Heat-proof impact-resistant thermoplastic resin continuous preparation method
A thermoplastic resin and heat-resistant technology, which is applied in the field of continuous preparation of polystyrene thermoplastic resin polymers, can solve the problems of the complexity of the process flow, the particularity of the toughening agent and the low production efficiency, and achieves improved production effect and better production efficiency. The effect of technical effects
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Embodiment 1
[0025] The two reactors are both in the form of screw + draft tube stirring, with volumes of 11 liters and 16.5 liters respectively.
[0026] Semi-continuous startup phase:
[0027] The batching composition comprises the following components in weight percentage: St 95%, ethylbenzene 5%, initiator 0.013%. 11.5 kg of mixed material was quickly poured into the second reactor, stirred and polymerized at 105°C, and 7.5 kg of mixed material was injected into the first kettle after 2 hours, stirred and polymerized at 90°C for 3 hours.
[0028] Double kettle continuous stage:
[0029]The feed composition of the first kettle comprises the following components in weight percentage: 8.8% of PB, 83.8% of St, 2.36% of MA, 5% of EB, 0.0286% of BPO. It is 560rpm; the second tank feed composition comprises the following components in weight percentage: MA 10.7%, St 82.3%, EB 5%, BPO 0.0715%, antioxidant "264" 0.396%, and the supplementary speed is 1600 grams / hour , the reaction temperatur...
Embodiment 2
[0031] Semi-continuous startup phase:
[0032] Take the same way as in Example 1.
[0033] Double kettle continuous stage:
[0034] The feed composition of the first kettle comprises the following components in weight percentage: 8.83% of PB, 75.0% of St, 2.37% of MA, 15.0% of EB, 0.0238% of BPO. It is 500 rpm; the second tank feed composition comprises the following components in weight percentage: MA 10.7%, St 74.3%, EB 15%, BPO0.0596%, antioxidant "1076" 0.33%, supplementary speed is 1810 grams / hour, the reaction temperature is 88°C, and the stirring speed is 85 rpm. Devolatilization and sample performance measurement are the same as in Example 1. The properties of the obtained resin are shown in Table 1.
Embodiment 3
[0036] Semi-continuous startup phase:
[0037] Take the same way as in Example 1.
[0038] Double kettle continuous stage:
[0039] The feed composition of the first kettle comprises the following components in weight percent: 7.03% of PB, 85.5% of St, 2.5% of MA, 10.0% of EB, and 0.0238% of BPO. 500 revs / min; The second still feed composition comprises following component MA 10.5% in percentage by weight, St 9.5%, EB 18.3%, BPO 0.0596%, antioxidant " 1076 " 0.33%, supplementary speed is 1780 grams / hours, the reaction temperature was 93°C, and the stirring speed was 85 rpm. Devolatilization and sample performance measurement are the same as in Example 1. The properties of the obtained resin are shown in Table 1.
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