Preparation method of special blow molding material for automobile plastic fuel tank resistant to environmental stress cracking

A technology that is resistant to environmental stress and fuel tanks, applied in the field of blow molding plastics, can solve problems such as high safety performance requirements, expensive raw materials, and difficulty in ensuring supply, and achieve outstanding low-temperature impact resistance, excellent rigidity and toughness balance, and excellent Effect of environmental stress cracking resistance

Active Publication Date: 2018-11-23
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, due to the constraints of the production process, the domestic HDPE production equipment is difficult to produce the special blow molding materials for automobile plastic fuel tanks (referred to as special materials for automobile fuel tanks) that meet the requirements and can be applied to six-layer fuel tanks, and the special materials for automobile fuel tanks The safety performance requirements are high, and it needs to be tested by the safety performance certification of the automobile industry. The localization of automobile plastic fuel tanks has become a difficult problem to solve. The special materials for automobile fuel tanks have to rely on imports in large quantities. The raw materials are expensive and difficult to guarantee supply.

Method used

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  • Preparation method of special blow molding material for automobile plastic fuel tank resistant to environmental stress cracking
  • Preparation method of special blow molding material for automobile plastic fuel tank resistant to environmental stress cracking
  • Preparation method of special blow molding material for automobile plastic fuel tank resistant to environmental stress cracking

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Raw materials for ethylene-hexene copolymerized polyethylene resin:

[0037] 1) The feed rate of polymer grade ethylene is 30t / h

[0038] 2) Catalyst: Chromium catalyst 963, adding amount 112kg / h

[0039] 3) The amount of 1-hexene added is 457kg / h

[0040] 4) diluent isobutane 36kg / h

[0041] The preparation method of ethylene-hexene copolymerized polyethylene:

[0042] 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 ℃, the ethylene feed rate is 30t / h, the 1-hexene feed rate is 457kg / h, the catalyst feed rate is 112kg / h, the melt flow rate of ethylene and 1-hexene reaction is 6.2g / 10min, and the density is 0.945g / h cm 3 The ethylene-hexene copolymerized polyethylene resin has a molecular weight distribution of 15.3 and a weight average ...

Embodiment 2

[0050] Raw materials for ethylene-hexene copolymerized polyethylene resin:

[0051] 1) The feed rate of polymer grade ethylene is 38t / h

[0052] 2) Catalyst: Chromium catalyst 963, adding amount 149kg / h

[0053] 3) The amount of 1-hexene added is 795kg / h

[0054] 4) diluent isobutane 36.8kg / h

[0055] The preparation method of ethylene-hexene copolymerized polyethylene resin:

[0056] 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 g / cm 3 The ethylene-hexene copolymerized polyethylene resin has a molecular weight distribution of 16.8 and a weight average mol...

Embodiment 3

[0065] Raw materials for ethylene-hexene copolymerized polyethylene resin:

[0066] 1) The feed rate of polymer grade ethylene is 33.8t / h

[0067] 2) Catalyst: Chromium catalyst 963, adding amount 196.1kg / h

[0068] 3) The amount of 1-hexene added is 842.8kg / h

[0069] 4) diluent isobutane 35.8kg / h

[0070] The preparation method of ethylene-hexene copolymerized polyethylene resin:

[0071] 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 ethylene feed rate is 33.8t t / h, the 1-hexene feed rate is 842.8kg / h, the catalyst feed rate is 196.1kg / h, and the melt flow rate obtained by the reaction of ethylene and 1-hexene is 5.5g / 10min. The density is 0.945g / cm 3 The ethylene-hexene copolymerized polyethylene resin has a molecular weight distribution of 19...

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Abstract

The invention discloses a preparation method of an environment stress cracking resistant blow molding material special for an auto plastic fuel tank. The preparation method comprises the following steps: (1) under the condition that a diluent is always in a circulating state and in the presence of a catalyst, placing raw materials including ethylene and 1-hexene into a reaction vessel for reacting, wherein the reaction temperature is 94 to 100 DEG C, and the reaction is stopped when the melt flow rate of a reaction product reaches 5.3 to 6.5g / 10min and the density is 0.943 to 0.947kg / m<3>, so as to obtain ethylene hexene copolymerization polyethylene resin; (2) taking and uniformly mixing 99.50 to 99.80 parts of ethylene hexene copolymerization polyethylene resin, 0.05 to 0.35 part of antioxidant, 0.03 to 0.15 part of auxiliary antioxidant and 0.02 to 0.06 part of zinc stearate, then adding the same into a mixing mill for extrusion pelletization, and cooling particles in cooling water; the obtained blow molding material special for the auto plastic fuel tank has relatively high melt strength, excellent environment stress cracking resistance and creep resistance, and good chemical corrosion resistance, and is suitable for machine shaping of single-layer and multilayer auto plastic fuel tanks.

Description

technical field [0001] The invention belongs to the field of blow molding plastics, and in particular relates to a preparation method of a special blow molding material for automobile plastic fuel tanks resistant to environmental stress cracking. Background technique [0002] The plasticization of fuel tanks is an important direction of modern automobile plasticization. With the requirements of automobile lightweight and the continuous development of high-density polyethylene material properties, plastics are more and more widely used in automobiles, and the application of automobile plastics is even greater. It has become one of the symbols to measure the level of automobile production technology and the level of new material research and development. Compared with metal fuel tanks, automotive plastic fuel tanks are light in weight, can be integrally formed, have flexible shape design, good anti-seepage and corrosion resistance, simple production process, high efficiency an...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08L23/08C08K5/098C08K5/134C08K5/524C08F210/16
CPCC08F210/16C08K5/098C08K5/1345C08K5/524C08L23/0815C08F210/14C08F2500/01C08F2500/13C08F2500/07
Inventor 岑静芸钟向宏蔡伟肖树萌梁戈钟朝云许敏刘国禹杜子明
Owner CHINA PETROLEUM & CHEM CORP
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