阅读说明：本技术 一种用于聚苯醚合成的高耐水性催化剂 (High-water-resistance catalyst for synthesizing polyphenyl ether ) 是由 张洪波 李勇 孙长久 衷晟 贾喜森 于 2021-09-24 设计创作，主要内容包括：本发明涉及一种用于聚苯醚合成的高耐水性催化剂。该催化剂由钴盐和低水溶性的有机胺络合而成。该催化剂体系具有很低的水溶性,所以几乎不受反应产生的水的影响,可大大提高反应活性和稳定性。(The invention relates to a high water-resistant catalyst for synthesizing polyphenyl ether. The catalyst is prepared by complexing cobalt salt and organic amine with low water solubility. The catalyst system has very low water solubility, so the catalyst system is hardly influenced by water generated by reaction, and the reaction activity and the stability can be greatly improved.)

1. A highly water-resistant catalyst for polyphenylene ether synthesis, which is prepared from a) a cobalt salt; b) low water solubility organic amine.

2. The ferrocobalt salt of claim 1, wherein the water-soluble inorganic salt of cobalt is selected from the group consisting of cobalt nitrate, cobalt sulfate, cobalt chloride, cobalt bromide, etc.

3. The organic amine having low water solubility according to claim 2, wherein the ratio C/N of the number of carbon atoms to nitrogen atoms in the molecule is not less than 7, such as heptylamine, dimethylheptylamine, dimethyldodecylamine, etc.

Technical Field

The invention relates to a high water-resistant catalyst for synthesizing polyphenyl ether.

Background

Polyphenylene ether, poly (2, 6-dimethyl-1, 4-phenylene oxide), abbreviated as PPO (polyphenylene oxide) or PPE (polyphenylene ether), also known as polyphenylene oxide or polyphenylene ether, is a general engineering plastic. Polyphenylene oxide is a polymer formed by oxidative coupling reaction of disubstituted phenol under the action of oxygen in the presence of metal salt/amine. The composite material has excellent comprehensive performance, and is characterized by excellent dimensional stability and outstanding electric insulation property under long-term load, wide use temperature range and long-term use within the range of-100 to 121 ℃. The product has high tensile strength, impact strength and creep resistance. In addition, the wear resistance and the electrical property are better. The method is mainly used for replacing stainless steel to manufacture surgical medical instruments. The method can be used for manufacturing gears, blower blades, pipelines, valves, screws, other fasteners, connectors and the like in the electromechanical industry, and is also used for manufacturing parts in the electronic and electrical industries, such as coil frames, printed circuit boards and the like.

The disubstituted phenol can generate water in the polymerization process, and the water can perform extraction and destruction effects on a metal salt/amine catalyst in a system, so that the reaction activity and the reaction rate in the later polymerization stage are reduced, and the yield and the quality of a product are adversely affected.

The invention discloses a high water-resistant catalyst which still has good polymerization activity in the presence of water and ensures that the polymerization process is carried out stably.

Disclosure of Invention

The invention provides a high water-resistant catalyst for synthesizing polyphenyl ether.

In order to ensure the reaction activity of the polyphenyl ether in the whole synthesis process and improve the yield and quality of the product, the invention provides the high water-resistant catalyst.

The following provides a more detailed description of the present invention.

A highly water-resistant catalyst for polyphenylene ether synthesis, which is prepared from a) a cobalt salt; b) low water solubility organic amine.

Cobalt salt refers to water-soluble inorganic salt of cobalt, such as cobalt chloride, cobalt nitrate, cobalt sulfate, and one or more mixtures thereof, but not limited to the above cobalt salt.

The organic amine with low water solubility refers to a compound with the number ratio C/N of carbon atoms to nitrogen atoms in the molecule being more than or equal to 7, such as one or a mixture of more than one of heptylamine, dimethylheptylamine, dimethyldodecylamine and the like, but is not limited to the compound.

The molar ratio of cobalt salt to organic amine of low water solubility is less than 1/10, preferably less than 1/20.

The polymerization process is as follows: dissolving a certain amount of raw material disubstituted phenol in a proper amount of organic solvent (such as dimethylbenzene) and introducing the mixture into a reaction kettle, introducing the premixed cobalt salt/low water-solubility organic amine mixture into the reaction kettle, adjusting the temperature of the reaction kettle to 20-50 ℃ under the stirring action, introducing oxygen into the bottom of the reaction kettle, wherein the purity of the oxygen is more than 97%, stopping oxygen after reacting for 1-3h, introducing the material into a poor solvent for precipitation, filtering, washing and drying to obtain a polyphenyl ether product.

The reaction process shows good reactivity and oxygen absorption rate without phase transfer catalyst.

The following examples are provided for better illustration of the present invention and are not intended to limit the scope of the present invention.

Example 1

Dissolving a certain amount of raw material 50 g of 2, 6-dimethylphenol in 200 ml of dimethylbenzene, introducing the mixture into a reaction kettle, weighing 0.2 g of cobalt nitrate and 4 g of heptylamine, mixing, adding the mixture into the reaction kettle, starting stirring, adjusting the temperature of the materials to 45 ℃, and introducing oxygen into the bottom of the reaction kettle, wherein the flow of the oxygen is 50 ml/min. Controlling the reaction temperature at 45-50 ℃ and polymerizing for 3 hours. The oxygen was then removed and the material was precipitated with 600 ml of methanol, filtered, the filter cake washed to a pale yellow colour with methanol and dried at 120 ℃ for 10 hours to give the polyphenylene ether product having a weight average molecular weight of 87700.

Example 2

Using 0.2 g of cobalt nitrate and 7 g of dimethyldodecylamine as a catalyst, the other operations were conducted in accordance with example 1, to thereby obtain a polyphenylene ether having a weight-average molecular weight of 98700.

Example 3

Using 0.2 g of cobalt chloride and 7 g of dimethyldodecylamine as a catalyst, the other operations were conducted in accordance with example 1, to thereby obtain a polyphenylene ether having a weight average molecular weight of 69700.

Comparative example 1

The other operation was conducted in accordance with example 1 using 0.2 g of copper chloride and 7 g of aniline as a catalyst, to thereby obtain a polyphenylene ether having a weight average molecular weight of 10500.

Comparative example 2

Using 0.2 g of cupric bromide and 5 g of butylamine as catalysts, the other operations were identical to those of example 1, resulting in a polyphenylene ether weight average molecular weight of 13500.

Comparative example 3

The other operations were carried out in accordance with example 1 using 0.2 g of copper bromide and 1 g of butylamine and 4 g of diethylpropylamine as catalysts, and the polyphenylene ether had a weight average molecular weight of 18300.

It should be understood that this example is for illustrative purposes only and is not intended to limit the scope of the present invention. Further, it should be understood that various changes or modifications of the present invention may be made by those skilled in the art after reading the contents of the present invention, and those equivalents are also within the scope of the present invention defined by the appended claims.