ES398632A1 - Hydrodesulphurization catalyst and preparation and use thereof - Google Patents

Hydrodesulphurization catalyst and preparation and use thereof

Info

Publication number
ES398632A1
ES398632A1 ES398632A ES398632A ES398632A1 ES 398632 A1 ES398632 A1 ES 398632A1 ES 398632 A ES398632 A ES 398632A ES 398632 A ES398632 A ES 398632A ES 398632 A1 ES398632 A1 ES 398632A1
Authority
ES
Spain
Prior art keywords
calcination
subjecting
precursor
hours
approximately
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
ES398632A
Other languages
Spanish (es)
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 ES398632A1 publication Critical patent/ES398632A1/en
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
    • 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
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56—Platinum group metals
    • B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652—Chromium, molybdenum or tungsten
    • 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

Landscapes

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

Abstract

Method for preparing a catalyst for residual oil hydrodesulfurization, which comprises formulating or composing a support material with the precursor of at least one catalytically active metallic component chosen from each of groups VIB and VIII of the Periodic Table of the Elements, said precursor being in the form of one or more thermally decomposable compounds, containing one or more of said chosen metals; subjecting the resulting composite body, if desired, after first drying it, to a first calcination for at least 0.5 hours, in an oxidizing atmosphere containing more than 20% by volume of water vapor, at a temperature between approximately 260ºC and approximately 371ºC; and then subjecting the composite body to a second calcination for a period of from about 1 to about 4 hours, in a substantially dry oxidizing atmosphere and at a temperature of between about 427ºC and about 649ºC. (Machine-translation by Google Translate, not legally binding)
ES398632A 1971-01-11 1972-01-05 Hydrodesulphurization catalyst and preparation and use thereof Expired ES398632A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10569971A 1971-01-11 1971-01-11

Publications (1)

Publication Number Publication Date
ES398632A1 true ES398632A1 (en) 1974-10-01

Family

ID=22307315

Family Applications (1)

Application Number Title Priority Date Filing Date
ES398632A Expired ES398632A1 (en) 1971-01-11 1972-01-05 Hydrodesulphurization catalyst and preparation and use thereof

Country Status (17)

Country Link
JP (1) JPS526712B1 (en)
BR (1) BR7200140D0 (en)
CA (1) CA967544A (en)
CS (1) CS170174B2 (en)
DD (1) DD95642A5 (en)
ES (1) ES398632A1 (en)
FR (1) FR2121654B1 (en)
GB (1) GB1367243A (en)
HU (1) HU167392B (en)
IE (1) IE35954B1 (en)
IT (1) IT948166B (en)
MY (1) MY7700067A (en)
NL (1) NL172832C (en)
PL (1) PL77342B1 (en)
SU (1) SU429572A3 (en)
YU (1) YU34847B (en)
ZA (1) ZA7230B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4191635A (en) * 1977-12-21 1980-03-04 Standard Oil Company (Indiana) Process for the cracking of heavy hydrocarbon streams
US4181602A (en) 1977-12-21 1980-01-01 Standard Oil Company (Indiana) Process for the hydrotreating of heavy hydrocarbon streams
US4188284A (en) * 1977-12-21 1980-02-12 Standard Oil Company (Indiana) Process for the hydrotreating of heavy hydrocarbon streams
US4306965A (en) 1979-03-19 1981-12-22 Standard Oil Company (Indiana) Hydrotreating process
US4224144A (en) 1979-03-19 1980-09-23 Standard Oil Company (Indiana) Hydrotreating a hydrocarbon stream to remove nitrogen and sulfur
CN119613219B (en) * 2025-02-13 2025-04-29 孝义市晋茂化工有限公司 Coking crude benzene catalytic hydrofining method

Also Published As

Publication number Publication date
NL172832C (en) 1983-11-01
NL172832B (en) 1983-06-01
CA967544A (en) 1975-05-13
JPS526712B1 (en) 1977-02-24
GB1367243A (en) 1974-09-18
SU429572A3 (en) 1974-05-25
DE2200269B2 (en) 1975-12-11
AU3764772A (en) 1973-07-12
NL7200426A (en) 1972-07-13
DD95642A5 (en) 1973-02-12
MY7700067A (en) 1977-12-31
YU34847B (en) 1980-04-30
IE35954L (en) 1972-07-11
BR7200140D0 (en) 1973-06-14
IT948166B (en) 1973-05-30
FR2121654A1 (en) 1972-08-25
PL77342B1 (en) 1975-04-30
YU3272A (en) 1979-10-31
HU167392B (en) 1975-09-27
DE2200269A1 (en) 1972-07-27
IE35954B1 (en) 1976-07-07
ZA7230B (en) 1972-09-27
CS170174B2 (en) 1976-08-27
FR2121654B1 (en) 1974-06-21

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Legal Events

Date Code Title Description
FD1A Patent lapsed

Effective date: 19850207