1992
DOI: 10.1002/aic.690380506
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Modeling fixed‐bed coal gasifiers

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Cited by 151 publications
(97 citation statements)
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References 48 publications
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“…The kinetic rate constants (kgm −3 s −1 ) are taken from the literature (Ross and Davidson, 1982;Hobbs et al, 1992) and are provided in Table 1.…”
Section: Heterogeneous Reactionsmentioning
confidence: 99%
“…The kinetic rate constants (kgm −3 s −1 ) are taken from the literature (Ross and Davidson, 1982;Hobbs et al, 1992) and are provided in Table 1.…”
Section: Heterogeneous Reactionsmentioning
confidence: 99%
“…Coal: Since commercial coal-gasification has been in use since 1830 (Stassen, 1995) an extensive experimental and simulation work has been done in this area (Cooper, et al, 1984, Smoot, et al, 1985, Nowacki 1980, and Hobbs, 1990. However, the study of particle sizes in the fixed bed gasification range (10-100 mm (0.4-4.0") particle size) is scarce (Hobbs, et al, 1990), as most of the study has been done for fluidized bed gasification of coal.…”
Section: Gasificationmentioning
confidence: 99%
“…2-133. Values of the rate parameters to use for char reaction with oxygen and carbon dioxide in PCGC-2 are shown in Table 2-8 A sample calculation for Ajl is given in Appendix K. Given the lack of reliable data for char reaction with steam and hydrogen, the assumptions of Hobbs et al (1992) are recommended. They assumed that the steam-char reaction rate is the same as the carbon dioxide reaction rate and that the char gasification rate by hydrogen is three orders of magnitude smaller than the gasification rate by carbon dioxide.…”
Section: -Pcgc-2 User's Manual Particle Phase Reaand=mentioning
confidence: 99%