• 제목/요약/키워드: Biogas compression

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25BAR급 바이오가스 고압 압축공급시스템 상세설계 (Detailed Design for 25bar-class Biogas Compression Supplying System)

  • 허광범;박정극;윤은영;이정빈
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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    • pp.173.1-173.1
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    • 2011
  • The high fuel flexibility of gas turbine power system has boosted their use in a wide variety of applications. Recently, the demand for biogas generated from the digestion of organic wastes and sewage waste water as a fuel for gas turbines has increased. We investigated the performance of high pressure biogas compression system and operating conditions for supplying biogas. The total flow per minute of biogas from food waste water digestion tank is $54Nm^3$. The main type of biogas compression system is the reciprocating system and screw type system. The target of biogas mechanical data is the as belows; inlet pressure 0.045bar, supplying biogas temperature is $30{\sim}60^{\circ}C$, and final pressure is above the 25 bar. Also, inlet conditions of biogas consist of CH4 48.5%~83%, $H_2S$ Max. 500ppm, $NH_3$ Max. 1,500ppm and Siloxane 2.7~4.6ppm. The boosting Blower system raises a pressure from 0.045bar to 1bar before main compressor. The main system lay out of reciprocating consisits of compressor driver, filter, cooling system, blowdown vessel, control system and ESD(Emergency Shut Down) system. And an enclosure package needs to be installed for reducing noise up to 75dB. The system driver is the electronic motor of explosion proof type. Forthe compressor system reliable operation, the cleaning system something like particulate filter needs to be set up in the inlet of compressor and Coalescing Filter in the outlet of compressor. Particulate Filter has to be removed above $10{\mu}m$ size of the particles in biogas. The coalescing filter(Micofine Borosilicate Glass Fibers Filter treated phenol acid) also removes moisture and oil of above $0.3{\mu}m$ to be involved in high pressure biogas up to 90%~98%.

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초단열 압축스파크 점화개질기를 이용한 바이오 합성가스 생산 연구 (Research of Biofuel Syngas Production Using Superadiabatic Compression Spark Ignition Reformer)

  • 임문섭;전영남
    • 한국수소및신에너지학회논문집
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    • 제21권1호
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    • pp.42-49
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    • 2010
  • Increasing environmental concerns regarding the use of fossil fuels and global wanning have prompted researcher to investigate alternative fuels. The purpose of this study is to investigate the syngas production by biogas reforming using a compression spark ignition engine. The parametric screening studies were carried out according to the variations of oxygen enrichment rate, biogas $CO_2$ ratio, intake gas temperature, and engine revolution. When the oxygen enrichment rate and input gas temperature increased, hydrogen and carbon monoxide were increased. But the biogas $CO_2$ ratio and engine revolution increased, the syngas were reduced. For the reforming of methane 100% only, generation of hydrogen and carbon monoxide was 58% and 17%, respectively. However when the biogas $CO_2$ ratio was 40%, hydrogen and carbon monoxide concentration were about 20% each.

반응 메커니즘 기반의 수소 첨가 바이오가스 HCCI 엔진 성능 및 배출가스에 대한 수치 해석적 연구 (Numerical analysis on performances and emission characteristics of HCCI engine fueled with hydrogen added biogas)

  • 박정수
    • 한국산학기술학회논문지
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    • 제19권12호
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    • pp.41-46
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    • 2018
  • 본 연구에서는 바이오가스 기반 예혼합 압축착화(Homogeneous charged compression ignition, HCCI) 엔진에 수소를 첨가하였을 때, 연소실 내부 압력, 온도 배출가스에 미치는 영향에 대해 살펴보았다. 자세히는 수소 첨가량과 과다공기량(${\lambda}$) 변화에 따른 연소실 압력 온도, 그리고 생성물로서의 NO, $CO_2$ 배출 특성을 화학 반응 해석 프로그램을 사용하여 고찰하였다. 대상의 엔진은 2300cc 바이오가스 엔진 발전기로서 압축비 13:1, 발전량 15kW 급이다. 과급압은 1.2bar 고정 조건이며, rpm은 1800rpm의 정속 조건이다. 엔진 연소 방식은 예혼합 압축 착화를 모사하였다. 본 연구를 진행하기에 앞서 바이오가스의 주요 조성인 메탄의 연소 및 산화 메커니즘에 대한 선행 연구에 대한 고찰을 통하여 연소반응 메커니즘을 규명하기 위한 반응 메커니즘 연구 기술의 경향을 살펴보고, 본 연구에 적용 가능한 반응 메커니즘을 선정하여 해석을 진행하였다. 수소를 첨가할 때 NO는 증가하는 반면, $CO_2$등의 배출량은 감소하였고 실린더 내부 압력이 상승하며, 상승 구간이 진각 됨을 알 수 있었다. 또한, 희박영역에서 수소 첨가가 가연 한계를 증가시켰다.

5MW급 바이오 가스터빈용 전처리시스템 설계연구 (Design Study of Fuel Supply System for 5MW-class Bio Gasturbine by Using Food Waste Water)

  • 허광범;박정극;윤은영;이정빈
    • 신재생에너지
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    • 제7권2호
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    • pp.10-17
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    • 2011
  • Korea is the 11th largest energy consumption country and 96% of its total energy consumption depends on imports from overseas. Therefore it is a very important task to secure renewable energy sources which can reduce both the carbon-dioxide emission and dependency on overseas energy imports. Among the various renewable energy sources, organic wastes are important sources. In Korea, 113 million toe of methane is generated from organic wastes annually, but only 3.7% is effectively used for energy conversion. Thus, it is very important to make better use of organic wastes, especially for power generation. The goals of this project are to develope the fuel supplying system of Bio Gasturbine (GT) for 5MW-class co-generation system. The fuel supplying system mainly consists of $H_2S$ removal system, Bio Gas compression system, Siloxane removal system and moisture separating systems. The fuel requirement of 5MW-class GT is at around 60% of $CH_4$, $H_2S$ (<30 ppm), Siloxane(<10 mg/$nm^3$) and supply pressure (> 25 bar) from biogas compressor. Main mechnical charateristics of Bio Gasturbine system have the specific performance; 1) high speed turbine speed (12,840 rpm) 2) very clean emmission NOx (<50 ppm) 3) high efficiency of energy conversion rate. This paper focuses on the development of design technology for food waste biogas pretreatment system for 5MW-class biogas turbine. The study also has the plan to replace the fuel of gas turbine and other distributed power systems. As the increase of bioenergy, this system help to contribute to spread more New & Renewable Energy and the establishment of Renewable Portfolio Standards (RPS) for Korea.

고품질화 바이오가스 이용 기술지침 마련을 위한 연구(III): 도시가스 및 수송용 - 기술지침(안) 중심으로 (A Study on Establishment of Technical Guideline of the Installation and Operation for the Biogas Utilization of Transportation and City Gas: Design and Operation Guideline)

  • 문희성;권준화;박호연;전태완;신선경;이동진
    • 유기물자원화
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    • 제27권2호
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    • pp.67-73
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    • 2019
  • 본 연구에서는 유기성폐자원의 바이오가스 생산 및 이용을 최적화를 위해 현장시설의 정밀모니터링과 시설별 에너지수지를 분석하고, 현장문제 해결방안에 대해서 조사하여 전처리시설 및 발전기 등의 설계 및 운전 가이드라인을 제시하였다. 고품질화 정제설비 운영에 잦은 고장 및 효율 저하를 해결하기 위해서는 가스전처리가 필요하며, 탈황, 제습, 탈실록산, 분진 처리, 휘발성유기화합물 등의 처리공정이 있다. 이 공정들은 고품질화 공정에서도 제거되는 물질들이기에 가스 전처리에서는 정량적 가이드라인은 제시하지 않고, 정성적 가이드라인으로 처리공간에 운영하도록 제시하였다. 특히, 분진, 실록산 및 휘발성유기화합물 등은 가스 전처리에서 제거되지 않으면 고품질화 공정의 잦은 고장의 주원인이된다. 바이오가스 고품질화 공정에 대한 설계 운전 가이드라인은 전체 가스 발생량의 90 % 이상 이용, 2계열화, 여유율 10 % 이상 감안 등이 있으며, 품질기준[메탄함량(프로판 포함) 95 % 이상]을 제시함. 또한 균등한 바이오가스 유입을 위해 가스균등조 설치, 보조연료 균등투입 제어를 위한 열량자동조절장치 설치, 가스압축과정에서 다량 발생하는 수분 제거를 위한 고품질화 후단의 제습장치 설치, 겨울철 설비의 결빙 및 효율 저하 방지를 위한 보온설비 설치, 특히 멤브레인 설비는 실내 설치 등을 제시하였다.

축분을 이용한 바이오가스 엔진 개발 - 기초설계 및 성능분석 - (A Study on the Development of Bio-gas Engine Using Livestock Manure - Fundamental Design and Experimental Analysis on the Performance -)

  • 백이;김영중;강금춘;유영선;조기현
    • Journal of Biosystems Engineering
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    • 제30권6호통권113호
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    • pp.354-359
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    • 2005
  • This is a fundamental study to develop a bio-gas utilization technology using livestock manure. Especially, this study was carried out to develop an engine using bio-gas. A bio-gas engine was designed and manufactured by modification of a diesel engine of 3 cylinders powering 13.31 kW/2800 rpm, changing the fuel supplying system fit for bio-gas. The result showed that, when the Air/Fuel ratio was controlled with fixed spark timing, the power of biogas-fueled engine is about $10.6{\~}14.6\%$ lower then that of LNG-fueled engine because of low volumetric efficiency. The engine output and torque was $11.85{\~}13.3$ kW, $39.5{\~}40.8\;N{\cdot}m$, respectively at the engine speed of 2600 rpm. Bio-gas consumption rate was 260.20 g/kW/hr, 315.20 g/kW/hr in engine speed or 1000 rpm, 2800 rpm, respectively.