• Title/Summary/Keyword: Fluidized Bed Combustion Boiler

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Incineration of Waste Water Sludge and Coal In a Circulating Fluidized Bed Combustor (순환유동층에서 폐수슬러지와 석탄의 혼소 특성)

  • Bae, Dal-Hee;Shun, Do-Won;Park, Jae-Hyeon;Ryu, Ho-Jung;Park, Do-Hyun
    • 한국연소학회:학술대회논문집
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    • 2004.06a
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    • pp.165-172
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    • 2004
  • Co-incineration of coal and wastewater sludge was r;erfonn:rl in a O.lMWth bench scale circulating fluidized bed combustor(CFBC) Sludge was received from a wastewater treatment plant in a dye industrial complex in Busan. Metropolis. Moisture content of received sludge was 80%. Coal and sludge mixture was prepared with weight ratio of 90/10, 85/15 and 80/20. Co-combustion characteristics of the coal and sludge mixture demonstrated stable combustion conditions. Component analysis, incineration characteristics, boiler performance was measured before and after the test and application for commercial 59MWth CFBC boiler. The release of hazardous components such as $SO_2$ and Cl was suppressed by the presence of inherent minerals of Ca, Na, K in coal and sludge mixture. Pre-drying was not essential but it was recommended for the benefits of manageability of sludge.

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A Numerical Study of the Characteristics of Heat Transfer in External Heat Exchanger of CFB Boiler (순환유동층보일러 외부열교환기의 열전달 특성에 관한 수치해석적 연구)

  • Hwang, Moonkyeong;Kim, Jungrae
    • 한국연소학회:학술대회논문집
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    • 2014.11a
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    • pp.15-16
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    • 2014
  • With the increasing trend in CFB(Circulating Fluidized Bed) boiler scale, the EHE(External Heat Exchanger) must be adopted to the large-scale boilers to recover insufficient heat transfer surface. In this study, the numerical analysis model for EHE in commercial 300MWe CFB boiler was developed with the inclusion of mechanistic model, which enables the heat transfer prediction. Finally, the calculated absorbed heat and derived heat transfer coefficient are evaluated through the verification with experimental data.

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Circulating Fluidized Bed Combustion of Refuse Derived Fuel (폐기물 연료의 순환유동층 연소기술)

  • Shun Dowon;Bae Dal-Hee;Lee Seung-Yong;Jo Sung-Ho
    • Resources Recycling
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    • v.15 no.1 s.69
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    • pp.58-65
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    • 2006
  • A new technology for refused derive fuel(RDF) utilization in circulating fluidized bed is under development. The RDF is tested in a bench scale circulating fluidized bed(CFB) combustor and its burning characteristics were investigated and collected as design parameters. The combustions were controllable and the HCl emission which is most important toxic emission were below 150 ppm at the exit of the combustor. The differences between conventional coal homing circulating fluidized bed boiler and the exclusive RDF boiler were studied and commercial scale co-generation CFB for RDF was designed.

Circulating Fluidized Bed Combustion of Refuse Derived Fuel (폐기물 연료의 순환유동층 연소기술)

  • Shun, Do-Won;Bae, Dal-Hee;Lee, Seung-Yong;Jo, Sung-Ho
    • Proceedings of the Korean Institute of Resources Recycling Conference
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    • 2005.10a
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    • pp.124-134
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    • 2005
  • A new technology for refused derive fuel(RDF) utilization in circulating fluidized bed is under development. The RDF is tested in a bench scale circulating fluidized bed(CFB) combustor and it's burning characteristics were investigated and collected as design parameters. The combustions were controllable and the HCl emission which is most important toxic emission were below 150ppm out of combustor. The differences between conventional coal burning circulating fluidized bed boiler and the exclusive RDF boiler were studied and commercial scale co-generation RDF CFB's were designed.

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Allowable Amount of Bed Inventory in a 300 MW Class Circulating Fluidized Bed Boiler (300 MW 급 유동층보일러에서 적정 층 물질량 산정)

  • Kim, Woo-Yong;Yoo, Ho-seon
    • Plant Journal
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    • v.14 no.2
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    • pp.33-38
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    • 2018
  • The CFB boilers technology is facing a number of challenges. Among them, boiler tube erosion, sintering by bed inventory overheating and high self consumed service power are major ones. This study was conducted to obtain allowable bed inventory with the Yeosu Power Plant, a 300 MW class CFB boiler. For the test, bed pressure was reduced from design pressure of 4.5 KPa to 2.5 KPa by reducing bed inventory, at fixed turbine output, coal consumption rate and air flow. Consequently, reducing the lower bed inventory is effective to decrease bed temperature but excessive reducing might increase bed temperature due to lack of circulating fluidized materials. Also, in case of the Yeosu Plant boiler using subbituminous coal as its primary fuel, its bed temperature change is highly affected by not only the amount of bed inventory, but also the boiler capacity and coal contents.

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Development of 3MWth Circulating Fluidized Bed Biomass Gasifier (3MWth급 순환유동층 바이오매스 가스화공정 개발)

  • Lee, Jeungwoo;Song, Jaehun;Lee, Dongyoon;Choi, Youngtai;Yang, Won;Lee, Uendo
    • 한국연소학회:학술대회논문집
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    • 2012.04a
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    • pp.231-233
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    • 2012
  • Circulating Fluidized Bed (CFB) is a technically and economically proven technology for boiler systems and large CFB coal boilers are making inroads into the domestic power boiler market. For biomass gasification, it is also considered as a very promising technology for commercial. Due to the lack of experiences of a large scale CFB gasifier, however, any large scale CFB gasifiers are hard to in Korea in spite of fast-growing demand of domestic market. In this study, a 3 $MW_{th}$ CFB gasifier was developed for biomass gasification. The CFB gasifier consists of interconnected fast and bubbling fluidized bed reactors including unique features for in-situ tar removal. Various numerical and experimental approaches will be presented such as basic modeling works, investigation of hydrodynamics with a cold model, computational particle fluid dynamics and experiments in the 3 MWth gasifier.

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Self-Cementitious Hydration of Circulating Fluidized Bed Combustion Fly Ash

  • Lee, Seung-Heun;Kim, Guen-Su
    • Journal of the Korean Ceramic Society
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    • v.54 no.2
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    • pp.128-136
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    • 2017
  • Fly ash from a circulating fluidized bed combustion boiler (CFBC fly ash) is very different in mineralogical composition, chemical composition, and morphology from coal ash from traditional pulverized fuel firing because of many differences in their combustion processes. The main minerals of CFBC fly ash are lime and anhydrous gypsum; however, due to the fuel type, the strength development of CFBC fly ash is affected by minor components of active $SiO_2$ and $Al_2O_3$. The initial hydration product of the circulating fluidized bed combustion fly ash (B CFBC ash) using petro coke as a fuel is Portlandite which becomes gypsum after 7 days. Due to the structural features of the portlandite and gypsum, the self-cementitious strength of B CFBC ash was low. While the hydration products of the circulating fluidized bed combustion fly ash (A CFBC ash) using bituminous coal as a fuel were initially portlandite and ettringite, after 7 days the hydration products were gypsum and C-S-H. Due to the structural features of ettringite and C-S-H, A CFBC ash showed a certain degree of self-cementitious strength.