Composite catalyst for aid-containing wastewater treatment
A composite catalyst and wastewater treatment technology, which is applied in physical/chemical process catalysts, molecular sieve catalysts, water/sewage treatment, etc., can solve the problems of large changes in pollutant concentration, avoid the loss of active metals, and stabilize catalyst performance. The effect of widening the operating temperature
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Embodiment 1
[0032] Preparation of Catalyst A:
[0033] 1) claim that 261g ruthenium chloride trihydrate is dissolved in 10L deionized water to form solution A;
[0034] 2) Weigh 1Kg of coconut shell activated carbon, place it in a muffle furnace at 100°C for high temperature activation for a period of time, and cool to room temperature to obtain activated carrier B;
[0035] 3) Add 500g of activated carrier B to 2L of solution A and soak for 5 hours, and filter to obtain catalyst precursor C;
[0036] 4) Precursor C was dried at 80° C. for 5 hours, and then calcined at 800° C. for 8 hours to obtain catalyst A. According to detection and analysis, the loading amount of ruthenium was 0.21 wt%.
Embodiment 2
[0038] Preparation of Catalyst B:
[0039] 1) Weigh 250g of manganese nitrate and dissolve it in 5L of deionized water, then add 150mL of 30% hydrogen peroxide, and react at 30°C for 1 hour to obtain reaction solution A;
[0040] 2) Add 1Kg ZSM-5 molecular sieve to the reaction solution A and soak for 5 hours, filter and dry to obtain catalyst precursor A;
[0041] 3) Dissolve 26g of cobalt chloride and 272g of zinc chloride in 5L of deionized water to obtain solution B, place precursor A in solution B and immerse for 5 hours to obtain catalytic precursor B;
[0042] 4) Dry the catalyst precursor B at 80°C for 3 hours, then put it into a muffle furnace, and calcinate it at 600°C for 8 hours to obtain catalyst B. After detection and analysis, the content of the catalyst active component Mn is 1.12wt %, the content of Co is 0.12wt%, and the content of zinc is 2.08wt%.
Embodiment 3
[0044] The catalyst A1 prepared in Example 1 is mixed with the catalyst B1 prepared in Example 1 in a mass ratio of 1:10 composite catalyst D1.
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