Analysis of non-isothermal, wet oxidation reactor data
β Scribed by Hochleitner, Wolfgang A.
- Publisher
- American Institute of Chemical Engineers
- Year
- 1996
- Tongue
- English
- Weight
- 755 KB
- Volume
- 15
- Category
- Article
- ISSN
- 0278-4491
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β¦ Synopsis
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 equilibria under non-is0 thermal conditions. n i s model is used with measured rate parameters to predict the gfect of process conditions on overall performance of specific wastes. This reduces the number of runs normally executed in a feasibility study, saving time and money. Phenol is selected as a model compound, and values for reaction rate constants and induction period length are obtained for temperatures up to 224C.
π SIMILAR VOLUMES
A generalized mathematical model has been developed to simulate the non-isothermal performance of bubble column reactors. Steady-state reactor behavior is rigorously described without limitations on the extent of macro-mixing, flow configuration, absorption-reaction regime, and nature of reactive sp