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Synthetic method for poly terephthalyl terephaldiamine polymer

A technology of poly(p-phenylene terephthalamide) and its synthesis method, which is applied in the field of synthesis of poly(p-phenylene terephthalamide) polymers, and can solve the problem of large amount of solvent recovery, large resin ash content, and complex production equipment and other problems, to achieve the effects of reducing investment cost and production cost, smooth polymerization reaction, and narrow molecular weight distribution

Inactive Publication Date: 2007-10-31
邢哲
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  • Summary
  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method requires a large investment cost for production equipment, a large amount of solvent recovery, and high requirements for the control accuracy of the production process. It is difficult to achieve precise control of reaction conditions, resulting in high production and operation costs, production equipment and control system investment.
[0004] Low-temperature solution polycondensation is to polymerize p-phenylenediamine and terephthaloyl chloride in strong polar solvents such as dimethylacetamide and N-methylpyrrolidone under low temperature conditions. In USP3,884,881, hexamethylphosphorus The amide is used as a solvent, and the jet mixer is used for mixing materials, and the twin-screw reactor is used for continuous polycondensation of low-temperature solution. The solvent hexamethylphosphoramide in this method has carcinogenic effect, and the jet mixer is easy to block, which affects the continuity of production; Zhao 53-133,296 uses N-methylpyrrolidone as a solvent and calcium chloride as a co-solvent, and p-phenylenediamine, calcium chloride and N-methylpyrrolidone are prepared into solutions and slurries respectively, and are mixed with molten terephthalamide After the acid chloride is mixed inside the S-1 mixer, it enters into the twin-screw kneader for polycondensation. The amount of calcium chloride used in this method is as high as 40%, and the resulting resin has a large ash content, and the S-1 mixer is easy to block; in the domestic open patent 90105870.x, Self-cleaning twin-shaft mixer and twin-screw reactor are used for low-temperature solution polycondensation. The production equipment is relatively complicated, and the heat exchange area of ​​the screw reactor is small. It is difficult to dissipate a large amount of reaction heat in the reaction process in time, which may easily cause local temperature overshoot. High lead to the generation of gel, and the requirements for the accuracy of material addition and reaction condition control in the production process are also very high, and the precise control of the reaction process is difficult to achieve, resulting in high investment in production equipment and control systems
[0005] During the low-temperature solution polycondensation process, with the increase of the by-product hydrogen chloride content in the system, the apparent viscosity of the reaction system will increase abnormally, which will slow down the mass transfer and heat transfer speed of the polymerization reaction system, which is not conducive to the progress of the reaction and is difficult Obtain high molecular weight poly-p-phenylene terephthalamide polymers, and in the above prior art, only increase the concentration of poly-p-phenylene terephthalamide polymers by using special solvents, or select special equipment to strengthen the reaction The means of the mixing effect of the system makes the reaction proceed, but this will make the reaction too violent and difficult to control, and does not take into account the removal of the by-product hydrogen chloride that is not conducive to the normal progress of the reaction

Method used

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  • Synthetic method for poly terephthalyl terephaldiamine polymer
  • Synthetic method for poly terephthalyl terephaldiamine polymer

Examples

Experimental program
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Effect test

Embodiment 1

[0022] Dissolve 0.20 kg of p-phenylenediamine and 0.23 kg of lithium chloride in 5.30 kg of dimethylacetamide with a water content below 100ppm, and prepare the weight of p-phenylenediamine in a reactor with a double-helix belt stirrer. The percentage concentration is 3.5%, and the lithium chloride weight percentage concentration is a solution of 4%. Cool the solution to -10°C, add 0.1 kg of terephthaloyl chloride to the reactor for the first time, and after 15 minutes of reaction, pass 0.016 kg of pure ammonia into the reactor to neutralize the hydrogen chloride produced by the reaction to obtain polycondensation intermediate The pH of the product solution is 6. For the second time, 0.1 kg of terephthaloyl chloride is added to the reactor. After 20 minutes of reaction, 0.016 kg of pure ammonia is passed into the reactor to neutralize the hydrogen chloride produced by the reaction, and the polycondensation intermediate product solution pH is obtained. 0.1 kilogram of terephtha...

Embodiment 2

[0028] Dissolve 0.30 kg of p-phenylenediamine and 0.30 kg of lithium chloride in 5.00 kg of N-methylpyrrolidone with a water content below 100ppm, and prepare the weight of p-phenylenediamine in a reactor with a double-helix belt stirrer. The percentage concentration is 6%, and the lithium chloride weight percentage concentration is a solution of 6%. Cool the solution to -10°C, add 0.2 kg of terephthaloyl chloride to the reactor for the first time, and after 15 minutes of reaction, pass 0.031 kg of pure ammonia into the reactor to neutralize the hydrogen chloride produced by the reaction to obtain polycondensation intermediate The pH of the product solution is 5. For the second time, 0.1 kg of terephthaloyl chloride is added to the reactor, and after 20 minutes of reaction, 0.017 kg of pure ammonia is passed into the reactor to neutralize the hydrogen chloride produced by the reaction to obtain the polycondensation intermediate product solution pH 0.1 kg of terephthaloyl chlor...

Embodiment 3

[0030]Dissolve 0.25 kg of p-phenylenediamine with a purity of more than 99.9% and 0.35 kg of calcium chloride with a purity of more than 99.9% in 5.00 kg of dimethylacetamide with a water content of less than 100ppm in a double-helix belt stirrer In the reactor, it is prepared as a solution containing 5% by weight of p-phenylenediamine and 7% by weight of calcium chloride. Cool the solution to -10°C, add 0.18 kg of terephthaloyl chloride to the reactor for the first time, and after 20 minutes of reaction, pass 0.029 kg of pure ammonia into the reactor to neutralize the hydrogen chloride produced by the reaction to obtain polycondensation intermediate The pH of the product solution is 6. For the second time, 0.15 kg of terephthaloyl chloride is added to the reactor, and after 25 minutes of reaction, 0.025 kg of pure ammonia is passed into the reactor to neutralize the hydrogen chloride produced by the reaction to obtain the polycondensation intermediate product solution pH 6.5,...

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Abstract

The present invention relates to the synthesis of polyterephthalyl phenyldiamine and belongs to the field of polymer material. The present invention synthesizes polyterephthalyl phenyldiamine polymer with p-phenyldiamine and paraththaolyl choride and through several reaction steps, and during the reaction, alkali matter is added continuously to produce hydrogen chloride to make the reaction mild and controllable to obtain high molecular weight polymer with narrow molecular weight distribution and high product homogeneity. The produced polymer may be used in many application fields.

Description

technical field [0001] The invention relates to a synthesis method of poly(p-phenylene terephthalamide) polymer, which belongs to the field of polymer materials. Background technique [0002] At present, the synthesis of poly-p-phenylene terephthalamide polymer mainly includes two processes: interfacial polycondensation and low-temperature solution polycondensation. [0003] Interfacial polycondensation is to dissolve p-phenylenediamine and terephthaloyl chloride in two immiscible solvents to prepare a solution of a certain concentration, and then quantitatively mix the two solutions under high-speed stirring, and then The interface is polymerized, and then the by-product hydrogen chloride is neutralized with an alkaline substance, and then the obtained poly-p-phenylene terephthalamide polymer is separated. This method requires a large investment in production equipment, a large amount of solvent recovery, and high requirements for the control accuracy of the production pro...

Claims

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Application Information

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IPC IPC(8): C08G69/32
Inventor 邢哲李吉东郭润栋
Owner 邢哲
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