GB1348736A - Method of vaporizing and superheating a cryogenic fluid - Google Patents

Method of vaporizing and superheating a cryogenic fluid

Info

Publication number
GB1348736A
GB1348736A GB2274072A GB2274072A GB1348736A GB 1348736 A GB1348736 A GB 1348736A GB 2274072 A GB2274072 A GB 2274072A GB 2274072 A GB2274072 A GB 2274072A GB 1348736 A GB1348736 A GB 1348736A
Authority
GB
United Kingdom
Prior art keywords
gas
stages
stream
fed
turbines
Prior art date
Legal status (The legal status 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 status listed.)
Expired
Application number
GB2274072A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Black Sivalls and Bryson Inc
Original Assignee
Black Sivalls and Bryson Inc
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
Application filed by Black Sivalls and Bryson Inc filed Critical Black Sivalls and Bryson Inc
Publication of GB1348736A publication Critical patent/GB1348736A/en
Expired legal-status Critical Current

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
    • 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
    • F17C2265/00Effects achieved by gas storage or gas handling
    • F17C2265/05Regasification

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Treating Waste Gases (AREA)

Abstract

1348736 Revaporizing gases BLACK SIVALLS & BRYSON Inc 15 May 1972 [20 May 1971] 22740/72 Heading F4P In a method of vaporizing and heating a liquefied gas, e.g. LNG, a stream of the gas is vaporized in a heat exchanger 18 by a stream of ambient water, the gas stream 36 then being divided into two portions, one of which passes in heat exchange with the exhaust gases of a gas turbine in a series of stages, a further quantity of liquefied gas being added to the gas stream between each stage. In practice a pair of gas turbines 28, 30 are used, each having a heat exchanger 34, 52 for the exhaust gases. The second portion of the gas stream is fed via conduits 62, 64 through exchangers 68, 80 again in a series of stages, to cool the inlet air to the turbines. The two portions of gas are reunited in conduit 88, 90 which feeds the gas to a contactor 92 fed with liquefied gas via conduit 94 to provide a temperature control on the gas issuing via line 96. Some of the gas in conduit 88, 90 may be directed by line 98 to fuel the turbines 28, 30. As shown in Fig. 2, the gas stream 36 is divided into two portions 38, 40, the former being divided into equal portions 42, 44 by flow controllers 43, 45 and fed to the first stages 156 and 166 of exchangers 34, 52 through which passes the exhaust of turbines 28, 30. A stream of liquefied gas is added to the heated gas issuing from stages 156 and 166 via conduits 114, 116, 162 and 172, the amount being regulated by temperature-controlled valves 176 and 184, the combined streams being fed into second stages 158, 168 before the addition of further liquefied gas and then being fed to third stages 160, 170. The second portion 40 of the vaporized gas is similarly treated in exchangers 68, 80.
GB2274072A 1971-05-20 1972-05-15 Method of vaporizing and superheating a cryogenic fluid Expired GB1348736A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US14521771A 1971-05-20 1971-05-20

Publications (1)

Publication Number Publication Date
GB1348736A true GB1348736A (en) 1974-03-20

Family

ID=22512108

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2274072A Expired GB1348736A (en) 1971-05-20 1972-05-15 Method of vaporizing and superheating a cryogenic fluid

Country Status (7)

Country Link
US (1) US3726101A (en)
JP (1) JPS578360B1 (en)
CA (1) CA948983A (en)
DE (1) DE2224826A1 (en)
FR (1) FR2138762B1 (en)
GB (1) GB1348736A (en)
IT (1) IT955555B (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2164434B1 (en) * 1971-11-22 1974-01-04 Raffinage Cie Francaise
US4331129A (en) * 1979-07-05 1982-05-25 Columbia Gas System Service Corporation Solar energy for LNG vaporization
US4438729A (en) 1980-03-31 1984-03-27 Halliburton Company Flameless nitrogen skid unit
US4607489A (en) * 1985-05-21 1986-08-26 Mg Industries Method and apparatus for producing cold gas at a desired temperature
US5295350A (en) * 1992-06-26 1994-03-22 Texaco Inc. Combined power cycle with liquefied natural gas (LNG) and synthesis or fuel gas
US5456084A (en) * 1993-11-01 1995-10-10 The Boc Group, Inc. Cryogenic heat exchange system and freeze dryer
NO180426C (en) * 1995-03-16 1997-04-16 Kvaerner Moss Tech As Device for heat exchangers
DE19725822A1 (en) * 1997-06-18 1998-12-24 Linde Ag Method for operating a gas or steam turbine power plant
DE10160834B4 (en) 2001-12-11 2007-03-15 P21 - Power For The 21St Century Gmbh Device for vaporizing and overheating at least one medium and fuel cell system
US20060260330A1 (en) * 2005-05-19 2006-11-23 Rosetta Martin J Air vaporizor
ITMI20061149A1 (en) * 2006-06-14 2007-12-15 Eni Spa PROCEDURE AND PLANT FOR THE REGASIFICATION OF NATURAL LIQUEFIED GAS AND THE SUOM STORAGE
NO328260B1 (en) * 2006-06-20 2010-01-18 Aker Engineering & Technology Process and plant for re-gasification LNG
US8356487B2 (en) * 2007-09-07 2013-01-22 SPX Cooling Technologies Control system and method for vaporizer with heating tower
DE102009057055A1 (en) * 2009-12-04 2011-06-09 Linde Ag Process and apparatus for the evaporation of cryogenic media

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3154928A (en) * 1962-04-24 1964-11-03 Conch Int Methane Ltd Gasification of a liquid gas with simultaneous production of mechanical energy
US3438216A (en) * 1967-05-09 1969-04-15 Texas Eastern Trans Corp Cryogenic recovery vaporizer
US3552134A (en) * 1969-07-22 1971-01-05 Black Sivalls & Bryson Inc Process and apparatus for vaporizing liquefied natural gas

Also Published As

Publication number Publication date
CA948983A (en) 1974-06-11
FR2138762B1 (en) 1976-01-16
FR2138762A1 (en) 1973-01-05
DE2224826A1 (en) 1972-12-07
IT955555B (en) 1973-09-29
JPS578360B1 (en) 1982-02-16
US3726101A (en) 1973-04-10

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
732 Registration of transactions, instruments or events in the register (sect. 32/1977)
PCNP Patent ceased through non-payment of renewal fee