Catalyst for removing low-concentration formaldehyde in gases and application thereof
A technology for removing gases and catalysts, applied in molecular sieve catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve problems such as failure, and achieve the effect of low energy consumption
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Embodiment 1
[0011] Example 1: HZSM-5 (referred to as HZ, the same below) powder was calcined at 600°C for 3 hours, and then tableted, crushed and sieved to obtain a particle size of 20-40 mesh.
[0012] A reactor capable of dielectric barrier discharge: a stainless steel high-voltage electrode with a diameter of 3mm is located at the axis of a quartz glass tube with an inner diameter of 8mm and a wall thickness of 1mm, and a stainless steel mesh with a height of 3mm is tightly wound on the outer wall of the quartz glass tube as a grounding electrode. Fill the discharge area between the quartz tube and the stainless steel high voltage electrode with 1.5ml of 20-40 mesh HZ particles. Under normal temperature and pressure, simulated air with a formaldehyde concentration of 24.4ppm and a water content of 50% relative humidity at 25°C passes through the HZ catalyst bed at a flow rate of 300ml / min, and formaldehyde is stored on the HZ catalyst. After 40 minutes, formaldehyde molecules began to ...
Embodiment 2
[0013] Example 2: After calcining the HZ powder at 600° C. for 3 hours, pour it into the mixed solution of silver nitrate and copper nitrate. After the HZ molecular sieve carrier was immersed in the solution for 12 hours, it was dried at 120° C. and calcined at 600° C. for 3 hours. Then press into tablets, crush and sieve to obtain 20-40 mesh AgCu / HZ catalyst particles. The weight percentages of Ag and Cu loadings in the catalyst were 3.6% and 2.1%, respectively.
[0014] 1.5 ml of 20-40 mesh AgCu / HZ catalyst particles were packed in the discharge area of the dielectric barrier discharge reactor described in Example 1. Under normal temperature and pressure, simulated air with a formaldehyde concentration of 26.2ppm and a water content of 50% relative humidity at 25°C passes through the AgCu / HZ catalyst bed at a flow rate of 300ml / min, and formaldehyde is stored on the AgCu / HZ catalyst. After 165 minutes, formaldehyde molecules began to penetrate the AgCu / HZ catalyst bed an...
Embodiment 3
[0015] Example 3: 1.5 ml of the AgCu / HZ catalyst prepared in Example 2 was loaded into the discharge area of the dielectric barrier discharge reactor described in Example 1. Under normal temperature and pressure, simulated air with a formaldehyde concentration of 26.6ppm and a water content of 93% relative humidity at 25°C passes through the AgCu / HZ catalyst bed at a flow rate of 300ml / min, and formaldehyde is stored on the AgCu / HZ catalyst. After 168 min, formaldehyde molecules began to penetrate the AgCu / HZ catalyst bed and the storage reached saturation. The formaldehyde breakthrough storage capacity under this condition was 1.8 mg. Then turn over to the regeneration stage: the flow of oxygen that is 60ml / min flows through the AgCu / HZ catalyzer that stores formaldehyde, and the AC high voltage that applies frequency is 2kHz to make this reactor take place dielectric barrier discharge (discharge power is 2.3W), to AgCu / HZ catalyst for regeneration. Formaldehyde stored on...
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