Harvesting and dewatering yeast by microflotation

被引:24
作者
Hanotu, James [1 ]
Karunakaran, Esther [1 ]
Bandulasena, Hemaka [2 ]
Biggs, Catherine [1 ]
Zimmerman, William B. [1 ]
机构
[1] Univ Sheffield, Dept Chem & Biol Engn, Sheffield S1 3JD, S Yorkshire, England
[2] Univ Loughborough, Dept Chem Engn, Loughborough LE11 3TU, Leics, England
基金
英国工程与自然科学研究理事会;
关键词
Bioflocculant; Chitosan; Dispersed air flotation; Dissolved air flotation; Fluidic oscillation; Microflotation; SACCHAROMYCES-CEREVISIAE; HEAVY-METALS; WATER; FLOCCULATION; SEPARATION; RECOVERY;
D O I
10.1016/j.bej.2013.10.019
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Microbubble has been applied for the recovery of yeast cells from their growth medium using the bioflocculant-chitosan. Results reaching 99% cell recovery were obtained under various conditions examined. The result of bubble size distribution showed that mean bubble size increased as microbubble diffuser pore size was increased. Also, cell recovery efficiency was a function of both bubble size and particle size (cell size). For smaller particles (<50 mu m), relatively smaller bubbles (<80 mu m) were found to be more effective for recovery, otherwise, relatively larger bubbles (80-150 mu m) proved to be efficient in recovering larger particles (particle size: similar to 250 mu m). Acidic and neutral pHs were effective in separation as hydrophobic particles were formed. As pH tends toward alkalinity, flocs become more hydrophilic, leading to low recovery from the aqueous solution. In addition, separation efficiency was dependent on flocculant dose as increase in concentration improved flocculation and consequently, yeast recovery. However, above a critical concentration, overdosing occurred and inadvertently, recovery efficiency decreased. The application of chitosan as a bioflocculant and the subsequent application of microflotation for the separation of yeast cells proved effective and promises several advantages over non-bubble based separation techniques that preclude continuous industrial-scale production. (C) 2013 Published by Elsevier B.V.
引用
收藏
页码:174 / 182
页数:9
相关论文
共 28 条
[1]  
Boussinesq J, 1885, CR Acad. Sc. Paris, V100, P935
[2]   Using chitosan as a coagulant in recovery of organic matters from the mash and lauter wastewater of brewery [J].
Cheng, WP ;
Chi, FH ;
Yu, RF ;
Lee, YC .
JOURNAL OF POLYMERS AND THE ENVIRONMENT, 2005, 13 (04) :383-388
[3]   Particle-bubble collision models - a review [J].
Dai, ZF ;
Fornasiero, D ;
Ralston, J .
ADVANCES IN COLLOID AND INTERFACE SCIENCE, 2000, 85 (2-3) :231-256
[4]  
Demain A. L., 1998, P13, DOI 10.1016/B978-044481312-1/50006-X
[5]  
Derjaguin B.V., 1961, B I MINING METALLURG, V651, P21
[6]   Flocculation of kaolinite suspensions in water by chitosan [J].
Divakaran, R ;
Pillai, VNS .
WATER RESEARCH, 2001, 35 (16) :3904-3908
[7]   Dissolved air flotation and me [J].
Edzwald, James K. .
WATER RESEARCH, 2010, 44 (07) :2077-2106
[8]  
Fleet GH, 2006, YEAST HANDB, V2, P1
[9]   THE ROLE OF HYDROPHOBICITY IN DISSOLVED AIR FLOTATION [J].
GOCHIN, RJ ;
SOLARI, J .
WATER RESEARCH, 1983, 17 (06) :651-657
[10]  
Grima EM, 2003, BIOTECHNOL ADV, V20, P491