MX2016013897A - Proceso de produccion de gasolina que comprende una etapa de isomerizacion seguida de al menos dos etapas de separacion. - Google Patents

Proceso de produccion de gasolina que comprende una etapa de isomerizacion seguida de al menos dos etapas de separacion.

Info

Publication number
MX2016013897A
MX2016013897A MX2016013897A MX2016013897A MX2016013897A MX 2016013897 A MX2016013897 A MX 2016013897A MX 2016013897 A MX2016013897 A MX 2016013897A MX 2016013897 A MX2016013897 A MX 2016013897A MX 2016013897 A MX2016013897 A MX 2016013897A
Authority
MX
Mexico
Prior art keywords
separation steps
production method
step followed
petrol
isomerisation step
Prior art date
Application number
MX2016013897A
Other languages
English (en)
Inventor
PIGOURIER Jérôme
Prevost Isabelle
Watripont Laurent
Martin Pierre-Yves
Original Assignee
Axens
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 Axens filed Critical Axens
Publication of MX2016013897A publication Critical patent/MX2016013897A/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
    • C10G61/00—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen
    • C10G61/02—Treatment of naphtha by at least one reforming process and at least one process of refining in the absence of hydrogen plural serial stages only
    • 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
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • 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
    • C10G7/00—Distillation of hydrocarbon oils
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/06—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
    • 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
    • C10G2300/104—Light gasoline having a boiling range of about 20 - 100 °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
    • C10G2300/10—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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2200/00—Components of fuel compositions
    • C10L2200/04—Organic compounds
    • C10L2200/0407—Specifically defined hydrocarbon fractions as obtained from, e.g. a distillation column
    • C10L2200/0415—Light distillates, e.g. LPG, naphtha
    • C10L2200/0423—Gasoline
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
    • C10L2290/543—Distillation, fractionation or rectification for separating fractions, components or impurities during preparation or upgrading of a fuel

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

Abstract

La presente invención describe un proceso de producción de gasolina con alto índice de octano mediante isomerización de un corte de nafta ligero, que incluye dos etapas de separación situadas corriente abajo de la etapa de reacción, que permite mejorar la eficacia energética del proceso.
MX2016013897A 2014-04-29 2015-04-20 Proceso de produccion de gasolina que comprende una etapa de isomerizacion seguida de al menos dos etapas de separacion. MX2016013897A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1453841A FR3020374B1 (fr) 2014-04-29 2014-04-29 Procede de production d'essence comprenant une etape d'isomerisation suivie d'au moins deux etapes de separation.
PCT/EP2015/058498 WO2015165763A1 (fr) 2014-04-29 2015-04-20 Procede de production d'essence comprenant une etape d'isomerisation suivie d'au moins deux etapes de separation

Publications (1)

Publication Number Publication Date
MX2016013897A true MX2016013897A (es) 2017-03-09

Family

ID=51063678

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2016013897A MX2016013897A (es) 2014-04-29 2015-04-20 Proceso de produccion de gasolina que comprende una etapa de isomerizacion seguida de al menos dos etapas de separacion.

Country Status (7)

Country Link
US (1) US10113121B2 (es)
EP (1) EP3137583B1 (es)
CN (1) CN106661460B (es)
FR (1) FR3020374B1 (es)
MX (1) MX2016013897A (es)
SA (1) SA516380157B1 (es)
WO (1) WO2015165763A1 (es)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5741906A (en) * 1996-11-15 1998-04-21 Air Products And Chemicals, Inc. Production of triethylenediamine using surface acidity deactivated zeolite catalysts
US10653975B2 (en) * 2018-04-30 2020-05-19 Gtc Technology Us Llc Network of dividing-wall columns in complex processing units
CN114901616B (zh) * 2019-12-30 2024-11-08 沙特基础工业全球技术公司 处理戊烷的方法和系统
US11648519B2 (en) * 2020-01-22 2023-05-16 Phillips 66 Company Systems for converting light paraffins to alcohols
CN115397553B (zh) * 2020-04-16 2024-10-18 凯洛格·布朗及鲁特有限公司 用于烃的异构化和产品分离的脱异丁烷塔中的集成稳定器
CN111500317A (zh) * 2020-04-24 2020-08-07 河北新启元能源技术开发股份有限公司 一种异构化汽油生产工艺
US12398330B2 (en) 2021-05-19 2025-08-26 Indian Oil Corporation Limited Process for isomerization of C5—C7 hydrocarbons in light naphtha range

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2905619A (en) * 1956-06-28 1959-09-22 Universal Oil Prod Co Upgrading gasoline
US3060116A (en) * 1959-11-06 1962-10-23 Socony Mobil Oil Co Inc Combination reforming and cracking process
US3131235A (en) * 1960-11-23 1964-04-28 Universal Oil Prod Co Simultaneous isomerization of pentane and hexane with selective fractionation
JPS5490122A (en) * 1977-12-27 1979-07-17 Chiyoda Chem Eng & Constr Co Ltd Distillation of multi-component hydrocarbon composition
US5994607A (en) * 1996-02-05 1999-11-30 Institut Francais Du Petrole Paraffin isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones
FR2828205B1 (fr) * 2001-08-06 2004-07-30 Inst Francais Du Petrole Procede d'isomerisation d'une coupe c5-c8 mettant en oeuvre deux reacteurs en parallele
US20100025221A1 (en) * 2008-07-31 2010-02-04 Purdue Research Foundation Process for distillation of multicomponent mixtures into five product streams

Also Published As

Publication number Publication date
CN106661460B (zh) 2020-04-03
WO2015165763A1 (fr) 2015-11-05
CN106661460A (zh) 2017-05-10
US20170044447A1 (en) 2017-02-16
SA516380157B1 (ar) 2020-11-18
EP3137583A1 (fr) 2017-03-08
FR3020374B1 (fr) 2017-10-27
US10113121B2 (en) 2018-10-30
EP3137583B1 (fr) 2020-03-25
FR3020374A1 (fr) 2015-10-30

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