Separation of Bacteria Kocuria rhizophila from Fermentation Broth by Cross-Flow Microfiltration Using Inexpensive Tubular Ceramic Membrane

Author(s):  
D. Dahiya ◽  
M. Kumar ◽  
G. Pugazhenthi ◽  
D. Vasanth
Membranes ◽  
2020 ◽  
Vol 10 (4) ◽  
pp. 67 ◽  
Author(s):  
Wirginia Tomczak ◽  
Marek Gryta

This paper reports the study of the cross-flow microfiltration (MF) of glycerol fermentation broths with Citrobacter freundii bacteria. A single channel tubular ceramic membrane with a nominal pore size of 0.14 µm was used. It has been demonstrated that the MF ceramic membrane has been successfully applied to bacteria cell removal and to effectively eliminate colloidal particles from glycerol fermentation broths. However, due to fouling, the significant reduction of the MF performance has been demonstrated. In order to investigate the impact of transmembrane pressure (TMP) and feed flow rate (Q) on MF performance, 24 experiments have been performed. The highest steady state permeate flux (138.97 dm3/m2h) was achieved for 0.12 MPa and 1000 dm3/h. Fouling analysis has been studied based on the resistance-in series model. It has been found that the percentage of irreversible fouling resistance during the MF increases with increasing TMP and Q. The permeate flux regeneration has been achieved by membrane cleaning with 3 wt % NaOH and 3 wt % H3PO4 at 45 °C. The results of this study are expected to be useful in industrially employing the MF process as the first step of glycerol fermentation broth purification.


1995 ◽  
Vol 60 (12) ◽  
pp. 2074-2084
Author(s):  
Petr Mikulášek

The microfiltration of a model fluid on an α-alumina microfiltration tubular membrane in the presence of a fluidized bed has been examined. Following the description of the basic characteristic of alumina tubular membranes, model dispersion and spherical particles used, some comments on the experimental system and experimental results for different microfiltration systems are presented. From the analysis of experimental results it may be concluded that the use of turbulence-promoting agents resulted in a significant increase of permeate flux through the membrane. It was found out that the optimum porosity of fluidized bed for which the maximum values of permeate flux were reached is approximately 0.8.


2013 ◽  
Vol 427 ◽  
pp. 118-128 ◽  
Author(s):  
Białas Wojciech ◽  
Ewelina Celińska ◽  
Radosław Dembczyński ◽  
Daria Szymanowska ◽  
Magdalena Nowacka ◽  
...  

1989 ◽  
Vol 15 (3) ◽  
pp. 638-644 ◽  
Author(s):  
Takuo Imasaka ◽  
Nobuhiko Kanekuni ◽  
Hiroyuki So ◽  
Shigeru Yoshino

Sign in / Sign up

Export Citation Format

Share Document