• Title/Summary/Keyword: circulating fluidized bed

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Characteristics of Co-Combustion of Korean Anthracite with Bituminous Coal in a Circulating Fluidized Bed (순환유동층에서 유.무연탄 혼소 특성)

  • Lee, J.M.;Kim, J.S.;Lee, E.M.
    • Journal of the Korean Society of Combustion
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    • v.10 no.3
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    • pp.1-9
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    • 2005
  • The characteristics of co-combustion of Korean anthracite and bituminous coal was determined in a TGA and a lab-scale CFB reactor. The combustion reactivity of Korean anthracite (E = 51.2 kcal/mol) was much lower than that of bituminous coal (E = 14.5 kcal/mol). As the addition amount of the bituminous coal into the anthracite was increased, the reactivity of the anthracite was found to be improved. The effluent rate of the emission gases from the CFB reactor was not changed appreciably when each coal burned. As the bituminous coal was added, however, the effluent rate of the emissions was increased. The unburned carbon in fly ash from the CFB reactor was decreased with increasing the ratio of bituminous coal in co-combustion. But as the ratio of the bituminous coal was larger than 40 %, the combustion reactivity was not increased any more.

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Coal Gasification characteristics in an Internally Circulating Fluidized bed (내부순환유동층에서의 석탄 가스화 반응 특성)

  • 김용전;이종민;김상돈
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 1995.11a
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    • pp.15-18
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    • 1995
  • 내경 0.1 m, 높이 0.9 m 의 draft tube 를 갖는 직경 0.3 m, 높이 2.7 m 인 내부순환유동층가스화 반응기에서 생성가스분리대를 설치하여 가스화구역에서 생성된 생성가스를 분리하여 중열량가스를 얻었다. 석탄공급량 4.3 - 8.6 kg/hr, $O_2$/C 의 비 0.25 - 0.35, $H_2O$/C 의 비 0.75 - 1.35 의 조업변수 변화조건에서 생성가스의 조성과 발열량이 측정되었다. 반응 온도가 증가함에따라 H$_2$ 와 CO가 증가하고 $CO_2$$N_2$는 감소하여 생성가스 발열량이 10 - 11.5 MJ/㎥ 으로 증가하였다.

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Properties of Concrete Precast Pavers using Non-Cement Binders (무시멘트 결합재를 사용한 콘크리트 보도블록의 특성)

  • Lee, Won-Gyu;Jo, Eun-Seok;Lee, Sang-Soo;Song, Ha-Young
    • Proceedings of the Korean Institute of Building Construction Conference
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    • 2018.11a
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    • pp.35-36
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    • 2018
  • Korea has many problems due to the asphalt pavement or impermeable pavement. Many methods are being implemented to improve water circulation. Among them, permeable packaging materials are used. However, existing permeable packaging materials have a problem of causing efflorescence and clogging the pores. The pores of the permeable packing material are clogged and the permeability is lost. This leads to economic problems and product problems. The purpose of this study was to develop a block to prevent efflorescence.

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Development of Non-cement Material using Recycled Resources (유동층연소방식 석탄재를 활용한 무시멘트 결합재)

  • Mun, Kyoung-Ju;Lee, Min-Hi;Yoon, Seong-Jin
    • Proceedings of the Korean Institute of Building Construction Conference
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    • 2014.11a
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    • pp.156-157
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    • 2014
  • Inorganic binding material was made by recycled resource and its applicability as pile-filling material was examined. The result was that the material had same liquidity with the liquidity of OPC and high reactivity with site soil. According to dynamic/static loading tests by site test-construction, the inorganic binding material met both design bearing capacity and settlement. Since the inorganic binding material showed same or better performance than OPC, the utilization possibility of the inorganic binding material made of recycled resource as pile-filling material was verified.

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Properties of Non-cement Matrix Using Biomass Fly Ash (바이오매스 플라이애시를 활용한 무시멘트 경화체의 특성)

  • Kim, Dae-Yeon;Lee, Sang-Soo
    • Proceedings of the Korean Institute of Building Construction Conference
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    • 2020.06a
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    • pp.185-186
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    • 2020
  • This study In order to reduce the amount of cement that generates a large amount of carbon dioxide and attempts to find a recycling method to solve environmental problems by using biomass fly ash. Experiments were conducted according to replacement ratio of biomass fly ash based on GGBFS, The test items are flowability, air content, unit volume weight, water absorption, flexural strength and compressive strength. As a result of the experiment, as increased replacement ratio of biomass fly ash, the flowability and air content was increased. As increased replacement ratio, the density was decreased and water absorption was increased. The compressive strength tended to decrease as increased replacement ratio. The flexural strength tended to increased as increased replacement ratio.

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Air-staging Effect for NOx Reduction in Circulating Fluidized Bed Combustion of Domestic Unused Biomass (국내 미이용 바이오매스 순환유동층 연소에서 NOx 저감을 위한 air-staging 효과)

  • Yoon, Sang-Hee;Beak, Geon-Uk;Moon, Ji-Hong;Jo, Sung-Ho;Park, Sung-Jin;Kim, Jae-Young;Seo, Myung-Won;Yoon, Sang-Jun;Yoon, Sung-Min;Lee, Jae-Goo;Kim, Joo-Sik;Mun, Tae-Young
    • Korean Chemical Engineering Research
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    • v.59 no.1
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    • pp.127-137
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    • 2021
  • Air emission charge for nitrogen oxide as a precursor of fine dust has been introduced and implemented within the country from 2020. Therefore, the development of economical combustion technology for NOx reduction has got more needed urgently. This study investigated the air-staging effect as a way to reduce the NOx during combustion of domestic unused forest biomass, recently possible to secure REC (Renewable Energy Certification) as a substitute for overseas wood pellets in a 0.1 MWth circulating fluidized bed combustion test-rig. Operating conditions were comparison with and without air-staging, the supply position of tertiary air (6.4 m, 8.1 m, 9.4 m in the combustor) and variation of air-staging ratio (Primary air:Secondary air:Tertiary air=91%:9%:0%, 82%:9%:9%, 73%:9%:18%). NO and CO concentrations in flue gas, profiles of temperature and pressure at the height of the combustion, unburned carbon in sampled fly ash and combustion efficiency on operating conditions were evaluated. As notable results, NO concentration with air-staging application under tertiary air supply at 9.4 m in the combustor reduced 100.7 ppm compared to 148.8 ppm without air-staging while, CO concentration increased from 52.2 ppm without air-staging to 99.8 ppm with air-staging. However, among air-staging runs, when tertiary air supply amount at 6.4 m in the combustor increased by air-staging ratio (Primary air:Secondary air:Tertiary air=73%:9%:18%), NO and CO concentrations decreased the lowest 90.8 ppm and 66.1 ppm, respectively. Furthermore, combustion efficiency at this condition was improved to 99.3%, higher than that (98.3%) of run without air-staging.

A Basic Study on the Development of Backfill Material with Fly Ash and Bottom Ash of Circulating Fluid Bed Combustion (순환유동층보일러의 Fly Ash, Bottom Ash를 활용한 채움재 개발에 관한 기초연구)

  • Cho, Yong-Kwang;Lee, Yong-Mu;Nam, Seong-Young;Kim, Chun-Sik;Seo, Shin-Seok;Jo, Sung-Hyun;Lee, Hyoung-Woo;Ahn, Ji-Whan
    • Journal of the Korea Institute of Building Construction
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    • v.18 no.1
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    • pp.25-31
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    • 2018
  • In this study, the Controlled Low Strength Material (CLSM) was investigated to utilize the bottom ash and fly ash generated in the Circulating Fluidized Bed Combustor (CFBC). It was confirmed that the CFBC fly ash (CFBC-F) and CFBC bottom ash (CFBC-B) had an irregular particle shape through SEM measurement. According to the results of the hazard analysis, it was also confirmed that they were environmentally safe. In the case of mixing with CFBC-F, the unit quantity was increased. Regarding the rate of change of length, shrinkage in the range of -0.05~0.50% occurred in the air dry curing condition and expansion in the range of 0.1~0.6% in the sealed curing condition. Compressive strength was increased in the sealed curing condition compared to the air dry curing condition because there was enough moisture for hydration reaction in the long term. Therefore, the results of this study are likely be used as basic research data of mine filler materials.

A Study of Co-Combustion Characteristics of North Korean Anthracite and Bituminous Coal in 2 MWe CFBC Power Plant (2 MWe 순환유동층 발전 플랜트에서 유연탄과 북한 무연탄 혼소시험 특성 연구)

  • Han, Keun-hee;Hyun, Ju-soo;Choi, Won-kil;Lee, Jong-seop
    • Korean Chemical Engineering Research
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    • v.47 no.5
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    • pp.580-586
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    • 2009
  • In this study, co-combustion characteristics of Chinese bituminous coal and North Korean anthracite were investigated using a 2 MWe scale circulating fluidized bed power plant. At first, the combustion efficiency of bituminous coal of China and Australia as a function of excess air ratio and temperature were observed. The results showed that the combustion efficiency was influenced by particle size and volatile content of coal, the combustion efficiency of Chinese bituminous coal was over 99.5%. The unburned carbon particles from fly ash and bottom ash were a content 5~7% and 0.3%, respectively. The combustion efficiency with the mixture ratio 20% of bituminous coal and anthracite decreased over 5% because of the increase of entrained particles by a small average particle size of anthracite in the combustor. However, the outlet concentration of $SO_2$ and $NO_x$ was not changed remarkably. The concentrations of the typical air pollutants such as $NO_x$ and $SO_2$ were 200~250 ppm($O_2$ 6%), 100~320 ppm($O_2$ 6%) respectively. The outlet concentration of $NO_x$ was decreased to 30~65% with $NH_3$ supplying rate of 2~13 l/min in SCR process. The $SO_x$ removal efficiency was up to 70% by in-furnace desulfurization using limestone with Ca/S molar of approximately 6.5. With wet scrubbing using $Mg(OH)_2$ as absorbent, the $SO_x$ removal efficiency reached 100% under near pH 5.0 of scrubbing liquid.

Desulfurization Characteristics of Domestic Limestones through Simultaneous Calcination and Desulfurization Reaction (국내 석회석들의 소성 탈황 동시반응 특성)

  • Shin, Ji Hoon;Kim, Yea Ra;Kook, Jin Woo;Kwak, In Seop;Park, Kyoung-Il;Lee, Jong-Min;Lee, See Hoon
    • Applied Chemistry for Engineering
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    • v.26 no.5
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    • pp.557-562
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    • 2015
  • In order to analyze and compare the desulfurization characteristics of five different kinds of domestic limestons, a thermogravimetric analyzer (TGA) was used in this study. Calcium carbonate contents of the domestic limestone varied from 91 to 96 wt%. Experimental temperature and sulfur dioxide concentration of $850^{\circ}C$ and 2,750 ppm, respectively were selected to simulate commercial operation conditions. In this study, the calcination and desulfurization reaction of limestones were simultaneously occurred and investigated to simulate in-situ desulfurization reaction in commercial circulating fluidized bed combustors. In addition, desulfurization reactivities of limes having the average particle sizes of 37.5, 90.5, 159, 356 and $750{\mu}m$ were investigated. Desulfurization reactivities via simultaneous calcination and desulfurization reactions were 5-20% lower than those of using general desulfurization reactions.

Kinetic Analysis of Isothermal Pyrolysis of Korean Refuse Plastic Fuel for Application to Circulating Fluidized Bed Boiler (순환유동층 적용을 위한 국내 폐플라스틱 고형연료의 등온 열분해 분석)

  • Park, Kyoung-Il;Kim, Dong-Won;Lee, Tae-Hee;Lee, Jong-Min
    • Korean Chemical Engineering Research
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    • v.51 no.6
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    • pp.692-699
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    • 2013
  • In this study, isothermal (350, 375, 400, 425, 450, 500, $850^{\circ}C$) experiments were carried out using a custom-made thermobalance to analyze the thermal decomposition properties of refuse plastic fuel (RPF), which is to be used as a cofiring fuel with a sub-bituminous coal at commercial circulating fluidized bed (CFB) boiler in Korea. In isothermal pyrolysis results, no change in the reaction model was observed in the temperature range of $375{\sim}450^{\circ}C$ and it was revealed that the first order chemical reaction (F1) is the most suitable among 12 reaction models. The activation energy shows similar results irrespective of application of reaction model in that the activation energy was 39.44 kcal/mol and 36.96 kcal/mol when using Arrhenius equation and iso-conversional method ($0.5{\leq}X{\leq}0.9$) respectively. Mean-while, the devolatilization time ($t_{dev}$) according to particle size (d) of RPF could be expressed as $t_{dev}=10.38d^{2.88}$ at $850^{\circ}C$, operation temperature of CFB and for even distribution and oxidation of RPF in CFB boiler, we found that the relationship of average dispersion distance (x) and particle size was $x{\leq}1.58d^{1.44}$.