Nitrile-containing organic waste gas purification catalyst and preparation method thereof
A technology for purifying catalysts and organic waste gas, which is used in catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., to achieve the effects of simple preparation process, high catalyst activity, and long service life
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0010] Weigh alumina, silica, CeO 2 , ZrO 2 , with Bi 2 o 3 Calculated Bi(NO 3 ) 3 The solution is 133.3g of alumina, 13.33g of silicon dioxide, and CeO calculated at a mass ratio of 1:0.1:0.2:0.1:0.1 2 (26.66g), ZrO 2 (13.33g), Bi(NO 3 ) 3 solution (with Bi 2 o 3 13.33g) mixed and stirred evenly with 1400g water and stirred evenly, after the solution was ball milled for 2 hours, adjusted to pH=2.0-2.5 with nitric acid to prepare A solution; weigh CeO 2 , ZrO 2 , La 2 o 3 , Cu(NO 3 ) 2 , with MnO 2 Calculated Mn(NO 3 ) 2 CeO with a mass ratio of 1:0.1:0.1:2:0.3 2 (28.57g), ZrO 2 (2.86g), La 2 o 3 (2.86g), Cu(NO 3 ) 2 (57.14g containing CuO), Mn(NO 3 ) 2 (with MnO 2 After the solution prepared for 8.57g) was stirred evenly, it was mixed with 1500g water and stirred evenly, after the solution was ball milled for 2 hours, it was adjusted to pH=2.0~2.5 with nitric acid to prepare B solution; weigh Cu(NO 3 ) 2 Solution (83.33g containing CuO), Mn(NO 3 )...
Embodiment 2
[0014] With the same preparation method of Example 1, the difference is that the content of CuO in each liter of prepared catalyst is doubled, the content of noble metals Pt and Pd is doubled, the catalyst activity evaluation conditions are the same as in Example 1, and the catalyst activity evaluation results See Table 2.
[0015]
Embodiment 3
[0017] Using the same preparation method as in Example 1, the difference is that the CuO content per liter of the prepared catalyst is reduced by 50%, and the catalyst activity evaluation conditions are the same as in Example 1, and the catalyst activity evaluation results are shown in Table 3.
[0018]
[0019] It can be seen that the catalyst of the present invention has a high conversion rate for simulated organic waste gas, a high selectivity for converting CN bonds into N2, and a good catalytic effect. The catalytic performance of Example 2 is better than that of the other two examples. The present invention has simple process , The characteristics of the prepared catalyst are high activity.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


