• Journal of the Korean Society of Combustion
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• v.8 no.2
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• pp.34-40
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• 2003

Analyses for concentration, surface phenomena, and crystal structure were performed to identify the causes of clinker formation in three type of pulverized coal fired boilers. Some clinkers had partially molten surface and more CaO and $Fe_2O_3$ as compared with fly ash, and the major crystalline phases identified in the clinker were mullite and quartz. Clinkers were formed in high temperature zone of the boiler according to the identification of mullite by XRD. Free $SiO_2$ in sand combined with K, Na and Ca in limestone served as a fluxing agent to form clinkers in a circulating bed boiler.

• 한국연소학회:학술대회논문집
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• 2012.04a
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• pp.227-229
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• 2012

Diversification of combustion fuel is the demands of the times and biomass is the most attractive option since it can contribute to the prevention of global warming at the same time. Due to the national renewable obligation, generally called Renewable Portfolio Standard (RPS), many power companies are considering direct combustion of biomass or co-firing with coal. In order to use biomass as a fuel, informations of its combustion characteristics and ash related problems should be investigated. In this study, combustion performance of biomass was assessed in a bubbling fluidized bed combustor, and ash characteristics of various biomass fuels were studied with standard test method.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1995.11a
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• pp.19-22
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• 1995

순환유동층 연소기술은 다양한 성상의 연료를 저공해 고효율로 연소할 수 있는 우수한 연소방식으로 재래의 기포유동층 연소방식에서 부터 고효율, 대용량으로 확장되어 발전 및 열병합, 소각, 또는 복합발전에 적용되는 차세대 연소기술이다 [1,2]. 국내에는 1980년 중반이후 현재까지 약 10여기의 보일러가 도입되었으며, 경제성 및 관리체계의 우수성을 인정받아 확대 보급될 전망이다.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1999.05a
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• pp.81-84
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• 1999

순환유동층 (Circulating Fluidized Bed : CFB) 은 기존의 기포유동층에 비하여 높은 유속에서 조업되는 반응기로, 고속의 기체와 크기가 작은 고체 입자간의 긴밀한 접촉을 통하여 비교적 대규모의 여러 가지 화학적, 물리적 작업을 수행하는 유동층기술의 한 분야이다. 순환유동층은 1940년부터 공업적으로 이용되기 시작하였으며 현재에는 가솔린의 제조, 석탄의 연소, 가스화 등에 널리 사용되고 있다.(중략)

• Journal of the KSME
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• v.21 no.3
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• pp.166-174
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• 1981

광물질(회분, 석회석 또는 모래) 입자의 "유동층" (fuidised bed)에 연료를 유입하여 연소시키는 소위 "유동층 연소" 기술은 최근 몇년동안 상당한 발전을 보이고 있다. 왜냐하면 유동층 연소는 특히 저발열량 연료 (저질탄, 쓰레기등)의 연소에 있어서 여러 가지 장점을 갖고 있기 때문이다. 저질탄의 연소에 있어서 이 유동층 연소 기술이 갖는 장점을 열거하면 다음과 같다. a) 회분성분이나 비활성(inert) 성분의 조성이 균일하지 않은 저질탄의 연소능력 b) 열전달 면에서 부식문제의 저하 c) 보통 미분연소때보다 입도가 커도 완전연소가 가능하므로 분탄제조비가 저렴 여기서는 이러한 장점을 가진 저질탄의 유동층 연소에 대해서, International Energy Agency에서 1978년 발행된 Combustion of low grade coal 보고서를 중심으로 살펴보기로 한다. 보고서를 중심으로 살펴보기로 한다.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1999.05a
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• pp.69-74
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• 1999

각종 산업체의 공정에서 혹은 석탄 혹은 석유를 사용하는 화력발전설비에서 다량 발생되는 질소산화물(NOx), 황산화물(SOx)의 배출규제가 점점 강화되어 감에 따라 배출량 절감이 절실히 요구된다. 기존의 배기가스 정화장치는 처리대상에 따라 다양한 방법들이 사용되는데 황산화물의 경우 습식, 반건식, 건식세정법에 의해, 질소산화물은 선택적 촉매환원법(Selective Catalytic Reduction)과 선택적 무촉매환원법(Selective Non Catalytic Reduction)이 널리 이용되고 있다.(중략)

• Asian Journal of Atmospheric Environment
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• v.5 no.3
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• pp.189-195
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• 2011

Korea-specific GHG emissions should be estimated correctly in order to ensure effective measurement of climate change variables. The use of country-specific data that reflects fuel and technology characteristics is needed for accurate GHG emissions estimation. Oxidation factors are used to convert existing data into equivalent GHG emissions, and changes in these oxidation factors are directly related to changes in emissions. As such, the oxidation factor is one of the most important variables in using country-specific data to determine GHG emissions. In this study, the oxidation factor of bituminous coal in large scale boilers was estimated using 4,527 data points sampled from eight large-scale boilers that had been using bituminous coal for two years. The average oxidation factor was determined to be 0.997, which is lower than the oxidation factor of 1 that is recommended by the IPCC G/L for large scale boilers when estimating national GHG emissions. However, an oxidation factor less than 1 is assumed for fluidized bed boilers, internal combustion engines, and other small-scale boilers. Accordingly, studies on oxidation factor estimation should be continued to allow for accurate estimation of GHG emissions.

• Bulletin of the Korean Chemical Society
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• v.35 no.6
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• pp.1613-1618
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• 2014

Perovskite-type oxides are promising oxygen carriers in producing oxygen-enriched $CO_2$ gas stream for oxyfuel combustion. In this study, a new series of $SrCo_{1-x}Fe_xO_{3-{\delta}}$ (x = 0.2, 0.4, 0.6, 0.8) was prepared and used to produce $O_2/CO_2$ mixture gas. The phase, crystal structure, and morphological properties of $SrCo_{1-x}Fe_xO_{3-{\delta}}$ were investigated through X-ray diffraction, specific surface area measurements, and environmental scanning electron microscopy. The oxygen desorption performance of $SrCo_{1-x}Fe_xO_{3-{\delta}}$ was studied in a fixed-bed reactor system. Results showed that the different x values of $SrCo_{1-x}Fe_xO_{3-{\delta}}$ have no obvious effects on crystalline structure. However, the oxygen desorption performance of $SrCo_{1-x}Fe_xO_{3-{\delta}}$ is improved by Co doping. Moreover, $SrCo_{0.8}Fe_{0.2}O_{3-{\delta}}$ synthesized via a new EDTA method has a larger BET surface area ($40.396m^2/g$), smaller particle size (48.3 nm), and better oxygen production performance compared with that synthesized through a liquid citrate method.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.36 no.8
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• pp.865-871
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• 2012

Because of the increasing cost of oil and natural gas, energy production technologies using coal, including synthetic natural gas (SNG) and integrated gasification combined cycle (IGCC), have attracted attention because of the relatively low cost of coal. During the early stage of a project, the developer or project owner has many options with regard to the selection of a gasifier. In particular, from the viewpoint of feasibility, the gasifier is a key factor in the economic evaluation. This study compares the technical aspects of gasifiers for a real SNG production project in an early stage. A fixed-bed slagging gasifier, wet-type entrained gasifier, and dry-type entrained gasifier, all of which have specific advantages, can be used for the SNG production project. Base on a comparison of the process descriptions and performances of each gasifier, this study presents a selection guideline for a gasifier for an SNG production project that will be beneficial to project developers and EPC (Engineering, Procurement, Construction) contractors.

• Resources Recycling
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• v.29 no.6
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• pp.41-47
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• 2020

This study was carried out to utilize the coal bottom ash generated in a circulating fluidized bed combustion boiler as a treatment agent for heavy metal ions, and experiments were conducted to remove heavy metal ions from the acid mine drainage. The batch experiments were conducted to investigate the influence of dosage of ash, initial concentration of solution on the removal capacity of heavy metal ions (Cu, Cd, Cr, Pb). The results of the experiment showed that the total removal capacity of heavy metals was 30.8 mg/L and 46.4 mg/g, respectively, under the condition that the concentration of coal ash was added as 15 g/L of heavy materials and 10 g/L of light materials. After that, a long-term column experiment was performed to determine the maximum removal capacity of heavy metal ions (Cu, Cd, Cr, Pb, As), and the removal capacity for each metal component was investigated. After approximately 60 days of operation, the maximum removal capacity of heavy metals was 23.6 mg/g at pH 9.25.