Tytuł artykułu
Autorzy
Identyfikatory
Warianty tytułu
Wpływ koncentracji ciała stałego na profile prędkości i zużycie mocy w reaktorze strumienicowo-pętlicowym
Języki publikacji
Abstrakty
Experimental investigations of liquid velocity distributions and power input in a jet-loop reactor have been carried out on a semi-industrial scale. The effect of solids concentrations on the liquid velocity distributions and the power input in the reactor is determined. It was found that solids reduce liquid flow velocity along the draft tube by 30%. Profiles of liquid velocity are flattened due to the presence of solids but dependent on the particle size. This effect increases with the decrease of the particle diameter and with the increase of the liquid flow rate. Radial velocity profiles are described by Schlichtings correlation. Power input is found to increase slightly with the solids concentration.
Przedstawiono wyniki badań rozkładu prędkości płynu oraz zużycia mocy wykonanych za pomocą reaktora strumienicowo-pętlicowego w skali półtechnicznej, w układzie trójfazowym gazcieczciało stałe. Zanalizowano wpływ koncentracji ciała stałego na rozkład profilu prędkości oraz zużycie mocy w reaktorze. Obecność ziaren ciała stałego powodowała ponad 30% zmniejszenie prędkości przepływu cieczy w rurze wznoszącej oraz spłaszczenie profili prędkości zależne od średnicy cząstek. Efekt ten zwiększał się wraz ze zmniejszeniem średnicy cząstek oraz wraz ze wzrostem prędkości przepływu płynu. Zużycie mocy wzrastało jedynie nieznacznie wraz ze wzrostem koncentracji ciała stałego. Promieniowe rozkłady prędkości opisano za pomocą korelacji Schlichtinga.
Słowa kluczowe
Czasopismo
Rocznik
Tom
Strony
33--45
Opis fizyczny
Bibliogr. 47 poz.
Twórcy
autor
- Institute of Chemical Engineering and Heating Equipment, Wrocław University of Technology
autor
- Institute of Chemical Engineering and Heating Equipment, Wrocław University of Technology
autor
- Institute of Chemical Engineering and Heating Equipment, Wrocław University of Technology
autor
- Institute of Environment Protection Engineering, Wrocław University of Technology
autor
- Institute of Environment Protection Engineering, Wrocław University of Technology
Bibliografia
- [1] KULKARNI A., SHAH Y.T., SCHUMPE A., Hydrodynamics and Mass Transfer in Downflow Bubble Column, Chem. Eng. Comm., 1983, 24,307.
- [2] TEBEL K.H., ZEHNER P., Fluid Dynamic Description of Jet-Loop Reactor in Multiphase Operation, Chemical Engineering & Technology, 1989, 12, 274.
- [3] WACHSMAN U., RAEBIGER N., VOGELPOHL A., The Compact Reactor - a Newly Developed Loop Reactor with a High Mass Transfer Performance, German Chemical Engineering, 1984,7, 39.
- [4] YENKIE M.K.N., GEISSEN S.U., VOGELPOHL A., Biokinetics of wastewater treatment in the high performance compact reactor (HCR), Chem. Eng. J., 1992,49 (1), B1-B12.
- [5] MALONE R.J., Loop Reactor Technology Improves Catalytic Hvdrogenation, Chem. Eng. Process., 1980, 76 (6), 53.
- [6] WACHSMAN U., RAEBIGER N., VOGELPOHL A., Effect of Geometry on Hydrodynamics and Mass Transfer in the Compact Reactor, German Chemical Engineering, 1985, 8, 411.
- [7] BHUTADA S.R., PANGARKAR V.G., Gas Induction and Hold-up Characteristics of Liquid jet Loop Reactors, Chem. Eng. Comm., 1987,61(1-6), 239.
- [8] BHUTADA S.R., PANGARKAR V.G., Solid Suspension and Mixing Characteristics of Liquid Jet Loop Reactors, Chem. Eng. Sci., 1989,44 (10), 2384.
- [9] DUTTA N.N., RAGHAVAN K.V., Mass Transfer and Hydrodynamic Characteristics of Loop Reactor with Downflow Liquid Jet Ejector, Chem. Eng. J., 1987, 36 (2), 111.
- [10] KMIEC A., KUCHARSKI J., SZCZEPANIAK L., SZYMANOWSKI W., Biotechnological Methods and Constructional Developments of Reactors for Sewage Utilization, Chemical & Apparatus Engineering, 1989, 28 (1), 3. *
- [11] JAIN D.K., PATWARI A.N., RAO M.B., KHAN A.A., Liquid Circulation Characteristics in Jet Loop Reactors, Can. J. Chem. Eng., 1990, 68 (6), 1047.
- [12] PADMAVATHI G., RAO K.R., Hydrodynamic Characteristics of Reversed Flow Jet Loop Reactor as a Gas-Liquid-Solid Contactor, Chem. Eng. Sci., 1991,46 (12), 3293.
- [13] VELAN M., RAMANUJAM T.K., Hydrodynamics in Down Flow Jet Loop Reactor, Can. J. Chem. Eng., 1991,69(6), 1257.
- [14] CRAMERS P.H.M.R., BEENACKERS A.A.C.M., VAN DIERENDONCK L.L. Hydrodynamics and Mass Transfer Characteristic of a Loop Venturi Reactor with a Downflow Liquid Jet Ejector, Chem. Eng. Sci., 1992,47(13/14), 3557.
- [15] GADD1S E.S., Hydrodynamics and Mass Transfer in an Impinging-Stream Loop Reactor Aerated from the Top, Chemical Engineering & Processing, 1994, 33 (4), 285.
- [16] PRASAD K.Y., RAMANUJAM T.K., Gas Hold-up and Overall Volumetric Mass Transfer Coefficients in a Modified Reversed Flow Jet Loop Reactor, Can. J. Chem. Eng., 1995, 73 (2), 190.
- [17] PRASAD K.Y., RAMANUJAM T.K., Enhancement of Gas-Liquid Mass Transfer in a Modified Reversed Flow Jet Loop Reactor With Three-Phase System, Chem. Eng. Sci., 1995, 50 (18), 2997.
- [18] VAN DIERENDONCK L.L., ZAHRADNIK J., LINEK V., Loop Venturi Reactor - A Feasible Alternative to Stirred Tank Reactors, Industry Engineering Chemistry Research, 1998, 37 (3), 734.
- [19] LEE S.YI., TSUI Y.P., Succeed at Gas/Liquid Contacting, Chem. Eng. Process., 1999, 95 (7), 23.
- [20] JIANPING W., LIN H., YONG Z., CHAO L., YUNLIN C, Solid-liquid mass transfer in a gas-liquid -solid three phase reversed flow jet loop reactor, Chem. Eng. J., 2000, 78 (2-3), 231.
- [21] FAN L.S., HWANG S.J., MATSUURA A., Hydrodynamic Behaviour of a Draft Tube Gas-Liquid-Solid Spouted Bed, Chem. Eng. Sci., 1984, 39 (12), 1677.
- [22] KARAMANEV D.G., NAGAMUNE T, ENDO I., Hydrodynamic and Mass Transfer Study of a Gas-Liquid-Solid Spouted Bed, Chem. Eng. Sci., 1992, 47 (13/14), 3581.
- [23] NITTA B.V. MORGAN III M.H., Particle Circulation and Liquid Bypassing in Three Phase Draft Tube Spouted Beds, Chem. Eng. Sci., 1992, 47 (13/14), 3459.
- [24] KUNDAKOVIC L., VUNJAK-NOVAKOVIC G., Mechanics of Particle Motion in Three-Phase Flow, Chem. Eng. Sci., 1995, 50 (20), 3285.
- [25] SADA E., KUMAZAWA H., LEE C.H., Influences of Suspended Fine Particles on Gas Hold-up and Mass Transfer Characteristics in a Slurry Bubble Column, AIChE J., 1986, 32 (5), 853.
- [26] SAUER TH., HEMPEL D.CH., Fluid Dynamics and Mass Transfer in a Bubble Column with Suspended Particles, Chemical Engineering & Technology, 1987, 10, 180.
- [27] SIEKMANN M., STEIFF A., WEINSPACH P.M., Dispersion der fluessigen Phase in einem dreiphasig betriebenen Strahlduesenreaktor, Chem. Ing. Techn., 1990, 62 (12), 1046.
- [28] SHAH Y.T., YANG N., CHARAT S.D., WISECARVER K., Circulation in Large Scale Jet Bubble Column, Chem. Eng. Comm., 1991,110,53.
- [29] SHAH Y.T., WISECARVER K., BOROLE A., SALAZAR B., JOSHI B., GUITIAN J., Hydrodynamics, Mixing and Mass Transfer in a Large Diameter Jet Bubble Column, Chem. Eng. Comm., 1995, 136, 95.
- [30] KoiDE K., Design Parameters of Bubble Column Reactors with and without Solid Suspension, A Review, J. Chem. Eng. Japan, 1996, 29 (5), 745.
- [31] SCHUEGERL K., Three Phase-Bioftuidization - Application of Three-Phase Fluidization in the Biotechnology, A Review, Chem. Eng. Sci., 1997, 52 (21/22), 3661.
- [32] JIANPING W., SHONGUN X., Local Hydrodynamics in a Gas-Liquid-Solid Three Phase Bubble Column Reactor, Chem. Eng. J., 1998, 70 (1), 81.
- [33] WEILAND P., ONKEN U., Fluid Dynamics and Mass Transfer in an Airlift Fermentor with External Loop, German Chemical Engineering, 1981, 4, 42.
- [34] IMMICH M., YU B., HOLLMANN D., ONKEN U., Stoffuebergang in einem Airlift-Schlaufenreaktor mil suspedierten Feststoff, Chem. Ing. Techn., 1990, 62 (11), 945.
- [35] KAWALEC-PIETRENKO B., Circulation of liquid in the draft-tube airlift reactor, Chem. Proc. Eng., 1992, (2), 229.
- [36] LELE S.S., JOSHI J.B., Modelling of Air-Lift Fluidized Bed: Optimization of Mass Transfer with Respect to Design and Operational Parameters, Chem. Eng. J., 1992,49 (2), 89.
- [37] KEMBLOWSKI Z., PRZYWARSKI J., DIAB A., An Average Gas Hold-up and Liquid Circulation Velocity in Airlift Reactors With External Loop, Chem. Eng. Sci., 1993,48 (23), 4023.
- [38] LIVINGSTON A.G., ZHANG S.F., Hydrodynamic Behaviour of Three-Phase (Gas-Liquid-Solid) Airlift Reactors, Chem. Eng. Sci., 1993, 48 (9), 1641.
- [39] Guo Y.X., RATHOR M.N., Tl H.C., Hydrodynamics and Mass Transfer Studies in a Novel External-Loop Airlift Reactor, Chem. Eng. J., 1997, 67 (3), 205.
- [40] HAVELKA P., LINEK V., SINKULE J., ZAHRADNIK J., FIALOVA M., Effect of the Ejector Configuration on the Gas Suction Rate and Gas Hold-up in Ejector Loop Reactors, Chem. Eng. Sci., 1997, 52 (11), 1701.
- [41] KAWAGOE M., YOSHIDA S., ISHII Y., NAOE K., Radial Liquid Velocity Distribution in an External-Loop Airlift Column with a Tapered Riser, Can. J. Chem. Eng., 1999, 77 (5), 811.
- [42] ZEHNER P., BENFER R., Modelling Fluid Dynamics in Multiphase Reactors, Chem. Eng. Sci., 1996, 51 (10), 1735.
- [43] LOHRENGEL B.. VOGELPOHL A., Einfiuss von Feststoffpartikeln auf die Hydrodynamik von Schlau-fenreaktoren, Chem. Ing. Techn., 1991, 63 (3), 262.
- [44] KMIEC A., SZCZEPANIAK L., ABDUL-LATIF S.S.H., On Flow Dynamics in a Jet-Loop Reactor, Collections of Czechoslovak Chemical Communications, 1994, 59 (11), 2426.
- [45] KMIEC A., An Experimental Study of Liquid-Solid Mixture Flows in a Jet-Loop Reactor, 2nd Israel Conference for Conveying and Handling of Particulate Solids, Jerusalem, May 26-28 1997, 5.22-5.26.
- [46] SCHLICHTING H., Boundary Layer Theory, New York, McGraw-Hill, 1960.
- [47] BIN A.K., Mass Transfer into Turbulent Free Liquid Interfaces, Reports of the Institute of Chemical Engineering at the Warsaw Technical University, 1986, 15, No. 1,1.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BGPK-1006-3931