Intelligent treatment device for electroplating synthetical wastewater and control method thereof
A technology of electroplating synthesis and treatment device, which is applied in water treatment parameter control, metallurgical wastewater treatment, multi-stage water treatment, etc. Effect
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Embodiment 1
[0045] This example provides a treatment method for generating 150 cubic meters of comprehensive electroplating wastewater every day.
[0046] 1. The composition of wastewater is as follows:
[0047] Table 1
[0048]
[0049] Note*: Cr is total chromium--Cr 6+ with Cr 3+ Sum.
[0050] 2. Flow / velocity
[0051] Peak flow Q P =15m 3 / h time T P = 4h
[0052] Average flow Q 0 =7.5m 3 / h time T 0 =20h
[0053] 3. Discharge standard after wastewater treatment:
[0054] Table 2
[0055]
[0056] Note*: Cr is total chromium--Cr 6+ with Cr 3+ Sum.
[0057] The system equipment is composed as follows: figure 1 shown
[0058] 1. Waste water collection system: composed of 8.01 tank, ultrasonic level gauge C01, PP centrifugal pump 6.01, electromagnetic flowmeter LM1 and UPVC pipe valve.
[0059] Q P =10m 3 / h T p = 4h batch processing time = 4h batch processing volume = 15×2m 3 (2 reactors, each effective volume = 15m 3 ) = 30m 3 Q t =30÷4=7.5m 3 / h
[00...
Embodiment 2
[0094] The comprehensive electroplating wastewater treatment method that produces 300 cubic meters of electroplating every day provided by this embodiment.
[0095] 1. The composition of wastewater is as follows:
[0096] Table 1
[0097]
[0098] Note*: Cr is total chromium--Cr 6+ with Cr 3+ Sum.
[0099] 2. Flow / velocity
[0100] Peak flow Q P =25m 3 / h time T P =6h
[0101] Average flow Q 0 =15m 3 / h time T 0 =20h
[0102] 3. Discharge standard after wastewater treatment:
[0103] Table 2
[0104]
[0105] Note*: Cr is total chromium--Cr 6+ with Cr 3+ Sum.
[0106] The system equipment is composed as follows:
[0107] 1. Waste water collection system: composed of 8.01 tank, ultrasonic level gauge C01, PP centrifugal pump 6.01, electromagnetic flowmeter LM1 and UPVC pipe valve.
[0108] Q P =25m 3 / h T p = 6h reaction tank batch time = 4h batch capacity = 30×2m 3 (2 reactors, each effective volume = 30m 3 ) = 60m 3 Q t =60÷4=15m 3 / h
[0109]...
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