摘要
在用固定化产腈水解酶细胞填充床反应器催化制备尼克酸的实验中,通过构建代数形式的经验方程,成功地完成了反应器操作参数的设计。通过分析已知的填充床反应器的轴向扩散模型(一维)的数值解,得到一个经验方程:L=7.898u cS0+114.6u+0.028,该方程描述了3个关键操作参数(柱长L,流速u和底物浓度cS0)之间的关系。在底物转化率和反应器孔隙率分别为95%和0.11的前提下,以所得的代数方程为约束条件进行了最优化计算,求解出最优操作参数,使尼克酸的产量达到最高。
By constructing an empirical equation with algebraic form,the key operational parameters of immobilized nitrilase-producing cells packed-bed reactor were determined successfully for nicotinic acid production.A simplified equation,L=7.898u cS0+114.6u+0.028,which describes the relationship of the three key operational parameters(column length L,flow rate u and substrate concentration cS0),was obtained by analyzing the numerical solutions of the established axial dispersion model(one-dimension) of packed-bed reactor.Under the condition of 3-cyanopyridine conversion rate of 95% and the void fraction of 0.11,the optimal operational parameters of packed-bed reactor were obtained by computation based on the algebraic equation for the purpose of maximization of the nicotinic acid production.
出处
《华东理工大学学报(自然科学版)》
CAS
CSCD
北大核心
2012年第1期39-44,共6页
Journal of East China University of Science and Technology
基金
国家重点基础研究发展(973)计划(2009CB724703)
关键词
填充床反应器
轴向扩散模型
关键操作参数
代数方程
尼克酸
packed-bed reactor
axial dispersion model
key operational parameters
algebraic equation
nicotinic acid