• 한국지반공학회논문집
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• 제31권5호
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• pp.5-21
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• 2015

에너지파일이란 새로운 형식의 지중열교환기로서, 건물의 기초 구조물인 말뚝 내부에 열교환 파이프를 삽입하고 파이프 내부로 유체를 순환시켜 지반과 말뚝 매질사이의 열교환을 유도한다. 에너지파일은 기존의 기초 구조물을 활용하여, 구조물의 지지 기능과 지중열교환기로서의 기능을 동시에 수행하는 에너지 구조체이다. 본 연구에서는 에너지파일의 실증연구를 위하여 총 6가지 형태의 열교환 파이프가 삽입된 실규모 현장타설 에너지파일을 시험 시공하였다. 열교환 파이프의 형태는 다양한 형태별 성능 및 시공성 비교를 위해 병렬 U형 3본(5쌍, 8쌍, 10쌍), 코일형 2본(피치간격 200mm와 500mm), S형 1본으로 선정하였다. 총 6가지 형태의 열교환 파이프를 시공하면서 시공 소요시간, 인력 소요, 필요 부대시설, 특이사항 등을 정리하여 각 형태별 시공성을 평가하였다. 또한 시공된 현장타설 에너지파일에 대한 열교환 성능 평가시험을 수행하였다. 열교환 성능 평가시험은 실제 상업 건물의 냉방 부하를 모사하기 위하여 8시간 가동 16시간 휴지의 간헐적 가동을 통하여 수행하였다. 열교환 성능 평가시험 결과를 통하여 각 현장타설 에너지파일의 열교환량을 산정하였으며, 이를 에너지파일 근입 깊이 및 열교환 파이프 길이로 정규화하여 각 형태별 열교환 효율을 평가하였다. 마지막으로 현장타설 에너지파일의 경제성을 분석하기 위하여 각 형태별 에너지파일의 시공비와 에너지파일 단위 길이 당 열교환 성능을 통해 1W/m 당 소요 비용을 산정하였다.

• 한국산학기술학회논문지
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• 제17권3호
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• pp.24-30
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• 2016

현재까지 지열 열펌프 시스템의 지중열교환기는 수직 밀폐형과 개방형 지중열교환기가 주로 설치되어 열응답시험을 이용한 열특성 평가가 수행되어 왔다. 본 논문에서는 열응답시험과 선형열원법을 이용하여 수평형 지중열교환기의 열특성을 분석하였다. 또한 지열 열펌프 시스템은 매일 단속 운전되어지므로 일일부하시험을 수행하여 수평형 지중열교환기의 지중온도 및 순환수 평균온도 일별 변화를 고찰하였다. 시험을 위해 경기도 안산에 직선식 수평형 지중열교환기(심도 2 m, 길이 50 m 8줄)를 설치하였다. 시험결과 수평형 지중열교환기의 지중 열전도율은 연중 $1.43{\sim}1.64W/m{\cdot}K$ 범위로 비교적 큰 변화가 없으며 12월에 최대값을, 5월에 최소값을 갖는 것으로 나타났다. 12일간 지중 열교환기로 하루 10시간동안 6.0 kW의 열량을 투입하는 연속 부하시험을 6월, 9월, 12월에 수행한 결과 지중온도는 이 기간 동안 각각 $4.31^{\circ}C$, $3.14^{\circ}C$, $1.21^{\circ}C$ 상승하는 것으로 나타났다.

• 한국산학기술학회논문지
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• 제16권4호
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• pp.2415-2423
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• 2015

본 논문은 12.7mm 원관을 변형하여 만든 세장비 0.6(짧은 직경 10.0mm, 긴 직경 16.5mm)의 타원관이 적용된 사인 웨이브 핀-관 열교환기의 습표면 공기측 성능실험에 관한 것이다. 핀 핏치와 열 수를 변화시켜 총 12개의 시료에 대하여 실험을 수행하였다. 타원관에서 핀 핏치 변화에 따른 j, f 인자의 영향은 미미 하였으나, 열수에 따라서는 1row에서 j인자가 가장 낮았다 (가장 높은 2row의 81%). 하지만 원관에서는 1row에서 가장 높게 나타나는 차이점을 보였다. 이는 타원관에 적용된 사인 웨이브 채널의 유동 특성에 기인한 것으로 판단된다. 원관 열교환기와 $j/f^{1/3}$값을 비교한 결과 1열을 제외하고는 타원관 열교환기의 전열성능이 우수함을 알 수 있다. 즉, 타원관 열교환기의 $j/f^{1/3}$값이 원관의 값보다 2열에서 1.6~2.5 배, 3열에서 1.4~2.4 배, 4열에서 1.2~1.8배 크게 나타났다.

• 한국태양에너지학회 논문집
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• 제26권4호
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• pp.9-16
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• 2006

Geothermal-energy has been getting popular as a natural energy source for green buildings these days. Public building with gross area more than $3000m^2$, planned after March, 2005, should spend about 5% of total building cost for equipment run by natural energy source (e.g. geothermal, solar heat, solar power, etc) according to renewable energy promotion law in Korea. As a result geothermal-energy using heat pump system is emerging as a effective alternative for realistic and economic plan although design guidelines and construction code for the system is in progress and technical data is far from sufficient. The quantitative analysis on the performance of geothermal-energy using heat pump system is insufficient for appropriate design of it. In this paper, cooling performance of geothermal-energy using heat pump system of residential and retail etc. mixed-use building has been analyzed on the basis of temperature comparison between inlet and outlet of heat exchangers of the operating system. Additionally, dry-bulb temperature and relative humidity have been measured and analyzed together as an index of indoor thermal environment.

• 설비공학논문집
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• 제22권4호
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• pp.248-257
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• 2010

An exhausted heat recovery system for a small gas engine cogeneration plant was investigated. The system was designed and built in a 300 kW class cogeneration demonstrative system. The basic performance was tested depending on load variation, and installed to a field site as a bottoming heat and power supply system. The exhaust gas heat exchangers (EGHXs) in shell-and-tube type and shell-and-plate type were tested. The entire efficiency of the cogeneration system was estimated between 85 to 90% under the 100% load condition, of which trend appears higher in summer due to the less thermal loss than in winter. Power generation efficiency and thermal efficiency was measured in a range of 31~33% and 54~57%, respectively.

• 설비공학논문집
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• 제17권1호
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• pp.62-70
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• 2005

In this study, the air-side heat transfer coefficients of several types of evaporators in the household freezer/refrigerators are investigated. The types considered in this work are: discrete flat plate fin-and-tube type(in-lined tube array), continuous flat plate fin-and-tube type(staggered tube array), and spine fin-and-tube type(in-lined tube array). The heat transfer correlations obtained from this study for each heat exchangers could expect heat transfer coefficients less than $5\%$ of errors. The result indicates that the air-side heat transfer performance of spine fin-and-tube type evaporator shows the highest value under dry conditions, but discrete flat plate fin-and-tube type evaporator shows the highest value among these three evaporators under frosting conditions.

• 설비공학논문집
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• 제28권7호
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• pp.293-298
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• 2016

A three-dimensional (3D) numerical model of the vertical ground-coupled heat exchanger is useful for analyzing the modern ground source heat pump system. Furthermore, a detailed description of the inner side of the exchanger allows to account for the effects of the thermal capacity. Thus, both methods are included in the proposed numerical model. For the ground portion, a FDM (Finite Difference Method) scheme has been applied using the Cartesian coordinate system. Cylindrical grids are applied for the borehole portion, and the U-tube configuration is adjusted at the grid, keeping the area and distance unchanged. Two sub-models are numerically coupled at each time-step using an iterative method for convergence. The model is validated by a reference 3D model under a continuous heat injection case. The results from a periodic heat injection input show that the proposed thermal capacity model reacts more slowly to the changes, resulting in lower borehole wall temperatures, when compared with a thermal resistance model. This implies that thermal capacity effects may be important factors for system controls.

• 대한기계학회논문집B
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• 제23권2호
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• pp.210-217
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• 1999

This paper reports the experimental results on heat transfer characteristics of R-22 and R-407C(HFC-32/125/134a 23/25/52 wt%) condensing inside horizontal smooth and finned tubes. The test condensers used In the study are double pipe heat exchangers of 7.5 mm ID, 9.5 mm OD smooth tube, and 60 finned micro-fin tube with 8.53 mm ID, 9.53 mm OD. Each of these tubes was 4 000 mm long tubes connected with an U-bend. These U type two-path test tubes are divided In 8 local test sections for the identification of the local condensing heat transfer characterisitcs and pressure drop, U-bend effects on condensing flows. Inlet quality is maintained 1.0, and refrigerant mass velocity is varied from 102.0 to $301.0kg/m^2{\cdot}s$. From the results, it was found that the pressure drop of the R-407C Increased, and heat transfer coefficient decreased compared to those of R-22. In comparison condensing heat transfer characteristics of micro-fm tube with those of smooth tube, increasing of condensing heat transfer coefficient was found outstanding compared to the increasing ratio of pressure drop. Furthermore, pressure drop In U-bend showed at most a 30 % compared to the total pressure drop in the test section.

• 한국지열·수열에너지학회논문집
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• 제14권1호
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• pp.22-29
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• 2018

The purpose of this study is to investigate the preliminary thermal performance of a plastic coated aluminum material(PCAM) plate heat exchanger. Plastic coating which has high corrosion resistivity and thermal conductivity can overcome corrosive weakness of aluminum material. The heat exchangers are modeled for STS316, Titanium and PCAM materials, and analyzed numerically using HTRI and ANSYS Fluent CFD softwares. The results show that PCAM heat exchanger is superior in heat transfer performance compared to existing materials. For chevron angle of $60^{\circ}$, thermal performances of Titanium and PCAM are higher by 12.2% and 48.9% when compared to STS316, respectively.

• Journal of Mechanical Science and Technology
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• 제20권7호
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• pp.1059-1067
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• 2006

In order to develop a compact evaporator, experiments that show characteristics of evaporating heat transfer and pressure drop in the helically coiled minichannel were performed in our previous research. This study was focused on the performance analysis of helically coiled heat exchangers with circular minichannels with an inner diameter=1.0 mm. The working fluid was R-22, and the properties of R-22 were estimated using the REFPROP program. Numerical simulation was performed to compare results with the experimental results of the helically coiled heat exchanger. As the heat transfer rate and pressure drop were calculated at the micro segment of the branch channels, the performance of the evaporator was evaluated. The following conclusions were obtained through the numerical simulations of the helically coiled heat exchanger. It showed good performance when the flow rate of each branch channels was suitable to heat load of air-side. The numerical simulation value agreed with experimental results within ${\pm}15%$. In this study, a numerical simulation program was developed to estimate the performance of a helically coiled evaporator. And, an optimum helically coiled minichannels evaporator was designed.