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Journal Articles

Development of a membrane reactor with a closed-end silica membrane for nuclear-heated hydrogen production

Myagmarjav, O.; Tanaka, Nobuyuki; Nomura, Mikihiro*; Noguchi, Hiroki; Imai, Yoshiyuki; Kamiji, Yu; Kubo, Shinji; Takegami, Hiroaki

Progress in Nuclear Energy, 137, p.103772_1 - 103772_7, 2021/07

https://doi.org/10.1016/j.pnucene.2021.103772
 Times Cited Count：8 Percentile：73.82(Nuclear Science & Technology)

Journal Articles

Comparison of experimental and simulation results on catalytic HI decomposition in a silica-based ceramic membrane reactor

Myagmarjav, O.; Tanaka, Nobuyuki; Nomura, Mikihiro*; Kubo, Shinji

International Journal of Hydrogen Energy, 44(59), p.30832 - 30839, 2019/11

https://doi.org/10.1016/j.ijhydene.2019.09.132
 Times Cited Count：10 Percentile：29.69(Chemistry, Physical)

Journal Articles

Hydrogen production tests by hydrogen iodide decomposition membrane reactor equipped with silica-based ceramics membrane

Myagmarjav, O.; Tanaka, Nobuyuki; Nomura, Mikihiro*; Kubo, Shinji

International Journal of Hydrogen Energy, 42(49), p.29091 - 29100, 2017/12

https://doi.org/10.1016/j.ijhydene.2017.10.043
 Times Cited Count：21 Percentile：48.96(Chemistry, Physical)

The catalytic decomposition of hydrogen iodide in a membrane reactor using silica membranes derived from hexyltrimethoxysilane (HTMOS) was investigated for the production of hydrogen in the thermochemical water splitting iodine-sulfur process. The silica membranes were prepared by counter-diffusion chemical vapor deposition using porous alumina support tubes in both the absence and presence of a $$gamma$$-alumina layer. The silica membranes formed on $$gamma$$-alumina-coated $$alpha$$-alumina tubes displayed a higher H$$_{2}$$ permeance than that formed directly on an $$alpha$$-alumina tube. A silica membrane based on a 1.5 $$mu$$m-thick $$gamma$$-alumina layer fabricated under deposition conditions of 450$$^{circ}$$C, 1200 s, and a N$$_{2}$$ carrier gas velocity of 0.044 m s$$^{-1}$$ exhibited a high H$$_{2}$$ permeance of 9.4 $$times$$ 10$$^{-7}$$ mol Pa$$^{-1}$$ m$$^{-2}$$ s$$^{-1}$$ while maintaining an H$$_{2}$$/N$$_{2}$$ selectivity of over 80.0. The performance of a membrane reactor based on an HTMOS-derived silica membrane was evaluated at 400$$^{circ}$$C by measuring the HI conversion and H$$_{2}$$ flow rates. The conversion was approximately 0.48 when the HI flow rate was 9.7 mL min$$^{-1}$$.

Journal Articles

Preparation of an H$$_{2}$$-permselective silica membrane for the separation of H$$_{2}$$ from the hydrogen iodide decomposition reaction in the iodine-sulfur process

Myagmarjav, O.; Ikeda, Ayumi*; Tanaka, Nobuyuki; Kubo, Shinji; Nomura, Mikihiro*

International Journal of Hydrogen Energy, 42(9), p.6012 - 6023, 2017/03

https://doi.org/10.1016/j.ijhydene.2017.01.074
 Times Cited Count：19 Percentile：47.14(Chemistry, Physical)

Journal Articles

Stability of a silica membrane prepared by CVD using $$gamma$$- and $$alpha$$-alumina tube as the support tube in the Hi-H$$_{2}$$O gaseous mixture

Hwang, G.*; Kim, J.*; Choi, H.*; Onuki, Kaoru

Journal of Membrane Science, 215(1-2), p.293 - 302, 2003/04

https://doi.org/10.1016/S0376-7388(03)00022-X
 Times Cited Count：16 Percentile：55.96(Engineering, Chemical)

no abstracts in English

Journal Articles

Simulation study on the catalytic decomposition of hydrogen iodide in a membrane reactor with a silica membrane for the thermochemical water-splitting IS process

Hwang, G.; Onuki, Kaoru

Journal of Membrane Science, 194(2), p.207 - 215, 2001/12

https://doi.org/10.1016/S0376-7388(01)00540-3
 Times Cited Count：59 Percentile：86.99(Engineering, Chemical)

no abstracts in English

Journal Articles

Separation of hydrogen from H$$_{2}$$-H$$_{2}$$O-HI gaseous mixture using a silica membrane

Hwang, G.; Onuki, Kaoru; Shimizu, Saburo

AIChE Journal, 46(1), p.92 - 98, 2000/01

https://doi.org/10.1002/aic.690460112
 Times Cited Count：38 Percentile：77.28(Engineering, Chemical)

no abstracts in English

Journal Articles

Hydrogen separation in H$$_{2}$$-H$$_{2}$$O-HI gaseous mixture using the silica membrance prepared by chemical vapor deposition

Hwang, G.*; Onuki, Kaoru; Shimizu, Saburo;

J. Membr. Sci., 162(1-2), p.83 - 90, 1999/00

https://doi.org/10.1016/S0376-7388(99)00125-8
 Times Cited Count：65 Percentile：89.87(Engineering, Chemical)

no abstracts in English

JAEA Reports

Studies on hydrogen separation membrane for IS process; Membrane preparation with porous $$alpha$$-alumina tube

Hwang, G.*; Onuki, Kaoru; Shimizu, Saburo

JAERI-Research 98-002, 8 Pages, 1998/01

JAERI-Research-98-002.pdf:0.53MB

no abstracts in English

Journal Articles

Gas permeation through CVD modified anodic alumina membrane

Onuki, Kaoru; ; Nakajima, Hayato; Shimizu, Saburo

J. Chem. Eng. Jpn., 30(2), p.359 - 362, 1997/00

https://doi.org/10.1252/jcej.30.359
 Times Cited Count：3 Percentile：35.13(Engineering, Chemical)

no abstracts in English

Oral presentation

Development of ceramic membranes for large-scale hydrogen production via thermochemical iodine-sulfur process

Myagmarjav, O.; Tanaka, Nobuyuki; Noguchi, Hiroki; Kubo, Shinji; Nomura, Mikihiro*; Takegami, Hiroaki

no journal, , 

Oral presentation

Development of a silica membrane for H$$_{2}$$ production from HI decomposition in the IS process

Myagmarjav, O.; Ikeda, Ayumi*; Nomura, Mikihiro*; Kubo, Shinji

no journal, , 

In this study, we have developed a highly hydrogen permeable silica membrane derived from hexyltrimethoxysilane as a Si precursor using porous alumina support. Modification of alumina support tubes in the absence of and in the presence of $$gamma$$-alumina coating was carried out by a counter diffusion chemical vapor deposition (CVD). A membrane with intermediate $$gamma$$-alumina layer showed higher H$$_{2}$$ permeance (7.7 $$times$$ 10$$^{-7}$$ mol m$$^{-2}$$ s$$^{-1}$$ Pa$$^{-1}$$) than that formed directly on the $$alpha$$-alumina tube (3.8 $$times$$ 10$$^{-8}$$ mol m$$^{-2}$$ s$$^{-1}$$ Pa$$^{-1}$$). It was found that the thickness of $$gamma$$-alumina layer played an important role in the improvement of membrane permeation performance. Modified membrane based on $$gamma$$-alumina coating with a thickness of 1.5 $$mu$$m exhibited H$$_{2}$$/SF$$_{6}$$ selectivity over 3000 at 270$$^{circ}$$C, while maintaining H$$_{2}$$ permeance in the order of 10$$^{-7}$$ mol m$$^{-2}$$ s$$^{-1}$$ Pa$$^{-1}$$. The results led to the conclusion that the modified membrane is a promising candidate for further enhancement of HI decomposition in membrane reactor.

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