| Brand Name: | BLUWAT |
| Model Number: | Blufloc Emulsion |
| MOQ: | 1000kgs |
| Price: | negotiable |
| Delivery Time: | 5-10days |
High-molecular-weight liquid polymer grades for dilute, buoyant DAF float sludge containing fats, fibers, biological solids, or coagulant precipitates, supporting improved thickening, water release, floc integrity, and mechanical dewatering.
DAF float sludge is often dilute, buoyant, and rich in fats, fibers, biological solids, or coagulant precipitates. Its response depends strongly on the upstream coagulant, pH, recycle pressure, and skimming practice.
The dewatering polymer should be selected on the float sludge itself, not only on raw wastewater. A grade that improves flotation may not be the best conditioner for the separated sludge.
Blufloc cationic polyacrylamide emulsion helps consolidate low-density, high-organic solids before thickening or mechanical dewatering.
Medium- to very-high-charge grades can be screened around the actual upstream coagulant, residual charge, DAF chemistry, transfer shear, and final dewatering objective.
Low solids, water-retaining organics, changing residual coagulant, and transfer shear can all change the observed polymer response.
Dilute float sludge may thicken slowly under gravity and deliver unstable feed solids to the mechanical dewatering machine.
Fats, oils, fibers, and biological solids can retain water and produce weak, sticky, or difficult-to-dewater sludge.
Changes in upstream inorganic or organic coagulant dose can shift the residual charge and preferred CPAM grade.
Floc can break during pumping from the DAF unit to the thickener or dewatering machine, reducing capture and water release.
Cationic PAM conditions fine, negatively charged float solids through charge neutralization and polymer bridging. The target is a cohesive but porous floc that survives transfer and releases water.
Cationic sites adsorb onto negatively charged float solids and reduce repulsion between fine color-bearing, biological, oily, fibrous, or precipitated particles.
High-molecular-weight chains connect destabilized particles, creating a larger, cohesive structure for thickening and dewatering.
Properly conditioned floc retains integrity through transfer, thickens more consistently, and releases water during mechanical dewatering.
Compare adjacent grades on the actual DAF float sludge using the same active-mass basis, dilution water, preparation procedure, mixing, temperature, upstream coagulant conditions, and dewatering method.
| Grade | Base | Molecular Weight | Charge | Suggested Screening Role |
|---|---|---|---|---|
| EC 8040 | Oil-based | High | Medium | Candidate when upstream coagulation already supplies substantial positive charge. |
| EC 8050 | Oil-based | High | High | Broad screening grade for DAF float sludge thickening and dewatering. |
| EWC 8060 | Water-based | High | Very high | Candidate for high-organic float sludge in compatible water-based preparation and dosing systems. |
Medium-, high-, and very-high-charge candidates can be screened around different DAF coagulant programs and residual charge.
Pumpable emulsion form supports controlled dosing where float sludge production and solids concentration vary.
Correct conditioning can accelerate free-water separation and produce more stable feed solids before mechanical dewatering.
A well-matched polymer can help the floc withstand transfer pumps between the DAF, thickener, and dewatering equipment.
Adjacent grades can be screened around the complete DAF chemistry, sludge characteristics, and agreed dewatering indicators.
Take sludge samples after the DAF reaches stable operation. Record upstream coagulant and polymer doses, pH, recycle pressure, skimming conditions, and float sludge solids.
Compare adjacent polymers on the separated float sludge at its normal solids concentration using the same active polymer mass basis and preparation conditions.
Assess thickening rate, free-water release, floc openness, filtrate quality, and shear resistance before machine trials.
During scale-up, stabilize upstream pH, coagulant dose, DAF recycle, sludge feed solids, and transfer conditions while changing one polymer variable at a time.
Compare coagulation, flotation, thickening, dewatering throughput, cake quality, polymer use, and final sludge disposal as one operating system.
Start with EC 8050 as a broad DAF float sludge screening grade.
Include EC 8040 when an inorganic or organic upstream coagulant already supplies significant charge neutralization.
Test EWC 8060 for highly organic float sludge or where water-based handling is preferred and the preparation system is compatible.
Neat-emulsion price per kilogram can be misleading when products differ in active content, preparation efficiency, activation, working dose, and equipment throughput.
The comparison should also include thickening rate, machine throughput, cake or underflow quality, filtrate clarity, floc survival, operator adjustment, and downstream disposal cost.
If polymer performance changes with no apparent difference in the float sludge, verify the upstream coagulant pump, pH, DAF recycle pressure, air saturation, skimming practice, feed solids, and dosing-equipment calibration.
Excess residual coagulant can alter or reverse the apparent charge demand, change the preferred polymer charge, and make historical dose comparisons misleading.
Inspect emulsion activation, dilution water, injection, mixing, transfer pumps, thickening conditions, and dewatering-machine settings before concluding that the grade itself is no longer suitable.
Confirm the required commercial grade specification and order documentation before production and shipment.
Shortlist products using representative float sludge under realistic upstream coagulant, pH, temperature, solids, dilution-water chemistry, and transfer shear.
Provide make-down, dilution, activation, dosing, injection, and scale-up guidance for the selected grade.
Review trial data and adjust charge level, dose, addition point, mixing, transfer, thickening, machine settings, or upstream chemical stability.
For thickening and dewatering, test the separated float sludge because its solids concentration, residual coagulant, charge, and water-retention behavior differ from the influent.
Yes. Residual positive charge and coagulant precipitates can materially change polymer demand. Adjacent charge grades should be re-screened when the coagulant program changes.
Often yes. Higher and more stable feed solids can improve dewatering capacity, reduce hydraulic variability, and make polymer control more consistent.
Sometimes, but each duty should be tested independently. The best polymer for wastewater flotation may not provide the best thickening, floc strength, water release, or cake quality on the separated float sludge.
For DAF float sludge thickening and dewatering, Bluwat can screen adjacent PAM emulsion grades, review preparation and dosing conditions, and help define a controlled plant-trial plan using float sludge solids, thickening rate, filtrate quality, cake solids, floc integrity, total chemical cost, and active polymer dose as agreed performance indicators.