Zinc and silicon coblended nano TiO2 light catalyst and its preparing method and use
A nano-titanium dioxide, photocatalyst technology, applied in catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve the problems of photocatalytic activity change, change of lattice type, etc. , to achieve the effect of simple operation, wide application and tight integration
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Embodiment 1
[0020] Using n-butyl titanate as the precursor of titanium dioxide, ethyl orthosilicate as the precursor of silicon doping, Zn(NO 3 ) 2 ·6H 2 O is a zinc-doped precursor, and Si: Zn: Ti = 0.01: 0.001: 1 nanometer TiO is prepared 2 Photocatalyst, the reaction of photocatalytic degradation of benzene, toluene, and xylene is carried out in a batch reactor, and the initial reaction conditions are: the initial concentration of benzene, toluene, and xylene is 58 mg / m 3 、60mg / m 3 , 53mg / m 3 , the humidity is 55%, the reaction temperature is 25°C, and the catalyst loading is 1.51mg / cm 2 . Based on the apparent reaction rate constant k and the degradation efficiency of P25 under the same experimental conditions, the results show that the k values of the catalyst for benzene, toluene, and xylene are 1.6 times, 2.1 times, and 1.8 times that of P25, respectively.
Embodiment 2
[0022] Using n-butyl titanate as the precursor of titanium dioxide, ethyl orthosilicate as the precursor of silicon doping, Zn(NO 3 ) 2 ·6H 2 O is a zinc-doped precursor, and Si: Zn: Ti = 0.01: 0.01: 1 nanometer TiO is prepared 2 Photocatalyst, the photocatalytic degradation of benzene, toluene, and xylene is carried out in a batch reactor. The initial reaction conditions are: the initial concentration of benzene, toluene, and xylene is 60mg / m 3 、65mg / m 3 , 58mg / m 3 , the humidity is 55%, the reaction temperature is 25°C, and the catalyst loading is 1.51mg / cm 2 . Based on the apparent reaction rate constant k and the degradation efficiency of P25 under the same experimental conditions, the results show that the k values of the catalyst for benzene, toluene, and xylene are 2.1 times, 3.5 times, and 2.5 times that of P25, respectively.
Embodiment 3
[0024] Using n-butyl titanate as the precursor of titanium dioxide, ethyl orthosilicate as the precursor of silicon doping, Zn(NO 3 ) 2 ·6H 2 O is a zinc-doped precursor, and Si: Zn: Ti = 0.01: 0.1: 1 nanometer TiO is prepared 2 Photocatalyst, the photocatalytic degradation of benzene, toluene, and xylene is carried out in a batch reactor. The initial reaction conditions are: the initial concentration of benzene, toluene, and xylene is 60mg / m 3 、65mg / m 3 , 58mg / m 3 , the humidity is 55%, the reaction temperature is 25°C, and the catalyst loading is 1.51mg / cm 2 . Based on the apparent reaction rate constant k and the degradation efficiency of P25 under the same experimental conditions, the results show that the k values of the catalyst for benzene, toluene, and xylene are 1.6 times, 2.5 times, and 1.9 times that of P25, respectively.
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