Adhesive resin for barrier composite hose and preparation method and application thereof
A technology for bonding resins and composite hoses, applied in the direction of hoses, graft polymer adhesives, pipes/pipe joints/fittings, etc., which can solve the problem of no product, insufficient adhesion, and monomers in barrier composite hoses Residue and other problems, to achieve the effect of less crystal points, high adhesion and stable performance
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Embodiment 1
[0034] (1) 3 parts by mass of maleic anhydride, 1 part by mass of acrylamide and 0.5 parts by mass of initiator (cumene hydroperoxide and BPO are compounded at a mass ratio of 2:1) are dissolved in 4.5 parts by mass of acetone, and then Add 100 parts by mass of HDPE (190°C / 2.16Kg, MFR=20g / 10min) into a high-speed mixer and mix evenly, and finally pass through a reactive twin-screw extruder (screw length-to-diameter ratio L / D is 44:1) Reactive extrusion to obtain maleic anhydride and acrylamide double monomer grafted PE masterbatch; the processing temperature of the twin-screw extruder is 140-180°C.
[0035] (2) 20 parts by mass of PE masterbatch grafted with dual monomers, 60 parts by mass of LLDPE (190°C / 2.16Kg, MFR=1g / 10min), ethylene-octene copolymer (190°C / 2.16Kg, MFR= 18g / 10min) 20 parts by mass, 0.15 parts by mass of PPA additive FX5920A (3M company) and 0.5 parts by mass of antioxidant B215 (BASF) were added together in a high-speed mixer, mixed evenly, and blended by a...
Embodiment 2
[0037] (1) 2 parts by mass of maleic anhydride, 0.7 parts by mass of acrylamide and 0.3 parts by mass of initiator (cumene hydroperoxide and BPO are compounded at a mass ratio of 2:1) are dissolved in 3 parts by mass of acetone, and then Add 100 parts by mass of LDPE (190°C / 2.16Kg, MFR=7g / 10min) into a high-speed mixer and mix evenly, and finally pass through a reactive twin-screw extruder (screw length-to-diameter ratio L / D is 44:1) Reactive extrusion to obtain maleic anhydride and acrylamide double monomer grafted PE masterbatch; the processing temperature of the twin-screw extruder is 140-180°C.
[0038] (2) 25 parts by mass of PE masterbatch grafted with dual monomers, 60 parts by mass of LLDPE (190°C / 2.16Kg, MFR=2g / 10min), ethylene-octene copolymer (190°C / 2.16Kg, MFR= 5g / 10min) 15 mass parts, PPA additive FX 5920A (3M company) 0.1 mass part and antioxidant 1010 (BASF) 0.1 mass part, antioxidant 168 (BASF) 0.2 mass part join in the high-speed mixer together, Mix evenly, a...
Embodiment 3
[0040] (1) 1.5 parts by mass of maleic anhydride, 0.5 parts by mass of acrylamide and 0.1 parts by mass of initiator (cumene hydroperoxide and BPO are compounded at a mass ratio of 2:1) are dissolved in 2.1 parts by mass of acetone, and then Add 100 parts by mass of LLDPE (190°C / 2.16Kg, MFR=2g / 10min) into a high-speed mixer and mix evenly, and finally pass through a reactive twin-screw extruder (screw length-to-diameter ratio L / D is 44:1) Reactive extrusion to obtain maleic anhydride and acrylamide double monomer grafted PE masterbatch; the processing temperature of the twin-screw extruder is 140-180°C.
[0041] (2) 30 parts by mass of PE masterbatch grafted with dual monomers, 60 parts by mass of LLDPE (190°C / 2.16Kg, MFR=7g / 10min), ethylene-octene copolymer (190°C / 2.16Kg, MFR= 0.5g / 10min) 10 parts by mass, 0.05 parts by mass of PPA additive FX5924 (3M company) and 0.2 parts by mass of antioxidant B225 (BASF) were added to the high-speed mixer together, mixed evenly, and blend...
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