BR9804013A - Catalisador e processo de hidrocraqueamento de cortes hidrocarbonados - Google Patents

Catalisador e processo de hidrocraqueamento de cortes hidrocarbonados

Info

Publication number
BR9804013A
BR9804013A BR9804013-8A BR9804013A BR9804013A BR 9804013 A BR9804013 A BR 9804013A BR 9804013 A BR9804013 A BR 9804013A BR 9804013 A BR9804013 A BR 9804013A
Authority
BR
Brazil
Prior art keywords
catalyst
sio
ratio
metal
hydrocracking process
Prior art date
Application number
BR9804013-8A
Other languages
English (en)
Inventor
Nathalie George-Marchal
Samuel Mignard
Slavik Kasztelan
Original Assignee
Inst Francais Du Petrole
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 Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Publication of BR9804013A publication Critical patent/BR9804013A/pt

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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/12—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing crystalline alumino-silicates, e.g. molecular sieves
    • 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
    • C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10—Cracking 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
    • C10G47/12—Inorganic carriers
    • C10G47/16—Crystalline alumino-silicate carriers
    • C10G47/20—Crystalline alumino-silicate carriers the catalyst containing other 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
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28078—Pore diameter
    • 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12—Silica and alumina
    • 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
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/85—Chromium, molybdenum or tungsten
    • 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
    • B01J29/08—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/16—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J29/166—Y-type faujasite
    • 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
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten 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
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles
    • 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
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J35/66—Pore distribution
    • 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
    • C10G2300/4006—Temperature
    • 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
    • C10G2300/4012—Pressure

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Abstract

Patente de Invenção: <B>"CATALISADOR E PROCESSO DE HIDROCRAQUEAMENTO DE CORTES HIDROCARBONADOS"<D>. A invenção refere-se a um catalisador de hidrocraqueamento, contendo pelo menos um metal do grupo VIB, e/ou pelo menos um metal do grupo VIII da calsssifacação periódica, uma matriz alumina, fósforo, eventualmente pelo menos um elemento do grupo VIIA (flúor) e uma zeólita Y desaluminada globalmente de parâmetro cristalino superior a 2, 438 nm, de relação SiO~ 2~/Al~ 2~O~ 3~ global inferior a 8, de relação SiO~ 2~/Al~ 2~O~ 3~ de carcaça inferior a 21 e superior à relação SiO~ 2~ /Al~ 2~O~ 3~ global. A invenção se refere igualmente a um processo de hdirocraqueamento com esse catalisador, notadamente às baixas pressões de 7,5 a 11 MPa.
BR9804013-8A 1997-10-20 1998-10-19 Catalisador e processo de hidrocraqueamento de cortes hidrocarbonados BR9804013A (pt)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR9713128A FR2769856B1 (fr) 1997-10-20 1997-10-20 Catalyseur et procede d'hydrocraquage de coupes hydrocarbonees

Publications (1)

Publication Number Publication Date
BR9804013A true BR9804013A (pt) 1999-12-07

Family

ID=9512436

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9804013-8A BR9804013A (pt) 1997-10-20 1998-10-19 Catalisador e processo de hidrocraqueamento de cortes hidrocarbonados

Country Status (9)

Country Link
US (1) US6174429B1 (pt)
EP (1) EP0911077B1 (pt)
JP (1) JP4088731B2 (pt)
KR (1) KR100635307B1 (pt)
BR (1) BR9804013A (pt)
CA (1) CA2248974C (pt)
DE (1) DE69838470T2 (pt)
ES (1) ES2294808T3 (pt)
FR (1) FR2769856B1 (pt)

Families Citing this family (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2778343B1 (fr) 1998-05-06 2000-06-16 Inst Francais Du Petrole Catalyseur a base de zeolithe y non globalement desaluminee, de bore et/ou de silicium et procede d'hydrocraquage
CN1096296C (zh) 1998-11-13 2002-12-18 中国石油化工集团公司 一种生产中间馏分油的加氢裂化催化剂及其制备
US6387246B1 (en) * 1999-05-19 2002-05-14 Institut Francais Du Petrole Catalyst that comprises a partially amorphous Y zeolite and its use in hydroconversion of hydrocarbon petroleum feedstocks
FR2793705B1 (fr) * 1999-05-19 2001-06-29 Inst Francais Du Petrole Catalyseur comprenant une zeolithe y partiellement amorphe, un element du groupe vb et son utilisation en hydroconversion et hydroraffinage de charges petrolieres hydrocarbonees
US6596662B2 (en) 2000-03-24 2003-07-22 Exxonmobil Chemical Patents Inc. Production of alkylated aromatic compounds using dealuminated catalysts
US6747182B2 (en) 2000-03-24 2004-06-08 Exxonmobil Chemical Patents Inc. Production of alkylated aromatic compounds using dealuminated catalysts
ES2200701B1 (es) * 2002-07-16 2005-05-01 Universidad Politecnica De Valencia Catalizador de hidrocraqueo conteniendo un material solido cristalino microporoso y uso de dicho catalizador para el hidrocraqueo de alimentacion de hidrocarburos.
US6902664B2 (en) * 2002-11-08 2005-06-07 Chevron U.S.A. Inc. Extremely low acidity USY and homogeneous, amorphous silica-alumina hydrocracking catalyst and process
FR2863913B1 (fr) * 2003-12-23 2006-12-29 Inst Francais Du Petrole Catalyseur zeolithique,support a base de matrice silico-aluminique et de zeolithe, et procede d'hydrocraquage de charges hydrocarbonees
US7323100B2 (en) * 2004-07-16 2008-01-29 Conocophillips Company Combination of amorphous materials for hydrocracking catalysts
US7611689B2 (en) * 2004-09-24 2009-11-03 Shell Oil Company Faujasite zeolite, its preparation and use in hydrocracking
CN100389178C (zh) * 2005-01-14 2008-05-21 中国石油化工股份有限公司 一种含氟加氢催化剂及其制备方法
CN101213269B (zh) * 2005-06-29 2012-01-25 格雷斯公司 在流化催化装置中用于轻质烯烃的五元环高硅沸石催化剂
US20110086755A1 (en) * 2008-03-28 2011-04-14 Petroleum Energy Center, A Juridical Incorporated Foundation Hydrocracking catalyst for heavy oil
BRPI1014950B1 (pt) 2009-04-21 2018-10-23 Albemarle Europe Sprl catalisador de hidrotratamento contendo fósforo e boro.
US8080492B2 (en) * 2009-04-29 2011-12-20 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
US7931799B2 (en) * 2009-04-29 2011-04-26 Chevron U.S.A. Inc. Hydroconversion multi-metallic catalyst and method for making thereof
JP5547923B2 (ja) 2009-08-03 2014-07-16 出光興産株式会社 重質油水素化分解触媒及びそれを用いた重質油の水素化処理方法
CN102463131B (zh) * 2010-11-04 2014-07-23 中国石油化工股份有限公司 一种加氢裂化催化剂及其制备方法
FR2970259B1 (fr) * 2011-01-07 2014-07-18 IFP Energies Nouvelles Procede d'hydrocraquage utilisant un catalyseur zeolithique contenant deux fonctions hydrogenantes distinctes.
CN103191775B (zh) * 2012-01-06 2014-08-20 中国石油化工股份有限公司 一种加氢裂化催化剂的制备方法
CN103191774B (zh) * 2012-01-06 2014-08-20 中国石油化工股份有限公司 制备加氢裂化催化剂的方法
CN103191772B (zh) * 2012-01-06 2014-09-17 中国石油化工股份有限公司 加氢裂化催化剂的制备方法
CN105536854B (zh) * 2014-11-03 2018-04-10 中国石油化工股份有限公司 一种制备含y分子筛的加氢裂化催化剂的方法
CN105536855B (zh) * 2014-11-03 2018-04-10 中国石油化工股份有限公司 一种含y分子筛的加氢裂化催化剂的制备方法
FR3046176A1 (fr) 2015-12-23 2017-06-30 Axens Procede d'hydrotraitement ou d'hydroconversion avec striper et ballon separateur basse pression sur la section de fractionnement

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US4326947A (en) * 1979-08-16 1982-04-27 Exxon Research & Engineering Co. Hydrocracking over alumina-aluminum fluorophosphate-containing catalysts
US5288396A (en) * 1979-10-15 1994-02-22 Union Oil Company Of California Hydrocracking process using a catalyst selective for making middle distillates
US4855036A (en) * 1984-10-03 1989-08-08 Uop Catalytic cracking process
FR2582665B1 (fr) * 1985-06-04 1988-08-05 Inst Francais Du Petrole Procede de craquage catalytique
US4663025A (en) * 1986-08-14 1987-05-05 Phillips Petroleum Company Catalytic cracking processes
GB8722839D0 (en) * 1987-09-29 1987-11-04 Shell Int Research Hydrocracking of hydrocarbon feedstock
US5036033A (en) * 1989-05-26 1991-07-30 Union Oil Company Of California Alkylation catalyst and processes for preparing
US5069890A (en) * 1989-06-19 1991-12-03 Texaco Inc. Zeolite treating process
US5286692A (en) * 1990-03-17 1994-02-15 China Petro-Chemical Corporation Mild hydrocracking catlyst and the process therefor
US5190903A (en) * 1991-03-31 1993-03-02 Uop Low acidity Y zeolite
US5342507A (en) * 1992-06-11 1994-08-30 Texaco Inc. Mild hydrocracking process employing catalysts containing dealuminated y-zeolites
JP3300064B2 (ja) * 1992-10-09 2002-07-08 財団法人石油産業活性化センター 炭化水素油用水素化精製触媒組成物及び水素化精製方法並びに脱硫軽油の製造方法
TW358120B (en) * 1994-08-24 1999-05-11 Shell Int Research Hydrocarbon conversion catalysts
US6051127A (en) * 1996-07-05 2000-04-18 Shell Oil Company Process for the preparation of lubricating base oils
FR2754742B1 (fr) * 1996-10-22 1998-12-11 Inst Francais Du Petrole Catalyseur contenant au moins deux zeolithes y desaluminees et procede d'hydroconversion conventionnelle de coupes petrolieres avec ce catalyseur

Also Published As

Publication number Publication date
CA2248974C (fr) 2008-05-13
EP0911077B1 (fr) 2007-09-26
ES2294808T3 (es) 2008-04-01
US6174429B1 (en) 2001-01-16
KR19990037213A (ko) 1999-05-25
EP0911077A1 (fr) 1999-04-28
FR2769856A1 (fr) 1999-04-23
DE69838470D1 (de) 2007-11-08
DE69838470T2 (de) 2008-01-10
KR100635307B1 (ko) 2007-06-07
JPH11192437A (ja) 1999-07-21
FR2769856B1 (fr) 1999-12-03
CA2248974A1 (fr) 1999-04-20
JP4088731B2 (ja) 2008-05-21

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Legal Events

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B08F Application dismissed because of non-payment of annual fees [chapter 8.6 patent gazette]

Free format text: REFERENTE A 6A , 7A , 8A E 9A ANUIDADES.

B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

Free format text: REFERENTE AO DESPACHO 8.6 PUBLICADO NA RPI 1912 DE 28/08/2007.