Catalytic cracking regeneration flue gas combustion-supporting catalyst and preparation method
A technology for combustion-supporting catalysts and flue gas regeneration, applied in the direction of physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problem of uneven distribution of precious metal particles inside and outside the bulk catalyst It is easy to destroy the three-dimensional ordered macroporous oxide structure, and the noble metal particles are not easy to be evenly loaded, so as to achieve the effects of controllable particle size, narrow particle size distribution, and optimal flow rate
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Embodiment 13D
[0051] Example 13 DOM Au x / LaFeO 3 catalyst
[0052] 6.5ml of HAuCl with a concentration of 121.2mmol / L 4 Aqueous solution mixes (solid content is 10wt%) with 250mlPMMA microsphere emulsion, stirs 4h, because microsphere surface electropositive group [=NH 2 ] + attracts such that [AuCl 4 ] - Uniform adsorption on the surface of microspheres. The solution of precursor salt and microspheres containing Au enters the membrane reactor under the action of the peristaltic pump, and the hydrogen input device is started at the same time. The hydrogen diffuses out of the membrane tube through the 40nm micropores on the two ceramic membrane tubes, generating a large amount of Hydrogen bubbles promote the mixing of the carrier and the solution, and the hydrogen flow rate is 50mL / min.
[0053] NaBH 4 According to the predetermined stoichiometric ratio (NaBH 4 with AuCl 4 - The molar ratio is 3:1) to prepare a solution, and use the advection pump to diffuse the reducing agent so...
Embodiment 2
[0063] Example 2 3DOM Pt x / C 0.7 Zr 0.3 o 2 catalyst
[0064] Concentration is 6.5ml concentration is the H of 121.2mmol / L 2 PtCl 6 Aqueous solution mixes (solid content is 10wt%) with 250mlPMMA microsphere emulsion, stirs 4h, because microsphere surface electropositive group [=NH 2 ] + attracts such that [PtCl 6 ] 2- Uniform adsorption on the surface of microspheres. The solution of Pt-containing precursor salt and microspheres enters the membrane reactor under the action of the peristaltic pump, and at the same time starts the hydrogen input device. The hydrogen diffuses out of the membrane tube through the 40nm micropores on the two ceramic membrane tubes, generating a large amount of Hydrogen bubbles promote the mixing of the carrier and the solution, and the hydrogen flow rate is 50mL / min.
[0065] NaBH 4 According to the predetermined stoichiometric ratio (NaBH 4 with [PtCl 6 ] 2- The molar ratio is 3:1) to prepare a solution, and use the advection pump to...
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