Investigating the Batch and Continuous Transesterification of Linseed Oil by Using a Alkaline Heterogeneous Catalyst in a Packed Bed Reactor
Both the continuous and batch transesterification of linseed oil were examined in order to maximize the fatty acid methyl esters (FAME) yield. The continuous process was conducted in a packed bed reactor using calcium oxide as a heterogeneous catalyst. In addition, the impact of two variables, namel...
Main Authors: | , , |
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Format: | Article |
Language: | English |
Published: |
Materials and Energy Research Center (MERC)
2017-09-01
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Series: | Journal of Renewable Energy and Environment |
Subjects: | |
Online Access: | https://www.jree.ir/article_85977_ebf218658132f9637f30179f972a7171.pdf |