• Title/Summary/Keyword: 열 복사

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고온과 닭의 생산성

  • 이상진
    • KOREAN POULTRY JOURNAL
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    • v.17 no.7 s.189
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    • pp.104-109
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    • 1985
  • 고온이 닭의 생산성에 미치는 영향은 매우 크다. 따라서 여름철에는 환기를 충분히 시키고 단열재를 사용하거나 물을 뿌려 복사열을 막고 계사내에 직사광선이 비치지 못하게 해야 한다.

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Effect of Flame Radiative Heat Transfer in Horizontal-Type HRSG with Duct Burner (덕트 버너 추가에 따른 수직형 HRSG 내 화염 복사 열전달의 영향에 관한 연구)

  • Kim, Daehee;Kim, Seungjin;Choi, Sangmin;Lee, Bong Jae;Kim, Jinil
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.37 no.2
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    • pp.197-204
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    • 2013
  • A method was developed for analyzing the radiation heat transfer from the duct burner flame to the heat exchanger in a heat recovery steam generator (HRSG) in order to supplement the existing thermal design process. The burner flame and the heat exchanger were considered to be imaginary planes, and the flame temperature, surface, and emissivity were simplified using an engineering approach. Three analysis cases in which the duct burner position and fuel were changed were considered. The calculated flame radiative heat transfer and local flux on the heating surface were compared with those of 3-atomic gas radiation and convection. In all analysis cases, heat transfer by 3-atomic gas radiation was very small. The ratio of the flame radiative heat transfer to the convection heat transfer on the heating surface was estimated to be as high as 8-41%. Moreover, the local heat flux on the heating surface centerline was dominated by flame radiative heat flux.

Temperature Prediction for the Wastewater Treatment Process using Heat Transfer Model (열전달 모델을 이용한 폐수처리공정의 온도 예측)

  • Rho, Seung-Baik
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.15 no.3
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    • pp.1795-1800
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    • 2014
  • The temperature change in the biologically activated sludge wastewater treatment process was predicted using the heat transfer model. All incoming and outgoing heats in wastewater treatment processes were considered. Incoming heats included the solar radiation heat, the heat from impeller mechanical energy, and the biochemical heat in the aeration process. Outgoing heats comprised the radiation heat from the waste itself, the heat of vaporization and surface aeration, the wind convection heat and the conduction heat between the surface and aerator. All heats were used as an input to the existing empirical heat transfer model. The heat transfer model of wastewater treatment processes is presented also. To test the validity of the heat transfer model, the operating conditions of the actual wastewater treatment plant were used. The temperatures were compared with the model temperatures. Model predictions were consistent within the $1.0^{\circ}C$.

Thermal Analysis of a Radial Heat Sink with Radiation and Natural Convection (복사 열전달을 고려한 자연대류 원형 히트싱크 열전달 해석)

  • Yu, Seung-Hwan;Jang, Dae-Seok;Lee, Kwan-Soo
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.36 no.4
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    • pp.385-390
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    • 2012
  • A radial heat sink, adopted to LED(light emitting diode) downlight, was optimized. Discrete transfer radiation model (DTRM) was used to calculate radiation heat transfer, and numerical model was verified with experimental results. The effects of number of fin, long fin length and middle fin length on overall thermal resistance and radiation heat transfer were analyzed. As the emissivity increased, thermal resistance decreased due to the increment of radiation heat transfer. The radial heat sink was optimized and optimum number of long fins is 19~28, optimum length of long fin is about half of radius of heat fink and optimum fin ratio is 0.4~0.7.

Overall Heat Transfer Coefficient Measurement of Covering Materials with Thermal Screens for Greenhouse using the Hot Box Method (핫박스를 이용한 온실 피복재 및 보온재의 조합에 따른 관류열전달계수 측정)

  • Diop, Souleymane;Lee, Jong-Won;Na, Wook-Ho;Lee, Hyun-Woo
    • Journal of The Korean Society of Agricultural Engineers
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    • v.54 no.5
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    • pp.1-7
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    • 2012
  • 본 연구의 목적은 국내에서 상용되고 있는 온실 피복재 및 보온재의 조합에 따른 관류열전달계수를 핫박스를 이용하여 평가하는 것이다. 온실용 일중 및 이중 피복재와 이중 보온재의 조합에 대하여 야간천공복사 차단여부에 따른 관류열전달계수를 핫박스를 이용하여 실외에서 측정하였다. 처리조건은 일중피복, 이중피복, 이중피복과 이중 마트보온재 및 이중피복과 이중 다겹보온재의 조합조건과 천공복사 유무에 따른 조건이며 총 8가지이다. 제작된 핫박스는 상시 변화하는 외부의 기상조건하에서도 내부온도를 설정된 온도로 일정하게 잘 유지할 수 있었다. 온실 피복재 및 보온재의 관류열전달계수를 측정하는 실내용 측정장치는 반드시 야간천공복사를 모의할 수 있는 측정장치가 되어야 할 것이다. 야간복사를 차단함으로서 온실의 열 손실을 줄여 보온효과를 얻을 수 있을 것으로 분석되었다. 모든 피복방식에 대해 야간복사 차단장치 유무에 관계없이 높은 풍속에서의 관류열전달계수가 낮은 풍속에서보다 더 큰 것으로 나타났다. 본 연구에서 사용된 측정기법을 사용하면 국내에서 생산되는 피복재 및 보온재의 관류열전달 특성을 정량적으로 비교할 수 있을 것으로 기대된다.

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$^{\circ}C$.

유압기기에 있어서의 각종 오염물의 영향과 대책

  • 이부형
    • Journal of the KSME
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    • v.20 no.2
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    • pp.141-144
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    • 1980
  • 유압장치를 사용함에 따라 발생하는 오염물의 순서에 따라 그에 대한 대책을 다음 (표 1)에 표 시한다. 열화, 오염 요인의 점검 항목으로서는 (1) 발생녹 (2) 수분함유량 (3) 스러지량 (4) 외부 로의 혼입 오염물 (5) 열의 발생 복사열 (6) 도료 (7) 필터 (8) 유압작 등유가 있다.

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Numerical Analysis of Characteristics of Cellular Counterflow Diffusion Flames near Radiative Extinction Limit (복사 열손실에 의한 소염근처에서 셀모양 대향류 확산화염의 특성에 대한 수치해석)

  • Lee, Su Ryong
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.38 no.6
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    • pp.493-500
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    • 2014
  • Nonlinear characteristics of cellular counterflow diffusion flame near the radiative extinction limit at large Damk$\ddot{o}$hler number are numerically investigated. Lewis number is assumed to be 0.5 and flame evolution is calculated by imposing an infinitesimal disturbance to a one-dimensional(1-D) steady state flame. The early stage of nonlinear development is very similar to that predicted in a linear stability analysis. The disturbance with the wavenumber of the fastest growing mode emerges and grows gradually. Eventual, an alternating pattern of reacting and quenching stripes is developed. The cellular flame temperature is higher than that of 1-D flame because of the gain of the total enthalpy. As the Damk$\ddot{o}$hler number is further increased, the shape of the cell becomes circular to increase the surface area per unit reacting volume. The cellular flames do not extinguish but survive even above the 1-D steady state extinction condition.