Simultaneous desulfuration and denitration method for smoke by combining photocatalytic oxidation with ammonia method
A photocatalytic oxidation, desulfurization and denitrification technology, applied in the field of flue gas purification, can solve the problems of large investment and difficulty in widespread implementation, and achieve the effects of improving economic benefits, low cost, and reducing operating costs
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Embodiment 1
[0028] With butyl titanate as precursor and ethanol as solvent, Fe(NO 3 ) 3 Introducing dopant ions to prepare Fe by sol-gel method 3+ -TiO 2 The photocatalyst gel was calcined to 550 °C for 3 h to prepare photocatalyst particles. The photocatalyst is supported by a photocatalyst-coated steel plate. The specific process includes: using a stainless steel plate as a substrate, placing SiO 2 After the adhesive and inorganic pigments form the bottom layer, SiO2 is coated on it. 2 Adhesives and Fe-containing 3+ Doped TiO 2 The photocatalyst layer is baked and coated to prepare a photocatalyst-coated steel sheet. Among them, the customized specifications of the stainless steel plate can be 2438 mm × 200 mm × 1 mm.
[0029] The photocatalyst with the above-mentioned coated steel plate fixed on the inner wall is installed between the boiler flue outlet and the desulfurization tower, such as figure 1 shown. The original flue gas volume of the boiler is 490,000 Nm 3 / h (wet b...
Embodiment 2
[0031] The photocatalyst adopts the P25 photocatalyst produced by Degussa, and the photocatalyst is coated on the steel plate. The specific process includes: using a stainless steel plate as a substrate, placing SiO2 After the adhesive and inorganic pigments form the bottom layer, SiO2 is coated on it. 2 The adhesive and the P25 photocatalyst layer are baked and coated to prepare the photocatalyst-coated steel plate.
[0032] Install the photocatalyst coated steel plate prepared above on the inner wall of the photocatalyst, such as figure 1 shown. When the original flue gas volume is 360,000 Nm 3 / h (wet basis), the sulfur content is 6000 mg / Nm 3 , with a nitrogen content of 600 mg / Nm 3 When using 20 wt% ammonia water as the ammonia source, the ammonia water consumption is about 5.9 t / h. The output of the by-product ammonium sulfate ammonium nitrate compound fertilizer is 3.8 t / h, the desulfurization rate reaches 98.5%, and the denitrification rate reaches 70%.
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