Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование
Impact of heat and mass transfer in porous catalytic monolith : CFD modeling of exothermic reaction. / Klenov, Oleg P.; Chumakova, Nataliya A.; Pokrovskaya, Svetlana A. и др.
в: Chemical Engineering Science, Том 205, 21.09.2019, стр. 1-13.Результаты исследований: Научные публикации в периодических изданиях › статья › Рецензирование
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TY - JOUR
T1 - Impact of heat and mass transfer in porous catalytic monolith
T2 - CFD modeling of exothermic reaction
AU - Klenov, Oleg P.
AU - Chumakova, Nataliya A.
AU - Pokrovskaya, Svetlana A.
AU - Noskov, Alexander S.
PY - 2019/9/21
Y1 - 2019/9/21
N2 - Impact of mass and heat transfer on exothermic reaction performance in porous catalytic monolith with triangular channels is investigated by CFD modeling. Detailed analysis of spatial distributions of process characteristics for methane oxidation shows that in the initial part of catalyst volume there is the active subsurface layer. The domain of sharp gradients of the reaction rate is revealed that includes the parts of external surface and thin subsurface layers near the monolith inlet, which results in sharp rearrangement of 3D-field of temperature and reagent concentrations. It is shown that the formation of such conditions is strongly influenced by complex gaseous flow reconstruction with gas penetration into the catalyst volume, significant heat release, and heat transfer between channel wall and gas flow. Though the region with high reaction rate is rather short this could be of high importance for reactor design and selection of optimal operation conditions.
AB - Impact of mass and heat transfer on exothermic reaction performance in porous catalytic monolith with triangular channels is investigated by CFD modeling. Detailed analysis of spatial distributions of process characteristics for methane oxidation shows that in the initial part of catalyst volume there is the active subsurface layer. The domain of sharp gradients of the reaction rate is revealed that includes the parts of external surface and thin subsurface layers near the monolith inlet, which results in sharp rearrangement of 3D-field of temperature and reagent concentrations. It is shown that the formation of such conditions is strongly influenced by complex gaseous flow reconstruction with gas penetration into the catalyst volume, significant heat release, and heat transfer between channel wall and gas flow. Though the region with high reaction rate is rather short this could be of high importance for reactor design and selection of optimal operation conditions.
KW - Computational fluid dynamics
KW - Conversion rate
KW - Exothermic reaction
KW - Honeycomb catalyst
KW - Porous structure
KW - REACTORS
KW - PROFILES
KW - BEHAVIOR
KW - CH4
KW - METHANE
KW - TEMPERATURE
KW - RH
KW - PARTIAL OXIDATION
KW - TRANSIENT
KW - SYNGAS
UR - http://www.scopus.com/inward/record.url?scp=85064555474&partnerID=8YFLogxK
U2 - 10.1016/j.ces.2019.04.010
DO - 10.1016/j.ces.2019.04.010
M3 - Article
AN - SCOPUS:85064555474
VL - 205
SP - 1
EP - 13
JO - Chemical Engineering Science
JF - Chemical Engineering Science
SN - 0009-2509
ER -
ID: 19629262