• Title/Summary/Keyword: 바이오 매스 가스화

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Techno-economic Analysis(TEA) on Hybrid Process for Hydrogen Production Combined with Biomass Gasification Using Oxygen Released from the Water Electrolysis Based on Renewable Energy (재생에너지기반 수전해 생산 수소와 바이오매스 가스화 하이브리드 공정의 기술 경제성 분석)

  • Park, Sungho;Ryu, JuYeol;Sohn, Geun
    • Journal of the Korean Institute of Gas
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    • v.24 no.5
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    • pp.65-73
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    • 2020
  • To reduce the hydrogen production cost through the utilizing the oxygen and improving the capacity factor of water electrolysis used to energy storage of renewable energy, the hybrid hydrogen production process which has dual operating concept of using the water electrolysis as energy storage and oxygen production process for biomass gasification was proposed. Moreover, Techno-economic analysis on this system was quantitatively performed.

Effect of equivalence ratio on operation of 3MWth circulating fluidized bed for biomass gasification (3MWth급 순환유동층 바이오매스 가스화기의 운전에서 Equivalence ratio 영향)

  • Park, Seongbum;Lee, Jeoungwoo;Song, Jaehun;Pak, Daewon
    • Journal of the Korean Applied Science and Technology
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    • v.34 no.1
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    • pp.58-65
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    • 2017
  • Fluidized bed gasification is technically and economically proven technology, which shows the high possibility of realization and commercialization. However, in Korea, development of FBG to the commercial scale for power generation and industry is mainly blocked by the fact that there is no experience of design, troubleshooting and operation of even pilot scale fluidized bed gasifier. In this study, a $3MW_{th}$ circulating fluidized bed(CFB) was newly developed for biomass gasification. The fluidized bed was mainly composed of circulating and bubbling fluidized reactors integrating in-situ tar removal step in the system. For cleaning of the tar and acid gas in the product gas, the sequential gas cleaning process comprised of a ceramic filter, rapid quencher and wet scrubber was adopted. Effect of equivalence ratio was investigated to find the optimal operating conditions for the $3MW_{th}$ integrated system of fluidized bed gasification.

Hydrogasification of mixture composed of plastics and biomass (플라스틱과 바이오매스 혼합물의 수소첨가가스화 반응 연구)

  • You, Seung-Han;Jang, Hyun-Tae;Cha, Wang-Seog
    • Proceedings of the KAIS Fall Conference
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    • 2011.12a
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    • pp.283-285
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    • 2011
  • 수소첨가 가스화반응 특성을 조사하기 위해 $800^{\circ}C$, 8 MPa에서 조업 가능한 회분식반응기를 이용하여 실험을 수행하였다. 실험에 사용한 플라스틱은 폴리에틸렌이었으며 바이오매스는 톱밥이었다. 반응기내 압력감소속도는 기상물 생성속도를 나타냄을 알 수 있었으며 이러한 결과는 반응시간에 따른 전환율 변화로부터 확인할 수 있었다. 기상물 생성량과 플라스틱-바이오매스 혼합물의 전환율은 플라스틱 함량비가 증가할수록 증가하였다.

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Development of Biomass Gasification System Using a Downdraft Gasifier (하향류식 가스화기를 이용한 바이오매스 가스화 시스템 개발)

  • Son, Young-Il;Yoon, Sang-Jun;Choi, Young-Chan;Kim, Yong-Ku;Ra, Ho-Won;Lee, Jae-Goo
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.11a
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    • pp.662-665
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    • 2007
  • Since biomass is given the status of "renewable resource" in contrast to "exhaustible resource" e.q., fossil fuels, it plays a significant role in the sustainable development in future. We installed a downdraft gasifier for power generation from biomass materials. The biomass raw materials were wood chips with a moisture content of 18-23 wt.%, supplied at 40-50kg/h. This paper describes on the optimum gasification air ratio that is defined as the ratio of the oxygen mole supplied into the gasifier to the oxygen mole required for complete combustion for producing syngas supplied into a gas engine. The results showed that, lower heating value of the syngas was 1200 $kcal/m^3$ $_N-dry$ and cold gas efficiency of the gasification system was 72% under optimum operating conditions.

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The effect on the components variation of syngas by changing temperature and steam addition in biomass gasification process (바이오매스 가스화 과정에서의 온도와 가습의 변화가 전환가스 조성에 미치는 영향)

  • Ahn, Seong-Yool;Choi, Gyung-Min;Kim, Duck-Jool
    • Proceedings of the KSME Conference
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    • 2007.05b
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    • pp.3429-3434
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    • 2007
  • An experimental study was carried out to investigate gasification process of wood sawdust in the I-dimensional downdraft fixed bed gasifier. The preheated air was used oxidizer and steam were used as a gasifying agent. The operating parameters, the supplied air temperature and steam were used. The oxidizer temperature was varied from 500K to 620K and vapor was added. The gasification process was monitored by measuring temperature at three position near the biomass using R-type thermocouples and the syngas composition was analyzed by gas chromatograph. The change of hydrogen and carbon monoxide, carbon dioxide, methane was observed. Overall, the volume fraction of hydrogen and methane were increased widely as increasing the oxidizer temperature and adding steam.

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The effect oxidizer temperature and steam addition on caloric value in biomass gasification process (공급공기의 온도 변화와 수증기가 바이오매스 가스화 과정에서 전환가스의 발열량에 미치는 영향)

  • Ahn, Seong-Yool;Mun, Cheol-Eon;Choi, Gyung-Min;Kim, Duck-Jool
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.06a
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    • pp.606-609
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    • 2007
  • An experimental study was carried out to investigate the heat value change by various conditions of wood sawdust gasification in the 1-dimensional downdraft flow fixed bed gasifier. The preheated air and steam were used as a gasifying agent. The components of syngas were influenced increasing residence time of supplied agent. The operating parameters, the supplied agent temperature and steam addition were used. The oxidizer temperature was varied from 500K to 620K. The gasification process was monitored by measuring temperature at three points near the biomass using R-type thermocouples and the syngas composition was analyzed by gas chromatograph. We get the sample gas at the end of gasifier. Finally, the amount of hydrogen and methane were increased widely as increasing the oxidizer temperature and adding steam.

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A Study on reforming product characteristics by gas phase secondary pyrolysis (기상2차 열분해에 의한 개질 생성물 특성에 관한 연구)

  • Son, Young-Il;Yoon, Sang-Jun;Choi, Young-Chan;Ra, Ho-Won;Lee, Jae-Goo
    • 한국신재생에너지학회:학술대회논문집
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    • 2008.05a
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    • pp.243-246
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    • 2008
  • 목질계 바이오매스 가스화 발전에 있어서는 가스화 가스중에 함유되어있는 타르를 가능한 한 가연성 가스로 전환하여 냉가스효율을 향상시키는 것 및 잔유하는 타르는 후단기기에 악영향을 초래할 우려가 있기 때문에 타르를 저감 제거하는 것이 바람직하다. 본 연구에서는 공기 수증기를 사용하여 타르개질 프로세스의 개선을 위해서 타르에서 가스성분으로의 전환에 관한 개질 실험을 실시하여 Wood chip 타르의 열분해 개질 생성물 거동에 대하여 검토하였다. Wood chip 열분해로 생성된 타르의 원소분석 및 $^1H$ NMR분석의 결과로 타르를 치환기를 가지지 않는 방향족, alkyl-기를 가지는 방향족, 산소 함유 방향족, 지방족의 4개로 분류하였다. 개질제에 의해 경질 타르, 중질 타르 모두 감소하였다. 개질 공기는 타르를 연소시키지만 그 속도는 가연성 가스와 경합하고 $900^{\circ}C$에서는 타르의 연소는 나타나지 않았다. alkyl-기를 가지는 방향족은 메탄과 치환기를 가지지 않는 방향족으로 전환되고, 치환기를 가지지 않는 방향족은 수소와 soot로 전환되고, 산소 함유 방향족은 일산화탄소와 치환기를 가지지 않는 방향족으로 전환되는 것을 알았다. 또한, 개질제에 의해alkyl-기를 가지는 방향족, 치환기를 가지지 않는 방향족, 산소 함유방향족 모두가 일산화탄소,이산화탄소로 전환되는 것을 알았다.

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Removal of tar and particulate from gasification process using pre-coating technology (바이오매스 가스화 공정의 생성가스 중 타르 및 입자 제거를 위한 pre-coating 기술 연구)

  • Kim, Joon-Yub;Choi, Byoung-Kwon;Jo, Young-Min;Kim, Sang-Bum
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.20 no.12
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    • pp.804-815
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    • 2019
  • Due to the depletion and environmental problems of fossil fuel, biomass has arisen as an alternative energy source. Biomass is a renewable and carbon-neutral source. However, it is moister and has lower energy density. Therefore, biomass needs thermal chemical conversion processes like gasification, and it does not only produce a flammable gas, called 'syngas', which consists of CO, H2, and CH4, but also some unwanted byproducts such as tars and some particulates. These contaminants are condensed and foul in pipelines, combustion chamber and turbine, causing a deterioration in efficiency. Thus this work attempted to find a method to remove tars and particles from syngas with a filter which adopts a pre-coating technology for preventing blockage of the filter medium. Hydrated limestone powder and activated carbon(wood char) powder were used as the pre-coat materials. The removal efficiency of the tars was 86 % and 80 % with activated carbon(wood char) coating and hydrated limestone coating, respectively.

Study on Design Factors of Methanol Synthesis Catalyst and Syngas Cleaning from Gasification of Municipal Solid Waste (도시폐기물 가스화공정에서 합성가스 세정 및 메탄을 합성촉매 설계인자에 관한 고찰)

  • 추수태;이계봉;유영돈;윤용승
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 2003.05a
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    • pp.633-638
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    • 2003
  • 현재, 각종 산업공정에서 발생하는 부생가스, 도시폐기물, 폐플라스틱, 바이오매스 등의 미활용 에너지원이나 석탄, 폐유 등을 가스화 혹은 열분해 하여 합성가스를 발생시켜 재활용하려는 연구가 활발히 진행하고 있다. 합성가스는 공업적으로 중요한 에너지원 및 화합물을 제조하는 가장 기초적인 반응가스인데, 합성가스를 제조하는 방법 중 가장 잘 알려진 천연가스 개질반응 이외에도 열분해/가스화 반응공정을 통해 제조되기도 한다.(중략)

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Life Cycle Greenhouse Gas Emission Assessment on Locally Generated Kenaf Residue Biomass Fuel in South Korea (EU RED-II 방법론을 적용한 국내 미이용 바이오매스 케나프 펠릿의 전과정 온실가스 배출량 산정)

  • Youn Il Kim;Sun Young Jung;Youngjae Jo;Sung Yoon;Byung Hwan Um
    • Korean Chemical Engineering Research
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    • v.61 no.2
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    • pp.258-264
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    • 2023
  • The greenhouse gas (GHG) emission assessment of kenaf pellet, produced from locally generated kenaf residues in South Korea, has been studied based on the EU RED-II methodology for calculating GHG impact of biomass fuels. Based on the production pathway of kenaf residue pellet and emission coefficients from EU JRC report, the life cycle GHG emission of kenaf residue pellet is assessed as 3.0 gCO2eq/MJpellet and the life cycle GHG emission of electricity generated from kenaf residue pellet is assessed as 11.9 gCO2eq/MJ when electrical efficiency of final conversion is 25%. The potential GHG emission reduction of electricity produced from kenaf pellet is 90.3% compared to the domestic electricity emission factor 42.8 kgCO2eq/MWh. Also, the electricity produced from kenaf pellet can reduce at least 59.6% of GHG emission compared to the electricity produced from imported wood pellets.