Catalyst for removing nitric oxide and preparation method thereof

Inactive Publication Date: 2019-05-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Benefits of technology

Problems solved by technology

Technological Problem addressed in this patented technical paper describes how to efficiently treat exhaust gasses emitted due to combustion processes like engines and industries. Current methods involve expensive equipment and consume significant amounts of fossil fuels, leading to increased greenhouse gas production and potential negative impacts upon our environment. Selective catalysis techniques have been developed but their effectiveness depends heavily on factors like temperatures and pressures. Additionally, current technologies require extensive capital expenditure and maintenance costs associated therewith.

Method used

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  • Catalyst for removing nitric oxide and preparation method thereof
  • Catalyst for removing nitric oxide and preparation method thereof
  • Catalyst for removing nitric oxide and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] 50 g of silica sol (40% SiO 2) mixed with aluminum nitrate aqueous solution containing 75 grams of aluminum oxide, fully stirred, placed in a three-necked bottle, and added dropwise with silver nitrate solution containing 5 grams of silver oxide, while vigorously electromagnetically stirring, maintaining the temperature of the oil bath at 70 ° C, loading The sol was solidified after stirring for three hours, and the stirring was stopped, and the temperature was raised to 100°C, and the solvent was evaporated for 12 hours. Transfer to a crucible, bake with an infrared lamp for 24 hours, then transfer to a muffle furnace at 700 ° C for 6 hours, and crush to 40-60 meshes to obtain the desired Ag-containing powder. 2 O 5% Ag / SiO 2 -Al 2 o 3 catalyst.

Embodiment 2

[0042] 50 g of silica sol (40% SiO 2 ) mixed with aluminum nitrate aqueous solution containing 75 grams of aluminum oxide, fully stirred, placed in a three-necked bottle, and added dropwise with silver nitrate solution containing 3 grams of silver oxide, while vigorously electromagnetically stirring, maintaining the temperature of the oil bath at 70 ° C, loading The sol was solidified after stirring for three hours, and the stirring was stopped, and the temperature was raised to 100°C, and the solvent was evaporated for 12 hours. Transfer to a crucible, bake with an infrared lamp for 24 hours, then transfer to a muffle furnace for 6 hours at 700°C, grind to 40-60 meshes, impregnate in an equal volume of titanium nitrate solution containing 2 grams of titanium oxide for 12 hours, and dry at 120°C Calcined in a muffle furnace at 450°C to obtain the desired 2% TiO 2 Modified, containing Ag 2 O 3% Ag / SiO 2 -Al 2 o 3 catalyst.

Embodiment 3

[0044] 125 g of silica sol (40% SiO 2 ) mixed with an aqueous solution of aluminum sulfate containing 47.8 grams of aluminum oxide, fully stirred, placed in a three-necked bottle, and added dropwise with a silver nitrate solution containing 0.2 grams of silver oxide, while vigorously stirring electromagnetically to maintain the temperature of the oil bath at 70 ° C. Return to the condensing tube, stir for three hours and then the sol solidifies, stop stirring, raise the temperature to 150°C, and evaporate the solvent for 12 hours. Transfer to a crucible, bake with an infrared lamp for 24 hours, then transfer to a muffle furnace and bake at 500°C for 8 hours, crush to 40-60 meshes, then impregnate with equal volume of zirconium nitrate solution containing 2 grams of zirconia for 12 hours, and dry at 80°C Roasted in a muffle furnace at 600°C to obtain the required 2% ZrO 2 Modified, containing Ag 2 O 0.2% Ag / SiO 2 -Al 2 o 3 catalyst.

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Abstract

The invention relates to a catalyst for removing nitric oxide, the catalyst is mainly used for solving the problems that in the prior art, the activity of the catalyst is low or the selectivity is poor under a high-temperature condition, and the nitrogen oxide cannot be effectively removed. A SOL-GEL method is adopted, a certain amount of silica SOL is mixed with an aqueous solution or alcohol solution containing a soluble aluminum salt to obtain a mixture, the mixture is dropwise added into an inorganic silver salt aqueous solution, after aging, drying, roasting and the like, a silver catalyst loaded with silicon oxide and aluminum oxide is prepared, metal oxides of IVB and VB are adopted for modification, and the problems are well solved. The catalyst is used in the reaction for removingnitrogen oxide waste gas, can be used to reduce nitrogen oxides effectively, has high catalytic activity and long service life, is simple and convenient to prepare and relatively low in price, and issuitable for industrial application.

Description

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Claims

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Application Information

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Owner CHINA PETROLEUM & CHEM CORP
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