QEQI-booster
Bring settled solids back into the treatment loop.
Basin sweeping and centrifugal filtration have a different role from electronic scale control. Configuration depends on the basin layout and operating conditions.
Confirm the model, pipe measurement basis and installation conditions before selection.
Request a quoteKnow the conditions.
Match the model specifications to the actual pipework. Confirm measurement basis, power supply and access before installation.
| Documented basin-sweeping flow | 11–206 m³/h |
|---|---|
| Documented side-stream flow | 15–252 m³/h |
| Collection vessel | 12 L |
| Separation performance | Particle and test conditions to confirm |
Fit the system, not just the pipe.
- 01
Assess basin dimensions, dead zones, solids and available hydraulic capacity.
- 02
Determine nozzle placement, flow, filtration and discharge as one system.
- 03
Provide safe access for inspection, discharge and maintenance.
A clear scope of treatment.
Do not size a basin-sweeping system from main-pipe flow percentage alone.
Filtration does not replace scale control, chemical management or disinfection where required.
Prepare for an informed decision.
Model-specific technical information
For installation planning, identify the model, pipe dimensions and site requirements. Consult the applicable manual and confirm the configuration before ordering.
QEQI-booster: practical questions
Pipe dimensions, installation and operation: answers for this product.
Explore treatment principlesHow does basin sweeping differ from electronic scale control?
Basin sweeping uses a planned water flow to move settled solids toward collection. Separation and discharge then remove suitable particles from that path. Electronic scale control addresses a different equipment-deposit task. The processes may be assessed together, but their duties and evaluation metrics remain distinct.
How are nozzle layout and flow selected?
Start with basin dimensions, obstacles, dead zones, the collection point and available pump capacity. Nozzle positions and flow paths need to work as one hydraulic arrangement. A fixed percentage of the main circulation flow does not by itself establish a suitable basin-sweeping design.
Can one separation efficiency describe all solids?
Separation depends on particle size, density, loading and hydraulic conditions. Evaluate the actual solids and agreed test conditions instead of applying a single percentage to every application. Sampling location and the method used to measure solids should be defined before testing.
What maintenance access should be reserved?
Provide safe access to nozzles, strainers, the separator and collection vessel. Plan inspection, discharge and disposal around the site's solids loading and operating schedule. Collection capacity is not a promise of a fixed maintenance interval; monitor accumulation to establish a practical routine.
A specification is only the starting point.
A useful configuration connects product ratings to the actual operating environment.
| Assessment area | Site information | Engineering decision |
|---|---|---|
| Pipework & connectivity | Outside / nominal diameter, material, branches and closed electrical loops | Model fit, clearance and signal conditions |
| Hydraulic conditions | Flow, circulation path, pump position and available pressure | Installation location and filtration configuration |
| Water & process | Hardness, suspended solids, temperature and existing treatment | Treatment roles and processes to retain |
| Operation & maintenance | Load profile, cleaning history, inspection and discharge access | Comparable baseline and practical service access |
Electronic scale control, particle separation and water-quality compliance are separate responsibilities. A site may need several coordinated processes. Neither scale control nor filtration universally replaces softening, membrane treatment, disinfection or chemical management.
Related applications
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