• Journal of the korean Society of Automotive Engineers
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• v.10 no.4
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• pp.14-18
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• 1988

액체의 미립화는 액체연료의 연소를 위한 분무, 분무 도장, 농약 살포, 의료기기, 용융 금속의 금속 분말의 제조 등의 여러분야에 널리 이용되고 있다. 특히 연소 기관은 액체 연료의 미립화와 증발 특성에 따라 기관의 연소와 성능은 크게 변화하므로 연소실 내의 연료 미립화 특성의 개선은 매우 중요하다. 미립화에 영향을 미치는 인자에는 연료의 물성과 분사 기구 및 분사 밸브 등의 구조와 분사압력 등은 연료 미립화에 주된 영향을 미치는 요인의 하나가 되고 있다. 여기서는 주로 액체연료의 미립화에 일반적인 기초 사항과 분무 특성의 표시 방법, 측정법에 대하여 기술하기로 한다.

• Proceedings of the Korean Fiber Society Conference
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• 2003.10b
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• pp.235-236
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• 2003

섬유의 습식 가공은 에너지 집약적 산업이다. 대부분의 에너지는 가공시 사용된 많은 양의 수분을 증발시키고, 건조하는데 소모되어진다. 따라서 거품가공은 물 소비를 감소시켜 에너지를 절약하고 폐수를 감소시키는데 주된 목적이 있다(1). 거품가공은 직물에 부가된 물의 양을 감소시켜 건조단계에서 상당한 에너지 소비(30~80%)를 감소시키는 것으로 알려져 있고(2~3), 최근에는 낮은 wet pick-up율에 의한 가공제 처리의 성능 및 수지의 가교분포에 대한 효과 등에 관한 많은 연구가 이루어지고 있으나 미흡한 점이 많이 보고되고 있다.(4~7) (중략)

• Proceedings of the SAREK Conference
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• 2007.06a
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• pp.119-119
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• 2007

• Journal of the KSME
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• v.33 no.11
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• pp.979-984
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• 1993

압축기는 냉동 . 공조 사이클에서 냉매를 압축하여 순환시키는 기능을 한다. 냉동 . 공조 사이클 에서 압축기의 효율 COP는 압축기 모터 입력에 대한 증발기에서의 냉각 능력의 비로서 정의 된다. 따라서 압축기 자체의 특성도 중요하지만 냉매의 열역학적 물성도 중요한 역할을 한다. 압축기의 효율향상문제가 최근에 대두되게 된 것은 첫 째, 몬트리올 협정에 의해 CFC의 사용이 제한되면서 새로 검토하게 된 대체냉매들의 열물성이 CFC보다 불리한 점과 둘째, 에너지 소비를 줄이려는 인식이 환경 측면에서 확산되고 있기 때문이다. 이 글에서는 압축기 효율을 결정하는 주요요소에 대하여 알아보고 최근 국내외에서 이루어지고 있는 효율향상 성과에 대하여 소개하 기로 한다.

• Proceedings of the SAREK Conference
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• 2003.07a
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• pp.41-41
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• 2003

• Proceedings of the Membrane Society of Korea Conference
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• 1999.04b
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• pp.69-90
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• 1999

역삼투공정을 이용하여 염료폐수를 공업용수로 재활용하기 위해 설비의 구성, 운전조건 및 경제성에 대한 검토를 실시하였다. 이를 위해 먼저 원수의 성상 및 처리수 수질기준에 대한 검토를 통해 단위공정으로 물리적여과, 역삼투 및 증발농축으로 선정하고 2차에 걸친 Pilot Test를 실시하여 실 Plant 설치를 위한 설계인자를 확보하였다. 이를 바탕으로 750m$^{3}$/일의 염료폐수재활용 Plant를 설치하고 시운전과정을 통하여 성능 확인 및 운전조건을 확보하고 이에 따른 설비투자비 및 운전비 등의 경제성 검토를 실시하였다.

• Journal of Advanced Marine Engineering and Technology
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• v.35 no.8
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• pp.1001-1008
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• 2011

This paper describes an analysis on performance and exergy of R744-R404A cascade refrigeration system with internal heat exchanger to optimize the design for the operating parameters of this system. The operating parameters considered in this study include subcooling and superheating degree, internal heat exchanger and compression efficiency, evaporation and condensation temperature in the R744 low- and R404A high- temperature cycle, respectively. The main results are summarized as follows : As the evaporation temperature of cascade heat exchanger increases, the COP of R404A high-temperature cycle increases. But the COP of R744 low-temperature cycle decreases, and the COP of total cascade cycle is almost constant. As cascade evaporation temperature increase, the exergy loss in the R404A condenser and the R744 internal heat exchanger is the largest and the lowest among all components, respectively. Therefore, the exergy loss in the condenser and compressor of R404A must be decreased to enhance the COP of R744-R404A cascade refrigeration system.

• Journal of the Korean Institute of Gas
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• v.2 no.4
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• pp.25-33
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• 1998

The characteristics of evaporation heat transfer for the utilization of LNG cold energy was investigated experimentally using liquified nitrogen and a solution of ethylene-glycol and water under horizontal two-phase conditions in the small-scale equipment of a cryogenic heat exchange system. The inner tubes in the double pipe heat exchanger with 8 mm and 15 mm inner diameter and 6 m length were adopted as a smooth test tubes and enhanced tubes by means of wire-coil inserts. Heat transfer coefficients and Nusselt number for the test tube were calculated from measurements of temperatures, flowrates and pressures. The correlations in a power-law relationship of the Nusselt number, the Reynolds number and Prandtl number for heat transfer were proposed which can be available for design of cryogenic heat exchangers. The correlations showed heat transfer coefficients for the wire-coil inserts were much higher than those for the smooth tubes, increased by more than 2.5 ${\~}$ 5.5 times depending upon the equivalent Reynolds number. Form and length of cryogenic double pipe heat exchanger were proposed for applicable to the utilization of LNG cold energy.

• Fire Science and Engineering
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• v.19 no.3 s.59
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• pp.13-19
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• 2005

An experimental study is presented for extinguishing characteristics of liquid fuel fire by water mist containing sodium acetate trihydrate. To evaluate the extinguishing performance of water mist containing an additive, the evaporation characteristics of a water droplet on a heated surface was examined. The evaporation process was recorded by a charge-coupled-device camera. Also, small-scale extinguishing tests were conducted for n-heptane pool fire in ventilated space to measure flame temperature variation. The average evaporation rate of a water droplet containing an additive was lower than that of a pure water droplet at a given surface temperature due to the precipitation of salt in the liquid-film and change of surface tension. In case of using an additive, the flame temperature was lower than that of pure water at a given discharge pressure and it was because the momentum of a water droplet containing an additive was increased reducing flame size. And also dissociated metal atoms, sodium, were reacted as a scavenger of the major radical species OH^-,\;H^+$ which were generated for combustion process. Moreover, at a high pressure of 4MPa, the fire was extinguished through blowing effect as well as primary extinguishing mechanisms.

• Korean Chemical Engineering Research
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• v.43 no.2
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• pp.243-248
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• 2005

Membrane pervaporation processes could have advantages over distillation for separation of water/organics mixtures: a low energy demand and the ability to separate azeotropic mixtures or isomers. Zeolite membranes might show better thermal, mechanical and chemical stabilities than polymer membranes. Water could be effectively separated from water/organic mixtures using the NaA zeolite membrane because of its high hydrophilicity. In this study, water was separated by pervaporation using the NaA zeolite membrane from water/ethanol mixtures. As a mole fraction of ethanol increased, the total permeation flux and the water flux decreased while the separation factor increased, reached a maximum point, and decreased. As an experimental temperature increased, the total permeation flux increased while the separation factor increased at the lower mole fraction of ethanol than 0.8 and it decreased at the higher mole fraction of ethanol than 0.8. The total permeation flux and the separation factor could be maintained constant during the long term experiment longer than 160 hours. It was found that the NaA zeolite membrane synthesized in our study showed better performance on water/ethanol separation than that of a distillation process or PVA polymeric pervaporation membranes.