• Title/Summary/Keyword: Korea Research Reactor

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Steam Explosion Experiments using ZrO$_2$ (ZrO$_2$를 이용한 증기폭발 실험)

  • Song, Jin-Ho;Kim, Hui-Dong;Hong, Seong-Wan;Park, Ik-Gyu;Sin, Yong-Seung;Min, Byeong-Tae;Kim, Jong-Hwan;Jang, Yeong-Jo
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.25 no.12
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    • pp.1887-1897
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    • 2001
  • Korea Atomic Energy Research Institute (KAERI) launched an intermediate scale steam explosion experiment named "Test for Real Corium Interaction with water (TROI)" using reactor material to investigate whether the molten reactor material would lead to energetic steam explosion when interacted wish cold water at low pressure. The melt-water interaction experiment is performed in a pressure vessel with the multi-dimensional fuel and water pool geometry. The novel concept of cold crucible technology, where powder of the reactor material in a water-cooled cafe is heated by high frequency induction, is firstly implemented for the generation of molten fuel. In this paper, the lest facility and cold crucible technology are introduced and the results or the first series of tests were discussed. The 5 kg of molten ZrO$_2$jet was poured into the 67cm deep water pool at 30 ∼ 95 $\^{C}$. Either spontaneous steam explosions or quenching was observed. The morphology of debris and pressure wave profiles clearly indicate the differences between the two cases.

Basic Design and Sensitivity Analysis of 3 MWth Chemical Looping Combustion System for LNG Combustion and Steam Generation (LNG 연소 및 스팀생산을 위한 3 MWth 급 매체순환연소 시스템의 기본설계 및 민감도 분석)

  • RYU, HO-JUNG;NAM, HYUNGSEOK;HWANG, BYUNG WOOK;KIM, HANA;WON, YOOSEOB;KIM, DAEWOOK;KIM, DONG-WON;LEE, GYU-HWA;BAEK, JEOM-IN
    • Journal of Hydrogen and New Energy
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    • v.32 no.5
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    • pp.374-387
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    • 2021
  • Basic design of 3 MWth chemical looping combustion system for LNG combustion and steam generation was conducted based on the mass and energy balance and the previous reactivity test results of oxygen carrier particles. Process configuration including fast fluidized bed (air reactor), loop seal and bubbling fluidized bed (fuel reactor) was confirmed and their dimensions were determined by mass balance. Then, the external fluidized bed heat exchanger (FBHE) was adopted based on the energy balance to extract heat from the system. The optimum reactor design and operating condition was confirmed with sensitivity analysis by modifying system configuration based on the mass and energy balance.

PRELIMINARY ESTIMATION OF ACTIVATED CORROSION PRODUCTS IN THE COOLANT SYSTEM OF FUSION DEMO REACTOR

  • Noh, Si-Wan;Lee, Jai-Ki;Shin, Chang-Ho;Kwon, Tae-Je;Kim, Jong-Kyung;Lee, Young-Seok
    • Journal of Radiation Protection and Research
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    • v.37 no.2
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    • pp.63-69
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    • 2012
  • The second phase of the national program for fusion energy development in Korea starts from 2012 for design and construction of the fusion DEMO reactor. Radiological assessment for the fusion reactor is one of the key tasks to assure its licensability and the starting point of the assessment is determination of the source terms. As the first effort, the activities of the coolant due to activated corrosion product (ACP) were estimated. Data and experiences from fission reactors were used, in part, in the calculations of the ACP concentrations because of lack of operating experience for fusion reactors. The MCNPX code was used to determine neutron spectra and intensities at the coolant locations and the FISPACT code was used to estimate the ACP activities in the coolant of the fusion DEMO reactor. The calculated specific activities of the most nuclides in the fusion DEMO reactor coolant were 2-15 times lower than those in the PWR coolant, but the specific activities of $^{57}Co$ and $^{57}Ni$ were expected to be much higher than in the PWR coolant. The preliminary results of this study can be used to figure out the approximate radiological conditions and to establish a tentative set of radiological design criteria for the systems carrying coolant in the design phase of the fusion DEMO reactor.

CANDU-6 Heat Transport System Stability Analysis With Canflex Fuel Bundle (CANFLEX 핵연료를 사용한 CANDU-6의 열수송계통 안정성 분석)

  • Shin, Jung-Cheol;Park, Ju-Hwan;Kim, Tae-Han;Suk, Ho-Chun
    • Nuclear Engineering and Technology
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    • v.27 no.3
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    • pp.358-373
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    • 1995
  • The Heat Transport system loop stability of CANDU-6 reactor using the CANFLEX fuel bundle was studied. The Thermal-hydraulic behavior of CANFLEX fuel bundle is similar to the conventional 37-element fuel bundle since the reactor power and the frictional pressure drop through the fuel channel is almost the same each other, Mounter the CANFLEX fuel bundle gives higher critical channel power and more homogeneous enthalpy distributions in the subchannels than 37-element fuel bundle. The SOPHT modelling or the CANFLEX fuel bundle and the Reactor outlet Header(ROH) interconnection line was made and the stability analysis response of Wolsong-1 reactor with CANFLEX fuel bundle was obtained. Without the ROH interconnection line the Heat Transport system loop using 43-element fuel bundle is unstable like the current 37-element fuel bundle. With the ROH interconnection line, however, the Heat Transport system is stable within $\pm$1% of nominal flow. In the Heat Transport system loop stability point of view for Wolsong-1 plant therefore, the CANFLEX fuel loading is considered to be acceptable.

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Optimal Design of Carbon Dioxide Dry Reformer for Suppressing Coke Formation (코크 생성 억제를 위한 이산화탄소 건식 개질 반응기의 최적 설계)

  • Lee, Jongwon;Han, Myungwan;Kim, Beomsik
    • Korean Chemical Engineering Research
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    • v.56 no.2
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    • pp.176-185
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    • 2018
  • As global warming accelerates, greenhouse gas reduction becomes more important. Carbon dioxide dry reforming is a promising green-house gas reduction technology that can obtain CO and $H_2$ which are high value-added materials by utilizing $CO_2$ and $CH_4$ which are greenhouse gases. However, there is a significant coking problem during operation of the dry reforming reactor. Because the carbon dioxide dry reforming is a strong endothermic reaction, the temperature of the reactor drops near the reactor inlet and causes coke formation. To solve this problem, it is important to ensure that the reaction takes place in a temperature range where coke production is minimized. In this study, we proposed a design method that can maintain reaction temperature in the region where the coke is rarely generated by using the new catalyst configuration method. The design method also optimizes the reactor by solving the optimization problem which minimizes the reactor length for a given reaction conversion by using the fuel flow rate, catalyst density, and output temperature by section as optimization variables.

Conceptual Design and Hydrodynamic Properties of a Moving Bed Reactor for Intrinsic $CO_2$ Separation Hydrogen Production Process ($CO_2$ 원천분리 수소 제조 공정을 위한 이동층 반응기의 개념 설계 및 수력학적 특성)

  • Park, Dong-Kyoo;Cho, Won-Chul;Seo, Myung-Won;Go, Kang-Seok;Kim, Sang-Done;Kang, Kyoung-Soo;Park, Chu-Sik
    • Clean Technology
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    • v.17 no.1
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    • pp.69-77
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    • 2011
  • The intrinsic $CO_2$ separation and hydrogen production system is a novel concept using oxidation and reduction reactions of oxygen carrier for both $CO_2$ capture and high purity hydrogen production. The process consists of a fuel reactor (FR), a steam reactor (SR) and an air reactor (AR). The natural gas ($CH_4$) is oxidized to $CO_2$ and steam by the oxygen carrier in FR, whereas the steam is reduced to hydrogen by oxidation of the reduced oxygen carrier in SR. The oxygen carrier is fully oxidized by air in AR. In the present study, the chemical looping moving bed reactor having 200 L/h hydrogen production capacity is designed and the hydrodynamic properties were determined. Compared with other reactors, two moving bed reactors (FR, SR) were used to obtain high conversion and selectivity of the oxygen carrier. The desirable solid circulation rates are calculated to be in the range of $20{\sim}100kg/m^2s$ from the conceptual design. The solid circulation rate can be controlled by aeration in a loop-seal. To maintain the gas velocity in the moving beds (FR, SR) at the minimum fluidization velocity is found to be suitable for the stable operation. The solid holdup in moving beds decrease with increasing gas velocity and solid circulation rate.