• Title/Summary/Keyword: 열회수 효율

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Performance Evaluation of Heat Recovery Steam Generator in Combined Cycle Gas Turbine Power Plants Based on First and Second-Law Analysis (복합사이클 발전플랜트 폐열회수 보일러의 열역학 제1법칙 및 제2법칙 해석)

  • In, Jong-Soo
    • Proceedings of the KAIS Fall Conference
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    • 2010.11b
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    • pp.684-687
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    • 2010
  • 본 논문은 복합사이클 발전플랜트의 폐열회수 보일러 최적운전 및 최적설계에 대한 새로운 접근 방법을 도출하기 위해 폐열회수 보일러에서 발생되는 증기로 증기터빈을 구동하는 하부사이클 효율을 검토하였다. 열역학 제1법칙 해석을 통해 하부사이클 에너지 평형을 검토하였고, 열역학 제2법칙을 통해 엑서지 평형을 검토하였다. 하부사이클 효율이 최대가 되는 폐열회수 보일러를 설계하기 위해서는 열역학 제1법칙을 해석할 경우 하부사이클 전체를 해석하여야 함을 알 수 있다. 하지만, 열역학 제2법칙을 통한 엑서지 해석을 행할 경우 하부사이클 효율이 최대가 되는 증발온도와 폐여회수 보일러에서 소모되는 엑서지가 최소가 되는 점이 일치함을 알 수 있었다. 따라서 본 논문을 통해 폐열회수 보일러에서 소모되는 엑서지 해석을 통해 하부사이클 효율이 최대가 되는 폐열회수 보일러 최적화가 가능함을 알 수 있다.

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생활폐열회수를 위한 열교환기 개발 중심 폐열회수 고효율 난방 시스템

  • 신현준;이태원
    • 월간 기계설비
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    • s.46
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    • pp.65-73
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    • 1994
  • 도시생활폐수에 포함되어 배출되는 폐열을 열펌프의 열원으로 하는 폐수열원 열펌프 시스템에 대한 관심이 오래전부터 집중되어 있었지만 폐수 열교환기 전열면의 오염문제 때문에 실용화에 커다란 진전을 보지 못하고 있다. 한편, 생활페수는 비교적 저온이기 때문에 열펌프시스템의 설계에 특별한 주의를 기울여야 한다. 즉, 이러한 폐열을 회수하여 유효에너지 자원화 하기 위한 신기술이 이루어 져야한다. 본 연구에서는 이러한 점을 감안하여 도시생활 폐수열의 이용가능성을 검토하고 이를 열원으로 하는 열펌프의 개발을 위한 폐수 열교환기의 모델을 개발하였다.

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A Study on a Resorption Beat Pump Using Methanol-Glycerine (메탄올-글리세린을 이용한 재흡수 열펌프의 열역학적 모사 연구)

  • Min, Byong-Hun
    • Journal of Energy Engineering
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    • v.15 no.4 s.48
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    • pp.284-290
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    • 2006
  • The improvement of energy recovery is mandatory to decrease consumption of fossil fuels and to minimize negative impacts on the environment which originates from large cooling and heating demand. The absorption heat pump technology has a large potential for energy saving in this respect. Absorption heat pump is a means to upgrade waste heat without addition of extra thermal energy. In this study, resorption heat pump for energy recovery has been investigated using methanol-glycerine. The simulated calculation of theoretical thermal efficiency was performed based on the thermodynamic properties of the working fluid over various operating conditions. The thermal efficiency of higher than 0.4 was obtained by raising industrial waste heat, $70{\sim}80^{\circ}C$, by $40^{\circ}C$ in this system.

Hydrate Production Performance Analysis with Multi-Well, Plate-Type Apparatus Using Depressurization and Thermal Methods (다중공 평판형 장비를 이용한 감압법과 열자극법에 의한 하이드레이트 가스 생산성 분석)

  • Lee, Youngsoo;Wang, Jihoon;Park, Jungkyoon;Sung, Wonmo
    • Korean Chemical Engineering Research
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    • v.47 no.1
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    • pp.133-140
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    • 2009
  • This paper presents the experimental study to analyze the pressure and production behavior using depressurization and thermal methods in order to evaluate the hydrate productivity in the 2-D multi-well, plate-type apparatus which has 80 md permeability and 30% hydrate saturation. Injecting methane gas through multi-well allowed to set up the highly saturated hydrate system and combining two different sorts of sands made possible to build up the low permeability system. In this system, both depressurization and electric stimulation methods were applied. When operating pressure was low, according to the depressurization experiments results, the gas recovery was high, however strong pulses which appeared at initial stage of production would damage the operation system. Moreover, cases that hydrate reformed have occurred by endothermic reaction. We have conducted experiments four and six times for the depressurization magnitudes of 140 psi and 320 psi, respectively, to analyze production behavior for the method more in detail. For the cases that the depressurization magnitude was set as 140 psi, the unstable period appears in the results, but stabilized soon. In the experiment results for 320 psi the discontinuous and intermittent behavior has been observed. Thermal stimulation experiments was conducted with depressurizing 80 psi which is the case that shows stable behavior and low recovery. In the results, the gas recovery was high and the energy efficiency was low for long stimulating time. The energy efficiency and gas recovery increased for the soaking time of 1 minute after 2 minute-preheating. In the cases of which the soaking time exceeds 1 minute, energy loss by long soaking time caused low gas recovery and poor energy efficiency.

Analysis of organic rankine cycle for designing evaporator of engine exhaust heat recovery system (엔진 배기열 회수 증발기 설계를 위한 유기랭킨사이클 분석)

  • Ko, Jea-Hyun;Choi, Byung-Chul;Park, Kweon-Ha
    • Journal of Advanced Marine Engineering and Technology
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    • v.37 no.5
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    • pp.446-452
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    • 2013
  • Interest in the energy efficiency and carbon reduction technology is increasing. Many studies have done on the technologies of heat recovery systems, because over 30% of the total energy is released into the atmosphere with the exhaust gas flow. In this study, the Rankine cycle is analyzed in the optimum conditions given through the previous work. The result shows that the exergy efficiency is 0.53 and the output is 1.43 kW at the condition of the pressure ratio of 0.6 and the mass flow rate of 0.7.

Development and efficiency evaluation of 30kW scale syngas cogeneration system (30kW 급 합성가스 열병합 시스템 개발 및 효율 성능평가)

  • Park, Il-Gun;Kim, Sang-Tae;Noh, Gwi-Sung
    • Journal of the Korean Applied Science and Technology
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    • v.36 no.4
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    • pp.1427-1433
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    • 2019
  • In this paper, Gas engine was tested for the energy of synthesis gas. As excess air ratio increase 1, 1.1, 1.2, 1.3, 1.4, 1.5, 1.6 in 1800 rpm and synthesis gas, thermal efficiency generally decrease and power generation was 34 kWm at λ 1.4. And excess air ratio increase 1, 1.1, 1.2, 1.3, 1.4 in power generation 34 kWm, thermal efficiency generally increase 34.2%, 36.9%, 37.2%, 37.4%, 38.1%. Total efficiency through power generation consumes 38.7 kg/h of fuel at 30 kWe load and recovers 57.3% of waste heat by recovering 57.3 kW of waste heat through 32.1% power generation efficiency and heat recovery from cooling water and exhaust gas. The total efficiency was 85.8%.

소형 열병합발전의 제도 및 경제성분석

  • 이진홍
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 1993.11a
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    • pp.49-56
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    • 1993
  • 열병합 발전이란 한가지의 에너지원을 열원으로 하여 2가지 이상의 동력을 회수하는 방법을 말하며 회수에너지는 고급에너지인 전기가 주가 되고 이 때 발생되는 폐열은 회수하여 증기, 난방용 온수, 냉방용 냉수로 이용할 수 있어 총 효율이 70 ∼ 80%에 달하는 방식이다. 열병합 발전은 규모에 따라 목동열병합과 같은 쓰레기 소각로 이용형, 분당, 일산 등과 같이 지역난방과 연결할 수 있는 가스터빈, 증기터빈 조합형인 복합 열병합형의 대형열병합과 각 산업체 공장에서 전기 및 공장 Process 증기 생산을 주목적으로 하는 중형 열병합과, 조선호텔, 신라호텔, 상공회의소등과 같이 Hotel, 병원, 사무실 등에서 주로 이용하는 소형 열병합으로 분류할 수 있다. (중략)

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High-efficiency Agricultural Heater and Smart Control System Utilizing Heat Pipe (히트파이프를 활용한 농업용 고효율난방기 및 스마트 제어시스템)

  • Kim, Eung-Kon;Lim, Chang-Gyoon
    • The Journal of the Korea institute of electronic communication sciences
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    • v.12 no.6
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    • pp.1151-1158
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    • 2017
  • The Effluent Heat Pipe integral with the heater is a device that recreates unused thermal energy from the plant in winter, and thus reuses unused energy before releasing the exhaust heat. Through the establishment of facility horticulture and glass greenhouses, we identified the problems of our agricultural heaters, and we proposed efficient agricultural efficiency and smart control systems for optimum agricultural efficiency and smart house.

Heat Exchanging Performance as Affected by Arrangement of Heat Exchanging Pipe (열회수장치의 열교환 파이프배치 형식별 열교환 성능)

  • 윤용철;강종국;서원명
    • Journal of Bio-Environment Control
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    • v.11 no.3
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    • pp.101-107
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    • 2002
  • This study was carried out to improve the performance of heat recovery device attached to exhaust gas flue connected to combustion chamber of greenhouse heating system. Three different units were prepared far the comparison of heat recovery performance; A-type is exactly the same with the typical one fabricated for previous study of analyzing heat recovery performance in greenhouse heating system, other two types (B-type and C-type) modified from the control unit are different in the aspects of airflow direction (U-turn airflow) and pipe arrangement. The results are summarized as follows ; 1. In the case of Type-A, when considering the initial cost and current electricity fee required for system operation, it was expected that one or two years at most would be enough to return the whole cost invested. 2. Type-B and Type-C, basically different with Type-A in the aspect of airflow pattern, are not sensitive to the change of blower capacity with higher than 25m$^3$.min$^{-1}$ . Therefore, heat recovery performance was not improved so significantly with the increment of blower capacity. This was assumed to be that air flow resistance in high air capacity reduced the heat exchange rate as well. Never the less, compared with control unit, resultant heat recovery rate of Type-B and Type-C was improved by about 5% and 13%, respectively 3. Desirable blower capacity of these heat recovery units experimented were expected to be about 25m$^3$.min$^{-1}$ , and at the proper blower capacity, U-turn airflow units showed better heat recovery performance than control unit. But, without regard to the type of heat recovery unit, it was recommended that comprehensive consideration of system's physical factors such as pipe arrangement density, unit pipe length and pipe thickness, etc., was required for the optimization of heat recovery system in the aspects of not only energy conservation but economic system design.

Preliminary Feasibility Study of Separated Aquifer Thermal Energy Storage System using Numerical Method (수치 모델링 기법을 이용한 개별 대수층 축열 시스템 활용성 예비 평가)

  • Kim, Jong-Chan;Kim, Hyoung-Soo;Lee, Young-Min
    • 한국신재생에너지학회:학술대회논문집
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    • 2009.11a
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    • pp.556-560
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    • 2009
  • 개별 대수층에 냉수와 온수를 저장하여 수자원과 냉난방 열원으로 활용하는 방안에 대한 평가를 지열-지하수 부정류 모델링을 통해 수행하였다. 저장 및 회수 가동 시간이 증가함에 따라서 각각의 대수층 내에 온열과 냉열이 축열되는 현상이 확인되었으며, 지하수 유동에 의해 축열된 수체가 지하수 흐름방향으로 이동하는 현상을 확인 하여 지하수 유동이 축열 정도를 결정하는 요인이 될 수 있음을 확인하였다. 설정된 모델에 대하여, 두 개의 개별 대수층 사이의 열 간섭은 거의 없는 것으로 나타났다. 주입과 양수의 가동 횟수가 증가되면, 대수층 축열 효과는 증대되는 것으로 나타났다. 열-지하수 모델링을 통한 온도 예측은 실제 냉난방의 효율성을 결정짓는 수온을 정량적으로 계산할 수 있는 유용한 기술로 평가됨과 더불어, 수자원의 지하 저장을 통해 효율적으로 물을 확보하고 관리할 수 있는 방안이 될 수 있을 것으로 기대된다.

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