滴流床反应器
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Liquid Properties:Enter
Data
Dimensionle
ss Numbers
density (kg/m3), rol769 1 St GL0.002484011 viscosity (kg/m.s), mul0.0009 2 Web L9.087E-01 surface tension(kg/s2), sigl0.0256 3 Re G 5.556E+01 superficial velocity(m/s), ul0.11 4 Ca GL9.141E-05 Diffusion Coefficient (m2/s) dal 2.00E-09 5 dc/H 4.167E-02 Gas Properties: 6 Sb 2.796E+00 density (kg/m3), rog207 Sc L 5.852E+02 viscosity(kg/m.s), mug 1.80E-05
superficial velocity(m/s), ug0.02
Diffusion Coefficient (m2/s) dag 1.40E-05
Particles and Bed Properties:
grain equivalent diameter (m), dv 2.50E-03Sh L = 1.2490E+03 sphericity factor (-), phi1K L.a = 2.0462E+00 bed porosity (-), eps0.386(s-1)
column diameter (m), dc0.05
Bed height (m), H 1.2
Foaming Property of the
liquid (1 if yes/ 0 if no)0
Calculated specific surface area
(m-1), as 1.55E+03
Calculated hydraulic diameter (m)
dh 1.10E-03
#
Dimensionle ss Numbers Dimensionle ss Numbers
1 Re L 2.350E+0
2 1 Re L 2.350E+02
2 St L 2.102E-0
3 2 Re G 5.556E+01
3 Re G 5.556E+01 3 Web G7.813E-04
4 Fr G 1.631E-02 4 Fr L 4.934E-01
5 Sc G 6.429E-02 5 Eotv7.279E-01
6 Sb 2.796E+00 6 Sb 2.796E+00
Sh G = 2.1368E-01 a.dh/(1-e) 4.1067E+00 K G.a = 2.4504E+00 a = 2.2821E+03 (s-1)(m-1)