• 설비공학논문집
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• 제21권6호
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• pp.367-372
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• 2009

The performance of a $CO_2$ heat pump water heater was measured with a variation of operating conditions such as refrigerant charge amount, outdoor temperature, compressor frequency, EEV opening, and water mass flow rate. The optimum refrigerant charge amount of the $CO_2$ system was 1800 g. At water mass flow rates of 75, 85, and 95 kg/h, the water heating temperatures were 74, 67, and $62^{\circ}C$ and COPs were 2.6, 2.8, and 3.0, respectively. Besides, the compressor frequency and water mass flow rate were adjusted to maintain the water heating temperature at $60^{\circ}C$ with the decrease of outdoor temperature. As the outdoor temperature decreased by $5^{\circ}C$, the compressor frequency increased beyond 60 Hz and the water mass flow rate decreased by 16.7%.

• 대한기계학회논문집 C: 기술과 교육
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• 제3권1호
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• pp.15-21
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• 2015

가스 엔진 히트 펌프는 가스 엔진의 축동력으로 압축기를 구동하는 시스템으로 전력을 거의 사용하지 않고, 엔진 폐열을 활용하기 때문에 하절기와 동절기에 전력 Peak 를 억제하는 공조기로 주목을 받고 있는 제품이다. 제품 개발 시 시스템 성능 예측이 중요하므로 이를 위해 초기 설정한 운전점에서 열교환기 및 압축기의 특성을 반영하여 반복 계산을 수행하면 최종적인 운전점을 도출할 수 있고, 가스 엔진의 성능 데이터를 활용하면 가스 엔진 히트 펌프의 정확한 효율을 예측할 수 있다. 난방 성능을 예측할 때에는 엔진 폐열이 시스템에 공급되기 때문에 외부 열을 흡입하는 구간과 엔진 폐열을 흡입하는 구간을 동시에 고려해야 예측의 정확도를 높일 수 있다. 25 마력 가스 엔진 히트 펌프의 성능을 예측한 값은 실제 측정한 값과 비교하였을 경우 5% 정도의 오차가 발생하며 향후 성능 예측 모델을 구성되는 부품 특성을 반영하면 오차의 폭이 감소될 것으로 예상된다.

• 설비공학논문집
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• 제23권12호
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• pp.791-798
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• 2011

In this study, performance of R410A(50%R32/50%R125) and HFC32/HFC125 mixture is measured to examine the effect of composition shift of R410A used for various air-conditioners and heat pumps. The composition of HFC32/HFC125 mixture varies from the reference composition of R410A ${\pm}10%$ with 5% interval. Tests carried out in a heat pump bench tester at the evaporation and condensation temperatures of $7/45^{\circ}C$ and $-7/41^{\circ}C$ for summer and winter conditions, respectively. Test results show that both the coefficient of performance (COP) and compressor power of the HFC32/HFC125 mixture have the maximum difference of 2.0% as compared to those of R410A. Compressor discharge temperatures of HFC32/HFC125 mixture are increased up to $6.7^{\circ}C$ as compared to that of R410A. The amount of charge for HFC32/HFC125 mixture vary within 5.6% as compared to that of R410A. Overall, performance of R410A is not appreciably affected by the composition shift of ${\pm}10%$ of R32 under both air-conditioning and heat pumping conditions.

• 한국자기학회지
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• 제3권3호
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• pp.201-207
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• 1993

$Pr_{15}Fe_{77}B_{8}$ 조성의 합금을 Ar분위기에서 유도용해로를 이용하여 주조하 였다. 이 합금을 석영관에 넣어 고주파 유도로를 이용하여 용해한 후 0.6 nm의 분출구를 통해 회전하는 Cu wheel위에 분사하여 비본형태로 제조하였다. 이 리본을 열간변형하여 결정방향성을 주었는데 이를 위 해 먼저 $680^{\circ}C$에서 $21.8\;kg/mm^{2}$의 압력으로 hot-press하여 92%의 densification을 갖는 시편을 얻을 수 있었다. 이 시편을 다양한 조건하에서 die-upset을 행하였다. 변형율이 높을 수록 $_{i}H_{c}$는 저하되었으나, $B_{r}$은 현저하게 증가되었으며, XRD 분석 결과(006)면에서의 회절강도가 증가되었다. 따라서 압축방향으로 자화용이축이 형성되었음을 알 수 있었다. Die-upset시의 변형속도가 빠를 수록 $_{i}H_{c}$는 증가되었으나, $B_{r}$은 감소되었다. 가공온도에 따른 $B_{r}$의 변화는 $750^{\circ}C$ 까지 상승한 후 감소되었다. 이 조성의 $4{\pi}M_{s}$는 11.8 kG였고 $750^{\circ}C$에서 0.05 mm/sec의 가공속도로 변형률 0.8로 die-upset한 경우에는 $B_{r}$이 11.0 kG로 우수한 자기이방성을 가지고 있으나, die-upset후에 $_{i}H_{c}$가 낮은 문제점이 있다.

• International Journal of Air-Conditioning and Refrigeration
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• 제16권3호
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• pp.77-82
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• 2008

For heat pumps used in a cold region, it is very important to obtain appropriate heating capacity. Several studies using a variable speed compressor and an additional heater have been performed to enhance heating capacity at low ambient temperatures. However, for outdoor temperature conditions below $-15^{\circ}C$, it is still difficult to obtain enough heating capacity above the rated value. In recent studies, the application of gas injection technique into a two-stage heat pump yielded noticeable heating performance improvement at low temperature conditions. In this study, the heating performance of a two-stage gas injection heat pump with a rated capacity of 3.5 kW was measured and analyzed by varying refrigerant charge amount and EEV opening at the standard heating condition. The heating performance of the two-stage gas injection heat pump was compared with that of a two-stage non-injection heat pump. The heating capacity and COP of the two-stage gas injection heat pump were improved by 2-10% at the optimal charging condition over those of the two-stage non-injection heat pump.

• 신재생에너지
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• 제5권3호
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• pp.40-48
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• 2009

Recovered heat has been considered as a renewable energy in Europe since 2008 because its great effect on energy saving and carbon decreasing in plant process. Energy saving and decreasing green gas are critical issue today, so various technologies to save energy and decrease carbon dioxide in plant process have been applied to many industrial area. In this paper, the feasibility of condenser heat recovery by heat pump in power plant for district heating and fuel line preheating were reviewed by verifying energy (heat) balance and mass balance of power plant model. Some ways to compose proper system to recover heat of condenser are suggested and their possibilities are also reviewed. Limitations on heat recovery in power plant are also reviewed. The results are verified by calculating input/output energy based on actual performance test data of Taean Thermal Power Plant in Korea. There is noticeable improvement of plant performance in some cases which demand low temperature (<100 C) heat like distrcit heating, fuel line heating, and so forth.

• 설비공학논문집
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• 제7권2호
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• pp.234-248
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• 1995

A super-heat pump system composed of a suction line heat exchanger, low and high stage economizers, and a screw compressor is simulated to examine the energy performance and design options. CFC12, HCFC22, HFC134a, HCFC22/HCFC142b, HFC32/HFC134a, and HFC125/HFC134a are used as working fluids for comparison. The results indicate that the proposed system charged with appropriate mixtures is up to 33.4% more energy efficient than the normal system with CFC12. The performance of the super-heat pump system charged with mixtures was influenced by such factors as the temperature matching, heat source temperature difference, low stage economizer, and high stage economizer. The fluids with a larger liquid specific heat such as HFC134a would have more benefits when a suction line heat exchanger is installed. 40%HCFC22/60%HCFC142b mixture seems to be a good candidate to replace CFC12. On the other hand, 25%HFC32/75% HFC134a would be a good long term candidate to replace HCFC22.

• 한국지열·수열에너지학회논문집
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• 제3권1호
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• pp.1-9
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• 2007

A steady-state simulation model for Dual-Source Heat Pump(DSHP) of 8RT was presented. A Dual-Source Heat Pump(DSHP) has been designed to make up for the conventional air source heat pumps. The performance evaluation has been conducted under internal standard test conditions such as ISO-13256-1 and KS C 9306. However, as test conditions such as entering water, indoor and outdoor air conditions could not be controlled to satisfy the standard test conditions in outdoor tests, a series of experiments have been conducted with the actual test conditions. Then, computer models for DSHP could be used for the standard condition have developed using EES program. The model was developed from basic thermodynamic principles and heat transfer relations. Most of the parameters were obtained with EES from the actual catalog data. The simulation results were in good agreement with the experiments.

• 한국공작기계학회:학술대회논문집
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• 한국공작기계학회 2002년도 춘계학술대회 논문집
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• pp.17-22
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• 2002

A conventional silica gel/water adsorption chiller has been analyzed numerically. A novel non-dimensional mathematical model has been presented to analyze the design effect of different components of an adsorption chiller. The design parameters of this system are characterized by the number of transfer unit, NTU, of different components and the inert material alpha number, ${\alpha}$of different components of the systems. Results show that condenser NTU$\sub$a/ has the most influential effect on the system performance, which is fellowed by absorber NTU$\sub$e/. It is also seen that coefficient of performance (COP) and non-dimensional specific cooling capacity increases with the increase of NTU$\sub$a/ and NTU$\sub$e/, but decreases with the increase of inert material alpha number. A thermo-economic data of the adsorption chiller and some other heat pump systems those are in practical operation are also presented.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2008년도 춘계학술대회 논문집
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• pp.154-156
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• 2008

A prototype of the desiccant cooling system with a regenerative evaporative cooler was built and tested for the performance evaluation. The regenerative evaporative cooler is to cool a stream of air using evaporative cooling effect without an inc6rease in the humidity ratio. It is comprised of multiple pairs of dry and wet channels and the evaporation water is supplied only to the wet channels. By redirecting a portion of the air flown out of the dry channel into the wet channel, the air can be cooled down to a temperature lower than its inlet wet-bulb temperature at the outlet end of the dry channels. Incorporating a regenerative evaporative cooler eliminates the need for deep dehumidification in the desiccant rotor 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. At the ARI condition with the regeneration temperature of $60^{\circ}C$, the prototype showed the cooling capacity of 4.4 kW and COP of 0.75.