Prarancangan Pabrik Heptena dari Propena dan Butena dengan Kapasitas 20.000 Ton/Tahun
Heptena is produced with co-dimerization method of propylene and butane with Ni-Alumina catalyst. Reaction takes place in liquid phase in a fixed bed multi stage reactor with operating conditions of 45 OC and 11 bar. Heat of reaction is taken from the system using a heat exchanger in each stage. Hep...
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| Format: | Thesis |
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[Yogyakarta] : Universitas Gadjah Mada
2013
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