GB1436458A - Catalyst method of manufacture and use thereof - Google Patents

Catalyst method of manufacture and use thereof

Info

Publication number
GB1436458A
GB1436458A GB3920273A GB3920273A GB1436458A GB 1436458 A GB1436458 A GB 1436458A GB 3920273 A GB3920273 A GB 3920273A GB 3920273 A GB3920273 A GB 3920273A GB 1436458 A GB1436458 A GB 1436458A
Authority
GB
United Kingdom
Prior art keywords
catalyst
aug
yield
liquid volume
metal component
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
GB3920273A
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.)
Honeywell UOP LLC
Original Assignee
UOP LLC
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 UOP LLC filed Critical UOP LLC
Publication of GB1436458A publication Critical patent/GB1436458A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/08Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the faujasite type, e.g. type X or Y
    • B01J29/16Crystalline 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/16Alumino-silicates
    • B01J20/18Synthetic zeolitic molecular sieves
    • B01J20/183Physical conditioning without chemical treatment, e.g. drying, granulating, coating, irradiation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking 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
    • C10G47/12Inorganic carriers
    • C10G47/16Crystalline alumino-silicate carriers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
GB3920273A 1972-08-21 1973-08-20 Catalyst method of manufacture and use thereof Expired GB1436458A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US28261672A 1972-08-21 1972-08-21

Publications (1)

Publication Number Publication Date
GB1436458A true GB1436458A (en) 1976-05-19

Family

ID=23082313

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3920273A Expired GB1436458A (en) 1972-08-21 1973-08-20 Catalyst method of manufacture and use thereof

Country Status (10)

Country Link
JP (1) JPS5216876B2 (de)
CA (1) CA1022918A (de)
DE (1) DE2341854C3 (de)
EG (1) EG11609A (de)
ES (1) ES418012A1 (de)
FR (1) FR2196847B1 (de)
GB (1) GB1436458A (de)
IN (1) IN140506B (de)
IT (1) IT990387B (de)
ZA (1) ZA735587B (de)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4476011A (en) * 1980-10-24 1984-10-09 Standard Oil Company (Indiana) Catalyst and process for the hydrogenitrogenation and hydrocracking of high-nitrogen feeds
EP1038579A1 (de) * 1997-12-10 2000-09-27 Idemitsu Kosan Company Limited Verfahren zur herstellung von katalysatoren
US6812180B2 (en) 1997-12-10 2004-11-02 Idemitsu Kosan Co., Ltd. Method for preparing catalyst
US7335800B2 (en) 2005-04-21 2008-02-26 Shell Oil Company Hydrogenation catalyst and hydrogenation method
US7381852B2 (en) 2006-04-13 2008-06-03 Shell Oil Company Process for hydrogenating an aldehyde
US7777085B2 (en) 2008-10-01 2010-08-17 Inventure Chemical, Inc. Method for conversion of oil-containing algae to 1,3-propanediol
US7943792B2 (en) 2007-04-02 2011-05-17 Inventure Chemical Inc. Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of materials with oil-containing substituents including phospholipids and peptidic content
US8212062B2 (en) 2007-04-02 2012-07-03 Inventure Chemical, Inc. Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of oil-containing materials with cellulosic and peptidic content

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3236761A (en) * 1951-01-28 1966-02-22 Union Carbide Corp Hydrocarbon conversion process and catalyst
NO115009B (de) * 1962-05-17 1968-07-01 Mobil Oil Corp
US3267022A (en) * 1964-01-24 1966-08-16 Union Oil Co Hydrocracking process and catalysts
US3384572A (en) * 1964-08-03 1968-05-21 Mobil Oil Corp Catalytic hydrocracking
US3293192A (en) * 1965-08-23 1966-12-20 Grace W R & Co Zeolite z-14us and method of preparation thereof
GB1158257A (en) * 1966-12-07 1969-07-16 Standard Oil Co Hydroprocessing Catalyst and Process.
US3424671A (en) * 1967-03-20 1969-01-28 Union Oil Co Hydrocracking processs with preconditioned zeolite catalyst
NL166494C (nl) * 1969-04-10 1981-08-17 Standard Oil Co Werkwijze voor het hydrokraken van een mengsel van petroleumkoolwaterstoffen, dat boven 180 graden c kookt en 1 tot 3000 mg/kg stikstof bevat.
NL168194C (nl) * 1970-02-25 1982-03-16 Shell Int Research Werkwijze voor de bereiding van aluminosilicaatzeolieten.

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4476011A (en) * 1980-10-24 1984-10-09 Standard Oil Company (Indiana) Catalyst and process for the hydrogenitrogenation and hydrocracking of high-nitrogen feeds
EP1038579A1 (de) * 1997-12-10 2000-09-27 Idemitsu Kosan Company Limited Verfahren zur herstellung von katalysatoren
EP1038579A4 (de) * 1997-12-10 2002-02-06 Idemitsu Kosan Co Verfahren zur herstellung von katalysatoren
US6812180B2 (en) 1997-12-10 2004-11-02 Idemitsu Kosan Co., Ltd. Method for preparing catalyst
US7335800B2 (en) 2005-04-21 2008-02-26 Shell Oil Company Hydrogenation catalyst and hydrogenation method
US7381852B2 (en) 2006-04-13 2008-06-03 Shell Oil Company Process for hydrogenating an aldehyde
US7943792B2 (en) 2007-04-02 2011-05-17 Inventure Chemical Inc. Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of materials with oil-containing substituents including phospholipids and peptidic content
US8212062B2 (en) 2007-04-02 2012-07-03 Inventure Chemical, Inc. Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of oil-containing materials with cellulosic and peptidic content
US8592613B2 (en) 2007-04-02 2013-11-26 Inventure Renewables, Inc. Production of biodiesel, cellulosic sugars, and peptides from the simultaneous esterification and alcoholysis/hydrolysis of materials with oil-containing substituents including phospholipids and cellulosic and peptidic content
US7777085B2 (en) 2008-10-01 2010-08-17 Inventure Chemical, Inc. Method for conversion of oil-containing algae to 1,3-propanediol

Also Published As

Publication number Publication date
AU5937873A (en) 1975-02-20
CA1022918A (en) 1977-12-20
ZA735587B (en) 1974-07-31
ES418012A1 (es) 1976-02-16
IN140506B (de) 1976-11-20
FR2196847B1 (de) 1979-01-19
DE2341854A1 (de) 1974-03-21
DE2341854C3 (de) 1981-07-30
JPS49133289A (de) 1974-12-20
FR2196847A1 (de) 1974-03-22
JPS5216876B2 (de) 1977-05-12
IT990387B (it) 1975-06-20
DE2341854B2 (de) 1978-10-12
EG11609A (en) 1978-03-29

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PCNP Patent ceased through non-payment of renewal fee