Continuous treatment method for dye industry acid wastewater
A technology for acidic wastewater and treatment methods, applied in multi-stage water treatment, water/sewage treatment, chemical instruments and methods, etc., can solve problems such as difficult treatment and secondary pollution, achieve significant energy saving and emission reduction, avoid waste residue generation, The effect of reducing production costs
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[0030] Example 1
[0031] Reference figure 2 , Acidic wastewater comes from wastewater containing sulfuric acid in dye production (sulfuric acid content is 5.68%, COD is 11380mg / L). Both the first desorption tower and the second desorption tower are built with a primary volume of 12m 3 The granular activated carbon adsorption column (granular activated carbon particle size 1.2~1.4mm), the neutralization device is a three-stage series neutralization pot, the physical filtration uses a cloth bag filter, and the temperature of the primary furnace (3) of the regeneration furnace is controlled at 880℃, and the secondary furnace (7) The temperature is 620℃, and the flow meter and valve are used to control the waste water to 5m 3 / h flow rate enters the following steps to control the residence time of the first and second desorption 2.5h, the specific operation is as follows:
[0032] (A) One-time decolorization: The acidic wastewater flows upward through the bottom of a desorption tower...
Example Embodiment
[0039] Example 2
[0040] Acidic wastewater comes from wastewater containing sulfuric acid in dye production (sulfuric acid content is 12.5%, COD is 12510mg / L), a desorption tower is built in four stages in parallel with a volume of 12m 3 The granular activated carbon adsorption column (granular activated carbon particle size 1.2~1.4mm), the second desorption tower has a built-in two-stage parallel connection with a volume of 12m 3 The granular activated carbon adsorption column (granular activated carbon particle size 1.2~1.4mm), the neutralization device is a three-stage series neutralization pot, the temperature of the first furnace of the regeneration furnace is 880 ℃, the temperature of the second furnace is 625 ℃, and the flow rate of waste water removal is 2.5m 3 / h, residence time 4.8h, second dehydration flow rate 5m 3 / h, the residence time is 2.5h, the specific steps are operated according to the method described in Example 1, the difference is that liquid ammonia is adde...
Example Embodiment
[0041] Example 3
[0042] Acidic wastewater comes from wastewater containing hydrochloric acid in dye production (hydrochloric acid content is 6.36%, COD is 16940mg / L). Both the first desorption tower and the second desorption tower have a built-in primary volume of 12m 3 The granular activated carbon adsorption column (granular activated carbon particle size 1.2~1.4mm), the neutralization device is a three-stage series neutralization pot, the physical filtration uses a cloth bag filter, and the temperature of the first furnace is 880℃ and the temperature of the second furnace is 600℃. Use flow meters and valves to control the waste water to 4m 3 / h The flow rate enters the wastewater treatment system, and the residence time of the first and second desorption is controlled to be 3h. The specific steps are operated according to the method described in Example 1. The difference is that part of the first desorption is used as the synthetic bottom water for dye production. The liquid ...
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