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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| Main Authors: | , |
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| Format: | Theses and Dissertations NonPeerReviewed |
| Published: |
[Yogyakarta] : Universitas Gadjah Mada
2013
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| Subjects: | |
| Online Access: | https://repository.ugm.ac.id/124085/ http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=64204 |
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| Institution: | Universitas Gadjah Mada |