Computational Fluid Dynamics Study of Channel Geometric Effect for Fischer-Tropsch Microchannel Reactor

被引:7
作者
Na, Jonggeol [1 ]
Jung, Ikhwan [1 ]
Kshetrimayum, Krishnadash S. [1 ]
Park, Seongho [1 ]
Park, Chansaem [1 ]
Han, Chonghun [1 ]
机构
[1] Sch Chem & Biol Engn, 1 Gwanak Ro, Seoul 151744, South Korea
来源
KOREAN CHEMICAL ENGINEERING RESEARCH | 2014年 / 52卷 / 06期
关键词
GTL; Fischer Tropsch; Microchannel; CFD; Simulation; Reactor;
D O I
10.9713/kcer.2014.52.6.826
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Driven by both environmental and economic reasons, the development of small to medium scale GTL(gas-to-liquid) process for offshore applications and for utilizing other stranded or associated gas has recently been studied increasingly. Microchannel GTL reactors have been prefrered over the conventional GTL reactors for such applications, due to its compactness, and additional advantages of small heat and mass transfer distance desired for high heat transfer performance and reactor conversion. In this work, multi-microchannel reactor was simulated by using commercial CFD code, ANSYS FLUENT, to study the geometric effect of the microchannels on the heat transfer phenomena. A heat generation curve was first calculated by modeling a Fischer-Tropsch reaction in a single-microchannel reactor model using Matlab-ASPEN integration platform. The calculated heat generation curve was implemented to the CFD model. Four design variables based on the microchannel geometry namely coolant channel width, coolant channel height, coolant channel to process channel distance, and coolant channel to coolant channel distance, were selected for calculating three dependent variables namely, heat flux, maximum temperature of coolant channel, and maximum temperature of process channel. The simulation results were visualized to understand the effects of the design variables on the dependent variables. Heat flux and maximum temperature of cooling channel and process channel were found to be increasing when coolant channel width and height were decreased. Coolant channel to process channel distance was found to have no effect on the heat transfer phenomena. Finally, total heat flux was found to be increasing and maximum coolant channel temperature to be decreasing when coolant channel to coolant channel distance was decreased. Using the qualitative trend revealed from the present study, an appropriate process channel and coolant channel geometry along with the distance between the adjacent channels can be recommended for a microchannel reactor that meet a desired reactor performance on heat transfer phenomena and hence reactor conversion of a Fischer-Tropsch microchannel reactor.
引用
收藏
页码:826 / 833
页数:8
相关论文
共 24 条
[1]   Computational fluid dynamics (CFD) analysis of micro-reactor performance: Effect of various configurations [J].
An, Hui ;
Li, Ang ;
Sasmito, Agus P. ;
Kurnia, Jundika C. ;
Jangam, Sachin V. ;
Mujumdar, Arun S. .
CHEMICAL ENGINEERING SCIENCE, 2012, 75 :85-95
[2]   Computational fluid dynamics study of heat transfer in a microchannel reactor for low-temperature Fischer-Tropsch synthesis [J].
Arzamendi, G. ;
Dieguez, P. M. ;
Montes, M. ;
Odriozola, J. A. ;
Falabella Sousa-Aguiar, E. ;
Gandia, L. M. .
CHEMICAL ENGINEERING JOURNAL, 2010, 160 (03) :915-922
[3]   Kinetic study of Fischer-Tropsch process on titania-supported cobalt-manganese catalyst [J].
Atashi, H. ;
Siami, F. ;
Mirzaei, A. A. ;
Sarkari, M. .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2010, 16 (06) :952-961
[4]   Liquid-vapor thermodynamic equilibrium in Fischer-Tropsch synthesis products [J].
Derevich, I. V. ;
Ermolaev, V. S. ;
Mordkovich, V. Z. .
THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2008, 42 (02) :216-219
[5]   Thermodynamics of wax formation in the fischer-tropsch synthesis products [J].
Derevich, I. V. ;
Ermolaev, V. S. ;
Zol'nikova, N. V. ;
Mordkovich, V. Z. .
THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2013, 47 (03) :191-200
[6]   Simulation of Fluid Dynamics in a Microchannel Fischer-Tropsch Reactor [J].
Derevich, I. V. ;
Ermolaev, V. S. ;
Mordkovich, V. Z. ;
Galdina, D. D. .
THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2012, 46 (01) :8-19
[7]   Development of a kinetic model for Fischer-Tropsch synthesis over Co/Ni/Al2O3 catalyst [J].
Fazlollahi, Farhad ;
Sarkari, Majid ;
Zare, Akbar ;
Mirzaei, Ali Akbar ;
Atashi, Hossein .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2012, 18 (04) :1223-1232
[8]   Comparison of different reactor types for low temperature Fischer-Tropsch synthesis: A simulation study [J].
Guettel, Robert ;
Turek, Thomas .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (05) :955-964
[9]  
Jarosch KT, 2005, ACS SYM SER, V914, P258
[10]  
Jun K. - W., 2009, KCS, V36, P8