AR055990A1 - INTEGRATED PROCESS TO PRODUCE HYDROCARBONS - Google Patents

INTEGRATED PROCESS TO PRODUCE HYDROCARBONS

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
Spanish (es)
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/en

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.A method to initiate a process to produce normally gaseous, liquid and optionally, normally solid hydrocarbons from a hydrocarbon source that includes the following steps: (1) Produce high pressure (HP) steam, preferably superheated HP steam, by means of at least one gas turbine generator and optionally one or more boilers to which a hydrocarbon source is poured; (2) Reduce the pressure of at least part of the HP vapor produced according to step 1 to a medium pressure vapor (HP); (3) use at least part of the MP steam produced according to step 2 to operate a compressor; (4) use the compressor to operate one or more means to compress and optionally separate an oxygen-containing gas; (5) Use at least part of the oxygen-containing gas to convert a hydrocarbon source into synthesis gas; (6) Convert the synthesis gas produced according to step 5 exothermically to the range of normally gaseous, normally liquid hydrocarbons, and optionally normally solid hydrocarbons in the Fischer-Tropach reaction; (7) Control the reaction temperature of step 6 by indirect heat exchange of the reaction medium with water; water becomes saturated steam (FT steam); (8) Separate the hydrocarbon products produced in step 6 into a stream of light products (which includes any unconverted synthesis gas and at least part of normally gaseous hydrocarbon products) and heavy product stream (which includes the normally solid hydrocarbon product and normally liquid) (9) Pour at least part of the light product stream into one or more gas turbine generators to form combustion gas and expand said combustion gas through an expansion chamber of the gas turbine generator to form hot combustion gas and energy; (10) Heating the source boiler water by heat exchange with hot combustion gas to produce additional high pressure (HP) steam, preferably superheated; (11) Cooling and / or condensing at least a part of the steam produced in step 10 of a heat exchanger against at least a part of the steam Ft produced in step 7 to produce additional MP steam to be used to generate electric power and / or mechanics for stages 1 to 10; and optionally (12) reduce the pressure of at least part of the superheated HP steam produced according to step 10 to a medium pressure vapor (MP) for use in the previous stages.

ARP060103067 2005-07-20 2006-07-18 INTEGRATED PROCESS TO PRODUCE HYDROCARBONS AR055990A1 (en)

Applications Claiming Priority (1)

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

Publications (1)

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

Family

ID=35457194

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP060103067 AR055990A1 (en) 2005-07-20 2006-07-18 INTEGRATED PROCESS TO PRODUCE HYDROCARBONS

Country Status (7)

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

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
AP2016009199A0 (en) 2013-11-07 2016-05-31 Sasol Tech Pty Ltd 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
AP2016009200A0 (en) 2013-11-07 2016-05-31 Sasol Tech Pty Ltd Method and plant for co-generation of heat and power
CA3030951A1 (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
US10597585B2 (en) 2016-11-07 2020-03-24 Shell Oil Company 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
WO2002060841A2 (en) 2001-02-01 2002-08-08 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 (en) 2011-12-21
AU2006271759B2 (en) 2009-10-29
AU2006271759A1 (en) 2007-01-25
EP1904422A1 (en) 2008-04-02
ZA200800030B (en) 2009-09-30
MY145801A (en) 2012-04-30
WO2007009951A1 (en) 2007-01-25
CN101228101A (en) 2008-07-23

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