Water flow measurement | Water utilization, introduction, and how to save water (English version)

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1. Representative Papers of Cheng Zhenmin

1.Cheng, Z. M., X. C. Fang, R. H. Zeng, B. P. Han, L. Huang, and W. K. Yuan,“Deep Removal of Sulfur and Aromatics from Diesel through Two-Stage Concurrently and Countercurrently Operated Fixed-Bed Reactors”,Chem. Eng. Sci., 59 (22-23): 5465-5472 (2004).2. Fang, X. C., Z. M. Cheng, L. Huang, B. P. Han, R. H. Zeng, and W. K. Yuan, “Flooding Velocity Prediction in a Trickle Bed,” Int. J. Multiphase Flow, 31(5): 666-673 (2005).3. Zhou, Z. M., Z. M. Cheng, Z. Li, W. K. Yuan,“Determination of Effectiveness Factor of a Partial Internal Wetting Catalyst from Adsorption Measurement”,Chem. Eng. Sci., 59: 4305 (2004).4. Zhou, Z. M., Z. M. Cheng, Z. Li, W. K. Yuan, “Simulating Upflow Multiphase Packed Bed Reactor with Continuous Phase Transition”, Chem. Eng. Sci., 2004 (in press).5. Yuan, P. Q., Z. M. Cheng, W. L. Jiang, R. Zhang, and W. K. Yuan, “Catalytic desulfurization of hydrocarbon through partial oxidation in supercritical water,” Journal of Supercritical Fluids, in press (2004).6. Cheng, Z. M., W. K. Yuan and S. K. Bhatia, “Unconventional Operation of Three-Phase Fixed-Bed Reactors: A Perspective Trend in Reaction Engineering,” Trends in Chemical Engineering, Vol.8 (2003) 35~59.7. Cheng, Z. M., A. M. Anter, X. C. Fang, Q. Xiao, W. K. Yuan and S. K. Bhatia, “ Dryout Phenomena in a Three-Phase Fixed-Bed Reactor, ” AIChE Journal, 49 (1): 225-231 (2003).8. Cheng, Z. M., F. D. Yu, G. Grevillot, L. Luo, W. K. Yuan, and D. Tondeur, “Redistribution of adsorbed VOCs in activated carbon under electrothermal desorption, ” AIChE Journal, 48 (5): 1132-1138 (2002).9. Cheng, Z. M., and W. K. Yuan, “ Influence of Hydrodynamic Parameters on Performance of a Multiphase Fixed-Bed Reactor u

water flow measurement
nder Phase Transition, ” Chem. Eng. Sci., 57 (16): 3407-3413 (2002).10. Cheng, Z. M., A. M. Anter, and W. K. Yuan, “Intensification of Phase Transition on Multiphase Reactions, ” AIChE Journal, 47(5):1185-1192 (2001).11. Cheng, Z. M., A, M, Anter, G. M. Khalifa, J. S. Hu, Y. C. Dai and W. K. Yuan, “An innovative reaction heat offset operation for a multiphase fixed bed reactor dealing with volatile compounds,” Chem. Eng. Sci., 56(21-22), 6025-6030 (2001).12. Xiao, Q., Z. M. Cheng, Z. X. Jiang, A. M. Anter, and W. K. Yuan, “Hydrodynamic behavior of a trickle bed reactor under “forced” pulsing flow,” Chem. Eng. Sci., 56(3): 1189-1195 (2001).13. Xiao, Q., A. M. Anter, Z. M. Cheng, and W. K. Yuan, “New Correlation of Dynamic Liquid Holdup in a Trickle Bed,” Chem. Eng. Journal, 78: 125-129 (2000).14. Cheng, Z. M. and W. K. Yuan, “ Necessary Condition for Pulsing Flow Inception in a Trickle Bed,” AIChE Journal, 45(7): 1394-1400 (1999).15. Li, Y. X., Z. M. Cheng, and W.K. Yuan, “Catalytic Oxidation of Dilute SO2 over Activated Carbon Coupled with Partial Liquid Phase Vaporization,” Chem. Eng. Sci., 54:1571-1576 (1999).16. Cheng, Z. M. and W. K. Yuan, “Estimating Radial Velocity of Fixed Beds with Low Tube-To-Particle Diameter Ratios,” AIChE Journal, 43(5): 1319-1324(1997).17. Cheng, Z. M. and W. K. Yuan, “Lumped Kinetics of Fixed-Bed Reactors,” Progr. Nature Sci., 7(1): 51-57 (1997).18. Cheng, Z. M. and W. K. Yuan, “Initial Estimation of Heat Transfer and Kinetic Parameters of a Wall Cooled Fixed-Bed Reactor,” Compt. Chem. Eng., 21(5): 511-519(1997).19. Cheng, Z. M. and W.K. Yuan, Simultaneous Estimation of Kinetic and Heat Transfer Parameters of a Wall-cooled Fixed-Bed Reactor, Chem. Eng. Sci., 51 (21): 4791-4800 (1996).

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