Multi-Objective Optimisation of Biodiesel Synthesis in Simulated Moving Bed Reactor

被引:2
作者
Ray, Nillohit Mitra [1 ]
Ray, Ajay K. [1 ]
机构
[1] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON N6A 3K7, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
multifunctional reactor; reactive separation; multi-objective optimization; chromatographic reactor; biodiesel synthesis; multi-column chromatography; simulated moving bed; CHROMATOGRAPHIC REACTOR; GENETIC ALGORITHM; SMB; SEPARATION; OPERATION; FRUCTOSE; ISOMERIZATION; PERFORMANCE; BIOREACTOR; GLUCOSE;
D O I
10.3390/separations8080127
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
In this work, multi-objective optimisation study was performed to determine the performance improvement in a simulated moving bed reactor (SMBR) for biodiesel synthesis. The selection of the operating parameters such as switching time, liquid flow rates in various sections, as well as the length and number of columns is not straightforward in an SMBR. In most cases, conflicting requirements and constraints influence the optimal selection of the decision (operating or design) variables. A mathematical model that predicts single-column experimental results well was modified and verified experimentally for multiple-column SMBR system. In this article, a few multi-objective optimisation problems were carried out for both existing set-up as well as at the design stage. A non-dominated sorting genetic algorithm (NSGA) was used as the optimisation tool for the optimisation study. Due to conflicting effect of process parameters, the multi-objective optimisation study resulted in non-dominated Pareto optimal solutions. It was shown that significant increase in yield and purity of biodiesel in SMBR was possible both for operating and at design stage.
引用
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页数:16
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