A kind of preparation method of twin-screw reactive extrusion nylon elastomer
A nylon elastomer and reactive extrusion technology, which is applied in the field of twin-screw reactive extrusion nylon elastomer preparation, can solve problems such as low reactivity, limited use range, complex process, etc., and achieve labor cost reduction, product quality and Its excellent stability effect
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Embodiment 1
[0027] 1) Prepare the following ingredients:
[0028] Lauryl lactam 160g
[0029] Deionized water 6g
[0030] Adipic acid 23.4g
[0031] Antioxidant 1010 0.6g
[0032] Ethylene glycol 10g;
[0033] 2) Add laurolactam, deionized water, adipic acid and antioxidant 1010 into the reaction kettle and dissolve at 150°C;
[0034] 3) Raise the temperature of the reactor to 250°C, control the stirring speed at 60RPM, and keep the reaction under 20bar pressure for 12h;
[0035] 4) Add ethylene glycol in the reactor;
[0036] 5) Reaction under 600mmHg negative pressure at 230°C for 8 hours to obtain a nylon oligomer;
[0037] 6) 200g of nylon oligomer obtained in step 5, 150g of polyether polyol PTMEG1000, and 87.5g of isocyanate MDI were mixed at a high speed in liquid form, and poured into a twin-screw machine, and extruded to obtain a nylon elastomer. The twin-screw reaction temperature was controlled at 200-260°C, screw speed at 400RPM.
Embodiment 2
[0039] 1) Prepare the following ingredients:
[0040] Caprolactam 123g
[0041] Deionized water 6g
[0042] Terephthalic acid 60g
[0043] Antioxidant 1010 1g
[0044] Diethylene glycol amine 10g;
[0045] 2) Add caprolactam, deionized water, terephthalic acid and antioxidant 1010 into the reactor and keep warm at 150°C to dissolve;
[0046] 3) Raise the temperature of the reactor to 300°C, control the stirring speed at 100RPM, and keep the reaction under 22bar pressure for 12h;
[0047] 4) Diethylene glycol amine is added in the reactor;
[0048] 5) Reaction under 100mmHg negative pressure at 260°C for 10 hours to obtain a nylon oligomer;
[0049] 6) 200g of nylon oligomer obtained in step 5, 120g of polyether polyol PTMEG1000, and 81.2g of isocyanate MDI were mixed at a high speed in liquid form, and poured into a twin-screw machine, and extruded to obtain a nylon elastomer. The twin-screw reaction temperature was controlled at 200-260°C, screw speed at 500RPM.
Embodiment 3
[0051] 1) Prepare the following ingredients:
[0052] Caprolactam 120g
[0053] Deionized water 9.4g
[0054] Hexamethylenediamine 20g
[0055] Antioxidant 1010 0.6g
[0056] Tartaric acid 50g;
[0057] 2) Add caprolactam, deionized water, hexamethylenediamine and antioxidant 1010 into the reaction kettle and dissolve at 150°C;
[0058] 3) Raise the temperature of the reactor to 250°C, control the stirring speed at 60RPM, and keep the reaction under 20bar pressure for 12h;
[0059] 4) add tartaric acid in reactor;
[0060] 5) Reaction under 600mmHg negative pressure at 230°C for 8 hours to obtain a nylon oligomer;
[0061] 6) 250g of nylon oligomer obtained in step 5, 94g of polyether polyol PTMEG1000, and 115g of isocyanate MDI were mixed in liquid form at high speed, and poured into a twin-screw machine, and extruded to obtain nylon elastomer. The twin-screw reaction temperature was controlled at 200 -260°C, screw speed at 500RPM.
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