Critical Flux with Respect to Aeration Rate for the Submerged Microfiltration Hollow Fiber Membrane in the Activated Sludge Solution

2016 ◽  
Vol 26 (2) ◽  
pp. 166-172
Author(s):  
Doin Jeong ◽  
◽  
Kun Yong Chung
Desalination ◽  
2002 ◽  
Vol 143 (3) ◽  
pp. 219-228 ◽  
Author(s):  
S.P. Hong ◽  
T.H. Bae ◽  
T.M. Tak ◽  
S. Hong ◽  
A. Randall

2016 ◽  
Vol 87 (1) ◽  
pp. 102-109 ◽  
Author(s):  
Chunyan Ma ◽  
Xiaoqian Wu ◽  
Zhenhong Liu

Filtration performance and fouling behavior of a five-bore hollow fiber membrane was investigated in a membrane bioreactor (MBR) treating printing and dyeing wastewater. A normal single-bore hollow fiber membrane module was used in the same bioreactor for comparison. During an operation over 30 days, the results of chemical oxygen demand (COD) and color removals demonstrated that the five-bore membrane was favorable for this wastewater treatment. The critical flux ( Jc) of the five-bore membrane and the single-bore membrane was determined at 21 and 15 L/(m2·h), respectively, using a flux-step method. During a steady running at sub-critical flux of 10 L/(m2·h) without cleaning for 50 days, the average increasing rates of trans-membrane pressure (TMP) for five-bore and single-bore membranes were 0.356 kPa/d and 0.444 kPa/d, respectively, indicating that the five-bore membrane had better fouling resistance. The total resistance values of five-bore membrane and single-bore membrane were 8.68 and 14.1 m−1, respectively. Scanning electron microscope (SEM) and atomic force microscope (AFM) results confirmed the cake layer resistance for five-bore membrane was much lower than single-bore membrane. It was expected that the membrane structure, especially the membrane diameter, influenced the anti-fouling property of five-bore membrane.


2007 ◽  
Vol 7 (4) ◽  
pp. 95-101
Author(s):  
Hyun-je Oh ◽  
June-Seok Choi ◽  
Byong-Bo Choi ◽  
Sangho Lee ◽  
Tae-Mun Hwang

Understanding the fouling phenomena in submerged membrane systems is challenging because the efficiency of hollow fiber membrane highly depends on the dimensions of the fibers as well as filtration conditions. Thus, modeling filtration behavior of hollow fibers is important for improving the performance of hollow fiber system. In this work, a theoretical model based on critical flux concept was developed to simulate filtration resistance and axial pressure drop along the fiber in drinking water treatment. The application of a model for experimental data indicated that the model matches the experiments quite well. Thus, simulation of membrane system was carried out under various conditions using the parameters from the model fit. The axial distribution of pressure and flux affect the filtration characteristics of hollow fiber membranes. The effect of model parameters (specific cake resistance and critical flux) and module geometry were theoretically also investigated using the model.


2013 ◽  
Vol 788 ◽  
pp. 413-417 ◽  
Author(s):  
Zhao Cui ◽  
Jie Wang ◽  
Hui Jia ◽  
Xiao Hong Dai ◽  
Yan Zhang

Based on the characteristics of non-uniform distribution in the fouling of hollow-fiber membrane, the non-uniform distribution of local flux and redistribution with different fiber length (0.6 m、1.2 m、1.6 m) was investigated experimentally. Experiment was conducted under the condition of operating flux 20 L/m2h (20 LMH). The results indicated that the longer fiber length was, the greater difference in local pressure and the more non-uniform the local flux distributed. Under operating mode of critical flux, the flux distribution in the length of 1.6 m membrane fiber is the most non-uniform with the fastest fouling rate. In addition, the distribution of local flux is more uniform for 0.6 m fiber under the operating flux of 16 LMH, which also slow down membrane fouling significantly. Shorter membrane fiber generally exhibited higher uniformity in the local flux distribution and slower development rate of membrane fouling.


2021 ◽  
Vol 43 (7) ◽  
pp. 547-556
Author(s):  
Hyun-Hoon Jung ◽  
Ji-Yun Seon ◽  
Tea-Hyoung Lim ◽  
Seung-Mok Lee ◽  
Seung-Kyun Park

Objectives : MBR (Membrane BioReactor) is well established wastewater treatment that combines biological and physical method with high quality effluent. The purpose of this study is to utilize an air scouring integral immersed hollow fiber membrane module through efficient structural improvement developed to reduce membrane fouling. In addition, the scouring aeration was optimized to determine the energy savings.Methods : In this study, membrane fouling test was evaluated in various of scouring aeration flow with range of 40 to 140 m3 air/m2 projected area・hr and influent and effluent was analyzed by water quality standard.Results and Discussion : In scouring aeration test, effective membrane contamination control was possible with supplying 80 m3 air/m2 projected area・hr, scouring aeration rate gradually increased the differential pressure from below 60 m3 air/m2 projected area・hr, which accelerates the membrane contamination phenomenon. By reducing more than 20% of the existing general scouring aeration rate of 100~140 m3 air/m2 projected area・hr, electricity and maintenance costs can be reduced due to aeration control, and at the same time, it is confirmed that the technology has the same performance. The pilot test results of SJMBR with the developed module showed that the effluent was BOD of 1.4 mg/L, COD of 4.2 mg/L, SS of 0.7 mg/L, T-N of 5.56 mg/L, T-P of 0.56 mg/L, total coliform group of 0 ea/mL, and ecotoxicity of 0 TU, respectively.Conclusions : These results are combined, when using an air scouring integral immersed hollow fiber membrane module, it is expected to reduce the amount of scouring air by more than 20% by optimizing the supply of scouring air. In addition, it can also be determined by technology that satisfy the same permeability and treated water quality as existing technologies.


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