Pyrolysis device for processing desulfurization waste liquid in partial oxidation environment
A technology for desulfurizing waste liquid and oxidizing environment, which is applied in the fields of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. problems, to achieve the effect of realizing resource recycling, flexible operation, and reducing production costs
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Embodiment 1
[0087] Sodium-containing desulfurization waste liquid (hereinafter referred to as waste liquid, the same below), the original liquid and the pyrolysis gas from the pyrolysis gas outlet 1 are concentrated by 30%, and then atomized by atomizing nozzles 6a and 6b, and enters along the tangent line of the inner wall. In the atomization pyrolysis section II, at about 600°C, the waste liquid is further evaporated and concentrated, and the aromatic compounds and other non-salt organic compounds in the waste liquid are decomposed. The decomposed gas, water vapor and the pyrolysis gas from the lower stage pass upwards through the mist eliminator 5 into the gas separation section I, and are discharged after the temperature drops to about 350°C. The waste liquid flow rate is adjusted by detecting the temperature of the temperature detection hole 8a to ensure that the temperature of the atomization pyrolysis section II is stable at about 600°C.
[0088] The waste liquid is concentrated and d...
Embodiment 2
[0101] The device and operation mode are the same as in Example 1, except that the air coefficient is 0.6 and the concentration of waste liquid is 50%. At this time, the temperature of atomized pyrolysis section II is about 550℃, and the temperature of mixed flow pyrolysis section III is 850 At about ℃, the temperature of inactive salt pyrolysis section IV is about 1100℃. The condensate produced by the concentration of waste liquid and the condensate obtained from pyrolysis gas-liquid separation pass through the chiller 10 together, but not spray into the pyrolysis salt chill section. V. Cool the pyrolysis salt together with the cooling medium in the jacket 3 to form solid particles, which can be used as a solid alkali source for gas desulfurization after being discharged through the solid outlet.
[0102] The pyrolysis gas and pyrolysis salt produced by the above two embodiments have the same composition, and the pyrolysis gas is mainly H 2 S, N 2 , CO 2 And H 2 ; Pyrolysis salt...
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