Integral catalyst for producing hydrogen dioxide solution as well as preparation and application thereof
An integrated catalyst, hydrogen peroxide technology, applied in catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve the problem of prolonging the diffusion path, low catalyst utilization, and reducing contact opportunities. and other problems, to achieve the effect of overcoming loss, filling and replacing catalysts conveniently and quickly, and reducing internal mass transfer resistance.
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Embodiment 1
[0026] Coating slurry preparation
[0027] Weigh 4.3gAl 2 o 3 ·3H 2 O, 5.5gAl(OH) 3 , 6.4g γ-Al 2 o 3 , 3.0gAl(NO 3 ) 3 And 60ml mass concentration is 10% HNO 3 solution, a slurry suspension was obtained after ball milling for 18 hours.
[0028] Catalyst preparation
[0029] Dilute the 400cpsi cordierite honeycomb matrix with a volume concentration of 3% HNO 3 Treatment, after washing with deionized water, drying at 120°C for 2 hours, after treatment at 1000°C for 2 hours, excessively impregnating the above-mentioned slurry suspension with a mass concentration of 20%, drying in microwave for 10min, and roasting at 850°C for 2 hours, after multiple dipping and roasting The coating loading was 38 wt% of the honeycomb substrate. Subsequent immersion in a PdCl3 solution with a concentration of 20mg / ml, microwave drying for 5min, and calcination at 500°C for 2 hours to obtain 0.6wt% Pd / Al 2 o 3 / Monolith catalyst A, impregnated layer thickness 35 μm.
[0030] Catalyst...
Embodiment 2
[0033] coating preparation
[0034] Weigh 12.0g of metatitanic acid, add 15ml of 10% HCl and 10% of HNO 3 5ml, ball milled for 18 hours to obtain a slurry suspension for use.
[0035] Catalyst preparation process is identical with embodiment 1, obtains 0.6wt%Pd / TiO 2 / Monolith Catalyst B, impregnated layer 30 μm. Evaluation conditions are the same as in Example 1. The results are shown in Table 1.
Embodiment 3
[0037] The catalyst preparation process is as described in Example 1. The calcination temperature in the muffle furnace is adjusted to 650 ° C. The active component is impregnated several times, and each time it is dried and calcined to obtain 1.3wt% Pd / Al 2 o 3 / Monolith Catalyst C with an impregnated layer thickness of 60 μm. Evaluation conditions are the same as in Example 1. The results are shown in Table 1.
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