• 제목/요약/키워드: Land Fill Gas

검색결과 14건 처리시간 0.024초

30kW급 LFG 가스터빈 발전용 연료화 정제시스템 개발 (Development of Fuel Conditioning System for 30 kW-class LFG Gasturbine Power Generation)

  • 허광범;박정극;임상규;이정빈
    • 신재생에너지
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    • 제6권1호
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    • pp.29-37
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    • 2010
  • Biogas is a carbon neutral energy and consists of mostly methane and carbon dioxide, with smaller amounts of water vapor, and trace amounts of $H_2S$, Siloxane and other impurities. Hydrogen sulfide and Siloxane usually must be removed before the gas can be used for generation of electricity or heat. The goals of this project are to develope the Fuel conditioning system of Land Fill Gas for 30kW-Micro Gas Turbine co-generation system. The fuel conditioning system mainly consists of $H_2S$ removal system, Land Fill Gas compressor, Siloxane removal system and many filtering systems. The fuel requirement of 30kW MGT is at least 32% of $CH_4$, $H_2S$ (<30 ppm), Siloxane (<5ppb) and supply pressure (> 0.6 MPa) from LFG compressor. Main mechnical charateristics of Micro Gas Turbine system by using LFG have the specific performance; 1) high speed turbine speed (96,000 rpm) 2) very clean emmission NOx (<9 ppm) 3) high efficiency of energy conversion rate. This paper focuses on the development of design technology for LFG fuel conditioning system. The study also has the plan to replace the fuel of gas turbine and other distributed power systems. As the increase of Land Fill Gas (LFG), this system help to contribute to spread more New & Renewable Energy and the establishment of Renewable Portfolio Standards (RPS) for Korea.

쓰레기 매립지 MGT 발전 및 유리온실 설계기술개발 (Development of Land Fill Gas(LFG)-MGT Power Generation and Green House Design Technology)

  • 허광범;박정극;이정빈
    • 에너지공학
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    • 제20권1호
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    • pp.13-20
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    • 2011
  • 마이크로 가스터빈의 높은 연료 다양성은 광범위한 범위의 적용처에 적용할 수 있도록 설계되었다. 최근에는 가스터빈 발전시스템의 연료로서, 유기성폐기물의 소화가스와 쓰레기 매립지로부터 발생되는 바이오 가스에 대한 수요가 증가하고 있다. 우리는 매립지 가스를 이용하여 마이크로 가스터빈 열병합 발전시스템의 성능특성 및 운전 특성에 대한 영향을 연구하고 있다. 메탄과 이산화탄소를 동시에 회수하는 공정을 개발하여 현장 실증 플랜트 규모로 시험을 수행하였으며, 유리온실에 농작물의 이산화탄소 고농도 집적을 목적으로 철-킬레이트 화합물을 기본으로 하는 액상촉매를 이용하여 매립지 가스내에 있는 불순물을 저렴한 비용으로 제거하고자 한다. Fe-EDTA(철-킬레이트)를 이용한 내부순환 다판식 기포탑 반응기에 의하여 농축정제와 이산화탄소 제거가 매립지 가스의 최적화 연료화를 추진하였다. 매립지가스의 유량은 0.207 $m^3$/min이고 5.5 kg/$cm^2$의 압력으로 공급되며 메탄농도 70%, 이산화탄소 27%로 공급되도록 농축반응기를 설계하였고 황화수소 99% 제거를 목표로 한다. 유리온실은 마이크로 가스터빈 배가스와 온수를 이용하여 대기중의 이산화탄소 농도에서 1500 ppm의 농도범위로 공급되도록 설계되었다.

예연소실 점화 플러그의 화염 분출구 직경에 따른 매립지가스의 연소 특성 (Combustion Characteristics of Land Fill Gas according to the Diameter of the Flame outlet of the Pre-chamber Spark Plug)

  • 김권세;전영철;최두석
    • 융합정보논문지
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    • 제11권7호
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    • pp.111-117
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    • 2021
  • 본 연구는 LFG(Land Fill Gas)의 주성분인 메탄(CH4) 60%와 이산화탄소(CO2) 40%로 구성된 매립지가스를 활용하여 정적연소 환경에서 연소의 초기 불안정성을 해결할 수 있는 실험적인 연구결과를 제안하는 것이다. 실험조건은 공기과잉율 0.9~1.6, 초기연소를 위한 압축압력 3bar, 실험주변온도 25℃, 실험용 연료가스 메탄, 예연소실 화염 분출구 직경 2.5, 3.0, 3.5, 4.0, 4.5mm로 설정하였다. 실험결과 M3.0 모델에서 초기화염의 확산성이 매우 증가된 특성을 확인할 수 있으며, 이와 같은 증가의 특성은 공기 과잉률이 0.9, 1.0, 1.2에서 오리피스의 효과가 극도로 향상하게 되었다는 점을 알 수 있었다. 결과적으로, 본 실험을 통하여 M3.0으로 설계된 예연소실 화염 분출구 치수를 LFG에 적용할 경우 기존의 점화 플러그 특성 보다 부분적인 연소의 성능을 높일 수 있다는 점을 확인할 수 있었다.

매립지가스(LFG)로부터 합성가스 제조를 위한 개질반응 연구 (A Study on Reforming Reaction for Preparation of Synthesis Gas from Land-Fill Gas)

  • 조욱상;윤중섭;박성규;모용기;백영순
    • 한국수소및신에너지학회논문집
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    • 제25권6호
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    • pp.570-576
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    • 2014
  • LFG (Land-Fill Gas) includes components of $CH_4$, $CO_2$, $O_2$, $N_2$, and water. The preparation of synthesis gas from LFG as a DME (Dimethyl Ether) feedstock was studied by methane reforming of $CO_2$, $O_2$ and steam over NiO-MgO-$CeO_2$/$Al_2O_3$ catalyst. Our experiments were performed to investigate the effects of methane conversion and syngas ratio on the amount of LFG components over NiO-MgO-$CeO_2$/$Al_2O_3$ catalyst. Results were obtained through the activity reaction experiments at the temperature of $900^{\circ}C$ and GHSV of 4,000. The results were as following; it has generally shown that methane conversion rate increased with the increase of oxygen and carbon dioxide amounts. Highly methane conversion of 92~93% and syngas ratio of approximately 1.0 were obtained in the feed of gas composition flow-rate of 243ml/min of $CH_4$, 241ml/min of $CO_2$, 195ml/min of $O_2$, 48ml/min of $N_2$, and 360ml/min of water, respectively, under reactor pressure of 15 bar for 50 hrs of reaction time. Also, it was shown that catalyst deactivation by coke formation was reduced by excessively adding oxygen and steam as an oxidizer of the methane reforming.

지역냉방 열원의 수요모형에 관한 연구 (A Study on the Demand Modelling for District Cooling Energy Source)

  • 김진형;최병렬
    • 자원ㆍ환경경제연구
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    • 제11권4호
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    • pp.633-657
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    • 2002
  • This study presents a demand modelling for landfill gas, which is used as alternative energy source for district cooling business. By analyzing the cost minimizing behavior of producer facing with three alternative energy sources such as electricity, cooling heat water, and gas, a demand function for landfill gas is derived from the optimal operating time of gas fired production facility, and estimated using unpublished data, which are associated with Seoul city's development plan for Sang-am area. The estimation results repeals that Seoul City could supply the land-fill gas of 13.76 million cubic meters each year at the price of about 16 won per cubic meters. However, if the investment costs associated with installation of gas collecting facilities are treated as sunk costs, annual amount of gas supplied is expected to increase to 14.22 million cubic meters at a lower unit price of 14.76 won.

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충청북도 민간 산업체에 대한 온실가스 인벤토리 구축 및 감축기술 분석 (Construction of Greenhouse Gas Inventory of Private Industry of Chungcheongbuk-do and Analysis of Greenhouse Gas Mitigation Technology)

  • 임수민;안주영;정초시;박정훈
    • 한국기후변화학회지
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    • 제8권1호
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    • pp.57-62
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    • 2017
  • Greenhouse gas (GHG) emissions of private industry of Chungcheongbuk-do were estimated. GHG emissions were classified by industry and GHG emissions ratio of each industry of Chungcheongbuk-do was found. Characteristics of GHG emissions of Chungcheongbuk-do and GHG mitigation technology were analyzed. To calculate GHG emissions, equations proposed through GHG emissions calculation guidelines published by Korean Energy Agency in 2009 were used. As a result, GHG emissions ratio of cement, semiconductor, paper and petrochemical industry was about 73%, 16%, 5%, and 2% respectively. GHG mitigation technologies of cement, semiconductor and waste were investigated. For cement, amine technology, for semiconductor, scrubber system and for waste, land fill gas utilization were analyzed.

연료(燃料) 과농(過濃)/희박(稀薄) 조절(調節)의 촉매연소(觸媒燃燒)에 의한 Fuel-Nox 저감(低減) 기술(技術) (Reducing technology of fuel-NOx generation using fuel-rich/-lean catalytic combustion)

  • 강성규;이승재;유인수;신현동;한헌식
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2006년도 제32회 KOSCO SYMPOSIUM 논문집
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    • pp.55-62
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    • 2006
  • A two-step fuel-rich/fuel-lean catalytic combustion seems to be one of the most effective methods to control simultaneously the NO generation and the hydrocarbon (HC) conversion from fuel-bound nitrogen. By controlling equivalent air ratio for maintaining fuel-rich and fuel-lean condition over each catalytic layer, space velocity, inlet temperature, and catalyst component, the HCand ammonia conversion efficiency higher than 95% could be achieved, with ammonia conversion to NO remaining below 5%. The experimental results wouldbe applied to the combustion of land fill gas and to gasified refuse-derived fuels as a method of minimizing NO generation.

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도시 환경용량평가에 관한 연구 -청주시를 사례로- (A Study on the Environmental Carrying Capacity Assessment of Chongju City)

  • 임재호;이종호
    • 환경영향평가
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    • 제11권1호
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    • pp.25-36
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    • 2002
  • The purpose of this study is to assess the environmental carrying capacity of Chongju City for the environmental management and the urban growth management. The urban environmental carrying capacity assessment of the city by the index of ecological footprint(EF), shows that the ecosystem of the city has been overloaded and most of the deficiencies has come from outside of the city. The EF index, the area of land per capita required for production and consumption in the city, was 1.731 ha per capita in 1989 and 1.901 ha per capita in 1999. On the other side, the ecologically productive land is 0.0175 ha per capita. It means that every citizen owes 1.88 ha per capita to the ecosystem in 1999. The land consumption of the city has increased by 0.1705 ha per capita during the last 10 years. The capacity of infrastructure and the service supply estimated by the Onishi model does not exceed the demand of the city in 1999. But the rapidly increasing population and fast urban growth need the expansion of the capacity. The water supply capacity of the city appears to be sufficient in 1999, but the water supply demand will increase in the future. The capacity of sewage treatment facilities seems to be sufficient, but the higher level of sewage treatment facilities should be adopted for the improvement of water quality as the generation of sewage will increase and its characteristics will also make the wastewater treatment difficult. Due to the decrease of solid waste generated, the land fill capacity for solid waste disposal is not insufficient at present, but the capacity will be saturated in the near future. Therefore, the scientific management system of solid wastes should be introduced. The air quality of the city meets both the national air quality standard and WHO recommendation standard, but the strong regulation and control of automobile emission gas such as CO, $CO_2$, NOx and HC is required for clean air.

매립지가스(LFG)로부터 합성가스 제조시 반응조건에 따른 수율에 미치는 연구 (A Effect of Reaction Conditions on Syngas Yield for the Preparation of Syngas from Landfill Gas)

  • 조욱상;최경돈;백영순
    • 한국수소및신에너지학회논문집
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    • 제26권5호
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    • pp.477-483
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    • 2015
  • LFG (Land-Fill Gas) includes components of $CH_4$, $CO_2$, $O_2$, $N_2$, and water. The preparation of synthesis gas from LFG as a DME (Dimethyl Ether) feedstock was studied by methane reforming of $CO_2$, $O_2$ and steam over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Our experiments were performed to investigate the effects of methane conversion and syngas yield on the amount of LFG components over $NiO-MgO-CeO_2/Al_2O_3$ catalyst. Results were obtained through the methan reforming experiments at the temperature of $900^{\circ}C$ and GHSV of 8,800. The results were as following; it has generally shown that syngas yield increase with the increase of oxygen and steam amounts and then decrease. Highly methane conversion of above 98% and syngas yield of approximately 60% were obtained in the feed of gas composition flow-rate of 243ml/min of $CH_4$, 241ml/min of $CO_2$, 195ml/min of $O_2$, 48ml/min of $N_2$, and 450ml/min of steam, respectively, under reactor pressure of 1 bar for 200 hrs of reaction time. Also, it was shown that catalyst deactivation by coke formation was reduced by excessively adding oxygen and steam as an oxidizer of the methane reforming.