Development of a membrane reactor for decomposing hydrogen sulfide into hydrogen using a high-performance amorphous silica membrane

被引:38
作者
Akamatsu, Kazuki [1 ]
Nakane, Masataka [1 ]
Sugawara, Takashi [1 ]
Hattori, Tadashi [2 ]
Nakao, Shin-ichi [1 ]
机构
[1] Univ Tokyo, Dept Chem Syst Engn, Bunkyo Ku, Tokyo 1138656, Japan
[2] Nagoya Ind Sci Res Inst, Chikusa Ku, Nagoya, Aichi 4640819, Japan
关键词
Membrane reactor; Silica membrane; Chemical vapor deposition; Hydrogen; Hydrogen sulfide;
D O I
10.1016/j.memsci.2008.08.005
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We have successfully developed a membrane reactor for decomposing hydrogen sulfide into hydrogen using an amorphous silica membrane for the first time. The membrane was prepared by the CVD method with tetramethoxysilane and oxygen, and showed excellent hydrogen permeance at 873 K of the order of 10(-7) mol m(-2) s(-1) Pa(-1) and high hydrogen/nitrogen permselectivity of 10(4). The membrane reactor constructed with our membrane and a commercially available catalyst decomposed hydrogen sulfide into hydrogen with higher conversion than the equilibrium conversion. This conversion enhancement was because of the selective extraction of hydrogen from the reaction side to the permeate side by the silica membrane. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:16 / 19
页数:4
相关论文
共 14 条
[1]   An analysis of the Peclet and Damkohler numbers for dehydrogenation reactions using molecular sieve silica (MSS) membrane reactors [J].
Battersby, Scott ;
Teixeira, Paula Werneck ;
Beltramini, Jorge ;
Duke, Mikel C. ;
Rudolph, Victor ;
da Costa, Joao C. Diniz .
CATALYSIS TODAY, 2006, 116 (01) :12-17
[2]  
BRECK DW, 1974, ZEOLITE MOL SIEVES, P636
[3]   THERMOLYSIS OF HYDROGEN-SULFIDE IN A METAL-MEMBRANE REACTOR [J].
EDLUND, DJ ;
PLEDGER, WA .
JOURNAL OF MEMBRANE SCIENCE, 1993, 77 (2-3) :255-264
[4]   DEPOSITION OF H-2-PERMSELECTIVE SIO2-FILMS [J].
GAVALAS, GR ;
MEGIRIS, CE ;
NAM, SW .
CHEMICAL ENGINEERING SCIENCE, 1989, 44 (09) :1829-1835
[5]   Hydrogen recovery from cyclohexane as a chemical hydrogen carrier using a palladium membrane reactor [J].
Itoh, N ;
Tamura, E ;
Hara, S ;
Takahashi, T ;
Shono, A ;
Satoh, K ;
Namba, T .
CATALYSIS TODAY, 2003, 82 (1-4) :119-125
[6]   PRODUCTION OF HYDROGEN FROM HYDROGEN-SULFIDE BY MEANS OF SELECTIVE DIFFUSION MEMBRANES [J].
KAMEYAMA, T ;
DOKIYA, M ;
FUJISHIGE, M ;
YOKOKAWA, H ;
FUKUDA, K .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1983, 8 (01) :5-13
[7]   POSSIBILITY FOR EFFECTIVE PRODUCTION OF HYDROGEN FROM HYDROGEN-SULFIDE BY MEANS OF A POROUS VYCOR GLASS MEMBRANE [J].
KAMEYAMA, T ;
DOKIYA, M ;
FUJISHIGE, M ;
YOKOKAWA, H ;
FUKUDA, K .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1981, 20 (01) :97-99
[8]   Preparation of a stable silica membrane by a counter diffusion chemical vapor deposition method [J].
Nomura, M ;
Ono, K ;
Gopalakrishnan, S ;
Sugawara, T ;
Nakao, SI .
JOURNAL OF MEMBRANE SCIENCE, 2005, 251 (1-2) :151-158
[9]   Preparation of a catalyst composite silica membrane reactor for steam reforming reaction by using a counterdiffusion CVD method [J].
Nomura, Mikihiro ;
Seshimo, Masahiro ;
Aida, Hitoshi ;
Nakatani, Katsuya ;
Gopalakrishnan, Suraj ;
Sugawara, Takashi ;
Ishikawa, Toru ;
Kawamura, Mitsutaka ;
Nakao, Shin-ichi .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (11) :3950-3954
[10]   Hydrogen production from hydrogen sulfide using membrane reactor integrated with porous membrane having thermal and corrosion resistance [J].
Ohashi, H ;
Ohya, H ;
Aihara, M ;
Negishi, Y ;
Semenova, SI .
JOURNAL OF MEMBRANE SCIENCE, 1998, 146 (01) :39-52