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WO2012015540A3 - Multi-stage hydroprocessing for the production of high octane naphtha - Google Patents

Multi-stage hydroprocessing for the production of high octane naphtha Download PDF

Info

Publication number
WO2012015540A3
WO2012015540A3 PCT/US2011/040785 US2011040785W WO2012015540A3 WO 2012015540 A3 WO2012015540 A3 WO 2012015540A3 US 2011040785 W US2011040785 W US 2011040785W WO 2012015540 A3 WO2012015540 A3 WO 2012015540A3
Authority
WO
WIPO (PCT)
Prior art keywords
naphtha
high octane
production
stage hydroprocessing
octane naphtha
Prior art date
Application number
PCT/US2011/040785
Other languages
French (fr)
Other versions
WO2012015540A2 (en
Inventor
Cong-Yan Chen
Stephen J. Miller
James N. Ziemer
Ann J. Liang
Original Assignee
Chevron U.S.A. Inc.
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 Chevron U.S.A. Inc. filed Critical Chevron U.S.A. Inc.
Priority to BR112013001890A priority Critical patent/BR112013001890A2/en
Priority to EP11812904.8A priority patent/EP2598608A2/en
Priority to RU2013108851/04A priority patent/RU2013108851A/en
Publication of WO2012015540A2 publication Critical patent/WO2012015540A2/en
Publication of WO2012015540A3 publication Critical patent/WO2012015540A3/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
    • C10G35/00—Reforming naphtha
    • C10G35/04—Catalytic reforming
    • C10G35/06—Catalytic reforming characterised by the catalyst used
    • C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group 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
    • 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
    • C10G69/08—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 step of reforming naphtha
    • C10G69/10—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 step of reforming naphtha hydrocracking of higher boiling fractions into naphtha and reforming the naphtha obtained
    • 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
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/301—Boiling range
    • 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
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/305—Octane number, e.g. motor octane number [MON], research octane number [RON]
    • 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
    • C10G2300/4018—Spatial velocity, e.g. LHSV, WHSV
    • 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
    • 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

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)
  • Catalysts (AREA)

Abstract

An integrated process is provided for producing high octane naphtha. Hydrocracked naphtha from a hydrocracking reaction zone is contacted with a reforming catalyst that includes a silicate having a silica to alumina molar ratio of at least 200, and a crystallite size of less than 10 microns. Products from the reforming include a reformed naphtha and a hydrogen-rich stream, which is passed to the hydrocracking reaction zone.
PCT/US2011/040785 2010-07-28 2011-06-16 Multi-stage hydroprocessing for the production of high octane naphtha WO2012015540A2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
BR112013001890A BR112013001890A2 (en) 2010-07-28 2011-06-16 multistage hydroprocessing for high octane naphtha production
EP11812904.8A EP2598608A2 (en) 2010-07-28 2011-06-16 Multi-stage hydroprocessing for the production of high octane naphtha
RU2013108851/04A RU2013108851A (en) 2010-07-28 2011-06-16 MULTI-STAGE HYDRO-TREATMENT FOR THE PRODUCTION OF HIGH-OCTANA NAFTA

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US12/845,605 US20120024752A1 (en) 2010-07-28 2010-07-28 Multi-Stage Hydroprocessing for the Production of High Octane Naphtha
US12/845,605 2010-07-28

Publications (2)

Publication Number Publication Date
WO2012015540A2 WO2012015540A2 (en) 2012-02-02
WO2012015540A3 true WO2012015540A3 (en) 2012-04-12

Family

ID=45525620

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2011/040785 WO2012015540A2 (en) 2010-07-28 2011-06-16 Multi-stage hydroprocessing for the production of high octane naphtha

Country Status (5)

Country Link
US (1) US20120024752A1 (en)
EP (1) EP2598608A2 (en)
BR (1) BR112013001890A2 (en)
RU (1) RU2013108851A (en)
WO (1) WO2012015540A2 (en)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8658021B2 (en) 2008-06-05 2014-02-25 Chevron U.S.A. Inc. Multi-stage reforming process to produce high octane gasoline
WO2013096072A2 (en) 2011-12-22 2013-06-27 Uop Llc Layered conversion synthesis of zeolites
SG11201402970RA (en) 2011-12-22 2014-11-27 Uop Llc Uzm-39 aluminosilicate zeolite
JP5852749B2 (en) 2011-12-22 2016-02-03 ユーオーピー エルエルシー Conversion reaction of aromatic compounds using UZM-39 aluminosilicate zeolite
RU2648239C2 (en) * 2012-11-09 2018-03-23 Каунсел Оф Сайнтифик Энд Индастриал Рисерч Single step catalytic process for conversion of n-paraffins and naphtha to diesel-range hydrocarbons
US8609910B1 (en) 2012-12-12 2013-12-17 Uop Llc Catalytic pyrolysis using UZM-39 aluminosilicate zeolite
US8609921B1 (en) 2012-12-12 2013-12-17 Uop Llc Aromatic transalkylation using UZM-44 aluminosilicate zeolite
US8912378B2 (en) 2012-12-12 2014-12-16 Uop Llc Dehydrocyclodimerization using UZM-39 aluminosilicate zeolite
US8907151B2 (en) 2012-12-12 2014-12-09 Uop Llc Conversion of methane to aromatic compounds using UZM-39 aluminosilicate zeolite
US8623321B1 (en) 2012-12-12 2014-01-07 Uop Llc UZM-44 aluminosilicate zeolite
US8618343B1 (en) 2012-12-12 2013-12-31 Uop Llc Aromatic transalkylation using UZM-39 aluminosilicate zeolite
US8609919B1 (en) 2012-12-12 2013-12-17 Uop Llc Aromatic transformation using UZM-44 aluminosilicate zeolite
US8609911B1 (en) 2012-12-12 2013-12-17 Uop Llc Catalytic pyrolysis using UZM-44 aluminosilicate zeolite
WO2014149247A1 (en) 2013-03-15 2014-09-25 Lummus Technology Inc. Hydroprocessing thermally cracked products
WO2015128042A1 (en) * 2014-02-25 2015-09-03 Saudi Basic Industries Corporation A method of controlling the supply and allocation of hydrogen gas in a hydrogen system of a refinery integrated with olefins and aromatics plants
US9670426B2 (en) 2014-06-11 2017-06-06 Uop Llc Methods for hydrocracking heavy and light hydrocarbons
WO2017116584A1 (en) * 2015-12-30 2017-07-06 Uop Llc Improved olefin and btx production using aliphatic cracking reactor
EP3318619A1 (en) * 2016-11-03 2018-05-09 Wolfdieter Klein Consulting GmbH Oel- und Gastechnologie Method for the production of fuels from gas condensates

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4036735A (en) * 1973-04-02 1977-07-19 Chevron Research Company Process for upgrading motor gasoline
US5073250A (en) * 1990-03-02 1991-12-17 Chevron Research & Technology Company Staged catalyst reforming to produce optimum octane barrel per calendar day reformate production
JPH05125368A (en) * 1991-07-02 1993-05-21 Chevron Res & Technol Co Crystalline silicate catalyst and method of reforming by using this
US5409595A (en) * 1993-08-16 1995-04-25 Mobil Oil Corporation Heavy naphtha conversion
US20090301934A1 (en) * 2008-06-05 2009-12-10 Chevron U.S.A. Inc. Multi-stage reforming process to produce high octane gasoline

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2703308A (en) * 1950-11-30 1955-03-01 Houdry Process Corp Catalytic conversion of hydrocarbon oils
US4137146A (en) * 1975-06-13 1979-01-30 Chevron Research Company Two-stage hydroconversion process (hydrocracking and reforming) using a stabilized aluminosilicate hydrocracking catalyst

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4036735A (en) * 1973-04-02 1977-07-19 Chevron Research Company Process for upgrading motor gasoline
US5073250A (en) * 1990-03-02 1991-12-17 Chevron Research & Technology Company Staged catalyst reforming to produce optimum octane barrel per calendar day reformate production
JPH05125368A (en) * 1991-07-02 1993-05-21 Chevron Res & Technol Co Crystalline silicate catalyst and method of reforming by using this
US5409595A (en) * 1993-08-16 1995-04-25 Mobil Oil Corporation Heavy naphtha conversion
US20090301934A1 (en) * 2008-06-05 2009-12-10 Chevron U.S.A. Inc. Multi-stage reforming process to produce high octane gasoline

Also Published As

Publication number Publication date
WO2012015540A2 (en) 2012-02-02
US20120024752A1 (en) 2012-02-02
RU2013108851A (en) 2014-09-10
BR112013001890A2 (en) 2016-05-24
EP2598608A2 (en) 2013-06-05

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