The role of shear conditions on floc characteristics and membrane fouling in coagulation/ultrafiltration hybrid process – the effect of flocculation duration and slow shear force

RSC Advances ◽  
2016 ◽  
Vol 6 (1) ◽  
pp. 163-173 ◽  
Author(s):  
Jun Nan ◽  
Meng Yao ◽  
Qinggui Li ◽  
Dan Zhan ◽  
Ting Chen ◽  
...  

The impact of shear conditions during coagulation on the ultrafiltration permeate flux in a coagulation–ultrafiltration (C–UF) process was investigated.


2017 ◽  
Vol 34 (1) ◽  
Author(s):  
Rakesh Baghel ◽  
Sushant Upadhyaya ◽  
Kailash Singh ◽  
Satyendra P. Chaurasia ◽  
Akhilendra B. Gupta ◽  
...  

AbstractThe main aim of this article is to provide a state-of-the-art review of the experimental studies on vacuum membrane distillation (VMD) process. An introduction to the history of VMD is carried out along with the other membrane distillation configurations. Recent developments in process, characterization of membrane, module design, transport phenomena, and effect of operating parameters on permeate flux are discussed for VMD in detail. Several heat and mass transfer correlations obtained by various researchers for different VMD modules have been discussed. The impact of membrane fouling with its control in VMD is discussed in detail. In this paper, temperature polarization coefficient and concentration polarization coefficient are elaborated in detail. Integration of VMD with other membrane separation processes/industrial processes have been explained to improve the performance of the system and make it more energy efficient. A critical evaluation of the VMD literature is incorporated throughout this review.



Membranes ◽  
2021 ◽  
Vol 11 (8) ◽  
pp. 643
Author(s):  
Hongjian Yu ◽  
Weipeng Huang ◽  
Huachen Liu ◽  
Tian Li ◽  
Nianping Chi ◽  
...  

The combination of conventional and advanced water treatment is now widely used in drinking water treatment. However, membrane fouling is still the main obstacle to extend its application. In this study, the impact of the combination of coagulation and ultrafiltration (UF) membrane rotation on both fouling control and organic removal of macro (sodium alginate, SA) and micro organic matters (tannic acid, TA) was studied comprehensively to evaluate its applicability in drinking water treatment. The results indicated that membrane rotation could generate shear stress and vortex, thus effectively reducing membrane fouling of both SA and TA solutions, especially for macro SA organics. With additional coagulation, the membrane fouling could be further reduced through the aggregation of mediate and macro organic substances into flocs and elimination by membrane retention. For example, with the membrane rotation speed of 60 r/min, the permeate flux increased by 90% and the organic removal by 35% in SA solution, with 40 mg/L coagulant dosage, with an additional 70% increase of flux and 5% increment of organic removal to 80% obtained. However, too much shear stress could intensify the potential of fiber breakage at the potting, destroying the flocs and resulting in the reduction of permeate flux and deterioration of effluent quality. Finally, the combination of coagulation and membrane rotation would lead to the shaking of the cake layer, which is beneficial for fouling mitigation and prolongation of membrane filtration lifetime. This study provides useful information on applying the combined process of conventional coagulation and the hydrodynamic shear force for drinking water treatment, which can be further explored in the future.



2008 ◽  
Vol 58 (9) ◽  
pp. 1849-1855 ◽  
Author(s):  
S. Lyko ◽  
T. Wintgens ◽  
T. Melin

Soluble organic macromolecules are ubiquitous in activated sludge supernatant. For the operation of membrane bioreactors (MBR) this group of substances is considered as the dominant factor causing severe membrane fouling due to the concentration polarisation phenomenon. The well established critical flux concept for the characterisation of membrane bioreactor's operation limits is based on filtration data only. As there is an cause-and-effect relation between the partial retention of organic compounds and the limited flux according the critical flux concept the aim of this study was to draw a comparison between different permeate fluxes on the retention of organic macromolecules. Thus, a municipal pilot-scale MBR with three capillary hollow fibre membrane modules was operated in sub critical, critical and supercritical flux mode, respectively and the retention of macromolecules was quantified by size exclusion chromatography. Three permeate extraction pumps allow a simultaneous operation with different operational conditions for each membrane module and proved the crucial impact of permeate flux on the fouling rate. The interchange of these conditions gave evidence of an optimised start-up procedure for MBRs characterised by higher permeate fluxes. An increased flux causes both a higher retention of soluble macromolecules and subsequent a higher fouling rate.



2003 ◽  
Vol 3 (5-6) ◽  
pp. 155-164 ◽  
Author(s):  
J.-M. Laîné ◽  
C. Campos ◽  
I. Baudin ◽  
M.-L. Janex

Since the first membrane applications at the end of the 1980s, the water treatment engineering community has been able to develop reliable low pressure membrane systems that are capable of producing high quality drinking water at a competitive price, making membrane technology an attractive solution to both upgrade existing plants and design new ones. A competitive price means low capital and operating cost, which are inversely proportional to membrane hydraulic performance (permeate flux). Porous membranes lose their hydraulic performance as materials accumulate on their surfaces and/or within their pores, a process called membrane fouling. Although a significant effort has been devoted to elucidating the fouling mechanisms of polymeric membranes by natural organic matter (NOM), no single model has yet been accepted. In fact, most of the existing literature is contradictory, showing that membrane fouling is far from being fully understood. This article reviews over a decade of Ondeo's experience on characterizing and preventing fouling of polymeric membranes by natural organic matter and inorganic compounds. The review focuses on the role of NOM size and hydrophobicity, of membrane chemistry, and of solution pretreatment (coagulation and/or adsorption). In addition, the efficacy of some currently used strategies to minimize membrane fouling is also discussed.



2002 ◽  
Vol 2 (5-6) ◽  
pp. 337-343 ◽  
Author(s):  
S.A. Lee ◽  
T.D. Waite ◽  
A.G. Fane ◽  
R. Amal

Treatment of waters and wastewaters by microfiltration (MF) requires the addition of chemical coagulants to enhance the removal of dissolved substances. Under these conditions the feed to the MF contains flocculated particulates which must be retained by the membrane. While an extensive knowledge base on the effect of dispersed particles on membrane cake formation and fouling exists, much less information is available on the impact of aggregates on cake characteristics. Results of impact of the size and structure (as characterized by the fractal dimension) of particulate aggregates on microfiltration membrane fouling are in qualitative agreement with a simple model based on the Carman-Kozeny equation. Larger flocs form a cake with large inter-floc porosity which results in a significantly higher permeate flux than achieved for smaller flocs. Concomitantly, looser flocs (of low fractal dimension) are likely to form a cake that has higher intra-floc voidage thus flux is higher than a cake made of compact flocs of similar size. Analysis of cake compression indicates that compressibility is strongly influenced by trans-membrane pressure (TMP). The placement of highly porous aggregates onto the membrane results in formation of a highly porous cake layer provided a low TMP is maintained. Rapid compression of the cake occurs at higher TMPs as shown by the significantly lower porosity of the cake. Under high TMP conditions, the cake porosity exhibits a strong size dependence with larger floc sizes yielding higher porosities. This result possibly indicates formation of relatively impermeable assemblages (as a result of significant compaction) with flux controlled by inter-aggregate flow, i.e. flow around compressed flocs. In comparison, the marked lack of size dependence of porosity at low TMP suggests that permeate flux is dominated by flow through (rather than around) the highly permeable flocs. These results suggest that it should be possible to control both operating conditions (such as TMP) and floc characteristics such that high permeate flux at a given TMP or low cake resistance at a fixed flux is achievable.



Membranes ◽  
2020 ◽  
Vol 10 (11) ◽  
pp. 321
Author(s):  
Yang-Hui Cai ◽  
Xiao Jin Yang ◽  
Andrea Iris Schäfer

Removal of naturally occurring strontium (Sr) from groundwater is vital as excessive exposure may lead to bone growth problems in children. Nanofiltration/reverse osmosis (NF/RO) is commonly used in groundwater treatment due to the high effectiveness and simple maintenance of these pressure driven membrane processes. In this research, a pilot-scale NF/RO system was used to desalinate a natural groundwater sample containing high Sr concentration (10.3 mg/L) and “old” groundwater organic matter (70.9 mg/L) from Esilalei in northern Tanzania to understand the removal of strontium by NF/RO. The impact of applied pressure (10–15 bar) and groundwater pH (3–12) on the membrane performance including permeate flux, strontium and total organic carbon (TOC) flux and removal was investigated. Increasing applied pressure was found to enhance the flux by increasing the driving force and enhance Sr and TOC removal by dilution effect (water flux higher than Sr passage). The alkaline pH caused severe flux decline likely due to membrane fouling and scaling, while it slightly enhanced Sr removal of RO membranes, but weakened the TOC removal. In contrast, acidic and neutral pH of groundwater enhanced TOC removal. These findings suggest that appropriately high applied pressure and acidic pH condition of groundwater are recommended to apply to the NF/RO membrane system in groundwater desalination to achieve better membrane performance.





2013 ◽  
Vol 864-867 ◽  
pp. 1226-1232
Author(s):  
Xue Hui Zhao ◽  
Hong Wei Zhang ◽  
Jie Wang

The effect of aggregated floc circulation on membrane fouling in contact circulated coagulation-membrane filtration hybrid process for treatment of surface water was investigated in this study. In order to understand the floc characteristics, the floc formation, breakage and re-growth were monitored by Mastersizer 2000 under the coagulation dosage of 5, 10, 15 and 20mg/l. A contact circulated coagulation tests were carried out and the effluent was filtered by a dead-end micro-filtration with the hollow fibre membrane. The coagulation effluent quality and the relative permeability J/J0 of membrane was determined at the circulated floc dosage of 22, 44 and 66mg/l. The experiment results indicated that the addition of circulated floc obviously improved the flux decline and the degree of improvement was closely related to the dosage of circulated floc. Compared to traditional coagulation, the contact circulated coagulation was an economic and efficient method to retard the membrane fouling.



Blood ◽  
2011 ◽  
Vol 118 (21) ◽  
pp. 1329-1329
Author(s):  
Jinlin Jiang ◽  
Eleftherios T. Papoutsakis

Abstract Abstract 1329 Introduction. Environmental (matrix) elasticity (Engler et al., Cell 126: 677 (2006)) and biomechanical forces (Baruch et al., Blood 114:1975 (2009)) are important differentiation signals for stem cells. In this study, we investigated how these biomechanical/biophysical signals affect megakaryocytic (Mk) differentiation, aiming to uncover signaling mechanisms behind these effects, and establish better culture environment for Mk differentiation and platelet biogenesis. CHRF cell (Fuhrken et al., Exp. Hematol. 35: 476 (2006)), a well- established Mk cell line, was used in this study. Upon PMA stimulation, CHRF cells undergo Mk-like differentiation, including endomitosis and projection of cytoplasmic extensions. Methods and Results. Application of shear stress (2.5 dyne/cm2; physiological range: 1.3∼4.1 dyne/cm2) to CHRF cells attached to fibronectin-coated surfaces for two hours resulted in retraction, shedding and formation of cytoplasmic extensions (proplatelet-like structures), whereas there were no morphological changes in static culture. Shear force also accelerated endomitosis as assessed by flow-cytometry based analysis of BrdU incorporation: CHRF cells exposed for two hours to shear flow had 16% more BrdU positive cells compared to cells under static conditions. The stress responsive p53 is a regulator in both cell-cycle arrest by laminar flow (Zeng et al., JBC 278: 24594 (2003)) and Mk differentiation (Fuhrken et al., JBC 283: 15589 (2008)). To determine if p53 is involved in the response of CHRF cells to shear stress, western analysis was used to show that two hours of exposure to shear (2.5 dyne/cm2) increased the ratio of K382-acetylated p53 to total p53 by more than 188% (n=3, p<0.05) while total p53 protein expression did not change significantly. These data suggest that p53 acetylation is mediating, partially at least, the response of Mk cells to biomechanical forces. In order to examine the effect of matrix elasticity on Mk differentiation, polyacrylamide gels were used to control elasticity. We coated the gel surface with fibronectin to provide holding points for CHRF cells to sense gel elasticity. As matrix elasticity increased, the % of CHRF cells with cytoplasmic extensions increased first and decreased later (Fig. 1, n=3, Error bar: SEM). The highest percentage (17%) of CHRF cells displaying cytoplasmic extensions was observed on a gel with elasticity (ca. 8.2 kPa) mimicking the in vivo vascular niche. Non-muscle myosin IIA (NMMIIA) has been shown to serve as elasticity sensor in mesenchymal stem cells. Thus, we aimed to investigate the role of NMMIIA in the response of CHRF cells to matrix elasticity. Blebbistatin, an inhibitor of NMMIIA, minimized the differences of the percentage of cells with cytoplasmic extensions between gels with different elasticity (Fig. 2), thus suggesting that NMMIIA is involved in the response of CHRF cells to matrix elasticity and may also serve as a biological elasticity sensor. As shown by fluorescent microscopy, the cellular distribution of NMMIIA was directed by matrix elasticity (Fig. 3). On soft gels (75 Pa; n=3), NMMIIA was concentrated in the center of the cytoplasm. On a moderately stiff gel (5.6 kPa; n=3), NMMIIA was distributed across the whole cell, while on glass (the stiffest condition tested; n=3), NMMIIA moved into the nucleus and the tips of cytoplasmic extensions. Others have shown NMMIIA is involved in regulation of gene expression when it moves into the nucleus, so our observations that NMMIIA translocates into the nucleus as gel elasticity increases strongly suggests that NMMIIA may regulate gene transcription during proplatelet formation and platelet biogenesis. In future we want to investigate and prove this hypothesis. Conclusions and Significance. Our data shed light on the largely unexplored role of biomechanical and biophysical parameters (of physiological significance) on Mk differentiation. The impact of these parameters is both of physiological and practical significance in the context of platelet biogenesis and ex vivo platelet generation. Disclosures: No relevant conflicts of interest to declare.



2013 ◽  
Vol 44 (5) ◽  
pp. 311-319 ◽  
Author(s):  
Marco Brambilla ◽  
David A. Butz

Two studies examined the impact of macrolevel symbolic threat on intergroup attitudes. In Study 1 (N = 71), participants exposed to a macrosymbolic threat (vs. nonsymbolic threat and neutral topic) reported less support toward social policies concerning gay men, an outgroup whose stereotypes implies a threat to values, but not toward welfare recipients, a social group whose stereotypes do not imply a threat to values. Study 2 (N = 78) showed that, whereas macrolevel symbolic threat led to less favorable attitudes toward gay men, macroeconomic threat led to less favorable attitudes toward Asians, an outgroup whose stereotypes imply an economic threat. These findings are discussed in terms of their implications for understanding the role of a general climate of threat in shaping intergroup attitudes.



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