Influence of particle size and surface charge on critical flux of crossflow microfiltration

1998 ◽  
Vol 38 (4-5) ◽  
1998 ◽  
Vol 38 (4-5) ◽  
pp. 481-488 ◽  
Author(s):  
D. Y. Kwon ◽  
S. Vigneswaran

The effect of particle size and ionic strength of the feed suspension on critical flux was studied. The critical flux was defined in two different ways (strong and mild definition). The fouling, the increase of resistance (which is the basis of the mild definition of the critical flux) was relatively sensitive to the deposition of particles of 0.46 μm on the membrane of 0.2 μm mean pore. On the other hand, the deposition of large particles of 3.2 μm to a certain value on the membrane surface of 0.2 μm mean pore did not lead to the increase in resistance. In case of 11.9 μm particles, the transmembrane pressure did not increase even with significant amount of deposition of particles. The ionic strength of suspension had significant effect on the critical flux. For an ionic strength less than 1×10−1.5 M, there was a decrease in the critical flux. This could be due to the dense layer of deposit which is the result of less diffuse layer thickness of particles. Above this ionic strength, a significant increase in critical flux was noticed which may be due to the aggregation of particles.


2016 ◽  
Vol 7 (32) ◽  
pp. 5123-5131 ◽  
Author(s):  
O. L. J. Virtanen ◽  
M. Brugnoni ◽  
M. Kather ◽  
A. Pich ◽  
W. Richtering

Many applications of poly(N-isopropylacrylamide) microgels necessitate robust control over particle size.


1997 ◽  
Vol 36 (12) ◽  
pp. 267-274 ◽  
Author(s):  
D. Y. Kwon ◽  
S. Vigneswaran ◽  
H. H. Ngo ◽  
H. S. Shin

In this study, use of a combined system of flocculation-microfiltration was assessed for its capability in removing solids and organics. The improvement of flux by the preflocculation was also investigated. The experimental set-up consisted of (i) Millipore flat plate microfiltration module with constant permeate withdrawal arrangement and (ii) a floating medium flocculator/filter consisting of polypropylene beads as a pretreatment. Commercial ferric chloride(FeCl3) was used for flocculation. The purpose of floating medium filter was primarily to produce filterable flocs and also to achieve partial solids and organics removal. The critical flux of kaolin clay suspension of 10–100mg/L was measured for membrane of pore size of 0.2μm in the presence of 0–4mg/L of fulvic acid in the suspension without any pretreatment. The critical flux was found to decrease with the increase in kaolin clay concentration. The results also indicated that there was no significant effect of organic (fulvic acid) concentration on critical flux. The pretreatment of floating medium filter alone without flocculant addition removed 30–40% of solids and resulted in a significant improvement of critical flux in crossflow microfiltration. Degree of solids and organic removal and the variation in critical flux were then studied in detail for the preflocculated/filtered kaolin clay suspension in the presence of organics. The pretreatment of flocculation/prefiltration removed approximately 50% of organics while producing uniform microflocs of 13–16 μm size. In addition, it enhanced the critical flux by 70% and resulted in 30–70% of the remaining organic removal in the crossflow microfiltration.


Biomaterials ◽  
2010 ◽  
Vol 31 (13) ◽  
pp. 3657-3666 ◽  
Author(s):  
Chunbai He ◽  
Yiping Hu ◽  
Lichen Yin ◽  
Cui Tang ◽  
Chunhua Yin

Nanoscale ◽  
2017 ◽  
Vol 9 (25) ◽  
pp. 8723-8739 ◽  
Author(s):  
Kritee Pant ◽  
Johanna Pufe ◽  
Kristof Zarschler ◽  
Ralf Bergmann ◽  
Jörg Steinbach ◽  
...  

Sign in / Sign up

Export Citation Format

Share Document