Method for producing acrylic acid with a fixed-bed multitubular reactor
US-9174910-B2 · Nov 3, 2015 · US
US9527792B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9527792-B2 |
| Application number | US-201515034109-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 27, 2015 |
| Priority date | Apr 30, 2014 |
| Publication date | Dec 27, 2016 |
| Grant date | Dec 27, 2016 |
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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.
Opening claim text (preview).
The invention claimed is: 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.
Washing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
with chromium, molybdenum, tungsten or polonium · CPC title
including substantial dissolution or chemical precipitation of a catalyst component in the ultimate reconstitution of the catalyst · CPC title
via the gaseous phase-sublimation · CPC title
Precipitation; Co-precipitation · CPC title
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