Catalyst for selective reduction of NOx with NH3 and preparation method thereof
A catalyst and reaction technology, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve problems such as high working temperature, ecological environment and human health hazards, pipeline corrosion, etc., achieve simple preparation process and improve catalytic performance , the effect of high catalytic activity
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0017] Embodiment 1: 0.716g La(NO 3 ) 3 ·6H 2 O and 0.405g Mn(CH 3 COO) 2 4H 2 O was dissolved in 20mL of water (equivalent to the concentration of each metal ion being 0.083mol / L), and after dissolving, 0.764g of citric acid was added (equivalent to a molar ratio of citric acid to total metal ions of 1.1), stirred for 3 hours and then added 1.6g TiO 2 , Stirring was continued for 3h, and then evaporated to a gel at 90°C. The gel was dried at 100°C for 24h, then at 180°C for 8h. The dried mixture was first calcined at 250°C for 3h and then at 650°C for 3h under the condition of air ventilation to obtain the supported LaBO 3 (B=Mn) perovskite catalyst, LaBO in catalyst by weight percentage 3 The content is 20%.
Embodiment 2-7
[0018] Examples 2-7: Catalysts were prepared according to the steps and conditions of Example 1. The changed preparation conditions included the type of B, the type of carrier, the calcination temperature and the content of perovskite, see Table 1.
[0019] Table 1 Loaded LaBO 3 Preparation of (B=Mn, Fe) perovskite catalyst
[0020]
Embodiment 8
[0022] Example 8: Using the above catalyst for NH of nitrogen oxides 3 Selective reduction reaction, the specific reaction conditions are as follows: reaction temperature 50-275 ℃, total gas flow rate 500mL / min, reaction gas composition of 500ppm NO, 500ppm NH 3 , 3% O 2 And balance gas nitrogen, gas hourly space velocity 2.7×10 4 -5.4×10 4 h -1 . The reactivity is shown in Table 2.
[0023] The reactivity of table 2 catalyst
[0024]
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 