EP2507195A4 - Erhöhung der oktanzahl von leichtnaphta mithilfe eines germanium-zeolit-katalysators - Google Patents

Erhöhung der oktanzahl von leichtnaphta mithilfe eines germanium-zeolit-katalysators

Info

Publication number
EP2507195A4
EP2507195A4 EP10835119.8A EP10835119A EP2507195A4 EP 2507195 A4 EP2507195 A4 EP 2507195A4 EP 10835119 A EP10835119 A EP 10835119A EP 2507195 A4 EP2507195 A4 EP 2507195A4
Authority
EP
European Patent Office
Prior art keywords
germanium
octane number
zeolite catalyst
light naphtha
increasing octane
Prior art date
Legal status (The legal status 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 status listed.)
Withdrawn
Application number
EP10835119.8A
Other languages
English (en)
French (fr)
Other versions
EP2507195A1 (de
Inventor
Scott Stevenson
Paul E Ellis
Mike Mier
Dustin Farmer
Alla Khanmamedove
Scott Mitchell
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Saudi Basic Industries Corp
Original Assignee
Saudi Basic Industries Corp
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 Saudi Basic Industries Corp filed Critical Saudi Basic Industries Corp
Publication of EP2507195A1 publication Critical patent/EP2507195A1/de
Publication of EP2507195A4 publication Critical patent/EP2507195A4/de
Withdrawn legal-status Critical Current

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
    • C10G35/065—Catalytic reforming characterised by the catalyst used containing crystalline zeolitic molecular sieves, other than aluminosilicates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/13—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation with simultaneous isomerisation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/16—Alumino-silicates
    • B01J20/18—Synthetic zeolitic molecular sieves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/44—Palladium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/047—Germanosilicates; Aluminogermanosilicates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • B01J29/42—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing iron group metals, noble metals or copper
    • B01J29/44—Noble metals
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
    • C07C5/373—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen with simultaneous isomerisation
    • C07C5/393—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen with simultaneous isomerisation with cyclisation to an aromatic six-membered ring, e.g. dehydrogenation of n-hexane to benzene
    • C07C5/41—Catalytic processes
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10—After treatment, characterised by the effect to be obtained
    • B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/1081—Alkanes
    • 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
    • C10G2300/1096—Aromatics or polyaromatics
    • 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
    • C10G2300/20—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
EP10835119.8A 2009-12-04 2010-12-02 Erhöhung der oktanzahl von leichtnaphta mithilfe eines germanium-zeolit-katalysators Withdrawn EP2507195A4 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US12/592,883 US20110132804A1 (en) 2009-12-04 2009-12-04 Increasing octane number of light naphtha using a germanium-zeolite catalyst
PCT/US2010/058723 WO2011068964A1 (en) 2009-12-04 2010-12-02 Increasing octane number of light naphtha using a germanium-zeolite catalyst

Publications (2)

Publication Number Publication Date
EP2507195A1 EP2507195A1 (de) 2012-10-10
EP2507195A4 true EP2507195A4 (de) 2014-11-26

Family

ID=44080965

Family Applications (1)

Application Number Title Priority Date Filing Date
EP10835119.8A Withdrawn EP2507195A4 (de) 2009-12-04 2010-12-02 Erhöhung der oktanzahl von leichtnaphta mithilfe eines germanium-zeolit-katalysators

Country Status (8)

Country Link
US (1) US20110132804A1 (de)
EP (1) EP2507195A4 (de)
JP (1) JP2013512317A (de)
KR (1) KR20120088829A (de)
CN (1) CN102639472A (de)
IN (1) IN2012DN03131A (de)
SG (1) SG181153A1 (de)
WO (1) WO2011068964A1 (de)

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US9242233B2 (en) 2012-05-02 2016-01-26 Saudi Basic Industries Corporation Catalyst for light naphtha aromatization
US8772192B2 (en) 2012-06-29 2014-07-08 Saudi Basic Industries Corporation Germanium silicalite catalyst and method of preparation and use
US9180441B2 (en) 2012-09-20 2015-11-10 Saudi Basic Industries Corporation Method of forming zeolite shaped body with silica binder
KR101451902B1 (ko) * 2012-11-26 2014-10-22 한국과학기술원 메조기공을 갖는 ｍｒｅ 구조의 제올라이트 또는 유사 ｍｒｅ 제올라이트 물질 및 그의 제조 방법
US9782758B2 (en) 2013-04-23 2017-10-10 Saudi Basic Industries Corporation Method of preparing hydrocarbon aromatization catalyst, the catalyst, and the use of the catalyst
WO2015077034A1 (en) * 2013-11-22 2015-05-28 Saudi Basic Industries Corporation Catalyst with improved activity/selectivity for light naphtha aromatization
US9446389B2 (en) * 2013-12-13 2016-09-20 Saudi Basic Industries Corporation Hydrocarbon aromatization catalyst composition and method of formation
US10654767B2 (en) 2014-06-26 2020-05-19 Sabic Global Technologies B.V. Process for producing alkylated aromatic hydrocarbons from a mixed hydrocarbon feedstream
CN106660896A (zh) * 2014-06-26 2017-05-10 Sabic环球技术有限责任公司 用于从混合的烃进料物流生产纯化的芳族烃的方法
US10744449B2 (en) * 2015-11-16 2020-08-18 Exxonmobil Upstream Research Company Adsorbent materials and methods of adsorbing carbon dioxide
CN107955644B (zh) * 2016-10-18 2020-07-14 中国石油化工股份有限公司 一种非芳轻烃的高效芳构化方法
EP3318619A1 (de) * 2016-11-03 2018-05-09 Wolfdieter Klein Consulting GmbH Oel- und Gastechnologie Verfahren zur herstellung von kraftstoffen aus gaskondensaten
CN106582793A (zh) * 2016-12-07 2017-04-26 张吉照 石脑油异构化及脱硫双效催化剂及其制备方法
CN109382115B (zh) * 2017-08-02 2021-08-10 中国石油化工股份有限公司 耐硫预变换催化剂及其制备方法
WO2019040487A1 (en) * 2017-08-23 2019-02-28 Phillips 66 Company METHODS OF SELECTIVELY REFORMING NAPHTHA
MX2020006238A (es) * 2017-12-15 2020-09-03 Koch Tech Solutions Uk Limited Procesos para preparar composiciones de hidrocarburos.
US10787618B2 (en) * 2018-01-23 2020-09-29 Saudi Arabian Oil Company Modified USY-zeolite catalyst for reforming hydrocarbons
US20210162380A1 (en) * 2018-08-30 2021-06-03 Sabic Global Technologies B.V. Aromatization catalyst with improved isomerization, process of making and using thereof
US11305264B2 (en) * 2019-09-12 2022-04-19 Saudi Arabian Oil Company Manufacturing hydrocracking catalyst
US11365358B2 (en) * 2020-05-21 2022-06-21 Saudi Arabian Oil Company Conversion of light naphtha to enhanced value products in an integrated two-zone reactor process
US11332678B2 (en) 2020-07-23 2022-05-17 Saudi Arabian Oil Company Processing of paraffinic naphtha with modified USY zeolite dehydrogenation catalyst
US11274068B2 (en) 2020-07-23 2022-03-15 Saudi Arabian Oil Company Process for interconversion of olefins with modified beta zeolite
US11420192B2 (en) 2020-07-28 2022-08-23 Saudi Arabian Oil Company Hydrocracking catalysts containing rare earth containing post-modified USY zeolite, method for preparing hydrocracking catalysts, and methods for hydrocracking hydrocarbon oil with hydrocracking catalysts
US11154845B1 (en) 2020-07-28 2021-10-26 Saudi Arabian Oil Company Hydrocracking catalysts containing USY and beta zeolites for hydrocarbon oil and method for hydrocracking hydrocarbon oil with hydrocracking catalysts
US11142703B1 (en) 2020-08-05 2021-10-12 Saudi Arabian Oil Company Fluid catalytic cracking with catalyst system containing modified beta zeolite additive
US11673845B2 (en) 2020-09-03 2023-06-13 Saudi Arabian Oil Company Aromatization of light hydrocarbons using metal-modified zeolite catalysts
US11465950B2 (en) 2020-09-03 2022-10-11 Saudi Arabian Oil Company Aromatization of light hydrocarbons using metal-doped zeolite catalysts with enhanced mesoporosity
US20220389334A1 (en) * 2021-06-04 2022-12-08 Saudi Arabian Oil Company Conversion of light naphtha to enhanced value products in an integrated reactor process
US11618858B1 (en) 2021-12-06 2023-04-04 Saudi Arabian Oil Company Hydrodearylation catalysts for aromatic bottoms oil, method for producing hydrodearylation catalysts, and method for hydrodearylating aromatic bottoms oil with hydrodearylation catalysts
US20230183584A1 (en) * 2021-12-14 2023-06-15 Uop Llc Process for naphtha aromatization using a multi-stage fluidized system
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US4645586A (en) * 1983-06-03 1987-02-24 Chevron Research Company Reforming process
US5114565A (en) * 1990-01-26 1992-05-19 Chevron Research And Technology Company Reforming naphtha with boron-containing large-pore zeolites
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See also references of WO2011068964A1 *

Also Published As

Publication number Publication date
JP2013512317A (ja) 2013-04-11
CN102639472A (zh) 2012-08-15
WO2011068964A1 (en) 2011-06-09
EP2507195A1 (de) 2012-10-10
SG181153A1 (en) 2012-07-30
US20110132804A1 (en) 2011-06-09
IN2012DN03131A (de) 2015-09-18
KR20120088829A (ko) 2012-08-08

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