A method and device for oxidizing and absorbing pollutants in natural gas boiler flue gas
A boiler flue gas, oxidation absorption technology, applied in chemical instruments and methods, waste heat treatment, separation methods, etc., can solve the problems of poor purity of by-products, low efficiency of NOx treatment, failure to meet emission standards, etc., and achieve low emissions and operating costs Reduce and eliminate the effect of white smoke
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Embodiment 1
[0036] The method for oxidizing and absorbing pollutants in the flue gas of a natural gas boiler in this embodiment includes the following steps:
[0037] S101. Cooling the flue gas to remove water to obtain dewatered flue gas and acidic flue gas condensed water, the cooling is to lower the temperature to below 47°C;
[0038] S102. The ozone generated by the ozone generator oxidizes the gaseous low-valence nitrogen oxides in the flue gas into water-soluble high-valence nitrogen oxides in the oxidation tower or an alternative oxidation tower. The molar ratio of NO content in the gas is 1.2, the residence time of the flue gas in the oxidation tower or alternative oxidation tower is 1s, and the main reaction is:
[0039] o 3 +NO=O 2 +NO 2
[0040] o 3 +NO 2 =O 2 +NO 3
[0041] NO 2 +NO 3 =N 2 o 5 .
[0042] S103, using a two-stage absorption method to absorb and treat nitrogen oxides and sulfur dioxide in the flue gas, and use an aqueous solution of ammonia substanc...
Embodiment 2
[0054] The method for oxidizing and absorbing pollutants in the flue gas of a natural gas boiler in this embodiment includes the following steps:
[0055] S201. Cooling the flue gas to remove water to obtain dewatered flue gas and acidic flue gas condensed water, the cooling is to lower the temperature to below 47°C;
[0056] S202. The ozone generated by the ozone generator oxidizes the gaseous low-valence nitrogen oxides in the flue gas into water-soluble high-valence nitrogen oxides in the oxidation tower or an alternative oxidation tower. The molar ratio of NO content in the gas is 1.5, the residence time of the flue gas in the oxidation tower or alternative oxidation tower is 1s, and the main reaction is:
[0057] o 3 +NO=O 2 +NO 2
[0058] o 3 +NO 2 =O 2 +NO 3
[0059] NO 2 +NO 3 =N 2 o 5 .
[0060] S203, using a two-stage absorption method to absorb and treat nitrogen oxides and sulfur dioxide in the flue gas, and use an aqueous solution of ammonia substanc...
Embodiment 3
[0072] The device for oxidizing and absorbing pollutants in natural gas boiler flue gas in this embodiment includes a three-way flue 1, a gas / liquid heat exchanger 2, an oxidation tower 3, a primary absorption tower 4, a secondary absorption tower 5, and an induced draft fan 6. Emission cylinder 7 and ozone generator 8;
[0073]The three-way flue 1 is connected to the flue gas outlet of the boiler, one outlet of the three-way flue 1 is connected to the flue gas inlet of the gas / liquid heat exchanger 2 through the flue pipe 10, and the other outlet is connected to the discharge cylinder 7 Connection, since the three-way flue 1 is provided, it can be used to balance the pressure in the combustion chamber of the natural gas boiler. In addition, the liquid inlet of the gas / liquid heat exchanger 2 communicates with the user heating return pipe 11 , and the liquid outlet communicates with the user heating water supply pipe 12 for recovering waste heat from flue gas. The temperature...
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