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Gas entrainment rate and flow characterization in downcomer of a Jameson cell

Wybrane pełne teksty z tego czasopisma
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The Jameson cell which is a new type of gas-liquid contacting device and can be considered as a type of plunging jet column, has been in use worldwide for the separation of fine minerals, coal particles and wastewater treatment etc. Flow characteristics in the downcomer of a Jameson cell are very important since the hydrodynamics of the cell is largely depends on the flow conditions. The hydrodynamics influences flow regimes in the downcomer and hence the gas holdup and bubble diameter are strongly affected by flow conditions. Depending on the air entrainment rate entered to the system, different flow regimes are observed in the downcomer. Bubbly flow which is observed at less air quantities is desired instead of churn-turbulent flow where the gas entrainment rate increase. In this research, the effect of operating conditions including nozzle diameter, downcomer diameter, jet velocity and jet length on gas entrainment rate, Qg , was evaluated experimentally for an air-water system for the bubbly and churn-turbulent flow. Between these factors, downcomer diameter was found to have very little effect on gas entrainment rate while increasing values of other factors had an increasing effect on it. The results were evaluated by forward stepwise linear regression (MLR) and a piecewise regression with Quasi-Newton estimation of breakpoint (PLR) to estimate the flow conditions and gas entrainment rates. The model by PLR was useful to understand the boundary of the flow characteristics since the two equations were valid in a certain air entrainment ranges, i.e. different flow conditions. The model developed was successful to determine the transition region from bubbly flow to churn-turbulent flow. Experimental data were in good agreement with theoretically predicted value.
Rocznik
Tom
Strony
61--78
Opis fizyczny
Bibliogr. 30 poz.
Twórcy
autor
autor
autor
  • Eskişehir Osmangazi University, Dept. of Mining Engineering, Division of Mineral Processing, 26480, Eskişehir, Turkey, atasdem@ogu.edu.tr
Bibliografia
  • 1. ATKINSON, B.W., JAMESON, G.J., NGUYEN, A.V. and EVANS, G.M., 2003, Increasing Gas-Liquid Contacting Using a Confined Plunging Liquid Jet, Journal of Chemical Technology and Biotechnology, 78: 269-275.
  • 2. BIN, A.K., 1993, Gas Entrainment by Plunging Liquid Jets. Chemical Engineering Science. 48(21): 3585-3630.
  • 3. BROZEK, M. and MLYNARCZYKOWSKA, A., 2010, Probability of Detachment of Particle Determined According to the Stochastic Model of Flotation Kinetics, Physicochemical Problems of Mineral Processing, 44: 23-34.
  • 4. ÇINAR, M., ŞAHBAZ, O., ÇINAR, F., KELEBEK, Ş. and ÖTEYAKA, B., 2007, Effect of Jameson Cell Operating Variables and Design Characteristics on Quartz Dodecylamine Flotation System, 20: 1391-1396.
  • 5. EVANS, G.M., 1990, A Study of a Plunging Jet Bubble Column, Ph. D. Thesis, Newcastle University, Australia.
  • 6. EVANS, G.M. and JAMESON G.J., 1995, Hydrodynamics of a Plunging Liquid Jet Bubble Column, Chemical Engineering Research & Design, 73: 679-684.
  • 7. EVANS, G.M., ATKINSON, B.W. and JAMESON, G.J., 1995, The Jameson Cell, Flotation Science and Engineering, Edited by K.A. Matis, 331-363.
  • 8. EVANS, G.M., ATKINSON, B.W. and JAMESON, G.J., 1996, Recent Advances in Jameson Cell Technology, Column’96, 39-49.
  • 9. EVANS, G.M., BIN, A. K., and MACHNIEWSKI, 2001, Performance of Confined Plunging Liquid Jet bubble Column as a Gas-liquid Reactor, Chemical Engineering Science, 56: 1151-1157.
  • 10. FUNATSU, K., HSU, Y. and KAMOGAWA, T., 1988, Gas Holdup and Gas Entrainment of a Plunging Water Jet with a Constant Entrainment Guide, Can. J. Chem. Eng., 66: 19-28.
  • 11. JAMESON, G.J. and MANLAPIG, E.V., 1991, Applications of the Jameson Cell, Column'91, Proceedings of an International Conference on Column Flotation, Sudbury, Ontario, 673-687.
  • 12. JAMESON, G.J., 1999, Hydrophobicity and Floc Density in Induced-Air Flotation for Water Treatment, Colloids Surfaces A: Physicochem. Eng. Asp, 151: 269-281.
  • 13. KANTARCI, N., BORAK, F. and ULGEN, K.O., 2005, Bubble Column Reactors, Process Biochemistry, 40: 2263-2283.
  • 14. KUSABIRAKI, D., NIKI, H., YAMAGIWA, K. and OHKAWA, A., 1990, Gas Entrainment Rate and Flow Pattern of Vertical Plunging Jets, Can. J. Chem. Eng., 68: 893-901.
  • 15. LIU, G. and EVANS, G.M.,1998, Gas Entrainment and Gas Holdup in a Confined plunging Liquid Jet Reactor, Proceedings of the 26th Australasian Chemical Engineering Conference, (Chemeca 98), Port Douglas, Australia.
  • 16. MANDAL, A., KUNDU, G. and MUKHERJEE, D., 2003, Gas Holdup and Entrainment Characteristics in a Modified Downflow Bubble Column with Newtonian and Non-Newtonian Liquid, Chemical Engineering and Processing, 42: 777-787.
  • 17. MANDAL, A., KUNDU, G. and MUKHERJEE, D., 2005, Comparative Study of Two-Phase Gas-Liquid Flow in the Ejector Induced Upflow and Downflow Bubble Column, International Journal of Chemical Reactor Engineering, 3: 1-13.
  • 18. MOHANTY, M.K. and HONAKER, R.Q., 1999, Performance Optimization of Jameson Flotation Technology for Fine Coal Cleaning, Minerals Engineering, 12(4): 367-381.
  • 19. OHKAWA, A., SHIOKAWA, Y., SAKAI, N. and IMAI, H., 1985, Flow Characteristics of Downflow Bubble Columns with Gas Entrainment by a Liquid Jet, j. Chem. Eng. Japan, 18: 466-469.
  • 20. OHKAWA, A., KUSABIRAKI, D., KAWAI, Y. and SAKAI, N.,1986, Some Flow Characteristics of a Vertical Liquid Jet System Having Downcomers, Chem. Eng. Sci., 41: 2347-2361.
  • 21. OHKAWA, A., KUSABIRAKI, D., KAWAI, Y. and SAKAI, N., 1987, Flow Characteristics of an Air-entrainment Type Aerator Having a Long Downcomer, Chem. Eng. Sci., 42: 2788-2790.
  • 22. SANCHEZ-PINO, S.E. and MOYS, M.H., 1991, Characterization of Co-Current Downwards Flotation Columns, Column’91, 1: 341-355.
  • 23. ŞAHBAZ, O., ÖTEYAKA, B., KELEBEK, Ş., UÇAR, A. and DEMİR, U., 2008, Separation of Unburned Carbonaceous Matter in Bottom Ash Using Jameson Cell, Separation and Purification Technology, 62: 103-109.
  • 24. TAŞDEMIR, A., TAŞDEMIR, T., and ÖTEYAKA, B., 2007a, The Effect of Particle Size and Some Operating Parameters in the Separation Tank and the Downcomer on the Jameson Cell Recovery, Minerals Engineering, 20: 1331-1336.
  • 25. TAŞDEMIR, T., ÖTEYAKA, B. and TAŞDEMIR, A., 2007b, Air Entrainment Rate and Holdup in the Jameson Cell, Minerals Engineering, 20/8: 761-765.
  • 26. STATISTICA 8.0, StatSoft Inc., 1984-2007.
  • 27. VIAL C., PONCIN, S., WILD, G. and MIDOUX, N., 2001, A Simple Method for Regime Identification and Flow Characterization in Bubble Columns and Airlift Reactors, Chemical Engineering and Processing, 40: 135-151.
  • 28. WILD, G., PONCIN, S., LI, H. and OLMOS, E., 2003, Some Aspects of the Hydrodynamics of Bubble columns, International Journal of Chemical Reactor Engineering, 1: 1-36.
  • 29. YAMAGIWA, K., KUSABIRAKI, D. and OHKAWA, A., 1990, Gas Holdup and Gas Entrainment Rate in Downflow Bubble Column with Gas Entrainment by a Liquid Jet Operating at High Liquid Throughput, J. Chem. Eng. Japan, 23: 343-348.
  • 30. YAN, Y.D. and JAMESON, G.J., 2004, Application of the Jameson Cell Techonology for Algae and Phosphorus Removal from Maturation Ponds, Int. J. Miner. Process., 73: pp 23-28.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BAT2-0003-0033
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