The Model of Catalytic Reactor of Ethylene Glycol Production
| Autor: | Suchkov Ju P, M. G. Makarov, R.A. Kozlovskiy, A. V. Koustov, V. F. Shvets, I. A. Kozlovskiy |
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| Rok vydání: | 2005 |
| Předmět: |
inorganic chemicals
Materials science Ethylene oxide Fixed bed Organic Chemistry technology industry and agriculture Tube reactor Product distribution Catalysis chemistry.chemical_compound chemistry Chemical engineering Scientific method Polymer chemistry medicine Physical and Theoretical Chemistry Swelling medicine.symptom Ethylene glycol |
| Zdroj: | Organic Process Research & Development. 9:768-773 |
| ISSN: | 1520-586X 1083-6160 |
| DOI: | 10.1021/op058005+ |
| Popis: | The ethylene oxide hydration process in a catalytic fixed bed tube reactor was studied. A cross-linked styrene-divinylbenzene anion-exchange resin in the HCO3-/CO32- -form was used as a catalyst. The deactivation and swelling of the catalyst during the process were detected. The mathematical model of the reactor with determined parameters adequately describing the rate of the reaction, product distribution and catalyst deactivation and swelling has been developed. |
| Databáze: | OpenAIRE |
| Externí odkaz: |
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