A composite catalyst for degrading organic chlorine pollutants and its preparation method
A composite catalyst and pollutant technology, applied in physical/chemical process catalysts, water pollutants, chemical instruments and methods, etc., can solve the problems of high purity of nano-zero valent iron, high technical equipment requirements, poor agglomeration performance, etc. Low equipment requirements, guaranteed degradation rate, and less agglomeration
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[0035] 1. Preparation of solution A: Take 30ml of absolute ethanol and add it to a 250ml Erlenmeyer flask, and put the Erlenmeyer flask into a 40°C water bath to heat and stir; slowly add 10ml of butyl titanate to the vigorously stirred Erlenmeyer flask , and then quickly add 3ml of glacial acetic acid and Fe(NO 3 ) 3 , keep stirring at 40°C for 30 minutes to prepare solution A, wherein the mass ratio of Ti to Fe is 0.05;
[0036] 2. Preparation of solution B: Take 10ml of absolute ethanol and 5ml of distilled water in a 50ml small beaker, then add hydrofluoric acid, adjust the pH to 2 with concentrated nitric acid, and make solution B, wherein the molar ratio of Ti to F is 0.01;
[0037] 3. Fe 3+ / F-TiO 2 Preparation of powder: Add solution B dropwise to solution A with vigorous stirring in a water bath at 40°C, age for 24 hours to obtain a gel, dry in an oven at 80°C, and roast in a vacuum at 100°C for 6 hours to obtain Fe 3+ / F-TiO 2 powder;
[0038] 4. Fe 0 / F-TiO ...
Embodiment 1
[0041] The influence of embodiment 1 calcining temperature on composite catalyst degradation performance
[0042] The calcination conditions were changed as shown in Table 1, and other steps were the same as the above preparation method, and 2,4,6-trichlorophenol was degraded according to the above method, and the effect of the composite catalyst on the degradation performance of organochlorine pollutants was studied.
[0043] Table 1 Degradation rate of composite catalyst under different calcination conditions
[0044]
[0045] As can be seen from the above table 1, under the vacuum condition limited by the present invention and the temperature of 100~400 DEG C, the degradation rate of the prepared composite catalyst to organic chlorine pollutants reaches more than 90%, but when the roasting conditions are changed, Decreasing or increasing the calcination temperature has a great influence on the degradation performance of the prepared composite catalyst, and its degradatio...
Embodiment 2
[0047] Embodiment 2 The influence of titanium-iron mass ratio on the degradation performance of composite catalyst
[0048] The mass ratio of titanium to iron was changed as shown in Table 2, and the other steps were the same as the above preparation method, and 2,4,6-trichlorophenol was degraded according to the above method, and the effect of the composite catalyst on the degradation performance of organochlorine pollutants was studied.
[0049] Table 2 Degradation rate of composite catalysts prepared with different titanium-iron mass ratios
[0050]
[0051] As can be seen from the above table 2, under the condition of 0.01~0.2 mass ratio of ferro-titanium limited by the present invention, the degradation rate of the prepared composite catalyst to organic chlorine pollutants reaches more than 90%, but when the mass ratio of ferro-titanium is changed When it is reduced, the degradation rate of the composite catalyst prepared by it to organic chlorine pollutants is reduced...
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