Hydrodynamic and mass transfer study in a rectangular three-phase air-lift loop reactor

被引:27
作者
Couvert, A
Bastoul, D
Roustan, M
Chatellier, P
机构
[1] Ecole Natl Super Chim Rennes, Lab Chim Nuisances & Gest Environm, F-35700 Rennes, France
[2] INSA, Dept GPI, Lab Ingn Proc Environm, F-31077 Toulouse, France
[3] LPCP, F-75732 Paris 15, France
关键词
air-lift; three-phase flow; hydrodynamics; mass transfer;
D O I
10.1016/j.cep.2003.06.001
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This study concerns a three-phase rectangular air-lift reactor. The first part deals with the reactor's gas-liquid two-phase flow hydrodynamics. Parameters, such as the gas hold-up, the liquid velocity, the mixing parameters, and the solid hold-up, were quantified in the presence of two different plastic solids-a regular shape solid called PI, and an heterogeneous shape solid, P4. No fundamental influence of the solids on the studied parameters was noticed, except for the gas hold-up. Indeed, a bubble coalescence phenomenon was highlighted for high solid concentrations (epsilon(s) > 16%). Moreover, a comparison of these two materials led to the conclusion that P4 exhibited better hydrodynamic performances. In a second set of experiments, the oxygen mass transfer was characterised in three-phase flow, with both kinds of plastic materials. The k(L)a coefficient was deduced from a mass balance on the gas phase. It was found to be weakly influenced by the presence, the nature or the quantity of solid. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:1381 / 1387
页数:7
相关论文
共 14 条
[1]  
BELLO RA, 1984, CAN J CHEM ENG, V62, P573, DOI DOI 10.1002/CJCE.5450620501
[2]   Hydrodynamics of a three-phase fluidized bed - the inverse turbulent bed [J].
Comte, MP ;
Bastoul, D ;
Hebrard, G ;
Roustan, M ;
Lazarova, V .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (21-22) :3971-3977
[3]   Two-phase hydrodynamic study of a rectangular air-lift loop reactor with an internal baffle [J].
Couvert, A ;
Roustan, M ;
Chatellier, P .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) :5245-5252
[4]  
COUVERT A, 2001, P 5 INT C GAS LIQ GA
[5]   HYDRODYNAMIC CHARACTERISTICS OF INVERSE FLUIDIZATION IN LIQUID SOLID AND GAS-LIQUID SOLID SYSTEMS [J].
FAN, LS ;
MUROYAMA, K ;
CHERN, SH .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1982, 24 (02) :143-150
[6]  
FAN LS, 1989, SERIES CHEM ENG, P763
[7]  
HATZIFOTIADOU O, 1989, THESIS INSA TOULOUSE
[8]   Hydrodynamic characteristics of a three-phase inverse fluidized-bed column [J].
Ibrahim, YAA ;
Briens, CL ;
Margaritis, A ;
Bergongnou, MA .
AICHE JOURNAL, 1996, 42 (07) :1889-1900
[9]   HYDRODYNAMICS AND LOCAL PARAMETERS IN 3-PHASE-FLOW IN AIRLIFT-LOOP REACTORS OF DIFFERENT SCALE [J].
KOCHBECK, B ;
LINDERT, M ;
HEMPEL, DC .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (13-14) :3443-3450
[10]   Control of nitrification efficiency in a new biofilm reactor [J].
Lazarova, V ;
Nogueira, R ;
Manem, J ;
Melo, L .
WATER SCIENCE AND TECHNOLOGY, 1997, 36 (01) :31-41