• 자원리싸이클링
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• 제9권4호
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• pp.28-36
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• 2000

본 연구는 입자가 혼합된 용제를 이중판형 열교환기 내에서 가열 및 증발과정을 통해 건조이자와 용제로 분리하여 회수하기 위한 연속식 순간 진공건조 시스템 해석에관한 것이다. 진공건조시스템은 용제 공급펌프, 이중관형 열교환기, 진공 스프레이 챔버 및 응축기로 구성된다. 연속적으로 공급되는 용제는 이중관형 열교환기 내에서 가열, 팽창 및 증발되며 관 출구부에서 팽창된 증기가 진공 스프레이 챔버 내로 분사되고 증기는 응축기로 수송되어 용제로 회수되고 입자는 관성력에 의해 증기로부터 분리되어 건조된다ㅣ. 안료입자가 함유된 벤젠 및 알킬벤젠의 분리 및 회수성능 실험을 수행한 결과, 습분양 1.1%로 건조된 안료입자를 94% 회수하였고, 99.9 wt%의 고순도 벤젠을 88% 회수하였다. 평균직경이 $6.5\mu\textrm{m}$인 안료입자를 진공건조시스템의 이중관형 열교환기에서 관출구부의 고속 분사에 의한 폭발적 분산력에 의해 입경이 14%감소된 $5.6\mu\textrm{m}$ 크기의 건조 안료입자를 회수하였다. 따라서 진공건조시스템은 용제에 함유된 입자를 건조 및 분리하여 미분제 제품으로 히수하는데 효율적이며 폐용제 정제용으로 적용이 가능하다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2309-2314
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• 2007

The application analysis of bubble pump on the domestic solar water heater system is presented. The system investigated in this study is a passive device, self pumping and self regulating. It was test to use the bubble pump on solar water heater system. The test experiment has been taken on the existed vacuum tube about the efficiency, working fluid temperature and pressure and circulated power. In order to check the working temperature and working pressure effectively, the bubble pump was test separated from the solar water heater. The equipment consists of the bubble pump, heater and heat exchanger. The main structure of bubble pump was design depend on the character of two phase flow. The complete system was instrumented to measure pressures, temperatures and flow-rates at various locations. The theory analysis of design bubble pump has been given and the experiment design has been included in the paper.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2005년도 제24회 춘계학술대회논문집
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• pp.168-175
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• 2005

액체로켓 추진시스템에서 가압시스템은 발사체 추진제 탱크의 얼리지 공간에 제어된 가스를 공급하는 것이다. 가압시스템에서 고온 가스 열교환기를 적용하는 데는 가압제의 비용적을 증가시켜 전체 발사체 시스템의 중량을 감소시키는 장점이 있다. 가압시스템 성능에 있어서 주목할 만한 개선점은 극저온 시스템에서 얻어질 수 있다. 이러한 경우 가스 공급은 극저온 탱크 내부에 저장되어 진다. 극저온 가압제의 온도 특성은 가압시스템에서 구성 단품을 개발하는데 있어서 매우 중요하다. 본 연구에서는 SINDA/FLUINT를 이용한 수치적 모델링과 PTF(Propellant-feeding Test Facility)에서 수행된 실험에 대하여 해석 및 시험이 수행되었다.

• 동력기계공학회지
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• 제7권4호
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• pp.25-30
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• 2003

Hydrocyclone has been widely used for the solid-Liquid separation in many industrial sites because of its comparatively preferable applications that can be applied to wide-range panicle sizes. If seawater with impurities flows through pumps or heat exchanger, it might cause an decrease in efficiency of cooling system. In this paper, we have suggested solid methods of separating impurities from seawater in the cooling system by using a Hydrocyclone. The effects of design factors as solid concentration, cyclone inlet pressure, flow rate and diameter of underflow on the seperating performance of the Hydrocyclone were investigated. The results from the study are summarized as follows: 1) In proportion to the increase of solid concentration, the efficiency of solid-liquid separation is improved. 2) According as the cyclone inlet pressure increases the efficiency of separation is improved. Conclusively, this research suggested that the Hydrocyclone will be used as a pre-treatment system of cooling water in ships, and eventually prevent unexpected accidents in engine systems.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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• pp.194.1-194.1
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• 2011

본 연구에서는 지열히트펌프 시스템의 열원으로써 지열이외에 건축물의 미활용 에너지라고 할 수 있는 상수도의 에너지를 활용하여 지중열교환기의 천공길이를 줄이는 것이 주요 목적이며, 또한 건물의 미활용에너지를 냉난방에너지원으로써 이용 가능한 것을 보여주는 것에 있다. 실험은 4인 가족기준으로 3RT 용량의 히트펌프를 설치하고 인당 평균 177 liter/day 기준으로 하루에 약 710 liter/day의 물을 사용하는 것으로 가정하였다(환경부 2007년 상수도 통계값). 시간당 가정내에서 사용하는 물량은 일정하지 않아 일일 8시간 사용하는 것으로 하여 약 1.5 LPM 으로 실험하였다. 저수조의 크기 및 지열 히트펌프의 열원으로써 사용가능한 열량을 계산하기 위해 CFD 시물레이션을 수행하였다. CFD의 결과 상수도를 급수하기 위한 저수조의 크기는 $2m^3$로 결정하였으며 이때 열원으로써 사용가능한 열량은 약 0.7RT였다. 48시간의 실험기간 동안 저수조를 통해 얻은 열원은 0.6RT 였으며 100m의 지중열교환기를 통해 얻은 열원은 2RT 였다. 히트펌프 자체의 난방 COP는 평균 4.2를 나타내었으며 펌프등의 소비전력을 포함한 System COP는 4.0 나타내었다. 이번 연구를 통해 건물의 미활용에너지인 저수조의 물을 이용하여 지열히트펌프의 열원으로써 이용 가능하며 기존의 지열히트펌프 시스템대비 천공길이 단축, 시공비 저감이 가능한 것을 볼 수 있었다.

• Journal of Electrical Engineering and Technology
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• 제9권6호
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• pp.1921-1927
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• 2014

A new method for optimizing the magnetic field gradient in the exciting coil of electronic anti-fouling (EAF) system is presented based on changing exciting coil size. In the proposed method, two optimization expressions are deduced based on biot-savart law. The optimization expressions, which can describe the distribution of the magnetic field gradient in the coil, are the function of coil radius and coil length. These optimization expressions can be used to obtain an accurate coil size if the magnetic field gradient on a certain point on the coil's axis of symmetry is needed to be the maximum value. Comparing with the experimental results and the computation results using Finite Element Method simulation to the magnetic field gradient on the coil's axis of symmetry, the computation results obtained by the optimization expression in this article can fit the experimental results and the Finite Element Method results very well. This new method can optimize the EAF system's anti-fouling performance based on improving the magnetic field gradient distribution in the exciting coil.

• Journal of Chest Surgery
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• 제23권6호
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• pp.1049-1056
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• 1990

The OXYREX hollow fiber membrane oxygenator developed by joint work of KIST and Green Cross Medical company has been evaluated by experimental investigation and clinical application, In this oxygenator gas exchanges occur through small pores of 0.1pm size which are distributed on 70% of surface of polypropylene hollow fiber. The Oxyrex membrane oxygenator consists of 36 thousand hollow fibers and it has 3.3m2 of gas exchange surface. The Oxyrex membrane oxygenator has unique blood flow path: blood enters the oxygenator passes between the hollow fibers and exits through outlet ports, that provides low transmembrane pressure drop. In the animal experiment and in vitro investigations of Oxyrex oxygenator, it showed low transmembrane pressure difference, effective heat exchanger performance, stable gas transfer function and less blood trauma. The Oxyrex oxygenator been used from March, 1990, to October, 1990, in 40 patients undergoing open heart operations. In the clinical applications of Oxyrex, adequate oxygenation[PaO2, 283$\pm$70mmHg] and carbon dioxide removal[PaCO2, 27\ulcorner6mmHg]were maintained under the condition of FiO2: below 0.6, Hct; 25%, perfusion flow; 2.4 L/min, gas flow: 2.1 L/min. During maximum 365 minutes of cardiopulmonary bypass[CPB] time period, the Oxyrex oxygenator maintained stable condition of PaO2, PaCO2 respectively and it also kept low plasma hemoglobin level. The complement proteins C3 and CH50 were not significantly changed pre to post CPB. There were no complications related to the oxygenator during and after the CPB.

• Journal of Biosystems Engineering
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• 제30권2호
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• pp.110-113
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• 2005

Relative humidity of air In the greenhouse has to be maintained at 70 to 80 percents to provide a better growth condition of crops. To control relative humidity of air in the greenhouse, a dehumidifier functioning by refrigeration cycle was designed and manufactured in this study. And, results of its performance test in the greenhouse site were reported. The developed dehumidifier has separated condenser and evaporator in the heat exchanger part in order to increase dehumidifying capacity at a low temperature condition. When the conditions of incoming air into the dehumidifier were temperature of $15\~25^{\circ}C$ and relative humidity of $0\~95\%$, quantity of condensed water per hour, ie, dehumidification rate was $4.7\~7.0\;kg/hr$. Relative humidity difference was not greater than 5 percents at various locations in the greenhouse due to proper distributing of dehumidified air through vinyl duct. Thermal energy output from the developed dehumidifier was about 8,5000 kcal/hr that was 7 percents of maximum greenhouse heating load of 10 a.

• 한국태양에너지학회 논문집
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• 제34권5호
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• pp.23-31
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• 2014

This study was accomplished to get the foundation design data of VMD(Vacuum Membrane Distillation) system for Solar Thermal VMD plant. VMD experiment was designed to evaluate thermal performance of VMD using PVDF(polyvinylidene fluoride) hollow fiber hydrophobic membranes. The total membrane surface area in a VMD module is $5.3m^2$. Experimental equipments to evaluate VMD system consists of various parts such as VMD module, heat exchanger, heater, storage tank, pump, flow meter, micro filter. The experimental conditions to evaluate VMD module were salt concentration, temperature, flow rate of feed sea water. Salt concentration of feed water were used by aqueous NaCl solutions of 25g/l, 35g/l and 45g/l concentration. As a result, increase in permeate flux of VMD module is due to the increasing feed water temperature and feed water flow rate. Also, decrease in permeate flux of VMD module is due to increasing salinity of feed water. VMD module required about 590 kWh/day of heating energy to produce $1m^3/day$ of fresh water.

• 태양에너지
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• 제19권3호
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• pp.63-73
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• 1999

Ice storage systems are used to shift the peak load in day time into night time in summer. This paper describes a system simulation of partial ice storage system composed of an encapsulated ice storage tank, a screw compressor chiller, a heat exchanger, and a brine pump. For the system simulation, a one-dimensional model of ice storage tank is developed and validated by comparison with the performance data from measurements of an ice storage tank installed at a building. The control strategies considered in this study are chiller priority and storage priority being used commercially. The system is simulated with design cooling load of 600 RT peak load in design day and with off-design day cooling load, and the electric energy costs of the two control strategies for the same system size are compared. As a result of calculation, the energy consumption in a week for storage priority is higher than that for chiller priority control. However due to lower cost of night electric charge rate, energy cost for storage priority control is lower than chiller priority.