Method for treatng wastewater of producing reactive dyes in class of bromamine acid, and for reclaiming resources
A technology for reactive dyes and production wastewater, applied in separation methods, adsorption water/sewage treatment, filter regeneration, etc., can solve problems such as effective treatment of bromamic acid reactive dye production wastewater, resource recycling, environmental river pollution, etc.
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Embodiment 1
[0018] Example 1: Each 10mL of NDA-99, NDA-180 and NDA-181 resins were loaded into three jacketed glass adsorption columns (Ф12×160mm), and the production wastewater of Active Brilliant Blue X-BR was at 25±5 °C flows through three adsorption columns at a flow rate of 20mL / h, 10mL / h and 10mL / h in sequence, and the processing volumes are 34mL / batch, 40mL / batch and 250mL / batch respectively.
[0019] For saturated NDA-99, use 10mL 2moL / L NaOH aqueous solution, 10mL 1moL / L NaOH aqueous solution and 20mL water as a composite desorbent, at a temperature of 60±5°C, flow through the resin bed at a flow rate of 10mL / h layer is desorbed. The desorbed high-concentration NaOH desorption solution (10 mL) is adjusted to acid and the organic matter obtained after distillation is mainly composed of 2,4-diaminobenzenesulfonic acid, which can be recycled. The low-concentration alkali and water desorption solution sets are used for the next batch of desorption operations.
[0020] For adsorbed ...
Embodiment 2
[0023] Embodiment 2: other basic conditions are the same as embodiment 1, except that the temperature of waste water flowing through three adsorption columns (towers) is 5 ± 5 ℃, and the desorption temperature is 10 ± 5 ℃, and the treatment effect is not as good as that of embodiment 1.
Embodiment 3
[0024] Embodiment 3: other basic conditions are the same as embodiment 1, except that the temperature of waste water flowing through three adsorption columns (towers) is 50 ± 5 ℃, and the desorption temperature is 60 ± 5 ℃, and the treatment effect is not as good as that of embodiment 1.
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