
STYRONICS POLYMER FAMILY
Styrenic polymers include:
Polystyrene (PS) – General-purpose plastic used in packaging, disposable containers, and insulation.
Expanded Polystyrene (EPS) – Foam applications (e.g., packaging, food containers).
High-Impact Polystyrene (HIPS) – Toughened PS with rubber additives.
Styrene-Butadiene Rubber (SBR) – Used in tires, footwear, and adhesives.
Acrylonitrile Butadiene Styrene (ABS) – Engineering plastic for automotive parts, electronics.
Styrene-Acrylonitrile (SAN) – Transparent, rigid plastic for bottles and containers.
Styrenic Block Copolymers (SBCs) – Thermoplastic elastomers (e.g., SBS, SEBS) used in adhesives, footwear, and medical devices.
PROCESS METHODS
Free Radical Polymerization: It involves the initiation, propagation, and termination of free radicals.
Bulk Polymerization: Pure styrene + initiator → clear PS (used for optical applications).
Suspension Polymerization: Monomer droplets in water → PS beads (for EPS foam).
Emulsion Polymerization: Latex form → used for SBR rubber and coatings.
Anionic Polymerization: This method uses an anionic initiator (e.g., butyllithium) to initiate the polymerization. Characteristics: Produces polystyrene with a very narrow molecular weight distribution (monodisperse). Applications: Used for specialty polystyrene with high purity and controlled molecular weight.
TYPICAL BULK POLYMERIZATION
Styrene is polymerized in the absence of a solvent or dispersing medium.
Process: Styrene monomer is mixed with a free radical initiator. The mixture is heated to initiate polymerization. The reaction is exothermic, and temperature control is critical. The polymer is cooled and extruded into pellets.
Advantages:
High purity product.
No solvent recovery required.
Disadvantages:
Difficult to control temperature due to exothermic nature.
High viscosity at high conversion rates.
HIGH IMPACT POLYSTYRENE PROCESS
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Typical Industrial Process Flow
Typical Industrial Process Flow
Feed Preparation – Styrene + polybutadiene rubber + initiator (e.g., peroxide).
Pre-polymerization – Partial conversion in a stirred tank (to reduce viscosity).
Plug Flow Reactor – Multi-zone temperature control (e.g., 80°C → 120°C → 160°C).
Devolatilization – Remove unreacted monomer via vacuum extrusion.
Pelletization – Final HIPS pellets for molding/extrusion.
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