Kinetika reaksi hidrogenasi isoprena dengan katalis Pd dalam reaktor monolith
| Main Author: | Perpustakaan UGM, i-lib |
|---|---|
| Format: | Article NonPeerReviewed |
| Terbitan: |
[Yogyakarta] : Universitas Gadjah Mada
, 2002
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| Subjects: | |
| Online Access: |
https://repository.ugm.ac.id/18667/ http://i-lib.ugm.ac.id/jurnal/download.php?dataId=1464 |
Daftar Isi:
- The hydrogenation of isoprene (2-methyl-I,3-butadiene) proceeds at 273 K-288 K in methanol solvent in the presence of Pd/Al2D3catalysts to produce methylbutene isomers. The reactor was operated in semibatch with respect to hydrogen, whereas the liquid phase was in batch recirculating through a storage tank. The parameters of mass tranfer were estimated from correlations. The reaction kinetics and the mass transfer were included in a plug-flow type model for the monolith. The kinetic parameters were optimized using the Hooke-Jeeve method Simulation and the experimental result showed that the rate model proposed can be used in isoprene hydrogenation.