Cyclic Fixed-Bed Operations over K2CO3-on-Carbon for the Recovery of Carbon Dioxide under Moist Conditions

1995 ◽  
Vol 68 (3) ◽  
pp. 1030-1035 ◽  
Author(s):  
Shinichi Hirano ◽  
Naoya Shigemoto ◽  
Shinichi Yamada ◽  
Hiromu Hayashi
Keyword(s):  
2018 ◽  
Vol 57 (18) ◽  
pp. 6391-6400 ◽  
Author(s):  
Steffi Matthischke ◽  
Stefan Roensch ◽  
Robert Güttel

1998 ◽  
Vol 37 (1) ◽  
pp. 185-191 ◽  
Author(s):  
Hiromu Hayashi ◽  
Jun Taniuchi ◽  
Nobuyoshi Furuyashiki ◽  
Shigeru Sugiyama ◽  
Shinichi Hirano ◽  
...  

2020 ◽  
Vol 4 (3) ◽  
pp. 1417-1426 ◽  
Author(s):  
Sebastian Bock ◽  
Robert Zacharias ◽  
Viktor Hacker

Fixed-bed chemical looping for the generation of high purity hydrogen with sequestration of pure carbon dioxide and nitrogen.


Author(s):  
Yanbing Li ◽  
Rui Xiao ◽  
Baosheng Jin ◽  
Huiyan Zhang

As one of the fundamental issues of the new poly-generation system on the basis of gasification gas and coke oven gas, carbon dioxide reforming of methane experiments have been performed over coal chars derived from different parent coals in a lab-scale fixed-bed reactor (internal diameter 12 mm, length 700 mm). The char derived from TongChuan coal exhibited higher activity than other samples employed under the same conditions. After the reforming reaction, the char samples were covered with different amounts of carbon deposition which resulted in the surface areas decrease. As the flow rate of feed gas increased from 200 ml/min to 600 ml/min over the Xuzhou char sample at 1050 degrees Celsius, the conversion of methane decreased from 52.7% to 17.5% and the H2 /CO dropped from 0.75 to 0.55. While maintaining the flow rate of CO2 at 20ml/min at 1050 degrees Celsius, the mole ratio of reactants CH4/CO2 was varied from 1 to 1.75 which led to the H2/CO ratio increase from 0.75 to 1.2.


1994 ◽  
Vol 27 (1) ◽  
pp. 45-51 ◽  
Author(s):  
Jong-Nam Kim ◽  
Kuck-Tack Chue ◽  
Kwon-Il Kim ◽  
Soon-Haeng Cho ◽  
Jong-Duk Kim

Author(s):  
Hua Chang ◽  
Tao Ma ◽  
Ling Liu ◽  
Hua-Qiang Yin ◽  
Xue-Dong He

The adsorption capability of carbon dioxide on 13X molecular sieve (13XMS) was investigated in a fixed-bed apparatus with two-road gas mixing system by dynamic column breakthrough method with helium as carrier gas at helium purification conditions of high-temperature gas-cooled reactor (HTGR). Experiments were performed at temperatures of 5°C ∼35 °C and low carbon dioxide partial pressure range of 10∼150Pa. By analyzing the breakthrough curve, both equilibrium adsorption capacity and kinetic adsorption capacity at breakthrough point were determined. Based on mass-transfer zone model, the experimental breakthrough curves at different operation conditions were analyzed. The carbon dioxide isotherm on 13XMS was fitted well by Langmuir model and the enthalpy of adsorption of carbon dioxide was estimated.


2016 ◽  
Vol 55 (29) ◽  
pp. 7964-7972 ◽  
Author(s):  
Asheesh Kumar ◽  
Tushar Sakpal ◽  
Gaurav Bhattacharjee ◽  
Anupam Kumar ◽  
Rajnish Kumar

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