A batch reactor designed to simulate the non-isother-ma1 temperature profile of a commercial, vertical-tube wet oxidation process is used to predict global process performance, and to estimate reaction rates. A model is developed for the batch reactor that predicts extent of reaction and vapovliquid
β¦ LIBER β¦
Isothermal quenching of the oxidation of wet CO
β Scribed by James E. Hardy; Richard K. Lyon
- Publisher
- Elsevier Science
- Year
- 1980
- Tongue
- English
- Weight
- 199 KB
- Volume
- 39
- Category
- Article
- ISSN
- 0010-2180
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## Abstract Catalytic wet oxidation carried out in a continual threeβphase trickleβbed reactor contributes to the sustainability of chemical technology. It was found that the hydrodynamics and the massβtransfer of reactants could have a significant impact on the performance of the trickleβbed react