A flue gas purification device for improving the utilization rate of waste heat and denitration rate and using method thereof
A flue gas purification and utilization technology, applied in chemical instruments and methods, separation methods, gas treatment, etc., can solve problems such as heavy moisture content, large water consumption, and impact on the life of FRP materials
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[0103] According to the first embodiment provided by the present invention, a flue gas purification device for improving waste heat utilization rate and denitrification rate is provided.
[0104] A flue gas purification device for improving waste heat utilization rate and denitrification rate, according to the direction of flue gas, the device includes a primary adsorption tower 1 and a secondary adsorption tower 2 arranged downstream of the primary adsorption tower 1 . The raw flue gas delivery pipeline L0 is connected to the flue gas inlet 101 of the primary adsorption tower 1 . The flue gas outlet 102 of the primary adsorption tower 1 is connected to the flue gas inlet 201 of the secondary adsorption tower 2 through a first pipeline L1. The device also includes a desorption tower 3 . The desorption tower 3 is provided with a heating section 4 and a cooling section 5 . The lower part of the heating section 4 is provided with a heating section gas inlet 401 , and the upper ...
Embodiment 1
[0121] Such as figure 1 As shown, a flue gas purification device for improving waste heat utilization rate and denitrification rate, according to the flue gas direction, the device includes a primary adsorption tower 1 and a secondary adsorption tower 2 arranged downstream of the primary adsorption tower 1 . The raw flue gas delivery pipeline L0 is connected to the flue gas inlet 101 of the primary adsorption tower 1 . The flue gas outlet 102 of the primary adsorption tower 1 is connected to the flue gas inlet 201 of the secondary adsorption tower 2 through a first pipeline L1. The device also includes a desorption tower 3 . The desorption tower 3 is provided with a heating section 4 and a cooling section 5 . The lower part of the heating section 4 is provided with a heating section gas inlet 401 , and the upper part of the heating section 4 is provided with a heating section gas outlet 402 . The gas outlet 402 of the heating section of the analysis tower 3 is connected to ...
Embodiment 2
[0126] Repeat Example 1, except that the secondary adsorption tower 2 is arranged on the top of the primary adsorption tower 1. The top of the secondary adsorption tower 2 is provided with a secondary adsorption tower activated carbon inlet 203 . The bottom of the primary adsorption tower 1 is provided with an outlet 104 for the activated carbon of the primary adsorption tower. The top of the analysis tower 3 is provided with an inlet 301 for the activated carbon of the analysis tower. The bottom of the analysis tower 3 is provided with an outlet 302 for the activated carbon of the analysis tower.
[0127] Wherein, the activated carbon outlet 104 of the primary adsorption tower is connected with the activated carbon inlet 301 of the desorption tower. The activated carbon outlet 302 of the analysis tower is connected with the activated carbon inlet 203 of the secondary adsorption tower.
[0128] The device also includes a first conveyor 7 for transporting the activated carbo...
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