• Title/Summary/Keyword: Reverse-osmosis

Search Result 420, Processing Time 0.027 seconds

A Numerical Study on the Impeller Meridional Curvature of High Pressure Multistage Pump (고압 다단 펌프의 임펠러 자오면 곡선에 대한 수치 해석적 연구)

  • Kim, Deok Su;Jean, Sang Gyu;Mamatov, Sanjar;Park, Warn Gyu
    • Transactions of the Korean Society of Mechanical Engineers B
    • /
    • v.41 no.7
    • /
    • pp.445-453
    • /
    • 2017
  • This paper presents the hydraulic design an impeller and radial diffuser of a high-pressure multistage pump for reverse osmosis. The flow distribution and hydraulic performance for the meridional design of the impeller were analyzed numerically. Optimization was conducted based on the response surface method by varying the hub and shroud meridional curvatures, while maintaining the impeller outlet diameter, outlet width, and eye diameter constant. The analysis results of the head and efficiency with the variation in the impeller meridional profile showed that angle of the front shroud near the impeller outlet (${\varepsilon}Ds$) had the highest effect on head increase, while the hub inlet length ($d_{1i}$) and shroud curvature (Rds) had the highest effect on efficiency. From the meridional profile variation, an approximately 0.5% increase in efficiency was observed compared with the base model (case 25).

Surface Modification of Reverse Osmosis Membrane Skin Layer by Silane Compound (Silane 화합물을 이용한 역삼투막 활성층의 표면개질)

  • Lee Yong-Taek;Shin Dong-Ho;Kim No-Won
    • Membrane Journal
    • /
    • v.16 no.2
    • /
    • pp.106-114
    • /
    • 2006
  • This study is concerned with preparation of chlorine resistant (CR) thin layer composite (TFC) membranes. The novel method for making CR membranes from commercially available RO membranes is based on sol-gel condensation of trialkoxyalkylsilane derivatives. The silane coupling agents used in this study have different number of alkyl carbon chain group (methyltriethoxysilane; METES and octyltriethoxysilane; OCTES). The OCTES composite membranes have a significant tolerance to chlorine compared to commercial polyamide RO membrane or METES composite membranes. The surface properties of membranes were examined to explain a significant difference of chlorine tolerance between OCTES composite membrane and the other two membranes. In this study, we tried several surface analyses to explain difference of chlorine tolerance. The element composition results of surface analysis by EDX confirmed that both silane fixed on polyamide firmly, The surface roughness and contact angle results showed long chain alkyl group of OCTES enhancing hydrophobicity considerably than METES. The hydrophobicity plays an important role in chlorine resistance of membrane.

The present and future of SWRO-PRO hybrid desalination technology development (SWRO-PRO 복합해수담수화 기술의 현재와 미래)

  • Chung, Kyungmi;Yeo, In-Ho;Lee, Wonil;Oh, Young Khee;Park, Tae Shin;Park, Yong-gyun
    • Journal of Korean Society of Water and Wastewater
    • /
    • v.30 no.4
    • /
    • pp.401-408
    • /
    • 2016
  • Desalination is getting more attention as an alternative to solve a global water shortage problem in the future. Especially, a desalination technology is being expected as a new growth engine of Korea's overseas plant business besides one of the solutions of domestic water shortage problem. In the past, a thermal evaporation technology was a predominant method in desalination market, but more than 75% of the current market is hold by a membrane-based reverse osmosis technology because of its lower energy consumption rate for desalination. In the future, it is expected to have more energy efficient desalination process. Accordingly, various processes are being developed to further enhance the desalination energy efficiency. One of the promising technologies is a desalination process combined with Pressure Retarded Osmosis (PRO) process. The PRO technology is able to generate energy by using osmotic pressure of seawater or desalination brine. And the other benefits are that it has no emission of $CO_2$ and the limited impact of external environmental factors. However, it is not commercialized yet because a high-performance PRO membrane and module, and a PRO system optimization technology is not sufficiently developed. In this paper, the recent research direction and progress of the SWRO-PRO hybrid desalination was discussed regarding a PRO membrane and module, an energy recovery system, pre-treatment and system optimization technologies, and so on.

Feasibility study on shale gas wastewater treatment using membrane distillation (막 증발법을 이용한 셰일가스 폐수 처리 가능성 평가)

  • Cho, Hyeongrak;Choi, Yongjun;Lee, Sangho
    • Journal of Korean Society of Water and Wastewater
    • /
    • v.30 no.4
    • /
    • pp.441-447
    • /
    • 2016
  • Development of shale gas has drawn increasing attention since it is one of promising alternative energy resources. However, contamination of groundwater and surface water during the extraction of shale gas is becoming a serious environmental issues, which brings the needs to treat wastewater generated from hydraulic fracking. In this study, the feasibility of membrane distillation (MD) for the treatment of shale gas wastewater was investigated using a laboratory scale experimental setup. Flat-sheet MD membranes were used to treat produced water from a shale gas well in the United States. Different configurations such as direct contact MD (DCMD) and air gap MD (AGMD) were compared in terms of flux and fouling propensity. The foulants on the surface of the membranes were examined. The results suggest that MD can treat the shale gas produced water containing more than 200,000 mg/L of total dissolved solids, which is impossible by other technologies such as reverse osmosis (RO) and forward osmosis (FO). In this study, we investigated the possibility of processing and characterization of shale gas produce wastewater using membrane distillation. Laboratory scale membrane distillation experimental device was developed. It was compared the flat-sheet direct contact membrane distillation and flat-sheet air gap membrane distillation. AGMD flux in lower than the flux of DCMD, it was expected that the contamination caused by organic matters.

Effect of Reverse Osmosis-treated Deep Sea Water Supplementation on the Quality Characteristics of Chicken Meat (역삼투 처리한 해양 심층수의 급여가 닭고기의 품질 특성에 미치는 영향)

  • Kang, Sun-Moon;Lee, Ik-Sun;Ohh, Sang-Jip;Kim, Gur-Yoo;Lee, Sung-Ki
    • Korean Journal of Poultry Science
    • /
    • v.37 no.4
    • /
    • pp.373-382
    • /
    • 2010
  • This study was carried out to investigate the effect of reverse osmosis (RO)-treated deep sea water (DSW) supplementation on the quality characteristics of chicken breast meat. For 28 days, one-day-old broiler chicks (Ross 308) were divided into two groups and supplemented with either water (control) or RO-treated DSW (diluted with deionized water at 1:20 [RO-treated DSW:deionized water] ratio). The control group was fed on a basal diet containing 0.21% salt. Five birds were slaughtered on each group and breast meat from carcasses was stored at $4^{\circ}C$ for 9 days. The proximate composition, fatty acid composition, cholesterol content, mineral content, pH value, water-holding capacity and Warner-Bratzler shear force value were not affected by RO-treated DSW supplementation. At 6 day of storage, lipid oxidation (2-thiobarbituric acid reactive substances) was significantly higher in RO-treated DSW group than in the control (P<0.05). With regard to meat color, CIE $L^*$ value was significantly lower in RO-treated DSW group than in the control after 6 day of storage (P<0.05), whereas CIE $a^*$ and $b^*$ values were not significantly different between two groups during storage. Consequently, RO-treated DSW supplementation led to a darker color and reduced the lipid oxidation stability in chicken meat during storage. Therefore, these results may indicate that RO-treated DSW can not be used as drinking water of chickens because it negatively affects the quality of chicken meat.

Technical and Economical Assessment of Adsorption and Reverse Osmosis for Removal of Ammonia from Groundwater of Kathmandu, Nepal (네팔 카트만두 지하수에서 암모늄 제거를 위한 이온 교환 및 역삼투의 기술 및 경제 평가)

  • Kunwar, Pallavi;Ahn, Jaewuk;Baek, Youngbin;Yoon, Jeyong
    • Journal of Appropriate Technology
    • /
    • v.6 no.2
    • /
    • pp.174-182
    • /
    • 2020
  • The permissible limit of ammonia concentration in drinking water recommended by the World Health Organization (WHO) is 1.5 mg/L. However, in the case of groundwater in Kathmandu, Nepal, the concentration of ammonia fluctuates dramatically from 0 to 120 mg/L at different locations and groundwater depths (Chapagain et al., 2010). Such a high concentration of ammonia causes aesthetic problems in drinking water, such as bad taste and odor; hence, prior treatment is required. In Kathmandu, half of the population utilizes groundwater, which is also employed for drinking water, but owing to a lack of knowledge of household water filters, residents of Kathmandu tend to depend greatly on commercially available jar water than on the installation of a proper household filtration method. Thus, in our study, we employed adsorption and reverse osmosis (RO) as two of the most viable decentralized/household treatment options to address the issue of high contamination of ammonia in drinking water. We evaluated their performances from technical and the economic perspectives using synthetically prepared groundwater at varying ammonia concentrations (50 mg/L and 15 mg/L). Consequently, it was found that adsorption via ion exchange (IE) resin was a comparatively better ammonia removal technology than RO, with 100% ammonia removal even after regeneration; the removal by RO was limited to up to 90%. Furthermore, our study suggests that IE is the most suitable ammonia removal technology for places with lower water consumption (< 50 L/day), whereas RO seemed to be a cost-effective technology for places with higher water consumption, where the daily water demand exceeds 50 L/day. Lastly, these assessments suggest that installing a suitable household treatment system would be more efficient and sustainable from both technical and economic points of view than purchasing commercially bottled water.

Characterization of Quorum-Quenching Bacteria Isolated from Biofouled Membrane Used in Reverse Osmosis Process (Biofouling이 일어난 역삼투막에서 분리한 쿼럼 저해 세균의 특성)

  • Moon, Sooyoung;Huang, Xinxin;Choi, Sung-Chan;Oh, Young-Sook
    • Korean Journal of Microbiology
    • /
    • v.50 no.2
    • /
    • pp.128-136
    • /
    • 2014
  • Acyl homoserine lactone (AHL) lactonase has been proved to be the AHL-degrading enzyme with the highest substrate specificity for AHL molecules and has shown a considerable potential as low-cost and efficient quorum quenching (QQ) technique. However, few studies focused on its inhibitory effect on biofilm formation which is also a quorum sensing (QS)-regulated phenomenon. In this study, QQ activity of six isolates from biofouled reverse osmosis membranes was studied using Chromobacterium violaceum CV026 and Agrobacterium tumefaciens NTL4 as biosensors under various conditions. All of the isolates belonged to the genus Bacillus and showed QQ activity regardless of the acyl chain length or substitution of AHL molecule. The isolates were capable of significantly inhibiting biofilm formation (46.7-58.3%) by Pseudomonas aeruginosa PAO1 and produced heat-sensitive extracellular QQ substances. The LC-MS analysis of the QQ activity of a selected isolate, RO1S-5, revealed the degradation of N-(3-oxododecanoyl)-L-homoserine lactone (3-oxo-C12 AHL) and the production of corresponding acyl homoserine (3-oxo-C12-HS), which indicated the activity of AHL lactonase. The broad AHL substrate range and high substrate specificity suggested that the isolate would be useful for the control of biofilm-related pathogenesis and biofouling in industrial processes.

Studies on the Fouling Reduction by Coating of Cationic Exchange Polymer onto Reverse Osmosis Membrane Surfaces (역삼투막 표면의 양이온 교환 고분자 코팅에 의한 파울링 감소 연구)

  • Park, Chan Jong;Kim, Sung Pyo;Cheong, Seong Ihl;Rhim, Ji Won
    • Polymer(Korea)
    • /
    • v.36 no.6
    • /
    • pp.810-815
    • /
    • 2012
  • The cation exchange polymer, poly(styrene sulfonic acid) (PSSA), was coated onto polyamide (PA) thin film composite reverse osmosis (RO) membranes. Then these membranes were investigated for the model foulants, bovine serum albumin (BSA), humic acid (HA), and sodium alginate (SA) to check whether there are some improvement. The contact angle of PSSA coated PA RO membrane showed $58^{\circ}$ from $78^{\circ}$, the value of PA RO membrane, which confirmed successful hydrophilization. As the operating pressure increased (2, 4, 8 atm for BSA, HA and SA 100 ppm in feed solution), the fouling phenomena was worse for both none- and PSSA-coated membranes. The fouling increased in the order of BSA>SA>HA due to the interactions between sulfonic acid in PSSA and functional groups of foulants. On the other hand more significant fouling reduction was observed in the order of HA>SA>BSA. The photographs of scanning electron microscopy showed the same trend. As a result, there was the improvement of fouling phenomena for the PSSA coated RO membranes, distinctly in the case of HA.

Studies on the Fouling Reduction through the Coating of Poly (vinyl alcohol) on Polyamide Reverse Osmosis Membrane Surfaces (역삼투막 표면에 폴리비닐알코올 코팅을 통한 파울링 현상 감소연구)

  • Kim, Il Hyoung;Ji, Eun Hee;Rhim, Ji Won;Cheong, Seong Ihl
    • Membrane Journal
    • /
    • v.22 no.4
    • /
    • pp.272-279
    • /
    • 2012
  • The neutral polymer, poly (vinyl alcohol) (PVA), was coated onto polyamide (PA) thin film composite reverse osmosis (RO) membranes. And then these membranes were investigated for the model foulants, bovine serum albumin (BSA), humic acid (HA), and sodium alginate (SA) whether there are aome improvement. As the operating pressure increased with 2, 4, 8 atm for BSA, HA and SA 100 ppm in feed solution, the fouling phenomena was worse for both none and PSSA coated membranes. The fouling occurred in the sequence of BSA > HA > SA due to the interactions between PVA snd functional groups of foulants, and on the other hand the fouling reduction was observed in the order of HA > BSA > SA. The observation of scanning electron microscopy photographs showed the same trend. As a result, there should be the improvement of fouling phenomena for the PVA coated RO membranes and the case of HA was shown distinct.

Treatment of AP Solutions Extracted from Solid Propellant by NF/RO Membrane Process (NF/RO 멤브레인 공정을 적용한 고체추진제에서 추출된 암모늄 퍼클로레이트 (AP) 처리 연구)

  • Kong, Choongsik;Heo, Jiyong;Yoon, Yeomin;Han, Jonghun;Her, Namguk
    • Membrane Journal
    • /
    • v.22 no.4
    • /
    • pp.235-242
    • /
    • 2012
  • Ammonium perchlorate (AP) is primarily derived from the process of liquid incineration treatment when dismantling a solid rocket propellant. A series of batch dead-end nanofiltration (NF) and reverse osmosis (RO) membrane experiments were conducted to explore the retention mechanisms of AP under various hydrodynamic and solution conditions. Low levels of silicate type of siloxane had been detected through the GC/MS and FTIR analysis of liquid solutions extracted from solid ammonium perchlorate composite propellant (APCP). It is indicated that NF/RO membranes fouling in the presence of APCP was mainly attributed to the AP interactions because the concentration of silicate type of siloxane was negligible compared to that of AP. The osmotic pressure of AP was presumably resulted in the flux declines ranging from 13 to 17% in the case of the application of low-pressure (551 and 896 kPa for NF and RO) compared to those in application of high-pressure. The retention of AP by NF/RO membranes significantly varied from approximately 10 to 70% for NF and 26 to 87% for RO, depending on the operating and solution water chemistry conditions. The results suggested that retention efficiency of AP was fairly increased by reducing concentration polarization (i.e. application of low-pressure and stirring speed of 600 rpm) and increasing the pH of a solution. The result of this study was also consistent with the previous modeling of 'solute mass transfer of NF/RO membranes' and demonstrated that hydrodynamic and solution water chemistry conditions are to be a key factor in the retention of AP by NF/RO membranes.