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Novel method for recovering solvent for polymerization of poly(p-phenytene terephthalamide)

A technology of poly-p-phenylene terephthalamide and a new method, which is applied in the field of polymer material synthesis, can solve the problems of easy decomposition, lower recovery rate of NMP, and low recovery rate, and achieve a high degree of continuity and lower energy consumption. low consumption and high recovery rate

Active Publication Date: 2008-10-22
SINOCHEM HIGH PERFORMANCE FIBER MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method has the following problems: (1) after the polymer is neutralized under reduced pressure, the salt in the polymer will be difficult to clean, and the ash content in the PPTA product is relatively high; (2) NMP is distilled under acidic conditions (3) The recovered NMP cannot meet the polymerization requirements of PPTA (the relative inherent viscosity of the polymer meeting the spinning requirements should be above 5.5dl / g)
The advantage of this method is that the solvent-containing washing liquid is separated from the product PPTA before the solvent recovery operation, which avoids the decomposition of the solvent NMP, the purity of the recovered solvent reaches 99.5%, the recovery rate reaches 91%, and the water content is lower than 100ppm, which is fully in line with Polymerization requirements of PPTA, but this method still has the problems of insufficient continuity for industrialization, low dehydration and desalination efficiency, high energy consumption, and low recovery rate

Method used

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  • Novel method for recovering solvent for polymerization of poly(p-phenytene terephthalamide)

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Contains 18% NMP, 3% CaCl 2 The neutralized washing liquid enters the first-stage thin-film evaporator from the storage tank at a flow rate of 50kg / hr, and its absolute pressure is controlled to be 1.0-1.5KPa, and the temperature is 100-120°C. Most of the NMP and water are vaporized and directly It enters the middle part of the crude distillation tower, and its heavy components enter the second-stage thin film evaporator. The absolute pressure inside the tower is 1.0-2.0Pa, and the temperature is 70-130°C. After removing most of the water in the solvent, enter the rectification tower to remove a small amount of water in the NMP, improve the purity of NMP, and control the absolute pressure inside the tower to 1.0~1.5Pa, the temperature is 70~130℃, and then through the purification tower to further reduce the trace moisture content in NMP, it enters the final NMP receiving tank, and the flow rate of receiving NMP is 8.7kg / hr, that is, the recovery rate of NMP reaches 96....

Embodiment 2

[0020] Contains 18% NMP, 3% CaCl 2 The neutralized washing liquid enters the first-stage thin-film evaporator from the storage tank at a flow rate of 40kg / hr, and its absolute pressure is controlled to be 1.0-1.5KPa, and the temperature is 100-120°C. Most of the NMP and water are vaporized and directly It enters the middle part of the crude distillation tower, and its heavy components enter the second-stage thin film evaporator. The absolute pressure inside the tower is 1.0-2.0Pa, and the temperature is 70-130°C. After removing most of the water in the solvent, enter the rectification tower to remove a small amount of water in the NMP, improve the purity of NMP, and control the absolute pressure inside the tower to 1.0~1.5Pa, the temperature is 70~130℃, and after further reducing the trace moisture content in NMP through the purification tower, it enters the final NMP receiving tank, and the flow rate of receiving NMP is 6.99kg / hr, that is, the recovery rate of NMP reaches 97...

Embodiment 3

[0022] Contains 18% NMP, 3% CaCl 2 The neutralized washing liquid enters the first-stage thin-film evaporator from the storage tank at a flow rate of 55kg / hr, and its absolute pressure is controlled to be 1.0-1.5KPa, and the temperature is 100-120°C. Most of the NMP and water are vaporized and directly It enters the middle part of the crude distillation tower, and its heavy components enter the second-stage thin film evaporator. The absolute pressure inside the tower is 1.0-2.0Pa, and the temperature is 70-130°C. After removing most of the water in the solvent, enter the rectification tower to remove a small amount of water in NMP, improve the purity of NMP, and control the absolute pressure inside the tower to 1.0~1.5Pa, the temperature is 70~130℃, after further reducing the trace moisture content in NMP through the purification tower, it enters the final NMP receiving tank, and the flow rate of receiving NMP is 9.53kg / hr, that is, the recovery rate of NMP reaches 96.3%, the...

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Abstract

The invention relates to a novel method for recycling a solvent used for polymerizing the poly (p-phenylene terephthalamide) which has a shortened form of para-aramid or PPTA. The method comprises the following steps that: the PPTA polymer made by the low-temperature solution polycondensation contains a large amount of solution N-Methyl pyrrolidine which has a shortened form of NMP and certain amount of calcium chloride (CaCl2), the PPTA polymer is washed by deionized water for a plurality of times, the PPTA polymer is collected to enter a drying system, a scrub solution is neutralized and enters a neutralizing liquid storage tank of a solvent recycling system; the neutralizing fluid is processed by a two-stage film evaporator to remove the CaCl2 added to the polyreaction and generated by the neutralizing reaction, the hydration NMP enters the middle part of a topping still from the top of the film evaporator in a state of mixed gas to remove most of water by the distillation process, the purity quotient of NMP is improved further and the minim water inside the NMP is lowered by the rectification and purification processes, the obtained NMP has a purity quotient higher than 99.5 percent, a water content lower than 100ppm, thereby completely satisfying the requirement of PPTA polymerization. The technique is used for recycling the solvent for PPTA polymerization; the recycling rate of the NMP is higher than 96 percent, thereby lowering the cost further and providing reliable guarantee for the industrialization of the para-aramid.

Description

technical field [0001] The invention relates to a solvent recovery method for the polymerization of poly-p-phenylene terephthalamide, which belongs to the field of polymer material synthesis. Background technique [0002] As we all know, poly-p-phenylene terephthalamide (PPTA) is a mixture of p-phenylenediamine and terephthaloyl chloride in N-methylpyrrolidone (NMP) and calcium chloride (CaCl 2 ) in the solvent system through low-temperature solution polycondensation reaction. In the process of preparing PPTA, a large amount of NMP needs to be used, and the requirements are extremely strict (water content is lower than 100ppm). One of the key factors of industrialization. Therefore, researchers in this field have successively proposed different methods to recover NMP. [0003] CN95102183.4 discloses a method for recovering the polymerization solvent of synthetic PPTA. It proposes to distill the polycondensate obtained by polymerization under reduced pressure, and after the...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08J11/02C08G69/32
Inventor 尤秀兰刘兆峰周助胜曹煜彤叶盛
Owner SINOCHEM HIGH PERFORMANCE FIBER MATERIALS CO LTD
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