Article ID Journal Published Year Pages File Type
588712 Process Safety and Environmental Protection 2007 7 Pages PDF
Abstract

This paper is concerned with performing laboratory scale alkali-catalyst transesterification for biodiesel reaction and ranking conversion and performance between a stirred tank reactor, and oscillatory flow meso reactors in both batch and continuous mode. The results show that a comparative conversion can be achieved for the same reaction conditions, thereby demonstrating that batch and continuous meso reactor configurations can be used for a high throughput screening biodiesel reactions.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Health and Safety
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