Intensification of phase transition on multiphase reactions

AIChE Journal

Volumn 47, Issue 5, 2001, Pages 1185-1192

  Cheng, Zhen Min ^a   Anter, Abdulhakeim M ^a   Yuan, Wei Kang ^a  

^a EAST CHINA UNIVERSITY OF SCIENCE AND TECHNOLOGY   (China)

Author keywords

[No Author keywords available]

Indexed keywords

BENZENE; CATALYSTS; EVAPORATION; HYDROGENATION; POROUS MATERIALS; QUENCHING;

PROCESS INTENSIFICATION;

PHASE TRANSITIONS;

BENZENE;

GAS FLOW; HYDROGENATION; LIQUID FLOW; MULTIPHASE FLOW; TEMPERATURE EFFECT; VOLATILE ORGANIC COMPOUND;

ARTICLE; CATALYST; CHEMICAL ENGINEERING; CHEMICAL REACTION; EVAPORATION; EXPERIMENTATION; FLOW KINETICS; FLOW RATE; GAS; HEAT TRANSFER; HYDROGENATION; LIQUID; PHASE TRANSITION; PRESSURE; TEMPERATURE;

EID: 0035334294     PISSN: 00011541     EISSN: None     Source Type: Journal    
DOI: 10.1002/aic.690470524     Document Type: Article

References (28)

1. Bhatia, S. K., "Steady State Multiplicity and Partial Internal Wetting of Catalyst Particles," AIChE J., 34, 969 (1988).
2. Bhatia, S. K., "Partial Internal Wetting of Catalyst Particles with a Distribution of Pore Size," AIChE J., 35, 1337 (1989).
3. Charpentier, J. C., and M. Favier, "Some Liquid Holdup Experimental Data in Trickle-Bed Reactors for Foaming and Nonfoaming Hydrocarbons," AIChE J., 21, 1213 (1975).
4. Cheng, Z. M., and W. K. Yuan, "Necessary Condition for Pulsing Flow Inception in a Trickle Bed," AIChE J., 45, 1394 (1999).
5. Cheng, Z. M., W. K. Yuan, A. M. Anter, and J. S. Hu, "A New Technology for Benzene Hydrogenation into Cyclohexane via Phase Transition," Chinese Patent Application, No. 00111762.9 (March 2, 2000).
6. Eigenberger, G., and U. Wegerle, "Runaway in an Industrial Hydrogenation Reactor," Proc. Int. Symp. on Chemical Reaction Engineering, Boston (1982).
7. Ellman, M. J., N. Midoux, G. Wild, A. Laurent, and J. C. Charpentier, "A New, Improved Liquid Hold-Up Correlation for Trickle-Bed Reactors," Chem. Eng. Sci., 45, 1677 (1990).
8. Funk, G. A., M. P. Harold, and K. M. Ng, "A Novel Model for Reaction in Trickle Beds with Flow Maldistribution," Ind. Eng. Chem. Res., 29, 738 (1990).
9. Hanika, J., K. Sporka, V. Ruzicka, and J. Krausova, "Qualitative Observations of Heat and Mass Transfer Effects on the Behaviour of a Trickle Bed Reactor," Chem. Eng. Commun., 2, 19 (1975).
10. Hanika, J., K. Sporka, V. Ruzicka, and J. Hrstka, "Measurement of Axial Temperature Profiles in an Adiabatic Trickle Bed Reactor," Chem. Eng. J., 12, 193 (1976).
11. Hanika, J., K. Sporka, V. Ruzicka, and R. Pistek, "Dynamic Behavior of an Adiabatic Trickle Bed Reactor," Chem. Eng. Sci., 32, 525 (1977).
12. Hanika, J., B. N. Lukjanov, V. A. Kirillov, and V. Stanek, "Hydrogenation of 1,5-Cyclooctadiene in a Trickle Bed Reactor Accompanied by Phase Transition," Chem. Eng. Commun., 40, 183 (1986).
13. Hanika, J., "Safe Operation and Control of Trickle-Bed Reactor," Chem. Eng. Sci., 54, 4653 (1999).
14. Hu, R., and T. C. Ho, "Steady State Multiplicity in an Incompletely Wetted Catalyst Particle," Chem. Eng. Sci., 23, 1239 (1987).
15. Jaguste, D. N., and S. K. Bhatia, "Partial Internal Wetting of Catalyst Particles: Hysteresis Effects," AIChE J., 37, 650 (1991).
16. Khadilkar, M. R., P. L. Mills, and M. P. Dudukovic, "Trickle-Bed Reactor Models for Systems with a Volatile Liquid Phase," Chem. Eng. Sci., 54, 2421 (1999).
17. Kheshgi, H. S., S. C. Reyes, R. Hu, and T. C. Ho, "Phase Transition and Steady-State Multiplicity in a Trickle-Bed Reactor," Chem. Eng. Sci., 47, 1771 (1992).
18. Kim, D. H., and Y. G. Kim, "An Experimental Study of Multiple Steady States in a Porous Catalyst due to Phase Transition," J. Chem. Eng. Jpn., 14, 311 (1981a).
19. Kim, D. H., and Y. G. Kim, "Simulation of Multiple Steady States in a Porous Catalyst due to Phase Transition," J. Chem. Eng. Jpn., 14, 318 (1981b).
20. Lange, R., J. Hanika, D. Stradiotto, R. R. Hudgins, and P. L. Silveston, "Investigations of Periodically Operated Trickle-Bed Reactors," Chem. Eng. Sci., 49, 5615 (1994).
21. Ng, K. M., "A Model for Flow Regime Transitions in Concurrent Down-Flow Trickle-Bed Reactors," AIChE J., 32, 115 (1986).
22. Satterfield, C. N., and F. Ozel, "Direct Solid-Catalyzed Reaction of a Vapor in an Apparently Completely Wetted Trickle Bed Reactor," AIChE J., 19(6), 1259 (1973).
23. Sedriks, W., and C. N. Kenney, "Partial Wetting in Trickle Bed Reactors - The Reduction of Crotonaldehyde over a Palladium Catalyst," Chem. Eng. Sci., 28, 559 (1973).
24. Shah, Y. T., Gas-Liquid-Solid Reactor Design, McGraw-Hill, New York (1979).
25. Stanek, V., J. Hanika, V. Hlavacek, and O. Trnka, "The Effect of Liquid Flow Distribution on the Behavior of a Trickle Bed Reactor," Chem. Eng. Sci., 36, 1045 (1981).
26. Turpin, J. L., and R. L. Huntington, "Prediction of Pressure Drop for Two-Phase, Two-Component Concurrent Flow in Packed Beds," AIChE J., 13, 1196 (1967).
27. Watson, P. C., and M. P. Harold, "Dynamic Effects of Vaporization with Exothermic Reaction in a Porous Catalyst Pellet," AIChE J., 39, 989 (1993).
28. Watson, P. C., and M. P. Harold, "Rate Enhancement and Multiplicity in a Partially Wetted and Filled Pellet: Experimental Study," AIChE J., 40, 97 (1994).