The Role of Liquid Holdup and Effective Wetting in the Performance of Trickle-Bed Reactors
暂无分享,去创建一个
[1] C. Kenney,et al. Partial wetting in trickle bed reactors — the reduction of crotonaldehyde over a palladium catalyst , 1973 .
[2] J. Villermaux,et al. Residence time distribution in the liquid phase of trickle flow in packed columns , 1969 .
[3] P. F. Way,et al. The role of the liquid phase in the performance of a trickle bed reactor , 1972 .
[4] I. Furzer,et al. Liquid‐phase dispersion in packed beds with two‐phase flow , 1970 .
[5] J. Hochman,et al. Two-Phase Cocurrent Downflow in Packed Beds , 1969 .
[6] A. Vogelpohl,et al. Effective interfacial area in irrigated packed columns , 1974 .
[7] E. V. Murphree,et al. Application of Contacting Studies to the Analysis of Reactor Performance , 1964 .
[8] K. Okada,et al. Liquid Holdup in Packed Towers , 1953 .
[9] H. C. Henry,et al. Scale Up of Pilot Plant Data for Catalytic Hydroprocessing , 1973 .
[10] Thomas K. Sherwood,et al. Mass transfer limitations in a trickle‐bed reactor , 1969 .
[11] V. E. Sater,et al. Two-Phase Flow in Packed Beds. Evaluation of Axial Dispersion and Holdup by Moment Analysis , 1966 .
[12] I. Furzer,et al. Mixing in trickle flow through packed beds , 1972 .
[13] H. Gelbe. A new correlation for liquid holdup in packed beds , 1968 .
[14] D. Mears,et al. The role of axial dispersion in trickle-flow laboratory reactors , 1971 .
[15] G. S. Laddha,et al. Prediction of liquid phase hold-up in random packed beds , 1965 .
[16] J. Buchanan. Holdup in Irrigated Ring-Packed Towers below the Loading Point , 1967 .
[17] C. Satterfield,et al. Direct solid‐catalyzed reaction of a vapor in an apparently completely wetted trickle bed reactor , 1973 .