US2003204102A1PendingUtilityA1
Method for oxidizing hydrocarbons
Priority: Aug 7, 1998Filed: Jun 3, 2003Published: Oct 30, 2003
Est. expiryAug 7, 2018(expired)· nominal 20-yr term from priority
Y10S977/775C07C 29/50C07B 41/00Y10S977/811Y10S977/89Y10S977/896C07D 301/10C07D 301/04Y10S977/773
30
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Claims
Abstract
The present invention relates to a catalyst for oxidizing hydrocarbons with a hydrogen/oxygen mixture. The catalyst contains a) a support material containing titanium and b) silver particles having an average particle size of from 0.3 to 100 nm.
Claims
exact text as granted — not AI-modified1 . Process for the oxidation of hydrocarbons in the presence of a hydrogen/oxygen mixture on a catalyst which contains silver, containing
a) a support containing titanium and b) silver particles with an average particle size from 0.3 to 100 nm.
2 . Process according to claim 1 , characterized in that olefins are used as hydrocarbons.
3 . Catalyst containing silver for the oxidation of hydrocarbons containing
a) a support containing titanium and b) silver particles with an average particle size from 0.3 to 100 run.
4 . Use of a catalyst according to claim 3 for the oxidation of hydrocarbons.
5 . Process according to one of more of claims 1 to 4 , characterized in that titanyl hydrates, titanium dioxides and silicon/titanium mixed oxides are preferably used as catalyst support.
6 . Process according to one or more of claims 1 to 4 , characterized in that before titanium application the catalyst support containing silicon is subjected to a treatment with water or aqueous salt solutions (e.g. solutions of ammonium chloride, ammonium nitrate, calcium nitrate, lanthanum nitrate) and the surplus water is then removed.
7 . Process according to one or more of claims 1 to 6 , characterized in that promoters from the groups (IUPAC periodic system, 1985) 1, 2, preferably potassium, caesium, magnesium, and from the groups 5, preferably tantalum, and from group 13, preferably Al are used.
8 . Process according to one or more of claims 1 to 6 , characterized in that sulfate contents from 0.1 to 1 wt. % are favourable when titanyl hydrates and/or titanium dioxides are used as catalyst support.Join the waitlist — get patent alerts
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