• Journal of Energy Engineering
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• v.21 no.1
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• pp.68-74
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• 2012

Sub-bituminous coals have been used increasingly in coal-fired power plants with a proportion of over 50% in the blend with bituminous coals. As a result, the unburned material in fly ash has increased and is causing problems in utilizing the fly ash as an additive for concrete production. In this study, analysis of fly ash obtained from a 500 MWe power plant was carried out and unburned material in the fly ash found to be soot. The coals used in the plant were analyzed with CPD model to investigate the sooting potential depending on the coal type and blending ratio.

• 한국신재생에너지학회:학술대회논문집
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• 2011.11a
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• pp.72-72
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• 2011

국내 및 세계의 천연가스 수요가 증가하고, 원유가 상승에 의한 천연가스의 지속적인 가격상승이 예측됨에 따라 천연가스의 99%를 수입에 의존하는 우리나라의 에너지 안보 확보 방안을 위한 기술개발이 필요하다. 국내에서 천연가스를 확보할 수 있는 현실적인 방법중의 하나는 석탄가스화를 통해 얻어진 합성가스를 이용하여 SNG(synthetic Natural Gas, 합성천연가스)를 제조하는 것이다. 본 연구에서는 다양한 석탄, 다양한 석탄 가스화기를 적용하는 경우에 대한 CASE별 공정해석을 수행하여 각 경우의 SNG 생산 특성을 파악하였다. 석탄의 종류는 역청탄, 아역청탄, 갈탄을 대상으로 하였으며, 역청탄을 사용하는 경우는 General Electric Energy(GEE), Shell Global Solutions(Shell), ConocoPhillips(CoP)사의 가스화기를, 아역청탄을 사용하는 경우는 KBR의 TRIG$^{TM}$, Siemens사의 SFG, Shell, CoP 가스화기를, 갈탄을 사용하는 경우는 Shell, Siemens 가스화기를 적용하였다. 사용한 석탄과 석탄가스화기에서 발생된 합성가스 조성은 NETL에서 발행된 보고서에 제시된 수치들을 활용하였다. 역청탄을 사용하고 CoP 가스화기를 적용한 경우, SNG 합성공정에 유입되는 유량이 100 Nm3/h 일 때, 생산되는 SNG의 조성은 $CH_4$ 96.26%, $H_2$ 1.49%, $CO_2$ 0.69%, CO 0.004% 이고 생산유량은 24 Nm3/h 였다. SNG 효율을 SNG 합성공정에 공급되는 합성가스 열량 대비 최종 생산되는 SNG의 열량을 기준으로 하고, 각 CASE 별 SNG 효율을 살펴보면, 역청탄을 대상으로 한 경우 GEE 74.05%, CoP 76.65%였다. 아역청탄을 대상으로 한 경우 TRIG 78.14%, Siemens 71.22%, CoP 75.72%였고, 갈탄을 대상으로 하는 경우 Shell 71.48%, Siemens 71.49%였다. 역청탄을 사용하는 경우는 CoP 가스화기를 대상으로 한 경우 SNG 효율 및 생산량이 가장 높았고, 아역청탄을 사용하는 경우는 TRIG 가스화기를 대상으로 한 경우의 SNG 효율 및 생산량이 높았다. 갈탄을 사용하는 경우는 Shell 가스화기와 Siemens 가스화기가 거의 비슷한 결과를 나타내었다. $$SNG\;efficiency({\eta})={\frac{Q_B}{Q_A}}={\frac{Q_{SNG}(kcal/h)}{Q_{Syngas}(kcal/h)}}{\times}100(%)$$.

• Plant Journal
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• v.18 no.1
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• pp.55-61
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• 2022

In this study, I analyzed the effect of slagging caused by blending bituminous coal and subbituminous coal while maintaining the generator output, combustion conditions, and ventilation conditions for 870MW thermal power plant designed with bituminous coal. Accordingly I proposed an acceptable method of blending coal method. the blending ratio of sub-bituminous coal was adjusted to 10%, 20%, 40%, 60%, 80%, etc. to confirm ultimate analysis, proximate analysis, ash fusion temperature change, slagging indices, etc. Proper blending coal conditions are blending with sub-bituminous coal at 40% or less, ratio of base component to acid component(B/A) is 0.4 or less or 1 or more, total alkali(TA) is 3.5 or less, fusion slagging index(Rfs) is 1,345℃ or more, and ash content is 13% or less in ultimate analysis, the ash content in proximate analysis is 15% or less, and the initial deformation temperature(IDT) should be at least 1,200℃ or more

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1992.11a
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• pp.113-114
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• 1992

• Journal of Conservation Science
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• v.29 no.4
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• pp.345-354
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• 2013

This study analyses geochemistrical, microscopic, mineralogical characteristics of coals which have been collected from in and out of the shipwreck No 1 of Mado island during underwater excavation in Taean. The result from mineralogical and geochemical analysis reveals that the specific gravity of the coals is $1.28g/cm^3$. Considering that coals contains 10% mineral of it and the specific gravity of the pure is $1.15g/cm^3$, it is believed that the collected coals would be lignite or biturminous coal. The X-ray diffraction analysis which displays the peak of $2{\theta}$ is 20~25C degree, proves that the collected coals would be categorised as low rank coal. The collected coals is composed of: 93%-94%(93.5%) of vitrinite maceral group, 5%-6%(5.5%) of exinite maceral group, and 1% of inertinite maceral group. In addition, the average of reflection rate is $R_{mean}$: 0.627 showing that it would be either high volatile bituminous C coal or sub-bituminous C coal. Such result confirms that the coal is sub-bituminous C or high volatile bituminous C coal in accordance with the U.S Bureau of Mine(USBM) classification system. The element analysis reveals that the coal is the coking coal which is grouped as the bituminous coal. Comparative analysis between the coals of Mado Shipwreck No 1 and domestic coals shows that the coals of Mado Shipwreck is similar to the bituminous coal used in the area of Janggi in Pohang city.

• Journal of Energy Engineering
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• v.23 no.2
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• pp.42-48
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• 2014

Soot and tar which were derived from combustion or pyrolysis processes in Puverized Coal(PC) furnace or boiler have been significantly dealing in a radiative heat transfer and an additional source of NOx. Furthermore, the increasing for the use of a coal with low caloric value gives rise to a lot of tar-soot yield and LOI in a recycled ash for using cement materials. So, the ash with higher tar-soot yield and LOI can not recycle due to decreased strength of concrete. In this study, tar-soot yields and flame structures were investigated using the LFR for a blending combustion with bituminous coal and sub-bituminous coal. Also, The investigation were conducted as each single coals and blending ratio. The coals are used in a doestic power plant. In the experimental results, sub-bituminous coal with high volatile contents shows longer soot cloud length than bituminous coal, but overall flame length was shorter than bituminous coal. Tar-soot yields of sub-bituminous coal is lower than those of bituminous coal. Combustion characteristics are different between single coal and blended coal. Therefore, finding an optimal coal blending ratio according to coal rank effects on tar-soot yields.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.33 no.11
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• pp.858-868
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• 2009

A numerical investigation has been carried out about the performance of a 500MW class tangentially coal-fired boiler, focusing on the optimization of separated overfire air (SOFA) position to reduce NOx emission. For this purpose, a comprehensive combination of NOx chemistry models has been employed in the numerical simulation of a particle-laden flow along with solid fuel combustion and heat and mass transfer. A reasonable agreement has been shown in baseline cases for predicted operational parameters compared with experimental data measured in the boiler. A further SOFA calculation has been made to obtain optimum elevation and position of SOFA port. Additionally, clarifying on the effect of SOFA on NOx emission has been carried out in the coal-fired boiler. As a result, this paper is valuable to provide an information about the optimum position of SOFA and the mechanism by which the SOFA would affect NOx emission.

• Applied Chemistry for Engineering
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• v.5 no.2
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• pp.337-344
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• 1994

Two coals which have a quite different properties were selected to compare the combustion characteristics in a cyclone combustor. The capacity of the combustion test rig is about 75kW and total volume is 5.7 liters. The pulverized sample coals are well burned from fuel rich(air ratio 0.4) to fuel lean(airs ratio 1.6). Two different property coals show quite different patterns of ash collection in slag pot, dust separator and combustion chamber. Combustion temperature of subbituminous coal is about $100^{\circ}C$ lower than bituminous coal at the entire region, and in case of bituminous coal, hot spot appeared at the lower part and axial line of the combustion chamber.

• Journal of Energy Engineering
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• v.6 no.2
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• pp.176-187
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• 1997

As a way to evaluate the performance of IGCC (Integrated Gasification Combined Cycle) processes, heating values of coal gas as well as plant efficiency were compared for different rank coals and coal feeding methods by employing the static process simulation technique. Performance of the process was compared with coal rank that was varied by three assorted bituminous coals and also by three subbituminous coals, in addition to the two types of feeding techniques, i.e., dry-feeding and slurry-feeding, that are utilized in entrained-bed coal gasifiers. For the verification of the simulation technique, simulated results were compared first with the actual pilot plant data published from Shell and Texaco. The simulation technique was, then, applied to other coals. Result from tests varying coal rank exhibits the trend of improving both heating content of the product gas and plant efficiency with increasing carbon content in coal. The effect of coal rank is more sensitive in slurry-feeding cases compared to the dry-feeding cases. In particular, considering notably lower values in gas heating value and plant efficiency calculated in the slurry-feeding case that uses a subbituminous coal, limited utilization of the slurry-feeding method for subbituminous coals can be expected. From the plant efficiency point of view, dry-feeding method resulted in higher simulated efficiency values by maximum 3% for subbituminous coals and ca. l% for bituminous coals.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1999.05a
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• pp.39-44
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• 1999

발전용 연료로 사용하는 석탄은 취급의 어려움과 가스 및 석유에 비해 품질이 낮은 단점이 있으나, 매장량이 풍부하고 가격이 저렴하여 발전용 연료로의 사용은 더욱 증대될 전망이다. 이에 따라 석탄의 안정적 수급 측면에서 구입원의 다양화가 예상되고 있으나, 현재 발전용 연료의 연소특성 평가는 주로 실험실적 기초 시험에 의존함에 따라 정확한 평가가 곤란한 실정이므로 시험연소로를 이용하여 각종 연소특성을 비교 평가하여 탄종별 최적 연소조건 규명과 적정 흔탄비에 대한 Data Base를 구축하고자 한다.(중략)