• Title/Summary/Keyword: 복사튜브버너

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Heat Transfer and Combustion Characteristics and Performance of U type Radiation Tube Burner with fin (핀 부착 U형 복사튜브 버너의 열전달 및 연소성능 실험)

  • Lee, Hyun-Chan;You, Hyun-Seok;Lee, Joong-Seong
    • Proceedings of the KSME Conference
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    • 2001.06d
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    • pp.516-521
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    • 2001
  • Present study deals with combustion characteristics and performance of U type radiation tube burner with fin which combustion capacity is 30,000kcal/hr and the maximum capacity of supply fuel is $30Nm^{3}/hr$. Temperature difference of radiation tube is about $173^{\circ}C$ at 25% capacity and this show relatively small temperature difference for convenient type. Thermal efficiency is satisfactory as $72{\sim}81%$. Also, radiative efficiency of radiation tube is $52{\sim}73%$. The efficiency of heat exchanger is $27{\sim}37%$. Therefore, radiative efficiency is improved to $1{\sim}10%$ after installing fin.

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Combustion Characteristics and Performance of U type Radiation Tube Burner (U형 복사튜브 버너 연소특성 및 성능실험)

  • Lee, Hyun-Chan;You, Hyun-Seok;Lee, Joong-Seong
    • Proceedings of the KSME Conference
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    • 2000.11b
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    • pp.710-714
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    • 2000
  • Present study deals with combustion characteristics and performance of U type radiation tube burner which combustion capacity is 30,000kcal/he and the maximum capacity of supply fuel is $3.0N m^3/hr$. Temperature range of radiation tube is maximum $170^{\circ}C$ and minimum $150^{\circ}C$ and this displays relatively small temperature range. And thermal efficiency is satisfactory as $75{\sim}80%$. Also, radiative efficiency of radiation tube is $52{\sim}63%$.

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Design and Performance Estimation of Heat Regenerator for Small-scale Regenerative Radiant Tube Burner (열처리로용 소형 축열식 복사관 버너의 축열기 설계 기술평가)

  • Cho H. C.;Cho K. W.;Lee Y. K.
    • Journal of Energy Engineering
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    • v.13 no.4
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    • pp.291-295
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    • 2004
  • Heat regenerator attached in small-scale regenerative radiant tube burner was designed using the theoretical computation code and was confirmed the performance of waste heat recovery ratio. From the computation, when ceramic ball of 4-5kg was used, temperature efficiency and available waste heat recovery ratio were predicted 80% and 70%, respectively. Similar efficiencies were obtained from the experiments using LPG. However, since exhaust gas temperature entered into regenerator was below 850$^{\circ}C$ which was moth lower than that we expected. air preheating temperature was lowered below 800$^{\circ}C$.

Design and Estimation of Performance of Heat Regenerator for Small-scale Regenerative Radiant Tube Burner (소형 축열식 복사관 버너시스템용 축열기 설계 및 성능평가)

  • 조한창;조길원;이용국
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 2004.05a
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    • pp.171-176
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    • 2004
  • Heat regenerator attached in small-scale regenerative radiant tube burner was designed using the theoretical computation code and was confirmed the performance of waste heat recovery ratio. From the computation, when ceramic ball of 4-5kg was used, temperature efficiency and available waste heat recovery ratio were predicted 80% and 70%, respectively. Similar efficiencies were obtained from the experiments using LPG. However, since exhaust gas temperature entered into regenerator was below 85$0^{\circ}C$ which was much lower than that we expected, preheat air temperature was lowered below 80$0^{\circ}C$.

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Effect of Process Gas and Burner Gas Temperature on Reaction and Thermal Deformation Characteristics in a Steam Reformer (증기 개질기의 반응 및 열변형 특성에 미치는 공정가스와 버너가스 온도의 영향)

  • Han, Jun Hee;Kim, Ji Yoon;Lee, Jung Hee;Lee, Seong Hyuk
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.17 no.9
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    • pp.126-132
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    • 2016
  • This study numerically investigates the characteristics of chemical reactions and thermal deformation in a steam reformer. These phenomena are significantly affected by the high-temperature burner gas and the process gas conditions. Because the high temperature of the burner gas ranges from 800 to 1000 K, the reformer tubes undergo substantial thermal deformation, eventually resulting in structural failure. Thus, it is necessary to understand the characteristics of the reaction and thermal deformation under the operating conditions to evaluate the reformer tubes for sustainable, stable operation. Extensive numerical simulations were carried out using commercial CFD code (ANSYS FLUENT/MECHANICA Ver. 13.0) while considering three-dimensional turbulent flows and combined heat transfer including conduction, convection, and radiation. Structural analysis considering conjugated heat transfer between solid tubes and fluid flows was conducted using the Fluid-Solid Interaction (FSI) method. The results show that when the injection temperature of the process gas and burner gas decreased, the hydrogen production rate decreased significantly, and thermal deformation decreased by at least 15 to 20%.