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Fire and Explosion Prevention
Storage of Monomers: Monomers such as acrylate (e.g., butyl acrylate, MMA) are flammable and explosive. Storage tanks must be nitrogen-sealed (oxygen content < 0.5%), shielded from light, maintained at a constant temperature below 25°C, and equipped with anti-static devices.
Operational Environment: The reaction workshop must have forced ventilation, use explosion-proof motors/electric equipment, and prohibit open flames.
Toxicity Protection
Monomers such as acrylic acid and styrene are irritating. Personnel must wear gas masks, safety goggles, and chemical-resistant gloves.
Install gas alarms to monitor VOC leakage in real time.
1. Raw Material Quality Control
2. Pre-emulsification Process
3. Polymerization Reaction Control
Parameter | Control Range | Deviation Risk |
---|---|---|
Reaction Temperature | 75-85°C (±1°C) | Too high → Runaway polymerization; too low → Incomplete reaction |
Addition Rate | Pre-emulsion added over 3-5 hours | Too fast → Local overheating and gelling |
Initiator Concentration | 0.3%-0.8% (of total monomer) | Excess → Low molecular weight; insufficient → Low conversion rate |
pH Value | 2.5-4.5 (during reaction) | Affects emulsion stability and particle morphology |
4. Key Steps in Post-Processing
Solid Content and Viscosity
Latex Particle Size
Freeze-Thaw Stability
Exhaust Gas Treatment
Wastewater Treatment
Solid Waste Recovery
Gel Formation: Caused by local overheating or stirring failure → Reinforce stirring torque design and install multi-point temperature monitoring.
Emulsion Breaking and Layering: Improper emulsifier ratio or pH shifts → Optimize HLB value matching in the pre-emulsification phase.
Abnormal Viscosity: Out of control molecular weight → Accurately control chain transfer agent (e.g., DDM) dosage (0.1-0.5%).