TY - JOUR
T1 - CFD Simulation of Microchannel Reactor Block for Fischer-Tropsch Synthesis
T2 - Effect of Coolant Type and Wall Boiling Condition on Reactor Temperature
AU - Kshetrimayum, Krishnadash S.
AU - Jung, Ikhwan
AU - Na, Jonggeol
AU - Park, Seongho
AU - Lee, Yongkyu
AU - Park, Seongeon
AU - Lee, Chul Jin
AU - Han, Chonghun
N1 - Publisher Copyright:
© 2015 American Chemical Society.
PY - 2016/1/27
Y1 - 2016/1/27
N2 - Computational fluid dynamic (CFD) simulation of heat transfer in a microchannel reactor block for low temperature Fischer-Tropsch (FT) synthesis was considered. Heat generation profiles for different operating conditions (GHSV 5000 h-1; catalyst loading 60%-120%, where 100% loading equals 1060 kg/m3 of cobalt based catalyst from Oxford Catalyst Ltd.) were obtained from a single channel model. Simulations on a reactor block quantified the effects of three coolant types: cooling oil (Merlotherm SH), subcooled water and saturated water, on reactor temperature, and also evaluated the effect of wall boiling conditions. At process conditions of GHSV 5000 h-1 and catalyst loading of 120%, predicted temperature gradients along channel length were 32, 17 and 12 K for cooling oil, subcooled water and saturated water, respectively. A modified reactor block showed improved thermal performance as well as heat transfer enhancement due to wall boiling conditions.
AB - Computational fluid dynamic (CFD) simulation of heat transfer in a microchannel reactor block for low temperature Fischer-Tropsch (FT) synthesis was considered. Heat generation profiles for different operating conditions (GHSV 5000 h-1; catalyst loading 60%-120%, where 100% loading equals 1060 kg/m3 of cobalt based catalyst from Oxford Catalyst Ltd.) were obtained from a single channel model. Simulations on a reactor block quantified the effects of three coolant types: cooling oil (Merlotherm SH), subcooled water and saturated water, on reactor temperature, and also evaluated the effect of wall boiling conditions. At process conditions of GHSV 5000 h-1 and catalyst loading of 120%, predicted temperature gradients along channel length were 32, 17 and 12 K for cooling oil, subcooled water and saturated water, respectively. A modified reactor block showed improved thermal performance as well as heat transfer enhancement due to wall boiling conditions.
UR - http://www.scopus.com/inward/record.url?scp=84956471030&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.5b03283
DO - 10.1021/acs.iecr.5b03283
M3 - Article
AN - SCOPUS:84956471030
SN - 0888-5885
VL - 55
SP - 543
EP - 554
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 3
ER -