• 한국태양에너지학회:학술대회논문집
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• 한국태양에너지학회 2011년도 춘계학술발표대회 논문집
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• pp.74-79
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• 2011

This study was accomplished to evaluate the performance of Multi Effect Distillation(MED) for solar thermal desalination system. It was designed Multi effect distillation with $3m^3/day$ capacity and Shell&Tube type heat exchanger. Also, The effective heat transfer of Shell&Tube heat exchanger was used Cu(90%)-Ni(10%) corrugated tube. The parameters relating to the performance of Multi Effect Distillation are known as hot water flow rate. The experimental conditions for each parameters were $18^{\circ}C$ for sea water inlet temperature, $6m^3/hour$ sea water inlet volume flow rate, $75^{\circ}C$ for hot water inlet temperature, 2.4, 3.6, and $4.8m^3/hour$ for hot water inlet volume flow rate, respectively. The results are as follows, Development for Multi effect distillation was required about 40kW heat and 35kW cooling source to produce $3m^3/day$ of fresh water. And, Performance ratio of Development Multi effect distillation was about 2.0191.

• 한국태양에너지학회 논문집
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• 제31권1호
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• pp.1-7
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• 2011

This study was accomplished to evaluate the performance of Multi Effect Distillation(MED) for solar thermal desalination system. It was designed Multi effect distillation with $3m^3$/day capacity and Shell&Tube type heat exchanger. Also, The effective heat transfer of Shell&Tube heat exchanger was used Cu(90%)-Ni(10%) corrugated tube. The parameters relating to the performance of Multi Effect Distillation are known as hot water flow rate. The experimental conditions for each parameters were $18^{\circ}C$ for sea water inlet temperature, $6m^3$/hour sea water inlet volume flow rate, $75^{\circ}C$ for hot water inlet temperature, 2.4, 3.6, and $4.8\;m^3$/hour for hot water inlet volume flow rate, respectively. The results are as follows, Development for Multi effect distillation was required about 40kW heat and 35kW cooling source to produce $3m^3$/day of fresh water. Based on the results of this study, It makes possible to secure economics of desalination system with solar energy which is basically needed development of high efficiency fresh water generator.

• Membrane and Water Treatment
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• 제10권5호
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• pp.387-394
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• 2019

Membrane distillation (MD) is one of the water treatment processes which involves the momentum, heat and mass transfer through channels and membrane. In this study, CFD modeling has been used to simulate the heat and mass transfer in the direct contact membrane distillation (DCMD). Also, the effect of operating parameters on the water flux is investigated. The result shows a good agreement with the experimental result. Results indicated that, while feed temperature is increasing in the feed side, water flux improves in the permeate side. Since higher velocity leads to the higher mixing and turbulence in the feed channel, water flux rises due to this increase in the feed velocity. Moreover, results revealed that temperature polarization coefficient is rising as flow rate (velocity) increases and it is decreasing while the feed temperature increases. Lastly, the thermal efficiency of direct contact membrane distillation is defined, and results confirm that thermal efficiency improves while feed temperature increases. Also, flow rate increment results in enhancement of thermal efficiency.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 춘계학술대회 초록집
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• pp.201-201
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• 2010

The evaporative desalination system with solar energy would be the efficient and attractive method to get fresh water. This study was described the development of Multi Effect Distillation(MED) with solar energy desalination system. The system was designed and manufactured Multi effect distillation on the capacity of $3m^3$/day. The experimental apparatus consists mainly of ejector pump, Hot water pump, flow meter, demister, cooler, evaporator and condenser. Evaporator and condenser were made Shell&Tube Heat Exchanger type with corrugated tube. The experimental variables were chosen $75^{\circ}C$ for hot water inlet temperature, 40, 60 and $80{\ell}$/min for hot water inlet volume flow rate, 6.0 and $8.0{\ell}$/min for evaporator feed seawater flow rate, $18^{\circ}C$ for sea water inlet temperature to cover the average sea water temperature and the salinity of sea water is measured about 33,000 PPM (parts per million). for a year in Korea. This study was analyzed the results of thermal performance of Multi Effect Distillation. The results are as follows, The experimental Multi effect distillation is required about 40 kW heat source for production of $3m^3$/day fresh water. Various operating flow rate was confirm in the experiments to get the optimum design data and the results showed that the optimum total flow was $8.0{\ell}$/min. Comparison of Single Effect Distillation with Multi Effect Distillation showed MED is at least more than double of SED.

• Membrane and Water Treatment
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• 제10권5호
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• pp.321-330
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• 2019

The objective of this study was to examine the recovery of the power plant cooling tower blowdown water (CTBD) by membrane distillation. The experiments were carried out using a flat plate poly vinylidene fluoride (PVDF) membrane with a pore diameter of $0.22{\mu}m$ by a direct contact membrane distillation unit (DCMD). The effects of operating parameters such as transmembrane temperature difference (${\Delta}T$), circulation rate and operating time on permeate flux and membrane fouling have been investigated. The results indicated that permeate flux increased with increasing ${\Delta}T$ and circulation rate. Whereas maximum permeate flux was determined as $47.4L/m^2{\cdot}h$ at ${\Delta}T$ of $50^{\circ}C$ for all short term experiments, minimum permeate flux was determined as $7.7L/m^2{\cdot}h$ at ${\Delta}T$ of $20^{\circ}C$. While $40^{\circ}C$ was determined as the optimum ${\Delta}T$ in long term experiments. Inorganic and non-volatile substances caused fouling in the membranes.

• 방사성폐기물학회지
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• 제8권1호
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• pp.65-70
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• 2010

비등온 및 등온조건에서의 열중량분석을 이용하여 다양한 압력조건(0.5 - 50 mmHg)에서 LiCl-KCl 공융염 증류속도를 우선 측정하였다. 비등온조건에서의 열중량분석결과로부터 온도의 함수로 표현될 수 있는 증류 속도식을 도출하였다. 이 속도식에 의해 계산된 휘발플럭스(flux)는 등온조건에서의 열중량분석을 통해 얻어진 증류속도와 일치하였다. 1300 K 이하의 온도조건과 0.5 mmHg와 50 mmHg 사이의 감압조건에서 $10^{-4}-10^{-5}$ mole $cm^{-2}sec^{-1}$의 증류속도를 얻을 수 있다. 실험실규모 실험장치에서 50 mmHg의 압력과 1150 K 이상의 온도 조건에서 한 시간 증류로 약 99%의 염이 분리되었다. 희토류 침전물내에 잔류하는 염을 증류에 의해 제거할 때 휘발시간이나, 온도를 증가시키는 것보다 휘발 계면적을 증가시키는 것이 효과가 더 큰 것으로 나타났으며, 휘발면적을 $4.52cm^2$에서 $12.56cm^2$로 증가시켜 한 시간 동안 증류하였을 때 99.95% 이상의 염이 분리되었다.

• International journal of advanced smart convergence
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• 제4권1호
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• pp.127-136
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• 2015

This paper is a study of a simple distillation process. Its objective is to compare fuel production from plastic waste, its data collecting is from the factory and simple data calculated a suitable evaluation on the simple distillation plant built before calculation. The experiment with a simple distillation process is separated into three sections. The first section is a simple distillation process of distillation producing diesel using heat source by biomass. The second section is distillation process which produces fuel using heat source by burner. The third section uses heat source by burner incorporate with biomass. The experiment reveals that the result of the second section is the most efficient. In comparison with the experiments and the simple calculation, the result on the efficiency of work has error less than 5% and it is sufficient for the next experimental process. Thus, the study and design on a simple distillation process produces fuel from plastic waste has to concern mainly on design heat exchangers, flow rate and optimized temperature. Further study on this plant can be developed throughout the county due to its low cost and efficiency.

• Applied Biological Chemistry
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• 제37권1호
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• pp.9-13
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• 1994

백하주의 증류현상을 살피보기 위하여 전통약주인 백하주를 제조하고 압력(760, 460, 260 mmHg)과 환류비(3.1 : 1, 1 : 1) 및 충전물질의 유무에 따른 증류조작에 대하여 연구한 결과는 다음과 같다. 백하주의 alcohol함량은 14.2%, 산도는 8.3 g/100 ml, ethyl acetate는 49 ppm, fusel oil은 657 ppm이었다. 증류가 진행됨에 따라 증류액의 alcohol 농도는 감소하였으며, 분액별 alcohol 농도는 상압이 감압 보다 높았다. Still액과 증기상의 alcohol 농도의 관계를 나타내는 기울기는 압력이 높을수록 크게 나타났다. 비환류시 증류종말점은 8분액 이었지만 환류시는 5분액 이었다. 또한 환류시 alcohol 평균농도는 환류비가 높을수록 증가하였으며, 상압상태에서 환류비가 3.1 : 1과 1 : 1 일 때 각각 0.56, 0.54 mole이었다. 증류속도는 증류가 진행됨에 따라 감소하였으며, 상압보다 감압에서 빨랐고 충전상태의 260 mmHg에서 0.14 ml/sec로 가장 빨랐다. 환류시는 환류비가 높을수록 감소하였고 평균 증류속도는 상압상태에서 환류비가 3.1 : 1과 1 : 1일 때 각각 0.05, 0.06 ml/sec이었다.

• 멤브레인
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• 제24권3호
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• pp.240-248
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• 2014

열유도상분리법(TIPS) 및 연신의 복합공정을 적용하여 막증류(Membrane distillation, MD)용 다공성 PVDF 중공사 분리막을 제조하였다. 분리막의 투과도를 증가시키기 위하여 분리막 투과도를 향상시킬 수 있는 성능인자들 중 분리막의 벽두께를 감소시키고자 하였다. 분리막의 두께를 감소시키기 위하여 분리막 제조 시 토출량을 감소시키고 중공 형성 시 주입하는 bore fluid 주입량을 증대시켰다. 토출량의 감소 및 bore fluid의 증가에 따라 벽두께는 감소하였고, 공기투과도와 수투과도는 크게 증가하였으며, 결과적으로 막증류 공정에 적용 시 투과플럭스도 증가하는 경향을 보여 주었다.

• 한국산학기술학회논문지
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• 제13권8호
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• pp.3774-3778
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• 2012

Reformate 분리 공정에 대한 열복합 증류탑의 가능한 제어 구조를 조사하고 그 제어 성능을 검토하기 위하여 동적 모사를 수행하였다. Aspen HYSYS를 사용하여 $3{\times}3$ 제어구조를 적용하여 여러 가지 제어구조로 동적 모사한 결과 Reformate 분리 공정 주탑의 상부, 중간, 하부 제품 조성은 각각 reflux flow rate, 주탑에서 전처리탑 상부로 흐르는 liquid draw rate, vapor boilup rate로 제어되는 구조가 가장 운전 안정성이 확보됨을 확인하였다.