• 제목/요약/키워드: loop reactor

검색결과 251건 처리시간 0.03초

유동상 담체를 이용한 Loop Reactor에서 유기물 및 질소, 인 제거 (The Removal of Organics, Nitrogen and Phosphorus in Loop Reactor Using Fluidized Media)

  • 선용호
    • KSBB Journal
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    • 제24권4호
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    • pp.353-360
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    • 2009
  • 본 연구에서는 혐기조 및 무산소조, 호기조로 구성된 상향류식 고정상 담체 반응장치와 호기조로 고정상 담체 대신에 유동상 담체를 사용한 Loop Reactor로 이루어진 장치에서 생활하수를 이용하여 성능실험을 수행한 후 HRT에 따른 유기물 및 T-N, T-P 등 오염물질의 제거 특성을 비교 분석하였다. 두 반응기 모두 평균 BOD 제거율과 SS 제거율은 HRT가 증가함에 따라 증가하다가 HRT 16 h 이상에서는 일정한 수치를 나타내고 있으며 HRT 16 h에서 고정상 담체 반응기와 Loop Reactor의 평균 BOD 제거율은 각각 86.6%, 90.9%이었으며 평균 SS 제거율은 각각 78.0%, 88.2%로 Loop Reactor의 경우가 각각 4.3%, 10.2%의 더 높은 BOD와 SS 제거율을 나타내었다. 또한 평균 $COD_{Cr}$, 제거율 및 평균 $COD_{Mn}$ 제거율은 BOD와 SS 제거율과 마찬가지로 HRT가 증가함에 따라 증가하다가 HRT 16 h에서 일정한 수치를 나타내고 있으며 고정상 담체 반응기와 Loop Reactor의 평균 $COD_{Cr}$, 제거율은 각각 63.5%, 75.2%이었으며 평균 $COD_{Mn}$ 제거율은 각각 60.7%, 73.6%로 Loop Reactor의 경우가 11.7%, 12.9% 더 높은 제거율을 나타내었다. 반면에 평균 T-N 제거율 및 T-P 제거율은 두 반응기 모두 HRT가 증가함에 따라 제거율은 계속 증가하는 양상을 보여주고 있으며 HRT 16 h에서 Loop Reactor의 경우 평균 T-N 제거율 및 평균 T-P 제거율은 각각 33.6%, 54.5%로 고정상 담체 반응기보다 14.1%, 10.8%의 더 높은 제거율을 나타내었다. 이상의 결과에서 Loop Reactor가 성능이 훨씬 더 우수하였으며 최적 HRT는 16 h임을 알 수 있었다.

SUPERCRITICAL WATER LOOP DESIGN FOR CORROSION AND WATER CHEMISTRY TESTS UNDER IRRADIATION

  • Ruzickova, Mariana;Hajek, Petr;Smida, Stepan;Vsolak, Rudolf;Petr, Jan;Kysela, Jan
    • Nuclear Engineering and Technology
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    • 제40권2호
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    • pp.127-132
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    • 2008
  • An experimental loop operating with water at supercritical conditions(25MPa, $600^{\circ}C$ in the test section) is designed for operation in the research reactor LVR-15 in UJV Rez, Czech Republic. The loop should serve as an experimental facility for corrosion tests of materials for in-core as well as out-of-core structures, for testing and optimization of suitable water chemistry for a future HPLWR and for studies of radiolysis of water at supercritical conditions, which remains the domain where very few experimental data are available. At present, final necessary calculations(thermalhydraulic, neutronic, strength) are being performed on the irradiation channel, which is the most challenging part of the loop. The concept of the primary and auxiliary circuits has been completed. The design of the loop shall be finished in the course of the year 2007 to start the construction, out-of-pile testing to verify proper functioning of all systems and as such to be ready for in-pile tests by the end of the HPLWR Phase 2 European project by the end of 2009.

EVALUATION OF PLANT OPERATIONAL STATES WITH THE CONSIDERATION OF LOOP STRUCTURES UNDER ACCIDENT CONDITIONS

  • MATSUOKA, TAKESHI
    • Nuclear Engineering and Technology
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    • 제47권2호
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    • pp.157-164
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    • 2015
  • Nuclear power plants have logical loop structures in their system configuration. This paper explains the method to solve a loop structure in reliability analysis. As examples of loop structured systems, the reactor core isolation cooling system and high-pressure core injection system of a boiling water reactor are considered and analyzed under a station blackout accident condition. The analysis results show the important role of loop structures under severe accidents. For the evaluation of the safety of nuclear power plants, it is necessary to accurately evaluate a loop structure's reliability.

Jet-Loop Reactor를 이용한 Polyester 감량폐수중 Ethylene Glycol의 생물학적 처리 (Biological Treatment of Ethylene Glycol in Polyester Weight-Loss Wastewater Using Jet-Loop Reactor)

  • 류원률;최장승;조무환
    • KSBB Journal
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    • 제14권1호
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    • pp.119-123
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    • 1999
  • Polyester 감량폐수의 주성분 중 물리.화학적 처리가 어려운 EG를 생물학적으로 처리하기 위하여 jet-loop reactor를 사용하였다 Jet-loop reactor의 산소전달계수는 air-lift reactor와 비교하여 훨씬 컸다. 합성 polyester 감량폐수를 사용하여 부하율 2.64 $kgCOD_{Mn}/m^3$.day, 3.07$kgCOD_{Cr}/m^3$.day로 처리한 경우 유출수의 농도는 154 $mgCOD_{Mn}/L$, 156$mgCOD_{Mn}/L$이었으며, 이 때 각각 93, 93.9%의 제거율을 나타내었다. $COD_{Mn}$의 비부하 속도가 0.25에서 1.72$kgCOD_{Mn}/kgMLVSS$.day로 증가 함에 따라 비기질제거 속도는 0.25에서 1.60$kgCOD_{Mn}-removed/kgMLVSS$.day로 선형적으로 증가하였다. 그리고, 동력학적 계수 Y는 0.78,$K_d$는 0.1$day^{-1}$, $K_s$는 89mg/L는 k는 0.05$hr^{-1}$이었다. 실제 polyester 감량폐수를 사용하여 부하율 2.64$kgCOD_{Mn}/m^3$.day,5.24$kgCOD_{Cr}/m^3$.day로 처리한 경우 유출수의 농도는 150$kgCOD_{Mn}/L$, 3.6$kgCOD_{Cr}/L$이었으며, 이때 각각 93.2,93%의 제거울을 나타내었다.

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Thermal-hydraulic simulation and evaluation of a natural circulation thermosyphon loop for a reactor cavity cooling system of a high-temperature reactor

  • Swart, R.;Dobson, R.T.
    • Nuclear Engineering and Technology
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    • 제52권2호
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    • pp.271-278
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    • 2020
  • The investigation into a full-scale 27 m high, by 6 m wide, thermosyphon loop. The simulation model is based on a one-dimensional axially-symmetrical control volume approach, where the loop is divided into a series of discreet control volumes. The three conservation equations, namely, mass, momentum and energy, were applied to these control volumes and solved with an explicit numerical method. The flow is assumed to be quasi-static, implying that the mass-flow rate changes over time. However, at any instant in time the mass-flow rate is constant around the loop. The boussinesq approximation was invoked, and a reasonable correlation between the experimental and theoretical results was obtained. Experimental results are presented and the flow regimes of the working fluid inside the loop identified. The results indicate that a series of such thermosyphon loops can be used as a cavity cooling system and that the one-dimensional theoretical model can predict the internal temperature and mass-flow rate of the thermosyphon loop.

내부순환반응기의 Scale-up에 따른 동력학적 특성의 변화 (Dynamic Behavior of an Internal Loop Reactor during Scale-up)

  • 최윤찬;박영식
    • 한국환경과학회지
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    • 제6권1호
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    • pp.25-31
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    • 1997
  • The variations of gas hold-up, overall volumetric oxygen mass transfer coefficients and liquid circulation velocity in an internal loop reactor were investigated to manifest scale-up effect. The relationship between superficial gas velocity and gas hold-up were found as Ugr = 0.045 $\varepsilon$r in the pilot-scale and Ugr = 0.056 $\varepsilon$r in the bench-scale reactor. The overall volumetric oxygen mass tractsfer coefficient, KLa was slightly increased in the pilot-scale than in the bench-scale reactor. Flow regime was changed from the bubble flow to the churn-turbulent flow when the superficial gas velocity reached to 3.5 - 4 cm/sec in the pilot-scale.

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초고온가스로 모사 실험회로 설계를 위한 전산유체역학 해석 (CFD Analysis for Simulating Very-High-Temperature Reactor by Designing Experimental Loop)

  • 윤철;홍성덕;노재만;김용완;장종화
    • 대한기계학회논문집B
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    • 제34권5호
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    • pp.553-561
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    • 2010
  • 한국원자력연구원에서는 초고온가스로를 모사할 수 있는 중형 헬륨 회로를 건설 중에 있다. 이 실험헬륨 회로에서 두 개의 전기 가열기가 헬륨 유체를 1 ~ 9 MPa 의 압력 하에서 $950^{\circ}C$ 까지 가열하게 된다. 이 실험 헬륨 회로의 설계 사양을 최적화하기 위하여, 본 연구에서는 두 개의 가열기 중 하류에 위치한 고온헬륨가열기 안의 복합열전달 현상을 전산유체역학으로 해석하였다. 해석 결과에서 헬륨 가열기 내 최대 온도는 허용 한계를 넘지 않았고, 이로써 선정된 기하구조의 열적 특성은 설계요건을 만족함이 확인되었다.

Semi-batch Jet Loop Reactor에서 연소 배가스중 CO2를 이용한 알칼리 폐수 중화 (Neutralization of Synthetic Alkaline Wastewater with CO2 in a Semi-batch Jet Loop Reactor)

  • 손민기;성호진;이제근
    • 한국연소학회지
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    • 제18권2호
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    • pp.17-22
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    • 2013
  • In this study, we tested the absorption of $CO_2$ in combustion gas into an alkaline wastewater to simultaneously control $CO_2$ and wastewater. During the experiment, we investigated the effects of operating parameters on neutralization characteristics of the wastewater by using $CO_2$ in a bench-scale semi-batch jet loop reactor (0.1 m diameter and 1.0 m in height). The operating parameters investigated in the study are gas flow rate of 1.0-2.0 L/min, liquid recirculation flow rate of 4-32 L/min, and liquid temperature of $20-25^{\circ}C$. It was shown that the initial pH of wastewater rapidly decreased with increased gas flow rate for a given liquid recirculation flow rate. This was due to the increase in the gas holdup and the interfacial area at higher gas flow rate in the reactor. At constant gas flow rate, the time required to neutralize the wastewater initial pH of 10.1 decreased with liquid recirculation flow rate ($Q_L$), reached a minimum value in the range of $Q_L$ = 16-24 L/min, and then increased with further increase in $Q_L$. Further, the time required to neutralize the wastewater was shortened at higher temperatures.

Semi-batch Jet Loop Reactor에서 연소 배가스중 CO2를 이용한 알칼리 폐수 중화 (Neutralization of Synthetic Alkaline Wastewater with CO2 in a Semi-batch Jet Loop Reactor)

  • 손민기;성호진;이제근
    • 한국연소학회지
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    • 제18권3호
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    • pp.38-43
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    • 2013
  • In this study, we tested the absorption of $CO_2$ in combustion gas into an alkaline wastewater to simultaneously control $CO_2$ and wastewater. During the experiment, we investigated the effects of operating parameters on neutralization characteristics of the wastewater by using $CO_2$ in a bench-scale semi-batch jet loop reactor (0.1 m diameter and 1.0 m in height). The operating parameters investigated in the study are gas flow rate of 1.0-2.0 L/min, liquid recirculation flow rate of 4-32 L/min, and liquid temperature of $20-25^{\circ}C$. It was shown that the initial pH of wastewater rapidly decreased with increased gas flow rate for a given liquid recirculation flow rate. This was due to the increase in the gas holdup and the interfacial area at higher gas flow rate in the reactor. At constant gas flow rate, the time required to neutralize the wastewater initial pH of 10.1 decreased with liquid recirculation flow rate ($Q_L$), reached a minimum value in the range of $Q_L$ = 16-24 L/min, and then increased with further increase in $Q_L$. Further, the time required to neutralize the wastewater was shortened at higher temperatures.

활성탄 담체가 포함된 Jet-Loop Reactor를 이용한 종합염색폐수처리 (Biological Treatment of Dyeing Wastewater Using Jet Loop Reactor with Activated Carton Supports)

  • 조무환;박종탁;이길호;류원률
    • KSBB Journal
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    • 제17권3호
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    • pp.241-246
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    • 2002
  • 오늘날 섬유 염색공정에서 발생하는 염색폐수로 인해 많은 문제점들을 야기한다. 염색폐수에는 난분해성의 EG, PVA, TPA, 여러 종류의 계면활성제가 포함되어 있어 완전하게 처리하기가 어렵다. 현재 일반적으로 사용하고 있는 물리화학적 처리와 활성오니공정의 처리성을 향상하기 위하여 jet-loop reactor (JLR)와 물리화학적 처리를 결합한 새로운 공정을 개발하였다. JLR의 부피산소전달계수는 air-lift 반응기에 비해 아주 우수하였다. 또한 좀더 효율적인 처리를 위하여 JLR에 활성탄 담체를 적용하여 (JLRAS) 실험하였다. 체류시간이 8시간일 때 BOD, $COD_{Mn}$, $COD_{Cr}$, 색도 제거율은 각각 99, 86, 84, 83%로 우수하였다. JLRAS 성능은 $COD_{Mn}$의 부하 변동에도 아주 빠르게 회복되었다. 2차 물리화학적 응집처리의 최적 응집제로는 폴리황산제2철이며 130 mg/L 투입하였을때 $COD_{Mn}$과 색도의 제거율은 자각 85, 73%였다. 결론적으로 이 공정으로 난분해성의 많은 유기물을 효율적으로 처리할 수 있으며 운전비용도 감소시킬 수 있었다.