APPARATUS FOR THE LIQUEFACTION OF NATURAL GAS AND METHODS RELATING TO SAME

An apparatus and method for producing liquefied natural gas. A liquefaction plant may be coupled to a source of unpurified natural gas, such as a natural gas pipeline at a pressure letdown station. A portion of the gas is drawn off and split into a process stream (154) and a cooling stream (152). Th...

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Hauptverfasser: WILDING, BRUCE M, PALMER, GARY L, BINGHAM, DENNIS N, TURNER, TERRY D, VRANICAR, JOHN J, RATERMAN, KEVIN T, MCKELLAR, MICHAEL G, KLINGER, KERRY M
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creator WILDING, BRUCE M
PALMER, GARY L
BINGHAM, DENNIS N
TURNER, TERRY D
VRANICAR, JOHN J
RATERMAN, KEVIN T
MCKELLAR, MICHAEL G
KLINGER, KERRY M
description An apparatus and method for producing liquefied natural gas. A liquefaction plant may be coupled to a source of unpurified natural gas, such as a natural gas pipeline at a pressure letdown station. A portion of the gas is drawn off and split into a process stream (154) and a cooling stream (152). The cooling stream (152) passes through a turbo expander (156) creating work output. A compressor (158) is driven by the work output and compresses the process stream. The compressed process stream is cooled, such as by the expanded cooling stream. The cooled, compressed process stream is divided into first and second portions with the first portion being expanded to liquefy the natural gas. A gas-Iiquid separator separates the vapor from the liquid natural gas. The second portion of the cooled, compressed process stream is also expanded and used to cool the compressed process stream. Additional features and techniques may be integrated with the liquefaction process including a water clean-up cycle and a carbon dioxide (CO2) clean-up cycle. L'invention concerne un appareil et un procédé de production de gaz naturel liquéfié. Une installation de liquéfaction peut être couplée à une source de gaz naturel non purifié, telle qu'un pipeline de gaz naturel au niveau d'une station de réduction de pression. Une partie du gaz est retirée et répartie en un flux de traitement (154) et en un flux de refroidissement (152). Celui-ci (152) passe à travers un turbo-extenseur (156) créant une production. Un compresseur (158) est entraîné par la production et comprime le flux de traitement. Le flux de traitement comprimé est refroidi par expansion du flux de refroidissement. Le flux de traitement refroidi et comprimé est réparti en des première et seconde parties, la première partie étant expansée aux fins de liquéfaction du gaz naturel. Un séparateur gaz-liquide sépare la vapeur du gaz naturel liquide. La seconde partie du flux de traitement refroidi et comprimé est également expansée et elle est utilisée pour refroidir le flux de traitement comprimé.
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A liquefaction plant may be coupled to a source of unpurified natural gas, such as a natural gas pipeline at a pressure letdown station. A portion of the gas is drawn off and split into a process stream (154) and a cooling stream (152). The cooling stream (152) passes through a turbo expander (156) creating work output. A compressor (158) is driven by the work output and compresses the process stream. The compressed process stream is cooled, such as by the expanded cooling stream. The cooled, compressed process stream is divided into first and second portions with the first portion being expanded to liquefy the natural gas. A gas-Iiquid separator separates the vapor from the liquid natural gas. The second portion of the cooled, compressed process stream is also expanded and used to cool the compressed process stream. Additional features and techniques may be integrated with the liquefaction process including a water clean-up cycle and a carbon dioxide (CO2) clean-up cycle. L'invention concerne un appareil et un procédé de production de gaz naturel liquéfié. Une installation de liquéfaction peut être couplée à une source de gaz naturel non purifié, telle qu'un pipeline de gaz naturel au niveau d'une station de réduction de pression. Une partie du gaz est retirée et répartie en un flux de traitement (154) et en un flux de refroidissement (152). Celui-ci (152) passe à travers un turbo-extenseur (156) créant une production. Un compresseur (158) est entraîné par la production et comprime le flux de traitement. Le flux de traitement comprimé est refroidi par expansion du flux de refroidissement. Le flux de traitement refroidi et comprimé est réparti en des première et seconde parties, la première partie étant expansée aux fins de liquéfaction du gaz naturel. Un séparateur gaz-liquide sépare la vapeur du gaz naturel liquide. La seconde partie du flux de traitement refroidi et comprimé est également expansée et elle est utilisée pour refroidir le flux de traitement comprimé.</description><language>eng ; fre</language><subject>ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL ; BLASTING ; CHEMISTRY ; COMBINED HEATING AND REFRIGERATION SYSTEMS ; DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OFGENERAL APPLICATION ; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED,LIQUEFIED, OR SOLIDIFIED GASES ; FIRELIGHTERS ; FIXED-CAPACITY GAS-HOLDERS ; FUELS ; FUELS NOT OTHERWISE PROVIDED FOR ; HEAT EXCHANGE IN GENERAL ; HEAT PUMP SYSTEMS ; HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT ; HEATING ; LIGHTING ; LIQUEFACTION SOLIDIFICATION OF GASES ; LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS ; LIQUEFIED PETROLEUM GAS ; LUBRICANTS ; MANUFACTURE OR STORAGE OF ICE ; MECHANICAL ENGINEERING ; METALLURGY ; MIXTURES BY PRESSURE AND COLD TREATMENT ; NATURAL GAS ; PEAT ; PERFORMING OPERATIONS ; PETROLEUM, GAS OR COKE INDUSTRIES ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; REFRIGERATION OR COOLING ; SEPARATION ; STORING OF DISTRIBUTING GASES OR LIQUIDS ; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K ; TECHNICAL GASES CONTAINING CARBON MONOXIDE ; TRANSPORTING ; VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED ORSOLIDIFIED GASES ; WEAPONS</subject><creationdate>2009</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20090707&amp;DB=EPODOC&amp;CC=CA&amp;NR=2473185C$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25542,76290</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&amp;date=20090707&amp;DB=EPODOC&amp;CC=CA&amp;NR=2473185C$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>WILDING, BRUCE M</creatorcontrib><creatorcontrib>PALMER, GARY L</creatorcontrib><creatorcontrib>BINGHAM, DENNIS N</creatorcontrib><creatorcontrib>TURNER, TERRY D</creatorcontrib><creatorcontrib>VRANICAR, JOHN J</creatorcontrib><creatorcontrib>RATERMAN, KEVIN T</creatorcontrib><creatorcontrib>MCKELLAR, MICHAEL G</creatorcontrib><creatorcontrib>KLINGER, KERRY M</creatorcontrib><title>APPARATUS FOR THE LIQUEFACTION OF NATURAL GAS AND METHODS RELATING TO SAME</title><description>An apparatus and method for producing liquefied natural gas. A liquefaction plant may be coupled to a source of unpurified natural gas, such as a natural gas pipeline at a pressure letdown station. A portion of the gas is drawn off and split into a process stream (154) and a cooling stream (152). The cooling stream (152) passes through a turbo expander (156) creating work output. A compressor (158) is driven by the work output and compresses the process stream. The compressed process stream is cooled, such as by the expanded cooling stream. The cooled, compressed process stream is divided into first and second portions with the first portion being expanded to liquefy the natural gas. A gas-Iiquid separator separates the vapor from the liquid natural gas. The second portion of the cooled, compressed process stream is also expanded and used to cool the compressed process stream. Additional features and techniques may be integrated with the liquefaction process including a water clean-up cycle and a carbon dioxide (CO2) clean-up cycle. L'invention concerne un appareil et un procédé de production de gaz naturel liquéfié. Une installation de liquéfaction peut être couplée à une source de gaz naturel non purifié, telle qu'un pipeline de gaz naturel au niveau d'une station de réduction de pression. Une partie du gaz est retirée et répartie en un flux de traitement (154) et en un flux de refroidissement (152). Celui-ci (152) passe à travers un turbo-extenseur (156) créant une production. Un compresseur (158) est entraîné par la production et comprime le flux de traitement. Le flux de traitement comprimé est refroidi par expansion du flux de refroidissement. Le flux de traitement refroidi et comprimé est réparti en des première et seconde parties, la première partie étant expansée aux fins de liquéfaction du gaz naturel. Un séparateur gaz-liquide sépare la vapeur du gaz naturel liquide. La seconde partie du flux de traitement refroidi et comprimé est également expansée et elle est utilisée pour refroidir le flux de traitement comprimé.</description><subject>ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL</subject><subject>BLASTING</subject><subject>CHEMISTRY</subject><subject>COMBINED HEATING AND REFRIGERATION SYSTEMS</subject><subject>DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OFGENERAL APPLICATION</subject><subject>FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED,LIQUEFIED, OR SOLIDIFIED GASES</subject><subject>FIRELIGHTERS</subject><subject>FIXED-CAPACITY GAS-HOLDERS</subject><subject>FUELS</subject><subject>FUELS NOT OTHERWISE PROVIDED FOR</subject><subject>HEAT EXCHANGE IN GENERAL</subject><subject>HEAT PUMP SYSTEMS</subject><subject>HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT</subject><subject>HEATING</subject><subject>LIGHTING</subject><subject>LIQUEFACTION SOLIDIFICATION OF GASES</subject><subject>LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS</subject><subject>LIQUEFIED PETROLEUM GAS</subject><subject>LUBRICANTS</subject><subject>MANUFACTURE OR STORAGE OF ICE</subject><subject>MECHANICAL ENGINEERING</subject><subject>METALLURGY</subject><subject>MIXTURES BY PRESSURE AND COLD TREATMENT</subject><subject>NATURAL GAS</subject><subject>PEAT</subject><subject>PERFORMING OPERATIONS</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</subject><subject>REFRIGERATION OR COOLING</subject><subject>SEPARATION</subject><subject>STORING OF DISTRIBUTING GASES OR LIQUIDS</subject><subject>SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><subject>TRANSPORTING</subject><subject>VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED ORSOLIDIFIED GASES</subject><subject>WEAPONS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2009</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZPByDAhwDHIMCQ1WcPMPUgjxcFXw8QwMdXVzdA7x9PdT8HdT8APKBjn6KLg7Bis4-rko-LqGePi7BCsEufo4hnj6uSuE-CsEO_q68jCwpiXmFKfyQmluBnk31xBnD93Ugvz41OKCxOTUvNSSeGdHIxNzY0MLU2djwioAk50sPQ</recordid><startdate>20090707</startdate><enddate>20090707</enddate><creator>WILDING, BRUCE M</creator><creator>PALMER, GARY L</creator><creator>BINGHAM, DENNIS N</creator><creator>TURNER, TERRY D</creator><creator>VRANICAR, JOHN J</creator><creator>RATERMAN, KEVIN T</creator><creator>MCKELLAR, MICHAEL G</creator><creator>KLINGER, KERRY M</creator><scope>EVB</scope></search><sort><creationdate>20090707</creationdate><title>APPARATUS FOR THE LIQUEFACTION OF NATURAL GAS AND METHODS RELATING TO SAME</title><author>WILDING, BRUCE M ; PALMER, GARY L ; BINGHAM, DENNIS N ; TURNER, TERRY D ; VRANICAR, JOHN J ; RATERMAN, KEVIN T ; MCKELLAR, MICHAEL G ; KLINGER, KERRY M</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_CA2473185C3</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; fre</language><creationdate>2009</creationdate><topic>ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL</topic><topic>BLASTING</topic><topic>CHEMISTRY</topic><topic>COMBINED HEATING AND REFRIGERATION SYSTEMS</topic><topic>DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OFGENERAL APPLICATION</topic><topic>FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED,LIQUEFIED, OR SOLIDIFIED GASES</topic><topic>FIRELIGHTERS</topic><topic>FIXED-CAPACITY GAS-HOLDERS</topic><topic>FUELS</topic><topic>FUELS NOT OTHERWISE PROVIDED FOR</topic><topic>HEAT EXCHANGE IN GENERAL</topic><topic>HEAT PUMP SYSTEMS</topic><topic>HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT</topic><topic>HEATING</topic><topic>LIGHTING</topic><topic>LIQUEFACTION SOLIDIFICATION OF GASES</topic><topic>LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS</topic><topic>LIQUEFIED PETROLEUM GAS</topic><topic>LUBRICANTS</topic><topic>MANUFACTURE OR STORAGE OF ICE</topic><topic>MECHANICAL ENGINEERING</topic><topic>METALLURGY</topic><topic>MIXTURES BY PRESSURE AND COLD TREATMENT</topic><topic>NATURAL GAS</topic><topic>PEAT</topic><topic>PERFORMING OPERATIONS</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</topic><topic>REFRIGERATION OR COOLING</topic><topic>SEPARATION</topic><topic>STORING OF DISTRIBUTING GASES OR LIQUIDS</topic><topic>SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><topic>TRANSPORTING</topic><topic>VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED ORSOLIDIFIED GASES</topic><topic>WEAPONS</topic><toplevel>online_resources</toplevel><creatorcontrib>WILDING, BRUCE M</creatorcontrib><creatorcontrib>PALMER, GARY L</creatorcontrib><creatorcontrib>BINGHAM, DENNIS N</creatorcontrib><creatorcontrib>TURNER, TERRY D</creatorcontrib><creatorcontrib>VRANICAR, JOHN J</creatorcontrib><creatorcontrib>RATERMAN, KEVIN T</creatorcontrib><creatorcontrib>MCKELLAR, MICHAEL G</creatorcontrib><creatorcontrib>KLINGER, KERRY M</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>WILDING, BRUCE M</au><au>PALMER, GARY L</au><au>BINGHAM, DENNIS N</au><au>TURNER, TERRY D</au><au>VRANICAR, JOHN J</au><au>RATERMAN, KEVIN T</au><au>MCKELLAR, MICHAEL G</au><au>KLINGER, KERRY M</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>APPARATUS FOR THE LIQUEFACTION OF NATURAL GAS AND METHODS RELATING TO SAME</title><date>2009-07-07</date><risdate>2009</risdate><abstract>An apparatus and method for producing liquefied natural gas. A liquefaction plant may be coupled to a source of unpurified natural gas, such as a natural gas pipeline at a pressure letdown station. A portion of the gas is drawn off and split into a process stream (154) and a cooling stream (152). The cooling stream (152) passes through a turbo expander (156) creating work output. A compressor (158) is driven by the work output and compresses the process stream. The compressed process stream is cooled, such as by the expanded cooling stream. The cooled, compressed process stream is divided into first and second portions with the first portion being expanded to liquefy the natural gas. A gas-Iiquid separator separates the vapor from the liquid natural gas. The second portion of the cooled, compressed process stream is also expanded and used to cool the compressed process stream. Additional features and techniques may be integrated with the liquefaction process including a water clean-up cycle and a carbon dioxide (CO2) clean-up cycle. L'invention concerne un appareil et un procédé de production de gaz naturel liquéfié. Une installation de liquéfaction peut être couplée à une source de gaz naturel non purifié, telle qu'un pipeline de gaz naturel au niveau d'une station de réduction de pression. Une partie du gaz est retirée et répartie en un flux de traitement (154) et en un flux de refroidissement (152). Celui-ci (152) passe à travers un turbo-extenseur (156) créant une production. Un compresseur (158) est entraîné par la production et comprime le flux de traitement. Le flux de traitement comprimé est refroidi par expansion du flux de refroidissement. Le flux de traitement refroidi et comprimé est réparti en des première et seconde parties, la première partie étant expansée aux fins de liquéfaction du gaz naturel. Un séparateur gaz-liquide sépare la vapeur du gaz naturel liquide. La seconde partie du flux de traitement refroidi et comprimé est également expansée et elle est utilisée pour refroidir le flux de traitement comprimé.</abstract><oa>free_for_read</oa></addata></record>
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subjects ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE ORUNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL
BLASTING
CHEMISTRY
COMBINED HEATING AND REFRIGERATION SYSTEMS
DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OFGENERAL APPLICATION
FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED,LIQUEFIED, OR SOLIDIFIED GASES
FIRELIGHTERS
FIXED-CAPACITY GAS-HOLDERS
FUELS
FUELS NOT OTHERWISE PROVIDED FOR
HEAT EXCHANGE IN GENERAL
HEAT PUMP SYSTEMS
HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
HEATING
LIGHTING
LIQUEFACTION SOLIDIFICATION OF GASES
LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS
LIQUEFIED PETROLEUM GAS
LUBRICANTS
MANUFACTURE OR STORAGE OF ICE
MECHANICAL ENGINEERING
METALLURGY
MIXTURES BY PRESSURE AND COLD TREATMENT
NATURAL GAS
PEAT
PERFORMING OPERATIONS
PETROLEUM, GAS OR COKE INDUSTRIES
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
REFRIGERATION OR COOLING
SEPARATION
STORING OF DISTRIBUTING GASES OR LIQUIDS
SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BYSUBCLASSES C10G, C10K
TECHNICAL GASES CONTAINING CARBON MONOXIDE
TRANSPORTING
VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED ORSOLIDIFIED GASES
WEAPONS
title APPARATUS FOR THE LIQUEFACTION OF NATURAL GAS AND METHODS RELATING TO SAME
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