• 설비공학논문집
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• 제17권2호
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• pp.165-172
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• 2005

Heat transfer enhancement of three types of brazed plate heat exchangers has been evaluated experimentally. The effects of flow resonance in a plate heat exchanger on the heat transfer rate and pressure drop have been investigated in a wide range of mass flow rates in detail. The problem is of particular interest in the innovative design of a plate heat exchanger by flow resonance. The results obtained indicate that both heat transfer coefficient and pressure drop are increased as mass flow rate is increased, as expected. It is also found that the heat transfer enhancement is increased with an increase in the plate pitch, while the heat transfer is decreased with a decrease in the chevron angle. Pressure drop also increased with an increase in the plate pitch and with a decrease in the chevron angle. Heat transfer enhancement in the plate heat exchangers is maximized by flow resonance and the resonance frequency of the present plate heat exchangers is found to be in the range of $10~15\;Hz$.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2005년도 동계학술발표대회 논문집
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• pp.347-352
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• 2005

The objectives of this paper are to study the characteristics of heat transfer and pressure drop in plate heat exchangers for absorption applications, and to quantify the effect of mass flow rate, solution concentration, and geometric conditions such as chevron angle on the heat transfer coefficient and pressure drop in the plate heat exchangers. The working fluid is $H_2O$/LiBr solution with the LiBr concentration range of 53.2 - 62.5 % in mass. The results show that the overall heat transfer coefficient increases linearly with increasing Re. The heat transfer rate increases with increasing the chevron angle while it does not significantly depend on the LiBr concentration. The pressure drop also increases with increasing the chevron angle. The effect of the chevron angle on the pressure drop is more significant than that of the concentration.

• 한국가스학회지
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• 제28권2호
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• pp.47-55
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• 2024

한국에는 2030년까지 100여 기의 액화수소 탱크가 도입될 것으로 전망된다. 액화수소는 -253 ℃ 상태로 진공단열구조 탱크에 저장되기 때문에 단열에 문제가 생기면 탱크가 파열되는 대재해의 가능성이 상존한다. 그래서 법령에서는 최후의 보루로 PRV를 설치하도록 규정하고 있다. 주의할 것은 액화수소의 경우 배관의 압력강하를 무시하고 용량을 잘못 계산하면 무용지물이 된다는 것이다. CGA S-1.3에서는 PRV 입·출구 압력강하율을 각각 3% 미만 및 10% 미만으로 하도록 하고 있다. 그러나 배관의 압력강하량과 유량 사이에 상호 의존성이 있어 이들 값을 단번에 계산하는 것이 불가능하다. 그래서 본 연구에서는 매트랩/시뮬링크를 이용하여 PRV시스템의 압력강하율을 계산하는 시뮬레이터를 개발하고, 설계 요소에 대한 압력강하율의 민감도를 평가하였다.

• 대한기계학회논문집
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• 제18권12호
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• pp.3377-3385
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• 1994

This paper introduces empirical correlations to obtain the gas/liquid flow rates and the spray drop size of low viscosity liquid injected by Y-jet twin-fluid atomizers. The gas flow rate is well correlated with the gas injection pressure and the mixing point pressure, based on the compressible flow theory. Similarly, the liquid flow rate is determined by the liquid injection pressure and the mixing point pressure, and a simple correlation for the liquid discharge coefficient at the liquid port was deduced from the experimental results. The mixing point pressure, which is one of the essential parameters, was expressed in terms of the gas/liquid flow rate ratio and the mixing port length. Disintegration and atomization mechanisms both within the mixing port and outside the atomizer were carefully re-examined, and a "basic" correlation form representing the mean diameter of drops was proposed. The "basic" correlation was expressed in terms of the mean gas density within the mixing port, gas/liquid mass flow rate ratio and the Weber number. Though the correlation is somewhat complicated, it represents the experimental data within an accuracy of ${\pm}15%$.EX>${\pm}15%$.

• 대한기계학회논문집B
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• 제29권3호
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• pp.402-408
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• 2005

The instantaneous temperature behaviors on impinging plate in case of ultra high pressure have been measured and analyzed by using the instantaneous temperature probe and ultra high pressure injection equipment. The temperature drop was largest at P1 which is center of impinging spray and decreased with propagation of spray to the radius direction. The temperature drop was bigger in case of higher temperature of impinging plate. The temperature drop decreased with increase of injection pressure. But decreasing rate of temperature drop was slight over 2,500 bars. Therefore, it was predicted that the fuel evaporation versus the increase of injection pressure was maximum at around 2,500 bars.

• 유기물자원화
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• 제23권4호
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• pp.52-62
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• 2015

본 연구에서는 퇴비화공정에서 첨가재로 주로 사용되는 톱밥을 대상으로 톱밥 내 공기투과성 변화에 영향을 미치고 있는 요인별 특성과 총차감압력에 미치는 기여도를 평가하였다. 공기투과성 변화에의 영향요소로서 층류속도(v), 난류속도($v^2$), 수분함량(MC*v), 공기공극률(AFP*v), 입자크기(SIZE*v)를 선정하여 차감압력 산정을 위한 회귀식을 제시하였다. 차감압력에의 증가요인은 층류속도(v)와 입자크기(SIZE*v)이며, 감소요인은 난류속도($v^2$), 수분함량(MC*v), 공기공극률(AFP*v)이다. 공기유입속도를 높이면 총차감압력이 지속적으로 증가하였으며, 이러한 총차감압력 변화에 영향을 크게 미치는 증가요인은 입자크기(SIZE*v)이며, 감소요인은 공기공극률(AFP*v)이다. 또한 총차감압력에의 증가기여도는 낮은 유속에서는 층류속도(v)가 높은 유속에서는 입자크기(SIZE*v)의 기여도가 높았으며, 감소기여도는 공기공극률(AFP*v)이 가장 높았다. 반면에 수분함량 변화에 따른 총차감압력 변화는 그리 크지 않았다. 따라서 총차감압력은 증가요인보다는 감소요인인 공기공극률(AFP*v)과 수분함량(MC*v)에 의하여 영향을 받고 있음을 알 수 있다. 본 연구결과로서, 효율적 퇴비화공정을 위하여는 적정 수분함량 유지와 함께 공기공극률이 높은 첨가재를 선정하여 공기투과성을 향상시키는 방법이 적절할 것이다.

• 한국초전도ㆍ저온공학회논문지
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• 제5권2호
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• pp.51-57
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• 2003

This paper proposes a new oscillating flow model of the pressure drop through the regenerator under pulsating pressure. In this oscillating flow model. pressure drop is expressed by the amplitude and the phase angle with respect to the inlet mass flow rate. In order to generalize the oscillating flow model. non-dimensional parameters, which are Reynolds number, Valensi number, gas domain length ratio, oscillating flow friction factor and phase angle of pressure drop, are derived from the capillary tube model of the regenerator. Correlations for the oscillating flow friction factor and the phase angle are obtained from the experiments for the twill-square screen regenerators under various operating frequencies and inlet mass flow rates. The oscillating friction factor is a function of the Reynolds number alone and the phase angle of pressure drop is a function of the Valensi number and the gas domain length ratio. Experiment is also performed to examine the effect of the weave style of screen. Experimental data demonstrate the superiority of the oscillating flow model over the previous steady flow model.

• 설비공학논문집
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• 제16권12호
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• pp.1227-1233
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• 2004

Air handling unit (AHU)'s air filter pressure difference is important for energy consumption and indoor air quality. Both energy Performance data and air filter differential pressure of AHU in real office buildings were monitored and analyzed to investigate quantitatively energy impact as dust buildup level on air filter grows. We also modeled and simulated CAV system using HVACSIM＋ program to examine the energy effect of dust buildup on filters. Through analysis of time series pressure drop data, the filter pressure difference rate has been increased due to cumulative supply air flow rate increase. As filter pressure drop increased to 1 inch water column, it is found that the supply air flow rate was decreased by 10%, the chilled water flow rate was increased by 5.9% and the pump energy consumption was increased to 5.9%.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2003년도 춘계학술대회
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• pp.1479-1484
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• 2003

The heat transfer enhancement by pulsating flow in a plate heat exchanger has been experimentally investigated in this study. The effect of the pulsating flow, such as pulsating frequency and flow rate, on the heat transfer as well as pressure drop in a plate heat exchanger has been studied in detail. Reynolds number in cold side of a plate heat exchanger is varied $100{\sim}530$ while that of hot side is fixed at 620. The pulsating frequency is considered in the range of $5{\sim}30$ Hz. The results of the pulsating flow are also compared with those of steady flow. It is found that the average heat transfer rate as well as pressure drop is increased as flow rate is increased for both steady flow and pulsating flow cases. When pulsating flow is applied to the plate heat exchanger, heat transfer could be substantially increased in particular ranges of pulsating frequency or Strouhal number; $St=0.36{\sim}0.60$ and pressure drop is also increased, compared with those of steady flow.

• 대한기계학회논문집B
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• 제28권2호
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• pp.199-206
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• 2004

The heat transfer enhancement by pulsating flow in a plate heat exchanger has been experimentally investigated in this study. The effect of the pulsating flow, such as pulsating frequency and flow rate on the heat transfer as well as pressure drop in a plate heat exchanger has been studied in detail. Reynolds number in cold side of a plate heat exchanger is varied 100∼530 while that of hot side is fixed at 620. The pulsating frequency is considered in the range of 5∼30 Hz. The results of the pulsating flow are also compared with those of steady flow. It is found that the average heat transfer rate as well as pressure drop is increased as flow rate is increased for both steady flow and pulsating flow cases. When pulsating flow is applied to the plate heat exchanger, heat transfer could be substantially increased in particular ranges of pulsating frequency or Strouhal number; St=0.36∼0.60 and pressure drop is also increased, compared with those of steady flow. However, in the region of low pulsating frequency or high pulsating frequency, heat transfer enhancement is in meager. Heat transfer enhancement map is suggested based on Strouhal number and Reynolds number of pulsating flow.