A kind of treatment method of dye wastewater
A dye wastewater, treatment method technology, applied in textile industry wastewater treatment, water/sewage treatment, special compound water treatment, etc. Stabilization, organic load reduction and toxicity suppression effects
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Embodiment 1
[0043] A printing and dyeing factory mainly processes dyeing and finishing treatment of cotton, hemp, and chemical fibers. The high-concentration wastewater generated mainly comes from desizing wastewater, scouring wastewater, dyeing wastewater, and printing wastewater. The types of dyes are complex, and the COD concentration, color high degree. The water quality indicators are shown in Table 1. Adopt processing method of the present invention to process, operate as follows:
[0044] Dye wastewater enters the flocculation tank, FeCl 3 The addition amount is 35mg / g (COD cr ), FeCl 3, Diatomaceous earth and lime are added in a mass ratio of 15:3:1, stirring and reacting for 5-15 minutes before precipitation. Add sulfuric acid to the supernatant to adjust the pH to 6 and then enter the UASB anaerobic reaction tank for a residence time of 6 hours. The pool effluent enters the CASS reaction pool, the residence time is 8 hours, and the dissolved oxygen concentration is 4-6mg / L....
Embodiment 2
[0048] A printing and dyeing factory mainly processes the dyeing and finishing treatment of cotton, hemp, chemical fibers, etc. The comprehensive wastewater generated mainly comes from desizing wastewater, cooking wastewater, dyeing wastewater, printing wastewater, bleaching wastewater and other processes. High degree. The water quality indicators are shown in Table 2. Adopt processing method of the present invention to process, operate as follows:
[0049] Dye wastewater enters the flocculation tank, FeCl 3 The addition amount is 15mg / g (COD cr ), FeCl 3 , Diatomaceous earth and lime are added in a mass ratio of 10::2:0.5, stirring and reacting for 5-15 minutes before precipitation. Add sodium hydroxide to the supernatant to adjust the pH to 7, then enter the IC anaerobic reaction tank, the residence time is 6 hours, the effluent from the anaerobic tank enters the hydrolysis acidification tank, the residence time is 18 hours, the concentration of dissolved oxygen is 0.2-0...
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