• 제목/요약/키워드: fixed-bed gasifier

검색결과 27건 처리시간 0.032초

공기의 온도와 수증기가 목재 톱밥의 가스화에 미치는 영향 (The effect of oxidizer temperature and steam addition on gasification in wood sawdust)

  • 안성율;최경민;김덕줄
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2007년도 제34회 KOSCO SYMPOSIUM 논문집
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    • pp.63-68
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    • 2007
  • An experimental study was carried out to investigate gasification process of wood sawdust in the 1-dimensional downdraft fixed bed gasifier. The preheated air which was used oxidizer and steam were used as a gasifying agent. The downdraft fixed bed gasifier obtains more amount of hydrogen and methane by increasing residence time of supplied air. 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. We get the sample gas at the end of gasifier and it was eonugh time to finishing the chemical reaction. Finally, the amount of hydrogen and methane were increased widely as increasing the oxidizer temperature and adding steam.

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5톤/일 고정층 가스화기를 이용한 바이오매스, RPF 가스화 특성 연구 (Gasification Characteristics of Biomass and RPF in a 5ton/day Fixed Bed Gasifier)

  • 윤상준;최영찬;이시훈;김재호;이재구
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2006년도 추계학술대회
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    • pp.75-78
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    • 2006
  • With the increasing environmental consideration and stricter regulations waste gasification is considered to be more attractive technology than conventional incineration for energy recovery as well as material recycling. The experiment for combustible waste was performed In the fixed bed gasifier to investigate the gasification behavior with the operating conditions in a 5ton/day fixed bed gasifier The experiments of operation with 10-50 hours were carried out to determine the effects of bed temperature and oxygen/waste rat io on the syngas composition, calorific value and carbon conversion. The calorific values of the produced syngas decreased with an Increase of bed temperature because combust ion reaet ion more act ively happened. The syngas composition of wood waste gasification is CO: 34.4%, $H_2: 10.7%,\;CH_4: 6.0%,\;CO_2: 48.9%$ and that of RPF is CO: 33.9%, $H_2: 26.1%,\;CH_4: 10.7%,\;CO_2: 29.2%$. The average calorific values of produced gas were about $1,933kcal/Nm^3,\;2,863kcal/Nm^3$, respectively

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2톤/일 고정층 가스화기를 이용한 폐목재의 에너지 전환 연구 (The Study of Energy Conversion in a 2 Ton/day Waste-wood Fixed Bed Gasifier)

  • 이시훈;손영일;고창복;최경빈;김재호
    • 공업화학
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    • 제20권4호
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    • pp.391-395
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    • 2009
  • 폐목재의 에너지 전환을 위하여 2톤/일 규모의 고정층 가스화기($0.9m{\times}2.4m$)를 제작하여 실험하였다. 고정층 가스화 설비는 3~5 cm의 목재칩을 이용하였으며 하부에는 회전식 스토커가 설치되어있다. 목재칩 연료 투입은 다단 나이프밸브 방식으로 되어 있으며 관성력 집진설비, 가스냉각용 열교환기, ID Fan 및 Cooling tower 등으로 구성되어져 있다. 가스화기는 $700{\sim}1000^{\circ}C$ 사이에서 조업하였으며 CO: 25~40 vol%, $H_2$: 7~12 vol%, $CH_4$: 2~4 vol%, $CO_2$: 12~24 vol%의 조성을 가지는 합성가스가 생성되었다. 합성가스 발열량은 $1100{\sim}1500kcal/Nm^3$으로 나타나 공업로의 적용이 가능하였다. 또한 합성가스의 가스 엔진을 통한 전력 생산도 가능하여 1~4 kW의 전력을 생산하였다.

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

  • 안성율;문철언;최경민;김덕줄
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2007년도 춘계학술대회
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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 Applying PID Control to a Downdraft Fixed Bed Gasifier using Wood Pellets

  • Park, Bu-Gae;Park, Seong-Mi;Park, Sung-Jun
    • 한국산업융합학회 논문집
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    • 제25권2_1호
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    • pp.149-159
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    • 2022
  • Biomass is material that is comprehensive of carbonaceous materials from plants, crops, animals, and algae. It has been used as one of heating fuel since the beginning the emergence of human beings. Since biomass is regarded as carbon-neutral energy source, it has recently been attracting attention as an energy source that can replace fossil fuels. The most widely applied field is distributed power generation, and a method of generating electric power by driving an internal combustion engine with syngas produced by gasifier is chosen. While the composition of the syngas produced in gasifiers changes depending on the air flowing into the reactor, commercialized gasifiers so far do not control the air flowing into the reactor. When the inner pressure in reactor increases, the air sucked into the reactor is reduced. That change of amount of air makes the composition of syngas varied. Those variations of composition of syngas cause the incomplete combustion hence the power output of engine drops, which is a critical weakness of the gasification technology. In this paper, to produce the uniformly composed syngas, PID control is applied. The result was shown when the amount of air into the reactor is supplied with the constant amount using PID control, the standard deviation of caloric values of syngas is around 2[%] of its average value. Meanwhile the gasifier without PID control has the standard deviation of caloric values is around 7[%]. Therefore, Adopting PID control to supply constant air to the gasifier is highly desirable.

Down-draft type 파일럿 가스화로에서의 톱밥 가스화 특성 (Sawdust gasification characterization in down-draft type pilot gasifier)

  • 민태진;길상인;윤진한;김우현;노선아
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2008년도 춘계학술대회 논문집
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    • pp.256-259
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    • 2008
  • The gasification of biomass, sawdust, was carried out in order to investigate gasification characteristics. The experiment was performed using a down-draft fixed bed gasifier to surpass tar components generation in the gasification process. In the experiments, we investigated synthetic gas composition by varying reaction temperature, steam/carbon ratio, and excess ratio (ER), respectively. Higher reaction temperature, $700^{\circ}C$ to $900^{\circ}C$, could obtain higher $H_2$ yield. However, we could not obtain any meaning data by varying S/C ratio. Using $O_2$-LNG burner in the top of the gasifier may surpass water-gas shift reaction by increasing $CO_2$ concentration from the LNG-$O_2$ combustion reaction.

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Comparative studies of gasification potential of agro-waste with wood and their characterization

  • Tripathi, Amarmani;Shukla, S.K.
    • Advances in Energy Research
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    • 제3권3호
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    • pp.181-194
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    • 2015
  • In this work, an experimental study of the gasification on wood was carried out in downdraft type fixed bed Gasifier attached with 10 kW duel fuel diesel engine. The main objective of the study was to use wood as the biomass fuel for downdraft Gasifier and to evaluate the operating parameter of gasifier unit to predict its performance in terms of gas yield and cold gas efficiency. The influence of different biomass on fuel consumption rate, gas yield and cold gas efficiency was studied. Composition of producer gas was also detected for measuring the lower heating value of producer gas to select the feed stock so that optimum performance in the existing gasifier unit can be achieved. Under the experimental conditions, Lower heating value, of producer gas, cold gas efficiency and gas yields, using wood as a feed stock, are $4.85MJ/m^3$, 46.57% and $0.519m^3/kg$.

석탄 및 폐기물로부터 합성가스 제조를 위한 가스화용융 Pilot Plant 운전특성 (Operation Characteristics of Gasification/Melting Pilot Plants for Synthesis Gas Production using Coal and Waste)

  • 정석우;윤용승;유영돈
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2005년도 춘계학술대회
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    • pp.561-564
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    • 2005
  • Gasification has been regarded as a very important technology to decrease environmental pollution and to obtain higher efficiency. The gasification process converts carbon containing feedstock into a synthesis gas, composed primarily of CO and $H_2$. And the synthesis gas can be used as a source for power generation or chemical material production. Through more than nine years, IAE developed and upgraded several gasification/melting pilot plant system, and obtained a good quality synthesis gas. This paper illustrates the gasification characteristics and operation results of two 3 ton/day synthesis gas production facilities. One is entrained-bed slagging type coal gasifier system which is normally operated in the temperature range of $1,400\~1,450^{\circ}C,\;8\~10$ bar pressure. And the other is fixed-bed type gasification/melting furnace system using MSW and industrial wastes as a feedstock.

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