A simple method for bakers’ yeast cell disruption using a three-phase fluidized bed equipped with an agitator

2008 ◽  
Vol 99 (18) ◽  
pp. 8935-8939 ◽  
Author(s):  
Tawatchai Charinpanitkul ◽  
Apinan Soottitantawat ◽  
Wiwut Tanthapanichakoon
Keyword(s):  
Yeast Cell ◽  
Fluidized Bed ◽  
Cell Disruption ◽  
Simple Method ◽  
Three Phase

Optimization of yeast cell disruption with a newly designed bead mill

1991 ◽  
Vol 13 (8) ◽  
pp. 665-671 ◽  
Author(s):  
D. van Gaver ◽  
A. Huyghebaert
Keyword(s):  
Yeast Cell ◽  
Cell Disruption ◽  
Bead Mill

Global modeling and simulation of a three-phase fluidized bed bioreactor

2009 ◽  
Vol 33 (1) ◽  
pp. 359-370 ◽  
Author(s):  
Mauren Fuentes ◽  
Miguel C. Mussati ◽  
Nicolás J. Scenna ◽  
Pío A. Aguirre
Keyword(s):  
Modeling And Simulation ◽  
Fluidized Bed ◽  
Global Modeling ◽  
Fluidized Bed Bioreactor ◽  
Three Phase

Effect of tapered angle on hydrodynamics of homogenous ternary mixture of regular particles in a three-phase tapered fluidized bed

2018 ◽  
Vol 61 (3) ◽  
pp. 269-285 ◽  
Author(s):  
R. K. Padhi ◽  
D. T. K. Dora ◽  
Y. K. Mohanty ◽  
G. K. Roy ◽  
B. Sarangi
Keyword(s):  
Fluidized Bed ◽  
Ternary Mixture ◽  
Three Phase ◽  
Tapered Angle

Study of Biofilm and Fluidization of Bioparticles in a Three-Phase Liquid-Fluidized-Bed Reactor

1991 ◽  
Vol 23 (7-9) ◽  
pp. 1347-1354 ◽  
Author(s):  
F. Trinet ◽  
R. Heim ◽  
D. Amar ◽  
H. T. Chang ◽  
B. E. Rittmann
Keyword(s):  
Fluidized Bed ◽  
Liquid Velocity ◽  
Substrate Surface ◽  
Biofilm Reactor ◽  
Strongly Correlated ◽  
Polysaccharide Content ◽  
High Particle ◽  
Air Turbulence ◽  
Three Phase ◽  
Phase Liquid

A three-phase, liquid-fluidized-bed biofilm reactor was operated over wide ranges of liquid velocity, air velocity, medium concentration, and substrate surface loading. The biofilm characteristics (total colonization, polysaccharide content, density, and thickness) and the specific detachment coefficient (bs) were determined by a combination of experimental measurements and a hydrodynamic model. The results demonstrated that dense and thin biofilms were induced by the physical condition of high particle-to-particle contacts and high liquid turbulence. The biofilm's polysaccharide content was increased by increased air turbulence and a low substrate availability. The specific detachment coefficient, bs, was strongly correlated to the concentration of the medium (negatively) and the polysaccharide content (positively). Overall, the bs can be controlled significantly by the gas and liquid velocities; increasing either velocity tends to increase bs.

Hydrodynamic characteristics of bubble-induced three-phase inverse fluidized bed (BIFB)

2019 ◽  
Vol 209 ◽  
pp. 115177 ◽  
Author(s):  
Keying Ma ◽  
Xiliang Sun ◽  
Yuanyuan Shao ◽  
Mingyan Liu ◽  
Jesse Zhu
Keyword(s):  
Fluidized Bed ◽  
Hydrodynamic Characteristics ◽  
Three Phase ◽  
Inverse Fluidized Bed

Enhancement of the oxygen transfer in a circulating three-phase fluidized bed bioreactor

1993 ◽  
Vol 39-40 (1) ◽  
pp. 455-466 ◽  
Author(s):  
Eduardo D. Dabdoub Paz ◽  
Maria Helena A. Santana ◽  
Silvia Y. Eguchi
Keyword(s):  
Fluidized Bed ◽  
Oxygen Transfer ◽  
Fluidized Bed Bioreactor ◽  
Three Phase

scholarly journals The performance of a three-phase fluidized bed reactor in treatment of wastewater with high organic load

2004 ◽  
Vol 21 (2) ◽  
pp. 219-227 ◽  
Author(s):  
R. R. Souza ◽  
I. T. L. Bresolin ◽  
T. L. Bioni ◽  
M. L. Gimenes ◽  
B. P. Dias-Filho
Keyword(s):  
Fluidized Bed ◽  
Fluidized Bed Reactor ◽  
Organic Load ◽  
Three Phase
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