AR055990A1 - Proceso integrado para producir hidrocarburos - Google Patents

Proceso integrado para producir hidrocarburos

Info

Publication number
AR055990A1
AR055990A1 ARP060103067A AR055990A1 AR 055990 A1 AR055990 A1 AR 055990A1 AR P060103067 A ARP060103067 A AR P060103067A AR 055990 A1 AR055990 A1 AR 055990A1
Authority
AR
Argentina
Prior art keywords
steam
gas
optionally
normally
hydrocarbon
Prior art date
Application number
Other languages
English (en)
Inventor
Thian Hoey Tio
Wilhelmus Johannes Fr Scholten
Original Assignee
Shell Int Research
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 Shell Int Research filed Critical Shell Int Research
Publication of AR055990A1 publication Critical patent/AR055990A1/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1022—Fischer-Tropsch products
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4012—Pressure

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

Un método para iniciar un proceso para producir hidrocarburos normalmente gaseosos, líquidos y opcionalmente, normalmente solidos a partir de una fuete de hidrocarburo que incluye las siguientes etapas: (1) Producir vapor de alta presion (HP), preferiblemente vapor HP sobrecalentado, por medio de al menos un generador de turbina de gas y opcionalmente una o más calderas a las cuales se vierte una fuete de hidrocarburos; (2) Reducir la presion de al menos parte del vapor HP producido segun la etapa 1 a un vapor de presion de medio (HP); (3) utilizar al menos parte del vapor MP producido segun la etapa 2 para operar un compresor; (4) utilizar el compresor para operar uno o más medios para comprimir y opcionalmente separar un gas que contiene oxígeno; (5) Utilizar al menos parte del gas que contiene oxígeno para convertir una fuente de hidrocarburo en gas de síntesis; (6) Convertir el gas de síntesis producido segun la etapa 5 exotérmicamente al rango de hidrocarburos normalmente gaseosos, normalmente líquidos, y opcionalmente normalmente productos hidrocarburos solidos en la reaccion de Fischer-Tropach; (7) Controlar la temperatura de reaccion de la etapa 6 por intercambio de calor indirecto del medio de reaccion con agua; el agua se convierte en vapor saturado (vapor FT); (8) Separar los productos hidrocarburo producidos en la etapa 6 en una corriente de productos liviano (que incluye cualquier gas de síntesis sin convertir y al menos parte de productos hidrocarburos normalmente gaseosos) y corriente de productos pesado (que incluye el producto hidrocarburo normalmente solido y normalmente líquido) (9) Verter al menos parte de la corriente de producto liviano a uno o más generadores de turbina de gas para formar gas de combustion y expandir dicho gas de combustion a través de una cámara de expansion del generador de turbina de gas para formar gas de combustion caliente y energía; (10) Calentar el agua caldera fuente por intercambio de calor con gas de combustion caliente para producir vapor de alta presion adicional (HP), preferiblemente sobrecalentado; (11) Enfriar y/o condensar al menos una parte del vapor producido en la etapa 10 de un intercambiador de calor contra al menos una parte del vapor Ft producido en la etapa 7 para producir vapor MP adicional para utilizar para generar energía eléctrica y/o mecánica para las etapas 1 a 10; y opcionalmente (12) reducir la presion de al menos parte del vapor HP sobrecalentado producido segun la etapa 10 a un vapor de presion de medio (MP) para utilizar en las etapas anteriores.
ARP060103067 2005-07-20 2006-07-18 Proceso integrado para producir hidrocarburos AR055990A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP05254505 2005-07-20

Publications (1)

Publication Number Publication Date
AR055990A1 true AR055990A1 (es) 2007-09-12

Family

ID=35457194

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP060103067 AR055990A1 (es) 2005-07-20 2006-07-18 Proceso integrado para producir hidrocarburos

Country Status (7)

Country Link
EP (1) EP1904422A1 (es)
CN (1) CN101228101B (es)
AR (1) AR055990A1 (es)
AU (1) AU2006271759B2 (es)
MY (1) MY145801A (es)
WO (1) WO2007009951A1 (es)
ZA (1) ZA200800030B (es)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7939953B2 (en) * 2008-04-16 2011-05-10 Schlumberger Technology Corporation Micro scale fischer-tropsch and oxygenate synthesis process startup unit
US9156691B2 (en) 2011-04-20 2015-10-13 Expander Energy Inc. Process for co-producing commercially valuable products from byproducts of heavy oil and bitumen upgrading process
US9169443B2 (en) 2011-04-20 2015-10-27 Expander Energy Inc. Process for heavy oil and bitumen upgrading
US9266730B2 (en) 2013-03-13 2016-02-23 Expander Energy Inc. Partial upgrading process for heavy oil and bitumen
CA2818322C (en) 2013-05-24 2015-03-10 Expander Energy Inc. Refinery process for heavy oil and bitumen
WO2015068087A1 (en) 2013-11-07 2015-05-14 Sasol Technology Proprietary Limited Method and plant for co-generation of heat and power
WO2015068088A1 (en) 2013-11-07 2015-05-14 Sasol Technology Proprietary Limited Method and plant for co-generation of heat and power
AP2016009201A0 (en) 2013-11-07 2016-05-31 Sasol Tech (Proprietary) Ltd Method and plant for co-generation of heat and power
WO2018015479A1 (en) 2016-07-22 2018-01-25 Shell Internationale Research Maatschappij B.V. Molybdenum-vanadium-niobium-ceria-based catalyst for oxidative dehydrogenation of alkanes and/or alkene oxidation
MY197616A (en) 2016-11-07 2023-06-28 Shell Int Research Method of producing hydrocarbons

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5733941A (en) * 1996-02-13 1998-03-31 Marathon Oil Company Hydrocarbon gas conversion system and process for producing a synthetic hydrocarbon liquid
EP1156026A1 (en) * 2000-05-19 2001-11-21 Shell Internationale Researchmaatschappij B.V. Process for the production of liquid hydrocarbons
AU2002226622A1 (en) * 2001-02-01 2002-08-12 Sasol Technology (Proprietary) Limited Production of hydrocarbon products
MY137714A (en) 2001-05-29 2009-02-27 Shell Int Research Method to start a process for hydrocarbons
US6794417B2 (en) * 2002-06-19 2004-09-21 Syntroleum Corporation System and method for treatment of water and disposal of contaminants produced by converting lighter hydrocarbons into heavier hydrocarbon

Also Published As

Publication number Publication date
CN101228101B (zh) 2011-12-21
CN101228101A (zh) 2008-07-23
MY145801A (en) 2012-04-30
EP1904422A1 (en) 2008-04-02
AU2006271759B2 (en) 2009-10-29
AU2006271759A1 (en) 2007-01-25
WO2007009951A1 (en) 2007-01-25
ZA200800030B (en) 2009-09-30

Similar Documents

Publication Publication Date Title
AR055990A1 (es) Proceso integrado para producir hidrocarburos
RU2434145C2 (ru) Способ и система для производства энергии из теплового источника
CA2713799C (en) Method for operating a thermodynamic circuit, as well as a thermodynamic circuit
WO2018068431A1 (zh) 分级蒸发联合循环蒸汽动力装置
PT1613841E (pt) Processo e dispositivo de realização de um ciclo termodinâmico
BR0206827A (pt) Processos integrados para produção de produtos de hidrocarbonetos e energia, e para produção de gás de sìntese e energia
BR0303324A (pt) Sistema e método para geração de eletricidade e energia a partir de fontes de calor residual e solar
JPH112106A (ja) 有効エネルギーへの熱変換方法およびその装置
WO2020220727A1 (zh) 联合循环动力装置
BRPI0908109A2 (pt) Procedimento para gerar energia mediante ciclos térmicos com vapor de pressão elevada e temperatura moderada
Zhao et al. Transcritical carbon dioxide power cycle for waste heat recovery: A roadmap analysis from ideal cycle to real cycle with case implementation
CN104727867B (zh) 中低温余热的利用方法及其降压吸热式蒸汽动力循环系统
US7316105B2 (en) Steam power plant
KR20060069852A (ko) 증기 발전기
JP6741758B2 (ja) ガス・蒸気・コンバインドサイクル発電所の運転方法
RU2562745C1 (ru) Способ утилизации тепловой энергии, вырабатываемой тепловой электрической станцией
CN204627689U (zh) 一种液体降压吸热式蒸汽动力循环系统
RU2562735C1 (ru) Способ утилизации тепловой энергии, вырабатываемой тепловой электрической станцией
JP2018534465A (ja) ガス・蒸気・コンバインドサイクル発電所の運転方法、並びに、ガス・蒸気・コンバインドサイクル発電所
Stachel et al. Influence of the type of working fluid in the lower cycle and superheated steam parameters in the upper cycle on effectiveness of operation of binary power plant
JP5441844B2 (ja) 発電システム
RU2562725C1 (ru) Способ утилизации тепловой энергии, вырабатываемой тепловой электрической станцией
RU2562736C1 (ru) Способ утилизации тепловой энергии, вырабатываемой тепловой электрической станцией
RU2569292C1 (ru) Способ утилизации тепловой энергии, вырабатываемой тепловой электрической станцией
RU2007128681A (ru) Способ получения и устройство для осуществления этого способа

Legal Events

Date Code Title Description
FA Abandonment or withdrawal