Device for preparing polyamide, prepolymerization method, and polyamide production equipment and production method
A production method and polyamide technology, applied in the field of polyamide, can solve problems such as the unsatisfactory temperature control effect of the tubular reactor, the difficulty in controlling the temperature of the reaction mixture, and the limited ability to adjust the temperature, so as to achieve industrial value, expand production and Wide range of applications and less loss of raw materials
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[0103] (1) Preparation of polyamide salt solution
[0104] Under the protection of nitrogen, the high-concentration 1,5-pentanediamine is diluted with degassed deionized water to a certain concentration solution (30%-50%). The aliphatic dibasic acid and the diluted 1,5-pentanediamine are continuously added to the reactor at the same time, and the cooling water removes the heat of reaction during the neutralization reaction in time. During the neutralization process, the pH value of the solution is constantly detected, so that the mol ratio of the diamine / diacid in the reactor is slightly lower than 1. After stabilization, the resulting salt solution is transferred to the reactor in series behind (can be connected in series) multiple units, but generally not more than 3 units), use diamine aqueous solution to further neutralize step by step and adjust the molar ratio of diamine / diacid and the mass concentration of salt, and control the flow of diamine aqueous solution with the ...
Embodiment 1
[0119] Configuration pH is the polyamide 56 salt solution of 65% concentration of 7.95, carries out polymerization by the processing condition of table 1 by the production equipment of the present invention, the pressure of final polymerization tank is 210mmHg A, obtains the slice that relative viscosity is 68.9, and its terminal amino content is 40.4.
Embodiment 2
[0121] Configuration pH is the polyamide 56 salt solution of 65% concentration of 8.05, carries out polymerization according to the process condition of embodiment 1 through the production equipment of the present invention, but the pressure of final polymerization kettle is adjusted to 180mmHg A, and output is higher than embodiment 1 was increased by 20%, and the chips with a relative viscosity of 69.7 and an amino-terminal content of 40.1 were obtained.
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