Hydrodynamic models for slurry bubble column reactors. Third technical progress report, January 1995--March 1995 Page: 4 of 20
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HYDRODYNAMIC MODEL for multiphase flow with reaction and interfacial mass
transports(D. Gidaspow 1994b).
a (8epg) +0- (egpgvg) = h.
-t( ep ) +-V(8egPVg) =rh1
a (Ep) +V-(espV,) =ins
(CgpgVg) +V-(e .Pgv) = - P -Epg+V 3+pg(Vls-Vg) +N1g(V1-Vg) +mgVg
Q (e1p1vi) +V-(EPV1v1) =-VP -ejp1g+V+t1+Pl( vgVi) + (.V-V:) +m, V,
a (epsVs) +V(espsVsV) = -Ps-eSpsg+V-,+Rg(Vg-Vs) +h'1s(V1-Vs) -msVs
is=0 f1=-mgE1i R"M i=H2, CO, CO2, CHI, CH3OH, H20
VPk=G (ek) Vek
1=e1p1 ( [VV1+ (VV) T] - 3V-VI)
kPk(Vk+ (OVk)) + ( k V k)
G(ek) =108.76 0.27 (dynes/crn2)
k 3k~dko(1-e) k
go= (1- (ek/Ck,.) /3)
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Gidaspow, D. Hydrodynamic models for slurry bubble column reactors. Third technical progress report, January 1995--March 1995, report, April 1, 1995; United States. (digital.library.unt.edu/ark:/67531/metadc667453/m1/4/: accessed June 23, 2018), University of North Texas Libraries, Digital Library, digital.library.unt.edu; crediting UNT Libraries Government Documents Department.