High-hexene grafted high-density polyethylene geomembrane blow-molding material
A technology for copolymerizing polyethylene with high-density polyethylene and ethylene-hexene is applied in the field of high-hexene-grafted high-density polyethylene geomembrane blow molding materials, which can solve the difficulty of breaking through the lower density limit of geomembrane special materials and reduce the conversion rate of special materials , Lawrence pump power sudden increase and other problems, to achieve excellent environmental stress cracking resistance, improve production stability, reduce the effect of sticking to the wall
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Embodiment 1
[0034] Preparation of ethylene-hexene copolymerized polyethylene resin:
[0035] The diluent isobutane is always in a circulating state. The monomers ethylene and 1-hexene are injected into the loop reactor respectively, and the antistatic agent ASA and the activated NTR-975 chromium catalyst are added for reaction. The reaction temperature is 92.8 ℃, ethylene feed rate 38t / h, 1-hexene feed rate 1440 kg / h, catalyst feed rate 149 kg / h, isobutane feed rate 38.0 kg / h, antistatic agent 0.39 kg / h, reacted to the reaction product The melt flow rate is 11.9g / 10min and the density is 0.937~0.939kg / m 3 , stop the reaction to obtain ethylene hexene copolymerized polyethylene resin.
[0036] Raw material (parts by weight) of geomembrane blow molding material:
[0037] Ethylene hexene copolymerized polyethylene resin 99.55 parts
[0038] Antioxidant 0.45 parts
[0039] Wherein the antioxidant is tetrakis[β-(3,5-di-tert-butyl-4-hydroxyphenyl) propionate] pentaerythritol ester.
[0040...
Embodiment 2
[0043] Preparation of ethylene-hexene copolymerized polyethylene resin:
[0044] The diluent isobutane is always in a circulating state. The monomers ethylene and 1-hexene are injected into the loop reactor respectively, and the antistatic agent ASA and the activated NTR-975 chromium catalyst are added for reaction. The reaction temperature is 93.7 ℃, ethylene feed rate 38t / h, 1-hexene feed rate 1897 kg / h, catalyst feed rate 169 kg / h, isobutane feed rate 38.6 kg / h, antistatic agent 0.56 kg / h, reacted to the reaction product The melt flow rate is 12.3g / 10min and the density is 0.938kg / m 3 , stop the reaction to obtain ethylene hexene copolymerized polyethylene resin.
[0045] Raw material (parts by weight) of geomembrane blow molding material:
[0046] Ethylene hexene copolymerized polyethylene resin 99.70 parts
[0047] Antioxidant 0.30 parts
[0048] Wherein the antioxidant is tetrakis[β-(3,5-di-tert-butyl-4-hydroxyphenyl) propionate] pentaerythritol ester.
[0049] Prep...
Embodiment 3
[0052] Preparation of ethylene-hexene copolymerized polyethylene resin:
[0053] The diluent isobutane is always in a circulating state. The monomers ethylene and 1-hexene are injected into the loop reactor respectively, and the antistatic agent ASA and the activated NTR-975 chromium catalyst are added for reaction. The reaction temperature is 95.2 ℃, ethylene feed rate 36t / h, 1-hexene feed rate 2059 kg / h, catalyst feed rate 198 kg / h, isobutane feed rate 36 kg / h, antistatic agent 0.36 kg / h, react until the reaction product The melt flow rate is 12.6g / 10min and the density is 0.937kg / m 3 , stop the reaction to obtain ethylene hexene copolymerized polyethylene resin.
[0054] Raw material (parts by weight) of geomembrane blow molding material:
[0055] Ethylene hexene copolymerized polyethylene resin 99.80 parts
[0056] Antioxidant 0.20 parts
[0057] Wherein the antioxidant is tetrakis[β-(3,5-di-tert-butyl-4-hydroxyphenyl) propionate] pentaerythritol ester.
[0058] Pre...
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