• Title/Summary/Keyword: 열 교환기

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Design of adsorption bed for Compact $H_2$ PSA process (Compact $H_2$ PSA 공정을 위한 흡착탑의 설계)

  • Lee, Jang-Jae;Lee, Sang-Jin;Moon, Jong-Ho;Choi, Dae-Ki;Lee, Chang-Ha
    • 한국신재생에너지학회:학술대회논문집
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    • 2006.06a
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    • pp.5-8
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    • 2006
  • 수소 station에서 수소분리정제를 위한 compact형 PSA 공정 설계를 위하여 활성탄으로 충진된 dual bed의 흡착동특성을 연구하였다. 기존 PSA 공정의 흡착탑이 차지하는 시스템의 공간을 줄이기 위하여 하나의 흡착탑 안에 다른 흡착탑을 넣어 흡착탑이 차지하는 공간을 최소화하고, 흡착탑 간의 열교환을 효과적으로 할 수 있도록 고안하였다. 수소 혼합물에 대한 dual bed에서의 흡착, 탈착 실험 실시하였으며, 시간에 따른 농도와 온도의 변화를 측정하였다. 수소 혼합물로는 $H_2/CO/CH_4/CO_2$ (69:2:3:26vol.%)를 사용하였으며, 흡착유량은 7LPM, 흡착압력은 9atm 조건에서 운전하였다. Inner bed와 outer bed의 수소 농도 파과곡선의 형태에 있어 차이를 보였으며, 이는 각 탑에서 열교환 효과로 인한 내부 온도 차이에 기인하여 발생하였다.

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Heat Transfer Performance of Individual Rows in Fin-Tube Heat Exchangers (2열 핀-관 열 교환기의 열별 전열성능 측정)

  • 권영철;정지환;장근선;홍기수;진심원
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.16 no.3
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    • pp.280-286
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    • 2004
  • An experimental study is peformed to examine the heat transfer performance of individual rows of fin-tube heat exchangers. The heat transfer performance is measured using an air-enthalpy type calorimeter. The examined heat exchangers consist of 7mm tube and fin patterns of them are slit and louver types. Equivalent fin spacings are 18 fins per inch(fpi) for all samples, and the number of tube rows are two. In order to confirm that thermal boundary condition on fins of each row are the same, physically separated between two rows as well as connected heat exchangers are used. The frontal air velocity is varied from 0.7 to 2.5㎧. Heat transfer performance for each row is measured. It is observed that the heat transfer coefficient of the second row is smaller than that of the first row at low Reynolds number while larger at high Reynolds number.

액체금속로 SAILMER 개념 개발

  • 남호윤;이용범;김용균;최병해;김종만
    • Proceedings of the Korean Nuclear Society Conference
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    • 1997.10a
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    • pp.509-515
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    • 1997
  • 환상형 이중벽 증기발생기와 환상형 전자펌프 신개념을 개발하여 중간열교환계통과 소듐 배관이 없는 단순하고 밀집된 형태의 액체금속로인 SAILMER 노형 개념을 제안하였다. 금속핵연료를 사용하는 모듈형으로 증기발생기에서의 소듐과 물 반응사고에 대비한 연구와 제작기술을 제고시키면 이 노형은 경제성과 고유안전성을 동시에 구현할 수 있다.

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Optimum Size Combination of Heat Exchangers in a Small Gifford-Mchon/ Joule-Thomson Refrigerator (소형 Gifford-McMahon/Joule-Thomson 냉동기에서 열교환기의 최적 조합)

  • 김영률;이상용;장호명
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.16 no.11
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    • pp.2196-2202
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    • 1992
  • The optimum size combination of heat exchangers in a Joule-Thomson(J-T) circuit for small cryogenic systems has been sought analytically, when the circuit is combined with a two-stage Gifford-McMahon(GM) cooler. Full thermodynamic cycle analysis was carried out to predict the performance of the combined refrigeration system. Relevant convective heat transfer coefficients, the computerized properties of helium, and the refrigeration capacity curve of a typical GM cooler have been used in the analysis. The result showed that, by changing the configuration(heat exchanger area ratio) of the system, the performance of the commonly-used GM/J-T refrigerators could be optimized. For the maximum refrigeration performance, the optimum mass flow rate of the refrigerant and the relative size between the heat exchangers have been obtained, when the cooling load was 0.1W at 3.995K with the total heat exchanger area being given.

Effect of the Heat Exchange between Low and High Temperature Refrigerant on the Heat Pump Performance (저온측과 고온측 냉매간 열교환이 열펌프의 성능특성에 미치는 영향)

  • 이건중;송현갑
    • Journal of Biosystems Engineering
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    • v.24 no.4
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    • pp.343-350
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    • 1999
  • The ambient air is commonly used as low-temperature heat source for heat pump operation. However, the coefficient of performance(COP) of the air to water heat pump is decreased with the ambient air temperature drop. In this study to solve this problem, the AVACTHE(Automatic Variable Area Capillary Type Heat Exchanger) with 3 levels of heat exchange area(0, 1,495.4, 1,794.5$\textrm{cm}^2$)was installed in the refrigerant circuit of the heat pump. The AVACTHE effect on the performance of heat pump was tested with the ambient air temperature variation. The COP improvement of the heat pump could be achieved by the AVACTHE installation when below -5$^{\circ}C$ of the ambient air temperature.

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Test Case Generation of GSMP Protocol for Open Multiservice Switching System (개방형 멀티서비스 교환 시스템에서 GSMP의 시험열 생성 기법)

  • Lee, Hyun-Jeong;Choi, Young-Il;Lee, Byung-Sun;Jun, Kyung-Pyo
    • Proceedings of the Korea Information Processing Society Conference
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    • 2000.10b
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    • pp.1129-1132
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    • 2000
  • 최근 인터넷 수요의 증가로 통신망에서 음성, 영상 및 데이터(data)를 복합적으로 지원할 수 있는 멀티서비스(multiservice)의 교환 기술이 필수적이다. 또한 망 사업자들이 여러 벤더(vendor)들로부터 최적의 장비를 선택하여 망을 구축할 수 있도록 통신 장비들의 상호 운용성을 지원하는 개방형 구조의 망 및 스위치 시스템(switch system)을 정의하는 작업이 필요하다. 페트리 넷(Petri Nets)은 시스템(system)을 분석하기 위한 도구로서, 시스템은 페트리 넷 이론에 의해 시스템의 수학적 표현인 페트리 넷으로 설계될 수 있다. CPN(Colored Petri Nets)은 페트리넷의 확장형으로서, 토근(token)에 칼라를 부여하여 다양한 특성을 지닌 시스템을 표현하기에 적합하다. Design/CPN은 CPN의 사용을 지원하는 소프트웨어 패키지(software package)이다. 본 논문에서는 개방형 멀티서비스 교환 시스템의 핵심으로 스위치와 제어기(Controller) 사이의 표준 프로토콜인 GSMP(General Switch Management Protocol) 프로토콜을 Design/CPN 으로 변환하고, 이로부터 시험열을 생성한다.

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Evaluation of Corrosion Resistance of Materials for Supercritical Carbon Dioxide Power Plant (초임계 이산화탄소 발전용 소재의 고온 내식성 평가)

  • Chae, Hobyung;Seo, Sukho;Jung, Yong Chan;Lee, Soo Yeol
    • KEPCO Journal on Electric Power and Energy
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    • v.1 no.1
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    • pp.109-113
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    • 2015
  • 초임계 이산화탄소 발전 시스템 구축을 위해서는 고온, 고압의 열악한 환경에 노출되는 터빈, 열 교환기, 압축기와 같은 핵심 부품들의 내식성 평가는 반드시 수행되어야 한다. 이를 위해 후보소재 3종 Ferritic-Martensitic Steel (T92), Austenitic Steel (SS316L), Ni-based Alloy (IN738LC)를 선정하여 고온의 유사 초임계 $CO_2$ 발전 환경에서의 내식성 평가를 진행하였다. $600^{\circ}C$, $700^{\circ}C$의 2개의 온도 구간에서 $CO_2$ 분위기를 조성하여 800 시간 동안 노출시킨 뒤, Weight Change, Surface Morphology, Cross Section, Composition을 분석하였다. Cr-rich Protective Layer를 형성하는 Ni-based Alloy와 Fe/Cr-rich oxide를 형성하는 Austenitic Steel은 우수한 부식 저항성을 보인 반면에 Ferritic-Martensitic Steel은 높은 Weight Change와 Fe-rich Non-Protective Oxide가 관찰되어 상대적으로 낮은 부식 저항성을 보였다.

Experimental study on heating performance characteristics of electric heat pump system using stack coolant in a fuel cell electric vehicle (연료전지 스택 폐열 활용 전동식 히트펌프 시스템 난방 성능 특성 연구)

  • Lee, Ho-Seong;Kim, Jung-Il;Won, Hun-Joo;Lee, Moo-Yeon
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.19 no.12
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    • pp.924-930
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    • 2018
  • The objective of this study was to investigate heating performance characteristics of electric heat pump system in a fuel cell electric vehicle (FCEV). In order to analyze heating performance characteristics of electric heat pump system with plate-type heat exchanger using stack coolant to evaporate the refrigerant, R-134a, each component was installed and tested under various operating conditions, such as air inlet temperature of inner condenser and compressor speed. When the air inlet temperature of inner condenser was varied from $0.0^{\circ}C$ to $-20.0^{\circ}C$, heating capacity was not quite different due to similar temperature gap between inlet and outlet of inner condenser with electric-driven expansion valve (EEV). However, COP increased until certain EEV opening, especially under 45.0%, because of decreasing power consumption. According to the compressor speed variation from 2,000 to 4,000 RPM, heating capacity and COP were found to have opposite trend. In the future works, stack coolant conditions as the heat source for tested heat pump system were analyzed with respect to heating performance, such as heating capacity and COP.

Heat Integration and Economic Analysis of Dry Flue Gas Recirculation in a 500 MWe Oxy-coal Circulating Fluidized-bed (CFB) Power Plant with Ultra-supercritical Steam Cycle (순환 유동층 보일러와 초초임계 증기 사이클을 이용한 500 MWe급 순산소 화력발전소의 건식 재순환 흐름의 열 교환 및 경제성 분석)

  • Kim, Semie;Lim, Young-Il
    • Korean Chemical Engineering Research
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    • v.59 no.1
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    • pp.60-67
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    • 2021
  • This study presented techno-economic analysis of a 500 MWe oxy-coal power plant with CO2 capture. The power plant included a circulating fluidized-bed (CFB), ultra-supercritical steam turbine, flue gas conditioning (FGC), air separation unit (ASU), and CO2 processing unit (CPU). The dry flue gas recirculation (FGR) was used to control the combustion temperature of CFB. One FGR heat exchanger, one heat exchanger for N2 stream exiting ASU, and a heat recovery from CPU compressor were considered to enhance heat efficiency. The decrease in the temperature difference (ΔT) of the FGR heat exchanger that means the increase in heat recovery from flue gas enhanced the electricity and exergy efficiencies. The annual cost including the FGR heat exchanger and FGC cooling water was minimized at ΔT = 10 ℃, where the electricity efficiency, total capital cost, total production cost, and return on investment were 39%, 1371 M$, 90 M$, and 7%/y, respectively.