Hohhot Laundry Wastewater Treatment Case
Commercial laundry wastewater can be difficult to manage because flow, temperature, detergent concentration, suspended fibers, and alkalinity may change throughout the working day. A treatment line therefore needs more than a single biological tank: it needs balanced hydraulic loading, controlled aeration, reliable solids separation, and a disinfection step that can be operated consistently.
A project record in the ZhongQiao Enlightenment company brochure documents a laundry wastewater treatment project in Hohhot, Inner Mongolia, with a design flow of 20 m3/d. The recorded process route is equalization, AO biological treatment, sedimentation, and disinfection. This case explains why that sequence is practical for a small industrial wastewater source and what operators should monitor during commissioning and routine operation.

Project Conditions and Treatment Objective
Laundry facilities often discharge water in batches as washing and rinsing cycles finish. The wastewater may contain detergents, surfactants, lint, fine suspended solids, and biodegradable organic matter. A 20 m3/d facility is relatively compact, but short-term peaks can still be much higher than the daily average. Directly feeding those peaks into a biological reactor can disturb dissolved oxygen, sludge settling, and downstream disinfection.
The documented Hohhot configuration addresses this variability with a staged treatment train. The objective is not to assume that every laundry has identical wastewater, but to create stable conditions for biological treatment. Influent sampling, detergent selection, operating hours, temperature, pH, and local discharge requirements should always be confirmed before final equipment sizing or process adjustment.
Equalization Protects the Biological Stage
The equalization tank is the first control point. It buffers the difference between sudden washing-machine discharges and the steadier flow preferred by downstream equipment. Mixing in this tank helps prevent solids from settling prematurely and reduces concentration swings. Where pH changes are significant, the same stage also provides a practical location for monitoring and controlled adjustment.
For operators, equalization performance should be checked through liquid level trends, transfer-pump cycling, pH, odor, and the condition of the mixing equipment. The usable storage volume must match the actual discharge pattern rather than the average daily flow alone. This is particularly important when several machines empty at nearly the same time or when production is concentrated into one shift.

AO Treatment for Biodegradable Pollutants
After equalization, the recorded process uses an AO biological stage. In an AO system, wastewater passes through an anoxic zone and then an aerobic zone. The arrangement supports the biological conversion of organic pollutants and can contribute to nitrogen control when the recycle, carbon availability, sludge age, and dissolved oxygen are correctly managed.
The aerobic section requires stable air delivery and appropriate biomass concentration. Excessive aeration wastes energy and can affect floc formation, while insufficient aeration may reduce treatment stability. During startup, operators should increase loading gradually, observe sludge color and settling behavior, and track basic indicators such as pH, dissolved oxygen, ammonia, and organic load. ZhongQiao Enlightenment can configure integrated wastewater treatment equipment around project-specific influent data, but biological adjustment still depends on field conditions.

Sedimentation and Sludge Control
The sedimentation stage separates biological solids from the treated water leaving the AO reactor. Reliable separation depends on calm hydraulic conditions, healthy sludge flocs, an appropriate return-sludge rate, and timely removal of excess sludge. Detergent residues can sometimes contribute to foaming or poor settling, so the operator should treat the clarifier as an active process unit rather than a passive tank.
Routine checks should include sludge blanket level, surface scum, carryover, return flow, and the condition of pumps and valves. If solids begin to escape with the effluent, the response should start with process data: review influent shocks, dissolved oxygen, sludge loading, pH, and settling tests before changing several settings at once. A disciplined adjustment sequence makes the cause easier to identify.
Disinfection and Safe Final Handling
Disinfection is the final recorded treatment step for the Hohhot project. Its design should be based on the selected disinfectant, target contact time, residual requirements, and the destination of the treated water. Effective disinfection also depends on upstream solids removal because suspended particles can shield microorganisms and increase chemical demand.
Operators should verify dosing equipment, chemical storage, contact-tank condition, and residual measurements according to the approved operating plan. The specific discharge or reuse standard was not stated in the project record, so it should not be inferred. Compliance decisions must be based on the local permit, verified laboratory results, and the final engineering design.
Operational Lessons from the Case
The Hohhot laundry wastewater treatment case shows the value of a simple, coordinated sequence: equalization absorbs batch variation, AO treatment manages biodegradable pollutants, sedimentation retains biological solids, and disinfection provides a controlled final barrier. The process is compact enough for a 20 m3/d application while still giving operators clear points for measurement and intervention.
For buyers comparing wastewater treatment equipment, the main lesson is to evaluate the entire treatment chain rather than only the reactor tank. Confirm the discharge schedule, wastewater chemistry, tank volumes, aeration capacity, sludge handling method, instrumentation, and access for maintenance. ZhongQiao Enlightenment uses project data to match integrated wastewater treatment equipment to the actual site, helping owners move from a nominal daily capacity to a workable operating plan.