Method for denitrifying flue gas by using amino reducing agent with high reaction activity
A reducing agent and active technology, applied in the field of flue gas denitrification, can solve the problems of high reaction energy consumption, high catalyst input cost, and difficult regeneration.
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Embodiment 1
[0039] Example 1: Flue gas denitrification in thermal power plants, NO X About 500ppmv.
[0040] NO in flue gas of thermal power plant X The main component is NO, accounting for about X More than 95% of the rest is NO 2 .
[0041] Add 34.5g of cyanuric acid into the reactor, control the temperature at about 350°C, and heat to produce active ammonia reducing agent cyanic acid and isocyanic acid, which are injected into the grid and mixed with NO X The flue gas is fully mixed into the denitrification reaction zone, and the NO X The molar ratio of the reaction is 0.8:1. After the reaction is carried out at a temperature of about 550° C. for 1 second, the reaction effluent enters the nitrogen oxide analyzer. Analysis of NO in flue gas before and after purification X Concentration, the removal rate of nitrogen oxides reaches 86%.
Embodiment 2
[0043] As described in Example 1, the difference is:
[0044] (1) Pre-decomposition of raw materials: 48g of urea is heated and decomposed into cyanuric acid and ammonia at 250°C;
[0045] (2) Gained cyanuric acid is carried out flue gas denitrification by the method for embodiment 1 again as the raw material of active amino reducing agent. Analysis of NO in flue gas before and after purification X Concentration, the removal rate of nitrogen oxides reaches 86%.
[0046] The ammonia gas in step (1) is used at 350°C for catalytic reduction and denitrification in the SCR system.
Embodiment 3
[0048] As described in Example 1, the difference is: 18.6g of methylamine is added to the reactor, the temperature is controlled at about 100°C, and the active ammonia reducing agent gaseous methylamine produced by heating is combined with NO X The molar ratio of the reaction is 0.6:1, and the reaction temperature is maintained at 540-580 ° C. After the reaction stays for 1 second, the reaction effluent enters the nitrogen oxide analyzer. NO in flue gas before and after purification X Concentration analysis shows that the removal rate of nitrogen oxides reaches 75%.
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