一种高TDS废水净化回用系统
By employing a synergistic process of biological pretreatment, chemical softening, and dual-stage reverse osmosis, the problem of poor treatment effect for high TDS wastewater has been solved, achieving efficient industrial wastewater reuse and near-zero discharge, which is suitable for the chemical and pharmaceutical industries.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- CHINA PETROLEUM & CHEMICAL CORP
- Filing Date
- 2025-07-18
- Publication Date
- 2026-07-17
AI Technical Summary
Existing biochemical methods for treating industrial wastewater with high TDS levels are ineffective and cannot meet the standards for industrial circulating water reuse. Furthermore, salt accumulation affects microbial activity, leading to treatment stability issues.
The system employs a synergistic process of biological pretreatment, chemical softening, ultrafiltration, and dual-stage reverse osmosis, including an activated sludge aeration tank, a softening tank, an ultrafiltration membrane system, a low-pressure reverse osmosis unit, and a disc tube reverse osmosis unit, to perform biodegradation, hardening removal, suspended solids removal, and efficient desalination, achieving tiered purification.
The effluent TDS is ≤200mg/L and suspended solids are ≤1mg/L, meeting industrial reuse standards. The system recovery rate is over 80%, significantly reducing concentrated wastewater discharge and achieving efficient reuse and near-zero discharge of high-salt wastewater.
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Figure CN224513334U_ABST
Abstract
Claims
1. A high TDS wastewater purification and reuse system, characterized in that, It includes an activated sludge aeration tank, a softening tank, an ultrafiltration membrane system, a low-pressure reverse osmosis unit, and a disc tube reverse osmosis unit connected in sequence. The activated sludge aeration tank is equipped with an aeration structure and aerobic bacterial activated sludge, which is used to biodegrade the received high TDS wastewater. The softening tank is used to receive the effluent from the activated sludge aeration tank for hardening removal treatment. The ultrafiltration membrane system is used to receive the water effluent from the softening tank to remove suspended solids and colloids; The low-pressure reverse osmosis unit is used to receive the effluent from the ultrafiltration membrane system to remove dissolved salts and small molecule organic matter, and the produced water is connected to the reuse system; The disc tube reverse osmosis unit is used to receive the concentrate discharged from the low-pressure reverse osmosis unit for further concentration, and the produced water is connected to the reuse system.
2. The high TDS wastewater purification and reuse system of claim 1, characterized in that, The softening tank is connected to a dosing device, which contains the chemical agents required for softening; the softening tank is equipped with a stirring device.
3. The high TDS wastewater purification and reuse system of claim 2, wherein, The dosing device contains sodium hydroxide and sodium carbonate.
4. The high TDS wastewater purification and reuse system according to claim 1, characterized in that, An ultrafiltration buffer tank is provided between the softening tank and the ultrafiltration membrane system to regulate water flow and pressure.
5. The high TDS wastewater purification and reuse system of claim 4, wherein, A pH adjustment device is installed on the connecting pipeline between the softening tank and the ultrafiltration buffer tank.
6. The high TDS wastewater purification and reuse system of claim 5, wherein, An ultrafiltration feed pump is provided between the ultrafiltration buffer tank and the ultrafiltration membrane system.
7. The high TDS wastewater purification and reuse system of claim 1, wherein, An RO feed water buffer tank is provided between the ultrafiltration membrane system and the low-pressure reverse osmosis device to regulate water flow and pressure.
8. The high TDS wastewater purification and reuse system according to any one of claims 1-7, wherein, It also includes a finished water tank, the inlet of which is connected to the product water inlet of the low-pressure reverse osmosis unit and the product water inlet of the disc tube reverse osmosis unit, respectively.
9. The high TDS wastewater purification and reuse system of claim 8, wherein, The finished water tank is connected to a finished water pump, which is used to pump the purified water in the finished water tank to the reuse system.
10. The high TDS wastewater purification and reuse system of claim 9, wherein, It also includes an evaporation crystallization system, whose inlet is connected to the concentrated water outlet of the disc tube reverse osmosis unit, for receiving the concentrated water discharged from the disc tube reverse osmosis unit and performing evaporation crystallization.