• 제목/요약/키워드: energy recovery

검색결과 1,668건 처리시간 0.027초

LNG FSRU의 재기화 공정에서 폐에너지회수시스템의 엑서지 분석 (Exergy Analysis of Waste Energy Recovery System in Regasification Process of LNG FSRU)

  • 한승현;조재호;권정태;박경우;최병철
    • 신재생에너지
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    • 제18권2호
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    • pp.82-89
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    • 2022
  • In this study, the exergy characteristics were analyzed, according to the mass flow rate of the propane working fluid and the pressure change in the turbine inlet, for the efficient recovery of cold energy and exhaust heat by the waste energy recovery system applied to the LNG FSRU regasification process. When the turbine inlet pressure and mass flow rate of the Primary Rankine Cycle were kept constant, the exergy efficiency and the net power increased. This occurred as the turbine inlet pressure and the mass flow rate of the working fluid increased in the Secondary Rankine Cycle, respectively, and the maximum values were confirmed. In this regard, the fluctuations in the exergy rate flowing into and out of the system and the exergy rate destroyed by pumps, evaporators, turbines, and LNG heat exchangers (condensers) were examined in detail.

화력발전용 복수기 폐열 회수를 위한 유기랭킨사이클 시스템 열교환 특성 해석 (A Heat Exchanging Characteristics of Organic Rankine Cycle for Waste Heat Recovery of Coal Fired Power Plant)

  • 정진희;임석연;김범주;유상석
    • 한국수소및신에너지학회논문집
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    • 제26권1호
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    • pp.64-70
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    • 2015
  • Organic Rankine cycle (ORC) is an useful cycle for power generation system with low temperature heat sources ($80{\sim}400^{\circ}C$). Since the boiling point of operating fluid is low, the system is used to recover the low temperature heat source of waste heat energy. In this study, a ORC with R134a is applied to recover the waste energy of condenser of coal fired power plant. A system model is developed via Thermolib$^{(R)}$ under Simulink/MATLAB environment. The model is composed of a refrigerant heat exchanger for heat recovery from coal fired condenser, a drum, turbine, heat exchanger for ORC heat rejection, storage tank, water recirculation pump and water drip pump. System analysis parameters were heat recovery capacity, type of refrigerants, and types of turbines. The simulation model is used to analyze the heat recovery capacity of ORC power system. As a result, increasing the overall heat transfer coefficient to become the largest of turbine power is the most economical.

Pd 분리막을 이용한 수소동위원소 회수 실험과 공정 시뮬레이션 (Hydrogen Isotopes Recovery Using Pd Membrane and Process Simulation)

  • 정우찬;박종환;한상우;장민호;이현곤
    • 한국수소및신에너지학회논문집
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    • 제32권4호
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    • pp.219-227
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    • 2021
  • Hydrogen isotopes, which are used as raw materials in fusion reaction, participate in the reaction only in small amount, and most of them are released together with impurities. In order to recover and reuse only hydrogen isotopes from this exhaust gas, a recovery process is required, and most of the hydrogen isotopes can be recovered using a Pd Membrane. In this study, the recovery rate of hydrogen isotopes was measured through the first and second stage Pd membrane experiments. In the case of the experiment using a single stage Pd membrane, about 99.2%, and in the case of the first stage and second stage Pd membrane connection experiments, a recovery rate of 99.9% or more was obtained. Therefore, the recovery rate of Pd membrane process applied to hydrogen can be applied to hydrogen isotopes. In addition, the simulation model was established using aspen custom modeler, a commercial software, and the validity of the simulation was checked by applying the references and experimental data. The simulation results based on the experimental data showed a difference of 2% or less.

아스펜 플러스를 이용한 폭발성 가스 건식 연소 처리공정의 열회수 모델링 및 엑서지 분석 (Heat Recovery Modeling and Exergy Analysis of Dry Combustion Process for Explosive Gas Treatment Using Aspen Plus)

  • 최용만;최창식;홍범의;조성수;김용진;김학준
    • 한국대기환경학회지
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    • 제33권5호
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    • pp.521-528
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    • 2017
  • In the combustion treatment of explosive gases with a high heating value such as $H_2$ and $NH_3$ used in semiconductor and chemical processes, the heat recovery modeling and exergy analysis of the process using the Aspen Plus simulator and its thermodynamic data were performed to examine the recovery of high temperature thermal energy. The heat recovery process was analyzed through this process modeling while the exergy results clearly confirmed that the rigorous reaction mainly occurs in the condenser and the chamber. In addition, the process modeling demonstrated that approximately 95% of the exergy is destructed on the basis of the exergies injected and the exergy being exhausted. Using the exergy technique, which can quantitatively analyze the energy, we could understand the energy flow in the process and confirm that our heat recovery process was efficiently designed.

Chemical Inhibition of Cell Recovery after Irradiation with Sparsely and Densely Ionizing Radiation

  • Evstratova, Ekaterina S.;Kim, Jin-Hong;Lim, Young-Khi;Kim, Jin Kyu;Petin, Vladislav G.
    • 방사선산업학회지
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    • 제10권4호
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    • pp.199-204
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    • 2016
  • The dependence of cell survival on exposure dose and the duration of the liquid-holding recovery (LHR) was obtained for diploid yeast cells irradiated with ionizing radiation of different linear energy transfer (LET) and recovering from radiation damage without and with various concentrations of cisplatin - the most widely used anticancer drug. The ability of yeast cells to recover from radiation damage was less effective after cell exposure to high-LET radiation, when cells were irradiated without drug. The increase in cisplatin concentration resulted in the disappearance of this difference whereas the fraction of irreversible damage was permanently enlarged independently of radiation quality. The probability of cell recovery was shown to be constant for various conditions of irradiation and recovery. A new mechanism of cisplatin action was suggested according with which the inhibition of cell recovery after exposure to ionizing radiations was completely explained by the production of irreversible damage.

침몰선박 잔존유 무인회수장비의 기본설계에 관한 연구 (A Study on the Basic Design of a Remotely Operated Recovery System for Removing Toxic Liquid Contained in a Sunken Ship)

  • 최혁진;이경중;변성훈;강창구;이승훈
    • 한국해양환경ㆍ에너지학회지
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    • 제6권3호
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    • pp.54-62
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    • 2003
  • 본 연구에서는 다양한 침몰선박 잔존유회수 방법 중에서 안전성과 경제성을 바탕으로 우리나라 해역특성에 적합한 무인 원격회수방법을 선정하였다. 이와 함께 우리나라 전 연안에서 회수작업을 실행할 수 있는 작업 수심 200m급 잔존유 무인회수시스템(Remotely Operated Recovery System)의 요구사양을 선정하고 회수장비에 대한 기본설계를 수행하였다.

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Load-Adaptive Address Energy Recovery Technique for Plasma Display Panel

  • 이준영
    • 한국반도체및디스플레이장비학회:학술대회논문집
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    • 한국반도체및디스플레이장비학회 2005년도 춘계 학술대회
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    • pp.192-200
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    • 2005
  • A high speed address recovery technique for AC plasma display panel(PDP) is proposed. By removing the GND switching operation, the recovery speed can be increased and switching loss due to GND switch also becomes to be reduced. The proposed method is able to perform load-adaptive operation by controlling the voltage level of energy recovery capacitor, which prevents increasing inefficient power consumption caused by circuit loss during recovery operation. Thus, th e technique shows the minimum address power consumption according to various displayed images, different from prior methods operating in fixed mode regardless of images. Test results with 50' HD single- scan PDP(resolution : $1366{\times}768$) show that less than 350ns of recovery time is successfully accomplished and about $54\%$ of the maximum power consumption can be reduced, tracing minimum power consumption curves.

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지하대수층을 이용한 축열시스템의 설계 (I) : 등온해석 (Design of an Aquifer Thermal Energy Storage System (I) : Isothermal Analysis)

  • 송영길;이관수;이태희;김양현
    • 설비공학논문집
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    • 제5권2호
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    • pp.102-110
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    • 1993
  • An isothermal analysis was conducted to develop the design tool of an aquifer thermal energy storage system. Taejeon aquifer was chosen for the analysis, and the variation of FRE(Fluid Recovery Efficiency) with respect to the aquifer natural velocity and thermal load were investigated. The analysis results were compared with those of ATESSS(Aquifer Thermal Energy Storage System Simulator) and agreed within 2% of discrepancy. It is recommended, based on the result of this study, that the system may be suitable for a large volume of hot or chill thermal energy storage system, such as for district heating or cooling.

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A Highly Efficient AC-PDP Driver Featuring an Energy Recovery Function in Sustaining Mode Operation

  • Kang, Feel-Soon;Park, Sung-Jun;Kim, Cheul-U
    • KIEE International Transaction on Electrical Machinery and Energy Conversion Systems
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    • 제2B권3호
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    • pp.100-108
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    • 2002
  • A simple sustain driver employing an energy recovery function is proposed as a highly efficient driver of a plasma display panel. The proposed driver uses dual resonance in the sustaining mode operation: a main resonance between an inductor and an external capacitor to produce alternative pulses and a sub-resonance between an inductor and a panel to recover the energy consumption by the capacitive displacement current of the PDP. The operational principle and design procedure of the proposed circuit are presented with theoretical analysis. The operation of the proposed sustain driver is verified through simulation and experiments based on a 7.5-inch-diagonal panel with a 200 KHz operating frequency.

세라믹 볼을 이용한 판형열교환기 세정장치의 볼 회수율 측정 (The Measurements of Ball Recovery Rate for the Cleaning Apparatus in Plate Heat Exchanger Using Ceramic Ball)

  • 채희만;권정태;차동안;권오경
    • 동력기계공학회지
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    • 제18권1호
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    • pp.38-44
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    • 2014
  • The objectives of this study are to measure the ball recovery rate of cleaning apparatus for plate heat exchanger. Ceramic ball is used for plate heat exchanger cleaning. The main components of cleaning apparatus are comprised of ball collector, ball trap, ejector, pump and plate heat exchanger. The ball recovery rate are obtained with change in recovery time and velocity of water. The results show that the ball recovery rate is slightly increased with increase in the recovery time and the velocity of water over 0.4 m/s in the straight flow. In the case of reverse flow, the ball recovery rate more increased than straight flow. The maximum ball recovery rate of the straight flow and reverse flow reach 83.97% and 86.61%, respectively, when the velocity and cleaning time are 0.5 m/s and 15min.