| Brand Name: | BLUWAT |
| Model Number: | Blufloc Emulsion |
| MOQ: | 1000kgs |
| Price: | negotiable |
| Delivery Time: | 5-10days |
Accelerate ultrafine mineral settling, improve thickener overflow clarity, and support process-water recovery with oil-based EA 6520 and water-based EWA 7520 screening options.
Tailings contain a broad particle-size distribution. Ultrafine clay or altered minerals can settle slowly even when coarse solids drop rapidly. Recycled process water, hardness, salinity, and residual flotation reagents can also shift polymer response.
A successful thickener polymer must deliver rapid aggregate growth, clear overflow, and a controllable underflow without creating fragile floc that breaks in the feedwell or rake zone.
High-molecular-weight anionic polyacrylamide emulsion accelerates mineral tailings settling and supports process-water recovery.
Blufloc EA 6520 and EWA 7520 are screened by ore mineralogy, clay content, water chemistry, solids loading, and thickener duty.
Particle-size distribution, mineral surfaces, dissolved ions, flotation reagents, feedwell energy, and rake-zone conditions all affect settling, clarification, and underflow control.
Clay and altered mineral fines may remain suspended long after the coarse fraction has settled.
Fine solids in the overflow can limit process-water reuse and increase downstream treatment demand.
Changes in mineralogy, clay content, grind, and recycled-water chemistry can alter polymer adsorption.
Excessive energy can damage growing floc, while poor distribution can leave polymer and solids unmixed.
Very-high-molecular-weight APAM chains adsorb across mineral particles and form large aggregates. Anionic charge influences chain extension and interaction with mineral surfaces and dissolved ions. Feedwell energy must distribute the polymer without destroying the growing floc.
Activate and dilute the selected emulsion, then distribute it evenly across the incoming tailings stream.
Long APAM chains adsorb onto multiple mineral particles and build larger, faster-settling aggregates.
Controlled feedwell energy preserves floc so clear overflow and stable mud-line compaction can develop.
Compare candidates at equal active polymer mass using fresh tailings at operating solids, temperature, water chemistry, and feedwell-like mixing conditions.
| Grade | Base | Molecular Weight | Charge | Suggested Screening Role |
|---|---|---|---|---|
| EA 6520 | Oil-based | Very High | High anionic | Primary candidate for demanding tailings thickening |
| EWA 7520 | Water-based | Very High | Medium anionic | Water-based comparator for moderate charge and automatic dosing |
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.
Use fresh tailings at operating solids concentration and temperature rather than an aged or diluted convenience sample.
Document ore blend, particle size, clay content, hardness, salinity, recycled water, and residual flotation reagents.
Prepare each carrier correctly and apply repeatable, feedwell-like distribution without excessive floc damage.
Record settling rate, supernatant clarity, mud-line compaction, underflow behavior, and floc strength.
Validate the preferred candidate under realistic feed rate and hydraulic loading before changing the full-scale program.
EA 6520 is the core high-anionic screen for difficult mineral fines. EWA 7520 can perform well where medium anionic charge and water-based handling suit the mineral system. Ore mineralogy, clay content, process water, reagents, and thickener duty matter more than the product label alone.
Neat-emulsion price per kilogram can be misleading. Compare on active polymer mass and include preparation efficiency, thickener throughput, overflow quality, underflow control, and downstream handling cost.
The polymer may be creating mixed floc sizes, or fine solids may be bypassing effective contact in the feedwell. Check dilution, injection distribution, feedwell energy, and dose before simply increasing molecular-weight demand.
Also separate polymer limitations from hydraulic short-circuiting, ore-blend changes, recycled-water chemistry, air entrainment, and excessive floc breakage in transfer or rake zones.
Keep the package sealed in a cool, dry, ventilated area. Protect it from direct sunlight, freezing, and excessive heat.
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 mineral tailings thickening and water recovery, Bluwat can screen adjacent PAM emulsion grades, review preparation and feedwell dosing conditions, and help define a plant-trial plan using agreed settling, overflow, underflow, and cost indicators.
Confirm the required grade specification and order documentation before production and shipment.
Shortlist products under realistic solids, temperature, mineralogy, water chemistry, reagents, and shear.
Supply clear make-down, dilution, dosing, feedwell, and scale-up recommendations for the selected grade.
Adjust charge level, dose, addition point, dilution, or mixing conditions using plant-trial data.
It is commonly compared as polymer mass per ton of dry solids. The optimum must be determined with representative tailings and verified in the operating thickener.
No. Mineralogy, clay content, particle size, water chemistry, flotation reagents, solids loading, and shear can all change adsorption and settling performance.
Emulsion can support rapid continuous make-down and liquid dosing. Performance, activity, site handling, logistics, equipment requirements, and total cost should still be compared.
Better settling and overflow clarity can support water recovery, subject to thickener capacity, process-water quality requirements, and stable downstream operation.
Screen EA 6520 and EWA 7520 with fresh representative tailings, controlled carrier-specific preparation, and feedwell-like mixing. Confirm the preferred grade using settling rate, overflow clarity, underflow density, floc strength, operating stability, and total cost.