• Title/Summary/Keyword: 에너지 플랜트

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

  • Ko, Areum;Park, Sungho;Kim, Joon-Young;Cha, Jae-Min
    • Journal of Energy Engineering
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    • v.27 no.4
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    • pp.50-63
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    • 2018
  • The issue of global warming and environmental pollutant has become an international concern due to the widespread use of fossil fuels, and thus waste heat recovery technologies has become important to improve energy utilization. The global market of power generation system using industrial waste heat is rapidly growing at an average rate of 5% due to its advantage of increasing energy efficiency. In order to design an optimal waste heat recovery system, it is necessary to develop a program that offers economic evaluation of each power generating technology according to the heat source conditions. In this paper, the economic analysis module to calculate LCOE is developed and verified the reliability against NETL economic analysis results. As a result of the verification, the error rate is about 6 ~ 7%, which satisfy the accuracy for business feasibility evaluation. In order to enhance the reliability, the module was improved by applying the levelization method used by NETL. As a result of the verification of reliability, the error rate is less than 1% and the accuracy is improved.

Evaluation Study on the Effects of $NO_x$ Reduction Techniques on the Performance and the Emission Characteristics of Medium Size Gasification Combined Cycle Plant (중급 규모 가스화 복합발전 플랜트의 $NO_x$ 저감 방식이 성능 및 환경특성에 미치는 영향에 관한 평가 연구)

  • Lee, Chan;Seo, Je-Young
    • Journal of Energy Engineering
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    • v.10 no.4
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    • pp.363-369
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    • 2001
  • Process design and performance evaluation were made for medium-size gasification combined/cogeneration plant. Based on the designed plant process configuration, the effects of $NO_x$ reduction techniques on the $NO_x$ emission, the power output, the efficiency and the stability of plant are investigated by applying various $NO_x$ reduction methods such as unsaturated/saturated nitrogen injection and fuel saturation of gas turbine combustor. The $NO_x$ reduction by nitrogen injection is more remarkable than that by fuel saturation, and its effect can be more enhanced by using saturated nitrogen. In addition, the applications of $NO_x$ reduction techniques accompany the improvement of plant power output and efficiency with the decrease of $NO_x$ emission, while it can cause unstable gas turbine operation.

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Evaluation of the Heat Conduction Model of Concrete Ground on Which LN2 Non-Spreading Pool Forms (비확산 액체질소 풀이 형성된 콘크리트 판의 열전도 모델 평가)

  • KIM, MYUNGBAE;NGUYEN, LE-DUY;CHUNG, KYUNGYUL;HAN, YONGSHIK;CHO, SUNGHOON
    • Journal of Hydrogen and New Energy
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    • v.32 no.5
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    • pp.365-373
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    • 2021
  • In this study, evaporation of LN2 non-spreading pool on concrete plate was dealt with experimentally. The thermophysical properties of concrete, which is a composite material, were obtained by minimizing the difference between the numerical analysis results obtained from the assumed properties and the results from experiments. The thermal energy required for evaporation of the liquid pool is supplied from the concrete plate and the wall of the container. As a result of the measurement, the thermal energy flowing in from the wall was negligible compared to the one supplied from the concrete plate. It was found that the measured evaporation rate of the liquid pool by the heat energy supplied through the concrete plate agrees well with the PTC model except for the initial section of the experiment. The validity of the semi-infinite assumption and the one-dimensional assumption, which are the main conditions of the PTC model, was also verified through experiments. The evaporation rate model in the non-spreading pool discussed in this study can provide a basic frame for the one in the spreading pool, which is a meaningful result considering that the spreading pool is very realistic compared to the non-spreading pool.

A Study on the Evaluation of DCSG Steam Efficiency of Oil Sand Plants for Underground Resources Development (지하자원개발을 위한 오일샌드플랜트의 DCSG 증기생산효율 평가에 관한 연구)

  • Young Bae Kim;Kijin Jeong;Woohyun Jung;Seok Woo Chung
    • Journal of the Korean Society for Geothermal and Hydrothermal Energy
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    • v.18 no.4
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    • pp.12-21
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    • 2022
  • Steam assisted gravity drainage(SAGD) is a process that drills well in the underground oil sands layer, injects hightemperature steam, lowers the viscosity of buried bitumen, and recovers it to the ground. Recently, direct contact steam generator(DCSG) is being developed to maximize steam efficiency for SAGD process. The DCSG requires high technology to achieve pressurized combustion and steam generation in accordance with underground pressurized conditions. Therefore, it is necessary to develop a combustion technology that can control the heat load and exhaust gas composition. In this study, process analysis of high-pressurized DCSG was conducted to apply oxygen enrichment technology in which nitrogen of the air was partially removed for increasing steam production and reducing fuel consumption. As the process analysis conditions, methane as the fuel and normal air or oxygen enriched air as the oxidizing agent were applied to high-pressurized DCSG process model. A simple combustion reaction program was used to calculate the property variations for combustion temperature, steam ratio and residual heat in exhaust gas. As a major results, the steam production efficiency of DCSG using the pure oxygen was about 6% higher than that of the normal air due to the reducing nitrogen in the air. The results of this study will be used as operating data to test the demonstration device.

Performance Analysis of Adiabatic Reactor in Thermochemical Carbon Dioxide Methanation Process for Carbon Neutral Methane Production (탄소중립 메탄 생산을 위한 열화학적 이산화탄소 메탄화 공정의 단열 반응기 성능 분석)

  • JINWOO KIM;YOUNGDON YOO;MINHYE SEO;JONGMIN BAEK;SUHYUN KIM
    • Journal of Hydrogen and New Energy
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    • v.34 no.3
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    • pp.316-326
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    • 2023
  • Development of carbon-neutral fuel production technologies to solve climate change issues is progressing worldwide. Among them, methane can be produced through the synthesis of hydrogen produced by renewable energy and carbon dioxide captured through a CO2 methanation reaction, and the fuel produced in this way is called synthetic methane or e-methane. The CO2 methanation reaction can be conducted via biological or thermochemical methods. In this study, a 30 Nm3/h thermochemical CO2 methanation process consisting of an isothermal reactor and an adiabatic reactor was used. The CO2 conversion rate and methane concentration according to the temperature measurement results at the center and outside of the adiabatic reactor were analyzed. The gas flow into the adiabatic reactor was found to reach equilibrium after about 1.10 seconds or more by evaluating the residence time. Furthermore, experimental and analysis results were compared to evaluate performance of the reactor.