A special blow molding material for automobile plastic fuel tank and its preparation method
A fuel tank and plastic technology, applied in the field of blow molding materials, can solve the problems of difficulty in supplying imported fuel tank materials, high price of automobile plastic fuel tanks, and high cost of automobile plastic fuel tanks, and achieve excellent environmental stress cracking resistance. Excellent toughness balance and reasonable molecular weight distribution
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Embodiment 1
[0050] Raw materials for ethylene-hexene copolymerized polyethylene resin:
[0051] 1) The feed rate of polymer grade ethylene is 28t / h
[0052] Ethylene: purity ≥99.20% C 2 h 2 ≤5×10 -6 CO≤1×10 -6
[0053] o 2 ≤2×10 -6 h 2 O≤1×10 -6 COS≤0.02×10 -6 .
[0054] 2) Catalyst: NTR-973 dosage 250kg / h
[0055] 3) The amount of 1-hexene added is 504kg / h
[0056] 1-Hexene: Purity ≥98.5% H 2 O≤20×10 -6 CO≤5×1O -6
[0057] Mono-olefins≥98.5% Isomerized alpha-olefins≤1% Normal non-alpha-olefins≤1%
[0058] Normal alpha olefin≥96% Peroxide≤1×10 -6 Sulfur≤1×10 -6 .
[0059] 4) diluent isobutane 36kg / h
[0060] Isobutane: Purity≥95.0% Acetylene≤2×10 -6 Total sulfur≤1×10 -6
[0061] Total olefins≤100×10 -6 Water≤20×10 -6 o 2 ≤5×10 -6 .
[0062] The preparation method of ethylene-hexene copolymerized polyethylene:
[0063] The diluent isobutane is always in a circulating state. The ethylene and hexene are respectively injected into the loop reactor, and the...
Embodiment 2
[0072] Raw materials for ethylene-hexene copolymerized polyethylene resin:
[0073] 1) The feed rate of polymer grade ethylene is 36.2t / h
[0074] Ethylene: purity≥99.20% CO≤1×10 -6 o 2 ≤2×10 -6 h 2 O≤1×10 -6 .
[0075] 2) Catalyst: NTR-973 dosage 249kg / h
[0076] 3) The amount of 1-hexene added is 513kg / h
[0077] 1-Hexene: Purity ≥98.5% H 2 O≤20×10 -6 CO≤5×1O -6 Isomerized alpha olefins ≤ 1%.
[0078] 4) diluent isobutane 34.8kg / h
[0079] Isobutane: Purity≥95.0% Acetylene≤2×10 -6 Total sulfur≤1×10 -6
[0080] Total olefins≤100×10 -6 Water≤20×10 -6 o 2 ≤5×10 -6 .
[0081] The preparation method of ethylene-hexene copolymerized polyethylene resin:
[0082] The diluent isobutane is always in a circulating state. The ethylene and hexene are injected into the loop reactor respectively, and the catalyst is added to carry out the synthesis reaction. The reaction temperature in the reactor is controlled at 90.2°C, and the ethylene feed rate is 36.2t / h. -...
Embodiment 3
[0091] Raw materials for ethylene-hexene copolymerized polyethylene resin:
[0092] 1) The feed rate of polymer grade ethylene is 36.5t / h
[0093] Ethylene: purity ≥99.20% C 2 h 2 ≤5×10 -6 CO≤1×10 -6
[0094] o 2 ≤2×10 -6 h 2 O≤1×10 -6 COS≤0.02×10 -6 .
[0095] 2) Catalyst: NTR-973 dosage 143kg / h
[0096] 3) The amount of 1-hexene added is 293.7kg / h
[0097] 1-Hexene: Purity ≥98.5% H 2 O≤20×10 -6 CO≤5×1O -6
[0098] Mono-olefins≥98.5% Isomerized alpha-olefins≤1% Normal non-alpha-olefins≤1%
[0099] Normal alpha olefin≥96% Peroxide≤1×10 -6 Sulfur≤1×10 -6 .
[0100] 4) diluent isobutane 35.8kg / h
[0101] Isobutane: Purity≥95.0% Acetylene≤2×10 -6 Total sulfur≤1×10 -6
[0102] Total olefins≤100×10 -6 Water≤20×10 -6 o 2 ≤5×10 -6 .
[0103] The preparation method of ethylene-hexene copolymerized polyethylene resin:
[0104] The diluent isobutane is always in a circulating state. The ethylene and hexene are injected into the loop reactor respectivel...
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