A method for synergistic resource treatment of acrylonitrile-containing waste gas and waste high-ammonia nitrogen water
A treatment method, acrylonitrile technology, applied in degassed water/sewage treatment, neutralized water/sewage treatment, textile industry wastewater treatment, etc., can solve the problem of increasing operating costs and investment, affecting equipment service life, secondary pollution of nitrogen oxides and other problems, to achieve the effect of low cost, convenient operation and simple process
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Embodiment 1
[0031] A company produces acrylonitrile waste gas in the production process of dye intermediates, with a gas volume of 500Nm 3 / h, acrylonitrile content 1650mg / m 3 , benzene concentration 0.1mg / m 3 , The high ammonia nitrogen wastewater produced by another dye workshop, the ammonia nitrogen is 2000mg / L, and the sodium chloride content is 10%.
[0032] (1) Alkali hydrolysis stripping: adjust the pH of the waste water to 10, raise the temperature of the waste water to 50°C, and feed acrylonitrile waste gas at a gas-liquid ratio of 100:1, the acrylonitrile content of the outlet gas is not detected, and the benzene is not detected. Ammonia nitrogen in wastewater is 300mg / L;
[0033] (2) polymerization evaporation: the above-mentioned waste water is added with hydrochloric acid to adjust pH to 5 and then add a certain amount of sodium persulfate, enter the evaporation system, the evaporation temperature is 85 ° C, the vacuum degree is 0.5 Mpa, and the sodium chloride salt and con...
Embodiment 2
[0036] A company produces acrylonitrile waste gas in the production process of dye intermediates, with a gas volume of 500Nm 3 / h, acrylonitrile content 1650mg / m 3 , benzene concentration 0.1mg / m 3 , The high ammonia nitrogen wastewater produced by another dye workshop, the ammonia nitrogen is 2000mg / L, and the sodium chloride content is 10%.
[0037] (1) Alkali hydrolysis stripping: adjust the pH of the waste water to 11, raise the temperature of the waste water to 60°C, and feed acrylonitrile waste gas at a gas-liquid ratio of 300:1, and the outlet gas acrylonitrile content is 0.2 mg / m 3 , benzene was not detected, and the ammonia nitrogen in the wastewater was 80 mg / L;
[0038] (2) polymerization evaporation: the above-mentioned waste water is added with hydrochloric acid to adjust pH to 5 and then add a certain amount of sodium persulfate, enter the evaporation system, the evaporation temperature is 85 ° C, the vacuum degree is 0.5 Mpa, and the sodium chloride salt and c...
Embodiment 3
[0041] A company produces acrylonitrile waste gas in the production process of dye intermediates, with a gas volume of 500Nm 3 / h, the content of acrylonitrile is 1650mg / m3, the concentration of benzene is 0.1mg / m3, and the high ammonia nitrogen wastewater produced by another dye workshop, the ammonia nitrogen is 2000mg / L, and the sodium chloride content is 10%.
[0042](1) Alkaline hydrolysis stripping: adjust the pH of the waste water to 11, raise the temperature of the waste water to 60°C, and feed acrylonitrile waste gas at a gas-liquid ratio of 300:1, the outlet gas acrylonitrile content is 0.2 mg / m3, and benzene is not detected , wastewater ammonia nitrogen is 80mg / L;
[0043] (2) polymerization evaporation: the above-mentioned waste water is added with hydrochloric acid to adjust pH to 5 and then add a certain amount of sodium persulfate, enter the evaporation system, the evaporation temperature is 85 ° C, the vacuum degree is 0.5 Mpa, and the sodium chloride salt and c...
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