• 제목/요약/키워드: exergy efficiency

검색결과 83건 처리시간 0.026초

Second Law Optimization of Water-to-Water Heat Pump System

  • Kim, Kyu-Hyung;Woo, Joung-Son;Lee, Se-Kyoun
    • Journal of Mechanical Science and Technology
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    • 제17권1호
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    • pp.122-128
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    • 2003
  • This paper presents a thermodynamic analysis of heat pump system using water as a heat source and heat sink. The primary object in this study is the optimization of exergetic efficiency. Two different systems, 2-stream and 1-stream system, are analyzed in detail. Mass flow ratio (the ratio of mass flow rate of water through evaporator to that through condenser) is identified as the most important parameter to be optimized. It is shown that there exists an optimum mass flow ratio to maximize exergetic efficiency. The variation of optimum exergetic efficiency of 2-stream system is quite small and the value lies between 0.2∼0.23 for the range of investigation in this study. However, far better performance can be obtained from 1-stream system. This means considerable irreversibilities are generated through condenser of the 2-stream system. The effects of adiabatic efficiency of compressor-motor unit on the overall system performance are also examined in the analysis.

열역학 제2법칙에 의한 압축과정의 합리적 효율 (Rational Efficiency of Compression Processes by the Second Law of Thermodynamics)

  • 정평석
    • 대한기계학회논문집
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    • 제14권5호
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    • pp.1200-1210
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    • 1990
  • 본 연구에서는 먼저, 단열 압축기 또는 단열압축 과정에 대한 기존의 효율들, 즉 등 엔트로피 효율과 폴리트로픽 효율 및 엑서지 효율에서의 출력에 해당하는 양의 의미를 검토하고, 이들을 엑서지 출력을 일반화 시킨 형태의 일종으로서 설명하며, 기 타의 가능한 효율을 정의하고, 나아가 같은 논리를 압축과정 중 외부와 열교환이 있는 비단열 압축과정에 대하여 확장 적용시켜 비단열 압축과정에서의 열역학 제2법칙적 출 력 및 효율들을 정의하고 그들의 특성을 살펴보려 한다.

R744를 2차냉매로 사용하는 R404A용 냉동시스템의 성능 분석 (Performance analysis of R404A refrigeration system using R744 as secondary refrigerant)

  • 오후규;손창효
    • 동력기계공학회지
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    • 제16권2호
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    • pp.24-29
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    • 2012
  • In this paper, an analysis on performance and exergy of R404A refrigeration system using R744 secondary refrigerant was performed numerically to optimize the design for the operating parameters. The operating parameters considered in this study include subcooling and superheating degree, internal heat exchanger and compression efficiency, evaporation and condensation temperature in the R404A refrigeration cycle and temperature difference of cascade heat exchanger. The main results are summarized as follows : The COP(coefficient of performance) of R404A refrigeration system increases with increasing evaporation temperature. The evaporation capacity of R744 as secondary refrigerant increases with the increase in evaporation pressure of R744 secondary refrigeration. And the enthalpy in the evaporator outlet of R744 increases with the increasing evaporation pressure of R744 secondary refrigeration. Therefore, it is important to analysis for the relationship between COP of R404A refrigeration system and refrigeration capacity of R744. As cascade evaporation temperature increase, the exergy loss of condenser and compressor using R404A is the largest among all components. Therefore, the exergy loss in the condenser and compressor using R404A must be decreased to enhance the COP of R404A refrigeration system with R744 secondary refrigerant.

액화천연가스 냉온열을 이용한 복합사이클의 설계 및 엑서지 해석 (Design and Exergy Analysis for a Combined Cycle using LNG Cold/Hot Energy)

  • 이근식
    • 설비공학논문집
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    • 제17권4호
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    • pp.285-296
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    • 2005
  • In order to reduce the compression power and to use the overall energy contained in LNG effectively, a combined cycle is devised and simulated. The combined cycle is composed of two cycles; one is an open cycle of liquid/solid carbon dioxide production cycle utilizing LNG cold energy in $CO_2$ condenser and the other is a closed cycle gas turbine which supplies power to the $CO_2$ cycle, utilizes LNG cold energy for lowering the compressor inlet temperature, and uses the heating value of LNG at the burner. The power consumed for the $CO_2$ cycle is investigated in terms of a production ratio of solid $CO_2$. The present study shows that much reduction in both $CO_2$ compression power (only $35\%$ of power used in conventional dry ice production cycle) and $CO_2$ condenser pressure could be achieved by utilizing LNG cold energy and that high cycle efficiency ($55.3\%$ at maximum power condition) in the gas turbine could be accomplished with the adoption of compressor inlet cooling and regenerator. Exergy analysis shows that irreversibility in the combined cycle increases linearly as a production ratio of solid $CO_2$ increases and most of the irreversibility occurs in the condenser and the heat exchanger for compressor inlet cooling. Hence, incoming LNG cold energy to the above components should be used more effectively.

열역학적 사이클의 제2법칙 효율의 정의에 대한 기본 연구 (Basic Study on the Definition of the Second Law Efficiencies of Thermodynamic Cycles)

  • 박경근
    • 설비공학논문집
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    • 제24권11호
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    • pp.792-798
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    • 2012
  • A general concept on the definition of the second law efficiencies of thermodynamic cycles is introduced. The efficiency is defined to be proportional to the entropy generation divided by the maximum possible entropy generation. This way of definition of the cycle efficiency is clear and concise and, moreover, follows faithfully the concept of the second law of thermodynamics. This definition is applied to heat engine, refrigerator and heat pump. The second law efficiencies of heat engine and refrigeration cycles are derived, which are the same as the existing ones, respectively. The second law efficiency of heat pump, however, finds to be different from the existing one. Discussion is given about the difference and its cause.

Exergy and exergoeconomic analysis of hydrogen and power cogeneration using an HTR plant

  • Norouzi, Nima;Talebi, Saeed;Fani, Maryam;Khajehpour, Hossein
    • Nuclear Engineering and Technology
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    • 제53권8호
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    • pp.2753-2760
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    • 2021
  • This paper proposes using sodium-cooled fast reactor technologies for use in hydrogen vapor methane (SMR) modification. Using three independent energy rings in the Russian BN-600 fast reactor, steam is generated in one of the steam-generating cycles with a pressure of 13.1 MPa and a temperature of 505 ℃. The reactor's second energy cycles can increase the gas-steam mixture's temperature to the required amount for efficient correction. The 620 ton/hr 540 ℃ steam generated in this cycle is sufficient to supply a high-temperature synthesis current source (700 ℃), which raises the steam-gas mixture's temperature in the reactor. The proposed technology provides a high rate of hydrogen production (approximately 144.5 ton/hr of standard H2), also up to 25% of the original natural gas, in line with existing SMR technology for preparing and heating steam and gas mixtures will be saved. Also, exergy analysis results show that the plant's efficiency reaches 78.5% using HTR heat for combined hydrogen and power generation.

정압식 압축공기저장(CAES) 발전 시스템 에너지 분석 (Energy Analysis of Constant-Pressure Compressed Air Energy Storage (CAES) Generation System)

  • 김영민;이선엽;이장희
    • 에너지공학
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    • 제20권3호
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    • pp.178-184
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    • 2011
  • 압축공기저장(CAES) 발전은 가스터빈에 필요한 압축공기를 야간이나 비첨두 시간에 저렴한 전기로 미리 압축해서 저장하였다가 주간에 활용하는 것으로 전력 저장과 발전의 하이브리드 기술이라고 할 수 있다. 그러나 기존 압축공기저장 발전의 경우 심야에 압축공기를 일정부피의 압축공기 저장조에 충전하게 되면 저장조내의 압력은 점점 증가하게 되고, 반대로 주간에 발전을 위해 압축공기를 방출하게 되면 저장조내의 압력은 감소하게 된다. 이와 같이 운전 압력비 조건이 넓은 범위로 변화하여 설계 압력비에서 벗어나게 되는 것은 압축 및 팽창효율이 크게 감소하게 되는 원인이 된다. 본 논문에서는 이러한 기존의 변압식 압축공기저장 발전 방식의 문제점을 해결하기 위해 새로운 방식의 정압식 압축공기저장 발전 방식을 제시하고 있으며, 엑서지 개념을 포함한 에너지 분석을 통해 에너지 밀도 증가와 효율 향상 효과를 예측하였다. 새로운 방식의 정압식 압축공기 저장 발전 방식은 정압식 압축공기 저장 발전과 공압식 양수발전의 하이브리드 개념으로 기존 변압식 압축공기저장 발전 방식에 비해 정압 운전에 의한 효율향상과 에너지 밀도 증가로 압축공기 저장조의 크기를 50%이상 줄일 수 있는 장점을 가지고 있다.

200kW 인산형 연료전지 발전시스템의 엑서지-열경제학적 해석 (Exergetic and Thermoeconomic Analysis of a 200kW Phosphoric Acid Fuel Cell Plant)

  • 전진석;곽호영;이현수;최동수;박달령;조영아
    • 대한기계학회:학술대회논문집
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    • 대한기계학회 2001년도 춘계학술대회논문집D
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    • pp.689-696
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    • 2001
  • Exergetic and thermoeconomic analysis were performed for a 200kW Phosphoric Acid Fuel Cell(PAFC) plant which offers many advantage for cogeneration in the aspect of high electrical efficiency and low emission. This analytical study was based on the data obtained by in-field measurement of PC25 fuel cell plant to find whether this system is viable economically. For 100% load condition, the electrical efficiency and the unit cost of electricity are about 45% and 0.032 $/kWh respectively, which turn out to be much better than those for the 1000kW gas turbine cogeneration plant. Further, at lower loads, the unit costs of electricity and hot water increase slightly and consequently more economic operation is possible at any loads.

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熱交換 過程을 考慮한 랜킨 사이클의 性能解析 (Analysis of the Rankine Cycle Including Heat Exchange Processes)

  • 정평석;노승탁
    • 대한기계학회논문집
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    • 제10권1호
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    • pp.150-156
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    • 1986
  • 본 논문에서는 열전달을 포함한 사이클 해석의 좀 더 실제적인 경우로서, 주어진 연소가스로부터 랜킨사이클을 사용하여 동력을 추출할 때 최대의 출력을 추출하기 위한 사이클의 운전조건을 고찰하고, 대표적인 랜킨 사이클에 대하여 여러가지 운전조건에 따른 출력등을 계산하여, 그 결과를 고찰하였다.

A proposal on SOFC-PEMFC combined system for maritime applications

  • Duong Phan Anh;Ryu Borim;Nguyen Quoc Huy;Lee Jinuk;Kang Hokeun
    • 한국항해항만학회:학술대회논문집
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    • 한국항해항만학회 2022년도 추계학술대회
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    • pp.162-163
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    • 2022
  • Maritime transportation is going to transfer to alternative fuels as a result of the worldwide demands toward decarbonization and tougher maritime emissions regulations. Methanol is considered as a potential marine fuel, which has the ability to reduce SOx and CO2 emissions, reduce climate change effects, and achieve the objective of green shipping. This work proposes and combines the innovative combination system of direct methanol solid oxide fuel cells (SOFC), proton exchange membrane fuel cells (PEMFC), gas turbines (GT), and organic Rankine cycles (ORC) for maritime vessels. The system's primary power source is the SOFC, while the GT and PEMFC use the waste heat from the SOFC to generate useful power and improve the system's ability to use waste heat. Each component's thermodynamics model and the combined system's model are established and examined. The multigeneration system's energy and exergy efficiency are 76.2% and 30.3%, respectively. When compared to a SOFC stand-alone system, the energy efficiency of the GT and PEMFC system is increased by 19.2%. The use of PEMFC linked SOFC has significant efficiency when a ship is being started or maneuvered and a quick response from the power and propulsion plant is required.

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