Home News Knowledges Upgrading Biotreated Tailwater: Why Separation Has to Run Ahead of Oxidation

Upgrading Biotreated Tailwater: Why Separation Has to Run Ahead of Oxidation

2026-09-30 3 readings

In the field of industrial wastewater treatment, advanced upgrading of biotreated tailwater has long been a pain point for the industry. Conventional processes often face low COD removal efficiency, high operating costs, and unstable effluent quality, making it hard to meet increasingly stringent environmental discharge standards. The approach that has been getting traction puts physical separation ahead of oxidation rather than the other way round.

The logic: clear the interference before spending oxidant

This process breaks the traditional single model of front-end biochemistry plus back-end advanced treatment, and is centred on two core units: CDFU cyclonic dissolved-air flotation plus CDOF ozone catalytic oxidation as the core pretreatment unit. The complete treatment chain runs from front-end precise impurity removal and modification, through core advanced oxidation degradation, to back-end biological deep purification, achieving stable compliant discharge and resource reuse of the wastewater.

The ordering matters because of what tailwater carries. The residual suspended colloids, aged sludge, hydrophobic organics, and oily substances in biotreated tailwater are the main interfering factors for downstream ozone catalytic oxidation and various biochemical advanced-treatment processes; they not only consume ozone chemicals but also clog media and inhibit microbial activity. Spending ozone on a stream that still carries aged sludge is the most common way these projects blow their operating budget.

Stage one: cyclonic dissolved-air flotation

The cyclonic dissolved-air flotation device, CDFU, enhances the collision and adsorption of microbubbles with pollutants through a cyclonic centrifugal field, and together with a water conditioner dosed by the dosing unit rapidly achieves flocculation, floatation, and separation of pollutants. This unit efficiently removes suspended solids, colloids, and oily substances, with a removal rate above 90%, and simultaneously reduces part of the COD bound to suspended solids, creating low-load, low-interference influent conditions for the ozone catalytic oxidation unit. The off-gas from separation is collected uniformly into a tail-gas treatment device to avoid secondary pollution.

Stage two: ozone catalytic oxidation

The treated effluent then enters the ozone catalytic oxidation device. Under the synergy of the strong oxidizing ozone supplied by the ozone generator and a special catalyst, ozone is catalytically decomposed to generate hydroxyl radicals that attack and break the molecular chains of refractory organics non-selectively, oxidizing them into easily biodegradable small-molecule organics while directly removing part of the residual COD.

Compared with the traditional ozone oxidation process, the technology greatly raises ozone utilization, above 99.98%, reduces chemical dosage, lowers operating costs, and improves treatment efficiency. After this unit, the wastewater B/C ratio can rise above 0.3, creating excellent nutrient-substrate conditions for microbial degradation in various downstream biochemical advanced-treatment processes and thoroughly solving the traditional problem of poor influent biodegradability and low treatment efficiency in advanced biochemical treatment units. The tail gas from the unit is fed uniformly into the tail-gas treatment device to achieve zero ozone emission, and a backwash water system regularly cleans and maintains the device to ensure catalyst activity.

What the downstream biochemical unit gains

After CDFU and CDOF dual optimized treatment, the wastewater has low suspended solids and markedly improved biodegradability; entering various downstream biochemical advanced-treatment processes, the microbial community can fully exert its degradation performance, efficiently biodegrading and filtering small-molecule organics, ammonia nitrogen, and other pollutants. Thanks to the precise pretreatment of the front-end process, the operating load of the downstream unit is greatly reduced, the media clogging risk drops significantly, the operating cycle is extended, and the effluent quality is more stable and reliable.

Four advantages, stated as engineering claims

Greatly improved pollutant removal efficiency: the synergistic action of the two units gives excellent removal of COD, suspended solids, color, and other pollutants in biotreated tailwater, with a COD removal rate of 40%-70% depending on water quality, achieving the dual effect of front-end pollution reduction plus back-end quality improvement.

Significantly enhanced stability of the downstream process: the front-end pretreatment unit effectively removes interfering substances such as suspended solids and oil, avoiding media clogging and microbial poisoning in the downstream biochemical unit, while ozone catalytic oxidation improves biodegradability, giving the downstream unit higher microbial community activity.

Economically controllable operating costs: ozone catalytic oxidation greatly raises ozone utilization and reduces power and chemical consumption, and front-end pretreatment reduces the load on the downstream biochemical unit and cuts backwash frequency and maintenance costs, lowering comprehensive operating cost by more than 30% compared with traditional Fenton, electrocoagulation, and similar processes.

Green, environmentally friendly, no secondary pollution: the ozone oxidation process produces no chemical sludge; the tail gas is treated uniformly and discharged up to standard, there is no chemical residue, and no secondary pollution is generated.

Where it fits

The process is widely suitable for advanced treatment of biotreated tailwater in the chemical, printing and dyeing, pharmaceutical, and municipal sewage industries, and is especially suited to upgrading projects of existing wastewater treatment plants. Through the empowerment of the core pretreatment unit, enterprises can not only achieve stable compliant discharge and avoid environmental risks but also reduce fresh water consumption through effluent reuse, realizing water resource recycling with both environmental and economic benefits.