Breakage of protein precipitates flowing through orifices

被引:9
作者
Zumaeta, Nixon
Byrne, Edmond P. [1 ]
Fitzpatrik, John J. [1 ]
机构
[1] Univ Coll Cork, Dept Chem & Proc Engn, Cork, Ireland
关键词
orifice; precipitate processing; breakage; precipitate transport; modelling; CFD;
D O I
10.1016/j.cherd.2007.10.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effect of orifice diameter and orifice length on the breakage of flowing protein precipitates was evaluated. These orifices were intended to mimic the flow intensity present in certain valves, pumps, flow meters and centrifuges that might be present in the transportation of precipitates. Different orifice contraction ratios (0.12-0.36), orifice lengths (0.3, 1.0 and 3.5 mm) and flow rates (6.0-9.0 g s(-1)) were studied. The extent, rate and mechanism of precipitate disruption were significantly affected by all these variables. The energy dissipation rate (F) within each flow geometry was computed using CFD. A wide range of F values (3.4 x 10(2) to 1.4 x 10(6) m(2) s(-3)) was generated and at least two different breakage mechanisms were observed. The first mechanism dominates at high F and is characterized by significant production of submicron particles; the other one dominates at low E: with negligible production of fines. Both the breakage rate and mechanism were modelled as continuous functions of c. The proposed breakage model predicts that significant precipitate disruption will occur according to the former breakage mechanism in certain post-formation processing equipment. (c) 2007 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:107 / 117
页数:11
相关论文
共 36 条
[1]   FLOC BREAKAGE - THE DYNAMIC-RESPONSE OF THE PARTICLE-SIZE DISTRIBUTION IN A FLOCCULATED SUSPENSION TO A STEP CHANGE IN TURBULENT ENERGY-DISSIPATION [J].
AKERS, RJ ;
RUSHTON, AG ;
STENHOUSE, JIT .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (04) :787-798
[2]  
AYAZISHAMLOU A, 1996, BIOPROCESS ENG, V14, P237
[3]   Break-up of flocs in contraction and swirling flows [J].
Blaser, S .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 2000, 166 (1-3) :215-223
[4]   Performance prediction of industrial centrifuges using scale-down models [J].
Boychyn, M ;
Yim, SSS ;
Bulmer, M ;
More, J ;
Bracewell, DG ;
Hoare, M .
BIOPROCESS AND BIOSYSTEMS ENGINEERING, 2004, 26 (06) :385-391
[5]   Characterization of flow intensity in continuous centrifuges for the development of laboratory mimics [J].
Boychyn, M ;
Yim, SSS ;
Shamlou, PA ;
Bulmer, M ;
More, J ;
Hoare, A .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (16) :4759-4770
[6]  
Budde C, 2002, CHEM ENG TECHNOL, V25, P1164, DOI 10.1002/1521-4125(20021210)25:12<1164::AID-CEAT1164>3.0.CO
[7]  
2-E
[8]   Influence of shear on particle size and fractal dimension of whey protein precipitates: implications for scale-up and centrifugal clarification efficiency [J].
Byrne, EP ;
Fitzpatrick, JJ ;
Pampel, LW ;
Titchener-Hooker, NJ .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (18) :3767-3779
[9]   DROP-SIZE DISTRIBUTIONS PRODUCED BY TURBULENT PIPE FLOW OF IMMISCIBLE LIQUIDS [J].
COLLINS, SB ;
KNUDSEN, JG .
AICHE JOURNAL, 1970, 16 (06) :1072-&
[10]   DROP SIZES OF EMULSIONS RELATED TO TURBULENT ENERGY-DISSIPATION RATES [J].
DAVIES, JT .
CHEMICAL ENGINEERING SCIENCE, 1985, 40 (05) :839-842