Gas-inducing impeller design and performance characteristics

被引:75
作者
Forrester, SE
Rielly, CD
Carpenter, KJ
机构
[1] Univ Cambridge, Dept Chem Engn, Cambridge CB2 3RA, England
[2] Zeneca Fine Chem Mfg Org, Huddersfield HD1 1FF, W Yorkshire, England
基金
英国工程与自然科学研究理事会;
关键词
gas-inducing impeller; gas-liquid mixing; concave-blade impeller;
D O I
10.1016/S0009-2509(97)00352-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A theoretical and experimental study on the design and performance characteristics of gas inducing impellers is presented. In particular, the model developed by Evans et al. (1991, A.I.Ch.E. Spring National Meeting, Houston, TX, gaper 33e) is critically reviewed and, as a result, improvements to the kinetic energy pressure loss analysis and to the initial conditions are proposed. In addition, the model is successfully extended to account for multiple gas outlet orifice on each blade. Experimental measurements of the power consumption, rate of gas induction, mass transfer coefficient and detached bubble size for a partially optimised, 0.154 m diameter, six-bladed concave gas-inducing impeller are presented. A significant increase in the induced gas rate is observed by adding more outlet orifices to each blade. The principal advantage of using multiple orifices is that similar size bubbles are produced, compared to a single orifice, but larger interfacial areas are generated; the aerated power input is only slightly reduced from its ungassed value. Mass transfer coefficients, k(L)a, of the order of 0.02 s(-1) are attainable for a single outlet orifice on each blade; k(L)a is significantly increased by using multiple orifices. The dimensionless bubble size distributions, d/d(gm) are independent of the impeller speed over the range 4-8 rps, and can be successfully represented by a log-normal distribution. (C) 1998 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:603 / 615
页数:13
相关论文
共 26 条
[1]   MASS-TRANSFER IN MULTIPHASE AGITATED CONTACTORS [J].
ALBAL, RS ;
SHAH, YT ;
SCHUMPE, A ;
CARR, NL .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1983, 27 (02) :61-80
[2]  
CALDERBANK PH, 1958, T I CHEM ENG-LOND, V36, P43
[3]  
Davidson J.F., 1960, TRANS INST CHEM ENG, V38, P144, DOI DOI 10.1016/S0263-8762(97)80008-1
[4]  
EVANS GM, 1991, AICHE SPRING NAT M H
[5]  
EVANS GM, 1990, ICHEME S SERIES, V121, P137
[6]  
FORRESTER SE, 1992, INVESTIGATION GAS IN
[7]  
FORRESTER SE, 1993, I CHEM E RES EVENT B, V2, P666
[8]   BUBBLE FORMATION FROM A SPARGER IN POLYMER-SOLUTIONS .2. MOVING LIQUID [J].
GHOSH, AK ;
ULBRECHT, JJ .
CHEMICAL ENGINEERING SCIENCE, 1989, 44 (04) :969-977
[9]   A THEORETICAL-MODEL FOR BUBBLE FORMATION AT A FRIT SURFACE IN A SHEAR FIELD [J].
JOHNSON, BD ;
GERSHEY, RM ;
COOKE, RC ;
SUTCLIFFE, WH .
SEPARATION SCIENCE AND TECHNOLOGY, 1982, 17 (08) :1027-1039
[10]   MECHANICALLY AGITATED GAS-LIQUID REACTORS [J].
JOSHI, JB ;
PANDIT, AB ;
SHARMA, MM .
CHEMICAL ENGINEERING SCIENCE, 1982, 37 (06) :813-844