| Brand Name: | BLUWAT |
| Model Number: | Blufloc Emulsion |
| MOQ: | 1000kgs |
| Price: | negotiable |
| Delivery Time: | 5-10days |
Accelerate iron ore tailings settling and clarify thickener overflow with oil-based EA 6520 and water-based EWA 7520 screening options.
Iron ore tailings can contain dense iron minerals alongside slow-settling silica and clay. The coarse fraction may settle quickly while ultrafines remain in the thickener overflow.
The polymer must capture the slow fraction without creating oversized, fragile floc or interfering with upstream beneficiation and downstream water reuse.
Blufloc anionic PAM emulsion accelerates sedimentation of iron ore tailings containing hematite, magnetite, silica, and clay fines.
Very-high-molecular-weight grades support overflow clarification, thickener control, and process-water recovery under mineral- and site-specific operating conditions.
Particle-size distribution, silica and clay content, feed solids, hardness, pH, and hydraulic conditions can change fine-particle capture, compaction, and thickener stability.
Low-density ultrafines may remain dispersed after dense hematite and magnetite particles have settled.
High solids and a shifting particle-size distribution can alter polymer demand and feedwell distribution.
Hardness, pH, conductivity, and recycled-water chemistry influence adsorption and polymer-chain behavior.
Excessive compaction or fragile oversized floc can increase rake loading or make underflow difficult to pump.
Very-high-molecular-weight APAM adsorbs across mineral surfaces and bridges dispersed silica, clay, and iron-mineral fines into larger aggregates. Anionic charge affects chain extension and adsorption, while mixing must distribute polymer without destroying growing floc.
Activate and dilute the emulsion, then distribute it evenly under feedwell-representative mixing.
Long APAM chains connect slow-settling silica, clay, and iron-mineral fines into settleable floc.
Preserve floc through the thickener while balancing overflow clarity, compaction, torque, and pumpability.
Compare candidates at equal active polymer mass using representative iron ore tailings and the actual pH, hardness, conductivity, particle-size distribution, and operating temperature.
| Grade | Base | Molecular Weight | Charge | Suggested Screening Role |
|---|---|---|---|---|
| EA 6520 | Oil-based | Very High | High anionic | Primary candidate for clay- and silica-rich tailings |
| EWA 7520 | Water-based | Very High | Medium anionic | Comparator for water-based dosing and different adsorption behavior |
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.
Record particle size, solids, hematite and magnetite content, silica, clay, pH, hardness, conductivity, and temperature.
Screen actual tailings at realistic concentration and temperature before selective settling changes the sample.
Control polymer dilution, addition point, distribution energy, and shear to represent full-scale feedwell conditions.
Assess initial settling, final mud-line compaction, overflow clarity, floc strength, and underflow pumpability.
Check rake torque, underflow density, pump response, overflow reuse, and polymer demand during representative operation.
EA 6520 is the strong high-anionic starting point for clay- and silica-rich iron ore tailings. EWA 7520 should also be tested because medium anionic charge can adsorb differently on iron-mineral and clay surfaces.
Confirm grade and dose with the actual hematite or magnetite tailings, recycled water, particle-size distribution, solids concentration, and thickener duty.
Neat-emulsion price per kilogram can be misleading. Compare active polymer mass and include preparation efficiency, dose, throughput, overflow quality, underflow behavior, pumping, water reuse, and downstream disposal cost.
If underflow becomes difficult to pump, review excessive compaction, polymer dose, dilution, addition point, mud bed, rake settings, and underflow withdrawal rate.
If silica or clay fines remain in overflow while coarse iron minerals settle rapidly, optimize charge level, dilution, distribution, and mixing before simply increasing dose or molecular-weight demand.
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 iron ore tailings sedimentation and water clarification, Bluwat can screen adjacent PAM emulsion grades, review preparation and dosing conditions, and help define a plant-trial plan using agreed settling, thickener, water, and cost indicators.
Confirm the required grade specification and order documentation before production and shipment.
Shortlist products under realistic pH, temperature, solids, mineralogy, hardness, conductivity, and shear.
Supply clear make-down, dilution, dosing, addition-point, mixing, and scale-up recommendations.
Adjust charge level, dose, addition point, dilution, or mixing using thickener and process-water data.
Dense coarse hematite or magnetite particles settle quickly, but fine silica and clay can remain dispersed unless polymer grade, dilution, distribution, and mixing capture the slow fraction.
Yes, when practical. Anionic degree and carrier system can affect adsorption, preparation, dosing-system compatibility, floc structure, and thickener response.
Better flocculation can improve thickener behavior, but underflow density, mud-bed depth, rake settings, feed rate, and withdrawal conditions also control torque.
Mineralogy, grind size, clay, surface chemistry, pH, hardness, and recycled-water quality can change polymer response, so each ore and water regime requires representative testing.
Screen EA 6520 and EWA 7520 with representative hematite or magnetite tailings, controlled carrier-specific preparation, actual process water, realistic solids concentration, and feedwell-like mixing. Confirm the preferred grade using settling rate, overflow turbidity, underflow density, rake torque, pumpability, water reuse, and total operating cost.