Yixing Bluwat Chemicals Co., Ltd.
| Product Name | Cationic Polyacrylamide Emulsion |
| Molecular Weight | High |
| Charge Degree | Medium to Ultra-High |
| Main Functions | Flocculation, Sludge Conditioning, Dewatering and Clarification |
| Delivery Time | 5-10days |
| Chemical Type | Cationic Polyacrylamide Copolymer |
| Available Formulations | Oil-Based Emulsion and Water-Based Emulsion |
| Physical Form | Liquid Emulsion |
| Packaging Details | 30kgs, 50kgs, 250kgs, 1250kgs drums |
| Product Category | Water-Soluble Polymer Flocculant |
| Appearance | Milky White or Off-White Emulsion |
| Abbreviation | CPAM Emulsion |
| Model Number | Blufloc Emulsion |
| Brand Name | BLUWAT |
| Certification | ISO9001 |
| Place of Origin | China |
View Detail Information
Explore similar products
Chemicals Polyacrylamide Polyelectrolyte Flocculants Sewage Treatment Plant
PAM Chemical Anionic Polyacrylamide Powder Wastewater Treatment High Effictive
Wastewater Polymers Treatment Polyelectrolyte Flocculant 9003-05-8 Sludge
Anionic PAM Emulsion for Oily Wastewater Clarification with Very High Molecular
Product Specification
| Product Name | Cationic Polyacrylamide Emulsion | Molecular Weight | High |
| Charge Degree | Medium to Ultra-High | Main Functions | Flocculation, Sludge Conditioning, Dewatering and Clarification |
| Delivery Time | 5-10days | Chemical Type | Cationic Polyacrylamide Copolymer |
| Available Formulations | Oil-Based Emulsion and Water-Based Emulsion | Physical Form | Liquid Emulsion |
| Packaging Details | 30kgs, 50kgs, 250kgs, 1250kgs drums | Product Category | Water-Soluble Polymer Flocculant |
| Appearance | Milky White or Off-White Emulsion | Abbreviation | CPAM Emulsion |
| Model Number | Blufloc Emulsion | Brand Name | BLUWAT |
| Certification | ISO9001 | Place of Origin | China |
| High Light | cationic polyacrylamide emulsion refinery sludge ，polyelectrolyte flocculant oily sludge dewatering ，polyacrylamide emulsion for refinery wastewater | ||
High-charge liquid polymer grades for consolidating fine solids after effective oil-water destabilization, supporting cleaner separated water, stronger floc, and more reliable mechanical dewatering.
Oily sludge can contain emulsified oil, mineral fines, corrosion solids, biological material, and treatment-chemical residues. Polymer alone cannot reliably break a stable emulsion, and direct overdosing can trap oil and water in a difficult gel.
The treatment sequence normally requires upstream demulsification or coagulation, followed by pH control and polymer conditioning. The correct CPAM grade must be evaluated in that complete sequence.
Cationic polyacrylamide emulsion is applied after appropriate oil-water destabilization to consolidate fine solids and improve mechanical dewatering.
Blufloc high-charge grades are screened with the actual demulsifier, coagulant, pH, temperature, mixing, and hydrocarbon conditions.
Oil type, solids composition, temperature, emulsion stability, demulsifier residuals, coagulant dose, pH, and shear can all change polymer demand and phase-separation performance.
Persistent emulsions resist simple flocculation and must be destabilized before CPAM can condition the separated solids.
Changing ratios of hydrocarbons, mineral fines, corrosion products, and biological solids alter charge demand.
Demulsifier and coagulant residuals can consume polymer or shift the apparent optimum cationic charge.
Incorrect chemistry, dose, or mixing can create poor cake release, trapped water, or excess oil in the separated phase.
After the emulsion is destabilized, cationic PAM neutralizes and bridges dispersed solids and organic-rich particles. The objective is to consolidate the separated phase without re-emulsifying oil or creating excessive viscosity.
A suitable demulsifier or coagulation step first weakens the stable oil-water interface and separates the phases.
Cationic sites adsorb onto dispersed fines and organic-rich particles while high-molecular-weight chains build larger floc.
Controlled conditioning forms cohesive, drainable solids for the selected centrifuge, press, or thickening equipment.
Compare candidates with the actual demulsifier and coagulant program, using the same active-polymer basis, pH, temperature, solids, preparation method, chemical order, mixing intensity, and separation time.
| Grade | Base | Molecular Weight | Charge | Suggested Screening Role |
|---|---|---|---|---|
| EC 8050 | Oil-based | High | High | Baseline screen after effective demulsification. |
| EC 8060 | Oil-based | High | Very high | Candidate for higher organic and fine-solids demand. |
| EC 8080 | Oil-based | High | Ultra | Special option when testing confirms that charge demand remains exceptionally high. |
Adjacent high-, very-high-, and ultra-charge grades support oily, organic-rich, and fine-solids applications.
Pumpable liquid polymer supports controlled dosing after the emulsion-breaking and pH-control stages.
Correct conditioning can consolidate separated fines, support clearer water, and improve mechanical dewatering.
Grade screening considers the actual demulsifier, coagulant, pH, temperature, chemical order, and realistic shear.
Factory documentation, industrial packaging, and export coordination support refinery treatment programs.
Measure or record free oil, emulsified oil, solids, pH, temperature, hydrocarbon composition, and current treatment chemicals before selecting polymer.
Optimize the demulsifier or coagulant step before CPAM screening. Do not use cationic PAM as a substitute for emulsion breaking.
Adjust pH as required by the treatment sequence, then add prepared polymer under controlled mixing that reflects the actual plant.
Assess phase separation, floc strength, water clarity, oil carryover, free-water release, cake behavior, and response on the intended equipment.
Maintain chemical order, preparation conditions, realistic shear, temperature, and separation time while increasing trial scale and optimizing total treatment cost.
Begin with EC 8050 and EC 8060 after the upstream emulsion-breaking step has been optimized.
Include EC 8080 only when controlled tests show a genuinely higher charge demand that is not caused by poor destabilization.
Confirm carrier compatibility, preparation equipment, materials of construction, and the site's hydrocarbon-handling rules.
Neat-emulsion price per kilogram can be misleading when products differ in active content, preparation efficiency, activation, dose, and equipment throughput.
The evaluation should also include separated-water oil and TSS, cake or underflow quality, machine capacity, operator adjustment, sludge handling, hydrocarbon recovery, and downstream disposal cost.
Poor separation after polymer addition often indicates that the emulsion was not properly destabilized. Recheck demulsifier selection, dose, pH, temperature, and chemical order before increasing CPAM.
Polymer overdosing can create excessive viscosity or a sticky gel that traps both oil and water, weakens phase separation, and causes poor cake release.
Also inspect feed consistency, polymer activation, dilution water, injection point, mixing intensity, dosing calibration, transfer shear, separation time, and dewatering-machine settings.
Confirm the required commercial grade specification and order documentation before production and shipment.
Shortlist products using actual sludge under realistic demulsifier, coagulant, pH, temperature, oil, solids, water chemistry, chemical order, and shear conditions.
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, separation time, or machine settings.
Generally no. CPAM conditions solids after destabilization; a stable oil-water emulsion often needs a dedicated demulsifier or coagulation step first.
Adding polymer too early can trap oil and water, consume polymer before the emulsion is destabilized, or create an excessively viscous and difficult-to-dewater phase.
Yes, but the test should reproduce the real temperature, chemical order, mixing intensity, separation time, sludge concentration, and dewatering objective as closely as practical.
Use the current grade-specific SDS and TDS, follow the refinery's hydrocarbon-handling procedures, and confirm carrier compatibility, storage, transport, and materials of construction before use.
For refinery and oily-sludge conditioning, Bluwat can screen adjacent PAM emulsion grades with the actual demulsifier and coagulant program, review preparation and dosing conditions, and help define a controlled plant trial using separated-water oil, TSS, cake or sludge solids, polymer use, dewatering response, and total treatment cost as agreed performance indicators.
Company Details
Business Type:
Manufacturer,Exporter
Year Established:
2004
Total Annual:
20000000-30000000
Employee Number:
300~500
Ecer Certification：
Verified Supplier
Bluwat Chemicals is a professional supplier of water treatment chemicals in China. We provide our customers with both traditional and innovative products to ensure optimum control in a wide variety of applications, which include treatment of drinking water, wastewater, pro... Bluwat Chemicals is a professional supplier of water treatment chemicals in China. We provide our customers with both traditional and innovative products to ensure optimum control in a wide variety of applications, which include treatment of drinking water, wastewater, pro...
Get in touch with us
Leave a Message, we will call you back quickly!