An Improved Configuration of Vertical-Flow Mesh Tube Filters for Seawater Pretreatment: Performance, Cleaning, and Energy Consumption

被引:4
作者
Kim, Dong-Ho [1 ]
Choi, Changkyoo [2 ]
Lee, Chulmin [1 ]
Adha, Rusnang Syamsul [1 ]
Nguyen, Thanh-Tin [1 ]
Ahn, Sang-Jun [3 ]
Son, Hee-Jong [4 ]
Kim, In S. [1 ]
机构
[1] Gwangju Inst Sci & Technol GIST, Sch Earth Sci & Environm Engn, Global Desalinat Res Ctr GDRC, Gwangju 61005, South Korea
[2] Korea Environm Corp, Korea Water Cluster, Dept Water Ind Promot, Water Convergence Res Team, Daegu 43008, South Korea
[3] KEOSONG Construct Co Ltd, KEOSONG Res Inst, Seoul 06640, South Korea
[4] Water Author Busan, Water Qual Inst, Gimhae 50804, Gyeongnam, South Korea
关键词
suspended particles; roughing filters; mesh tube filtration; porous filter bed; specific energy consumption; IONIC-STRENGTH; POROUS-MEDIA; PARTICLE; ULTRAFILTRATION; AGGREGATION; ADSORPTION; DEPOSITION; EFFICIENCY; STABILITY; TRANSPORT;
D O I
10.3390/w12102804
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Roughing filters are types of porous media filter used in pretreatment systems where the raw water contains a large amount of suspended particles (SPs) and organic matter. Mesh tube filtration (MTF) media are roughing-filter media composed of low-density polyethylene used for SP removal during wastewater treatment. In this study, we present an improved MTF design-a porous filter bed (PFB), which exhibits superior SP removal performance compared to conventional MTF media. We then compare the applicability of MTF and PFB to both the primary pretreatment process for seawater desalination and the water reuse process. In bench-scale SP removal experiments, PFB shows removal rates of 46.7%, 68.0%, 67.6%, and 68.4% at hydraulic retention times of 15, 20, 30, and 60 min, respectively, which are better than those of MTF. The specific energy consumption (SEC) of batch dissolved air flotation (DAF) was known to range from 0.035 to 0.047 kWh/m(3), whereas the SEC calculated for pilot-scale MTF and PFB is 0.027 kWh/m(3) and minimum energy for influent supply, respectively. This suggests that PFB can compete with DAF as a primary pretreatment process. MTF predominantly removes SPs by sedimentation, whereas SP removal in PFB typically occurs via deposition of SPs on the mesh tube media.
引用
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页数:21
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[1]  
[Anonymous], 2013, PARTICLE DEPOSITION, DOI DOI 10.1016/C2013-0-04548-3
[2]   Aggregation in charge-stabilized colloidal suspensions revisited [J].
Behrens, SH ;
Borkovec, M ;
Schurtenberger, P .
LANGMUIR, 1998, 14 (08) :1951-1954
[3]   Coupled Effects of Ionic Strength, Particle Size, and Flow Velocity on Transport and Deposition of Suspended Particles in Saturated Porous Media [J].
Bennacer, Lyacine ;
Ahfir, Nasre-Dine ;
Alem, Abdellah ;
Wang, HuaQing .
TRANSPORT IN POROUS MEDIA, 2017, 118 (02) :251-269
[4]   Membrane fouling and chemical cleaning in water recycling applications [J].
Beyer, Monique ;
Lohrengel, Burkhard ;
Nghiem, Long D. .
DESALINATION, 2010, 250 (03) :977-981
[5]   Surface element integration: A novel technique for evaluation of DLVO interaction between a particle and a flat plate [J].
Bhattacharjee, S ;
Elimelech, M .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1997, 193 (02) :273-285
[6]   Improving energy efficiency of pretreatment for seawater desalination during algal blooms using a novel meshed tube filtration process [J].
Cha, Gyuhyon ;
Choi, Soohoon ;
Lee, Hyunkyung ;
Kim, Kwangse ;
Ahn, Sangjun ;
Hong, Seungkwan .
DESALINATION, 2020, 486 (486)
[7]   A kinetic investigation of cationic starch adsorption and flocculation in kaolin suspension [J].
Chen, Yanxiao ;
Liu, Shaoying ;
Wang, Gongying .
CHEMICAL ENGINEERING JOURNAL, 2007, 133 (1-3) :325-333
[8]   Numerical study of fluid behavior on protruding shapes within the inlet part of pressurized membrane module using computational fluid dynamics [J].
Choi, Changkyoo ;
Lee, Chulmin ;
Park, No-Suk ;
Kim, In S. .
ENVIRONMENTAL ENGINEERING RESEARCH, 2020, 25 (04) :498-505
[9]   Seawater pretreatment for reverse osmosis: Chemistry, contaminants, and coagulation [J].
Edzwald, James K. ;
Haarhoff, Johannes .
WATER RESEARCH, 2011, 45 (17) :5428-5440
[10]   Dissolved air flotation and me [J].
Edzwald, James K. .
WATER RESEARCH, 2010, 44 (07) :2077-2106