• 제목/요약/키워드: Liquefier

검색결과 9건 처리시간 0.022초

GM 냉동기를 이용한 네온 액화기 제작 (I) (Neon liquefier system using GM cryocooler (I))

  • 권운식;손명환;백승규;이언용;권영길;권용덕
    • 한국초전도저온공학회:학술대회논문집
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    • 한국초전도저온공학회 2003년도 학술대회 논문집
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    • pp.266-268
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    • 2003
  • The neon liquefier by using GM cryocooler is designed and in process of manufacturing for the cooling of 100 hp high temperature superconductor (HTS) motor. It was used the principle of thermosyphon that the rotor of the motor is cooled by the latent heat of liquidized neon. The cold-box was designed to minimize heat loss by conduction, convection, radiation. Two heat exchanger were made to liquefy neon by the direct contact of neon gas on the cold head. As a first stage of our project, evaporation apparatus will be setup in the inner field of the cold-box and then the performance of neon liquefier will be test.

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소형 수소액화기 설계 및 운전에 관한 연구 (Design and Operation of a Small-Scale Hydrogen Liquefier)

  • 백종훈;강상우;강형묵;나다니엘 갈소;김서영;오인환
    • 한국수소및신에너지학회논문집
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    • 제26권2호
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    • pp.105-113
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    • 2015
  • In order to accelerate hydrogen society in current big renewable energy trend, it is very important that hydrogen can be transported and stored as a fuel in efficient and economical fashion. In this perspective, liquid hydrogen can be considered as one of the most prospective storage methods that can bring early arrival of the hydrogen society by its high gravimetric energy density. In this study, a small-scale hydrogen liquefier has been designed and developed to demonstrate direct hydrogen liquefaction technology. Gifford-McMahon (GM) cryocooler was employed to cool warm hydrogen gas to normal boiling point of hydrogen at 20K. Various cryogenic insulation technologies such as double walled vacuum vessels and multi-layer insulation were used to minimize heat leak from ambient. A liquid nitrogen assisted precooler, two ortho-para hydrogen catalytic converters, and highly efficient heat pipe were adapted to achieve the target liquefaction rate of 1L/hr. The liquefier has successfully demonstrated more than 1L/hr of hydrogen liquefaction. The system also has demonstrated its versatile usage as a very efficient 150L liquid hydrogen storage tank.

LonWorks를 이용한 액체헬륨 제조장치의 원격감시 및 제어 (Remote Monitoring and Control of Helium Liquefier Using LonWorks Network System)

  • 이정민;조재근;전정섭;유준
    • 대한전자공학회:학술대회논문집
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    • 대한전자공학회 2003년도 하계종합학술대회 논문집 V
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    • pp.2613-2616
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    • 2003
  • This paper presents a realization of LonWorks communication based remote monitoring and control system for old-dated Helium Liquefier to be automated in operation and data acquisition. Through Inn nodes, tank level, valve position, gasbag level and temperatures are collected and valve position is adjusted by step motor control. Also, field data acquired can be monitored at a remote site through LAN.

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포항 방사광가속기용 초전도 장치개발을 위한 헬륨 액화시설의 응용 (Application of He Liquefier for Development of SC Devices at Pohang Light Source)

  • 박인수;손영욱;김형균;김경렬;정진화
    • 한국초전도저온공학회:학술대회논문집
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    • 한국초전도저온공학회 2002년도 학술대회 논문집
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    • pp.378-381
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    • 2002
  • The helium liquefier was installed for 7.5 T superconducting wiggler, which is a source of synchrotron radiation, in Pohang Accelerator Laboratory (PAL) in 1995. It is MODEL 1410 fabricated by LINDE (old PSI America) of which capacity is about 17 liter per hour in normal mode and 47 liter per hour with liquid nitrogen pre-cooling. In addition to SC wiggler, we are anticipating that some devices related to electron accelerator are to be upgraded with superconducting application in order to improve the quality of photon beam.

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FDM에서 SLICE INTERVAL이 시작품의 표면에 미치는 영향 (The Influence of Surface Roughness on Slice Interval Adjustment at FDM)

  • 하만경;전재억
    • 한국공작기계학회논문집
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    • 제11권4호
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    • pp.68-74
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    • 2002
  • The FD process is analogous to the direct piston extrusion process where the cold feed filament acts as a piston extruding the molten filament from the heated liquefier through a nozzle. The extruded filament is deposited on top of futureless platform, where the liquefier and the nozzle move in X and Y direction control by computer based on the part geometry. After the first layer, the Z platform indexes down and the next layer get deposited on top of the first layer. the layer by layer building process introduces surface problem. This paper describes effect of slice interval of the parts built by fused deposition modelling rapid prototyping system.

ICT 기반의 휘발성 유기 화합물(VoC) 액화기 통합관리시스템 개발 (Development of a Volatile organic Compounds(VoCs) Liquefier on Integrated Management System based on ICT)

  • 김관형
    • 한국정보통신학회논문지
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    • 제19권6호
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    • pp.1301-1306
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    • 2015
  • 본 논문은 실생활에서 낭비되는 다양한 에너지 손실 중 주유소, 세탁소 등에서 손실되는 휘발성 유기화합물 (VoCs : Volatile organic Compounds)을 재활용하는 장치를 지능화하고 자동화 하는데 있다. 또한, 지그비(zigbee) 모듈 및 TCP/IP 통신기술을 활용한 ICT(Information Communication Technology) 기술을 도입하여 액화기를 원격지에서 모니터링하고 관리할 수 있는 통합관리시스템을 제시한다. 뿐만아니라, 안드로이드(android) 기반의 스마트 앱(App.)를 개발하여 원격지에서 관리할 수 있는 서비스 모델을 제시하고자 한다. 본 논문의 구성은 MCU 기반의 지능형 액화기 제어시스템의 구성과 지그비(zigbee) 기반의 브릿지(bridge) 모듈내부에 구현되는 통신 프로토콜을 제시한다. 통합관리시스템의 모바일 서비스를 위하여 안드로이드(android) 기반의 스마트 앱의 개발과 액화기 원격지 관리용 DB 서버(MS SQL 2012)와 웹서버(OS:Windows 2008)를 제시한다.

수소액화 예냉용 소형 스털링 극저온 냉동기 특성 연구 (A Study on Stirling Cryocooler for Precooling Hydrogen Liquefier)

  • 박성제;고준석;홍용주;김효봉;염한길;인세환
    • 한국수소및신에너지학회논문집
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    • 제27권6호
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    • pp.651-659
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    • 2016
  • Korea Institute of Machinery & Materials (KIMM) has developed a high efficient Stirling cryocooler with moving magnet linear compressor for precooling hydrogen liquefier and cooling high temperature superconductor (HTS) devices, such as superconductor cable and superconductor fault current limiters. Hydrogen liquefier and HTS electric devices require cryocooler with cooling capacity of hundred watts to kilowatts at 77 K. The compressor in the Stirling cryocooler uses opposed moving magnet linear motors to drive opposed pistons. High efficient Stirling cryocooler is designed by SAGE-software, manufactured and tested systematically. A cooling capacity of 1 kW at 77 K with an electric input power of 9.6 kW has been analyzed. But prototype test results of the Stirling cryocooler have the cooling capacity of 0.65 kW at 76.8 K with an electric input power of 8.1 kW. And then, 21.5% Carnot COP (Coefficient of performance) of the prototype Stirling cryocooler is achieved. The comparison analysis between SAGE-model and experimental results has shown the direction for further design optimization of the Stirling cryocooler.

극저온냉동기 예냉 수소액화기의 기초설계 (Basic design of hydrogen liquefier precooled by cryogenic refirgerator)

  • 김승현;장호명;강병하
    • 설비공학논문집
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    • 제9권3호
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    • pp.389-400
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    • 1997
  • A thermodynamic cycle analysis is performed for refrigerator-precooled Linde-Hampson hydrogen liquefiers, including catalysts for the ortho-to-para(o-p) conversion. three different configurations of the liquefying system, depending upon the method of the o-p conversion, are selected for the analysis. After some simple and justifiable models are introduced, a general analysis program to predict the liquid yield and the figure of merit(FOM) is developed with incorporating the commercial computer code for the hydrogen properties. The discussion is focused on the effect of the two primary design parameters-the precooling temperature and the high pressrure of hydrogen. When the precooling temperature is in the range between 45 and 60 K, the optimal high pressure for the maximal liquid yield is found to be in the range between 100 to 140 bar, regardless of the o-p conversion. However, the FOM can be maximized at slightly smaller values of high pressures. It is remarkable to observe that the lower precooling temperatures are favorable since both the liquid yield and the FOM can be obtained without compressing hygrogen to extremely high pressures.

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Basic Design of Hydrogen Liquefier Precooled by Cryogenic Refrigerator

  • Kim, Seung-Hyun;Chang, Ho-Myung;Kang, Byung-Ha
    • International Journal of Air-Conditioning and Refrigeration
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    • 제6권
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    • pp.124-135
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    • 1998
  • A thermodynamic cycle analysis is performed for refrigerator-precooled Linde-Hampson hydrogen liquefiers, including catalysts for the ortho-to-para conversion. Three different configurations of the liquefying system, depending upon the method of the o-p conversion, are selected for the analysis. After some simplifying and justifiable assumptions are made, a general analysis program to predict the liquid yield and the figure of merit (FOM) is developed with incorporating the commercial computer code for the thermodynamic properties of hydrogen. The discussion is focused on the effect of the two primary design parameters - the precooling temperature and the high pressure of the cycle. When the precooling temperature is in a range between 45 and 60 K, the optimal high pressure for the maximal liquid yield is found to be about 100 to 140 bar, regardless of the ortho-to-para conversion. However, the FOM can be maximized at slightly lower high pressures, 75 to 130 bar. It is concluded that the good performance of the precooling refrigerator is significant in the liquefiers, because at low precooling temperatures high values of the liquid yield and the FOM can be achieved without compression of gas to a very high pressure.

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