• Title/Summary/Keyword: 증기 주입량

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Energy Accounting in Peach Canning Operations (복숭아통조림의 가공중 에너지소비)

  • Lee, Dong-Sun;Park, Know-Hyun;Shin, Hyu-Nyun;Shin, Dong-Hwa;Min, Byong-Yong
    • Korean Journal of Food Science and Technology
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    • v.14 no.3
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    • pp.232-235
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    • 1982
  • In order to establish the energy conservation strategy in canning of acid food, the enery consumption of peach canning factory was monitored. The energy intensity was investigated and quantification of thermal and electrical energy was undertaken in individual operations. For processing of 1 kg raw peach, thermal energy 864 kcal and electrical energy 0.045 KWh was consumed in overall factory. From daily processing of 14 M/T peach, 2060 kg waste like seeds and 1510 kg low grade product were produced, and syrup of 6240 kg was prepared for filling in can. Enery intensive operations were lyepeeling(35%) and pasteurization(53%). Steam quality in the monitored factory was in the range of $87{\sim}88%$ with no difference among processing lines and 23% of supplied thermal energy in pasteurization was utilized actually for heating food.

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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%.

Analysis of the Vent Path Through the Pressurizer Manway Under the Loss of Residual Heat Removal(RHR) System During Mid-Loop Operation in PWR (가압경수로 부분충수 운전중 잔열제거 (RHR)계통 상실시 가압기 통로를 통한 배출유로 특성 분석)

  • Ha, G.S.;Kim, W.S.;Chang, W.P.;Yoo, K.J.
    • Nuclear Engineering and Technology
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    • v.27 no.6
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    • pp.859-869
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    • 1995
  • The present study is to understand the physical phenomena anticipated during the accident with RHR loss under mid-loop operation in a PWR and, at the same time, to examine the prediction capability of RELAP5/MOD3.1 on such an accident, by simulating an integral test relevant to this accident for reliable analysis in an actual PWR. The selected experiment, i.g. BETHSY Test 6.9a, represents the configuration with the pressurizer manway open and steam generators unavailable during the accident. Accordingly, the results of this ok are sure to contribute to understanding both the key events as well as the sensitive parameters, anticipated in the accident, for validity of the actual analysis. In the simulation result overall behavior as well as major phenomena observed in the experiment have been predicted reasonably by RELAP5/MOD3.1, however, the problem associated with enormous computing time .due to small time step size has been encountered. Besides, the code prediction of higher swollen level in the pressure vessel has given rise to overestimation of both pressurizer level and RCS pressure. Subsequently, overprediction of the break flow through the manway has led to earlier core uncovery than that in the experiment by about 400 seconds. As a whole, it is demonstrated from both the experiment and the analysis that gravity feed has not been sufficient to recover the core level and thus additional forced feed has been necessary in this configuration.

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A Study on the Experimental Measurements and Its Recovery for the Rate of Boil-Off Gas from the Storage Tank of the CO2 Transport Ship (CO2 수송선 저장탱크의 BOG 측정 실험 및 회수에 관한 연구)

  • Park, Jin-Woo;Kim, Dong-Sun;Ko, Min-Su;Cho, Jung-Ho
    • Clean Technology
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    • v.20 no.1
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    • pp.1-6
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    • 2014
  • $CO_2$ is generated by the combustion reaction, when getting the energy from fossil fuel. If the carbon dioxide emissions increases more, the global warming problem will become more serious. CCS (carbon capture storage) needs to be developed for the prevention of this. When liquefied $CO_2$ is transported, BOG (boil-off gas) is generated because of several problems. In the study, by injecting liquefied $CO_2$ in two tanks which contains $40m^3$each, the amount of BOG and its composition were measured during 30 days when generating pressure changes and external heat, loading, unloading. In result, 16,040 kg of BOG was generated and the composition has been found out to be 99.95% $CO_2$ and 0.05 % $N_2$. Also, we conducted simulation process for reliquefaction of generated BOG with vapor compression cycle using the PRO/II with PROVISION version 9.2. As a result, the refrigeration cycle of the total circulation flow rate was 42.07 kg/h and the condenser utility consumption was 48.85 kg/h.