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- W183647579 abstract "An empirical Langmuir-Hinshelwood kinetic model for the potassium catalyzed gasification of Illinois No. 6 bituminous coal has been developed. This model provides a good fit to fixed bed reactor data over pressures ranging from atmospheric to 500 psig and a 30-fold range of steam flow rates. It also predicts conversions for the temperature range 1200/sup 0/F to 1300/sup 0/F and catalyst loadings from 0.1 to 0.2 grams K/sub 2/CO/sub 3/ per gram of coal. For the catalyst levels examined, the gasification rate was proportional to the amount of catalyst present. Additional studies need to be performed over a broader range of catalyst loadings to determine the limits of this relationship. It was also shown that these kinetics can be applied to predict trends in conversion for H/sub 2/O, H/sub 2/ and CO mixed gas feeds. The kinetic expression obtained has been shown to have adequate predictive capabilities in the range of interest. It is in a form which can be used directly in the development of models for fluid bed gasification reactors. Thus, the goal for this study has been achieved. Future work will be directed toward formulating a fluid bed reactor model." @default.
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- W183647579 date "1978-09-10" @default.
- W183647579 modified "2023-09-24" @default.
- W183647579 title "Kinetics of potassium catalyzed gasification" @default.
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