Preparation method of stacking-resistant rigid medium-sized hollow blow molding material
A medium-sized and rigid technology, applied in the field of stacking-resistant rigid medium-sized hollow blow molding materials, can solve problems such as affecting product appearance and insufficient stacking rigidity, and achieve high melt strength, high weight-average molecular weight, and excellent stacking resistance. performance effect
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Embodiment 1
[0038] The diluent isobutane is always in a circulating state. The monomers ethylene and 1-hexene are injected into the loop reactor respectively, and the activated NTR-972 chromium catalyst is added for reaction. The ethylene feed rate is 30t / h, the feed rate of 1-hexene is 360kg / h, the feed rate of isobutane is 20t / h, the feed rate of catalyst is 180kg / h, and the reaction temperature is 100°C until the melt flow rate of the reaction product is 10.5g / 10min, and the density 0.952g / cm 3 , the reaction was stopped to obtain an ethylene-hexene copolymerized polyethylene resin with a weight average molecular weight of 187,000, a molecular weight distribution of 8.7, and a 1-hexene comonomer content of 0.09 mol%.
[0039] Raw materials (parts by weight) of medium-sized hollow container blow molding material:
[0040] Ethylene hexene copolymerized polyethylene resin 99.75 parts
[0041] Compounding additive ST-510 0.25 parts
[0042] Preparation method of medium-sized hollow con...
Embodiment 2
[0045] The diluent isobutane is always in a circulating state. The monomers ethylene and 1-hexene are injected into the loop reactor respectively, and the activated NTR-972 chromium catalyst is added for reaction. The ethylene feed rate is 35t / h, the feed rate of 1-hexene is 105kg / h, the feed rate of isobutane is 28t / h, the feed rate of catalyst is 175kg / h, the reaction temperature is 98°C, until the melt flow rate of the reaction product is 8.5g / 10min, the density 0.956g / cm 3 , the reaction was stopped to obtain an ethylene-hexene copolymerized polyethylene resin with a weight average molecular weight of 198,000, a molecular weight distribution of 9.6, and a 1-hexene comonomer content of 0.04 mol%.
[0046] Raw materials (parts by weight) of medium-sized hollow container blow molding material:
[0047] Ethylene hexene copolymerized polyethylene resin 99.90 parts
[0048] Compounding additive ST510 0.10 parts
[0049] Preparation method of medium-sized hollow container blo...
Embodiment 3
[0052] The diluent isobutane is always in a circulating state. The monomers ethylene and 1-hexene are injected into the loop reactor respectively, and the activated NTR-972 chromium catalyst is added for reaction. The ethylene feed rate is 45t / h, 1-hexene feed rate is 360kg / h, isobutane feed rate 22.5t / h, catalyst feed rate 288kg / h, reaction temperature 101 ℃, until the melt flow velocity of reaction product is 7.5g / 10min, The density is 0.953g / cm 3 , the reaction was stopped to obtain an ethylene-hexene copolymerized polyethylene resin with a weight average molecular weight of 204,000, a molecular weight distribution of 11.7, and a 1-hexene comonomer content of 0.08 mol%.
[0053] Raw materials (parts by weight) of medium-sized hollow container blow molding material:
[0054] Ethylene hexene copolymerized polyethylene resin 99.80 parts
[0055] Compounding additive ST510 0.20 parts
[0056] Preparation method of medium-sized hollow container blow molding material:
[005...
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