DE602004027432D1 - Katalysator enthaltend mindestens einen Zeolith ZBM-30 und mindestens einen Zeolith Y und Verfahren zur Hydrokonversion von Kohlenwasserstoffen mit einem solchen Katalysator - Google Patents

Katalysator enthaltend mindestens einen Zeolith ZBM-30 und mindestens einen Zeolith Y und Verfahren zur Hydrokonversion von Kohlenwasserstoffen mit einem solchen Katalysator

Info

Publication number
DE602004027432D1
DE602004027432D1 DE602004027432T DE602004027432T DE602004027432D1 DE 602004027432 D1 DE602004027432 D1 DE 602004027432D1 DE 602004027432 T DE602004027432 T DE 602004027432T DE 602004027432 T DE602004027432 T DE 602004027432T DE 602004027432 D1 DE602004027432 D1 DE 602004027432D1
Authority
DE
Germany
Prior art keywords
catalyst
zeolite
hydroconversion
hydrocarbons
methods
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.)
Expired - Lifetime
Application number
DE602004027432T
Other languages
English (en)
Inventor
Eric Benazzi
Emmanuelle Guillon
Yohan Martens
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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 Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of DE602004027432D1 publication Critical patent/DE602004027432D1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12Inorganic carriers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/80Mixtures of different zeolites
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12Inorganic carriers
    • C10G47/14Inorganic carriers the catalyst containing platinum group metals or compounds thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G65/00Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/10Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only cracking steps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/20After 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30After treatment, characterised by the means used
    • B01J2229/42Addition of matrix or binder particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/084Y-type faujasite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/70Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
DE602004027432T 2003-03-24 2004-03-11 Katalysator enthaltend mindestens einen Zeolith ZBM-30 und mindestens einen Zeolith Y und Verfahren zur Hydrokonversion von Kohlenwasserstoffen mit einem solchen Katalysator Expired - Lifetime DE602004027432D1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR0303529A FR2852864B1 (fr) 2003-03-24 2003-03-24 Catalyseur comprenant au moins une zeolithe choisie parmi zbm-30, zsm-48, eu-2 et eu-11 et au moins une zeolithe y et procede d'hydroconversion de charges hydrocarbonees utilisant un tel catalyseur

Publications (1)

Publication Number Publication Date
DE602004027432D1 true DE602004027432D1 (de) 2010-07-15

Family

ID=32799713

Family Applications (1)

Application Number Title Priority Date Filing Date
DE602004027432T Expired - Lifetime DE602004027432D1 (de) 2003-03-24 2004-03-11 Katalysator enthaltend mindestens einen Zeolith ZBM-30 und mindestens einen Zeolith Y und Verfahren zur Hydrokonversion von Kohlenwasserstoffen mit einem solchen Katalysator

Country Status (7)

Country Link
US (1) US7300900B2 (de)
EP (1) EP1462167B1 (de)
JP (1) JP4806897B2 (de)
DE (1) DE602004027432D1 (de)
DK (1) DK1462167T3 (de)
FR (1) FR2852864B1 (de)
ZA (1) ZA200402136B (de)

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FR2852863B1 (fr) * 2003-03-24 2005-05-06 Inst Francais Du Petrole Catalyseur et son utilisation pour l'amelioration du point d'ecoulement de charges hydrocarbonnees
US7575688B2 (en) * 2004-03-15 2009-08-18 Honeywell International Inc. Apparatus and method for removing sulfur containing compounds from a post-refinery fuel stream
DK1830959T3 (da) * 2004-12-23 2011-10-24 Inst Francais Du Petrole Zeolitisk katalysator med kontrolleret indhold af et doteringselement og forbedret fremgangsmåde til behandling af bitumenindsatse
CN100377783C (zh) * 2005-01-31 2008-04-02 中国石油化工股份有限公司 一种石脑油加工产物改质催化剂及方法
EP1779929A1 (de) * 2005-10-27 2007-05-02 Süd-Chemie Ag Katalysatorzusammensetzung zum Hydrierkracken und Verfahren zum milden Hydrierkracken und zur Ringöffnung
CA2616979C (en) * 2005-10-27 2012-04-17 Statoil Asa Ring opening process
TWI450762B (zh) * 2005-12-13 2014-09-01 Exxonmobil Res & Eng Co 具有高活性之zsm-48及用以去蠟之方法
US7482300B2 (en) * 2005-12-13 2009-01-27 Exxonmobil Research And Engineering Company High activity ZSM-48 and methods for dewaxing
WO2008027139A1 (en) * 2006-08-31 2008-03-06 Exxonmobil Chemical Patents Inc. Method for upgrading steam cracker tar using pox /cocker
WO2008027130A1 (en) * 2006-08-31 2008-03-06 Exxonmobil Chemical Patents Inc. Vps tar separation
WO2008027131A1 (en) 2006-08-31 2008-03-06 Exxonmobil Chemical Patents Inc. Disposition of steam cracked tar
US20100133193A1 (en) * 2007-02-14 2010-06-03 Honeywell International, Inc. Diesel sulfur filter-nanoadsorber and method of filtering a liquid fuel
US7704383B2 (en) * 2007-10-16 2010-04-27 Honeywell Interational Inc. Portable fuel desulfurization unit
FR2926085B1 (fr) * 2008-01-04 2010-02-12 Inst Francais Du Petrole Procede de production de distillats moyens par hydroisomerisation et hydrocraquage de charges issues du procede fischer-tropsch
FR2926028B1 (fr) * 2008-01-04 2010-02-12 Inst Francais Du Petrole Catalyseur comprenant au moins une zeolithe particuliere et au moins une silice-alumine et procede d'hydrocraquage de charges hydrocarbonees utilisant un tel catalyseur
FR2932812B1 (fr) * 2008-06-24 2011-07-29 Inst Francais Du Petrole Procede de conversion de charges issues de sources renouvelables en bases carburants gazoles de bonne qualite mettant en oeuvre un catalyseur zeolithique sans separation gaz liquide intermediaire
FR2932811B1 (fr) * 2008-06-24 2010-09-03 Inst Francais Du Petrole Procede de conversion de charges issues de sources renouvelables en bases carburants gazoles de bonne qualite mettant en oeuvre un catalyseur de type zeolithique
KR101767375B1 (ko) 2009-04-21 2017-08-11 알베마를 유럽 에스피알엘 인 및 붕소를 함유하는 수소처리 촉매
KR101354235B1 (ko) * 2010-04-14 2014-02-13 에스케이이노베이션 주식회사 수소화 탈왁스 공정을 위한 촉매 및 이의 제조 방법
US9487723B2 (en) 2010-06-29 2016-11-08 Exxonmobil Research And Engineering Company High viscosity high quality group II lube base stocks
US8617383B2 (en) 2010-06-29 2013-12-31 Exxonmobil Research And Engineering Company Integrated hydrocracking and dewaxing of hydrocarbons
US8992764B2 (en) 2010-06-29 2015-03-31 Exxonmobil Research And Engineering Company Integrated hydrocracking and dewaxing of hydrocarbons
US8557106B2 (en) 2010-09-30 2013-10-15 Exxonmobil Research And Engineering Company Hydrocracking process selective for improved distillate and improved lube yield and properties
CA2842164C (en) 2011-07-20 2018-04-17 Exxonmobil Research And Engineering Company Production of lubricating oil basestocks
SG11201504335RA (en) 2012-12-19 2015-07-30 Exxonmobil Res & Eng Co Mesoporous zeolite -y hydrocracking catalyst and associated hydrocracking processes
US9650312B2 (en) 2013-03-14 2017-05-16 Lummus Technology Inc. Integration of residue hydrocracking and hydrotreating
US20150174559A1 (en) 2013-12-19 2015-06-25 Basf Corporation Phosphorus-Modified FCC Catalysts
US9796932B2 (en) * 2013-12-19 2017-10-24 Basf Corporation FCC catalyst compositions containing boron oxide and phosphorus
US9719034B2 (en) 2013-12-23 2017-08-01 Exxonmobil Research And Engineering Company Co-production of lubricants and distillate fuels
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CN110404581A (zh) * 2018-04-28 2019-11-05 中国石油天然气股份有限公司 一种加氢裂化催化剂的制备方法、劣/重柴油加氢裂化的方法

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Also Published As

Publication number Publication date
US20040232047A1 (en) 2004-11-25
JP2004283829A (ja) 2004-10-14
FR2852864A1 (fr) 2004-10-01
EP1462167B1 (de) 2010-06-02
DK1462167T3 (da) 2010-08-23
JP4806897B2 (ja) 2011-11-02
EP1462167A1 (de) 2004-09-29
FR2852864B1 (fr) 2005-05-06
US7300900B2 (en) 2007-11-27
ZA200402136B (en) 2005-10-26

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Legal Events

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8327 Change in the person/name/address of the patent owner

Owner name: IFP ENERGIES NOUVELLES, RUEIL-MALMAISON, FR

8328 Change in the person/name/address of the agent

Representative=s name: VONNEMANN, KLOIBER & KOLLEGEN, 81667 MUENCHEN