• 제목/요약/키워드: Bed temperature

검색결과 1,039건 처리시간 0.029초

저온기 딸기 고설 수경재배시 온실기온에 따른 배지내 온도강하 모델 개발 (Modeling of Medium Temperature Drops of the Elevated-bench Hydroponics for Strawberry Cultivation during Low Temperature Season)

  • 박재완;하유신;김기동;박대흠;이기명;전하준;권순구;최원식;정성원
    • 생물환경조절학회지
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    • 제19권3호
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    • pp.123-129
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    • 2010
  • 본 연구는 저온기 딸기 고설 수경재배 방식의 배지 내 온도 관리를 위한 기초자료를 얻기 위하여 베드 2종류(플랜트형, V형), 배지 4종류(왕겨, 펄라이트, 왕겨 80% + 피트모스20%, 휠라이트80% + 피트모스20%), 멀칭 2종류(멀칭무, 멀칭유)의 처리구별로 온실기온 4수준(1.5, 3.2, 5.0, $6.7^{\circ}C$)에 따른 배지 내 온도의 변화를 측정하였다. 그 결과, 베드의 온도강하는 V형 베드가 플랜트형 베드보다 평균 $1.2{\sim}20^{\circ}C$ 느리게 나타났으며, V형 베드의 보온 효과가 크게 나타났다. 배지의 종류별로는 왕겨 80%의 배지보다 펄라이트 80%의 배지에서 멀칭의 유무에 관계없이 배지온 강하가 약 $7^{\circ}C$ 느리게 나타났다. 멀칭유무별로는 멀칭한 경우에서 온도강하가 느리게 나타나 멀칭을 하는 것이 배지온 유지에 유리하였다. 보온효과가 큰 V형 베드, 펄라이트80% + 피트모스20% 배지, 멀칭한 경우의 배지온 강하 모텔은 f(x) = -0.2656 + 0.1345x로 나타났으며, 개발된 모델을 이용하면 저온기에서 야간의 온실 내 기온에 따른 배지내의 온도강하를 예측할 수 있을 것으로 판단되었다.

유동층을 이용한 열처리부품의 세정 시스템 설계 및 개발 (I) -유동층 이용 세정 실험장치 설계, 개발 및 실험 - (Design and Development of Fluidized Bed Cleaning System for on Heat Treatment Parts (I) - Design and Development the Experimental Fluidized Bed Cleaner and Experiments on its Cleaning Efficiency -)

  • 김찬수;김기대
    • Journal of Biosystems Engineering
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    • 제31권4호
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    • pp.376-384
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    • 2006
  • This study was conducted to perform for comparative analysis of the cleaning efficiency on 3 kinds of cleaning liquid state, 3 steps of cleaning temperature $(45^{\circ}C,\;60^{\circ}C,\;70^{\circ}C,\;)$ and 6 steps of cleaning time (2.5, 5, 7.5, 10, 12.5, 15 minute). 3 kinds of cleaning liquid state are the non fluidized bed, liquid fluidized bed and liquid/solid fluidized bed. UV spectrophotometer was used in estimation of cleaning efficiency, which it is experimental equipment using the absorptiometric analysis method. Cleaning efficiency by cleaning time was increase from 2.5 minutes to 15 minutes, liquid/siolid fluidized bed was indicated the highest cleaning efficiency among the 3 kinds of cleaning liquid state and $70^{\circ}C$ of cleaning temperature at liquid/solid fluidized bed was indicated the highest cleaning efficiency as 98% among the 3 steps of cleaning temperature.

소성Dolomite 수화물계의 축열시스템에 관한 연구 - 소성Dolomite 수화반응층의 전열해석 - (A Study on Heat Storage System Using Calcined Dolomite - Numerical Analysis of Heat Transfer in Calcined Dolomite Hydration Pocked Bed -)

  • 박영해;김종식
    • 한국태양에너지학회 논문집
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    • 제22권1호
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    • pp.9-21
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    • 2002
  • To develope chemical heat pump using available energy sources, solar heat and other kinds of waste thermal energy, we have studied the heat transfer rate in cylindrical bed reactor packed with calcined Dolomite. Two dimensional (radial and circumferential) Partial differential equations, concerning heat and mass transfer in packed bed of calcined Dolomite, are solved numerically to describe the characteristics of the reaction of calcined Dolomite and heat transfer. The results obtained by numerical analysis about two dimensional profiles of temperature and conversion of reactant in the packed bed reactor and the amount of exothermic heat released from the reactor are follows. It was found that all of calcined Dolomite packed bed kept the reaction temperature of about 750K throughout the entire part of the bed, immediately after the steam was introduced exothermic reaction of hydration was proceeded from the packed bed inpu to output and from wall side to center. The rate of thermochemical reaction depends on the temperature and concentration and it is also governed by the boundary conditions and heat transfer rate in the particle packed bed.

활성탄을 충전한 흡착탑에서 벤젠 회수를 위한 세정공정의 연구 (A Study on Cleaning Process for Benzene Recovery in Activated Carbon Bed)

  • 강성원;민병훈;서성섭
    • 한국응용과학기술학회지
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    • 제19권2호
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    • pp.108-116
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    • 2002
  • Experimental Study was carried out for benzene desorption by purge gas or evacuation in an activated carbon bed. As purge gas flow rate increased, desorption rate increased due to the higher interstitial linear gas velocity. For various purge gas flow rates, desoption curves almost got together if they were plotted against dimensionless time. At a higher flow rate, mass transfer zone became narrower. Temperature drop in the bed was more fast and severe at higher flow rates and higher outer temperature. It was found out that desorption was almost completed when the temperature in the drop of the bed returned to the initial temperature before temperature drop. Desorption by vacuum purge was completed in shorter time than desorption by purge gas. Countercurrent purge was more effective than cocurrent purge.

순환유동층 보일러 전열관의 열전달 특성 (Heat Transfer of Smooth and Finned Tubes in A CFBC)

  • 김부현;조형희
    • 대한기계학회:학술대회논문집
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    • 대한기계학회 2000년도 추계학술대회논문집B
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    • pp.651-655
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    • 2000
  • The objective of present work is to investigate experimentally the characteristics of heat transfer. A fluidized bed combustion has advantages of pollution control, fuel flexibility and excellent heat transfer. The present study investigates fundamental phenomena of bed-to-surface heat transfer in high temperature fluidized beds to improve design of immersed tube surface. The tested operating variables are bed temperature, supeficial velocity, mean size of bed material, and the rake angle of fin. Generally, heat transfer rates between the fluidized bed and immersed finned-tube are much higher than those of a smooth tube. A life time of finned-tube is generally longer than that of smooth tube.

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Coal pyrolysis behaviors at supercritical CO2 conditions

  • Hakduck Kim;Jeongmin Choi;Heechang Lim;Juhun Song
    • Advances in Energy Research
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    • 제8권4호
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    • pp.265-273
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    • 2022
  • In this study, a product gas yield and carbon conversion were measured during the coal pyrolysis. The pyrolysis process occurred under two different atmospheres such as subcritical (45 bar, 10℃) and supercritical CO2 condition (80 bar, 35℃). Under the same pressure (80 bar), the atmosphere temperature increased from 35℃ to 45℃ to further examine temperature effect on the pyrolysis at supercritical CO2 condition. For all three cases, a power input supplied to heating wire placed below coal bed was controlled to make coal bed temperature constant. The phase change of CO2 atmosphere and subsequent pyrolysis behaviors of coal bed were observed using high-resolution camcorder. The pressure and temperature in the reactor were controlled by a CO2 pump and heater. Then, the coal bed was heated by wire heater to proceed the pyrolysis under supercritical CO2 condition.

유동층연소로에서 탈황효율 실험 및 예측에 관한 연구 (A Study on the Experiments and Prediction of Desulfurization Efficiency in Fluidized Bed Combustor)

  • 조상원;김영식
    • 한국환경보건학회지
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    • 제28권5호
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    • pp.93-101
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    • 2002
  • We have studied that the prediction of desulfurization efficiency by limestone in fluidized-bed coal combustor. The results were presented as follows : Firstly, the bed temperature had a great deal of effect on the desulfurization and the optimum temperature of limestone was 85$0^{\circ}C$~90$0^{\circ}C$. Secondly, as the velocity and temperature increased, $K_{s}$, K and the desulfurization efficiency increased. So, $k_{s}$, $k_{d}$ highly depended on the air velocity and bed temperature, and $k_{s}$, $k_{d}$ were 82.53 mm/sec, 0.0041/sec at 0.2 m/sec, 85$0^{\circ}C$, $k_{s}$, $k_{d}$ were 125.62 mm/sec. 0.00532/sec at 0.3 m/sec, 80$0^{\circ}C$ respectively. And $k_{s}$, $k_{d}$ were 143.78 mm/sec, 0.00568/sec at 0.3 m/sec, 85$0^{\circ}C$. Thirdly, as a result of desulfurization modeling, there was good agreement between theory and experiments as anthracite fraction increased. At 3.0 of optimum Ca/S molar ratio, there was very good agreement between theory and experiments.riments.riments.s.

비예열 시동특성을 갖는 이원 촉매 베드 과산화수소 가스발생기 (Hydrogen Peroxide Gas Generator with Dual Catalytic Bed for Non-preheating Start-up)

  • 임하영;안성용;권세진
    • 한국추진공학회:학술대회논문집
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    • 한국추진공학회 2007년도 제28회 춘계학술대회논문집
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    • pp.163-167
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    • 2007
  • 은 촉매는 과산화수소 촉매분해에 많이 사용되지만, 상온에 시동이 어렵고 높은 온도에 적용하기 곤란하다. 본 논문에서는 은이 가지고 있는 단점을 극복하기 위해 기화기와 고온 촉매 베드로 구성된 이원 촉매 베드에 대한 연구를 수행하였다. 백금을 기화기 촉매로, perovskite 구조를 가지는 촉매를 고온 촉매로 선정하였고, 가스발생기를 이용한 시험을 통해 상온에서 예열이 없이도 시동이 가능함과 고온에서 안정적으로 작동함을 보여주었다.

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수면시 침상기후와 인체생리반응에 관한 연구 -온돌환경을 중심으로- (A Study on the Bed Climate and the Physiological Responses in Sleep. - On Ondol Environment -)

  • 김명주;최종화
    • 한국의류학회지
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    • 제15권2호
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    • pp.77-87
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    • 1991
  • The purpose of this study were to investigate the bed climate and the physiological responses in sleep on the traditional Korean floor heating system called Ondol. Ondol has been the most widely used heating system in Korea, yet there has been a no systematic studies examined its environmental effects on human body. Experimental room was constructed to match the typical thermal environment of Ondol. (floor surface temperature; $32\~33^{\circ}C$, air temperature; $22.5{\pm}1.0^{\circ}C$, relative humidity; $64.0{\pm}4.0\%$RH, air velocity; 0.25 m/sec.) Three different combinations of bedclothes were chosen for the experiment based on the study results showing that they were the most widely used types in Korea. Type 1 was the combination of a cotton-padded mattress with a cotton-padded Korean style blanket. Type 2 was a cotton-padded mattress with a cotton-guilted Korean style blanket. Type 3 was a cotton-padded matless with a polyacryl blanket. Thermal resistance of each of these combina-tions in the bedclothes was measured using thermal manikin. Two adult female was chosen for the seven hour sleeping experiment which was known to be the average sleeping hours of Korean adult female. The bed climate was measured with the temperature under the mattress, the surface temper-ature of the mattress, and the air temperature and the relative humidity of the space between the mattress and blanket. The skin temperature, rectal temperature of the subjects and the bed climate were measured eight times, one hour before the experiment and every hour during the experiment. The weight loss and the subjective sensation were measured for the each subjects before and after the experiment. The procedure was repeated twice with two subjects and three types of bedclothes, yielding twelve combinations of results. The results were as follows; 1. With the surface temperature of $32\~33^{\circ}C$ of Ondol, air temperature was $22.5{\pm}1.0^{\circ}C$ with $64.0{\pm}4.0\%$ RH. The bed climates were $39.2{\pm}40.8^{\circ}C$ under the mattress, $35.3\~36.2^{\circ}C$ on the mattress, and $26.9\~32.0^{\circ}C$ with $56.0\~71.3\%$ RH between the mattress and the blanket. 2. Mean skim temperature during sleep was 34.2"C with local skin temperature of $34.0\~35.5^{\circ}C$. The skin temperatures of abdomen, thigh, foot were higher than the other parts of the body. 3. The skin temperature of chest, thigh, leg and back varied significantly according to the combinations of bedclothes. With the cotton-padded blanket, the skin temperature was the highest, while with the cotton-guilted blanket showed lowest. 4. Examining the relationship between the mean skin temperature and the local skin temper-ature, the chest temperature showed the highest correlation with the former. Therefore, the chest temperature can be recommended to represent the skin temperature in measuring the bed climate. 5. The subjective bed climates were $39.0\~40.4^{\circ}C$ under the mattress, $35.2\~35.9^{\circ}C$ on the mattress, $29.8\~31.6^{\circ}C$ with $56.8\~68.4\%$ RH between the mattress and blanket. In sum, from this experiment we not only obtained the reliable value of bed climates on Ondol, but also showed that the bed climates and the physiological responses were affected differently according to the materials of bed clothes.

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Energy Storage Characteristics In Fixed Beds (Charging, Storing, Discharging)

  • Hassanein, Soubhi A.;Choi, Sang-Min
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2004년도 제29회 KOSCI SYMPOSIUM 논문집
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    • pp.17-23
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    • 2004
  • In the present work, the numerical model was refined to predict the thermal analysis of energy storage in a fixed beds during (charging ,storing, discharging) mode. The governing energy equations of both fluid and the solid particles along with their initial and boundary conditions are derived using a two-phase, one dimensional model. The refined model is carried out by taking into account change of (air density , air specific heat) with air temperature and also by taking into considerations heat losses from bed to surrounding. Finite difference method was used to obtain solution of two governing energy equations of both fluid and solid particles through a computer program especially constructed for this purpose. The temperature field for the air and the solid are obtained, also efficiency of energy stored inside the bed is computed. Finally using refined model the effect of air flow rate per unit area Ga (0.2, 0.3, and 0.4 kg/$m^2$-s), and inlet air temperature (200, 250, 300 $^{\circ}C$) on energy storage characteristics was studied in three mode ( charging ,storing, discharging). The rock particles of diameter 1 em is used as bed material in this research.

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