Trickle-bed reactors: state of art and perspectives
暂无分享,去创建一个
[1] Y. Shah,et al. The Role of Liquid Holdup, Effective Catalyst Wetting, and Backmixing on the Performance of a Trickle Bed Reactor for Residue Hydrodesulfurzation , 1975 .
[2] C. Satterfield,et al. Liquid‐solid mass transfer in packed beds with downward concurrent gas‐liquid flow , 1978 .
[3] Yuji Sato,et al. LIQUSD PHASE MASS TRANSFER IN PACKED BED REACTOR WITH COCURRENT GAS-LIQUID DOWNFLOW , 1974 .
[4] J. M. Smith,et al. Mass Transfer and Contacting Efficiency in a Trickle-Bed Reactor , 1978 .
[5] N. Midoux,et al. Hydrodynamics and interfacal areas in downward cocurrent gas-iquid flow through fixed beds - Influence of the nature of the liquid. , 1982 .
[6] C. Kenney,et al. Partial wetting in trickle bed reactors — the reduction of crotonaldehyde over a palladium catalyst , 1973 .
[7] J. Smith,et al. Effectiveness factors and mass transfer in trickle-bed reactors , 1979 .
[8] S. Jaffe. Hot Spot Simulation in Commercial Hydrogenation Processes , 1976 .
[9] 悟 小林,et al. 充填層内下降 2 相流の流動と液混合 , 1979 .
[10] J. M. Smith,et al. Liquid distribution in trickle‐bed reactors: Part I. Flow measurements , 1978 .
[11] Peter L. Silveston,et al. Thermal waves in the periodic operation of a trickle-bed reactor , 1990 .
[12] V. Specchia,et al. Hydrodynamics and solid‐liquid contacting effectiveness in trickle‐bed reactors , 1978 .
[13] Hiroshi Takeuchi,et al. Liquid distribution in a packed column , 1973 .
[14] V. Specchia,et al. Absorption in packed towers with concurrent upward flow , 1974 .
[15] Andrzej Burghardt,et al. Experimental studies of liquid—solid wetting efficiency in trickle-bed cocurrent reactors , 1990 .
[16] S. Goto,et al. Mass Transfer in Packed Beds with Two-Phase Flow , 1975 .
[17] A. Drinkenburg,et al. Transition to pulsing flow, holdup and pressure drop in packed columns with cocurrent gas-liquid downflow , 1983 .
[18] D. Luss,et al. Packed Bed Liquid Phase Dispersion in Pulsed Gas-Liquid Downflow , 1980 .
[19] Yuji Sato,et al. LIQUID-TO-PARTICLE MASS TRANSFER IN FIXED BED REACTOR WITH COCURRENT GAS-LIQUID DOWNFLOW , 1976 .
[20] H. Hofmann,et al. Influence of gas velocity and packing geometry on pulsing inception in trickle-bed reactors , 1980 .
[21] Milorad P. Dudukovic,et al. Evaluation of liquid‐solid contacting in trickle‐bed reactors by tracer methods , 1981 .
[22] M. Herskowitz,et al. Global rates of reaction in trickle-bed reactors: effects of gas and liquid flow rates , 1983 .
[23] S. Fukushima,et al. Liquid-phase volumetric and mass-transfer coefficient, and boundary of hydrodynamic flow region in packed column with cocurrent downward flow. , 1977 .
[24] G. Tosun. A study of cocurrent downflow of nonfoaming gas-liquid systems in a packed bed. 1. Flow regimes: search for a generalized flow map , 1984 .
[25] Faïçal Larachi,et al. Experimental study of a trickle-bed reactor operating at high pressure: two-phase pressure drop and liquid saturation , 1991 .
[26] André Laurent,et al. A new, improved pressure drop correlation for trickle-bed reactors , 1988 .
[27] P. Marchot,et al. LIQUID FLOW MALDISTRIBUTIONS IN TRICKLE-BED REACTORS , 1980 .
[28] V. G. Rao,et al. SOLID-LIQUID MASS-TRANSFER IN PACKED-BEDS WITH COCURRENT GAS-LIQUID DOWNFLOW , 1985 .
[29] Gabriel Wild,et al. The Hydrodynamic Characteristics of Cocurrent Downflow and Cocurrent Upflow Gas-Liquid-Solid Catalytic Fixed Bed Reactors: the Effect of Pressure , 1991 .
[30] K. Onda,et al. Effect of Packing Materials on the Wetted Surface Area , 1967 .
[31] A. Germain,et al. Experimental Study of a Catalytic Trickle Bed Reactor , 1975 .
[32] E. Nowak,et al. A diagnostic test of the kinetic regime in a packed bed reactor , 1967 .
[33] V. Specchia,et al. Distribution and radial spread of liquid in packed towers with two-phase concurrent flow: effect of packing shape and size , 1976 .
[34] J. Hochman,et al. Two-Phase Cocurrent Downflow in Packed Beds , 1969 .
[35] Silvio Sicardi,et al. Flow regime transition in trickle bed reactors , 1979 .
[36] J. Charpentier. Recent progress in two phase gas—liquid mass transfer in packed beds , 1976 .
[37] J. Smith,et al. Hydration of isobutene in a trickle‐bed reactor: Wetting efficiency and mass transfer , 1987 .
[38] Klaas R. Westerterp,et al. The influence of pressure on the liquid hold-up in a cocurrent gas-liquid trickle-bed reactor operating at low gas velocities , 1991 .
[39] J. M. Smith,et al. Oxidation of sulfur dioxide in a trickle-bed reactor , 1981 .
[40] J. Levec,et al. Solid‐liquid mass transfer in packed beds with cocurrent downward two‐phase flow , 1990 .
[41] J. Smith,et al. Trickle-Bed Oxidation Reactors , 1978 .
[42] D. Mears,et al. Tests for Transport Limitations in Experimental Catalytic Reactors , 1971 .
[43] Ka Ming Ng,et al. A model for flow regime transitions in cocurrent down‐flow trickle‐bed reactors , 1986 .
[44] J. Hanika,et al. Measurement of axial temperature profiles in an adiabatic trickle bed reactor , 1976 .
[45] V. Specchia,et al. Packing wetting in trickle bed reactors: Influence of the gas flow rate , 1981 .
[46] V. Specchia,et al. Absorption in packed towers with concurrent downward high-velocity flows: II - Mass transfer , 1973 .
[47] Yuji Sato,et al. FLOW PATTERN AND PULSATION PROPERTIES OF COCURRENT GAS-LIQUID DOWNFLOW IN PACKED BEDS , 1973 .
[48] Y. Shah,et al. Communications - Effect of Catalyst Particle Size on Performance of a Trickle Bed-Reactor , 1977 .
[49] H. Hofmann,et al. Multiphase Catalytic Packed-Bed Reactors , 1978 .
[50] Y. Shah,et al. Effect of Holdup Incomplete Catalyst Wetting and Backmixing during Hydroprocessing in Trickle Bed Reactors , 1975 .
[51] J. Smith,et al. A dynamic method for liquid‐particle mass transfer in trickle beds , 1982 .
[52] Klaas R. Westerterp,et al. Hydrodynamics in a cocurrent gas-liquid trickle bed at elevated pressures , 1991 .
[53] P. L. Silveston,et al. Periodic operation of a trickle‐bed reactor , 1989 .
[54] Klaas R. Westerterp,et al. The transition between trickle flow and pulse flow in a cocurrent gas—liquid trickle-bed reactor at elevated pressures , 1990 .
[55] G. Baldi,et al. Solid-Liquid Mass Transfer in Concurrent Two-Phase Flow through Packed Beds , 1978 .
[56] V. Specchia,et al. Catalyst areas wetted by flowing and semistagnant liquid in trickle-bed reactors , 1980 .
[57] S. Mochizuki,et al. Liquid—solid mass transfer rate in liquid-gas upward cocurrent flow in packed beds , 1974 .
[58] D. Mears,et al. The role of axial dispersion in trickle-flow laboratory reactors , 1971 .
[59] M. A. Latifi,et al. Hydrodynamic study of a trickle-bed reactor by means of microelectrodes: analysis of the probability densities , 1992 .
[60] D. Luss,et al. Transition to Pulsed Flow in Mixed-Phase Cocurrent Downflow through a Fixed Bed , 1977 .
[61] A. E. Sáez,et al. Static liquid holdup in packed beds of spherical particles , 1991 .
[62] Silvio Sicardi,et al. Solid-liquid contacting effectiveness in trickle bed reactors , 1976 .
[63] Milorad P. Dudukovic,et al. A new tracer method for determination of liquid‐solid contacting efficiency in trickle‐bed reactors , 1976 .
[64] C. Satterfield,et al. Direct solid‐catalyzed reaction of a vapor in an apparently completely wetted trickle bed reactor , 1973 .
[65] C. Prater,et al. The temperature produced by heat of reaction in the interior of porous particles , 1958 .
[66] K. Westerterp,et al. The influence of the reactor pressure on the hydrodynamics in a cocurrent gas-liquid trickle-bed reactor , 1990 .
[67] Sankaran Sundaresan,et al. Onset of pulsing in two‐phase cocurrent downflow through a packed bed , 1988 .
[68] J. Charpentier,et al. Some liquid holdup experimental data in trickle-bed reactors for foaming and nonfoaming hydrocarbons , 1975 .
[69] Charles N. Satterfield,et al. Trickle‐bed reactors , 1975 .
[70] J. Turpin,et al. Prediction of pressure drop for two‐phase, two‐component concurrent flow in packed beds , 1967 .
[71] H. C. Henry,et al. Scale Up of Pilot Plant Data for Catalytic Hydroprocessing , 1973 .
[72] Vito Specchia,et al. Pressure drop and liquid holdup for two-phase concurrent flow in packed beds , 1977 .