Device system for preparing nitric acid and using method of device system
A technology of nitric acid and dust removal system, applied in the direction of nitric acid, nitrogen oxides/oxyacids, etc., can solve the problems of reducing the height of the compressor scale absorption tower, large compressor scale, and high equipment investment, so as to reduce equipment investment and scale.  , the effect of volume reduction
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Embodiment 1
[0062] like figure 1 As shown, a device system for preparing nitric acid includes a steam mixing chamber 1, a cooler assembly, a buffer tank 4, a compressor 5, an absorption tower 6 and a tail gas treatment device in turn; wherein, the cooler assembly includes a primary cooler 2. Secondary cooler 3 ; the tail gas treatment device includes a tail gas heat exchanger 8 and a reactor 9 .
[0063] like figure 1 As shown, the steam mixing chamber 1 is used for receiving nitrate decomposition exhaust gas or NO prepared by ammonia oxidation method 2 2. Mixing reaction is carried out after the water vapor; the steam mixing chamber 1 is provided with a first air inlet 11 and a second air inlet 12, and the first air inlet 11 is used for feeding nitrate decomposition tail gas or ammonia oxidation method prepared NO 2 ; The second air inlet 12 is used to introduce high temperature steam; the steam mixing chamber 1 is provided with a first sprayer 111, the first sprayer 111 is connected ...
Embodiment 2
[0069] like figure 2 As shown, a device system for preparing nitric acid includes a steam mixing chamber 1, a dust removal system 7, a cooler assembly, a buffer tank 4, a compressor 5, an absorption tower 6 and a tail gas treatment device in turn; wherein, the cooler assembly includes The primary cooler 2, the secondary cooler 3; the tail gas treatment device includes a tail gas heat exchanger 8 and a reactor 9, and the tail gas heat exchanger is provided with two channels, which are the third air inlet 81 - the first An air outlet and a fourth air inlet 82 - a second air outlet, the two gas passages are used for heat exchange of different gases.
[0070] like figure 2 As shown, the steam mixing chamber 1 is used for receiving nitrate decomposition exhaust gas or NO prepared by ammonia oxidation method 2 2. Mixing reaction is carried out after the water vapor; the steam mixing chamber 1 is provided with a first air inlet 11 and a second air inlet 12, and the first air inlet ...
Embodiment 3
[0079] The decomposed and dust-collected gas of cobalt nitrate was introduced into the device system of Example 2, wherein the NOX concentration in the decomposed and dust-collected gas of cobalt nitrate was 80%, and the temperature was 180°C. The gas first passes through the steam mixing chamber 1, so that the water content in the mixture rises to 56%, and the temperature rises to 220°C. After that, the exhaust gas is preheated by the exhaust gas heat exchanger 8, and the temperature of the gas after heat exchange drops to 190 ° C. The gas after heat exchange is deeply dedusted by the dust removal system 7. Cooling lowered the temperature below the dew point temperature of nitric acid, which was 67°C. A large amount of 28% condensed dilute nitric acid is obtained, and the gas is cooled again through the secondary cooler 3 to make the temperature drop to 30° C. to obtain another part of dilute nitric acid, and both parts of the condensed dilute nitric acid are injected into th...
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