Vanillin production from lignin oxidation in a batch reactor

被引:182
作者
Araujo, Jose D. P. [1 ]
Grande, Carlos A. [1 ]
Rodrigues, Alirio E. [1 ]
机构
[1] Univ Porto, LSRE, Dept Chem Engn, Fac Engn, P-4200465 Oporto, Portugal
关键词
Vanillin; Kraft lignin; Batch reactor; HARDWOOD KRAFT-LIGNIN; PHENOLIC DERIVATIVES; KINETICS;
D O I
10.1016/j.cherd.2010.01.021
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Vanillin production from lignin oxidation is a biomass-based process that employs a by-product of the pulp and paper industry and air to obtain a high-added value compound. However, lignin is an organic polymer with a structure that depends strongly on the source and the conditions to obtain vanillin should be adjusted for different samples. The objective of this work is to establish a fast and standard protocol to characterize lignin conversion to vanillin by batch oxidation. The experimental technique is coupled with a mathematical model that allows us to fit the data and determine kinetic rate constants under non-isothermal conditions. Two examples of vanillin oxidation with very different lignin sources are presented. The results revealed vanillin yields with respect to the lignin mass ranging from 3.5% to 7.6% for the high and low-molecular weight lignins, respectively. (C) 2010 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1024 / 1032
页数:9
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