• Title/Summary/Keyword: Regenerative furnace

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A Study on the Compact Regenerative Burner Development (compact 축열 버너 개발 연구)

  • Dong, Sang-Keun;Lee, Eun-Kyoung;Yang, Jae-Bok
    • 한국연소학회:학술대회논문집
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    • 2004.06a
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    • pp.248-255
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    • 2004
  • For the compactness of regenerative combustion, self regenerative combustion and embedding regenerator inside furnace are proposed. The Self Regenerative burner system was developed to enhance thermal efficiency and Low Nox emission. In the twin regenerative system, two burner heads are generally used for preheating and exhausting combustion mode. But self regenerative burner system use only single nozzle body for regenerative combustion. Also two kind of regenerator, internal and external type, were designed to operate conveniently in both large and small furnace. According to test result, the self regenerative combustion system gives strong internal exhaust gas recirculation that reduce NOx emission significantly. NOx was measured as 50ppm(5% O2, 1290C furnace temperature). Also it is found that the fuel saving rate due to the self regenerative burner system reach to 30-40%. Thus it can be concluded that self regenerative mild combustion system appears to provide a reasonable regenerative burner for compactness and high performance as compared with conventional twin regenerative burner system. Also in the RT Application , compact twin regenerative burner was developed with the help of embedding regenerator inside furnace.

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The Development of User Oriented CFD Program for Optimum Design of a Regenerative Combustion Furnace (축열 연소시스템의 최적화 구현을 위한 사용자 전용 해석 프로그램의 개발)

  • Kang, K.G.;Ryou, H.S.;Ryou, S.Y.;Kim, H.J.;Noh, D.S.
    • Journal of the Korean Society for Heat Treatment
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    • v.16 no.3
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    • pp.148-158
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    • 2003
  • In this study, a user oriented CFD program for optimum design of a regenerative combustion furnace, REBURN was developed. For user's convenience, user friendly Graphic User Interface was made and the renumbering interface program was developed in order to directly input any generated mesh system from ICEM CFD/FEA. Also an automatic processing system for switching mode was developed. The program was verified through compahng with commercial CFD code about regenerative combustion furnace. Then, numerical simulation of real walking beam furnace used in real industry was performed and the parametric analysis was studied about the arrangement mode. As a results, the uniform temperature was appeared in the cross mode.

Energy Saving and Development of an Industrial Regenerative Oxy-Fuel Combustion Furnace for CO2 Capture (에너지 절약 및 이산화탄소 포집을 위한 축열식 순산소 연소로 개발)

  • Oh, Jeongseog;Noh, Dongsoon;Lee, Daegeun;Hong, Sungkook;Yang, Jebok;Ko, Changbok;Lee, Eunkyung
    • 한국연소학회:학술대회논문집
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    • 2013.06a
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    • pp.121-122
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    • 2013
  • In recent years, the usage of fossil fuels has caused problems of climate change and global warming. Because the combustion of fossil fuels is related to the production of greenhouse gases ($CO_2$, $CH_4$, etc.), new technology in the field of combustion is needed in order to handle the crisis of climate change and the global warming. As one of the efforts to reduce the emission of greenhouse gases, the concept of regenerative oxy-fuel combustion for energy efficiency and carbon capture was suggested, In the current study, the development of an industrial regenerative oxy-fuel combustion furnace was introduced, which has been being performed at Korea Institute of Energy Research (KIER).

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Flow and Heat Transfer along Burner Positions in Aluminium Pool Furnace (버너의 위치에 따른 알루미늄 용해로내의 유동 및 열전달)

  • Kim, Jin-Ho;Kang, Deok-Hong;Kim, Ki-Hong
    • Proceedings of the KSME Conference
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    • 2004.04a
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    • pp.1207-1212
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    • 2004
  • For the design of Aluminium pool furnace, position of burner and pool depth effects on flow and temperature field in Aluminium pool furnace are examined by the commercial computational code, CFD-ACE+. From the results, position of burner which is on the same face in side wall is better to distribute the flow field in Al furnace. That yields temperature to distribute more uniformly. And the burner position is on upper wall, fire frame reach pool surface. Customer must consider that, because it make Aluminium to oxidize.

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A NUMERICAL STUDY ON THE HEAT AND FLUID FLOW IN A REGENERATIVE OXY-FUEL COMBUSTION SYSTEM (순산소 연소용 축열시스템 내에서의 열 유동 수치해석)

  • Kang, K.;Hong, S.K.;Noh, D.S.;Ryou, H.S.
    • Journal of computational fluids engineering
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    • v.18 no.3
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    • pp.1-7
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    • 2013
  • A pure oxygen combustion technology is crucial in Carbon Capture and Storage (CCS) technology especially in capturing of $CO_2$, where CCS will reduce 9 $GtCO_2$ by 2050, which is 19% of the total $CO_2$ reduction amount. To make pure oxygen combustion feasible, a regenerative system is required to enhance the efficiency of pure oxygen combustion system. However, an existing air combustion technology is not directly applicable due to the absence of nitrogen that occupies the 78% of air. This study, therefore, investigates the heat and fluid flow in a regenerative system for pure oxygen combustion by using commercial CFD software, FLUENT. Our regenerative system is composed of aluminium packed spheres. The effect of the amount of packed spheres in regenerator and the effect of presence or absence of a bypass of exhaust gas are investigated. The more thermal mass in regenerator makes the steady-state time longer and temperature variation between heating and regenerating cycle smaller. In the case of absence of bypass, the regenerator saturates because of enthalpy imbalance between exhaust gas and oxygen. We find that 40% of exhaust gas is to be bypassed to prevent the saturation of regenerator.

Technical/Systemic Approach to Safety Assesment of Thermoprocessing Equipment Consuming LNG for Classification of Hazardous Area (LNG를 사용하는 설비에서의 폭발위험장소 적용 및 구분에 대한 제도/기술적 접근방안)

  • Choi, Sang-Won
    • Journal of the Korean Society of Safety
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    • v.26 no.5
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    • pp.33-40
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    • 2011
  • In the hazardous areas where explosive liquids, vapors and gases exist, electrical apparatus/equipment should have explosion-proof construction. The consuming of liquefied natural gas(LNG) has markedly increased in the industrial field, especially in aspect of some thermoprocessing equipment, boiler, dryer, furnace, annealer, kiln, regenerative thermal oxidizer(RTO) and so on. Because it has many merits, clean fuel, safety, no transportation/storage facility and so on. It is strongly recommend that the classification of hazards has to be decided to prevent and protect explosion which may occur in thermoprocessing equipment. In this paper, the operated thermoprocessing equipments in industrial area investigated and explosion risk assessment about LNG leakage from its facilities was performed through numerical calculation and computer simulation. Finally, we suggest the systemic/technical approach for safety assessments of thermoprocessing equipments consumed LNG fuel which are specially subjected to classification of hazardous area.