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pro vyhledávání: '"Shahla Aryana"'
Publikováno v:
Chemical Product and Process Modeling. 4
A dynamic model of an industrial packed-bed multi-tubular reactor was developed to investigate performance of an industrial ethylene oxide (EO) reactor, conducting epoxidation of ethylene over a silver-based catalyst. The set of nonlinear kinetic rat
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::4b4624b98e69d9d7a50fea34b258cd5d
https://doi.org/10.2202/1934-2659.1231
https://doi.org/10.2202/1934-2659.1231
