manufacture of styrene-acrylonitrile copolymers,
San Plastic Raw Material, SAN prodiction, SAN Raw Material,
The process comprises: (a) the introduction, into a reactor, [lacuna] a reaction mixture comprising all the water, acrylonitrile, initiator or initiators, chain-transfer agent or agents and suspending agent or agents and optionally a predetermined fraction of the total amount of the styrene; (b) stirring the reaction mixture and increasing the temperature of this reaction mixture to 60 °C and then to 120 °C; (c) when the temperature of the reaction mixture has reached 60 °C or 120 °C, the addition of the remaining amount of styrene, so as to keep constant the styrene monomer/acrylonitrile monomer ratio in the reaction mixture throughout the duration of the addition; (d) raising the temperature of the reaction mixture to 140 °C and the maintenance at this temperature for a sufficient duration to bring the copolymerization to completion; and (e) cooling the reaction mixture and the recovery of the styrene/acrylonitrile copolymer. Application to the manufacture of SAN copolymers having a level of acrylonitrile of at least 40 % by weight.
CAS Number | 100-42-5 |
EINECS No. | 202-851-5 |
H.S. Code | 2902.50 |
Chemical formula | H2C=C6H5CH |
Chemical Properties | |
Melting point | -30-31 C |
Boling point | 145-146 C |
Specific gravity | 0.91 |
Solubility in water | < 1% |
Vapour density | 3.60 |
Cinnamene; Cinnamenol; Diarex HF 77; Ethenylbenzene; NCI-C02200;Phenethylene; Phenylethene; Phenylethylene; Phenylethylene, inhibited; Stirolo(Italian); Styreen (Dutch); Styrene (CZECH); Styrene Monomer (ACGIH); StyreneMonomer, Stabilized (DOT); Styrol (German); Styrole; Styrolene; Styron; Styropor; Vinylbenzen (CZECH); Vinylbenzene; Vinylbenzol.
Property | Data | Unit |
Bases | A level≥99.5%;B level≥99.0%. | - |
Appearance | colorless transparent oily liquid | - |
Melting point | -30.6 | ℃ |
Boiling point | 146 | ℃ |
Relative density | 0.91 | Water=1 |
Relative vapor density | 3.6 | Air=1 |
Saturated vapor pressure | 1.33(30.8℃) | kPa |
Heat of combustion | 4376.9 | kJ/mol |
Critical temperature | 369 | ℃ |
Critical pressure | 3.81 | MPa |
Octanol/water partition coefficients | 3.2 | - |
Flash point | 34.4 | ℃ |
Ignition temperature | 490 | ℃ |
Upper explosive limit | 6.1 | %(V/V) |
Lower explosive limit | 1.1 | %(V/V) |
Solubleness | Insoluble in water, soluble in alcoho and most organic solvents. | |
Main application | Used for manufacturing polystyrene, synthetic rubber, ion-exchange resin ,etc. |
Packaging Detai: Packed in 220kg/drum,17 600kgs/20’GP
ISO TANK 21.5MT
1000kg/drum, Flexibag, ISO tanks or according to customer`s request.
Used in the manufacture of rubbers, plastics, and polymers.
a) Production of: expandable polystyrene (EPS);
b) Production of polystyrene (HIPS) and GPPS;
c) Production of styrenic co-polymers;
d) Production of unsaturated polyester resins;
e) Production of styrene-butadiene rubber;
f) Production of styrene-butadiene latex;
g) Production of styrene isoprene co-polymers;
h) Production of styrene based polymeric dispersions;
i) Production of filled polyols. Styrene is mainly used as a monomer for the manufacture of polymers (such as polystyrene, or certain rubber and latex)