A DCS-based three-stage wastewater pH control method and system
A control method and technology for wastewater, applied in water treatment parameter control, comprehensive factory control, chemical instruments and methods, etc., can solve the problems of pH value overshoot, no protection adjustment tank, inability to accurately control the pH value of wastewater, etc. The effect of reducing hysteresis, reducing pH fluctuations
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Embodiment 1
[0079] A chemical plant produces an alkaline wastewater with a pH between 10 and 12. 8% hydrochloric acid is used as a neutralizing agent to adjust the pH in the third-stage neutralization tank. It is hoped that the pH should be controlled at 5 to 7. In addition to this stream of wastewater, this wastewater tank also receives another alkaline wastewater with a pH value above 13 (2 to 3 times per shift), which makes the flow and composition of wastewater entering the neutralization tank fluctuate greatly. The simple designed loop cannot achieve stable pH control, requiring frequent manual intervention by the operator. The operation volume is as high as 15 times per shift, and the pH overshoot is more than ±3, which not only hinders the long-term stable operation of the wastewater treatment system, but also seriously affects the the degree of automation of the device. To this end, according to the patent, the corresponding hardware and the 5% caustic soda pipeline of the tertiar...
Embodiment 2
[0095] A chemical plant produces an acidic wastewater with a pH value between 3 and 4. 10% caustic soda is used as a neutralizing agent for pH adjustment in the neutralization tank. It is hoped that the pH value should be controlled at 6 to 8, because there is only one level of neutralization. The mixing time of acid wastewater and caustic soda is short, and the neutralization is incomplete. Therefore, the pH value of the wastewater at the outlet of the neutralization tank can only be controlled at (6-10), which affects the service life of downstream devices. To this end, according to this patent, it is transformed into a three-level protection pool, and a 10% caustic soda pipeline is added to the fine adjustment pool, and a 10% caustic soda pipeline and a 10% hydrochloric acid pipeline are added to the protection pool. The scheme is reconfigured.
[0096] After the transformation, the alkaline wastewater first enters the rough adjustment tank, and the neutralizer ratio contro...
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