Hydrogen permeation enhancement in a Pd membrane tube system under various vacuum degrees

2020 ◽  
Vol 45 (12) ◽  
pp. 7401-7411 ◽  
Author(s):  
Wei-Hsin Chen ◽  
Jamin Escalante ◽  
Yen-Hsun Chi ◽  
Yu-Li Lin
2012 ◽  
Vol 37 (17) ◽  
pp. 12666-12679 ◽  
Author(s):  
Wei-Hsin Chen ◽  
Wei-Ze Syu ◽  
Chen-I. Hung ◽  
Yu-Li Lin ◽  
Chang-Chung Yang

2019 ◽  
Vol 44 (28) ◽  
pp. 14434-14444 ◽  
Author(s):  
Wei-Hsin Chen ◽  
Shang-Wei Lin ◽  
Chia-Yang Chen ◽  
Yen-Hsun Chi ◽  
Yu-Li Lin

2009 ◽  
Vol 620-622 ◽  
pp. 13-16
Author(s):  
Kyeong Il Kim ◽  
Tae Whan Hong

Many laboratories have researched membrane for gasification of coal technique, separating hydrogen from fossil fuel. In general, Pd membrane of separating hydrogen is very good a property of hydrogen selectivity on high temperature, but it has some problems, hydrogen embrittlement and costly material. So, we need some materials of good properties about hydrogen selectivity instead of Pd. In this research, we fabricate membrane for hydrogen permeation, that is great in resistance to acids and chemically steady TiN. Our laboratory investigated about hydrogen selectivity. TiN powder is milled 30, 60 and 240 minutes by vibration mill, respectively. After than the samples put in operate spark plasma sintering. We analyze XRD, SEM, BET and TG/DSC. Also, in this research take an inspect hydrogen selectivity by ourselves manufactured Sievert’s type hydrogen permeation membrane equipment.


2014 ◽  
Vol 39 (1) ◽  
pp. 1-5
Author(s):  
Masakazu Mukaida ◽  
Nobuo Takahashi ◽  
Misaki Ishitsuka ◽  
Shigeki Hara ◽  
Hiroyuki Suda ◽  
...  

2002 ◽  
Vol 752 ◽  
Author(s):  
Masahiko Matsukata ◽  
Takashi Nishizuka ◽  
Yasushi Sekine ◽  
Eiichi Kikuchi

ABSTRACTA Pd/α-Al2O3 composite membrane was prepared on a porous α-Al2O3 disk via the thermal decomposition of bis(hexafluoroacetylacetonato)Pd(II), Pd(hfac)2. Pd(hfac)2 was dissolved in supercritical CO2 at 303 K, supplied to the substrate, and thermally decomposed at 403 and 443 K. The decomposition of Pd(hfac)2 at 443 K resulted in a sufficient pore filling of substrate with Pd as well as the formation of a thin Pd top layer. The hydrogen flux through this membrane was about 1.7 times than that of a electro-less plating Pd membrane with about 20 μm thick. Hydrogen permeation was governed by the solution-diffusion mechanism which gave a high separation selectivity.


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