SE8106925L - HYDRO-TREATMENT CATALYST AND USE THEREOF - Google Patents

HYDRO-TREATMENT CATALYST AND USE THEREOF

Info

Publication number
SE8106925L
SE8106925L SE8106925A SE8106925A SE8106925L SE 8106925 L SE8106925 L SE 8106925L SE 8106925 A SE8106925 A SE 8106925A SE 8106925 A SE8106925 A SE 8106925A SE 8106925 L SE8106925 L SE 8106925L
Authority
SE
Sweden
Prior art keywords
catalyst
hydro
hydrotreating
treatment catalyst
feedstocks
Prior art date
Application number
SE8106925A
Other languages
Unknown language ( )
Swedish (sv)
Other versions
SE448951B (en
Inventor
H 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 SE8106925L publication Critical patent/SE8106925L/en
Publication of SE448951B publication Critical patent/SE448951B/en

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

A catalyst, for hydrotreating heavy feedstocks, comprised of nickel and molybdenum supported on alumina having a defined pore size distribution which has been calcined at a temperature of from 621 DEG C to 705 DEG C, and a process for hydrotreating using the catalyst. Calcining of such a catalyst at such temperatures has been found to provide for effective use thereof as a hydrotreating catalyst for higher boiling feedstocks.
SE8106925A 1980-11-21 1981-11-20 HYDRATION CATALYST AND METHOD OF CATALYTIC HYDRATION SE448951B (en)

Applications Claiming Priority (1)

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

Publications (2)

Publication Number Publication Date
SE8106925L true SE8106925L (en) 1982-05-22
SE448951B SE448951B (en) 1987-03-30

Family

ID=22776714

Family Applications (1)

Application Number Title Priority Date Filing Date
SE8106925A SE448951B (en) 1980-11-21 1981-11-20 HYDRATION CATALYST AND METHOD OF CATALYTIC HYDRATION

Country Status (12)

Country Link
JP (1) JPS5946666B2 (en)
AU (1) AU540245B2 (en)
CA (1) CA1159039A (en)
DE (1) DE3145718A1 (en)
ES (1) ES507340A0 (en)
FR (1) FR2494597A1 (en)
GB (1) GB2087747B (en)
IT (1) IT1143446B (en)
MX (2) MX172430B (en)
NL (1) NL8105267A (en)
SE (1) SE448951B (en)
ZA (1) ZA817732B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3522538A1 (en) * 1984-06-22 1986-01-02 Chiyoda Chemical Engineering & Construction Co. Ltd., Yokohama, Kanagawa Process and catalyst for the hydrogenation of coal tar pitch
DE3581777D1 (en) * 1984-09-12 1991-03-28 Nippon Kokan Kk HYDROGENATING CATALYST FOR CARBON TEAR, METHOD FOR HYDROGENATING CARBON TAR WITH THE CATALYST, AND METHOD FOR PRODUCING SUPER NEEDLE COCONUT FROM THE HYDROGENATING PRODUCT OF CARBON TAR.
GC0000065A (en) * 1998-09-01 2004-06-30 Japan Energy Corp Hydrocracking catalyst, producing method threof, and hydrocracking method.
JP4493997B2 (en) * 2003-12-10 2010-06-30 財団法人石油産業活性化センター Hydrodesulfurization catalyst for hydrocarbon oil and method for producing the same
US8110527B2 (en) 2006-08-11 2012-02-07 China Petroleum & Chemical Corporation Alumina having a complex pore structure, and catalyst and process for selective hydrogenation of cracking gasoline
JP4902424B2 (en) * 2007-05-21 2012-03-21 Ｊｘ日鉱日石エネルギー株式会社 Hydrorefining catalyst and hydrorefining method

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL261905A (en) * 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 (en) * 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
ZA817732B (en) 1982-10-27
NL8105267A (en) 1982-06-16
SE448951B (en) 1987-03-30
IT8149747A0 (en) 1981-11-20
FR2494597A1 (en) 1982-05-28
ES507340A1 (en) 1985-03-01
GB2087747B (en) 1984-07-04
CA1159039A (en) 1983-12-20
AU7747681A (en) 1982-05-27
DE3145718C2 (en) 1987-06-19
MX160789A (en) 1990-05-17
FR2494597B1 (en) 1985-01-04
MX172430B (en) 1993-12-16
GB2087747A (en) 1982-06-03
JPS5946666B2 (en) 1984-11-14
AU540245B2 (en) 1984-11-08
DE3145718A1 (en) 1982-06-16
ES507340A0 (en) 1985-03-01
JPS57117343A (en) 1982-07-21
IT1143446B (en) 1986-10-22

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