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pro vyhledávání: '"J.H. Edwards"'
Autor:
J.H. Edwards
Publikováno v:
Historia. Instituciones. Documentos, Vol 4, Pp 11-33 (1977)
Externí odkaz:
https://doaj.org/article/3c1004dbdc024bb9bc9d1d4b6390fb94
Autor:
J.H. Edwards, Y. Sun
Publikováno v:
Energy Procedia. 69:1828-1837
An energetic upgrade factor has been defined as the ratio of the lower heating value (LHV) of the syngas (H 2 plus CO) produced plus unreacted feedstock to that of the feedstock processed. It is used to evaluate the thermal performance of the steam r
Akademický článek
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Akademický článek
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Publikováno v:
International Journal of Hydrogen Energy. 37:1475-1481
The effect of H 2 S on the performance of La 0.7 Ce 0.2 FeO 3 perovskite catalyst was investigated for the production of hydrogen from simulated coal-derived syngas via the water–gas shift reaction at 600 °C and 1 atm. The results show that the ca
Publikováno v:
Journal of Natural Gas Chemistry. 20:568-576
Thermodynamic analysis of the reforming of methane with carbon dioxide alone (“dry reforming”) and with carbon dioxide and steam together (“mixed reforming”) is performed as part of a project which investigates the suitability of these endoth
Publikováno v:
International Journal of Hydrogen Energy. 36:6638-6645
The performance of a commercially-available sour shift catalyst (SSC1) under selected syngas compositions was investigated and kinetic parameters were obtained. The watergas shift experiments were carried out in a differential reactor using simulated
Autor:
J.H. Edwards, G.J. Duffy, Daniel G. Roberts, San Shwe Hla, Alexander Y. Ilyushechkin, Ashleigh Cousins, L.D. Morpeth, Yong Sun
Publikováno v:
International Journal of Hydrogen Energy. 36:518-527
The kinetics of the water-gas shift (WGS) reaction over a novel La0.7Ce0.2FeO3 perovskite-like catalyst is investigated using simulated coal-derived syngas at temperatures of 550 °C and 600 °C which are higher than the maximum operating temperature
Autor:
Ashleigh Cousins, L.D. Morpeth, Yong Sun, G.J. Duffy, San Shwe Hla, J.H. Edwards, Daniel G. Roberts, David French
Publikováno v:
International Journal of Hydrogen Energy. 36:79-86
La (0.9− x ) Ce x FeO 3 perovskite-like catalysts were investigated for the production of hydrogen from simulated coal-derived syngas via the water–gas shift reaction in the temperature range 450–600 °C and at 1 atm. These catalysts exhibited
Autor:
L.D. Morpeth, G.J. Duffy, David French, Daniel G. Roberts, Y. Sun, San Shwe Hla, Ashleigh Cousins, J.H. Edwards
Publikováno v:
Applied Catalysis A: General. 390:201-209
CeO2–La2O3-based Cu catalysts were investigated for their ability to produce hydrogen from simulated coal-derived syngas via the water–gas shift reaction in the temperature range of 450–600 °C. CeO2–La2O3-based Cu catalysts exhibited high ac