Cationic Polyacrylamide Emulsion

Cationic Polyacrylamide Emulsion

Details
Cationic Polyacrylamide Emulsion is synthesized via inverse emulsion polymerization, presenting as a low-viscosity, water-in-oil liquid polymer. Upon contact with dilution water under high-shear mixing, the emulsion inverts within ≤ 15 minutes, releasing high-molecular-weight cationic polymer chains into aqueous solution.
Category
Polyacrylamide Emulsion
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Description
Technical Parameters

Product Overview

 

 

Cationic Polyacrylamide Emulsion is synthesized via inverse emulsion polymerization, presenting as a low-viscosity, water-in-oil liquid polymer. Upon contact with dilution water under high-shear mixing, the emulsion inverts within ≤ 15 minutes, releasing high-molecular-weight cationic polymer chains into aqueous solution. Engineered for mechanical solid-liquid separation, it neutralizes negatively charged colloidal structures and bridges suspended solids to form dense, shear-resistant flocs. It eliminates dust hazards and prevents undissolved agglomerates ("fish-eyes") in automated dosing systems.

 

Cationic Charge Density & Polymer Characteristics

 

 

Charge Density: Ranging from 10% to 80% molar substitution, introduced via copolymerization of acrylamide with cationic functional monomers (e.g., ADAME-Q, DADMAC). Controls electrostatic attraction intensity.


Molecular Weight: Ultra-high molecular weight range (10 to 18 Million Daltons), verified via dilute solution capillary viscometry. Provides physical chain length for simultaneous multi-particle bridging.

 

Charge Neutralization & Floc Formation

 

 

Municipal and industrial sludges carry a net negative zeta potential driven by absorbed organic acids, extracellular polymeric substances (EPS), and biological cell debris.


Electrostatic Patching: Dissolved cationic segments adsorb onto negative particle sites, neutralizing surface charges and collapsing the electrical double layer.


Polymer Bridging: Extended polymer chains anchor onto multiple suspended particles concurrently, building structured 3D flocs.


Water Release: Robust flocs encapsulate free interstitial water, permitting rapid drainage through filter belts or screening meshes under mechanical compression without structural shear collapse.

 

Technical Specifications

 

 

Test Parameter

Specification Range

Test Method / Standard

Appearance

Milky white to light yellow viscous liquid

Visual Inspection

Solid Content (%)

50.0 ± 2.0%

Gravimetric Drying (105°C, 2 hrs)

Cationic Degree

10% – 80% (Customizable)

Colloidal Titration

Molecular Weight

10 – 18 Million Daltons

Intrinsic Viscosity Measurement

Brookfield Viscosity (cps)

500 – 2500 (25°C, Spindle 3, 60 rpm)

Brookfield LV Viscometer

Inversion Time (min)

≤ 15 minutes

Standard Jar Test Apparatus

Residual Monomer (%)

< 0.05%

HPLC Analysis

pH Value (0.5% Aqueous)

5.0 – 8.0

Glass Electrode pH Meter

 

Grade Selection by Sludge Characteristics

 

 

Sludge Origin

Sludge Zeta Potential

Recommended Charge Density

Target Molecular Weight

Municipal Biological (WAS)

-20 mV to -40 mV

Medium (30% – 50%)

Ultra-High (>15 Million)

Paper Mill Sludge (Cellulosic)

-10 mV to -25 mV

Low to Medium (20% – 35%)

High (12 – 15 Million)

Textile / Dyeing Effluent

-30 mV to -50 mV

High (60% – 80%)

Medium-High (10 – 14 Million)

Oil & Gas Produced Water Sludge

-40 mV to -60 mV

High (70% – 80%)

High (14 – 16 Million)

 

Dilution, Maturation & Dosing Requirements

 

 

Primary Injection: Invert neat emulsion at 0.5% to 1.0% concentration utilizing an inline mechanical static mixer or high-shear atomization nozzle.


Aging Duration: Retain primary solution in a maturation vessel for 15 to 30 minutes to facilitate complete polymer uncoiling.


Secondary Dilution: Dilute aged solution down to 0.05% to 0.1% working concentration immediately before entering the sludge line.


Shear Protection: Exclude centrifugal pumps downstream of the aging tank; deploy low-shear progressive cavity (screw) pumps or peristaltic pumps to prevent mechanical degradation.

 

Dewatering Equipment Compatibility

 

 

Decanter Centrifuges: Demands high charge density and rapid kinetic adsorption to handle high-G-force mechanical shear zones.


Belt Filter Presses (BFP): Requires medium molecular weight polymers yielding large, permeable flocs that release free water instantly in gravity drainage sections.


Multi-Disc Screw Presses: Requires resilient, uniform flocs capable of sustaining low-shear continuous compaction without blinding filtration micro-gaps.

 

Storage Stability & Quality Control

 

 

Thermal Boundaries: Maintain storage temperatures between 5°C and 35°C. Prevent freezing (which breaks the oil-continuous emulsion matrix) and direct UV exposure.


Agitation Protocol: Periodic low-speed gentle mixing of bulk storage tanks every 7 to 10 days prevents minor creaming or phase separation.


Factory Quality Verification: Every production lot undergoes laboratory testing for active solid content, Brookfield viscosity, and residual acrylamide monomer prior to release.

 

Packaging, Shelf Life & Supply

 

 

Packaging Configurations 25 kg / 200 kg HDPE drums
1,000 kg IBC totes
Bulk ISO tank containers for high-throughput municipal applications
Shelf Life 6 months from production date when stored in unopened original containers under specified warehouse environments.

 

FAQ

 

 

Q: How do I determine whether my process requires an emulsion or a dry powder polymer?

A: Emulsion polymers invert faster (≤ 15 minutes), dissolve without dust generation, and fit compact automated liquid skids. Dry powders provide higher absolute active content per kilogram but demand multi-compartment maturation systems and longer wetting times (45–60 minutes). Emulsions are specified where continuous dosing, footprint constraints, or rapid dissolution kinetics are prioritized.

Q: What causes polymer phase separation or oil creaming inside IBC totes during storage?

A: Phase separation typically stems from thermal cycling (severe temperature swings) or static storage exceeding 6 months without agitation. To re-homogenize minor separation, circulate the container using a pneumatic diaphragm pump or low-shear mechanical stirring prior to use.

Q: Why are my flocs breaking down inside the sludge feed pipe prior to the dewatering unit?

A: Shear breakdown is generally caused by excessive turbulence downstream of the polymer injection point. Eliminate centrifugal pumps, sharp pipe bends, or aggressive static mixers after secondary dilution. Introduce the polymer as close to the dewatering machine inlet as possible via a progressive cavity pump.

Q: How can I manage cationic charge matching when influent sludge characteristics fluctuate daily?

A: When seasonal or industrial load variations shift the sludge zeta potential, transitioning to a medium-charge (40%) general-purpose grade or installing an online streaming current detector (SCD) feedback loop helps dynamically adjust dosing rates.

Q: What is the standard residual monomer compliance threshold for industrial and municipal discharge?

A: Our CPAM emulsions maintain residual acrylamide monomer limits strictly below 0.05%, complying with environmental regulatory thresholds for treated wastewater effluents and digested biosolids land application.

Q: Can you formulate custom molecular weights or charge densities for specialized industrial effluent?

A: Yes. As a primary manufacturer, we synthesize custom copolymer ratios of acrylamide and cationic functional monomers driven by jar-test performance data obtained from your specific industrial waste stream.

 

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