Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
188 words
A method for producing a catalyst usable for the preparation of maleic anhydride by catalytic oxidation of unsaturated hydrocarbon having 4 to 6 carbon atoms, comprising mixing a titanium oxide and a vanadium compound, in an atomic ratio of Ti to V of from 1 to 15, said vanadium compound being selected from the group consisting of vanadium oxides, vanadium halides, metavanadic acid, ammonium vanadate and vanadium oxychlorides, calcining said mixture at a temperature of from 630° to 1000° C. to form a precursory catalyst, and bringing a gas mixture containing an organic phosphorus compound selected from the group consisting of phosphines, trialkyl phosphates and trialkyl phosphites, and a carrier gas into contact with a mass of said precursory catalyst at a temperature of from 350° to 600° C. and at a supply rate of said phosphorus compound of from 0.01 to 10 millimoles/hr. per 1 ml. of the mass of said precursory catalyst during when a total amount of from 0.3 to 30 millimoles, of said organic phosphorus compound per 1 ml. of the mass of said precursory catalyst passes through the mass of said precursory catalyst.
Claim 2
Independent Claim
188 words
A method for producing a catalyst usable for the preparation of maleic anhydride by catalytic oxidation of unsaturated hydrocarbon having 4 to 6 carbon atoms, comprising mixing a titanium oxide and a vanadium compound, in an atomic ratio of Ti to V of from 1 to 15, said vanadium compound being selected from the group consisting of vanadium oxides, vanadium halides, metavanadic acid, ammonium vanadate and vanadium oxychlorides, calcining said mixture at a temperature of from 630° to 1000° C. to form a precursory catalyst, and bringing a gas mixture containing an organic phosphorus compound selected from the group consisting of phosphines, trialkyl phosphates and trialkyl phosphites, and a carrier gas into contact with a mass of said precursory catalyst at a temperature of from 350° to 600° C. and at a supply rate of said phosphorus compound of from 0.01 to 10 millimoles/hr. per 1 ml. of the mass of said precursory catalyst during when a total amount of from 0.3 to 30 millimoles, of said organic phosphorus compound per 1 ml. of the mass of said precursory catalyst passes through the mass of said precursory catalyst.
Claim 3
Dependent Claim
27 words
A method as claimed in claim 1, wherein said precursory catalyst is granulated into granules each having a volume of from 0.01 to 2 cm 3 .
Claim 4
Dependent Claim
23 words
A method as claimed in claim 1, wherein said titanium oxide is either a rutile type or an anatase type of titanium dioxides.
Claim 5
Dependent Claim
27 words
A method as claimed in claim 1, wherein said carrier gas is selected from air, steam, nitrogen and mixtures of two or more of the above-mentioned gases.
Claim 6
Dependent Claim
29 words
A method as claimed in claim 1, wherein said organic phosphorus compound is contained in an amount of from 0.01 to 1% by gas volume in said gas mixture.
Claim 7
Dependent Claim
20 words
A method as claimed in claim 1, wherein said vanadium compound is either a vanadium oxide or an ammonium metavanadate.
Claim 8
Dependent Claim
24 words
A method as claimed in claim 1, wherein each of the alkyl groups in said organic phosphorus compound has 1 to 5 carbon atoms.