Treatment method for normal-temperature catalytic ignition of VOCs for self sustaining combustion
A technology of catalytic ignition and treatment methods, applied in the direction of combustion methods, combustion types, incinerators, etc., can solve the problems of small total amount, lack of economic benefits, dispersion, etc., and achieve the effect of protecting the environment and simple process
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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 in a ball mill (Nanjing Laibu Technology Industrial Co., Ltd. QM model) with 50rpm rotating speed ball milling 2h, obtain the slurry of suspension, then add this slurry and adopt the mode of impregnating to be coated on 1000g honeycomb type cordierite ceramics (purchased from Jiangxi Xingfeng chemical filler company’s square-hole carrier), and dried at 120°C for 24h, and then calcined at 500°C for 6h to obtain γ-Al 2 o 3 Coated honeycomb cordierite support.
[0035] (b) Immerse the carrier obtained in step (a) in an aqueous solution of 1% by weight of palladium chloride for 12h, then dry at 120°C for 4h, and then calcinate at 50...
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 loaded into the reactor, and the catalyst loading was 0.02L, 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 VOCs waste gas (composition shown in Table 1) and the hydrogen gas of 1.5L / h were mixed with a volume flow rate of 12L / h They are passed into the reactor together, and then 20L / h of air is passed in to make the VOCs exhaust gas catalytically ignite, and the temperature of the catalyst bed rises rapidly to 450°C; it enters the catalytic self-sustained combustion stage, and then stops the introduction of hydrogen and reduces the volume of the ...
Embodiment 2
[0053] This embodiment is used to illustrate a kind of room temperature catalytic ignition of the present invention contains the VOCs waste gas treatment method of a certain amount of low unsaturated hydrocarbons and hydrogen.
[0054] The doped noble metal composite oxide catalyst shown in the preparation example was loaded into the reactor, and the catalyst loading was 0.02L, 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 VOCs waste gas (composition shown in Table 4) with a volume flow rate of 12L / h was passed into the reactor, and then Introduce 20L / h of air to ignite the VOCs exhaust gas catalytically, and the temperature of the catalyst bed rises rapidly to 450°C; enter the catalytic self-sustaining combustion stage, then adjust the volume flow rate of the VOCs exhaust gas to 6L / h, and feed 75L / h With the volume flow of air, the temper...
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