| Brand Name: | BLUWAT |
| Model Number: | Blufloc Emulsion |
| MOQ: | 1000kgs |
| Price: | negotiable |
| Delivery Time: | 5-10days |
Bridge separated oil-bearing solids and coagulant floc after demulsification for reliable DAF, settling, or filtration under controlled chemical sequence and mixing.
Oil droplets stabilized by surfactants or fine solids do not behave like normal suspended mineral particles. A flocculant cannot reliably replace the demulsification step that destabilizes the oil-water interface and releases the dispersed phase.
Once destabilized, oil-bearing solids and coagulant floc can be aggregated by APAM for DAF, settling, or filtration. Excessive shear after polymer addition can break floc and re-disperse the separated phase.
Blufloc anionic PAM emulsion is applied after demulsification or coagulation to bridge separated oil-bearing solids, precipitate, and coagulant floc into larger aggregates.
Liquid grades support continuous preparation and dosing for flotation or settling. Final selection depends on the destabilized solids, oil type, pH, temperature, shear, separation equipment, and required treated-water quality.
Successful treatment requires the correct chemical sequence, representative testing, and enough floc strength for the selected DAF, clarifier, or filtration process.
Surfactants and interfacial films can keep oil droplets dispersed until a suitable demulsifier or coagulant destabilizes them.
After coagulation, very small oil-coated particles and precipitate may still require long-chain bridging for efficient separation.
Feedstock, cleaning chemicals, temperature, salts, pH, and suspended solids can change demulsification and polymer demand.
Poor chemical order, insufficient bubble contact, low settling density, or excessive shear can carry oil into treated water.
After the emulsion is destabilized and droplets or solids have suitable adsorption sites, very-high-molecular-weight APAM bridges them into separable floc. DAF floc must attach effectively to bubbles, while settling floc must develop enough density to sink.
Optimize demulsifier, coagulant, pH, temperature, and mixing until the dispersed phase becomes available for separation.
Distribute the prepared polymer rapidly, then reduce shear so the long chains can bridge oil-bearing solids and precipitate.
Match floc size, strength, bubble attachment, and density to the actual separation device and verify residual oil analytically.
Stabilize the upstream demulsification or coagulation program before comparing APAM candidates at equal active polymer mass under representative oil, solids, pH, temperature, shear, and separation conditions.
| Grade | Base | Molecular Weight | Charge | Suggested Screening Role |
|---|---|---|---|---|
| EWA 7520 | Water-based | Very High | Medium anionic | Water-based candidate for post-coagulation separation |
| EA 6520 | Oil-based | Very High | High anionic | High-anionic comparator for difficult fine solids |
The product pages classify the cationic EC and EWC series as high molecular weight and the anionic EA and EWA grades as very high molecular weight. Confirm exact commercial specification limits, active content, viscosity, shelf life, and preparation instructions on the current grade-specific TDS and order specification.
Measure free, dispersed, and emulsified oil together with TSS, pH, temperature, salts, surfactants, and flow variation.
Establish the demulsifier, coagulant, pH, dose, addition point, and mixing conditions before APAM screening.
Use rapid initial distribution followed by gentle floc growth to avoid breaking the separated phase or formed aggregates.
Evaluate oil in water, TSS, DAF or settling behavior, sludge volume, sludge quality, dewatering, and treated-water compliance.
Preserve the successful order, dilution, addition points, contact time, and shear conditions when transferring the trial to the plant.
EWA 7520 is a practical water-based candidate for post-coagulation screening. EA 6520 provides higher anionic charge and strong bridging for comparison when difficult fine solids remain after destabilization.
Select the grade using the actual oil type, destabilized particle surface, residual coagulant, salts, pH, temperature, DAF bubble conditions, settling density, filtration duty, shear history, and treated-water target.
Neat-emulsion price per kilogram can be misleading. Compare active polymer mass with preparation efficiency, dose, equipment throughput, treated-water quality, sludge or underflow properties, dewatering, and downstream disposal cost.
If no separate phase forms before APAM addition, revisit the demulsifier, coagulant, pH, temperature, dose, addition sequence, and mixing. APAM cannot reliably replace the step that breaks a stable oil-water emulsion.
If floc forms but oil carryover remains high, examine DAF recycle, bubble size and attachment, hydraulic loading, settling density, short-circuiting, and downstream shear before increasing polymer dose.
Keep the package sealed in a cool, dry, ventilated area. Protect it from direct sunlight, freezing, excessive heat, water ingress, and physical damage.
Follow the grade-specific TDS and SDS for shelf life, handling limits, and transport classification. Polymer spills can make floors extremely slippery and should be contained and cleaned promptly.
For post-demulsification oily wastewater clarification, Bluwat can screen adjacent PAM emulsion grades, review the complete chemical sequence and dosing conditions, and help define a plant-trial plan using agreed performance and operating-cost indicators.
Confirm the required grade specification, order documentation, packaging, handling, and destination-market requirements before production and shipment.
Shortlist candidates with real samples under realistic oil type, pH, temperature, solids, water chemistry, coagulant residual, mixing, and shear.
Supply clear make-down, dilution, dosing, addition-point, chemical-sequence, and scale-up recommendations for the selected grade.
Adjust charge level, dose, addition point, mixing, or separation conditions using oil, TSS, floc, sludge, throughput, and cost data.
Its main role is flocculation after destabilization. Stable emulsions generally require a dedicated demulsifier or coagulant step before APAM is used for bridging.
Yes, when the upstream emulsion has been destabilized and the floc is formed and mixed to support bubble attachment without excessive shear.
Oil content, solids density, air-to-solids ratio, bubble contact, hydraulic conditions, and separation design determine whether the aggregate floats or sinks.
Yes. Visual clarity and TSS do not fully describe residual oil. Use the required analytical method and confirm treated-water quality against the applicable discharge or reuse target.
Screen EWA 7520 and EA 6520 only after the demulsifier, coagulant, pH, and mixing program has been stabilized. Select the grade, active dose, dilution, addition point, shear, and separation settings using oil and grease, TSS, DAF or settling performance, sludge properties, throughput, and total chemical cost.