• Title/Summary/Keyword: 액화수소

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수소액화 및 극저온 저장기술

  • Baek, Jong-Hun;Kim, Seo-Yeong
    • Journal of the KSME
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    • v.53 no.4
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    • pp.38-43
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    • 2013
  • 이 글에서는 수소 연료전지차, 우주개발용 로켓추진체의 연료공급기술로 활용이 예상되는 수소액화 기술 및 영하 253도의 극저온 액체수소의 저장기술에 대해 살펴보고 액화사이클 및 극저온 액화수소 저장용기로의 열침입을 차단하기 위한 다양한 단열기술에 대해 기술한다.

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Establishing the Safety of the Hydrogen Industry Through the Revision of Domestic Liquefied Hydrogen Safety Standards (국내 액화수소 안전기준 제·개정을 통한 수소산업 안전성 확립)

  • Kim, Hyun-Jin;Song, Boe-Hee;Tak, Song-Su;Joe, Hoe-Yeon;Kang, Seung-Kyu
    • Journal of the Korean Institute of Gas
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    • v.25 no.6
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    • pp.98-105
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    • 2021
  • Currently, the government's announcement of the Korean version of the New Deal Comprehensive Plan ('20.7.14), expanding the supply of hydrogen production and charging facilities, and major companies are rapidly building related facilities such as liquefied hydrogen plants and charging stations. However, safety standards for production, storage facilities, transportation, and utilization of liquefied hydrogen value chains in Korea are insufficient, and safety technologies and safety standards over the entire period of liquefied hydrogen are urgently needed. Accordingly, the Korea Gas Safety Corporation is trying to realize a safe hydrogen economy in Korea by enacting safety standards over the entire period, including liquefied hydrogen plants

Design and Analysis for Hydrogen Liquefaction Process Using LNG Cold Energy (LNG냉열이용 수소액화 공정해석 및 설계)

  • Yun, Sang-Kook
    • Journal of the Korean Institute of Gas
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    • v.15 no.3
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    • pp.1-5
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    • 2011
  • For the hydrogen liquefaction, the large amount of energy is consumed, because precooling, liquefaction and ortho/para conversion heats should be eliminated. In this paper the basic design and thermal analysis are carried out to reduce the energy consumption by using LNG cold energy for precooling process in hydrogen liquefaction processes. The LNG cold energy utilization for hydrogen precooling enables not only to get energy saving for liquefaction, but to recover the wasted cold energy to sea water at the LNG terminal. The results show that the energy saving rate for liquefaction using LNG cold energy is almost 75% of current industrial hydrogen liquefaction plant. The demand flow-rate of LNG is only 15T/D for 1T/D hydrogen liquefaction.

Technical Analysis and Future Development of Liquefied Hydrogen Carriers (액화수소 산적 운반선의 기술성 분석 및 향후 개발 과제)

  • Lee, Hyunyong;Kang, Hokeun;Roh, Gilltae;Jung, Inchul
    • Journal of the Korean Society of Marine Environment & Safety
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    • v.28 no.2
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    • pp.361-369
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    • 2022
  • Countries worldwide are shifting to a hydrogen economy to respond to stringent environmental regulations, and the transport of hydrogen between countries is expected to increase in the mid- to long-term. Hydrogen is traded between countries in different forms, such as ammonia, liquid hydrogen, and LOHC (Liquid Organic Hydrogen Carrier), on account of the renewable energy resources in exporting countries, the type of hydrogen use in importing countries, and the technological maturity; however, it is not traded only in a singular form. As marine transportation of ammonia and LOHC is a relatively mature technology compared to that of liquid hydrogen, in this article, we analyzed the technical feasibility of liquid hydrogen carriers while identifying detailed technologies required for their future development and securing possible designs through various technical alternatives.

Development of Standards for the Use of Liquefied Hydrogen for Ship Using Risk Assessment Techniques (위험성 평가기법을 활용한 선박용 액화수소 사용시설 기준개발)

  • Young-taeg, Hur;Hye-Soo, Han;Gyoung-min, Noh;Hee-soo, Chung;Chung-keun, Chae
    • Journal of the Korean Institute of Gas
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    • v.26 no.6
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    • pp.52-58
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    • 2022
  • According to the government's roadmap for revitalizing the hydrogen economy, various industries carry out projects using liquefied hydrogen as an energy source. However, safety standards necessary for operational demonstration projects are not prepared in Korea, thus, it is necessary to prepare safety standards as soon as possible. Therefore, in order to secure the safety of liquefied hydrogen instrumentation and handling facilities, it is necessary to prepare safety standards that comprehensively consider the risk of liquefied hydrogen. This study aims to prioritize safety standard items using ETA, FMEA, and AHP, which are risk assessment techniques, to present the feasibility of selecting safety standard items.

Design and Performance Test of a Direct Cooling Equipment for Hydrogen Liquefaction (수소액화용 직접냉각장치의 설계 및 성능시험)

  • Baik, Jong-Hoon;Kang, Byung-Ha;Chang, Ho-Myung
    • Transactions of the Korean hydrogen and new energy society
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    • v.7 no.2
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    • pp.121-128
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    • 1996
  • A direct cooling equipment for hydrogen liquefaction has been developed and tested. A direct cooling equipment consists of a liquefaction vessel, a radiation shield, a cryostat and a GM refrigerator. The cool-down and warm-up characteristics of the liquefaction apparatus have been investigated in detail. It is found that the hydrogen starts to be liquefied in the liquefaction vessel after 45 minutes of cool-down. The cool-down and warm-up tests of helium gas are also performed. The cool-down and warm-up characteristics of helium gas are found to be very different from those of hydrogen gas, since helium is not liquefied under the present operating conditions. When the liquefaction vessel is evacuated, natural convection phenomena of charged gas in liquefaction vessel can be removed. It is seen that the cool-down time of liquefaction vessel is substantially increased in vacuum environment.

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CFD procedure of Multi-phase flow to predict the trend of Boil-off for the various filling ratio of C-Type liquefied hydrogen tank subject to sloshing motion (슬로싱에 놓인 C-Type 액화수소 탱크의 적재율에 따른 BOG 발생량 경향 예측을 위한 다상 유동 CFD 해석 절차)

  • Jin-Ho Lee;Sung-Je Lee;Se-Yun Hwang;Jang Hyun Lee
    • Proceedings of the Korean Institute of Navigation and Port Research Conference
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    • 2022.06a
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    • pp.213-213
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    • 2022
  • 본 논문은 슬로싱(Sloshing) 거동에 놓인 극저온 액체수소 화물창의 BOG 예측을 위한 CFD 해석 절차를 다루고 있다. 특히, 적재율(Filling Ratio)에 따라 달라지는 열 유입과 그에 따른 액체수소의 기화 경향을 파악하기 위한 목적으로 수행되었다. 액체수소와 기체수소의 혼재에 의한 다상 열유동(Multiphase-Thermal flow) 특성을 반영하고 유동에 따른 강제 대류 현상을 열유속에 반영하기 위한 CFD 해석을 수행하였다. 다상 유동 모델의 정확성을 검증하기 위하여 슬로싱 실험의 압력 계측 값과 해석의 압력 값 및 자유수면(Free surface) 형상을 비교하였다. 소형 C-Type 독립형 액화수소 탱크를 대상으로 슬로싱 유동과 BOG 발생을 수치적으로 예측하였다. 해석 과정에서 VOF(Volume of fraction) 모델과 Eulerian 모델을 모두 적용하여, 액체수소에 유입되는 열 유속(Heat flux)의 예측 정확성을 비교하였다. 슬로싱 유무에 따라 액체수소에 유입되는 열 유속을 비교하여 슬로싱 유동의 포함 여부에 따른 BOG 발생량의 변화를 제시하였으며, 최종적으로 액체수소의 충전율(Filling ratio) 별로 BOG 발생량의 경향성을 제시하였다.

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A Study for Key Points of PSM to Guarantee the Safety of Liqufied Hydrogen Storage Tank (액화수소 저장탱크 안전성 확보를 위한 PSM 중점사항에 관한 연구)

  • Myoung Sun Wu;Chang Jun Lee
    • Korean Chemical Engineering Research
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    • v.61 no.1
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    • pp.74-79
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    • 2023
  • As the demand for hydrogen increases, the facilities for storing hydrogen has been important, and a few laws for hydrogen facilities should be complied. According to the Occupational Safety and Health Act in Korea, in case liquid hydrogen with a storage capacity of 5 tons or more is handled, a Process Safety Management (PSM) system should be complied. However, there are some standards which are not proper for flammable low-temperature liquefied substances on the current Occupational Safety and Health Act. In this study, 7 key points in process safey information and safety operation procedures among PSM components are suggested and how these key points should be improved is derived based on scientific analysis.

Improving Safety by Preparing Measures to Strengthen Safety Management for Special Hydrogen-Related Regulatory Projects (수소관련 규제특례사업 안전관리강화 방안 마련을 통한 안전성 제고)

  • Kim, Doe-Hyun;Han, Joo-Yeon;Tak, Song-Su;Joe, Hoe-Yeon
    • Journal of the Korean Institute of Gas
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    • v.25 no.6
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    • pp.106-110
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    • 2021
  • The emergence of new hydrogen-related technologies and new businesses has expanded the need to reorganize systems in related fields such as manufacturing liquefied hydrogen (charging), and manufacturing liquefied hydrogen storage tanks and containers, and special applications continue to increase. Accordingly, we intend to establish and implement measures to strengthen safety management to share the status of designation of special hydrogen-related regulatory projects and secure minimum safety.

Effects of ortho-para hydrogen conversion on hydrogen liquefaction performance (Ortho-para 수소변환이 수소액화성능에 미치는 영향)

  • 최항집;강병하;최영돈
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.12 no.2
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    • pp.131-139
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    • 2000
  • A direct hydrogen liquefaction equipment has been developed and tested, which consists of a GM refrigerator, a liquefaction vessel, a radiation shield, a cryostat, and an ortho-para converter with catalyst. The effect of ortho-para hydrogen conversion on the performance of hydrogen liquefaction has been investigated. The time needed for the hydrogen liquefaction process with hydrogen pressure charge of 4 atm was delayed to around 75 minutes, and the liquefied mass flow rate of the hydrogen was about 0.0150∼ 0.0205 g/s when the hydrogen was liquefied with the direct hydrogen liquefaction system considering ortho-para conversion. With ortho-para conversion, the liquefied mass flow rate decreased up to 20%. Considering ortho-para conversion, there were up to 30% increase in the work input per unit liquefied mass flow rate. When the ortho-para conversion was considered, FOM decreased to be about 0.031∼0.045.

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