• Title/Summary/Keyword: heat exchange

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The maximum power condition of the Brayton cycle with heat exchange processes (熱交換 過程 을 考慮한 브레이튼 사이클 의 最大出力條件)

  • 정평석;차진걸;노승탁
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.9 no.6
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    • pp.795-800
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    • 1985
  • The ideal Brayton cycle has been analyzed with the heat exchange processes between the working fluid and the heat source and the sink while their heat capacity rates are constant. The power fo the cycle can be expressed in terms of a temperature of the cycle and the heat capacity rate of the working fluid. There exists an optimum power condition where the heat capacity rate of the working fluid has a value between those of the heat source and the heat sink, and the cycle efficiency is determined by the inlet temperatures of the heat source and the sink.

Evaluation of Heat Exchange Rate in Horizontal Slinky and Coil Type Ground Heat Exchangers Considering Pitch Interval (피치 간격에 따른 수평 슬링키형과 코일형 지중 열교환기의 열효율 평가)

  • Yoon, Seok;Lee, Seung-Rae;Kim, Min-Jun;Kim, Woo-Jin;Go, Gyu-Hyun;Jeon, Jun-Seo
    • Journal of the Korean Geotechnical Society
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    • v.30 no.7
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    • pp.55-61
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    • 2014
  • The need of geothermal energy is constantly increasing for economical and environmental utilization. Horizontal ground heat exchangers (GHEs) can reduce installation cost and increase efficiency. There are many kinds of GHEs, and it is known that slinky and spiral coil type GHEs show high thermal performance. Therefore, this paper presents experimental results of heat exchange rates in horizontal slinky and spiral coil type GHEs installed in a steel box whose size is $5m{\times}1m{\times}1m$. Dried Joomunjin standard sand was filled in a steel box, and thermal response tests (TRTs) were conducted for 30 hours to evaluate heat exchange rates by changing different pitch spaces of horizontal slinky and spiral coil type GHEs. As a result, spiral coil type GHE showed 30~40% higher heat exchange rates per pipe length than horizontal slinky type GHEs. Furthermore, long pitch interval (Pitch/Diameter=1) showed 200~250% higher heat exchange rates per pipe length than short pitch interval (Pitch/Diameter=0.2) in both spiral coil and horizontal slinky type GHEs, respectively.

Effects of Pitch Length of Stack-type EGR Cooler on Heat Exchange Characteristics in a Diesel Engine (적층형 EGR Cooler의 Pitch 길이 변화가 열교환 특성에 미치는 영향)

  • Hwang, Se-Joon;Kim, Min-Chol;Jang, Sang-Hoon;Kim, Hyung-Man
    • Transactions of the Korean Society of Automotive Engineers
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    • v.18 no.2
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    • pp.135-140
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    • 2010
  • An important goal in diesel engine research is the development of a means to reduce the emissions of nitrogen oxides (NOX). The use of a cooled exhaust gas recirculation (EGR) system is one of the most effective techniques currently available for reducing nitrogen oxides. Since Particular Matter (PM) fouling reduces the efficiency of an EGR cooler, a trade-off exists between the amount of NOX and PM emissions, especially at high engine loads. In the present study, engine dynamometer experiments have been performed to investigate the heat exchange characteristics of the stack-type EGR coolers with wave fin pitches of 3.6 and 4.6 mm. The results show that the heat exchange effectiveness is decreased as surface area decrease with pitch of 4.6 mm due to PM fouling. As surface area increase at pitch of 3.6 mm, super-cooling happens in the recirculated exhaust gas.

Estimation of Heat Exchange Rate of Standing Column Well for Sustainable Groundwater Curtain for Greenhouse Heating (순환식 지하수 수막시스템 그린하우스 난방을 위한 스탠딩컬럼웰 열교환율 산정)

  • Byoung Ohan Shim;Seung Gyun Baek;Seonghoon Jeong
    • Journal of the Korean Society for Geothermal and Hydrothermal Energy
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    • v.20 no.2
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    • pp.11-23
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    • 2024
  • In order to design a standing column well (SCW) for a sustainable groundwater curtain system for greenhouse heating, we conducted parameter sensitivity tests. These tests simulated the outlet temperature changes of the SCW in a groundwater recirculating greenhouse cultivation system. Our modeling considered ground thermal conductivity and hydrogeological conditions. Specifically, we examined several factors, including SCW length, enhanced thermal conductivity of the ground, and groundwater circulation rate. The simulation results indicated that there was not a significant difference in the heat exchange rate based on the characteristics of enhanced thermal conductivity. However, we anticipate a substantial difference in the case of varying SCW lengths. Therefore, we conclude that the simulation results are primarily influenced by conductive heat exchange values, as the circulating water remains at a constant groundwater level.

Analysis of the Influence of Anti-icing System on the Performance of Combined Cycle Power Plants (가스터빈 결빙방지 시스템이 복합화력발전 시스템의 성능에 미치는 영향)

  • Moon, Seong Won;Kim, Jeong Ho;Kim, Tong Seop
    • The KSFM Journal of Fluid Machinery
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    • v.19 no.6
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    • pp.19-25
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    • 2016
  • Anti-icing is important in gas turbines because ice formation on compressor inlet components, especially inlet guide vane, can cause performance degradation and mechanical damages. In general, the compressor bleeding anti-icing system that supplies hot air extracted from the compressor discharge to the engine intake has been used. However, this scheme causes considerable performance drop of gas turbines. A new method is proposed in this study for the anti-icing in combined cycle power plants(CCPP). It is a heat exchange heating method, which utilizes heat sources from the heat recovery steam generator(HRSG). We selected several options for the heat sources such as steam, hot water and exhaust gas. Performance reductions of the CCPP by the various options as well as the usual compressor bleeding method were comparatively analyzed. The results show that the heat exchange heating system would cause a lower performance decrease than the compressor bleeding anti-icing system. Especially, the option of using low pressure hot water is expected to provide the lowest performance reduction.

Mean Heat Flux at Gunsan Harbor (군산항의 평균 열속)

  • CHOI Yong-Kyu;JO Young-Jo;CHOI Ok-In;YANG Won-Seok
    • Korean Journal of Fisheries and Aquatic Sciences
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    • v.36 no.5
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    • pp.535-540
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    • 2003
  • Based on the monthly weather report of Korea Meteorological Administration (KMA) and daily sea surface temperature (SST) data from National Fisheries Research and Development Institute (NFRDl) (1991-2001), mean heat fluxes were estimated at the Gunsan harbor Net heat flux was transported from the air to the sea surface during March to early September, and it amounts to $125\;Wm^{-2}$ in average daily during May to June. During the middle of September to February, the transfer of net heat flux was conversed from the sea surface to the air with $-125\;Wm^{-2}$ in mininum value in October. Short wave radiation was ranged from 50 to $248\;Wm^{-2}$ showing maxima in April to June. Long wave radiation was ranged from 25 to $92\;Wm^{-2}$ with mininum value in June to July. Sensible heat flux denoting negative values in April to August was ranged from -30 to $72\;Wm^{-2}.$ Latent heat flux was ranged from 15 to $82\;Wm^{-2}$ with maxima in August to September. The phase of heat exchange was changed from cooling to heating in the end of February, and from heating to cooling In the beginning of September. The advective term of heat flux showed minima in April to June and maxima in November. The ratio of temperature variations was 1.37 in the sea surface process and the horizontal process by advection. This indicates that the main factor in variation of temperature at Gunsan harbor is the heat exchange process through the sea surface from the air.

Aluminum and Plastic Heat Exchange Element : A Performance Comparison for Cooling of Telecommunication Cabinet (통신 함체 냉각용 알루미늄과 플라스틱 열교환 소자의 성능 비교)

  • Kim, Nae-Hyun
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.29 no.6
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    • pp.279-288
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    • 2017
  • Heat generation rate in a telecommunication cabinet increases due to the continued usage of mobile devices. Insufficient removal of heat intensifies the cabinet temperature, resulting in the malfunction of electronic devices. In this study, we assessed both aluminum and plastic heat exchangers used for cooling of the telecommunication cabinet, and compared the results against theoretical predictions. The aluminum heat exchanger was composed of counter flow parallel channels of 4.5 mm pitch, and the plastic heat exchangers were composed of cross flow triangular channels of 2.0 mm pitch. Samples were made by installing two plastic heat exchangers in both series and parallel. Results showed that the heat transfer rate was highest for the series cross flow heat exchanger, and was least for the aluminum heat exchanger. The temperature efficiency of the series cross flow heat exchanger was 59% greater than that of the aluminum heat exchanger, and was 4.3% greater than that of the parallel cross flow heat exchanger. In contrast, the pressure drop of the parallel cross flow heat exchanger was significantly lower than other samples. The heat exchange efficiency was also the largest for the parallel cross flow heat exchanger. The theoretical analysis predicted the temperature efficiency to be within 3.3%, and the pressure drop within 6.1%.

An Analysis on the Construction of Energy Exchange Network to Recover Waste Heat Energy in Pohang Steel Industrial Complex (포항철강산업단지 내부 폐열 회수를 위한 에너지 교환망 구축 방안 분석)

  • Lee, Gwang-Goo;Jung, In-Gyung;Chun, Hee-Dong
    • Clean Technology
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    • v.17 no.4
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    • pp.406-411
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    • 2011
  • A detailed database of waste heat is built to propose energy exchange networks to recover waste energy in Pohang Steel Industrial Complex. A visualized technique is used to figure out the status of waste heat energy and to suggest potential energy exchange networks. Several energy networks are proposed in terms of temperature level, the amount of available energy, distance, and construction cost. A simple economical assessment is applied to the energy exchange networks which have higher economic potential. Their average payback period is estimated to be 2.8 years. The total amount of energy saving by constructing the proposed energy exchange networks is 4,778 TOE per year. It corresponds to 11,160 ton $CO_2$ reduction with the assumption that the recycled waste energy replaces the use of LNG in energy-demanding companies.

The Performance Analysis for Low-Depth Unit-type Ground Heat Exchanger According to Grouting Materials (저심도 지중열교환기 개발을 위한 그라우트 재료에 따른 채열성능 검토 연구)

  • Oh, Jin-Hwan;Nam, Yujin
    • Journal of the Korean Society for Geothermal and Hydrothermal Energy
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    • v.11 no.2
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    • pp.7-11
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    • 2015
  • Recently, as the demand for sustainable energy sources is increasing, ground-source heat pump (GSHP) systems are receiving growing attention. However, the initial cost of GSHP system is higher than it of the conventional systems, especially, in small-size buildings. Therefore, for the application to the small-size building, it is necessary to develop small-size ground heat exchanger with small-size buildings. In this study, analysis of unit-type heat exchanger due to grouting materials. As a result, 1492.14 W of heat exchange rate was acquired in the condition of cement-silica sand-graphite materials.

Characteristics of Evaporation Heat Transfer in a Small-Scale Cryogenic Heat Exchange System for the Utilization of LNG Cold Energy (LNG 냉열활용을 위한 초저온 열교환시스템의 축소모형에서 증발 열전달 특성)

  • Nam S. C.;Lee S. C.;Lee Y. W.;Sohn Y. S.
    • 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.

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