• Journal of Korean Society of Water and Wastewater
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• v.33 no.6
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• pp.437-446
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• 2019

Reverse osmosis seawater desalination facilities can extend the cleaning cycle and replacement time of the reverse osmosis membrane by pretreatment process. Selection of pretreatment process depends on water quality. It was attempted in this study to select approriate pretreatment process for the Masan bay, which was high in particles and organic content. For this purpose, performances of pretreatment processes such as filter adsorber (FA), pore controllable fiber (PCF), and ultrafiltration (UF) were compared based on the silt density index (SDI). The SDI value of the filtrate should be less than 3. The study results showed that UF can produce the filtrate quality satisfying the requirement. However, the transmembrane pressure (TMP) of UF increased quickly, reaching 0.6 bar within 4 days. In order to secure stable operation, FA and PCF were combined with UF. The study results showed that combination of PCF and UF was able to extend the filtration duration (more than 2 months) until to reach TMP of 0.6 bar.

• Journal of Korean Society of Water and Wastewater
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• v.33 no.4
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• pp.281-289
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• 2019

Desalination plants are generally studied with higher operating costs compared to water supply facilities. This study was conducted to reduce the cost of water production and to preserve existing water resources. Therefore, the purpose of this study was to utilize the control valves to increase maximum efficiency, thereby reducing the power of the pumps and operating costs. Specific energy consumption was shown to reduce the process operating power by up to 1.7 times from 6.17 to $3.55kWh/m^3$ based on seawater reverse osmosis 60 bar. In addition, the water intake process was divided into pre, inter, and post-according to the use method of blasting, and the water treatment process was divided into pre, inter, and post blending. In order to reduce power consumption, the blending process was combined to operate the facility, which resulted in the reduction of power consumption in the order post > pre-inter> inter blending.

• Membrane and Water Treatment
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• v.5 no.2
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• pp.73-86
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• 2014

Membrane fouling is a major challenge limiting the use of membrane applications. In this study high induced shear rates were utilized at the membrane surface in order to reduce the organic and inorganic scaling by using the torsional vibration of flat sheet membranes. The performances of a vibratory shear-enhanced processing (VSEP) system for the ultrafiltration (UF), nanofiltration (NF) and reverse osmosis (RO) membrane filtration of industrial dairy wastewater were investigated. The vibration and non-vibration methods were compared with the same membrane and operational parameters during the purification of real dairy industrial process wastewater. In the initial experiments, short-term tests were carried out in which the effects of vibration amplitude, recirculation flow rate and transmembrane pressure were measured and compared. The permeate flux, turbidity, conductivity and chemical oxygen demand (COD) reduction of dairy wastewater were investigated by using UF, NF and RO membranes with vibration and non-vibration methods. In the subsequent experiments, concentration tests were also carried out. Finally, scanning electron microscopy (SEM) revealed that the vibration method gave a better performance, which can be attributed to the higher membrane shear rate, which reduces the concentration of solids at the membrane, and the transmission.

• Proceedings of the Membrane Society of Korea Conference
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• 1995.04a
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• pp.26-27
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• 1995

Most of synthetic polymeric membranes used in ultrafiltration, reverse osmosis and microfiltration processes are prepared by phase inversion(or phase separation) technique. In this technique, a homogeneous polymer solution is cast into thin film or hollow fiber shape and then immersed into a nonsolvent coagulant bath. The exchange of solvent and nonsolvent across the interface between casting solution and coagu!ant can make the casting solution phase-separate and form a membrane with a symmetric or asymmetric structure. Because of importance of this technique in membrane field, many investigations have been dedicated to elucidate the mechanism of membrane formation by phase inversion technique.[1-10] These investigation have suggested that the structure formation and permeation properties of phase inversion membrane depend on the variables such as the nature and content of casting solution and coagulant, temperature of casting solution and coagulant, and the diffusional exchange rate of solvent and nonsolvent etc. which can be related to the thermodynamic and kinetic properties of the casting system. The variables such as the nature and content of casting solution can also be the important factor affecting the structure formation and permeation property of the phase inversion membrane.

• Environmental Engineering Research
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• v.20 no.3
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• pp.285-289
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• 2015

Complicated and expensive seawater desalination technology is a big challenge in boron removal process. Conventional seawater desalination process of coagulation utilized for pre-treatment is difficult to remove boron. Boron can be removed more effectively in Reverse Osmosis (RO) process than any other processes. In this study, a coagulant with the name Mineral Cluster was examined its boron removal ability. Boron removal efficiency of Mineral Cluster depended on pH value and Mineral Cluster dosage. Desalination process combines the pre-treatment process with Mineral cluster diluted at the ratio of 1:2500 and the RO membrane process. The original sea water could be desalinated to drinking water quality, 1 mg/L, without any pH adjustments. Therefore, if the Mineral cluster is added without any other chemicals for adjusting pH, the desalination process would be much safer, efficient and economical.

• Proceedings of the Membrane Society of Korea Conference
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• 2008.05a
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• pp.176-179
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• 2008

• Proceedings of the Membrane Society of Korea Conference
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• 1994.10a
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• pp.60-61
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• 1994

복합막은 기존의 비대칭막에 비해서 극히 얇은 표면층을 형성할 수 있다. 이러한 복합막은 배제율도 우수할 뿐만아니라 투과속도 또한 매우 큰 특징을 가지고 있으며, 해수의 담수화를 비롯하여 초순수 제조 등 각종 산업분야에서 많이 응용되고 있다. 우수한 분리막을 제조하기 위해서는 막의 표면층을 보다 더 치밀하고 얇게 형성할 수 있어야 한다. 이렇게 하기 위해서는 지지막 또한 매우 중요한 요인으로 작용한다. 표면층이 치밀하고, 가능한 한 porosity가 큰 지지막을 제조해야한다. 따라서 본 연구에서는 고분자 물질로 Polyethersulfone을 사용하여 지지막을 만들었다. 이 지지막위에 계면중합법으로 NF/RO용 복합막을 제조하였다. 높은 투과 속도 및 염의 배제율이 우수한 복합막을 제조하기 위해서 먼저 Polymer 농도, 첨가제 종류및 농도 등에 의한 각종 제막조건에 따른 지지막의 성능을 조사하였다. 여기에 Monomer 농도를 변화시켜서 계면중합으로 복합막을 제조하여 그 성능 변화를 측정하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.06a
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• pp.183-205
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• 1997

산업발전에 따라 발생하는 각종 오염물질에 의한 양질의 물 부족현상을 해결하거나 산업적으로 특정물질을 분리하기 위하여 새로운 분리기술이 개발되고 있으며 이는 앞으로 인류에 대한 가장 절실한 기술로 떠오를 것이다. 이러한 측면에서 분리막은 가장 효율절인 분리기술로 여겨져 지난 30년간 눈부신 발전을 해왔고 최근 국내에서도 소재개발과 함께 이를 응용한 분리막 System개발이 활발히 이루어지고 있다. 분리막에 의한 공정은 상변화가 없는 분리공정이므로 에너지 측면에서 효율적이며 공정자체가 간단하여 점차 보편적인 기술로 자리를 잡아가고 그 기본원료가 부직포, 중공사나 장단섬유이므로 주로 화섬회사 위주로 소재개발이 주로 되고 있다. 본 발표에서는 최근에 국내에서 생산되기 시작한 역삼투막의 제조 방법과 특성 및 개발동향을 총괄적으로 소개하고자 한다.

• Proceedings of the Membrane Society of Korea Conference
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• 1998.04a
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• pp.124-126
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• 1998

1. INTRODUCTION : With good physical and chemical properties as a membrane material, poly(vinyl alcohol) (PVA) has been widely used for the preparation of several kinds of membranes for different applications. Considering such good physical chemical properties, some people have tried to use it for the formation of reverse osmosis (RO) membranes with a good chemical stability as well as high flux and high rejection rate. However, unfortunately, the performance of the RO membranes based on PVA has not been satisfactory yet. The PVA RO membranes thermally crosslinked have shown very low flux and relatively low salt rejection. In this experiment, ionic polymers such as sodium alginate and chitosan were used together with PVA to increase the nanofiltration performance of the PVA membranes.

• Proceedings of the Membrane Society of Korea Conference
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• 1998.10a
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• pp.156-158
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• 1998

원자력 발전소에서 사용하는 1차 냉각수에 대해 살펴보면, 일차냉각수의 pH는 5~8 범위이며, 수질기준은 염소이온과 불소이온이 0.15 ppm, 현탁고형물 이 0.2 ppm이나 실제 농도는 기준치보다 훨씬 낮은 매우 순수한 상태로 유지된다. 다만, 핵분열 반응도를 제어하기 위해 주입되는 붕소가 수백 ppm정도, pH를 조절하기 위해 부가되는 리튬의 1 ppm정도 포함되며, 그밖에 1ppm 정도의 실리카가 포함될 수 있다. 붕산으로 포화 운전되는 이온교환 수지탑 내에서는 붕산보다 이온선택도가 낮은 실리카는 이온교환수지에 흡착되지 않기 때문에 발전소의 가동년수의 증가에 ㄷ아라 원자로 냉각제의 실리카 농도는 점차 증가하게 되었다.