Process for the manufacture of maleic anhydride
AssigneeMaruzen Petrochemical Co., Ltd.
InventorIkuya Matsuura
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AssigneeMaruzen Petrochemical Co., Ltd.
InventorIkuya Matsuura
Estimating the term…
The present invention provides a process for the manufacture of maleic anhydride by the vapor phase catalytic oxidation of n-butane with molecular oxygen by the use of a specially prepared phosphorus vanadium-oxygen composite catalyst containing specific kind of a divalent metal. The catalyst used in the present invention is prepared from a mixture of vanadyl hydrogen orthophosphate and at least one compound selected from the group consisting of a divalent metal hydrogen orthophosphate (Divalent metal is selected from Mg, Ca, Ba, Mn, Fe, Co, Ni, Cu, and Zn.), a divalent metal ammonium orthophosphate (Divalent metal is the same as above.), and a divalent metal orthophosphate (Divalent metal is the same as above.), with the atomic ratio of the divalent metal/vanadium of 0.003-0.5, by calcining the mixture at 300.degree.-400.degree. C., and then pretreating said catalyst in an inert gas or a mixed gas containing n butane and molecular oxygen at 350.degree.-700.degree. C. Maleic anhydride can be manufactured at a high conversion, a high selectivity and a high yield according to the present invention.
In a process for manufacturing maleic anhydride by the vapor phase catalytic oxidation of n-butane with molecular oxygen, an improvement which comprises using a catalyst prepared by mixing vanadyl hydrogen orthophosphate represented by the formula VOHPO.sub.4 .multidot.0.5H.sub.2 O (I), and at least one compound selected from the group consisting of a divalent metal hydrogen orthophosphate represented by the formula MHPO.sub.4 .multidot.nH.sub.2 O (II) wherein M is a divalent metal selected from the group consisting of Mg, Ca, Ba, Mn, Fe, Co, Ni, Cu and Zn and n is a number of coordinated water which differs depending on the temperature at which the compound is prepared, a divalent metal ammonium orthophosphate represented by the formula NH.sub.4 MPO.sub.4 .multidot.nH.sub.2 O (III) wherein M and n have the same meanings as defined above and a divalent metal orthophosphate represented by the formula M.sub.3 (PO.sub.4).sub.2 .multidot.nH.sub.2 O (IV) wherein M and n have the same meanings as defined above, with the atomic ratio of M/V (M has the same meaning as defined above) of 0.003-0.5, by calcining the mixture at 300.degree.-400.degree. C., and then pretreating said catalyst in an inert gas or a mixed gas containing n butane and molecular oxygen at 350.degree.-700.degree. C.
Dependencies are inferred from the claim text.