GB352850A - An improved process for the reactivation of catalyst used in the destructive hydrogenation of hydrocarbon oils - Google Patents

An improved process for the reactivation of catalyst used in the destructive hydrogenation of hydrocarbon oils

Info

Publication number
GB352850A
GB352850A GB31445/30A GB3144530A GB352850A GB 352850 A GB352850 A GB 352850A GB 31445/30 A GB31445/30 A GB 31445/30A GB 3144530 A GB3144530 A GB 3144530A GB 352850 A GB352850 A GB 352850A
Authority
GB
United Kingdom
Prior art keywords
hydrogen
catalyst used
reactivation
hydrogenation
destructive hydrogenation
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
GB31445/30A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development 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 Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB352850A publication Critical patent/GB352850A/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
    • B01J38/00Regeneration or reactivation of catalysts, in general

Abstract

Catalyst used in the destructive hydrogenation of oils, and not susceptible to sulphur poisoning, is reactivated by separating it from the oil and treating it with hydrogen, preferably at an elevated pressure such as 50 atmospheres or more and at a temperature not above 700 DEG F. The hydrogen is preferably free from hydrocarbons liquid at normal temperature: gases from a hydrogenation retort may be used after cooling and scrubbing with oil under pressure. If unpurified hydrogen is used, the catalyst should preferably be treated with substantially pure hydrogen for a short period before return to the retort. Catalysts specified are the oxides and sulphides of chromium, molybdenum, tungsten, aluminium, zinc, and of the metals of the alkali, alkaline earth, and rare earth groups.
GB31445/30A 1929-11-13 1930-10-20 An improved process for the reactivation of catalyst used in the destructive hydrogenation of hydrocarbon oils Expired GB352850A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US352850XA 1929-11-13 1929-11-13

Publications (1)

Publication Number Publication Date
GB352850A true GB352850A (en) 1931-07-16

Family

ID=21881719

Family Applications (1)

Application Number Title Priority Date Filing Date
GB31445/30A Expired GB352850A (en) 1929-11-13 1930-10-20 An improved process for the reactivation of catalyst used in the destructive hydrogenation of hydrocarbon oils

Country Status (1)

Country Link
GB (1) GB352850A (en)

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