NO20180948A1 - Intermediate fluid type vaporizer - Google Patents

Intermediate fluid type vaporizer Download PDF

Info

Publication number
NO20180948A1
NO20180948A1 NO20180948A NO20180948A NO20180948A1 NO 20180948 A1 NO20180948 A1 NO 20180948A1 NO 20180948 A NO20180948 A NO 20180948A NO 20180948 A NO20180948 A NO 20180948A NO 20180948 A1 NO20180948 A1 NO 20180948A1
Authority
NO
Norway
Prior art keywords
intermediate fluid
liquid
flow channels
flow
heat exchanger
Prior art date
Application number
NO20180948A
Other languages
English (en)
Inventor
Shinji Egashira
Original Assignee
Kobe Steel Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from PCT/JP2016/088414 external-priority patent/WO2017115723A1/ja
Application filed by Kobe Steel Ltd filed Critical Kobe Steel Ltd
Publication of NO20180948A1 publication Critical patent/NO20180948A1/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C9/00Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F17C9/02Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
    • F28D3/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits with tubular conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/08Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0302Heat exchange with the fluid by heating
    • F17C2227/0309Heat exchange with the fluid by heating using another fluid
    • F17C2227/0316Water heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2260/00Heat exchangers or heat exchange elements having special size, e.g. microstructures
    • F28F2260/02Heat exchangers or heat exchange elements having special size, e.g. microstructures having microchannels

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

An intermediate fluid type vaporizer 10 is equipped with: an intermediate fluid evaporator El that evaporates at least a part of a Liquid intermediate fluid M through heat exchange between seawater and the intermediate fluid M; and an LNG evaporator E2 that vaporizes LNG by condensing the intermediate fluid evaporated by the intermediate fluid evaporator El and causes vaporized NG to flow out. The LNG evaporator E2 is configured by a stack-type heat exchanger having a stacked body which is formed with a first flow channel that is a channel for the flow of the intermediate fluid M and a second flow channel that is a channel for the flow of the LNG. The stack-type heat exchanger is inst a lied in a posture where the first flow channels extend in an up-and-Down direction or in a direction tilted relative to the up-and-down direction so that the Intermediate fluid M flows down in the first flow channels due to gravity.
NO20180948A 2015-12-28 2018-07-05 Intermediate fluid type vaporizer NO20180948A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP2015256407 2015-12-28
JP2016246384A JP6839975B2 (ja) 2015-12-28 2016-12-20 中間媒体式気化器
PCT/JP2016/088414 WO2017115723A1 (ja) 2015-12-28 2016-12-22 中間媒体式気化器

Publications (1)

Publication Number Publication Date
NO20180948A1 true NO20180948A1 (en) 2018-07-05

Family

ID=59272107

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20180948A NO20180948A1 (en) 2015-12-28 2018-07-05 Intermediate fluid type vaporizer

Country Status (5)

Country Link
JP (1) JP6839975B2 (no)
KR (1) KR20180098341A (no)
CN (1) CN108369074A (no)
NO (1) NO20180948A1 (no)
SG (1) SG11201805050WA (no)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6868587B2 (ja) * 2018-03-30 2021-05-12 株式会社神戸製鋼所 中間媒体式気化器
CN110080846A (zh) * 2018-04-23 2019-08-02 江苏科技大学 一种带lng冷能利用功能的整体式中间介质汽化器及发电系统
WO2020105658A1 (ja) * 2018-11-22 2020-05-28 住友精密工業株式会社 拡散接合型熱交換器
JP6767546B1 (ja) * 2019-07-02 2020-10-14 株式会社神戸製鋼所 液化天然ガス気化器及び冷水供給方法
WO2021235337A1 (ja) * 2020-05-22 2021-11-25 株式会社神戸製鋼所 中間媒体式熱交換器
JP7411601B2 (ja) 2020-06-19 2024-01-11 株式会社神戸製鋼所 中間媒体式熱交換器
JP2023000414A (ja) * 2021-06-17 2023-01-04 千代田化工建設株式会社 液化炭酸ガス昇温設備および液化炭酸ガス昇温方法
CN115479209B (zh) * 2022-11-15 2023-03-10 无锡特莱姆气体设备有限公司 一种高效节能的中间介质气化器

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4734213U (no) * 1971-05-08 1972-12-16
JPS535207A (en) * 1976-07-05 1978-01-18 Osaka Gas Co Ltd Vaporizer of liquefied natural gas
JPS5955272U (ja) * 1982-09-25 1984-04-11 住友精密工業株式会社 液化ガス用熱交換器
JPS59117999A (ja) * 1982-12-23 1984-07-07 Kyodo Sanso Kk 低温液化ガスの冷熱回収装置
JPH0633970B2 (ja) * 1989-09-12 1994-05-02 東京瓦斯株式会社 液化天然ガスの冷熱回収用熱交換器
JPH08291899A (ja) * 1995-04-20 1996-11-05 Chubu Electric Power Co Inc 液化天然ガスの気化装置及びその冷却待機保持方法
JP3676604B2 (ja) * 1999-02-04 2005-07-27 株式会社神戸製鋼所 中間媒体式気化器及び当該気化器を用いた天然ガスの供給方法
JP2003214777A (ja) * 2002-01-21 2003-07-30 Yazaki Corp 液化ガス蒸発装置
US6622519B1 (en) * 2002-08-15 2003-09-23 Velocys, Inc. Process for cooling a product in a heat exchanger employing microchannels for the flow of refrigerant and product
JP2005282951A (ja) * 2004-03-30 2005-10-13 Institute Of Tsukuba Liaison Co Ltd 一体型積層構造熱交換器
JP5221070B2 (ja) * 2007-07-26 2013-06-26 株式会社豊田中央研究所 積層型流路要素の製造方法及び積層型流路要素
CN202328324U (zh) * 2011-09-23 2012-07-11 航天科工哈尔滨风华有限公司 管壳式中间介质气化器
JP5943619B2 (ja) * 2012-01-31 2016-07-05 株式会社神戸製鋼所 積層型熱交換器及び熱交換システム
KR101376531B1 (ko) * 2012-11-22 2014-03-19 주식회사 코헥스 천연가스 추진선박용 액화천연가스 기화 시스템
CN103822092B (zh) * 2014-01-27 2016-02-17 中国船舶重工集团公司第七一一研究所 板壳式中间流体型气化器

Also Published As

Publication number Publication date
JP6839975B2 (ja) 2021-03-10
KR20180098341A (ko) 2018-09-03
JP2017120125A (ja) 2017-07-06
CN108369074A (zh) 2018-08-03
SG11201805050WA (en) 2018-07-30

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