• 제목/요약/키워드: waste heat recovery

검색결과 246건 처리시간 0.027초

중고온 히트파이프를 이용한 열회수기술에 관한 연구 (Technology of Waste Heat Recovery Using Heat Pipe Heat Exchanger for Industrial Practice)

  • 이영수;김종률;장기창;백영진
    • 설비공학논문집
    • /
    • 제16권11호
    • /
    • pp.1044-1050
    • /
    • 2004
  • The present study has been conducted to develop a heat pipe heat exchanger for middle-high temperature ranged from 300 to $600^{\circ}C$. Heat transfer rate, overall heat transfer coefficient and temperature effectiveness were investigated using a heat pipe heat exchanger with Dowtherm A as working fluid. Theoretical analysis was also conducted, and the followings were obtained: (1) Heat exchange rate increased as waste gas temperature supplied to evaporator and frontal velocity in condenser increased, (2) Overall heat transfer coefficient increased by $3{\sim}7\%$ as frontal velocity in evaporator and condenser increased, (3) Temperature effectiveness was about $30\%$ in evaporator and was about $40\%$ in condenser, (4) Heat recovery rate was about $38\%$, (5) Pressure drop did not exceed $8\;mmH_{2}O$ under the running condition of $1{\sim}3Nm/s$, (6) Simulation results were corresponded with experimental results.

해수 열원 및 폐열 이용 고성능 열펌프 시스템 모사 (Simulation for High Efficient Heat Pump System using Seawater Heat Source and Exhaust Energy)

  • 최광일;오종택;오후규
    • 설비공학논문집
    • /
    • 제15권1호
    • /
    • pp.59-66
    • /
    • 2003
  • The purpose of this study is to analyze the characteristics (COP) of the heat pump system for various operating conditions with the use of seawater heat source and exhaust energy. To accomplish the goal, first of all, the computer simulation for heat pump system is carried out. The heat pump system model is made of a waste heat recovery system and a vapor compression refrigeration system, and the working fluid is R-22. The model calculated the change of COP with the variation of temperature and flow rate. The COP and the plate heat exchanger (PHE) area of the heat pump system are considered moderately high in the condensation temperature of $25^{\circ}^C$ and the evaporation temperature of $2^{\circ}^C$ in indoor culture system. The simulation results will be used effectively for the design and the performance prediction of heat pump system using unused energy in a land base aquaculture system.

기관 폐열 회수를 위한 열교환기의 Baffle 길이 변경에 따른 성능 예측에 관한 수치 해석적 연구 (An Investigation on Flow and Structural Characteristics of Heat Exchanger in Rankine Steam Cycle for Co-generation System)

  • 류규현;김구성;이영훈;강석호;박기범
    • 신재생에너지
    • /
    • 제9권4호
    • /
    • pp.32-39
    • /
    • 2013
  • A 2-loop waste heat recovery system with Rankine steam cycles for the improvement of fuel efficiency of gasoline vehicles has been investigated. A high temperature loop is used to recover waste heat from exhaust gas and a low temperature loop is used to recover waste heat from cold engine coolant. This paper has dealt with a layout of low temperature loop system, the review of the velocity contours through numerical analysis. According to the result of analysis, the designed heat exchanger. And comparing with flow analysis results, LT Boiler is safe to operation.

폐열 회수용 사판식 스팀 팽창기 설계 (Design of a Swash Plate Type of Steam Expander for Waste Heat Recovery)

  • 김현재;김현진
    • 설비공학논문집
    • /
    • 제23권5호
    • /
    • pp.313-320
    • /
    • 2011
  • For a steam Rankine cycle to recover waste heat from the exhaust gas of an Internal combustion engine, a swash plate type of expander as a power conversion unit has been designed. Numerical simulation has been carried out to estimate the performance of the designed expander. With the steam pressure and temperature of 35 bar and $300^{\circ}C$ at the expander inlet, respectively, the expander was estimated to produce the shaft power output of about 2.67 kW from the exhaust gas waste heat of 25.2 kW. The expander output increased almost linearly with the amount of exhaust gas waste heat in the range of from 5~40 kW, and the expander and Rankine cycle efficiencies showed gradual decreases in the ranges of 72.2%~69.5% and 10.8%~10.4%, respectively.

자동차 배기가스 폐열 회수용 팽창기 개념설계 (Conceptual design of an expander for waste heat recovery of an automobile exhaust gas)

  • 김현재;김유찬;김현진
    • 한국신재생에너지학회:학술대회논문집
    • /
    • 한국신재생에너지학회 2009년도 추계학술대회 논문집
    • /
    • pp.237-242
    • /
    • 2009
  • A steam Rankine cycle was considered to recover waste heat from the exhaust gas of an automobile. Conceptual design of a swash plate type expander was practiced to convert steam heat to shaft power. With the steam pressure and temperature of 35 bar and $300^{\circ}C$ at the expander inlet, respectively, the expander was estimated to produce the shaft power output of about 1.93 kW from the exhaust gas waste heat of 20 kW. The expander output increased linearly accordingly to the amount of exhaust gas waste heat in the range of from 10-40 kW, and the Rankine cycle efficiency was more or less constant at about 9.6% regardless of the waste heat amount.

  • PDF

소형 가스엔진 발전기의 배기가스 폐열을 이용한 바이오가스 개질 가능성에 관한 실험적 연구 (An Experimental Study on the Possibility of Biogas Reforming using the Waste Heat of a Small-Sized Gas Engine Generator)

  • 차효석;김태수;엄태준;정충수;전광민;송순호
    • 한국수소및신에너지학회논문집
    • /
    • 제23권3호
    • /
    • pp.236-242
    • /
    • 2012
  • This study has been carried out the experiment for the possibility of biogas reforming using waste heat. The source of this waste heat is the exhaust gas from a small-sized gas engine generator. For recovering the waste heat, Two-stage heat exchanger is manufactured. The two-stage heat exchanger is composed of a heat exchanger for the exhaust gas and a heat exchanger for the water. This two-stage heat exchanger is used for reforming the biogas by means of on-site hydrogen production at the small-sized gas engine generator. The two-stage heat exchanger is coupled with the biogas reformer which is a kind of catalytic reformer. To confirm a heat recovery efficiency of the two-stage heat exchanger, temperature differences of inlet and outlet locations are measured. Also, the variations of syngas concentrations with various biogas flow rates are investigated. As a result using manufactured two-stage heat exchanger, the biogas can be reformed from waste heat recovery. This experiment suggests that the exhaust gas heat exchanger is available for reforming the biogas.

산업폐열 발전시스템 경제성분석 모듈 개발 및 신뢰성 최적화 (Development and Reliability Optimization of Economic Analysis Module for Power Generation System from Industrial Waste Heat Recovery)

  • 고아름;박성호;김준영;차재민
    • 에너지공학
    • /
    • 제27권4호
    • /
    • pp.50-63
    • /
    • 2018
  • 화석연료의 무분별한 사용으로 인해 지구 온난화 및 환경오염 문제가 대두되고 있으며, 이에 따라 효율적인 에너지 활용을 위해 기존에 버려지는 폐열을 회수하는 기술에 대한 필요성이 커지고 있다. 산업폐열 발전 시장은 발전효율을 높일 수 있다는 장점으로 인해 연평균 5% 성장하고 있다. 고효율 폐열발전시스템 설계를 위해 열원별 조건에 따른 발전 기술별 경제성을 평가할 수 있는 프로그램 개발이 필요하다. 따라서 본 연구에서는 산업폐열 발전시스템에 최적화된 경제성분석 모듈 개발을 위해 균등화 전력원가를 산출하는 모듈을 개발하고 NETL의 경제성분석 사례를 바탕으로 시스템의 신뢰도를 검증하였다. 검증 결과, 오차율은 약 6~7%로 사업 타당성 평가를 위한 정확도를 만족하였으나, 신뢰성 향상을 위해 NETL에서 사용하는 균등화 방법론을 적용하여 알고리즘을 개선하였고 이에 따라 오차율은 1% 미만으로 신뢰도가 향상되었다.

습증기를 포함한 연소가스의 폐열회수를 위한 열교환기 성능 예측 (Performance Prediction of Heat Exchanger for Waste Heat Recovery from Humid Flue Gases)

  • 정동운;이상용;이한주
    • 대한기계학회:학술대회논문집
    • /
    • 대한기계학회 2000년도 춘계학술대회논문집B
    • /
    • pp.276-281
    • /
    • 2000
  • A simulation program using the mass transfer correlation was constructed to analyze 1-D simplified condensing flow across the tube bank. Higher efficiency was anticipated by reducing the flue gas temperature down below the dew point where the water vapor in the flue gas is condensed at the surface of the heat exchanger; that is, the heat transfer by the latent heat is added to that by the sensible heat. Thus, there can be an optimum operating condition to maximize the heat recovery from the flue gas. The temperature rises of the flue gas and the cooling water between the inlet and the outlet of the tube bank were compared with the experimental data reported previously. The predicted results agree well with the experimental data. Using this simulation program, the parametric studies have been conducted fur various operating conditions, such as the velocities and temperatures of the vapor/gas mixture and the cooling water, the number of the rows, and the conductivity of the wall material.

  • PDF

EGR 가스 폐열회수에 의한 디젤엔진의 연비에 미치는 ATF 워밍업의 영향 (Effect of Fast ATF Warm-up on Fuel Economy Using Recovery of EGR Gas Waste Heat in a Diesel Engine)

  • 허형석;이동혁;강태구;이헌균;김태진
    • 한국자동차공학회논문집
    • /
    • 제20권4호
    • /
    • pp.25-32
    • /
    • 2012
  • Cold start driving cycles exhibit an increases in friction losses due to the low temperatures of metal components and media compared to the normal operating engine conditions. These friction losses are adversely affected to fuel economy. Therefore, in recent years, various techniques for the improvement of fuel economy at cold start driving cycles have been introduced. The main techniques are the upward control of coolant temperature and the fast warm-up techniques. In particular, the fast warm-up techniques are implemented with the coolant flow-controlled water pump and the WHRS (waste heat recovery system). This paper deals with an effect of fast ATF (automatic transmission fluid) warm-up on fuel economy using a recovery system of EGR gas waste heat in a diesel engine. On a conventional diesel engine, two ATF coolers have been connected in series, i.e., an air-cooled ATF cooler is placed in front of the condenser of air conditioning system and a water-cooled one is embedded into the radiator header. However, the new system consists of only a water-cooled heat exchanger that has been changed into the integrated structure with an EGR cooler to have the engine coolant directly from the EGR cooler. The ATF cooler becomes the ATF warmer and cooler, i.e., it plays a role of an ATF warmer if the temperature of ATF is lower than that of coolant, and plays a role of an ATF cooler otherwise. Chassis dynamometer experiments demonstrated the fuel economy improvement of over 2.5% with rapid increase in the ATF temperature.