초록 ▼

The present invention provides a complex oxide catalyst whose general formula is Mo12VaCubWcXdYeOf/Z. reducing agent needs to be added into the catalyst during the preparation process of the active component of the catalyst and (or) molding process of the catalyst. Specifically, X is at least one se

The present invention provides a complex oxide catalyst whose general formula is Mo12VaCubWcXdYeOf/Z. reducing agent needs to be added into the catalyst during the preparation process of the active component of the catalyst and (or) molding process of the catalyst. Specifically, X is at least one selected from a group consisting of Nb, Sb, Sr, Ba and Te; Y is at least one selected from a group consisting of La, Ce, Nd, Sm and Cs; “a” is ranging from 2 to 8; “b” is ranging from 1 to 6; “c” is ranging from 0.5 to 5; “d” is ranging from 0.01 to 4; “e” is ranging from 0.01 to 4; f is determined by the oxidation state of the component element; Z is silicon powder; the reducing agent is C2˜C6 diol or polyol.

대표청구항 ▼

1. A complex oxide catalyst used for acrolein to prepare acrylic acid, having a general formula Mo12VaCubWcXdYeOf/Z, wherein X is at least one selected from a group consisting of Nb, Sb, Sr, Ba and Te; Y is at least one selected from a group consisting of La, Ce, Nd, Sm and Cs; “a” is ranging from 2

1. A complex oxide catalyst used for acrolein to prepare acrylic acid, having a general formula Mo12VaCubWcXdYeOf/Z, wherein X is at least one selected from a group consisting of Nb, Sb, Sr, Ba and Te; Y is at least one selected from a group consisting of La, Ce, Nd, Sm and Cs; “a” is ranging from 2 to 8; “b” is ranging from 1 to 6; “c” is ranging from 0.5 to 5; “d” is ranging from 0.01 to 4; “e” is ranging from 0.01 to 4; f is determined by an oxidation state of the component element; Z is silicon powder, wherein a reducing agent is added during a preparation or a molding process of the catalyst, and the reducing agent is C2˜C6 diol or polyol, wherein a weight of the Z component is 20% to 80% of a weight of the catalyst in a form of powder. 2. The complex oxide catalyst, as recited in claim 1, wherein Mo is selected from a group consisting of molybdic acid, secondary ammonium molybdate and molybdenum oxide; V is selected from a group consisting of ammonium metavanadate, vanadium oxide and vanadium oxalate; W is selected from a group consisting of tungstic acid, ammonium paratungstate and ammonium metatungstate, Cu is selected from a group consisting of copper nitrate, copper acetate and copper oxalate; X and Y are selected from a group consisting of corresponding oxides, or salt or hydroxide that can be decomposed to the oxides. 3. A preparation process of a catalyst according to claim 1, comprising steps of: adding Mo, V and W sources into water of 70 to 100° C. to obtain A solution;adding Cu, X and Y sources into water of 60 to 80° C. to obtain B solution;mixing B solution with A solution to obtain C solution at 40 to 80° C.;mixing Z component with the C solution to obtain D solution and drying D solution to obtain catalyst powder, or drying C solution to obtain powder and mixing the powder with Z component to obtain catalyst powder, in such a manner that a weight of the Z component is 20% to 80% of a weight of the catalyst. 4. The preparation process of a catalyst, as recited in claim 3, further comprising a step of adding reducing agent during preparation of A solution, B solution, C solution, D solution or during mixing process of the powder and Z component. 5. The preparation process of a catalyst, as recited in claim 4, wherein a weight of the reducing agent is 3% to 50% of a weight of the catalyst. 6. The preparation process of a catalyst, as recited in claim 3, wherein the drying process is implemented in a static drying condition under 90 to 200° C. or in a spray drying condition with entrance temperature 280 to 350° C. and exit temperature 130 to 160° C. 7. The preparation process of a catalyst, as recited in claim 3, further comprising a step of molding the catalyst powder by adding water and adhesive agent, wherein a weight of the adhesive agent is 0.5 to 10% of a weight of the catalyst, and the molded catalyst is granules of spherical shape, or solid or hollow column shape. 8. The preparation process of a catalyst, as recited in claim 7, wherein catalyst is roasted under a temperature ranging from 320° C. to 480° C. for 1 to 30 hours in a gas consisting of oxygen, inert gas, and reducing gas to become final product. 9. The preparation process of a catalyst, as recited in claim 3, specifically comprising: adding 150 g ammonium molybdate, 34.2 g ammonium paratungstate, and 40.5 g ammonium metavanadate into 700 g and 80° C. water to obtain A solution; adding 5 g barium nitrate, 2.3 g lanthanum nitrate, and 35.7 g copper nitrate into 80 g and 60° C. water to obtain B solution, mixing the A solution and the B solution at 60° C. to obtain C solution, and drying the C solution at 120° C. for 20 h to obtain a dry powder, mixing evenly 100 g the dry powder, 85 g silicon powder, 37 g propanediol and 18.5 g silicasol (30%), and squeezing the mixture into column-shape granules of 2 mm length and 1 mm diameter, and roasting the granules at 390° C. for 6 h in the air for being used as catalyst in the oxidation reaction of acrolein,wherein the oxidation reaction reacts in a reactor having a 20 mm inner diameter, which has a tube inside thereof having a 3 mm outer diameter, 15 ml catalyst is filled into the reactor, raw gases are 7% acrolein, 9% oxygen, 15% vapor, 1.4% unreacted propylene and other organic compounds, and nitrogen taking up the rest volume, an airspeed is 1500 h−1; a reaction temperature is 242° C.; and a hot spot temperature is 275° C. 10. The preparation process of a catalyst, as recited in claim 3, specifically comprising: adding 50 g butanediol, 130.2 g ammonium molybdate, 28.4 g ammonium metatungstate, and 38.1 g ammonium metavanadate into 600 g and 90° C. water to obtain A solution; adding 2.6 g cerium nitrate and 38.1 g copper nitrate into 80 g and 60° C. water to obtain B solution, mixing the A solution and the B solution at 60° C. to obtain C solution, mixing 320 g silicon powder with the C solution, and drying the mixture at 150° C. for 10 h to obtain a dry powder, mixing evenly 100 g the dry powder, 1.5 g graphite and 6.5 g silicasol (30%), and squeezing the mixture into column-shape granules of 2 mm length and 1 mm diameter, and roasting the granules at 390° C. for 6 h in the air for being used as catalyst in the oxidation reaction of acrolein,wherein the oxidation reaction reacts in a reactor having a 20 mm inner diameter, which has a tube inside thereof having a 3 mm outer diameter, 15 ml catalyst is filled into the reactor, raw gases are 7% acrolein, 9% oxygen, 15% vapor, 1.4% unreacted propylene and other organic compounds, and nitrogen taking up the rest volume, an airspeed is 1500 h−1; a reaction temperature is 265° C., and a hot spot temperature is 290° C. 11. The preparation process of a catalyst, as recited in claim 3, specifically comprising: adding 30 g neopentyl glycol, 130.2 g ammonium molybdate, 28.4 g ammonium metatungstate, and 38.1 g ammonium metavanadate into 600 g and 90° C. water to obtain A solution; adding 1.8 g lanthanum nitrate, 2.3 g strontium nitrate and 38.1 g copper nitrate into 80 g and 80° C. water to obtain B solution, mixing the A solution and the B solution at 60° C. to obtain C solution, and drying the C solution at 120° C. for 20 h to obtain a dry powder, mixing evenly 100 g the dry powder, 60 g silicon powder, 10 g silicon oxide, 3.4 g graphite and 11 g silicasol (30%), and squeezing the mixture into column-shape granules of 2 mm length and 1 mm diameter, roasting the granules at 390° C. for 6 h in the air for being used as catalyst in the oxidation reaction of acrolein,wherein the oxidation reaction reacts in a reactor having a 20 mm inner diameter, which has a tube inside thereof having a 3 mm outer diameter, 15 ml catalyst is filled into the reactor, raw gases are 7% acrolein, 9% oxygen, 15% vapor, 1.4% unreacted propylene and other organic compounds, and nitrogen taking up the rest volume, an airspeed is 1500 h−1; a reaction temperature is 245° C., a hot spot temperature is 280° C.