A method for treating self-sustained combustion of VOCs by catalytic ignition at room temperature
A technology of catalytic ignition and treatment method, applied in the direction of combustion method, combustion type, incinerator, etc., can solve the problems of lack of economic benefit, small total amount, dispersion, etc., to achieve the effect of simple process and environmental protection
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preparation example 1
[0033] This preparation example is used to illustrate the doped noble metal composite oxide catalyst used in the present invention.
[0034] (a) 100g of pseudo-boehmite powder (purchased from Zibo Taiguang Chemical Co., Ltd. GL-1 brand), 20g of cerium zirconium solid solution (CZ), 4.5g of manganese carbonate, 4g of nickel carbonate and 400g of water were placed in a ball mill (Nanjing Laibu Technology Industrial Co., Ltd. (QM model) was ball milled at 50rpm for 2h to obtain a suspended slurry, and then the slurry was coated on 1000g of honeycomb cordierite ceramics (purchased from Jiangxi Xingfeng Chemical Packing) by dipping. Company square hole type carrier), and dried at 120 ° C for 24 h, and then calcined at 500 ° C for 6 h to obtain γ-Al 2 O 3 Coated honeycomb cordierite support.
[0035] (b) immersing the carrier obtained in step (a) in an aqueous solution of 1 wt % palladium chloride for 12 hours, then drying at 120° C. for 4 hours, and then calcining at 500° C. for ...
Embodiment 1
[0037] This example is used to illustrate a method for treating VOCs waste gas containing a certain amount of low unsaturated hydrocarbons by catalytic ignition at room temperature of the present invention.
[0038] The doped noble metal composite oxide catalyst shown in the preparation example was charged into the reactor, and the catalyst loading amount was 0.02 L, accounting for 80% by volume of the fixed bed reactor. When the temperature of the catalyst bed in the reactor equipped with the doped noble metal composite oxide catalyst was 33 °C, the volume flow rate of VOCs waste gas of 12 L / h (the composition is shown in Table 1) and 1.5 L / h of hydrogen Pass into the reactor together, and then pass in 20L / h of air to make the VOCs waste gas catalytically ignite, and the temperature of the catalyst bed is rapidly raised to 450 °C; enter the catalytic self-sustained combustion stage, and then stop the flow of hydrogen and reduce the volume of VOCs waste gas. The flow rate was ...
Embodiment 2
[0053] This example is used to illustrate a method for treating VOCs waste gas containing a certain amount of low unsaturated hydrocarbons and hydrogen by catalytic ignition at room temperature of the present invention.
[0054] The doped noble metal composite oxide catalyst shown in the preparation example was charged into the reactor, and the catalyst loading amount was 0.02 L, accounting for 80% by volume of the fixed bed reactor. When the temperature of the catalyst bed in the reactor equipped with the doped noble metal composite oxide catalyst is 33 °C, the VOCs waste gas (the composition is shown in Table 4) with a volume flow of 12 L / h is passed into the reactor, and then Introduce 20L / h of air to make the VOCs waste gas catalytically ignite, and the temperature of the catalyst bed is rapidly raised to 450°C; enter the catalytic self-sustained combustion stage, and then adjust the volume flow of VOCs waste gas to 6L / h, and feed 75L / h With the volume flow of air, the tem...
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