TY - JOUR
T1 - Multi-objective optimization of microchannel reactor for Fischer-Tropsch synthesis using computational fluid dynamics and genetic algorithm
AU - Na, Jonggeol
AU - Kshetrimayum, Krishnadash S.
AU - Lee, Ung
AU - Han, Chonghun
N1 - Publisher Copyright:
© 2016
PY - 2017
Y1 - 2017
N2 - We propose a multi-objective optimization methodology using a stochastic optimization algorithm, a genetic algorithm (GA) with ε-constraint method, and a 2D axisymmetric computational fluid dynamics (CFD)-based Fischer-Tropsch microchannel reactor model, validated by experimental data of CO conversion and CH4selectivity, for simultaneously maximizing C5+productivity and minimizing the temperature rise of a Fischer-Tropsch microchannel reactor. The main mixed integer nonlinear programming (MINLP) optimization problem is decomposed into an external CFD reactor model function and internal optimization constraints. The methodology is applied to the catalyst packing zone division, which is divided and packed with a different dilution ratio to distribute the heat of reaction evenly. The best solutions of the proposed optimizer are reproducible with different crossover fractions and are more efficient than other traditional non-convex constraint local solvers. Based on the Pareto optimal solution of the final optimizer with 4 zones, discrete dilution increases C5+productivity to 22% and decreases ΔTmaxto 63.2% compared to the single zone catalyst packing case. Finally, several Pareto optimal solutions and sub-optimal solutions are compared and the results are documented in terms of C5+productivity and maximum temperature increase.
AB - We propose a multi-objective optimization methodology using a stochastic optimization algorithm, a genetic algorithm (GA) with ε-constraint method, and a 2D axisymmetric computational fluid dynamics (CFD)-based Fischer-Tropsch microchannel reactor model, validated by experimental data of CO conversion and CH4selectivity, for simultaneously maximizing C5+productivity and minimizing the temperature rise of a Fischer-Tropsch microchannel reactor. The main mixed integer nonlinear programming (MINLP) optimization problem is decomposed into an external CFD reactor model function and internal optimization constraints. The methodology is applied to the catalyst packing zone division, which is divided and packed with a different dilution ratio to distribute the heat of reaction evenly. The best solutions of the proposed optimizer are reproducible with different crossover fractions and are more efficient than other traditional non-convex constraint local solvers. Based on the Pareto optimal solution of the final optimizer with 4 zones, discrete dilution increases C5+productivity to 22% and decreases ΔTmaxto 63.2% compared to the single zone catalyst packing case. Finally, several Pareto optimal solutions and sub-optimal solutions are compared and the results are documented in terms of C5+productivity and maximum temperature increase.
KW - Catalyst packing
KW - Computational fluid dynamics
KW - Fischer-Tropsch
KW - Microchannel reactor
KW - Multi-objective optimization
KW - Stochastic optimization
UR - http://www.scopus.com/inward/record.url?scp=85027919546&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2016.11.040
DO - 10.1016/j.cej.2016.11.040
M3 - Article
AN - SCOPUS:85027919546
SN - 1385-8947
VL - 313
SP - 1521
EP - 1534
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
ER -