NL6616849A - - Google Patents

Info

Publication number
NL6616849A
NL6616849A NL6616849A NL6616849A NL6616849A NL 6616849 A NL6616849 A NL 6616849A NL 6616849 A NL6616849 A NL 6616849A NL 6616849 A NL6616849 A NL 6616849A NL 6616849 A NL6616849 A NL 6616849A
Authority
NL
Netherlands
Application number
NL6616849A
Other versions
NL139246B (nl
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 filed Critical
Publication of NL6616849A publication Critical patent/NL6616849A/xx
Publication of NL139246B publication Critical patent/NL139246B/xx

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
    • 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
    • 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
    • B01J35/64—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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/36—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed through which there is an essentially horizontal flow of particles
    • 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
    • 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
    • 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
    • B01J23/90—Regeneration or reactivation
    • 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
    • C10G2300/10—Feedstock materials
    • C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
    • 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
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/06—Gasoil

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
NL666616849A 1965-11-30 1966-11-30 Werkwijze voor de behandeling van zware gasolien en koolwaterstofresiduen met waterstof. NL139246B (nl)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US510656A US3393148A (en) 1965-11-30 1965-11-30 Hydrofining catalyst and process using same

Publications (2)

Publication Number Publication Date
NL6616849A true NL6616849A (de) 1967-05-31
NL139246B NL139246B (nl) 1973-07-16

Family

ID=24031628

Family Applications (1)

Application Number Title Priority Date Filing Date
NL666616849A NL139246B (nl) 1965-11-30 1966-11-30 Werkwijze voor de behandeling van zware gasolien en koolwaterstofresiduen met waterstof.

Country Status (8)

Country Link
US (1) US3393148A (de)
BE (1) BE690488A (de)
DE (1) DE1545397C3 (de)
DK (1) DK129945B (de)
ES (1) ES333965A1 (de)
FR (1) FR1503063A (de)
NL (1) NL139246B (de)
SE (1) SE335896B (de)

Families Citing this family (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3471399A (en) * 1967-06-09 1969-10-07 Universal Oil Prod Co Hydrodesulfurization catalyst and process for treating residual fuel oils
US3509044A (en) * 1967-06-26 1970-04-28 Exxon Research Engineering Co Hydrodesulfurization of petroleum residuum
US3449456A (en) * 1968-06-03 1969-06-10 Exxon Research Engineering Co Startup procedure of isomerizing polymethylbenzene
BE755778A (fr) * 1969-09-05 1971-03-04 Texaco Development Corp Desulfuration des huiles hydrocarbonees lourdes
US3548020A (en) * 1969-10-29 1970-12-15 Standard Oil Co Process for the disproportionation of petroleum hydrocarbons
US3669873A (en) * 1970-03-31 1972-06-13 Chevron Res Hydrofining-hydrocracking process
FR2097016B1 (de) * 1970-07-27 1973-05-25 Inst Francais Du Petrole
US3793186A (en) * 1971-07-19 1974-02-19 Chevron Res Lube oil improvement
IT965445B (it) * 1971-09-24 1974-01-31 Standard Oil Co Perfezionamento nel procedimento per il trattamento con idrogeno di olii idrocarburici del petrolio e composizione catalitica impiegata
GB1397959A (en) * 1971-09-24 1975-06-18 Standard Oil Co Catalyst and process for hydrotreating petroleum hydrocarbons
US3923638A (en) * 1971-12-10 1975-12-02 Standard Oil Co Two-catalyst hydrocracking process
US3926786A (en) * 1972-11-20 1975-12-16 Texaco Inc Production of lubricating oils
US3944482A (en) * 1973-08-08 1976-03-16 Gulf Research & Development Company Process for the cracking of high metals content feedstocks
US3893947A (en) * 1973-09-10 1975-07-08 Union Oil Co Group VI-B metal catalyst preparation
US3977962A (en) * 1974-02-07 1976-08-31 Exxon Research And Engineering Company Heavy crude conversion
US3977961A (en) * 1974-02-07 1976-08-31 Exxon Research And Engineering Company Heavy crude conversion
US3928176A (en) * 1974-04-01 1975-12-23 Exxon Research Engineering Co Heavy crude conversion
US4082695A (en) * 1975-01-20 1978-04-04 Mobil Oil Corporation Catalyst for residua demetalation and desulfurization
US4069139A (en) * 1975-12-29 1978-01-17 Exxon Research & Engineering Co. Hydrodesulfurization of oil utilizing a narrow pore size distribution catalyst
GB1597165A (en) * 1977-03-30 1981-09-03 Exxon France White oils and method of making same
FR2390493B1 (fr) * 1977-05-12 1985-04-26 Linde Ag Procede de preparation d'olefines
US4191635A (en) * 1977-12-21 1980-03-04 Standard Oil Company (Indiana) Process for the cracking of heavy hydrocarbon streams
US4257922A (en) * 1979-03-13 1981-03-24 Electric Power Research Institute, Inc. Process for coal liquefaction and catalyst
US4242236A (en) * 1979-03-29 1980-12-30 Chevron Research Company 65-130 Angstrom mean radius silica-alumina catalyst support
US4301037A (en) * 1980-04-01 1981-11-17 W. R. Grace & Co. Extruded alumina catalyst support having controlled distribution of pore sizes
EP0042461B1 (de) * 1980-06-23 1984-05-02 Exxon Research And Engineering Company Verfahren zur katalytischen Hydrierung hydrierbarer Verbindungen in einer Kohlenwasserstofffraktion und hydrierte Kohlenwasserstoffprodukte
US4513090A (en) * 1981-07-09 1985-04-23 Exxon Research And Engineering Co. Crystalline silica zeolite-containing catalyst
US4431526A (en) * 1982-07-06 1984-02-14 Union Oil Company Of California Multiple-stage hydroprocessing of hydrocarbon oil
US4780446A (en) * 1982-09-30 1988-10-25 W. R. Grace & Co. Alumina-silica cogel
US4548710A (en) * 1982-12-28 1985-10-22 Union Oil Company Of California Hydrocarbon processing
US4460707A (en) * 1982-12-28 1984-07-17 Union Oil Company Of California Hydroprocessing catalyst and method for preparing it
US4913797A (en) * 1985-11-21 1990-04-03 Mobil Oil Corporation Catalyst hydrotreating and dewaxing process
US8114806B2 (en) 2008-04-10 2012-02-14 Shell Oil Company Catalysts having selected pore size distributions, method of making such catalysts, methods of producing a crude product, products obtained from such methods, and uses of products obtained

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2890162A (en) * 1955-02-28 1959-06-09 Exxon Research Engineering Co Porous silica free gamma alumina base contacting agents and use thereof
US2924568A (en) * 1955-02-28 1960-02-09 Exxon Research Engineering Co Process for hydrodesulfurizing and subsequently catalytically cracking gas oil
US2962435A (en) * 1956-12-14 1960-11-29 Union Oil Co Hydrocarbon cracking process and catalyst
US3020245A (en) * 1959-05-27 1962-02-06 Catalysts & Chem Inc Preparation of catalysts containing cobalt and molybdenum oxides
GB931936A (en) * 1960-04-06 1963-07-24 British Petroleum Co Improvements relating to the production of alumina
NL262698A (de) * 1960-04-15
DE1256824B (de) * 1960-11-29 1967-12-21 Union Oil Co Verfahren zum Hydrocracken von Kohlenwasserstoffen
US3143491A (en) * 1962-02-20 1964-08-04 Socony Mobil Oil Co Inc Catalytic conversion of hydrocarbons with a silica-alumina and crystalline zeolite catalyst composite
US3169918A (en) * 1962-07-02 1965-02-16 Universal Oil Prod Co Hydrorefining heavy oils using a pseudo-dry catalyst
US3242101A (en) * 1962-07-24 1966-03-22 Sinclair Research Inc Nickel-molybdenum-alumina hydrocarbon conversion catalyst
US3277018A (en) * 1964-01-24 1966-10-04 Mobil Oil Selective cracking catalyst
US3322666A (en) * 1964-08-25 1967-05-30 Gulf Research Development Co Chemical process for hydrocracking and hydrorefining of hydrocarbon oils

Also Published As

Publication number Publication date
FR1503063A (fr) 1967-11-24
US3393148A (en) 1968-07-16
DK129945B (da) 1974-12-02
SE335896B (de) 1971-06-14
DK129945C (de) 1975-05-12
ES333965A1 (es) 1967-10-16
DE1545397B2 (de) 1979-10-18
BE690488A (de) 1967-05-02
DE1545397C3 (de) 1984-05-30
DE1545397A1 (de) 1970-01-29
NL139246B (nl) 1973-07-16

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Legal Events

Date Code Title Description
NL80 Information provided on patent owner name for an already discontinued patent

Owner name: STANDARD OIL

V4 Discontinued because of reaching the maximum lifetime of a patent