BR0210416A - Método para recuperação de petróleo de um reservatório natural de petróleo - Google Patents

Método para recuperação de petróleo de um reservatório natural de petróleo

Info

Publication number
BR0210416A
BR0210416A BR0210416-4A BR0210416A BR0210416A BR 0210416 A BR0210416 A BR 0210416A BR 0210416 A BR0210416 A BR 0210416A BR 0210416 A BR0210416 A BR 0210416A
Authority
BR
Brazil
Prior art keywords
natural
nitrogen
oil
rich stream
produce
Prior art date
Application number
BR0210416-4A
Other languages
English (en)
Other versions
BRPI0210416B1 (pt
Inventor
Gareth David Huntley Shaw
Roger Johansen
Original Assignee
Pet Oil & Gas Corp S Africa
Statoil Asa
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 Pet Oil & Gas Corp S Africa, Statoil Asa filed Critical Pet Oil & Gas Corp S Africa
Publication of BR0210416A publication Critical patent/BR0210416A/pt
Publication of BRPI0210416B1 publication Critical patent/BRPI0210416B1/pt

Links

Classifications

    • E—FIXED CONSTRUCTIONS
    • E21—EARTH DRILLING; MINING
    • E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/166—Injecting a gaseous medium; Injecting a gaseous medium and a liquid medium
    • E21B43/168—Injecting a gaseous medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
    • F25J3/04012—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling
    • F25J3/0403—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling of nitrogen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
    • F25J3/04109—Arrangements of compressors and /or their drivers
    • F25J3/04115—Arrangements of compressors and /or their drivers characterised by the type of prime driver, e.g. hot gas expander
    • F25J3/04121—Steam turbine as the prime mechanical driver
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04527—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general
    • F25J3/04539—Integration with an oxygen consuming unit, e.g. glass facility, waste incineration or oxygen based processes in general for the H2/CO synthesis by partial oxidation or oxygen consuming reforming processes of fuels
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04521—Coupling of the air fractionation unit to an air gas-consuming unit, so-called integrated processes
    • F25J3/04563—Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating
    • F25J3/04569—Integration with a nitrogen consuming unit, e.g. for purging, inerting, cooling or heating for enhanced or tertiary oil recovery

Abstract

"MéTODO PARA RECUPERAçãO DE PETRóLEO DE UM RESERVATóRIO NATURAL DE PETRóLEO". Método para recuperação de petróleo de um reservatório natural de petróleo que inclui as etapas de separar ar para produzir uma corrente rica em oxigênio e uma corrente rica em nitrogênio, proporcionar uma corrente de gás natural e alimentar pelo menos parte da corrente rica em oxigênio e da corrente de gás natural a uma instalação de liquefação química ou GTL ("gas-to-liquid") para produzir produtos hidrocarbonetos e calor. O calor produzido na instalação de liquefação química é utilizado para produzir energia para pressurizar o nitrogênio na corrente rica em nitrogênio para produzir uma corrente rica em nitrogênio pressurizada. A corrente rica em nitrogênio pressurizada é feita passar para um reservatório natural de petróleo para melhorar a recuperação de petróleo do reservatório.
BRPI0210416A 2001-06-15 2002-06-12 método para recuperação de petróleo de um reservatório natural de petróleo, método de modificação de um processo de recuperação aumentada de petróleo, método de modificação de uma instalação de recuperação melhorada de petróleo, instalação para a recuperação melhorada de petróleo, instalação modificada para a recuperação melhorada de petróleo BRPI0210416B1 (pt)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ZA200104939 2001-06-15
PCT/IB2002/002159 WO2002103157A1 (en) 2001-06-15 2002-06-12 Process for the recovery of oil from a natural oil reservoir

Publications (2)

Publication Number Publication Date
BR0210416A true BR0210416A (pt) 2004-08-17
BRPI0210416B1 BRPI0210416B1 (pt) 2017-04-25

Family

ID=25589202

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0210416A BRPI0210416B1 (pt) 2001-06-15 2002-06-12 método para recuperação de petróleo de um reservatório natural de petróleo, método de modificação de um processo de recuperação aumentada de petróleo, método de modificação de uma instalação de recuperação melhorada de petróleo, instalação para a recuperação melhorada de petróleo, instalação modificada para a recuperação melhorada de petróleo

Country Status (9)

Country Link
US (1) US7077202B2 (pt)
CN (1) CN1323222C (pt)
BR (1) BRPI0210416B1 (pt)
CA (1) CA2447677C (pt)
EA (1) EA005363B1 (pt)
EG (1) EG23345A (pt)
NO (1) NO333365B1 (pt)
WO (1) WO2002103157A1 (pt)
ZA (1) ZA200308708B (pt)

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WO2005005773A2 (en) * 2003-07-14 2005-01-20 The Energy Research Institute A process for enhanced recovery of crude oil from oil wells using novel microbial consortium
US9605522B2 (en) * 2006-03-29 2017-03-28 Pioneer Energy, Inc. Apparatus and method for extracting petroleum from underground sites using reformed gases
US8123827B2 (en) 2007-12-28 2012-02-28 Greatpoint Energy, Inc. Processes for making syngas-derived products
WO2009086407A2 (en) 2007-12-28 2009-07-09 Greatpoint Energy, Inc. Steam generating slurry gasifier for the catalytic gasification of a carbonaceous feedstock
US8652222B2 (en) 2008-02-29 2014-02-18 Greatpoint Energy, Inc. Biomass compositions for catalytic gasification
CA2718295C (en) 2008-04-01 2013-06-18 Greatpoint Energy, Inc. Processes for the separation of methane from a gas stream
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KR101290423B1 (ko) 2008-12-30 2013-07-29 그레이트포인트 에너지, 인크. 촉매된 석탄 미립자의 제조 방법
CN102639435A (zh) 2009-12-17 2012-08-15 格雷特波因特能源公司 整合的强化采油方法
US20110146978A1 (en) * 2009-12-17 2011-06-23 Greatpoint Energy, Inc. Integrated enhanced oil recovery process
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US9145524B2 (en) 2012-01-27 2015-09-29 General Electric Company System and method for heating a gasifier
CN102606122B (zh) * 2012-03-15 2015-09-23 中国海洋石油总公司 一种用于稠油油藏的多元热流体生产工艺以及热采工艺
CN102606121B (zh) * 2012-03-15 2015-07-22 中国海洋石油总公司 一种用于稠油油藏的多元热流体生产工艺以及热采工艺
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KR101576781B1 (ko) 2012-10-01 2015-12-10 그레이트포인트 에너지, 인크. 응집된 미립자 저등급 석탄 공급원료 및 그의 용도
EP2735696A1 (en) * 2012-11-27 2014-05-28 Shell Internationale Research Maatschappij B.V. Method and system for enhancing natural gas production
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Also Published As

Publication number Publication date
EA005363B1 (ru) 2005-02-24
ZA200308708B (en) 2004-09-13
US20040149438A1 (en) 2004-08-05
CA2447677A1 (en) 2002-12-27
CN1513079A (zh) 2004-07-14
BRPI0210416B1 (pt) 2017-04-25
CA2447677C (en) 2008-08-26
EG23345A (en) 2004-12-28
EA200400046A1 (ru) 2004-04-29
WO2002103157A1 (en) 2002-12-27
CN1323222C (zh) 2007-06-27
US7077202B2 (en) 2006-07-18
NO333365B1 (no) 2013-05-13
NO20035504D0 (no) 2003-12-10

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B06A Patent application procedure suspended [chapter 6.1 patent gazette]
B06A Patent application procedure suspended [chapter 6.1 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B09Y Publication of grant cancelled [chapter 9.1.2 patent gazette]
B09A Decision: intention to grant [chapter 9.1 patent gazette]
B16A Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]
B21F Lapse acc. art. 78, item iv - on non-payment of the annual fees in time

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B24J Lapse because of non-payment of annual fees (definitively: art 78 iv lpi, resolution 113/2013 art. 12)

Free format text: EM VIRTUDE DA EXTINCAO PUBLICADA NA RPI 2623 DE 13-04-2021 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDA A EXTINCAO DA PATENTE E SEUS CERTIFICADOS, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013.