초록 ▼

There is disclosed an improved process of olefin metathesis which employs catalysts which are tungsten oxides or tungsten sulfides on suitable supports. The improvement is the pretreatment of such catalysts or the regeneration of such catalysts with ethylene or a butene at about 450°C to about 750°C

There is disclosed an improved process of olefin metathesis which employs catalysts which are tungsten oxides or tungsten sulfides on suitable supports. The improvement is the pretreatment of such catalysts or the regeneration of such catalysts with ethylene or a butene at about 450°C to about 750°C.

대표청구항 ▼

In a process of converting an olefin in an olefin metathesis reaction wherein at least one olefin selected from the group of cyclic and acyclic mono and polyene olefin hydrocarbons and mixtures of such hydrocarbons are converted in a reaction zone to products of the olefin metathesis reaction, which

In a process of converting an olefin in an olefin metathesis reaction wherein at least one olefin selected from the group of cyclic and acyclic mono and polyene olefin hydrocarbons and mixtures of such hydrocarbons are converted in a reaction zone to products of the olefin metathesis reaction, which as defined herein, can be visualized as comprising the reaction between two first pairs of carbon atoms, the two carbon atoms of each first pair being connected by an olefinic double bond, to form two new pairs from the carbon atoms of the said first pairs, the two carbon atoms of each said new pairs being connected by an olefinic double bond, in the presence of an olefin metathesis catalyst comprising an oxide of tungsten on a silica support active for converting propylene into ethylene and butene, having an initial period of low activity under metathesis conditions including temperatures of from about 300°C to about 550°C and pressures of from about 0 to about 2000 psig and a reaction time in the range of from about 0.1 second to about 10 hours, the improvement comprising treating the catalyst with an olefin selected from the group comprising ethylene and butylenes at temperatures ranging from about 450°C to about 750°C for a period of time varying from about 0.1 minute to about 60 minutes prior to its use as an olefin metathesis catalyst. In a process of converting an olefin in an olefin metathesis reaction wherein at least one olefin selected from the group of cyclic and acyclic mono and polyene olefin hydrocarbons and mixtures of such hydrocarbons are converted in a reaction zone to products of the olefin metathesis reaction, which as defined herein, can be visualized as comprising the reaction between two first pairs of carbon atoms, the two carbon atoms of each first pair being connected by an olefinic double bond, to form two new pairs from the carbon atoms of the said first pairs, the two carbon atoms of each said new pairs being connected by an olefinic double bond, in the presence of an olefin metathesis catalyst comprising an oxide of tungsten on a silica support active for converting propylene into ethylene and butene, under metathesis conditions including temperatures of from about 300°C to about 550°C and pressures of from about 0 to about 2000 psig and a reaction time in the range of from about 0.1 second to about 10 hours, said process having a decreased activity, the improvement comprising regenerating the catalyst by treating the catalyst with an olefin selected from the group comprising ethylene and butylenes at temperatures ranging from about 450°C to about 750°C for a period of time varying from about 0.1 minute to about 60 minutes prior to its use again as an olefin metathesis catalyst.