Desulfurization catalyst of limestone-gypsum wet coal-fired boiler flue gas desulfurization process
A technology for desulfurization catalysts and coal-fired boilers, applied in physical/chemical process catalysts, organic compounds/hydrides/coordination complex catalysts, separation methods, etc., can solve problems such as short synergistic time, strong odor, and hazards. Achieve the effects of improving desulfurization efficiency, catalytic oxidation process, and improving reaction efficiency
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Embodiment 1
[0019] Limestone-gypsum wet coal-fired boiler flue gas desulfurization catalyst, including the following weight (kg) of raw materials: 80kg of CH 3 COONH 4 , 18kg of NH 4 Cl, 0.5kg of alcohol ether phosphate monoester, 1kg of alkyl alcohol ether carboxylate and 0.5kg of fatty alcohol ethyl oxide. The pH value of the desulfurization catalyst is 6.
Embodiment 2
[0021] Limestone-gypsum wet coal-fired boiler flue gas desulfurization catalyst, including the following weight (kg) of raw materials: 85kg of CH 3 COONH 4 , 12kg of NH 4 Cl, the alcohol ether phosphate monoester of 1kg, the alkyl alcohol ether carboxylate of 1.5kg and the fatty alcohol ethyl oxide of 0.5kg. The pH value of the desulfurization catalyst is 5.5.
Embodiment 3
[0023] Limestone-gypsum wet coal-fired boiler flue gas desulfurization catalyst, including the following weight (kg) of raw materials: 78kg of CH 3 COONH 4 , 20kg of NH 4 Cl, 0.5 kg of alcohol ether phosphate monoester, 0.5 kg of alkyl alcohol ether carboxylate and 1 kg of fatty alcohol ethyl oxide. The pH value of the desulfurization catalyst is 6.
[0024] The use of the catalyst of the limestone-gypsum wet coal-fired boiler flue gas desulfurization process of the present invention is described in detail below:
[0025] 1. Record the load of the absorption tower after adding the desulfurization catalyst, the original flue gas SO at the required time interval 2 content, net flue gas SO 2 Desulfurization efficiency and SO 2 Emissions meet the requirements.
[0026] 2. Release part of the slurry in the absorption tower to the pit of the drainage pool, add the desulfurization catalyst of the present invention (the first addition amount needs to be based on the required des...
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