-
1
-
-
0009569176
-
Mathematical models for the transient behavior of a packed bed reactors
-
Feick, J. & Quon, D. (1970). Mathematical models for the transient behavior of a packed bed reactors. Can. J. Chem. Eng. 48, 205-211.
-
(1970)
Can. J. Chem. Eng.
, vol.48
, pp. 205-211
-
-
Feick, J.1
Quon, D.2
-
2
-
-
0026918514
-
Trickle-bed reactor: State of art and perspectives
-
Gianetto, A. & Specchia, V. (1992). Trickle-bed reactor: State of art and perspectives. Chem. Eng. Sci., 47 (13-14), 3197-3213.
-
(1992)
Chem. Eng. Sci.
, vol.47
, Issue.13-14
, pp. 3197-3213
-
-
Gianetto, A.1
Specchia, V.2
-
3
-
-
0020549905
-
Trickle-bed reactors: A review
-
Herskowitz, M. & Smith, J.M. (1983). Trickle-bed reactors: A review. A.I.Ch.E. J., 29 (1), 1-18.
-
(1983)
A.I.Ch.E. J.
, vol.29
, Issue.1
, pp. 1-18
-
-
Herskowitz, M.1
Smith, J.M.2
-
6
-
-
0017994437
-
Solid-liquid mass transfer in concurrent two-phase flow through packed beds
-
Specchia, V., Baldi, G. & Gianetto, A. (1978). Solid-liquid mass transfer in concurrent two-phase flow through packed beds. Ind. Eng. Chem. Process. Des. Dev., 17 (3), 362-367.
-
(1978)
Ind. Eng. Chem. Process. Des. Dev.
, vol.17
, Issue.3
, pp. 362-367
-
-
Specchia, V.1
Baldi, G.2
Gianetto, A.3
-
8
-
-
0030131418
-
Modelling of three phase catalytic upflow reactor: A significant chemical determination of liquid-solid and gaz-liquid mass transfer coefficients
-
Stueber, F., Wilhelm, A.M. & Delmas, H. (1996). Modelling of three phase catalytic upflow reactor: A significant chemical determination of liquid-solid and gaz-liquid mass transfer coefficients. Chem. Eng. Sci., 51 (10), 2161-2167.
-
(1996)
Chem. Eng. Sci.
, vol.51
, Issue.10
, pp. 2161-2167
-
-
Stueber, F.1
Wilhelm, A.M.2
Delmas, H.3
-
10
-
-
84984082547
-
Prediction of pressure drop for two-phase, two-component concurrent flow in packed beds
-
Turpin, J.L. & Huntington, R.L. (1967). Prediction of pressure drop for two-phase, two-component concurrent flow in packed beds. A.I.Ch.E. J., 13 (6), 1196-1202.
-
(1967)
A.I.Ch.E. J.
, vol.13
, Issue.6
, pp. 1196-1202
-
-
Turpin, J.L.1
Huntington, R.L.2
-
11
-
-
0028481297
-
Dynamic operation of a three-phase upflow reactor for the hydrogenation of phenylacetylene
-
Visser, J.B.M., Stankiewicz, A., Van Dierendonck, L.L., Manna, L., Sicardi, S. & Baldi, G. (1994). Dynamic operation of a three-phase upflow reactor for the hydrogenation of phenylacetylene. Catalysis Today, 20, 485-500.
-
(1994)
Catalysis Today
, vol.20
, pp. 485-500
-
-
Visser, J.B.M.1
Stankiewicz, A.2
Van Dierendonck, L.L.3
Manna, L.4
Sicardi, S.5
Baldi, G.6
-
12
-
-
0029753072
-
Dynamic modelling of catalytic three phase reactors
-
Waerna, J. & Salmi, T. (1996). Dynamic modelling of catalytic three phase reactors. Comput. Chem. Eng., 20 (1), 39-47.
-
(1996)
Comput. Chem. Eng.
, vol.20
, Issue.1
, pp. 39-47
-
-
Waerna, J.1
Salmi, T.2
-
13
-
-
0025211438
-
Modelling and design of industrial reactors with a stationary bed of catalyst and two-phase gas-liquid flow - A review
-
Zhukova, T.B., Pisarenko, V.N. & Kafarov, V.V. (1990). Modelling and design of industrial reactors with a stationary bed of catalyst and two-phase gas-liquid flow - A review. Int. Chem. Eng. 30 (1), 57-102.
-
(1990)
Int. Chem. Eng.
, vol.30
, Issue.1
, pp. 57-102
-
-
Zhukova, T.B.1
Pisarenko, V.N.2
Kafarov, V.V.3
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