• 설비공학논문집
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• 제16권6호
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• pp.566-573
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• 2004

Comparison of the cooling performance is provided between the desiccant cool-ing systems incorporating a direct evaporative cooler and a regenerative evaporative cooler, respectively. Cycle simulation is conducted, and the cooling capacity and COP are evaluated at various temperature and humidity conditions. The COP of the system with a regenerative evaporative cooler and the regeneration temperature of 6$0^{\circ}C$ is evaluated 0.65 at the outdoor air condition of 35$^{\circ}C$ and 40% RH. This value is found about 3.4 times larger than that of the system with a direct evaporative cooler. Furthermore, incorporating a regenerative evaporative cooler eliminates the need for deep dehumidification in a desiccant dehumidifier that is necessary to achieve low air temperature in the system with a direct evaporative cooler. Subsequently, the regenerative evaporative cooler enables the use of low temperature heat source to regenerate the dehumidifier permitting the desiccant cooling system more beneficial compared with other thermal driven air conditioners.

• 동력기계공학회지
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• 제13권4호
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• pp.38-42
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• 2009

The Injection molding is used more than 70% of total production in plastic products. The injection molding process has 4 processes such as filling, packing, cooling and ejecting. now then, cooling process spends the most of times in Injection molding cycle time. Therefore, it is important to control the mold temperature in producing plastic products. The cooling system and time affect the product's quality and productivity. Especially, cooling time has about 60% of total injection cycle time. Therefore, we can improve a productivity by shortening cooling time. In this study, the rapid cooling system was developed and performed a efficiency test. This system could refrigerate coolant to $1^{\circ}C$ and had to need 10 minutes for normal operating.

• Journal of Advanced Marine Engineering and Technology
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• 제39권6호
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• pp.592-598
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• 2015

본 연구에서는 공랭식 VI(Vapour-Injection) 사이클을 적용한 R410A용 고성능 하절기 냉방 열펌프의 성능 특성을 실험적으로 규명하였다. 실험에 사용한 장치는 VI 압축기, 응축기, 유분리기, 판형열교환기, 에코노마이져(economizer), 증발기, 그리고 재냉기(re-cooler)로 구성하였다. 냉방 성능 실험 조건은 다음과 같이 3가지 사이클로 VI 사이클을 적용하고 증발기 출구 냉매와 VI사이클 흡입 냉매가 재냉기에서 서로 열교환 하지 않는 사이클(사이클 A)과 열교환을 하는 사이클(사이클 B), 그리고 VI 사이클도 적용하지 않고 증발기 출구 냉매와 VI 사이클 흡입 냉매와의 열교환도 없는 사이클(사이클 C)로 구분하였다. 분석 결과, 냉방 성능은 증발기 출구 냉매와 VI사이클 흡입 냉매가 서로 열교환하는 VI사이클(사이클 B)이 가장 높았으며 VI사이클을 적용하지 않은 사이클 C가 가장 낮음을 알 수 있었으며, 사이클B의 냉방성능계수($COP_C$)가 평균 3.5로 사이클A보다 8.6%, 사이클C보다 33% 높은 값을 나타내었다.

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2005년도 춘계학술대회 논문집
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• pp.1761-1765
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• 2005

The plastic injection molding industry is increasing pressure to reduce the cycle time in order to improve the productivity. The time of a cooling die is a large part of the cycle time. The conformal cooling channels can reduce the cooling time effectively as compared with conventional production die. It is hard to make the die with a conformal cooling channel by the conventional method. This paper introduces the method of a conformal cooling channel manufacturing by the DMT (Direct Metal Tooling) that is a new technology.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2006년도 하계학술발표대회 논문집
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• pp.1119-1124
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• 2006

The objectives of this paper are to investigate the performance of silica gel-water adsorption refrigeration system with heat recovery process from the system experiment. This system can be driven by waste heat at near ambient temperature from $60^{\circ}C$ to $90^{\circ}C$. The cooling capacity and coefficient of performance(COP) were measured from various experimental conditions. An experimental results revealed the influence of operating temperatures(hot, cooling and chilled water), water flow rates, and adsorption-desorption cycle times on cooling capacity and COP. Under the standard conditions of $80^{\circ}C$ hot water, $25^{\circ}C$ cooling water, $14^{\circ}C$ chilled water inlet temperatures and 420sec cycle time, a cooling capacity of 1.14kW and a COP for cooling of 0.55 can be achieved.

• 동아시아식생활학회지
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• 제24권1호
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• pp.62-69
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• 2014

Jungkwa is a traditional Korean dessert preserved in honey or sucrose. This study was carried out to investigate the antioxidant activities and quality characteristics of Rehmannia glutinosa Jungkwa (RJ). RJ was prepared after six repeated cycles of boiling-cooling. After blanching fresh Rehmannia glutinosa (600 g) for 5 min at $100^{\circ}C$, Rehmannia glutinosa was boiled in sucrose syrup (sucrose 720 g in water 600 g) for 60 min and then cooled for 24 hr. Moisture, pH and color values of lightness, redness and yellowness in the Hunter color system of Jungkwa decreased as the number of boiling-cooling cycles increased, whereas acidity, $^{\circ}Brix$ and reducing sugar contents of syrup increased. Total phenol content increased in by the 6th boiling-cooling cycle. Antioxidant activities, including DPPH and hydroxyl radical scavenging activities, increased in RJ by the 6th boiling-cooling cycle. Based on these results, the antioxidant activities of Rehmannia radix Jungkwa was improved according to an increasing number of boiling-cooling cycles due to increased total phenol contents.

• 한국산학기술학회논문지
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• 제20권6호
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• pp.288-296
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• 2019

그간 복사 냉방은 천정이나 바닥면을 냉각 표면으로 활용하기 때문에 표면 온도를 노점 온도 이상으로 높이거나 보조적인 제습 에어컨을 설치해야 하는 문제가 있었다. 본 연구에서는 주택 적용을 목표로 복사 판넬 표면에 결로를 유발시킴으로써 냉각 열량을 증가시키고 실내 쾌적감도 개선할 수 있는 1.0 kW 용량의 복사-대류 방식의 하이브리드 냉방기에 대하여 검토하였다. 이 냉방기는 2개의 냉동 사이클 - 강제 대류 제습 사이클과 복사 판넬 냉방 사이클로 구성된다. 시제품 실험 결과 복사 판넬 사이클의 경우 실외 $35^{\circ}C/24^{\circ}C$, 실내 $27^{\circ}C/19.5^{\circ}C$의 표준 조건에서 냉매 순환량은 8.8 kg/h, 응축 온도 $51^{\circ}C$, 증발 온도 $8.8^{\circ}C$, 냉방 능력은 376 W, 성적계수는 1.75로 나타났다. 또한 복사 판넬의 온도는 $13^{\circ}C{\sim}14^{\circ}C$ 사이에서 고르게 분포되었다. 또한, 상대 습도가 감소할수록 냉방 능력은 감소하나 소비 동력은 거의 변화가 없었다. 제습 사이클의 경우, 표준 조건에서 냉매 순환량은 21.1 kg/h, 응축온도 $61^{\circ}C$, 증발 온도 $5.0^{\circ}C$, 냉방능력은 949 W, COP는 2.11로 나타났다. 한편, 복사 판넬과 제습 냉방 사이클을 동시에 가동시키며 표준 조건에서 시험 결과, 복사 판넬의 냉방 능력은 333 W, 제습부의 냉방 능력은 894 W, COP는 1.89로 나타났다. 홴 풍량이 감소하면 복사 판넬, 제습부 모두 냉방 능력이 감소함을 보였는데 특히 제습부에서 감소량이 두드러졌다. 본 실험 데이터를 기반으로 냉방 부하의 변동에 대비하여 가능한 제어 로직을 제시하였다.

• 설비공학논문집
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• 제7권3호
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• pp.488-500
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• 1995

An air-cooled ammonia/water GAX(Generator-Absorber heat eXchange) absorption cooling cycle is proposed and its performance is numerically evaluated. It is shown that the performance of the system is greatly dependent on the quality of the refrigerant leaving the evaporator. For any refrigerant concentration in the investigated range(99.1~99.9% ammonia), the cycle COP(coefficient of performance) reaches the highest value, when some amount(about 7%) of refrigerant evaporates in the refrigerant heat exchanger. Among temperature differences in various heat exchangers, the temperature difference between GAX-absorber and the GAX-generator shows the greatest effect on the system performance, whereas pressure losses cause no significant decrease in COP. The system COP increases almost linearly with increasing evaporator temperature, decreasing absorber temperature or decreasing condenser temperature. If both absorber and condenser temperature increase simultaneously, the decrease in the COP becomes larger.

• 동력기계공학회지
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• 제13권6호
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• pp.70-75
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• 2009

In this paper, cycle performance analysis of R744($CO_2$) two-stage compression and one-stage expansion refrigeration system is presented to offer the basic design data for the operating parameters of the system. The operating parameters considered in this study include superheating degree, compressor efficiency, gas cooling pressure, mass flowrate ratio, outlet temperature of gas cooler and evaporating temperature in the carbon dioxide two-stage refrigeration cycle. The main results were summarized as follows : The cooling capacity of two-stage compression and one-stage expansion refrigeration system increases with the increasing superheating degree, compressor efficiency and gas cooling pressure, but decreases with the increasing mass flowrate ratio and evaporating temperature. The compression work of two-stage compression and one-stage expansion refrigeration system increases with the increasing superheating degree, outlet temperature of gas cooler, gas cooling pressure and evaporating temperature, but decreases with the increasing compressor efficiency and mass flowrate ratio. The COP of two-stage compression and one-stage expansion refrigeration system increases with the increasing compressor efficiency, but decreases with the increasing superheating degree, gas cooling pressure, mass flowrate ratio and evaporating temperature. Therefore, superheating degree, compressor efficiency, gas cooling pressure, mass flowrate ratio, outlet temperature of gas cooler and evaporating temperature of R744($CO_2$) two-stage compression and one-stage expansion refrigeration system have an effect on the cooling capacity, compressor work and COP of this system.

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2009년도 춘계학술대회 논문집
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• pp.653-654
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• 2009