• 한국연소학회지
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• 제20권2호
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• pp.1-13
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• 2015

Drying, which is the oldest and most energy-intensive process, is an essential process for treatment of solid product. The specific procedure to design and evaluate the dryers, which are a rotary kiln dryer and a flash dryer, in case of drying the high-moisture coal was described. From determination of size to the heat and mass balance in one-dimensional model were conducted to evaluate the performance of dryers. Heat consumption, inlet gas temperature and size of the dryers were compared between a rotary kiln dryer and a flash dryer. Further considerations to evaluate the reactor elaborately were also discussed. Performance simulation of dryers along with the design procedure described here will provide helpful basis for understanding the concept of reactor design.

• 한국연소학회지
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• 제20권2호
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• pp.14-27
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• 2015

Calcination, which represents thermal decomposition of $CaCO_3$, is the key reaction in a cement process. Some reactions including heating-up also take place simultaneously in the calcination reactors. Basic thermal performance and dimensions of the reactors in two cases, which are a rotary kiln wih a four-stage cyclone pre-heater and a simple single rotary kiln, were compared. To employ the heat transfer, mass transfer and reaction rate as well as calcination, one-dimensional modeling was conducted in each case. Some simplification about the reactors was described, however, the reliable Nusselt number and heat transfer coefficients on the reactors were used to make results reliable.

• 한국결정성장학회지
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• 제18권3호
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• pp.125-130
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• 2008

소형 전기로 및 이동장치가 있는 시뮬레이터를 사용하여 로타리킬른에서 생산되는 인공경량골재의 물성을 예측 할 수 있다면 대규모 로타리 킬른을 사용하여 인공경량골재 시제품 생산할 때 필요한 물자와 시간을 대폭 절감할 수 있다. 본 실험에서는 생산될 인공경량 골재의 물성을 정확히 예측할 수 있는 시뮬레이터를 제작하여 실제 로타리 킬른에서 생산된 골재의 물성과 비교함으로써 그 유용성을 검토하고자 하였다. 골재의 물성을 예측하기 위해서 8 mm 크기의 에코 인공경량 골재를 사용하였고 시뮬레이터의 분위기를 탄소를 이용해 조절하였다. 시뮬레이터와 로타리킬른에서 소성된 골재의 비중, 흡수율, 골재의 단면의 면적을 측정하고 비교하였다. 산화 분위기와 달리 환원분위기에서 소성된 시편은 탄소량이 증가할수록 비중이 증가하였으며 흡수율은 탄소 첨가량이 증가할수록 증가하는 경향을 보였다. 소성분위기는 환원 분위기 조성을 위해 탄소분말 0.7g을 첨가하였을 때 로라리 킬른과 가장 흡사한 분위기가 형성되는 것으로 판단되며, 두 골재의 물성 역시 비슷하였다.

• 자원리싸이클링
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• 제16권4호
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• pp.61-67
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• 2007

국내 석탄 발전소에서 발생하는 Fly ash를 이용한 경량 골재 제조는 환경 보호와 천연 골재 고갈을 동시에 해결할 수 있을 것으로 기대된다. 건축물의 초고층화는 골재의 경량화를 요구하고 있다. Dwight-Lloyd kiln은 운전이 쉽고 신뢰성이 높아 현재 유일하게 석탄회 소결 골재 상업 생산에 이용되고 있다. 본 고에서는 일본 Oomura 발전소의 Dwight-Lloyd kiln설비에 대해 자세히 설명하였고, 아울러 현재 개발 단계인 Circular grate kiln, Shaft kiln, Rotary kiln 설비에 대해서 개략적으로 소개하였다.

• 한국연소학회:학술대회논문집
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• 한국연소학회 2004년도 제29회 KOSCI SYMPOSIUM 논문집
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• pp.41-45
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• 2004

A dust injection system was developed for the lime calcining rotary kiln for the coke dust from the coke dry quenching(CDQ) facility to be used as a fuel. The CDQ dust was injected with the gaseous fuel through the hole in the burner. In order to prevent the spot heating large particles should be removed from dust and dust should be injected as fast as possible so that particle combustion lasts as long as possible without precipitation. This is especially necessary when dust is burned together with gaseous fuel because the gaseous fuel can not go so far and in addition dust combustion aggravates hot spot heating. In this research a rotation drum screen was used to remove particles with diameter larger than 4mm and dust injection speed was 40m/sec. And the burner was adjusted not to use swirl that hinders flame go far away. With these measures scale generation iside the kiln could be reduced to be negligible and in addition NOx emission could be reduced from 150ppm to 20ppm. The fuel reduction was about 85Mcal/T-lime.

• 시멘트 심포지엄
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• 1호
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• pp.64-68
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• 1973

One of the most difficult problems in cement rotary kiln operation must be ring and coating formation. In the Dopol kiln with the capacity of 1,500 t/d($4.4m\phi\times70mL$, meal rings have been accreted on transit zone and end of the kiln and

• 시멘트
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• 통권31호
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• pp.23-28
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• 1969

Rotary kiln의 원만한 열평형과 경제적 운전을 목적으로 kiln inlet zone의 내화연와를 이중으로 축로하기도 하는데 당공장에서 실시간 one-layer lining과 two-layer lining과의 논리적 열손실량 비교 및 실제측정 결과에 대해 기술하고자 한다.

• 한국연소학회지
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• 제19권3호
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• pp.18-25
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• 2014

Bottom ash from a coal-fired power plant is usually landfilled to a nearby site, which causes a growing environmental concern and increased operating costs. One way of recycling the bottom ash is to produce light-weight aggregate (LWA) using a rotary kiln. This study investigated the temperature profiles of raw LWA particles in a rotary kiln to identify the range of operating conditions appropriate for ideal bloating. For this purpose, a new simulation method was developed to integrate a 1-dimensional model for the bed of LWA particles and the computational fluid dynamics (CFD) for the fuel combustion and gas flow. The temperature of LWA particles was found very sensitive to the changes in the air preheating temperature and excess air ratio. Therefore, an accurate control of the operation parameters was essential to achieve the bloating of LWA particles without excessive sintering or melting.

• Carbon letters
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• 제3권4호
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• pp.205-209
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• 2002

In the reaction of gas-solid phases, the microwave energy plays a role as a catalyst, because it causes friction between adjacent molecules and enables an unique characteristics of interior heating of the materials. When the dipole gases are adsorbed inside of the pore of carbon materials, the gases are decomposed by the microwave energy and reacted with the carbon atoms. Using this principle, we could make the activated carbon from coconut shell within 20 minute, and this residence time for activation is about 1/16 of rotary kiln. The BET surface area of activated carbon made by microwave is about $1,100m^2/g$ similar to conventional method of rotary kiln. In this study, the power of microwave generator was 400~1000W, and the gas for activation was steam mainly.

• 한국연소학회지
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• 제9권3호
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• pp.1-9
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• 2004

This study is aimed to characterize the combustion behavior of solid fuel in the various types of the combustors: stoker, rotary kiln and fluidized bed type combustors. Three different types of reduced-scale combustors are introduced, and temperatures and flue gas compositions are measured for various fuel sizes, water contents, initial temperature, and air flow rates. In case of the rotary kiln combustor, effects of rotating speed of the combustor are also investigated. Mean carbon conversion time (MCCT) and flame propagation rate (FPR) are used for the quantitative analysis. It is revealed that the reaction rates of the fuel are significantly influenced by the fuel characteristics, type of the combustors and air flow rate. Major design parameters for each type of the combustors are summarized through the reduced-scaled model analysis.