A device for treating hydrazine waste gas of aircraft emergency power system and its application
An emergency power system and exhaust gas treatment technology, which is applied in the directions of gas treatment, air quality improvement, separation methods, etc., can solve the problems of unavailable layout of equipment, no space for inspection or test work, etc., and achieve strong removal effect and high capacity , High removal efficiency
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Embodiment 1
[0046] A device for treating hydrazine exhaust gas of an aircraft emergency power system, such as figure 1 As shown, it includes a static mixer 7, a vapor-liquid separator 6, a high-gravity reactor 1, an absorption liquid storage tank 2, an absorption liquid circulation pump 9 and a waste liquid storage tank 13; the gas outlet of the static mixer 7 is connected to the gas The gas inlet of the liquid separator 6; the liquid outlet of the gas-liquid separator 6 is connected to the liquid inlet of the absorption liquid storage tank 12, and the gas outlet of the gas-liquid separator 6 is connected to the gas inlet of the supergravity reactor 1; The liquid outlet is connected to the liquid inlet of the absorption liquid storage tank 2; the liquid outlet of the absorption liquid storage tank 2 is connected to the absorption liquid circulation pump 9, and the absorption liquid circulation pump 9 is connected to the waste liquid storage tank 13 through the absorption liquid discharge v...
Embodiment 2
[0053] Adopt the device and process steps as described in embodiment 1 to remove hydrazine and ammonia in the hydrazine waste gas, wherein the hydrazine concentration in the hydrazine waste gas is 98ppm, the ammonia concentration is 2068ppm, and the supergravity level of the supergravity reactor is 200g, enters the supergravity The absorbing liquid flow of reactor is 60L / min, and absorbing liquid temperature is 25 ℃, and absorbing liquid adopts sulfuric acid aqueous solution, and pH value is 2.5, and the hydrazine concentration at the outlet is recorded as 0ppm (instrument detection limit is 0.0012mg / m 3 ), the ammonia concentration is 0.065mg / m 3 .
Embodiment 3
[0055] The device and process steps as described in Example 1 are used to remove hydrazine and ammonia in the hydrazine waste gas, wherein the hydrazine concentration in the hydrazine waste gas is 1030ppm, the ammonia concentration is 25368ppm, and the supergravity level of the supergravity reactor is 200g. The flow rate of the absorbing liquid in the reactor is 100L / min, the temperature of the absorbing liquid is 25°C, the absorbing liquid is sulfuric acid aqueous solution, the pH value is 1.5, the measured concentration of hydrazine at the outlet is 0.056ppm, and the concentration of ammonia is 1.253mg / m 3 .
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