Ammoxidation catalyst and preparation method and application thereof

A technology of ammoxidation reaction and catalyst, applied in the direction of preparation of hydrocarbon ammoxidation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc. Reducing the yield, increasing the cost of three wastes treatment and environmental protection, and increasing the cost of raw materials, etc., to achieve the effect of improving the reaction activity, reducing the activation energy of the reaction, and reducing the amount of use

Active Publication Date: 2020-05-12
WANHUA CHEM GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology describes how precise control over the proportion between different components within a chemical reactor helps achieve better performance without increasing its cost or requiring more expensive reactants like urea compared with traditional methods such as acidic nitrogen compounds. By adding specific types of metals into this mixture, it becomes possible for certain atoms called X(V) to participate in various processes involved in reducing NOx emissions from combustion engines. Overall, these techniques aimed towards efficient production of valuable products while minimizing waste generated due to excessive use of urethanamine hydrochloride precursors.

Problems solved by technology

This technical problem addressed in this patents relates to optimizing the reduction of ammino compounds during the preparing of certain types of organic substances called organoamino acids like paraformylenetide acidimony ester (PPTA) and pigment monofluorotranilmate diamond pyrochlorobenzolone(FMP). Current methods involve reactors with excessive amounts of water and require expensive starting materials. Therefore, new processes aim towards improved efficiency and reduced emissions from these sources would help lower down on pollution levels associated with these chemistry industries while increasing yields and quality output.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] 1) Heat 2500g of water to 85°C, and stir 1950g of oxalic acid (H 2 C 2 o 4 ) was added into water to form an aqueous oxalic acid solution; 455g vanadium pentoxide, 680g silver nitrate and 1360g arsenic trichloride were added to 680g water to form a reaction solution one;

[0052] Under stirring, the above-mentioned reaction solution 1 was added to the oxalic acid aqueous solution to form a mixed solution 1;

[0053] 2) 1074g manganese nitrate, 1073g zirconium nitrate pentahydrate and 8.7g rhodium nitrate were dissolved in 3918.3g water to form reaction solution two;

[0054] Add 2750 g of silica sol with a mass percentage of 40% and the above-mentioned reaction solution 2 to the mixed solution 1 to obtain the mixed solution 2;

[0055] 3) Stir the above mixed solution 2 at 90°C at a speed of 350rpm for 200min, then raise the temperature to 105°C and let stand for 60min for aging treatment, and evaporate the solution after aging treatment to a slurry with a solid content

Embodiment 2

[0062] 1) Heat 2550g of water to 75°C, and stir 2000g of oxalic acid (H 2 C 2 o 4 ) was added into water to form an aqueous oxalic acid solution; 455g of vanadium pentoxide, 765g of silver nitrate and 1269g of arsenic trichloride were added to 780g of water to form a reaction solution 1;

[0063] Under stirring, the above-mentioned reaction solution 1 was added to the oxalic acid aqueous solution to form a mixed solution 1;

[0064] 2) 1988g of lead nitrate, 293g of cesium nitrate and 12.4g of iridium trichloride hydrate were dissolved in 4594.6g of water to form reaction solution 2;

[0065] Add 2800 g of silica sol with a mass percentage of 40% and the above-mentioned reaction solution 2 to the mixed solution 1 to obtain the mixed solution 2;

[0066] 3) Stir the above mixed solution 2 at 85°C at a speed of 300rpm for 180min, then raise the temperature to 108°C and let stand for 75min for aging treatment, and evaporate the solution after aging treatment to a slurry with a so

Embodiment 3

[0073] 1) Heat 2600g of water to 80°C, and stir 2100g of oxalic acid (H 2 C 2 o 4 ) was added into water to form an aqueous oxalic acid solution; 455g of vanadium pentoxide, 510g of silver nitrate and 998g of arsenic trichloride were added to 800g of water to form a reaction solution 1;

[0074] Under stirring, the above-mentioned reaction solution 1 was added to the oxalic acid aqueous solution to form a mixed solution 1;

[0075] 2) 1190g zinc nitrate hexahydrate, 1519g cerium nitrate hexahydrate and 16.85g platinum chloride were dissolved in 3513.15g water to form reaction solution 2;

[0076] Add 3000 g of silica sol with a mass percentage of 40% and the above-mentioned reaction solution 2 to the mixed solution 1 to obtain the mixed solution 2;

[0077] 3) Stir the above mixed solution 2 at 90°C at a speed of 310rpm for 150min, then raise the temperature to 110°C and let stand for 180min for aging treatment, and evaporate the solution after aging treatment to a slurry with

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PUM

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Abstract

The invention provides an ammonia oxidation catalyst as well as a preparation method and application thereof. The ammoxidation catalyst comprises a carrier and an active component, wherein the activecomponent meets the following structure in terms of atomic ratio: V1.0AgaAsbDcEdGeOx, wherein the D is selected from one or more of Mn, Zn, Ca, Ba and Pb, the E is selected from one or more of Cs, Zr,La, Ce and Pr, and the G is selected from one or more of Rh, Ru, Ir, Pt and Au; a is equal to 0.01-3, b is equal to 0.01-3, c is equal to 0.01-2, d is equal to 0.001-1, e is equal to 0.001-0.6, b/(1+a) is more than 0.3 and less than 1.2, and (b+e)/(c+d) is more than 0.1 and less than 15; x is determined by the oxidation degree of other elements shown in the formula I. The catalyst is high in conversion rate and selectivity, good in stability and suitable for industrial production during low-ammonia/xylene-ratio feeding.

Description

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Claims

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Application Information

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Owner WANHUA CHEM GRP CO LTD
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