GB1346856A

GB1346856A – Regeneration of dehydrogenation catalysts
– Google Patents

GB1346856A – Regeneration of dehydrogenation catalysts
– Google Patents
Regeneration of dehydrogenation catalysts

Info

Publication number
GB1346856A

GB1346856A
GB1795871A
GB1795871A
GB1346856A
GB 1346856 A
GB1346856 A
GB 1346856A
GB 1795871 A
GB1795871 A
GB 1795871A
GB 1795871 A
GB1795871 A
GB 1795871A
GB 1346856 A
GB1346856 A
GB 1346856A
Authority
GB
United Kingdom
Prior art keywords
tin
catalyst
deactivated
platinum
catalysts
Prior art date
1970-06-03
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
GB1795871A
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.)

Phillips Petroleum Co

Original Assignee
Phillips Petroleum 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.)
1970-06-03
Filing date
1971-05-28
Publication date
1974-02-13

1971-05-28
Application filed by Phillips Petroleum Co
filed
Critical
Phillips Petroleum Co

1974-02-13
Publication of GB1346856A
publication
Critical
patent/GB1346856A/en

Status
Expired
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

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

B01J23/835—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 germanium, tin or lead

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

B01J23/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead

B01J23/622—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead

B01J23/626—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead with tin

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

B01J23/94—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper

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

B01J23/96—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the noble metals

C—CHEMISTRY; METALLURGY

C07—ORGANIC CHEMISTRY

C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS

C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms

C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen

C07C5/321—Catalytic processes

C07C5/324—Catalytic processes with metals

C07C5/325—Catalytic processes with metals of the platinum group

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

C10G35/00—Reforming naphtha

C10G35/04—Catalytic reforming

C10G35/06—Catalytic reforming characterised by the catalyst used

C10G35/085—Catalytic reforming characterised by the catalyst used containing platinum group metals or compounds thereof

C10G35/09—Bimetallic catalysts in which at least one of the metals is a platinum group metal

Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE

Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS

Y02P20/00—Technologies relating to chemical industry

Y02P20/50—Improvements relating to the production of bulk chemicals

Y02P20/584—Recycling of catalysts

Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC

Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS

Y10S585/00—Chemistry of hydrocarbon compounds

Y10S585/8995—Catalyst and recycle considerations

Y10S585/901—Catalyst and recycle considerations with recycle, rehabilitation, or preservation of solvent, diluent, or mass action agent

Abstract

1346856 Dehydrogenation catalysts PHILLIPS PETROLEUM CO 28 May 1971 [3 June 1970] 17958/71 Heading B1E [Also in Division C5] The activity of deactivated dehydrogenation catalyst comprising Group VIII metal selected for example from nickel, ruthenium, rhodium, palladium, osmium, iridium and platinum and, optionally, activator material, for example selected from compounds of alkali metals, alkaline earth metals, germanium, tin and lead, and/or support material, for example selected from alumina (including HF-treated alumina and flame-hydrolyzed alumina), magnesia, silica, zirconia, aluminosilicates and Group II metal aluminate spinels, is restored by a process wherein the deactivated catalyst is impregnated, optionally after oxidative burnoff to remove carbonaceous deposit, with tin or a compound thereof in an amount sufficient to provide that the reactivated catalyst contains, additional to any tin present in the deactivated catalyst, from 0.01 to 2 weight per cent of tin. The impregnated catalyst may be dried, for example at a temperature of from 100 to 400‹F, and calcined, for example at a temperature of from 800 to 1200‹F. Impregnation may be effected either by vaporization of tin or a compound thereof in the presence of the catalyst or by the use of solution; the specification discloses many suitable solvents for use in preparing such solution, water being preferred, and many suitable tin compounds which must be convertible to tin or tin oxide, must be silicon-free and preferably contain no metal other than tin and alkali metal. As exemplified, deactivated catalysts comprising platinum and tin supported on zinc aluminate spinel are immersed in aqueous stannous chloride solution and subsequently dried and, optionally, calcined at 1050‹F in air; details relating to the initial preparation of such catalysts are given in the specification. Reference also is made to impregnating with platinum a deactivated catalyst comprising platinum and tin supported on zinc aluminate spinel.

GB1795871A
1970-06-03
1971-05-28
Regeneration of dehydrogenation catalysts

Expired

GB1346856A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

US4320270A

1970-06-03
1970-06-03

Publications (1)

Publication Number
Publication Date

GB1346856A
true

GB1346856A
(en)

1974-02-13

Family
ID=21926008
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB1795871A
Expired

GB1346856A
(en)

1970-06-03
1971-05-28
Regeneration of dehydrogenation catalysts

Country Status (6)

Country
Link

US
(1)

US3674706A
(en)

BE
(1)

BE768047A
(en)

CA
(1)

CA977327A
(en)

DE
(1)

DE2127353C3
(en)

FR
(1)

FR2095869A5
(en)

GB
(1)

GB1346856A
(en)

Cited By (5)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

WO2010069548A1
(en)

2008-12-18
2010-06-24
Uhde Gmbh
Variation of the tin impregnation of a catalyst for the dehydrogenation of alkanes

DE102008062782A1
(en)

2008-12-18
2010-07-01
Uhde Gmbh
Catalyst, useful to dehydrogenate alkane or alkyl substituent of hydrocarbon, comprises molding body containing oxide of group II-IV elements as base material, and platinum compound and compound of element of group IV as surface component

DE102009056539A1
(en)

2009-12-03
2011-06-09
Uhde Gmbh
Catalyst, useful to dehydrogenate alkane or alkyl substituent of hydrocarbon, comprises molding body containing oxide of group II-IV elements as base material, and platinum compound and compound of element of group IV as surface component

WO2015022548A1
(en)

*

2013-08-15
2015-02-19
University College Cardiff Consultants Ltd
Catalyst for direct synthesis of hydrogen peroxide

CN114425364A
(en)

*

2020-10-15
2022-05-03
中国石油化工股份有限公司
Catalyst for preparing butadiene by oxidative dehydrogenation of butene, preparation method and application thereof

Families Citing this family (19)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US3883418A
(en)

*

1973-01-02
1975-05-13
Phillips Petroleum Co
Lead free motor fuel production

US3894110A
(en)

*

1973-11-15
1975-07-08
Phillips Petroleum Co
Catalytic dehydrogenation process

US4169815A
(en)

*

1973-11-15
1979-10-02
Phillips Petroleum Company
Catalyst for dehydrogenation process

US4268188A
(en)

*

1979-08-06
1981-05-19
Phillips Petroleum Company
Process for reducing possibility of leaching of heavy metals from used petroleum cracking catalyst in land fills

US4348273A
(en)

*

1980-06-25
1982-09-07
Phillips Petroleum Company
Treating cracking catalyst fines containing a passivating material

NL8202647A
(en)

*

1982-07-01
1984-02-01
Shell Int Research

METHOD FOR PREPARING A CATALYST

US4568784A
(en)

*

1985-02-19
1986-02-04
Phillips Petroleum Company
Preparation of polymethylbenzenes

US4692430A
(en)

*

1985-06-17
1987-09-08
Phillips Petroleum Company
Zinc aluminate double bond isomerization catalyst and process for its production

US4620053A
(en)

*

1985-06-17
1986-10-28
Phillips Petroleum Company
Zinc aluminate double bond isomerization catalyst and double bond isomerization of olefins employing said catalyst

US5344805A
(en)

*

1993-05-03
1994-09-06
Phillips Petroleum Company
Platinum and tin-containing catalyst and use thereof in alkane dehydrogenation

US5710091A
(en)

1995-06-07
1998-01-20
Phillips Petroleum Company
Sorbent compositions

US5898011A
(en)

*

1997-08-28
1999-04-27
Phillips Petroleum Company
Hydrocarbon conversion catalyst composition and processes therefor and therewith

US6218328B1
(en)

1998-12-29
2001-04-17
Phillips Petroleum Company
Method of preparing a zeolite based catalyst material

US6740615B2
(en)

*

2000-12-22
2004-05-25
Hydrocarbon Technologies, Inc.
Regeneration of used supported noble metal catalysts

US6908873B2
(en)

*

2000-12-22
2005-06-21
Headwaters Nanokinetix, Inc.
Regeneration of spent supported metal catalysts

US7655137B2
(en)

*

2003-07-14
2010-02-02
Headwaters Technology Innovation, Llc
Reforming catalysts having a controlled coordination structure and methods for preparing such compositions

US7569508B2
(en)

*

2004-11-17
2009-08-04
Headwaters Technology Innovation, Llc
Reforming nanocatalysts and method of making and using such catalysts

US7632775B2
(en)

*

2004-11-17
2009-12-15
Headwaters Technology Innovation, Llc
Multicomponent nanoparticles formed using a dispersing agent

US7541309B2
(en)

*

2006-05-16
2009-06-02
Headwaters Technology Innovation, Llc
Reforming nanocatalysts and methods of making and using such catalysts

1970

1970-06-03
US
US43202A
patent/US3674706A/en
not_active
Expired – Lifetime

1971

1971-02-16
CA
CA105,488A
patent/CA977327A/en
not_active
Expired

1971-05-28
GB
GB1795871A
patent/GB1346856A/en
not_active
Expired

1971-06-02
DE
DE2127353A
patent/DE2127353C3/en
not_active
Expired

1971-06-03
FR
FR7120141A
patent/FR2095869A5/fr
not_active
Expired

1971-06-03
BE
BE768047A
patent/BE768047A/en
unknown

Cited By (6)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

WO2010069548A1
(en)

2008-12-18
2010-06-24
Uhde Gmbh
Variation of the tin impregnation of a catalyst for the dehydrogenation of alkanes

DE102008062782A1
(en)

2008-12-18
2010-07-01
Uhde Gmbh
Catalyst, useful to dehydrogenate alkane or alkyl substituent of hydrocarbon, comprises molding body containing oxide of group II-IV elements as base material, and platinum compound and compound of element of group IV as surface component

DE102009056539A1
(en)

2009-12-03
2011-06-09
Uhde Gmbh
Catalyst, useful to dehydrogenate alkane or alkyl substituent of hydrocarbon, comprises molding body containing oxide of group II-IV elements as base material, and platinum compound and compound of element of group IV as surface component

WO2015022548A1
(en)

*

2013-08-15
2015-02-19
University College Cardiff Consultants Ltd
Catalyst for direct synthesis of hydrogen peroxide

CN105579131A
(en)

*

2013-08-15
2016-05-11
卡迪夫大学顾问有限公司
Catalyst for direct synthesis of hydrogen peroxide

CN114425364A
(en)

*

2020-10-15
2022-05-03
中国石油化工股份有限公司
Catalyst for preparing butadiene by oxidative dehydrogenation of butene, preparation method and application thereof

Also Published As

Publication number
Publication date

BE768047A
(en)

1971-12-03

CA977327A
(en)

1975-11-04

DE2127353C3
(en)

1975-03-20

DE2127353A1
(en)

1971-12-09

FR2095869A5
(en)

1972-02-11

US3674706A
(en)

1972-07-04

DE2127353B2
(en)

1974-07-11

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Legal Events

Date
Code
Title
Description

1974-07-03
PS
Patent sealed [section 19, patents act 1949]

1976-12-22
PLNP
Patent lapsed through nonpayment of renewal fees

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