| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 588712 | Process Safety and Environmental Protection | 2007 | 7 Pages |
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.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Health and Safety
Authors
M. Zheng, R.L. Skelton, M.R. Mackley,