A method and device for recovering NO2 and SO2 in flue gas by rectification
A technology of SO2 and rectification, which is applied in the field of rectification to recover NO2 and SO2 in flue gas, which can solve the problems of low income, high concentration of main components in rectification, and high cost
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Embodiment 1
[0083] This embodiment proposes a rectification recovery of NO in flue gas 2 and SO 2 devices such as figure 1 As shown, the device includes:
[0084] A cooling heat exchanger for precooling high-temperature flue gas;
[0085] a first rectification column for high-pressure rectification;
[0086] One is used for the second rectification tower of atmospheric rectification;
[0087] a SO 2 liquid storage tank;
[0088] The cooling heat exchanger, the first rectification tower, the second rectification tower and the SO 2 The liquid storage tanks are connected in turn, and the SO 2 The liquid storage tank is connected with the condenser of the second rectification column.
[0089] The device also includes:
[0090] A gas storage tank for storing the tail gas obtained after treatment in the first rectification tower and the tail gas obtained after treatment in the second rectification tower for circulation and separation;
[0091] A gas mixing tank for mixing the gas in t...
Embodiment 2
[0135] A rectification recovery of NO in the flue gas proposed in this embodiment 2 and SO 2 The device is basically the same as in Example 1, except that:
[0136] The specific data of the test are: the inlet flow rate of high-temperature mixed gas (simulated flue gas) is 5L / miI, and the mixed gas component is NO 2 / SO 2 / CO 2 =21.6% / 61.1% / 17.3%, compressor outlet pressure 1.5bar, condenser condensing temperature 0°C; first rectification column pressure 1.1bar, reflux ratio 1.28, theoretical plate number 27, feed plate number 13; The pressure of the second rectifying column is 1.05 bar, the reflux ratio is 3.78, the number of theoretical plates is 7, and the number of feed plates is 3.
[0137] After steady state distillation, NO 2 and SO 2 The purities are 0.999 (volume fraction) and 0.99 (volume fraction) respectively.
Embodiment 3
[0139] This embodiment proposes a rectification recovery of NO in flue gas 2 and SO 2 method, such as figure 2 As shown, the method adopts the device described in Embodiment 1, and the method comprises the steps of:
[0140] Step 1, pressurizing and cooling the high-temperature flue gas to cool the high-temperature flue gas to 0-20°C;
[0141] Step 2, the flue gas cooled in step 1 enters the first rectification tower for one-stage high-pressure rectification, and the NO of heavy components 2 and SO 2 After the mixed liquid is condensed, it enters the tower kettle, and the light component gas is distilled from the top of the tower;
[0142] The light gases include N 2 , CO 2 and NO;
[0143] Step 3, the mixed liquid that enters the tower kettle in step 2 is pumped into the second rectification tower by a metering pump, and the atmospheric pressure rectification separates NO 2 and SO 2 , the tower kettle gets high-purity NO 2 , high-purity SO is obtained at the top of...
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