Char-supported Fe-Zn-Cu sorbent prepared by ultrasonic-assisted impregnation for simultaneous removal of H2S and COS from coke oven gas

2015 ◽  
Vol 35 (2) ◽  
pp. 352-358 ◽  
Author(s):  
Jinxiao Dou ◽  
Arash Tahmasebi ◽  
Xianchun Li ◽  
Fengkui Yin ◽  
Jianglong Yu
2020 ◽  
Vol 10 (9) ◽  
pp. 2961-2969
Author(s):  
Eva Kamp ◽  
Holger Thielert ◽  
Olaf von Morstein ◽  
Sven Kureti ◽  
Norman Schreiter ◽  
...  

Simultaneous hydrogenation of organosulfur compounds and O2 by Pd/Al2O3 catalyst was studied in a fixed bed reactor and by DRIFTS.


1992 ◽  
Vol 31 (1) ◽  
pp. 415-419 ◽  
Author(s):  
Kouichi Miura ◽  
Kazuhiro Mae ◽  
Tomohiko Inoue ◽  
Tomoyuki Yoshimi ◽  
Hiroyuki Nakagawa ◽  
...  

2020 ◽  
Vol 33 (2) ◽  
pp. 183
Author(s):  
Hongqing Feng ◽  
Zhirong Nan ◽  
Xinyi Wang ◽  
Weiwen Zhang

2010 ◽  
Vol 156-157 ◽  
pp. 1024-1028
Author(s):  
Da Hai Hu ◽  
Xiong Gang Lu ◽  
Hong Wei Cheng ◽  
Wei Zhong Ding

The performance of Ni/SiO2 Catalysts modified by La2O3, ZrO2 and CeO2 were tested in a BaCo0.7Fe0.2Nb0.1O3-δ (BCFNO) membrane reactor by catalytic partial oxidation of coke oven gas (COG) under atmospheric pressure. The results show that the oxygen permeation flux increased dramatically with Ni/RxOy/SiO2 (R = La, Zr or Ce) catalysts by adding the element of rare earth especially the La during the reforming reaction. At optimized reaction conditions, the dense oxygen permeable membrane had an oxygen permeation flux around 16.4 ml/cm2•min and a CH4 conversion of 99.2% have been achieved at 900 oC.


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