Metathesis process using a moving phase reactor
A method for metathesizing at least two gaseous olefins using a moving catalyst bed gas phase metathesis reactor and counter current flowing subdivided solid catalyst.
1 . In a method for metathesizing at least two gaseous olefin reactants wherein said olefin reactants are contacted with a metathesis promoting catalyst under operating conditions that favor the transformation of said olefin reactants to at least one other olefin as the product of the process, the improvement comprising carrying out said metathesis using subdivided solid metathesis catalyst in a moving catalyst bed gas phase reactor that has opposing ends, said at least two gaseous olefin reactants being introduced into said reactor near one of said opposing reactor ends, said solid metathesis catalyst being introduced into said reactor near the other of said opposing reactor ends, and passing said olefin reactants into counter current contact with said metathesis catalyst in said reactor under metathesis promoting conditions of operation.
2 . The method of claim 1 wherein said olefins are selected from the group consisting of C2 to C8 olefins having at least one of alpha or internal double bonds.
3 . The method of claim 1 wherein said subdivided solid metathesis catalyst has a particle size of from about 0.1 inch up to right cylindrical pellets of up to about one inch in length and up to one half inch in diameter.
4 . The method of claim 1 wherein said catalyst is at least one of halides, oxides, and carbonyls of at least one of molybdenum, tungsten, rhenium, and magnesium carried on a solid support.
5 . The method of claim 4 wherein said catalyst contains at least one activating agent.
6 . The method of claim 1 wherein said operating conditions are a temperature of from about 300 to about 800 F, and a pressure of from about 200 to about 600 psig.
7 . The method of claim 1 wherein said olefin reactants are at least ethylene and 2-butene, said catalyst is magnesium oxide and tungsten oxide supported on silica, and said at least one other olefin product is propylene.
8 . The method of claim 1 wherein said solid metathesis catalyst is passed downwardly in said reactor and said gaseous olefin reactants are passed upwardly in said reactor, whereby said catalyst and said reactants contact one another and mix with one another in counter current fashion.