Method for producing (meth)acrylic acid
View Patent ↗The present invention provides a (meth)acrylic acid-producing method capable of suppressing formation of carbides so that the production yield of (meth)acrylic acid is enhanced. In such a method, (meth)acrylic acid is produced through gas-phase catalytic oxidation reactions of (meth)acrolein by using molecular oxygen in a fixed-bed reactor configured to have a packed layer containing a packing material and a catalyst layer formed with a catalyst containing at least molybdenum and vanadium. The packed layer contains a packing material that has been used at least once for above gas-phase catalytic oxidation reactions, and the catalyst is present in the packed layer at 0.001˜0.15 mass % of the total amount of the packing material.
1. A method for producing (meth)acrylic acid, the method comprising:
conducting gas-phase catalytic oxidation reactions of (meth)acrolein by using molecular oxygen in a fixed-bed reactor configured to have a packed layer containing a packing material and a catalyst layer formed with a catalyst containing at least molybdenum and vanadium,
wherein the packed layer contains a packing material that has been used at least once for the gas-phase catalytic oxidation reactions, and
the catalyst is present in the packed layer at 0.001—0.15 mass % of a total amount of the packing material.
2. The method according to claim 1 , wherein the catalyst is present in the packed layer at 0.001—0.1 mass % of the total amount of the packing material.
3. The method according to claim 1 , wherein the catalyst is present in the packed layer at 0.001—0.05 mass % of the total amount of the packing material.
4. A method for producing (meth)acrylic acid, the method comprising:
conducting gas-phase catalytic oxidation reactions of (meth)acrolein by using molecular oxygen in a fixed-bed reactor configured to have a packed layer containing a packing material and a catalyst layer formed with a catalyst containing at least molybdenum and vanadium,
wherein the packed layer contains a packing material that has been used at least once for above gas-phase catalytic oxidation reactions, and
the catalyst is attached to the packing material in the packed layer at 0.001—0.15 mass % of a total amount of the packing material in the packed layer.
5. The method according to claim 4 , wherein the catalyst is attached to the packing material in the packed layer at 0.001—0.1 mass % of the total amount of the packing material.
6. The method according to claim 4 , wherein the catalyst is attached to the packing material in the packed layer at 0.001—0.05 mass % of the total amount of the packing material.
7. The method according to claim 1 , wherein the used packing material is what is obtained by cleaning the packing material used at least once for the gas-phase catalytic oxidation reactions.
8. The method according to claim 7 , wherein the used packing material is what is obtained after the packing material used at least once for the gas-phase catalytic oxidation reactions is soaked in ammonia water and is then cleaned in deionized water.
9. The method according to claim 1 , wherein the packing material is a mixture of the used packing material and an unused packing material.
10. The method according to claim 1 , wherein the packing material is at least one type selected from the group consisting of a silica-alumina material and an SUS material.
11. The method according to claim 1 , wherein the packing material is shaped in at least one type selected from the group consisting of a spherical material and a coil material.
12. The method according to claim 1 , wherein the packing material is at least one type selected from the group consisting of ceramic balls and SUS coil springs.