AR095952A1 - PRODUCTION OF COMPOSITIONS OF DISTILLED MEDIA HYDROCARBONS - Google Patents

PRODUCTION OF COMPOSITIONS OF DISTILLED MEDIA HYDROCARBONS

Info

Publication number
AR095952A1
AR095952A1 ARP140101430A ARP140101430A AR095952A1 AR 095952 A1 AR095952 A1 AR 095952A1 AR P140101430 A ARP140101430 A AR P140101430A AR P140101430 A ARP140101430 A AR P140101430A AR 095952 A1 AR095952 A1 AR 095952A1
Authority
AR
Argentina
Prior art keywords
product
stream
oligomerization
range
heavy
Prior art date
Application number
ARP140101430A
Other languages
Spanish (es)
Inventor
Richard Lucy Andrew
Original Assignee
Bp Plc
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 Bp Plc filed Critical Bp Plc
Publication of AR095952A1 publication Critical patent/AR095952A1/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
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
    • 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
    • C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/20—Organic compounds not containing metal atoms
    • C10G29/205—Organic compounds not containing metal atoms by reaction with hydrocarbons added to the hydrocarbon oil
    • 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
    • C10G50/00—Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
    • 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
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/12—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step
    • C10G69/126—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one polymerisation or alkylation step polymerisation, e.g. oligomerisation
    • 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
    • C10G2300/1088—Olefins
    • C10G2300/1092—C2-C4 olefins
    • 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
    • C10G2400/04—Diesel oil
    • 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
    • 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
    • C10G2400/08—Jet fuel

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Un proceso para la preparación de una composición de destilados medios de hidrocarburos a partir de etileno, donde dicho proceso comprende los siguientes pasos: (a) alimentar una composición de etileno a una zona de reacción de oligomerización que contiene un catalizador de oligomerización de níquel sobre un soporte para formar un producto de oligomerización A, donde la reacción de oligomerización se opera a una temperatura dentro del rango entre 30 y 300ºC y a una presión de por lo menos 10 barias; (b) separar una corriente de productos livianos B, una corriente de producto de destilado medio C y una corriente de productos pesados D del producto de oligomerización A, donde la corriente de producto liviano B comprende la fracción de producto de oligomerización A que entra en ebullición en el rango de puntos de ebullición de las monoolefinas C₂₋₈ y la corriente de producto de destilado medio C comprende una fracción de producto de oligomerización A que entra en ebullición a una temperatura sobre el rango de puntos de ebullición de la corriente de producto liviano B y por debajo del rango de puntos de ebullición de la corriente de productos pesados D, y donde la corriente de producto pesado D comprende la fracción de producto de oligomerización A que entra en ebullición a una temperatura sobre el rango de puntos de ebullición de las monoolefinas C₂₂; (c) reciclar por lo menos una porción de la corriente de productos livianos B ala zona de la reacción de oligomerización del paso (a) del proceso; (d) alimentar la corriente de producto pesado D y una composición de etileno a una zona de reacción de etenólisis para producir una corriente de producto de etenólisis E; (e) separar un producto de destilado medio F de la corriente de producto de etenólisis E; y (f) hidrogenar la corriente de producto de destilado medio C, donde la composición de destilados medios de hidrocarburos comprenden por lo menos una porción de la corriente de producto de destilado medio hidrogenado C y por lo menos una porción del producto de destilado medio F.A process for the preparation of a composition of hydrocarbon middle distillates from ethylene, wherein said process comprises the following steps: (a) feeding an ethylene composition to an oligomerization reaction zone containing a nickel oligomerization catalyst on a support to form an oligomerization product A, where the oligomerization reaction is operated at a temperature within the range between 30 and 300 ° C and at a pressure of at least 10 bar; (b) separating a stream of light products B, a stream of medium distillate product C and a stream of heavy products D from the oligomerization product A, where the stream of light product B comprises the fraction of oligomerization product A that enters boiling in the range of boiling points of the monoolefins C₂₋₈ and the medium distillate product stream C comprises a fraction of oligomerization product A that boils at a temperature over the range of boiling points of the product stream light B and below the boiling point range of the heavy product stream D, and where the heavy product stream D comprises the fraction of oligomerization product A that boils at a temperature over the boiling point range of Coo monoolefins; (c) recycle at least a portion of the stream of light products B to the oligomerization reaction zone of step (a) of the process; (d) feeding the heavy product stream D and an ethylene composition to an etheolysis reaction zone to produce a stream of ethenolysis product E; (e) separating a medium distillate product F from the etheolysis product stream E; and (f) hydrogenate the medium distillate product stream C, where the hydrocarbon middle distillate composition comprises at least a portion of the hydrogenated medium distillate product stream C and at least a portion of the middle distillate product F .

ARP140101430A 2013-03-28 2014-03-28 PRODUCTION OF COMPOSITIONS OF DISTILLED MEDIA HYDROCARBONS AR095952A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP13161794 2013-03-28

Publications (1)

Publication Number Publication Date
AR095952A1 true AR095952A1 (en) 2015-11-25

Family

ID=47997263

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP140101430A AR095952A1 (en) 2013-03-28 2014-03-28 PRODUCTION OF COMPOSITIONS OF DISTILLED MEDIA HYDROCARBONS

Country Status (2)

Country Link
AR (1) AR095952A1 (en)
WO (1) WO2014154798A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2660618T3 (en) 2015-01-19 2018-03-23 Evonik Degussa Gmbh Combined preparation of at least butene and octene from ethene
MX369759B (en) 2015-01-19 2019-11-20 Evonik Operations Gmbh Combined preparation of butene and octene from ethene.

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3647906A (en) * 1970-05-11 1972-03-07 Shell Oil Co Alpha-olefin production
EP2196444A1 (en) * 2008-12-11 2010-06-16 Total Petrochemicals Research Feluy Process to make alpha olefins from ethanol
FR2959752B1 (en) * 2010-05-06 2012-06-08 Inst Francais Du Petrole FLEXIBLE METHOD OF TRANSFORMING ETHANOL TO MEDIUM DISTILLATES USING A HOMOGENEOUS CATALYTIC SYSTEM AND A HETEROGENEOUS CATALYTIC SYSTEM
FR2959750B1 (en) * 2010-05-06 2013-02-15 Inst Francais Du Petrole PROCESS FOR PRODUCING KEROSENE FROM BIO-ETHANOL
US20120197053A1 (en) * 2010-09-21 2012-08-02 Synfuels International., Inc. System and method for the production of liquid fuels

Also Published As

Publication number Publication date
WO2014154798A1 (en) 2014-10-02

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