Osmotic power is to produce electric power by using the chemical potential of two flows with the difference of salinity. Water permeates through a semipermeable membrane from a low concentration feed solution to a high concentration draw solution due to osmotic pressure. In a pressure retarded osmosis (PRO) process, river water and wastewater are commonly used as low salinity feed solution, whereas seawater and brine from the SWRO plant are employed as draw solution. During the PRO process using wastewater effluent as feed solution, PRO membrane fouling is usually caused by the convective or diffusive transport of PRO which is the most critical step of PRO membrane in order to prevent membrane fouling. The main objective of this study is to assess the PRO membrane fouling reduction by pretreatment to remove organic matter using coagulation-UF membrane process. The experimental results obtained from the pretreatment test showed that the optimum ferric chloride and PAC dosage for removal of organic matter applied for the coagulation and adsorption process was 50 mg/L as FeCl3 (optimum pH 5.5). Coagulation-UF pretreatment process was higher removal efficiency of organic matter, as also resulting in the substantial improvement of water flux of PRO membrane.

Pretreatment system of desalination process using seawater reverse osmosis(SWRO) membrane is the most critical step in order to prevent membrane fouling. One of the methods is coagulation-UF membrane process. Coagulation-UF membrane systems have been shown to be very efficient in removing turbidity and non-soluble and colloidal organics contained in the source water for SWRO pretreatment. Ferric salt coagulants are commonly applied in coagulation-UF process for pretreatment of SWRO process. But aluminum salts have not been applied in coagulation-UF pretreatment of SWRO process due to the SWRO membrane fouling by residual aluminum. This study was carried out to see the effect of residual matal salt on SWRO membrane followed by coagulation-UF pretreatment process. Experimental results showed that increased residual aluminum salts by coagulation-UF pretreatment process by using alum lead to the decreased SWRO membrane salt rejection and flux. As the salt rejection and flux of SWRO membrane decreased, the concentration of silica and residual aluminum decreased. However, when adjusting coagulation pH for coagulation-UF pretreatment process, the residual aluminum salt concentration was decreased and SWRO membrane flux was increased.

합성 지표수 용액을 가압식 한외여과 시스템을 통하여 100 L/m2/h 정속 및 0.15bar 정압 조건에서 전량 여과하였다. 공극 크기 0.05μm의 중공사막으로 구성된 가압식 모듈을 통해 실리카(SiO2) 입자 50, 10, 2 mg/L와 알긴산 나트륨(SA) 10, 2, 0.4 mg/L가 혼합된 용액을 여과하였다. 여과 공정은 30분 여과 후 30초 역세와 30초 정세의 주기적 물리 세정과 병행하여 수행되었다. 실험 결과 높은 농도 조건에서 정속 / 정압 여과조건에 따른 파울링 거동은 큰 차이를 보이지 않았으나, 낮은 농도 조건에서는 정속 여과가 정압 여과에 비해 파울링 속도가 빠른 것으로 관찰되었다. 모델링 결과 이는 정속 여과에서 막간 차압 증가에 의한 케이크 층 압축에 의한 것으로 나타났다.

호소수에 대한 막여과 공정 설계 및 운영인자를 도출하기 위하여 부산시 소재 회동 수원지의 물을 원수로 하는 200 m3/일 용량의 정수처리 침지식 막여과 pilot을 운영하였다 (운영기간 : 2018년 1월 ~ 9월). 막여과 공정 운영 관점에서 주요한 원수 수질변화로는 1월 ~ 2월 사이 수온이 5 ℃ 이하를 유지하였고, 6~7월의 평균 탁도는 24±40 NTU 이었으며, 7월 중 태풍 발생으로 인하여 약 229 NTU의 고탁도가 유입되었다. 막여과 pilot 운영결과를 바탕으로 막여과 공정의 주요 설계값인 막여과 유속, 막여과 차압, 약품 세척 주기 및 단위공정의 운전순서를 결정하였다. 운영결과 중에서 특별히 괄목할 만한 관찰점은 막여과 배출수 탁도의 중력침전 제거율이 평균 94±4%로 분석된 것이다.

In this research, the applicability of modified fouling index (MFI) on ultrapure water (UPW) production system was assessed to predict performance of reverse osmosis (RO) process. The practical study on MFI-UF was first performed at a pilot-scale UPW plant (Hwaseong-si, Gyeonggi-do, Korea), monitoring water quality parameters (i.e., conductivity, turbidity and TOC) as well as MFI-UF of pretreatment stage for 10 months. While water quality parameters were maintained in a stable manner, the MFI-UF was fluctuated implying the different propensity of RO influent. The increment of fouling potential was intimately related with RO performance, the aggravation of permeate quality. The sensitivity of MFI-UF was also verified by evaluating the fouling potential of reclaimed water in UPW production system.

지표수 성상을 재현한 용액을 가압식 한외여과 시스템을 통하여 100 L/m²/h 정속 조건에서 전량 여과하였다. 공극 크기 0.05 μm의 한외여과 중공사막으로 구성된 가압식 모듈을 통해 휴민산(HA) 10 mg/L 용액과 알긴산 나트륨(SA) 10mg/L 용액, 그리고 이 두 용액에 실리카(SiO2) 입자 50 mg/L이 포함된 총 4가지 용액을 여과하였다. 여과 공정은 30분 여과 후 30초 역세와 30초 정세의 주기적 물리 세정과 병행하여 수행되었다. 실험 결과, HA와 SA 용액에 SiO2 입자가 존재하는 경우 파울링 속도는 다소 감소하였으며 특히 SA 여과에서 SiO2 입자 위에 형성된 SA 케이크층이 세정에 의해 SiO2 입자와 함께 탈착되어 물리세정에 의한 분리막 성능 회복이 크게 증가하는 것으로 나타났다.

A series of amphiphilic block copolymers consisting of hydrophobic poly(methyl methacrylate) (PMMA) and poly(polyethylene glycol methyl ether methacrylate) (PPEGEMA) were synthesized by Cu based ATRP and utilized as an additive to prepare asymmetric ultrafiltration (UF) membranes by non-solvent induced phase separation (NIPS) with PVDF. Obtained PVDF based UF membranes gave in-situ hydrophilic surfaces on the hydrophobic PVDF matrix because of strong compatibility PMMA block segment to PVDF and the hydrophilicty of PPEGMA block segment to the non-solvent (water), which showed improved water flux in comparison to neat PVDF UF membrane.

본 연구에서는 파일럿 및 상용급 규모에서 UF 분리막을 결합한 혐기성 소화 공정을 장기간 운영하여 분리막의 성능, 소화효율, 바이오가스 생산량과 수질 등의 다양한 인자를 도출하였다. 파일럿 규모에서 막의 투과 플럭스는 15∼20 LMH, 막간 차압은 1∼3 kgf/cm2로 운전되었다. 유입수의 TCOD 와 SCOD 는 각각 113 g/L, 62 g/L 이었고, 유출수의 TCOD 와 SCOD는 UF 공정 이후 제거효 율이 93% 및 86% 로 나타났다. 상용급 규모의 운전 결과, 분리막의 투과 플럭스는 12∼15 LMH로 나타났다. 유입수의 CODcr, TS, VS는 각각 236 g/L, 62.5 g/L, 50.2 g/L였으며, 농축여과분리막을 통과 후 제거율은 각각 99%, 94% 및 98%로 조사되었다.

최근 국내외에서는 수질안정성 향상 및 부지면적 저감을 위해 막여과 공정도입이 활발한 추세이며 특히, 정수처리 분야에서는 정밀여과(Microfiltration) 및 한외여과(Ultrafiltration) 공정이 많이 적용되고 있다. 막여과 공정의 경제성 향상을 위해서는 세정 시점의 예측 및 세정 주기 연장이 매우 중요한 요소이다. 따라서, 본 연구에서는 인공신경망(Artificial neural network)을 활용하여 UF 공정차압(Transmembrane pressure) 예측 모델을 개발하고자 한다. 입력변수로는 유입수 온도, pH, 탁도 등의 일평균값을 이용하였다.

Microfiltration (MF) and Ultrafiltration (UF) membrane processes capable of producing highly purified water have been extensively applied as a pretreatment process in the wastewater reuse field with the improvement of membrane properties and resistance, development of operating protocols, and improvement of technologies of backwashing and physicochemical cleaning, and improvement of scale and antifoulants. However, despite of the development of membrane production and process technologies, fouling still remains unresolved. This study confirmed that foulants such as polysaccharides, proteins and humic substances existed in final treated effluent (secondary effluent) by fluorescence excitation emission matrix (FEEM) and fourier transform infrared spectroscopy (FTIR) analysis. In addition, when constructing ozone oxidation and coagulation processes as a hybrid process, the removal efficiency was 5.8%, 6.9%, 5.9%, and 28.2% higher than that of the single process using coagulation in turbidity, color, dissolved organic carbon (DOC), and UV254, respectively. The reversible and irreversible resistances in applying the hybrid process consisting of ozone oxidation and coagulation processes were lower than those in applying ozone oxidation and coagulation processes separately in UF membrane process. Therefore, it is considered possible to apply ozonation/coagulation as a pretreatment process for stable wastewater reuse by and then contributing to the reduction of fouling when calculating the optimal conditions for ozone oxidation and coagulation and then to applying them to membrane processes.

PVDF Membrane has been used as material for the UF membrane through in-situ interfacial polymerization (IP) because of it’s outstanding properties such as high chemical resistance, thermal stability, and mechanical strength. In this study, surface morphology change of PVDF membrane was researched depending on evaporation time. 13% PVDF 6020 was used for casting and the evaporation time period was from 5s to 600s. The surface morphology of the membrane was investigated by scanning electron microscopy (SEM) and filtration was conducted in the cross flow method to evaluate the a performance of UF membrane. As a result, average pore size was increased with longer evaporation times which caused the decrease of rejection.