Treating fluid for treating nitric oxide in waste gas
A nitrogen oxide and treatment liquid technology, applied in chemical instruments and methods, dispersed particle separation, separation methods, etc., can solve the problems of difficult to meet the standard treatment, complex process, a large amount of urea waste liquid, etc., to reduce equipment investment costs and Operating costs, extensive promotion and application value, and high processing efficiency
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Embodiment 1
[0026] Method for producing nitrogen oxide exhaust gas for the test: Add 5kg of carbon steel into an open plastic barrel with 10kg of 50% nitric acid to generate brown-red smoke of nitrogen oxide. On the self-developed gas treatment device, the gas flow rate of the fan is 10-20m 3 / min is adjustable, and the handheld detector shows that the concentration of nitrogen oxides is 5000mg / L. Due to the unstable flue gas concentration, the maximum concentration time period was used for the test, and new reaction raw materials were taken each time to prevent adverse effects caused by the dilution of nitric acid. The initial reaction temperature for nitrogen oxides is room temperature, about 20-25°C, and the reaction process is exothermic.
[0027] Prepare 5 tons of treatment liquid, the composition of the treatment liquid is:
[0028] 15% urea, 20mmol / L tetraethylenepentamine cobalt, temperature 60 ℃, continuous air for 2h to start.
[0029] The above-mentioned nitrogen oxide waste...
Embodiment 2
[0030] Prepare 5 tons of treatment solution, the composition is: 15% (w) urea, 30mmol / L tetraethylenepentamine cobalt, heat the treatment solution to a working temperature of 58°C, add 50kg of starter agent with a concentration of 30% hydrogen peroxide, and react for 1h.
[0031] The nitrogen oxide waste gas obtained in Example 1 first enters the reflux condenser, and the nitric acid volatilized in the waste gas is condensed into a liquid; then enters the gas-liquid separator, and the liquefied nitric acid is separated from the nitrogen oxide waste gas; The separated gas enters the bubbling absorption reaction device, and the exhaust gas containing nitrogen oxides reacts with the above-mentioned treatment liquid in the bubbling absorption reaction device. The temperature of the treatment liquid is 58°C, and the flow rate of the waste gas is 18m 3 / min; Finally, the remaining gas after being treated with the treatment liquid in the bubbling absorption reaction device enters the ...
Embodiment 3
[0033] Run continuously for 12 hours according to Example 2, and replenish desalted water every 4 hours to maintain the volume of the treatment solution. The online detection concentration at the outlet is 99mg / L, and the treatment efficiency is 98.02%.
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