Blow moulding material being resistant to environmental stress cracking and being specially used for automobile plastic fuel tank
A technology that is resistant to environmental stress and fuel tanks, applied in the field of blow molding plastics, can solve the problems of high safety performance requirements, expensive raw materials, and difficulty in ensuring supply, and achieve outstanding low-temperature impact resistance, excellent rigidity and toughness balance, excellent Effects of Environmental Stress Cracking Resistance
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Embodiment 1
[0041] Raw materials for ethylene-hexene copolymerized polyethylene resin:
[0042] 1) The feed rate of polymer grade ethylene is 30t / h
[0043] 2) Catalyst: Chromium-based catalyst Magnapore? 963, adding amount 112kg / h
[0044] 3) The amount of 1-hexene added is 457kg / h
[0045] 4) diluent isobutane 36kg / h
[0046] The preparation method of ethylene-hexene copolymerized polyethylene:
[0047] The diluent isobutane is always in a circulating state. The ethylene and 1-hexene are injected into the loop reactor respectively, the ethylene-hexene feed ratio is strictly controlled, and the activated catalyst is added to control the reaction temperature in the reactor to 94.8 ℃, ethylene feed rate is 30t / h, 1-hexene feed rate is 457kg / h, catalyst feed rate is 112kg / h, the melt flow rate of ethylene and 1-hexene reaction is 6.2g / 10min, and the density is 0.945kg / h m 3 The ethylene-hexene copolymerized polyethylene resin has a molecular weight distribution of 15.3 and a weight...
Embodiment 2
[0058] Raw materials for ethylene-hexene copolymerized polyethylene resin:
[0059] 1) The feed rate of polymer grade ethylene is 38t / h
[0060] 2) Catalyst: Chromium-based catalyst Magnapore? 963, adding amount 149kg / h
[0061] 3) The amount of 1-hexene added is 795kg / h
[0062] 4) diluent isobutane 36.8kg / h
[0063] The preparation method of ethylene-hexene copolymerized polyethylene resin:
[0064] The diluent isobutane is always in a circulating state, inject ethylene and 1-hexene into the loop reactor respectively, strictly control the feed ratio of ethylene and hexene, and add a pre-activated catalyst to control the reaction temperature in the reactor to 98.2 ℃, the feed rate of ethylene is 38t / h, the feed rate of 1-hexene is 795kg / h, the feed rate of catalyst is 149kg / h, the melt flow rate of ethylene and 1-hexene is 5.4g / 10min, and the density is 0.945 kg / m 3 The ethylene-hexene copolymerized polyethylene resin has a molecular weight distribution of 16.8 and a...
Embodiment 3
[0075] Raw materials for ethylene-hexene copolymerized polyethylene resin:
[0076] 1) The feed rate of polymer grade ethylene is 33.8t / h
[0077] 2) Catalyst: Chromium-based catalyst Magnapore? 963, adding amount 196.1kg / h
[0078] 3) The amount of 1-hexene added is 842.8kg / h
[0079] 4) diluent isobutane 35.8kg / h
[0080] The preparation method of ethylene-hexene copolymerized polyethylene resin:
[0081] The diluent isobutane is always in a circulating state, inject ethylene and 1-hexene into the loop reactor respectively, strictly control the feed ratio of ethylene and hexene, and add a pre-activated catalyst to control the reaction temperature in the reactor to 95 ℃, the feed rate of ethylene is 33.8tt / h, the feed rate of 1-hexene is 842.8kg / h, the feed rate of catalyst is 196.1kg / h, the melt flow rate obtained by the reaction of ethylene and 1-hexene is 5.5g / 10min, The density is 0.945kg / m 3 The ethylene-hexene copolymerized polyethylene resin has a molecular we...
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