• Title/Summary/Keyword: Bed Temperature

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Studies on a Effective Scheme to Obtain High Temperature Working Plasma for MHD Power Generation (MHD발전용 작동 플라즈마를 고온가열하기 위한 효율적 방안에 관한 연구)

  • 김윤식;노창주;김영길;공영경;최춘성
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.17 no.1
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    • pp.153-161
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    • 1993
  • Heat transfer processes in the combustion chamber of a pebble bed regenerative heat exchanger for MHD power generation has been analyzed numerically for heating, evacuation argon heating periods individually. The calculated result well explain the measured temperature change at the top of the pebble bed. The analytical result point out that the length of evacution period and the geometry optimization both for the combustion chamber and the heat storage bed are very important factors for the improvement of thermal performance in MHD power generation.

Studies on the Drying Methods of Sea Foods 1 . Fixed Bed Drying of Squid (수산식품의 건조방법에 관한 연구 1 . 오정어의 고정층건조)

  • HUR Jong-Wha
    • Korean Journal of Fisheries and Aquatic Sciences
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    • v.15 no.1
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    • pp.107-110
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    • 1982
  • Fixed bed drying method was selected to reduce the initial drying time of squid and the effects of drying air temperature and bed height on the drying rate were investigated, with following results. 1. The drying rate in the fixed bed dryer was faster than that of natural convection type dryer heated indirectly and that of hot air dryer heated directly. 2, Shirai-equation was applicable to squid being dried. Using the equation, drying rate constant obtained was as shown in table 1.

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Characteristics of Air-blown Gasification In a Pebble bed Gasifier (고온공기를 이용한 고형연료의 가스화 운전 특성)

  • Choi, Young-Chan;Kim, Jae-Ho;Hong, Jae-Chang;Kim, Young-Ku;Lee, See-Hoon;Lee, Jae-Goo
    • 한국연소학회:학술대회논문집
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    • 2004.11a
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    • pp.238-243
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    • 2004
  • High temperature air blown gasification is new concept to utilize the waste heat from gasifier that is called the multi-staged enthalpy extraction technology. This process was developed to solve the economic problem due to air separation cost for the oxygen-blown as a gasifiying agent. In this study, we have performed the construction of pebble bed gasifier and operated it by controlling the pebble size and bed height. As a result, we can produce the syngas with the calorific value of 700kcal/$Nm^3$ at the condition of air temperature 650$^{\circ}C$.

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High Temperature Solar Gas Heating by a Compact Fluidized-Bed Receiver of Open-Type (개방형 유동층을 이용한 태양광 고온가스 가열장치의 연구)

  • Choi, Jun-Seop
    • Solar Energy
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    • v.12 no.1
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    • pp.95-102
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    • 1992
  • A small scale solar collector system composed of a Fresnel lens of $0.5m^2$ area as a solar concentrator and a compact fluidized-bed solar receiver was developed. Performance and temperature distribution in the fluidized bed receiver were measured using SiC for particles and air for working fluid. The maximum gas temperature was attained up to 1250K at this moment. In this study, energy efficiency achieved by the present experiment was high for the small scale solar collector system and compact receiver.

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Rice Seedling Establishment for Machine Transplanting II. Effects of Sprouting and Seed Bed Temperature on the Seedling Characteristics (수도 기계이앙 육묘에 관한 연구 II보. 간역출아방법 및 육묘상내 온도가 묘소질에 미치는 영향)

  • Yong-Dea Yun;Hyun-Ok Choi;Jong-Hoon Lee
    • KOREAN JOURNAL OF CROP SCIENCE
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    • v.22 no.2
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    • pp.32-36
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    • 1977
  • Experiments were conducted to know the effects of seed bed temperatures on the sprouting of seeds and seedling growth in the phytotron and field. Sprouting of seeds were most uniform when seed bed was stored under the straw and vinyl mulching for 48 hours after seed bed temperature increased up to 3$0^{\circ}C$ by the sun. In the phytotron, optimum temperature was 32$^{\circ}C$ for sprouting and day/night temperature of 25/30 and 20/15$^{\circ}C$ for greening and hardening of seedlings, respectively. In the field, the best results were obtained under the conditions of sprouting in the seedling chamber heated by electricity and greening the hardening under the double vinyl tunnel in the upland nusery bed.

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The Infiltration Velocity of a Sewage Disposal System with Water Plant and Gravel Bed (수초·골재 하수처리장의 투수속도)

  • Chung, Dong Yang
    • Journal of the Korean Society of Environmental Restoration Technology
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    • v.6 no.3
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    • pp.29-34
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    • 2003
  • This paper describes the effects of sewage amount, temperature, and years in operation on the infiltration rate of a sewage disposal system. The self-purifying sewage disposal system, which is typically used in rural areas, consists of reeds and fine gravel. Water plants are planted on the gravel bed which provides the habitat for microbes. The basic process is that the gravel bed filters incoming sewage. Thus this system requires the smooth flow of sewage through the gravel. However, the efficiency of the disposal system will be lowered if the gravel bed is clogged with sewage sludge. A three year study shows that infiltration rate slows down significantly until the 7th day, depending on the sewage amount and the temperature. After the 7th day, the infiltration rate remains almost constant. In addition, the infiltration rate decreases as the temperature falls. It also decreases as the number of years in operation increase. But there is no significant change in the infiltration rate after the 7th day, independent of the temperature, the sewage amount, and years in operation. In order to take advantage of high infiltration rate, which improves the efficiency of the disposal system in its early stages, having two gravel beds and using them alternatively will be efficient. This operation method is called intermittent load and makes the disposal system last longer. The water plant roots above the gravel bed make the effective filtration possible because they delay accumulation of the sewage sludge and stabilize the filtration ability.

Design of the Fixed-Bed Catalytic Reactor for Phthalic Anhydride Production: Optimal Reactor Length and Radius Estimation (무수프탈산 생산을 위한 고정층 촉매 반응기 설계: 최적 촉매층 길이 및 반경 추정)

  • Yoon, Young-Sam;Koo, Eun Hwa;Park, Pan-Wook
    • Applied Chemistry for Engineering
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    • v.10 no.8
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    • pp.1200-1209
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    • 1999
  • Prediction model was composed by optimal parameter estimation from best fitting on reactant temperature profile, inlet and outlet temperature of coolant and yield of dual fixed-bed catalytic reactor(FBCR) which was measured in the industrial field. In order to design the FBCR which could obtain maximum conversion and yield, we investigated the effect of catalyst bed length and reactor radius changes. An uniform activity FBCR showed the best performance at z = 2.8 m of total catalysst bed length in case of reactor radius r = 0.01241 m and z =2.80 m(upper layer: 1.88 m, lower layer: 0.92 m) under reactor radius r = 0.01254 m for a dual activities FCBR. In case of reactor radius changes, the axial temperature profile and maximum radial temperature was rapidly risen for radius increase. The reactor radius decrease showed the opposite result.

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Pretreatment by the Process of BAC Fluidized Bed to produce the Biologically Stable Drinking Water (생물활성탄 유동상법에 의한 상수원수의 생물학적 전처리공정)

  • 우달식;남상호
    • Journal of Environmental Health Sciences
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    • v.24 no.1
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    • pp.38-46
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    • 1998
  • This study was to investigate the effects of carbon loadings, temperature and expansion ratio on the waterborne organic removal by the biologically active GAC fluidized bed on a laboratory scale. The raw water to be treated comes from midstream of Han river. BACFB(Biological Activated Carbon Fluidized Bed) process was very effective to remove the biodegradable fraction of dissolved organic matter. The more carbon weighed, the more DOC removed in a range from 16.7 to 133.3 g/l. DOC and UV$_{254}$ were removed more than 40% and 20% above 20$\circ$C respectively. Between 5$\circ$C and 10$\circ$C, DOC and UV$_{254}$ were eliminated about 30% and 15% respectively. In general, even if the temperature was higher, DOC removal was a little sensitive, probably influenced by GAC's residual adsorption capacity. UV$_{254}$ reduction was little fluctuated in accordance with water temperature. The gradual increase in expansion ratio from 10% to 75% didn't greatly affect on the removal of DOC and UV$_{254}$. The expansion ratio, therefore, is not a key factor over the critical expansion ratio.

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An Experimental Study on Heat Transfer Performance of Heating Medium Oil Fluidized Bed Heat Exchanger (열매체유 유동층 열교환기의 전열성능에 대한 실험적 연구)

  • Park, Sang-Il;Ko, Chang-Bok;Lee, Young-Soo
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.27 no.3
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    • pp.146-151
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    • 2015
  • The heat transfer performance of heating medium oil fluidized bed heat exchanger was measured. The operation variables were air flow rate, air inlet temperature, moisture content, water flow rate and water inlet temperature. The outside heat transfer coefficient was determined from the heat exchanger experiment and its experimental correlation was determined as a function of air velocity and viscosity of heating medium oil. Effect of viscosity was well agreed with the previous studies. Errors of the correlation equation was less than about 10% for outside heat transfer coefficient developed in this study when compared with the measured value. Hot water with the temperature greater than $77^{\circ}C$ could be produced by using the heating medium oil fluidized bed heat exchanger.

Hydriding Performance in a Uranium Bed depending on the Initial Bed Temperatures and Helium Contents (우라늄 베드 초기온도 및 헬륨농도의 수소 흡장 영향)

  • KOO, DAESEO;KIM, YEANJIN;JUNG, KWANGJIN;YUN, SEI-HUN;CHUNG, HONGSUK
    • Transactions of the Korean hydrogen and new energy society
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    • v.27 no.2
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    • pp.163-168
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    • 2016
  • Korea has been developing nuclear fusion fuel storage and delivery system (SDS) technologies including a basic scientific study on hydrogen storage. To develop nuclear fusion technology, it is necessary to store and supply hydrogen isotopes needed for Tokamak operation. SDS is used for storing hydrogen isotopes as a metal hydride form. The rapid hydriding of tritium is very important not only for safety reasons but also for the economic design and operation of the SDS. In this study, we designed and fabricated a medium-scale getter bed of depleted uranium (DU). The hydriding of DU has been measured by varying the initial temperature ($100-300^{\circ}C$) of the DU getter bed to investigate the influence of the cooling temperature. Furthermore, we analyzed the effect of a helium blanket on the hydriding performance with 0 - 12% helium content in hydrogen.