ES261152A1 - Un procedimiento para la purificaciën de hidrocarburos - Google Patents

Un procedimiento para la purificaciën de hidrocarburos

Info

Publication number
ES261152A1
ES261152A1 ES0261152A ES261152A ES261152A1 ES 261152 A1 ES261152 A1 ES 261152A1 ES 0261152 A ES0261152 A ES 0261152A ES 261152 A ES261152 A ES 261152A ES 261152 A1 ES261152 A1 ES 261152A1
Authority
ES
Spain
Prior art keywords
composite
catalyst
oxide
calcining
silica
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
Application number
ES0261152A
Other languages
English (en)
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products Co
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 Universal Oil Products Co filed Critical Universal Oil Products Co
Publication of ES261152A1 publication Critical patent/ES261152A1/es
Expired legal-status Critical Current

Links

Classifications

    • 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
    • B01J23/88—Molybdenum
    • B01J23/883—Molybdenum and nickel
    • 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
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/20—Sulfiding
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

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

Abstract

Un procedimiento para la purificación de hidrocarburos a temperatura elevada y bajo una presión de oxígeno impuesta con un catalizador de hidrodesulfuración, caracterizado porque el tratamiento de purificación se efectúa en presencia de un compuesto que contiene alúmina, sílice, sulfuro de molibdeno y sulfuro de niquel, que ha sido preprarado tratando un compuesto que contiene alúmina, sílice, óxido de molibdeno y óxido de níquel con una mezcla de sulfuración gaseosa que contiene hidrógeno y sulfuro de hidrógeno en una relación molar de, sustancialmente, desde 1:2 a 4:1 en ausencia de dichos hidrocarburos a una temperatura entre 204º y 427º C, y enfriando luego el compuesto sulfurado hasta menos de 204ºC bajo una presión positiva de sulfuro de hidrógeno.
ES0261152A 1959-09-21 1960-09-21 Un procedimiento para la purificaciën de hidrocarburos Expired ES261152A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US841402A US3016347A (en) 1959-09-21 1959-09-21 Hydrocarbon purification process and catalyst

Publications (1)

Publication Number Publication Date
ES261152A1 true ES261152A1 (es) 1961-02-01

Family

ID=25284789

Family Applications (1)

Application Number Title Priority Date Filing Date
ES0261152A Expired ES261152A1 (es) 1959-09-21 1960-09-21 Un procedimiento para la purificaciën de hidrocarburos

Country Status (11)

Country Link
US (1) US3016347A (es)
CH (1) CH393276A (es)
DE (1) DE1246148B (es)
DK (1) DK117445B (es)
ES (1) ES261152A1 (es)
FR (1) FR1268131A (es)
GB (1) GB930760A (es)
MY (1) MY6500025A (es)
NL (1) NL256096A (es)
OA (1) OA00548A (es)
SE (1) SE306075B (es)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3132111A (en) * 1960-03-31 1964-05-05 Sinclair Research Inc Process for the preparation of a catalyst
US3169931A (en) * 1960-12-06 1965-02-16 Universal Oil Prod Co Method of preparing an alumina-silica supported catalyst composition
US3231520A (en) * 1962-12-26 1966-01-25 Texaco Inc Catalyst and method of making same
US3320181A (en) * 1964-01-30 1967-05-16 Chevron Res Hydrocarbon conversion catalysts com prising molybdenum sulfide and nickel sulfide dispersed within alumina
US3291751A (en) * 1964-01-30 1966-12-13 Chevron Res Preparation of a catalyst containing a molybdenum compound dispersed within alumina
US3487011A (en) * 1966-11-23 1969-12-30 Gulf Research Development Co Hydrodesulfurization of naphthas
US3509044A (en) * 1967-06-26 1970-04-28 Exxon Research Engineering Co Hydrodesulfurization of petroleum residuum
US3528910A (en) * 1967-06-26 1970-09-15 Sinclair Research Inc Hydrotreating process utilizing alkyl disulfide for in situ catalyst activation
US3546104A (en) * 1968-05-08 1970-12-08 Nippon Oil Co Ltd Hydrodesulfurization of petroleum hydrocarbons containing asphaltenes
US3494857A (en) * 1968-05-10 1970-02-10 Gulf Research Development Co Process for the hydrogenation of unsaturated hydrocarbons
FR2503733B1 (fr) * 1981-04-09 1985-09-06 Inst Francais Du Petrole Procede d'hydrotraitement d'une charge hydrocarbonee en presence d'un catalyseur soumis a une presulfuration
US4725569A (en) * 1984-11-27 1988-02-16 Tuszynski William J Organopolysulfide-impregnated catalyst and methods of preparation and use
FR2743512B1 (fr) * 1996-01-17 1998-03-13 Eurecat Europ Retrait Catalys Procede d'incorporation de soufre dans la porosite d'un catalyseur de traitement d'hydrocarbures
FR2758478B1 (fr) 1997-01-21 1999-02-26 Elf Aquitaine Procede pour la presulfuration de catalyseurs
DE69931837T2 (de) * 1998-03-20 2006-11-09 China Petrochemical Corp. Hydroentschwefelung von Kohlenwasserstoffölen
US6037306A (en) * 1998-03-20 2000-03-14 China Petrochemical Corporation Catalyst containing molybdenum and/or tungsten for hydrotreating light oil distillates and preparation method thereof
FR2792551B1 (fr) 1999-04-20 2001-06-08 Atochem Elf Sa Procede de sulfuration de catalyseurs d'hydrotraitement
FR2820991B1 (fr) * 2001-02-22 2003-10-03 Atofina Procede de sulfuration des catalyseurs d'hydrotraitement
AR043242A1 (es) * 2003-02-24 2005-07-20 Shell Int Research Preparacion y uso de una composicion de catalizador
EP2463260B1 (en) * 2003-09-23 2016-08-24 BASF Corporation Process for the removal of sulfur compounds from hydrocarbon feedstocks
JP2008512223A (ja) * 2004-09-08 2008-04-24 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 水素化分解用触媒組成物
FR2880823B1 (fr) * 2005-01-20 2008-02-22 Total France Sa Catalyseur d'hydrotraitement, son procede de preparation et et son utilisation
FR2910348B1 (fr) * 2006-12-22 2012-05-18 Arkema France Agent de sulfuration de catalyseur d'hydrotraitement et son utilisation pour la presulfuration in-situ et ex-situ
WO2009065878A2 (en) * 2007-11-19 2009-05-28 Shell Internationale Research Maatschappij B.V. Method for the start-up of a catalytic process

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2129693A (en) * 1935-08-27 1938-09-13 Houdry Process Corp Catalysis
DE816853C (de) * 1949-02-25 1951-10-15 Basf Ag Verfahren zur Herstellung von Metallsulfiden auf geformter Tonerde fuer katalytische Zwecke
US2783211A (en) * 1950-07-31 1957-02-26 Gulf Research Development Co Method of preparing impregnated catalysts
US2761816A (en) * 1954-06-21 1956-09-04 Exxon Research Engineering Co Hydrodesulfurization process using a cobalt molybdate catalyst presulfided with the feed under specific conditions
GB796175A (en) * 1954-10-04 1958-06-04 California Research Corp Improvements in or relating to catalysts and the production thereof
NL105563C (es) * 1955-02-25 1900-01-01
US2905636A (en) * 1957-06-27 1959-09-22 Universal Oil Prod Co Manufacture and use of supported molybdenum-containing catalysts

Also Published As

Publication number Publication date
GB930760A (en) 1963-07-10
FR1268131A (fr) 1961-07-28
DK117445B (da) 1970-04-27
CH393276A (de) 1965-06-15
OA00548A (fr) 1966-07-15
DE1246148B (de) 1967-08-03
SE306075B (es) 1968-11-18
MY6500025A (en) 1965-12-31
US3016347A (en) 1962-01-09
NL256096A (es)

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