MX172430B - Catalizador para hidratar cataliticamente una alimentacion hidrocarbonada pesada - Google Patents

Catalizador para hidratar cataliticamente una alimentacion hidrocarbonada pesada

Info

Publication number
MX172430B
MX172430B MX016070A MX1607081A MX172430B MX 172430 B MX172430 B MX 172430B MX 016070 A MX016070 A MX 016070A MX 1607081 A MX1607081 A MX 1607081A MX 172430 B MX172430 B MX 172430B
Authority
MX
Mexico
Prior art keywords
catalyst
pores
diameter
catalytically
heavy hydrocarbon
Prior art date
Application number
MX016070A
Other languages
English (en)
Inventor
Harvey D Schindler
Original Assignee
Lummus 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 Lummus Co filed Critical Lummus Co
Publication of MX172430B publication Critical patent/MX172430B/es

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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
    • C10G49/04—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing nickel, cobalt, 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
    • 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
    • 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
    • B01J35/61—Surface area
    • B01J35/615—100-500 m2/g
    • 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
    • B01J35/63—Pore volume
    • B01J35/635—0.5-1.0 ml/g
    • 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
    • B01J35/64—Pore diameter
    • B01J35/647—2-50 nm
    • 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
    • B01J35/64—Pore diameter
    • B01J35/651—50-500 nm

Landscapes

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

Abstract

La presente invención se refiere a catalizador para hidrotratar catalíticamente una alimentación hidrocarbonada pesada, caracterizado porque comprende una cantidad catalíticamente eficaz de níquel y molibdeno soportados sobre un soporte de alúmina, teniendo el catalizador una porosidad total de al menos 0,5 cc/g y una distribución del tamaño de poros como sigue: de 0,25 a 0,40 cc/g de poros con un diámetro inferior a 250 A; de 0,10 a 0,25 cc/g de poros con un diámetro de 250 a 500 A; de 0,20 a 0,30 cc/g de poros con un diámetro de 500 a 1,500 A; de 0,05 a 0,15 cc/g de poros con un diámetro de 1,500 a 4,000 A; y de 0,03 a 0,10 cc/g de poros con un diámetro superior a 4,000 A; catalizar que ha sido calcinado a 621 - 704 grados C.
MX016070A 1980-11-21 1981-11-19 Catalizador para hidratar cataliticamente una alimentacion hidrocarbonada pesada MX172430B (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US20894880A 1980-11-21 1980-11-21

Publications (1)

Publication Number Publication Date
MX172430B true MX172430B (es) 1993-12-16

Family

ID=22776714

Family Applications (2)

Application Number Title Priority Date Filing Date
MX016070A MX172430B (es) 1980-11-21 1981-11-19 Catalizador para hidratar cataliticamente una alimentacion hidrocarbonada pesada
MX190208A MX160789A (es) 1980-11-21 1981-11-19 Procedimiento para hidrotratar cataliticamente una alimentacion hidrocarbonada pesada

Family Applications After (1)

Application Number Title Priority Date Filing Date
MX190208A MX160789A (es) 1980-11-21 1981-11-19 Procedimiento para hidrotratar cataliticamente una alimentacion hidrocarbonada pesada

Country Status (12)

Country Link
JP (1) JPS5946666B2 (es)
AU (1) AU540245B2 (es)
CA (1) CA1159039A (es)
DE (1) DE3145718A1 (es)
ES (1) ES507340A1 (es)
FR (1) FR2494597A1 (es)
GB (1) GB2087747B (es)
IT (1) IT1143446B (es)
MX (2) MX172430B (es)
NL (1) NL8105267A (es)
SE (1) SE448951B (es)
ZA (1) ZA817732B (es)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3522538A1 (de) * 1984-06-22 1986-01-02 Chiyoda Chemical Engineering & Construction Co. Ltd., Yokohama, Kanagawa Verfahren und katalysator zur hydrierung von kohleteerpech
DE3581777D1 (de) * 1984-09-12 1991-03-28 Nippon Kokan Kk Hydrierkatalysator fuer kohlenteer, methode zur hydrierung von kohlenteer mit dem katalysator, und methode zur herstellung von supernadelkoks aus dem hydrierungsprodukt von kohlenteer.
GC0000065A (en) 1998-09-01 2004-06-30 Japan Energy Corp Hydrocracking catalyst, producing method threof, and hydrocracking method.
JP4493997B2 (ja) * 2003-12-10 2010-06-30 財団法人石油産業活性化センター 炭化水素油の水素化脱硫触媒及びその製造方法
WO2008019581A1 (fr) 2006-08-11 2008-02-21 China Petroleum & Chemical Corporation Alumine ayant une structure poreuse complexe, et catalyseur et procédé d'hydrogénation sélective de l'essence de craquage
JP4902424B2 (ja) * 2007-05-21 2012-03-21 Ｊｘ日鉱日石エネルギー株式会社 水素化精製触媒及び水素化精製方法

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL123195C (es) * 1960-03-02
US3361526A (en) * 1964-06-19 1968-01-02 Grace W R & Co Process for producing alumina having a narrow pore size distribution
CA943944A (en) * 1967-10-27 1974-03-19 Michael C. Chervenak Catalysts, methods of preparation of same and processes for using same
JPS5141641B2 (es) * 1972-01-06 1976-11-11
US3952069A (en) * 1973-01-26 1976-04-20 Gulf Research & Development Company Hydrogenation of aromatics
JPS51122105A (en) * 1975-04-18 1976-10-26 Toa Nenryo Kogyo Kk Process for hydrofining of hydrocarbon oil
US4013547A (en) * 1976-01-22 1977-03-22 Union Oil Company Of California Desulfurization of residual petroleum oils with a catalyst calcined at higher temperatures
US4301037A (en) * 1980-04-01 1981-11-17 W. R. Grace & Co. Extruded alumina catalyst support having controlled distribution of pore sizes

Also Published As

Publication number Publication date
JPS5946666B2 (ja) 1984-11-14
MX160789A (es) 1990-05-17
IT8149747A0 (it) 1981-11-20
GB2087747B (en) 1984-07-04
SE8106925L (sv) 1982-05-22
ES507340A0 (es) 1985-03-01
IT1143446B (it) 1986-10-22
FR2494597B1 (es) 1985-01-04
ZA817732B (en) 1982-10-27
CA1159039A (en) 1983-12-20
AU7747681A (en) 1982-05-27
AU540245B2 (en) 1984-11-08
JPS57117343A (en) 1982-07-21
DE3145718A1 (de) 1982-06-16
NL8105267A (nl) 1982-06-16
ES507340A1 (es) 1985-03-01
FR2494597A1 (fr) 1982-05-28
GB2087747A (en) 1982-06-03
DE3145718C2 (es) 1987-06-19
SE448951B (sv) 1987-03-30

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