]   PREPARATION OF ZEOLITE FILLED GLASSY POLYMER MEMBRANES [J].
DUVAL, JM ;
KEMPERMAN, AJB ;
FOLKERS, B ;
MULDER, MHV ;
DESGRANDCHAMPS, G ;
SMOLDERS, CA .
JOURNAL OF APPLIED POLYMER SCIENCE, 1994, 54 (04) :409-418
[10]   Synthesis of nanometer-sized sodalite without adding organic additives [J].
Fan, Wei ;
Morozumi, Kazumasa ;
Kimura, Riichiro ;
Yokoi, Toshiyuki ;
Okubo, Tatsuya .
LANGMUIR, 2008, 24 (13) :6952-6958