Novel process for treating industrial wastewater with benzyl alcohol
A technology for industrial wastewater and benzyl alcohol, applied in multi-stage water treatment, water/sewage treatment, natural water treatment and other directions, can solve the problems of production system impact, multi-effect evaporation method side reaction, inability to biochemically treat benzyl alcohol wastewater, etc. To achieve the effect of reducing operating costs, saving steam, and achieving significant economic and environmental benefits
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Embodiment 1
[0028] combine figure 1 , 2 , Shown in 3, novel technique of the present invention comprises the following steps:
[0029] 1) Waste water 1 enters waste water storage tank a, adds flocculant 2, and performs continuous oil-water separation. The upper layer oil phase 3 continuously overflows into the crude distillation tower b, the middle layer water phase 4 is continuously pumped into the resin adsorption tower c, and the lower layer mud 5 according to After settling time, it is withdrawn from the waste water storage tank a, enters the filter press d for pressure filtration, and the filtrate is transferred back to the waste water storage tank a.
[0030] 2) The middle water phase 4 is sequentially pumped into the fourth-stage resin adsorption tower c for adsorption treatment. The adsorption flow rate is generally 1.2bv / h of resin capacity, and the first-stage adsorption tower reaches saturation after 8 hours of adsorption time, and the content of benzyl alcohol in the effluen...
Embodiment 2
[0035] combine figure 1 , 2 , Shown in 3, novel technique of the present invention comprises the following steps:
[0036] 1) Waste water 1 enters waste water storage tank a, adds flocculant 2, and performs continuous oil-water separation. The upper layer oil phase 3 continuously overflows into the crude distillation tower b, the middle layer water phase 4 is continuously pumped into the resin adsorption tower c, and the lower layer mud 5 according to After settling time, it is withdrawn from the waste water storage tank a, enters the filter press d for pressure filtration, and the filtrate is transferred back to the waste water storage tank a.
[0037] 2) The middle water phase 4 is sequentially pumped into the fourth-stage resin adsorption tower c for adsorption treatment. The adsorption flow rate is generally 1.3bv / h of resin capacity, and the first-stage adsorption tower reaches saturation after 10 hours of adsorption time, and the content of benzyl alcohol in the effluent...
Embodiment 3
[0042] combine figure 1 , 2 , Shown in 3, novel technique of the present invention comprises the following steps:
[0043] 1) Waste water 1 enters waste water storage tank a, adds flocculant 2, and performs continuous oil-water separation. The upper layer oil phase 3 continuously overflows into the crude distillation tower b, the middle layer water phase 4 is continuously pumped into the resin adsorption tower c, and the lower layer mud 5 according to After settling time, it is withdrawn from the waste water storage tank a, enters the filter press d for pressure filtration, and the filtrate is transferred back to the waste water storage tank a.
[0044] 2) The middle water phase 4 is sequentially pumped into the fourth-stage resin adsorption tower c for adsorption treatment. The adsorption flow rate is generally 1.5bv / h of resin capacity. Generally, the first-stage adsorption tower reaches saturation after 12 hours of adsorption time, and the content of benzyl alcohol in the...
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