The production process of ultra-pure water (UPW) involves dozens of unit processes such as reverse osmosis (RO), pretreatments, membrane degasifier, and several ion exchange processes. Recently, continuous electrodeionization (CEDI) has replaced the 2-bed and 3-tower (2B3T) ion exchange process. As a result, the majority of wastewater in UPW production now comes from the RO concentrate. The important of RO in UPW production is to produce high-quality water with a low ion concentration (around 1 mg/L) for CEDI feed water. Minimizing RO concentrate is essential to reduce the wastewater produced in the UPW production process. This can be achieved by maximizing the recovery of the RO system. However, increasing the recovery is limited by the water quality of the RO permeate. To ensure high-quality permeate water, the RO system is designed with a two-pass configuration. The recovery of each pass in the RO system is limited (e.g., < 85%) due to the expected increase in permeate water concentration at higher RO feed water concentrations. Interestingly, tests using 4-inch RO modules with low concentration feed water (≤ 35 mg/L as NaCl) revealed that the permeate concentration remains almost constant regardless of the feed water concentration. This implies that the recovery of the first RO pass can be increased as long as the average feed/concentrate concentration of the second RO pass is less than 35 mg/L. According to this design criterion for the RO system, the recovery of the first and second RO pass, with a feed water concentration of 250 mg/L as NaCl, can be increased up to 94.8% and 96.0%, respectively. Compared to the conventional RO system design (e.g., 70% and 80% for the first and second RO pass) for UPW production, this maximum recovery design reduces the volume of RO feed and concentrate by up to 38.4% and 89.2%, respectively.

중수는 경수와 다른 물리화학적 특징으로 다양한 생물화학적 변화를 유도할 수 있다. 기존 분리공정의 단점인 에 너지소비량을 줄이고자 전기방사 폴리아마이드 분리막을 이용하여 정삼투공정을 이용하였다. 유도용액으로 NaCl과 인산을 사용하였다. 중수농도를 정량화하기 위해 FT-IR 분광법을 활용하였다. 인산과 수소/중수소의 특별한 상호작용력을 분광학적 으로 확인하였으며, 정삼투공정으로 농축이 가능할 수 있다는 것을 관찰하였다.

This study was conducted to evaluate the filtration performance according to the feed temperature composed of NaCl and the operating pressure of the brackish water reverse osmosis (BWRO) process. The temperature is known that decides the filtration performance of reverse osmosis (RO). It is noted that temperature increase activates the permeate of salts due to augment of diffusivity and mass transfer. Filtration of the lab-scale RO system was performed with constant pressure and the constant flow was simulated. The salt rejection measured by the concentration of the feed and permeate was compared with water permeability and salt permeability in the conditions containing various temperatures (5, 10, 15, 20, 25, and 30℃) and pressures (10, 12, 15, and 18 bar). An increase in feed temperature from 5 °C to 30 °C caused a 4.65% decrease in salt rejection in CSM, due to an increase in salt permeability (4.06 times) rather than an increase in water permeability (2.62 times). Specific energy consumption (SEC) was calculated by using an electricity meter set in the RO system. It was expected that the SEC by the increases in temperature and pressure decreased due to the viscosity decline of the feed and the permeate flux augment, respectively. The SEC decreased by 63.4% in CSM and by 54.3% in Nittodenko when the feed temperature increased from 5 °C to 30 °C. It discussed how to operate the optimal RO process through the effect of temperature and operating pressure and the comparison of SEC.

In this study, the effect of osmotic drying conditions of mangoes on hot air drying was investigated. Four different osmotic agents of 60 Brix, such as S60, SM10, HF80, and SG25, were prepared. Mango slabs were osmotically dried with the agents at a ratio of 1:4 (w/w) for up to 8 hours. SG25 showed the lowest weight reduction and moisture loss during the process. As a result of hot-air drying, all samples showed a high correlation with the Page model (0.9761~0.9997), and the required drying time of all samples that were osmotically dried was reduced compared to the non-osmotically dried group. After hot-air drying, the pH value increased according to the drying temperature. The L, a, and b values and the total polyphenol content also decreased. Through this study, the possibility of osmotic drying was confirmed to increase the efficiency of hot air drying of mangoes, which is expected to contribute to the industrial use of domestic mangoes.

In this study, using the developed pilot device, an experiment was conducted with groundwater according to the calcium carbonate concentration and silica concentration for a certain period of time to determine the degree of RO membrane contamination according to water quality. In addition, using wastewater with severe fouling of raw water, the treatment efficiency is compared through an experiment with a pilot device, the operation progress is evaluated for the scale effect, and the stability and convenience of the developed product are considered.

무삼투압차 역삼투압(Δπ= 0)은 KAIST H. N. Chang 명예교수가 2013년 발명, 2014년 미국 특허 출원, 2018년 특 허 취득(US 9,950,297) 해수담수화기술. Chang 등의 RO 기술은 삼투압 조정조와 저압 역삼투압의 2 챔버로 구성. Chang 등은 소금물을 비롯한 모든 수용액은 물과 용질(소금)로 완전 분리 가능 주장. 삼투압차 조정조, 저압 역삼투압조 2 챔버로 구성됨. 고농도 용액의 삼투압은 1908년 미국화학회지 출간된 MIT G. N. Lewis식 이용. 두 번째 특허(US 10,953,3367)에서 RO가 10~12 bar 저 삼투압차 수행 가능 증명. 세 번째 특허(Korea 10-2322755, 해외 출원 중) Singularity ZERO 활용하면 기존 RO 에 비해 물은 50% 추가, 막 면적은 1/3, 이론에너지는 1/5, 동일 용량의 S-ZERO 기술은 기존 RO 건설비의 50~60%로 예측됨.

정수기는 일반적인 산업용 막여과 수처리 공정과 다르게 운전과 휴지를 반복하는 특성이 있다. 이러한 특징 때문 에 역삼투막을 사용하는 정수기의 경우, 재정수시에 정수수의 농도가 정상적인 값보다 높게 나오는 현상(제거율이 정상값보 다 낮게 나오는 현상)이 있는데, 이를 “TDS creep”이라고 한다. 본 연구에서는 휴지시간과 농도에 따른 TDS creep 정도를 관 찰하였다. 또한, TDS creep 현상을 저감하기 위해 원수 세척, 정수부의 부피 증가 및 정수 세척 방법 등을 시험하였고 이에 대한 실질적인 효과를 관찰하였다. 이러한 방법들 중에 정수수의 세척과 같이 역삼투막의 feed side와 permeate side의 농도차 를 최소화하는 것이 TDS creep 현상을 해소하는 궁극적인 해결책임을 확인하였다.

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.

물 오염, 지구 온난화, 기후 변화를 해결하기 위한 해결책이 시급한 상황에서, 담수의 수요를 충당하고 친환경 에너지를 생산하기 위한 방법으로 염도차를 이용한 압력지연삼투공정이 제시되고 있다. 압력지연삼투공정에 대한 꾸준한 연구에도 불구하고 최근 기술의 부족과 비싼 멤브레인의 가격 등의 한계로 인해 상용화가 되지 않고 있다. 한편 멤브레인은 압력 지연삼투공정과 염도차 발전 기술에 가장 중요한 구성품이다. 염도차 발전 기술에 사용되는 산화그래핀 멤브레인과 나노복합체 멤브레인의 기술 발전 연구가 지속되고 있다. 특히 낮은 온도의 폐기물 온도에서도 높은 에너지 효율 발전이 가능하도록 효율이 높은 멤브레인과 용매 및 용질에 대한 연구가 활발하다. 높은 투과도와 분리도를 가진 멤브레인, 특히 산화그래핀 멤브레인을 사용함으로써 농도 분극을 줄이고 전력 밀도를 높이는 연구들도 진행 중이다. 본 총설에서는 압력지연삼투 멤브레 인과 이를 통한 이론적 모델링, 그 외 기술을 통해 공정의 효율을 발전시키는 방법에 대해 논의한다.