Simultaneous gas-phase desulfurization and denitration method for smoke gas
A technology for desulfurization, denitrification and flue gas, which is applied in the field of simultaneous gas-phase desulfurization and denitrification of flue gas and gas-phase desulfurization and denitrification of flue gas, which can solve the problems of complex operation, high operation and maintenance costs, and high investment in fixed assets.
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[0029] The technical solutions of the present invention will be further described below in conjunction with the examples, but the protection scope of the present invention is not limited thereto.
[0030] The flue gas to be treated described in the embodiment is flue gas from thermal power plant, NO X About 600mg / m 3 , SO 2 About 3000mg / m 3 ; NO in flue gas of thermal power plant X The main component is NO, accounting for about X More than 95% of the total, the rest is NO 2 .
Embodiment 1
[0032] A method for simultaneous gas-phase desulfurization and denitrification of flue gas, comprising the following steps:
[0033] (1) Using air as the carrier gas, inject a mixture of 805.5kg of urea and 78.5kg of ammonium chloride, a compound desulfurization and denitrification agent, into the reaction zone. The desulfurization and denitrification agent and the SO in the flue gas 2 The molar ratio is 0.9:1, and the NO in the flue gas X The molar ratio is 1:1, the total usage is the sum of the two, and the injection pressure is 35kpa;
[0034] (2) Under the condition that the temperature of the reaction zone is 850°C, after 2 seconds of reaction, it is ready;
[0035] SO in flue gas before and after treatment was detected by flue gas analyzer 2 , NO X Concentration, calculated to give SO 2 The removal rate reaches 96.0%, NO X The removal rate is 75.7%.
Embodiment 2
[0037] The method for simultaneous gas-phase desulfurization and denitrification of flue gas as described in Example 1 is different in that: the temperature in the reaction zone is 950°C, and the reaction time is 2s.
[0038] SO in flue gas before and after treatment was detected by flue gas analyzer 2 , NO X Concentration, calculated to give SO 2 The removal rate reaches 98.0%, NO X The removal rate reached 81.5%.
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