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This invention relates to a method for producing a partially oxidized organic compound, e.g., an unsaturated aldehyde/carboxylic acid having three or more carbon atoms, or an organic acid anhydride/nitrile compound having four or more carbon atoms. This method requires a catalyst prepared by treatin

This invention relates to a method for producing a partially oxidized organic compound, e.g., an unsaturated aldehyde/carboxylic acid having three or more carbon atoms, or an organic acid anhydride/nitrile compound having four or more carbon atoms. This method requires a catalyst prepared by treating a carrier in such a manner that water used in the treatment achieves specific resistance.

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1. A method for the production of a partially oxidized organic compound, which comprises effecting gas phase partial oxidation of an organic substrate or an organic substrate-containing gas with molecular oxygen or a molecular oxygen-containing gas in the presence of a catalyst including an inert ca

1. A method for the production of a partially oxidized organic compound, which comprises effecting gas phase partial oxidation of an organic substrate or an organic substrate-containing gas with molecular oxygen or a molecular oxygen-containing gas in the presence of a catalyst including an inert carrier and a catalytically active component supported thereon, wherein the carrier is washed with water, with water and an aqueous acid solution, or with water and an aqueous ammonia solution, dried, exposed to additional water, and separated from the additional water, such that the additional water exhibitsspecific resistance of not less than 10,000 ohms.cm (25.degree. C.) when the catalyst is used for producing an unsaturated aldehyde or unsaturated carboxylic acid of not less than three carbon atoms, or specific resistance of not less than 20,000 ohms.cm (25.degree. C.) when the catalyst is used for producing an organic anhydride or nitrile compound of not less than four carbon atoms; wherein the specific resistance is measured according to the following treatment: in a conical beaker having an inner volume of 500 mL, 300 mL of the carrier is placed inside and dried at 120.degree. C. for two hours and then the dried carrier and an amount of purified water equal to the total of the "amount of water absorption" in mL plus 220 mL ("amount of water absorption"+220, mL) added thereto are heated together under normal pressure at 90.degree. C. for 30 minutes, wherein the "amount of water absorption" is A/B in which A=300 (mL).times.packing density (g/mL).times.water absorption ratio (% by weight)/100, and B=density of water (g/mL).