BRPI0510476A - process for preparing a diesel - Google Patents

process for preparing a diesel

Info

Publication number
BRPI0510476A
BRPI0510476A BRPI0510476-9A BRPI0510476A BRPI0510476A BR PI0510476 A BRPI0510476 A BR PI0510476A BR PI0510476 A BRPI0510476 A BR PI0510476A BR PI0510476 A BRPI0510476 A BR PI0510476A
Authority
BR
Brazil
Prior art keywords
diesel
fraction
preparing
catalyst
isolating
Prior art date
Application number
BRPI0510476-9A
Other languages
Portuguese (pt)
Inventor
Jan Lodewijk Maria Dierickx
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
Priority claimed from PCT/EP2004/050931 external-priority patent/WO2004106462A1/en
Application filed by Shell Int Research filed Critical Shell Int Research
Publication of BRPI0510476A publication Critical patent/BRPI0510476A/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
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
    • C10G2/32—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts
    • C10G2/33—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used
    • C10G2/331—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals
    • C10G2/332—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen with the use of catalysts characterised by the catalyst used containing group VIII-metals of the iron-group
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • C10G11/05—Crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1037—Hydrocarbon fractions
    • C10G2300/1048—Middle distillates
    • C10G2300/1059—Gasoil having a boiling range of about 330 - 427 °C
    • 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
    • C10G2300/4006—Temperature
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/06—Gasoil

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)
  • Crystallography & Structural Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PROCESSO PARA PREPARAR UM GASóLEO. Processo para preparar um gasóleo, por (a) isolamento de um produto de síntese de Fischer-Tropsch uma primeira fração de gasóleo e uma fração ebulindo acima da fração de gasóleo, (b) contato da fração mais pesada com um sistema catalítico compreendendo um catalisador, cujo catalisador compreende uma matriz ácida e uma peneira molecular de poro grande em um reator de coluna vertical em uma temperatura de entre 450<198>C e 650<198>C em um tempo de contato de entre 1 segundo e 10 segundos e em uma razão de catalisador para óleo de entre 2 kg/kg e 20 kg/kg, (c) isolamento do produto da etapa (b) e uma segunda fração de gasóleo; (d) combinação da primeira fração de gasóleo com o segundo gasóleo.PROCESS FOR PREPARING A GAS. A process for preparing a diesel by (a) isolating a Fischer-Tropsch synthesis product a first diesel fraction and a boiling fraction above the diesel fraction, (b) contacting the heavier fraction with a catalytic system comprising a catalyst , whose catalyst comprises an acid matrix and a large pore molecular sieve in a vertical column reactor at a temperature of between 450Â ° C and 650Â ° C at a contact time of between 1 second and 10 seconds and at a catalyst to oil ratio of between 2 kg / kg and 20 kg / kg, (c) isolating the product from step (b) and a second fraction of diesel; (d) combining the first fraction of diesel with the second diesel.

BRPI0510476-9A 2004-05-26 2005-05-25 process for preparing a diesel BRPI0510476A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
PCT/EP2004/050931 WO2004106462A1 (en) 2003-05-27 2004-05-26 Process to prepare a gasoline
EP04106189 2004-11-30
PCT/EP2005/052391 WO2005118747A1 (en) 2004-05-26 2005-05-25 Process to produce a gas oil by catalytic cracking of a fisher-tropsch product

Publications (1)

Publication Number Publication Date
BRPI0510476A true BRPI0510476A (en) 2007-11-06

Family

ID=38557244

Family Applications (1)

Application Number Title Priority Date Filing Date
BRPI0510476-9A BRPI0510476A (en) 2004-05-26 2005-05-25 process for preparing a diesel

Country Status (7)

Country Link
US (1) US20070227946A1 (en)
EP (1) EP1753841A1 (en)
JP (1) JP4955541B2 (en)
CN (1) CN1965059B (en)
BR (1) BRPI0510476A (en)
RU (1) RU2388791C2 (en)
WO (1) WO2005118747A1 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5988875B2 (en) 2009-10-22 2016-09-07 中国石油化工股▲ふん▼有限公司 Catalytic conversion method to increase cetane barrel of diesel fuel
EP2319900A1 (en) * 2009-11-02 2011-05-11 Shell Internationale Research Maatschappij B.V. Cracking process
WO2011051438A1 (en) * 2009-11-02 2011-05-05 Shell Internationale Research Maatschappij B.V. Cracking process
US20130030232A1 (en) * 2010-01-20 2013-01-31 Jx Nippon Oil & Energy Corporation Catalyst for production of monocyclic aromatic hydrocarbons and method of producing monocyclic aromatic hydrocarbons
WO2012051004A1 (en) * 2010-10-11 2012-04-19 Shell Oil Company A process for catalytic cracking a fischer-tropsch derived feedstock with heat balanced operation of the catalytic cracking system
JP5671412B2 (en) * 2011-05-26 2015-02-18 Ｊｘ日鉱日石エネルギー株式会社 Light oil composition and method for producing the same
US20130158138A1 (en) * 2011-12-15 2013-06-20 Chevron U.S.A. Inc. Integral synthesis gas conversion catalyst extrudates and methods for preparing and using same
JP6239584B2 (en) 2013-02-21 2017-11-29 Ｊｘｔｇエネルギー株式会社 Monocyclic aromatic hydrocarbon production method
CN106010585B (en) * 2016-06-23 2018-09-28 张启泰 Carbonization integral furnace is dried in environment protection type rotary formula multilayer destructive distillation
WO2023203895A1 (en) * 2022-04-18 2023-10-26 Ｅｎｅｏｓ株式会社 Fuel production apparatus and fuel production method
WO2023234212A1 (en) * 2022-05-31 2023-12-07 Ｅｎｅｏｓ株式会社 Method for producing hydrocarbon
WO2023234211A1 (en) * 2022-05-31 2023-12-07 Ｅｎｅｏｓ株式会社 Method for producing hydrocarbons

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3992474A (en) * 1975-12-15 1976-11-16 Uop Inc. Motor fuel production with fluid catalytic cracking of high-boiling alkylate
FR2362208A1 (en) * 1976-08-17 1978-03-17 Inst Francais Du Petrole PROCESS FOR VALUING EFFLUENTS OBTAINED IN FISCHER-TROPSCH TYPE SYNTHESES
US4471145A (en) * 1982-12-01 1984-09-11 Mobil Oil Corporation Process for syngas conversions to liquid hydrocarbon products utilizing zeolite Beta
US4684756A (en) * 1986-05-01 1987-08-04 Mobil Oil Corporation Process for upgrading wax from Fischer-Tropsch synthesis
GB9114390D0 (en) * 1991-07-03 1991-08-21 Shell Int Research Hydrocarbon conversion process and catalyst composition
US5481057A (en) * 1994-03-25 1996-01-02 Mobil Oil Corporation Alkylation with activated equilibrium FCC catalyst
US6296757B1 (en) * 1995-10-17 2001-10-02 Exxon Research And Engineering Company Synthetic diesel fuel and process for its production
FR2799202B1 (en) * 1999-09-30 2002-04-26 Inst Francais Du Petrole PROCESS FOR PRODUCING ESSENCES WITH IMPROVED OCTANE INDEX
BR0109793A (en) * 2000-04-03 2004-02-10 Chevron Usa Inc Integrated process for preparing isools from synthesis gas and distilled fuel composition
CN1123625C (en) * 2000-10-26 2003-10-08 中国石油化工股份有限公司 Process for treating and mixing residual oil
BR0207894A (en) * 2001-03-05 2004-06-22 Shell Int Research Process for the preparation of one or more hydrocarbon fuels, and hydrocarbon product
CN100587034C (en) * 2003-05-27 2010-02-03 国际壳牌研究有限公司 Process for preparing gasoline

Also Published As

Publication number Publication date
CN1965059B (en) 2010-06-16
WO2005118747A1 (en) 2005-12-15
RU2006146060A (en) 2008-07-10
EP1753841A1 (en) 2007-02-21
RU2388791C2 (en) 2010-05-10
US20070227946A1 (en) 2007-10-04
JP2008500418A (en) 2008-01-10
JP4955541B2 (en) 2012-06-20
CN1965059A (en) 2007-05-16

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Legal Events

Date Code Title Description
B07A Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]
B15I Others concerning applications: loss of priority
B12F Other appeals [chapter 12.6 patent gazette]
B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE A 11A ANUIDADE.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: EM VIRTUDE DO ARQUIVAMENTO PUBLICADO NA RPI 2385 DE 20-09-2016 E CONSIDERANDO AUSENCIA DE MANIFESTACAO DENTRO DOS PRAZOS LEGAIS, INFORMO QUE CABE SER MANTIDO O ARQUIVAMENTO DO PEDIDO DE PATENTE, CONFORME O DISPOSTO NO ARTIGO 12, DA RESOLUCAO 113/2013.