AR128005A1 - PROCEDURE FOR TREATMENT OF A FUEL CONTAINING SULFIDE COMPOUNDS - Google Patents

PROCEDURE FOR TREATMENT OF A FUEL CONTAINING SULFIDE COMPOUNDS

Info

Publication number
AR128005A1
AR128005A1 ARP220103480A ARP220103480A AR128005A1 AR 128005 A1 AR128005 A1 AR 128005A1 AR P220103480 A ARP220103480 A AR P220103480A AR P220103480 A ARP220103480 A AR P220103480A AR 128005 A1 AR128005 A1 AR 128005A1
Authority
AR
Argentina
Prior art keywords
fuel
procedure
hydrogen
reactor
brought
Prior art date
Application number
ARP220103480A
Other languages
Spanish (es)
Inventor
Sophie Couderc
Marie Dehlinger
Adrien Gomez
Damien Hudebine
Marie Marion
- Fecant Antoine Claire
Original Assignee
Ifp Energies Now
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 Ifp Energies Now filed Critical Ifp Energies Now
Publication of AR128005A1 publication Critical patent/AR128005A1/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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
    • 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
    • C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
    • C10G21/06—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
    • C10G21/12—Organic compounds only
    • C10G21/20—Nitrogen-containing compounds
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds
    • C10G45/34—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
    • C10G45/36—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/38—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum or tungsten metals, or compounds thereof
    • 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
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/06—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a selective hydrogenation of the diolefins
    • 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
    • C10G2300/1044—Heavy gasoline or naphtha having a boiling range of about 100 - 180 °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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/201—Impurities
    • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
    • 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
    • C10G2300/4081—Recycling aspects

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

Abstract

Procedimiento de tratamiento de un combustible que contiene los compuestos sulfurosos, las olefinas y las diolefinas, que el procedimiento comprende al menos las siguientes etapas: a) se pone en contacto en al menos un reactor, el combustible, el hidrógeno y un catalizador de hidrodesulfuración que comprende un soporte de óxido y una fase activa que comprende un metal del grupo VIB y un metal del grupo VIII; b) se pone en contacto en al menos un reactor, el efluente resultante de la etapa a), el hidrógeno y un catalizador de hidrodesulfuración que comprende un soporte de óxido y una fase activa constituida por al menos un metal del grupo VIII; c) se envía el efluente resultante de la etapa b) a un matraz de separación que funciona a una presión comprendida entre 1,0 y 2,0 MPa para obtener una fracción gaseosa que contiene el H₂S y el hidrógeno y una fracción líquida que contiene el combustible desulfurado y una fracción de H₂S disuelto; d) se envía la citada fracción líquida obtenida en la etapa c) a una columna de estabilización para obtener en cabeza un flujo que comprende el H₂S residual y los compuestos hidrocarbonados en C₄⁻ y en el fondo un combustible estabilizado; e) se recicla al menos en parte la fracción gaseosa obtenida al final de la etapa c) hacia al menos una de las etapas a) y/o b).Procedure for treating a fuel containing sulfur compounds, olefins and diolefins, which the procedure comprises at least the following stages: a) the fuel, hydrogen and a hydrodesulfurization catalyst are brought into contact in at least one reactor. comprising an oxide support and an active phase comprising a group VIB metal and a group VIII metal; b) in at least one reactor, the effluent resulting from step a), hydrogen and a hydrodesulfurization catalyst comprising an oxide support and an active phase constituted by at least one group VIII metal, are brought into contact; c) the effluent resulting from step b) is sent to a separation flask that operates at a pressure between 1.0 and 2.0 MPa to obtain a gaseous fraction containing H₂S and hydrogen and a liquid fraction containing the desulfurized fuel and a fraction of dissolved H₂S; d) the aforementioned liquid fraction obtained in step c) is sent to a stabilization column to obtain at the top a flow that comprises the residual H₂S and the hydrocarbon compounds in C₄⁻ and at the bottom a stabilized fuel; e) the gas fraction obtained at the end of step c) is recycled at least in part towards at least one of steps a) and/or b).

ARP220103480A 2021-12-20 2022-12-16 PROCEDURE FOR TREATMENT OF A FUEL CONTAINING SULFIDE COMPOUNDS AR128005A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR2114038A FR3130834A1 (en) 2021-12-20 2021-12-20 Process for treating a gasoline containing sulfur compounds

Publications (1)

Publication Number Publication Date
AR128005A1 true AR128005A1 (en) 2024-03-20

Family

ID=80786455

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP220103480A AR128005A1 (en) 2021-12-20 2022-12-16 PROCEDURE FOR TREATMENT OF A FUEL CONTAINING SULFIDE COMPOUNDS

Country Status (8)

Country Link
EP (1) EP4453146A1 (en)
KR (1) KR20240125579A (en)
CN (1) CN118414411A (en)
AR (1) AR128005A1 (en)
AU (1) AU2022417857A1 (en)
FR (1) FR3130834A1 (en)
MX (1) MX2024007283A (en)
WO (1) WO2023117531A1 (en)

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6409913B1 (en) 1996-02-02 2002-06-25 Exxonmobil Research And Engineering Company Naphtha desulfurization with reduced mercaptan formation
US6231754B1 (en) 1996-02-02 2001-05-15 Exxon Research And Engineering Company High temperature naphtha desulfurization using a low metal and partially deactivated catalyst
FR2797639B1 (en) 1999-08-19 2001-09-21 Inst Francais Du Petrole PROCESS FOR PRODUCING LOW SULFUR ESSENCE
EP1285047A4 (en) 2000-04-18 2003-07-23 Exxonmobil Res & Eng Co Selective hydroprocessing and mercaptan removal
FR2811328B1 (en) 2000-07-06 2002-08-23 Inst Francais Du Petrole PROCESS INCLUDING TWO STAGES OF GASOLINE HYDRODESULFURATION AND AN INTERMEDIATE REMOVAL OF THE H2S FORMED DURING THE FIRST STAGE
US6736962B1 (en) 2000-09-29 2004-05-18 Exxonmobil Research And Engineering Company Catalytic stripping for mercaptan removal (ECB-0004)
US6960291B2 (en) 2001-06-19 2005-11-01 Exxonmobil Research And Engineering Company Naphtha desulfurization method
US7799210B2 (en) 2004-05-14 2010-09-21 Exxonmobil Research And Engineering Company Process for removing sulfur from naphtha
US7507328B2 (en) 2004-12-27 2009-03-24 Exxonmobile Research And Engineering Company Selective hydrodesulfurization and mercaptan decomposition process with interstage separation
FR2888583B1 (en) * 2005-07-18 2007-09-28 Inst Francais Du Petrole NOVEL METHOD OF DESULFURIZING OLEFINIC ESSENCES FOR LIMITING THE MERCAPTAN CONTENT
US20070114156A1 (en) 2005-11-23 2007-05-24 Greeley John P Selective naphtha hydrodesulfurization with high temperature mercaptan decomposition
ITTO20120525A1 (en) 2012-06-15 2013-12-16 Sabelt Spa CONNECTION BUCKLE FOR SEAT BELTS, IN PARTICULAR FOR COMPETITION VEHICLES
FR3099175B1 (en) * 2019-07-23 2021-07-16 Ifp Energies Now PROCESS FOR THE PRODUCTION OF A GASOLINE WITH LOW SULFUR AND MERCAPTANS

Also Published As

Publication number Publication date
EP4453146A1 (en) 2024-10-30
MX2024007283A (en) 2024-06-28
AU2022417857A1 (en) 2024-05-23
KR20240125579A (en) 2024-08-19
FR3130834A1 (en) 2023-06-23
CN118414411A (en) 2024-07-30
WO2023117531A1 (en) 2023-06-29

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