Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
158880 | Chemical Engineering Science | 2007 | 6 Pages |
Abstract
The catalytic process of aldehyde production from alkaline lignin extracted from sugarcane bagasse was evaluated in a batch slurry reactor and operated in a continuous three-phase fluidized-bed reactor with a palladium catalyst, at the operating conditions 373–413 K under 2–10 bar oxygen partial pressure. The scale-up of the fine aldehyde production process from batch to continuous operation presented a yield increase of approximately 15 times higher in 2 h of operation.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Fernando G. Sales, Laísse C.A. Maranhão, Nelson M. Lima Filho, Cesar A.M. Abreu,