CN119663473A - Preparation method of melt-spun anion polyamide fiber - Google Patents

Preparation method of melt-spun anion polyamide fiber Download PDF

Info

Publication number
CN119663473A
CN119663473A CN202410220344.7A CN202410220344A CN119663473A CN 119663473 A CN119663473 A CN 119663473A CN 202410220344 A CN202410220344 A CN 202410220344A CN 119663473 A CN119663473 A CN 119663473A
Authority
CN
China
Prior art keywords
melt
polyamide
anion
preparing
polyamide fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202410220344.7A
Other languages
Chinese (zh)
Inventor
曹雪婷
冉启迪
王松林
戴仁强
王文辉
倪宇檬
喻福念
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang Hengyi Petrochemical Co Ltd
Original Assignee
Zhejiang Hengyi Petrochemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhejiang Hengyi Petrochemical Co Ltd filed Critical Zhejiang Hengyi Petrochemical Co Ltd
Priority to CN202410220344.7A priority Critical patent/CN119663473A/en
Publication of CN119663473A publication Critical patent/CN119663473A/en
Pending legal-status Critical Current

Links

Landscapes

  • Polyamides (AREA)

Abstract

The invention relates to the field of polyamide fibers, and provides a preparation method of a melt-directly-spun negative ion polyamide fiber, aiming at the problem of poor dispersibility of a negative ion generator in polyamide slices, comprising the following steps of (1) blending a polymerization monomer and an auxiliary agent, and sequentially carrying out prepolymerization and final polymerization; the auxiliary agent comprises a ring-opening agent, a blocking agent, a stabilizing agent and an anion generator treated by a compatibilizer modifier, wherein (2) the monomer is removed by one or two of a disc evaporator and a cage evaporator at the same time of or after the final polymerization reaction to obtain a melt after the removal of monomers, and (3) the melt after the removal of monomers is directly pelletized to obtain slices or directly spun to obtain the anion polyamide fiber. The negative ion generator is kept in a melt state all the time, which is favorable for the stability of surface modification and the high efficiency of functions, thus not only improving the product performance, but also improving the production efficiency.

Description

Preparation method of melt-spun anion polyamide fiber
Technical Field
The invention relates to the field of polyamide fibers, in particular to a preparation method of a melt-spun anion polyamide fiber.
Background
The polyamide fiber (nylon) has excellent physical properties, high breaking strength, high wear resistance, good hygroscopicity, excellent elastic recovery rate and fatigue resistance, and good dyeing property, and is widely applied to the clothing field. In recent years, with social progress and continuous improvement of living standard of people, the demands of the masses on clothes are not simple and comfortable, warm-keeping and attractive, and more people begin to pursue health-preserving and health-care functions. Based on this demand, anion functional fibers have been developed. The anion fiber fabric can accelerate the emission of anions in the air in the human body movement process, and 82% of anions of the human body are absorbed through skin, and the skin is in direct contact with the anion fiber fabric, so that the health care function of the anion fabric can be exerted. The anion fabric not only can sterilize and disinfect, but also can promote blood circulation and metabolism, relieve muscle and joint pain and regulate a nervous system. Therefore, research and development of the fiber fabric with the function of releasing anions have important practical significance.
The anion generator represented by Qizhi stone is a kind of cyclic silicate mineral and contains multiple microelements such as magnesium, iron, tin, manganese, sodium, cobalt, silicon, fluorine, etc. The crystal structure belongs to a three-party or hexagonal crystal system, and the special crystal structure enables the crystal structure to form a piezoelectric effect and a pyroelectric effect under the external temperature and pressure change or spontaneous polarization effect, and charges are generated on the surface to ionize air molecules, so that anions are formed. At present, some research results have been accumulated on the anion fiber, and the patent 'an anion polyamide fiber and a manufacturing method (200710012497.9) thereof' discloses a preparation method of the anion polyamide fiber, which comprises the steps of preparing anion master batch after surface treatment of an anion generator and preparing the anion polyamide fiber by slicing and melt spinning. Although the method enhances the dispersion of the anion generator in the matrix of the master batch to a certain extent, the strong shearing action of the screw rod easily damages the effect of surface treatment in the process of melt blending spinning of the master batch and polyamide chips, so that the inorganic salt particles are agglomerated again, the stability and the anion function of spinning are damaged and weakened, and the processing steps of the method are complicated. Therefore, other modification methods need to be proposed while simplifying the process flow.
Disclosure of Invention
In order to overcome the problem of poor dispersibility of the negative ion generating agent in polyamide chips, the invention provides the preparation method of the melt-spun negative ion polyamide fiber, and the negative ion generating agent is always maintained in a melt state, so that the stability of surface modification and the high efficiency of functions of the negative ion generating agent are facilitated, the product performance is improved, and the production efficiency is also improved.
In order to achieve the above purpose, the present invention adopts the following technical scheme:
A method for preparing melt-spun anion polyamide fiber, which comprises the following steps:
(1) Blending a polymerization monomer and an auxiliary agent, and sequentially carrying out prepolymerization and final polymerization, wherein the auxiliary agent comprises a ring-opening agent, a blocking agent, a stabilizer and a negative ion generator treated by a compatibilizer modifier;
(2) At the same time of the final polymerization reaction or after the final polymerization reaction is finished, removing the monomer by using one or two combination of a disc evaporator and a cage evaporator to obtain a melt after the removal of the monomer;
(3) And directly granulating the melt after the singulation to obtain slices or directly spinning to obtain the anion polyamide fiber.
The method comprises the steps of preparing raw materials, and blending a polymerization monomer and various assistants. And (3) carrying out prepolymerization after uniformly stirring the raw materials to obtain the polyamide oligomer. And then heating the prepolymer for final polymerization, and carrying out polycondensation reaction between short chains to further increase the molecular weight, and obtaining the polyamide melt with high molecular weight after the final polymerization reaction is finished. The invention is characterized in that after the final coalescence, a disc evaporator or a cage evaporator is selected, and residual micromolecular substances in the polyamide melt are removed under specific process conditions, so that the liquid phase extraction of the polyamide is realized, the melt reaches the spinning standard, and the process can be controlled accurately. And then conveying the obtained melt after the removal of the single to a spinning box, and directly carrying out melt spinning and forming to obtain the anion polyamide fiber. The traditional polyamide 6 can only adopt an indirect spinning process, and the existing production flow is that the slice is extracted, dried and then melted for indirect spinning. After the step (3) of the process, other functional components can be added into the melt before the melt enters the spinning system.
Preferably, the polyamide is polyamide 6, polyamide 56, polyamide 610, polyamide 6-66 copolymer or polyamide 6-10 copolymer.
Preferably, the ring-opening agent in the step (1) is deionized water, the addition amount is 1-4wt% of the polymerized monomer, the end-capping agent is one or more of acetic acid, benzoic acid, terephthalic acid, decanediamine, oxalic acid and homologs thereof, the addition amount is 0.2-0.6wt% of the polymerized monomer, the stabilizer is one or more of SEED, salicylic acid, benzophenone benzotriazole, calcium carbonate and talcum powder, the addition amount is 0.1-0.5wt% of the polymerized monomer, and the addition amount of the negative ion generator treated by the compatibilizer modifier is 1-5wt% of the polymerized monomer.
Preferably, the anion generator in the step (1) is one or more of Qiyang stone, tourmaline, opal and Qiyang stone, the particle size is 100-300nm, and the compatibilizer modifier is one or more of 3-aminopropyl triethoxysilane, 3-aminopropyl trimethoxysilane and 3-isocyanic acid propyl triethoxysilane.
Preferably, the mass of the compatibilizing modifier is 0.02-2 times that of the negative ion generator.
Preferably, the treatment method of the anion generator in the step (1) comprises the steps of dispersing the anion generator in absolute ethyl alcohol, adjusting pH to be acidic, adding a compatibilizer modifier, uniformly dispersing, centrifuging, collecting a solid phase, and drying to obtain the functionalized modified anion generator.
Preferably, the pH is 3-5, the centrifugation is carried out at 3000-10000rpm for 3-10min, the centrifugation is repeated for 3-5 times, and the drying is carried out at 50-80 ℃ for 6-12h.
As a further preferable method, the anion generator is treated by adding inorganic salt anion generator into absolute ethyl alcohol to form suspension with concentration of 1-5wt%, adjusting pH to 3-5 with one or more of hydrochloric acid, glacial acetic acid and sulfuric acid, adding compatibilizer modifier with mass of 0.1-2% of that of the suspension, and magnetically stirring at 300-800rpm for 5-12h to uniformly disperse the anion generator in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 3000-10000rpm for 3-10min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3-5 times. Collecting the bottom sediment obtained by the last centrifugation, and drying in vacuum at 50-80 ℃ for 6-12h to obtain the functionalized modified anion generator.
Preferably, the pre-polymerization in the step (1) is carried out at the temperature of 190-260 ℃ and the absolute pressure of 0.1-3MPa for 2-10 hours.
Preferably, the final polymerization in step (1) is carried out at a temperature of 220-280 ℃ and an absolute pressure of 0.05-100kPa for 2-10 hours.
Preferably, the conditions of the step (2) of the deallocation are that the temperature is 240-280 ℃, the absolute pressure is 0.05-10kPa, the time is 0.1-4 hours, and the number average molecular weight of the melt after the deallocation is 25000-45000.
Therefore, the invention has the beneficial effects that:
(1) The method has the advantages of simple process, strong flexibility and wide application range, and the obtained melt after the removal of the single can be directly granulated to obtain functional slices, and can also be directly spun to obtain functional fibers.
(2) The newly added single removing section after the final polymerization section can replace the existing extraction step, reduce the content of small molecules, directly spin the melt, greatly simplify the process flow and greatly reduce the energy consumption.
(3) The negative ion generator is always maintained in a melt state, which is beneficial to the stability of surface modification and the high efficiency of functions. Not only improves the product performance, but also improves the production efficiency, simplifies the process flow, is beneficial to reducing the production cost, reduces the carbon emission and promotes the sustainable development of society and economy.
Detailed Description
The technical scheme of the invention is further described through specific embodiments.
In the present invention, unless otherwise specified, the materials and equipment used are commercially available or are commonly used in the art, and the methods in the examples are conventional in the art unless otherwise specified. Unless otherwise indicated, parts are parts by weight, temperatures are expressed in degrees Celsius or at ambient temperature and pressure is absolute. There are numerous variations and combinations of reaction conditions (e.g., component concentrations, solvents needed, solvent mixtures, temperatures, pressures, and other reaction ranges) that can be used to optimize the purity and yield of the product obtained by the process, with only reasonable routine experimentation to optimize such process conditions.
A method for preparing melt-spun anion polyamide fiber, which comprises the following steps:
(1) The preparation of the compatibilizer modifier treated anion generator comprises the steps of adding inorganic salt anion generator into absolute ethyl alcohol to form suspension with the concentration of 1-5wt%, adjusting the pH value to 3-5 by one or more of hydrochloric acid, glacial acetic acid and sulfuric acid, adding the compatibilizer modifier accounting for 0.1-2% of the mass of the suspension, and magnetically stirring at 300-800rpm for 5-12h to uniformly disperse the anion generator in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 3000-10000rpm for 3-10min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3-5 times. Collecting the bottom sediment obtained by the last centrifugation, and drying in vacuum at 50-80 ℃ for 6-12h to obtain the functionalized modified anion generator.
The anion generator is one or more of Qiyang stone, tourmaline, opal and Qiyang stone, and has particle diameter of 100-300nm. The compatibilizer modifier is one or more of 3-aminopropyl triethoxysilane, 3-aminopropyl trimethoxysilane and 3-isocyanatopropyl triethoxysilane. The mass of the compatibilizing modifier is 0.02-2 times of that of the negative ion generator.
(2) Compounding, namely blending the polymerized monomer and the auxiliary agent.
The polymerized monomer is polyamide 6, polyamide 56 or polyamide 6-66 copolymer, and is selected from caprolactam, pentanediamine, hexanediamine and adipic acid.
The auxiliary agent comprises a ring-opening agent, a blocking agent, a stabilizing agent and a negative ion generator treated by the compatibilizing modifier in the step (1). The ring-opening agent is deionized water, the addition amount is 1-4wt% of the polymerized monomer, the end-capping agent is one or more of acetic acid, benzoic acid, terephthalic acid, decanediamine, oxalic acid and homologs thereof, the addition amount is 0.2-0.6wt% of the polymerized monomer, the stabilizer is one or more of SEED, salicylic acid, benzophenone benzotriazole, calcium carbonate and talcum powder, the addition amount is 0.1-0.5wt% of the polymerized monomer, and the addition amount of the negative ion generator treated by the compatibilizer modifier is 1-5wt% of the polymerized monomer.
(3) And (3) performing polycondensation reaction, namely sequentially performing prepolymerization and final polymerization reaction.
The prepolymerization condition is that the temperature is 190-260 ℃, the absolute pressure is 0.1-3MPa, the time is 2-10h, and the number average molecular weight of the prepolymerized melt is 5000-15000.
The final polymerization condition is that the temperature is 220-280 ℃, the absolute pressure is 0.05-100kPa, the time is 2-10 hours, and the number average molecular weight of the final polymerization melt is 15000-30000.
(4) And (3) monomer removal treatment, namely removing the monomers by using one or two combinations of a disc evaporator and a cage evaporator at the same time of the final polymerization reaction or after the final polymerization reaction to obtain a melt after the monomer removal.
The conditions of the deallocation are that the temperature is 240-280 ℃, the absolute pressure is 0.05-10kPa, the time is 0.1-4 hours, and the number average molecular weight of the melt after the deallocation is 25000-45000.
(5) And directly granulating the melt after the singulation to obtain slices or directly spinning to obtain the anion polyamide fiber.
Example 1
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a compatibilizer modifier treated anion generator, namely adding 5g of Qixite nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form a suspension, adjusting the pH to 3.5 by hydrochloric acid, adding 1mL of 3-aminopropyl trimethoxy silane, and magnetically stirring at 800rpm for 12 hours to uniformly disperse Qixite in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 5000rpm for 5min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3 times. And collecting bottom sediment obtained by the last centrifugation, and drying the sediment in vacuum at 80 ℃ for 12 hours to obtain the silane functionalized Qizhongshi nano particles.
(2) Compounding 100kg caprolactam, 2kg deionized water, 0.4kg PTA, 0.2kg SEED and 1kg silane functionalized Qiyte were blended and stirred at 80℃for 2h.
(3) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 240 ℃, control the absolute pressure to 0.2MPa, react for 5 hours, then perform the final polymerization reaction, raise the temperature of the prepolymer to 260 ℃, control the pressure to 100kPa, and react for 5 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling temperature at 260 deg.C, absolute pressure at 0.1kPa, reacting for 2h, and number average molecular weight of melt after removing monomers 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Example 2
The difference from example 1 is that the silane-functionalized Qiyaku of step (2) has a mass of 5kg.
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a compatibilizer modifier treated anion generator, namely adding 5g of Qixite nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form a suspension, adjusting the pH to 3.5 by hydrochloric acid, adding 1mL of 3-aminopropyl trimethoxy silane, and magnetically stirring at 800rpm for 12 hours to uniformly disperse Qixite in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 5000rpm for 5min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3 times. And collecting bottom sediment obtained by the last centrifugation, and drying the sediment in vacuum at 80 ℃ for 12 hours to obtain the silane functionalized Qizhongshi nano particles.
(2) Compounding 100kg caprolactam, 2kg deionized water, 0.4kg PTA, 0.2kg SEED and 5kg silane functionalized Qiyte were blended and stirred at 80℃for 2h.
(3) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 240 ℃, control the absolute pressure to 0.2MPa, react for 5 hours, then perform the final polymerization reaction, raise the temperature of the prepolymer to 260 ℃, control the pressure to 100kPa, and react for 5 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling temperature at 260 deg.C, absolute pressure at 0.1kPa, reacting for 2h, and number average molecular weight of melt after removing monomers 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Comparative example 1
The difference from example 1 is that step (2) does not add silane functionalized qibing stone.
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Compounding 100kg caprolactam, 2kg deionized water, 0.4kg PTA and 0.2kg SEED were blended and stirred at 80℃for 2h.
(2) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 240 ℃, control the absolute pressure to 0.2MPa, react for 5 hours, then perform the final polymerization reaction, raise the temperature of the prepolymer to 260 ℃, control the pressure to 100kPa, and react for 5 hours.
(3) Removing monomers from final polymer by disc evaporator, controlling temperature at 260 deg.C, absolute pressure at 0.1kPa, reacting for 2h, and number average molecular weight of melt after removing monomers 25000-45000.
(4) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Comparative example 2
The difference from example 1 is that the silane-functionalized Qiyaku of step (2) has a mass of 0.3kg, which is less than the preferred range of 1-5wt%.
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a compatibilizer modifier treated anion generator, namely adding 5g of Qixite nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form a suspension, adjusting the pH to 3.5 by hydrochloric acid, adding 1mL of 3-aminopropyl trimethoxy silane, and magnetically stirring at 800rpm for 12 hours to uniformly disperse Qixite in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 5000rpm for 5min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3 times. And collecting bottom sediment obtained by the last centrifugation, and drying the sediment in vacuum at 80 ℃ for 12 hours to obtain the silane functionalized Qizhongshi nano particles.
(2) Compounding 100kg caprolactam, 2kg deionized water, 0.4kg PTA, 0.2kg SEED and 0.3kg silane functionalized Qiyte were blended and stirred at 80℃for 2h.
(3) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 240 ℃, control the absolute pressure to 0.2MPa, react for 5 hours, then perform the final polymerization reaction, raise the temperature of the prepolymer to 260 ℃, control the pressure to 100kPa, and react for 5 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling temperature at 260 deg.C, absolute pressure at 0.1kPa, reacting for 2h, and number average molecular weight of melt after removing monomers 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Comparative example 3
The difference from example 1 is that the silane-functionalized Qiyaku of step (2) has a mass of 8kg, which is in excess of the preferred range of 1 to 5% by weight.
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a compatibilizer modifier treated anion generator, namely adding 5g of Qixite nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form a suspension, adjusting the pH to 3.5 by hydrochloric acid, adding 1mL of 3-aminopropyl trimethoxy silane, and magnetically stirring at 800rpm for 12 hours to uniformly disperse Qixite in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 5000rpm for 5min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3 times. And collecting bottom sediment obtained by the last centrifugation, and drying the sediment in vacuum at 80 ℃ for 12 hours to obtain the silane functionalized Qizhongshi nano particles.
(2) Compounding 100kg caprolactam, 2kg deionized water, 0.4kg PTA, 0.2kg SEED and 8kg silane functionalized Qiyte were blended and stirred at 80℃for 2h.
(3) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 240 ℃, control the absolute pressure to 0.2MPa, react for 5 hours, then perform the final polymerization reaction, raise the temperature of the prepolymer to 260 ℃, control the pressure to 100kPa, and react for 5 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling temperature at 260 deg.C, absolute pressure at 0.1kPa, reacting for 2h, and number average molecular weight of melt after removing monomers 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Example 3
The difference from example 2 is that the anion generator in step (1) is tourmaline and the compatibilizer modifier is 3-isocyanatopropyl triethoxysilane.
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a compatibilizer modifier treated anion generator, namely adding 5g of tourmaline nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form suspension, adjusting the pH to 3.5 by hydrochloric acid, adding 1mL of 3-isocyanatopropyl triethoxysilane, and magnetically stirring at 800rpm for 12 hours to uniformly disperse the tourmaline in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 5000rpm for 5min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3 times. Collecting the bottom sediment obtained by the last centrifugation, and vacuum drying at 80 ℃ for 12 hours to obtain the silane functionalized tourmaline nano particles.
(2) Compounding 100kg caprolactam, 2kg deionized water, 0.4kg PTA, 0.2kg SEED and 1kg silane functional tourmaline were blended and stirred at 80 ℃ for 2 hours.
(3) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 240 ℃, control the absolute pressure to 0.2MPa, react for 5 hours, then perform the final polymerization reaction, raise the temperature of the prepolymer to 260 ℃, control the pressure to 100kPa, and react for 5 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling temperature at 260 deg.C, absolute pressure at 0.1kPa, reacting for 2h, and number average molecular weight of melt after removing monomers 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Example 4
The difference from example 2 is that the negative ion generator in step (1) is opal and the compatibilizer modifier is 3-aminopropyl triethoxysilane.
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a negative ion generator treated by the compatibilizer modifier, namely adding 5g of opal nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form a suspension, adjusting the pH to 3.5 by hydrochloric acid, adding 1mL of 3-aminopropyl triethoxysilane, and magnetically stirring at 800rpm for 12 hours to uniformly disperse the opal in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 5000rpm for 5min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3 times. And collecting bottom sediment obtained by the last centrifugation, and drying the sediment in vacuum at 80 ℃ for 12 hours to obtain the silane functionalized opal nano particles.
(2) The ingredients were blended 100kg caprolactam, 2kg deionized water, 0.4kg PTA, 0.2kg SEED and 1kg silane functionalized opal and stirred at 80℃for 2h.
(3) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 240 ℃, control the absolute pressure to 0.2MPa, react for 5 hours, then perform the final polymerization reaction, raise the temperature of the prepolymer to 260 ℃, control the pressure to 100kPa, and react for 5 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling temperature at 260 deg.C, absolute pressure at 0.1kPa, reacting for 2h, and number average molecular weight of melt after removing monomers 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Example 5
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) As in example 1.
(2) Compounding, namely blending 55kg of adipic acid and 45kg of pentanediamine with 0.3L of water respectively, and stirring for 1h to dissolve. Mixing adipic acid and hexamethylenediamine solution, continuously stirring for 1h, fully cooling, filtering, performing true drying at 60 ℃ for 5h to obtain polyamide 56 salt, and adding 0.4kg of PTA, 0.2kg of SEED and 5kg of silane functionalized Qiyaku for blending to obtain a polymerization raw material.
(3) The polycondensation reaction is to perform the prepolymerization reaction, heat the raw materials to 220 ℃, control the absolute pressure to 1.5MPa, react for 3 hours, then perform the final polymerization reaction, heat the prepolymer to 260 ℃, control the pressure to 10kPa, and react for 3 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling the temperature to 270 deg.C, absolute pressure to 0.1kPa, reacting for 0.1h, and obtaining melt with number average molecular weight 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 255 ℃, and obtaining the functionalized anion polyamide 56 fiber.
Example 6
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) As in example 1.
(2) Blending 80kg of caprolactam and 20kg of polyamide 66 salt, adding 10kg of water, 0.4kg of PTA, 0.2kg of SEED and 5kg of silane functionalized Qiyaku, and blending to obtain a polymerization raw material.
(3) The polycondensation reaction is to perform the prepolymerization reaction, raise the temperature of the raw materials to 200 ℃, control the absolute pressure to 1.5MPa, react for 3 hours, and then perform the final polymerization reaction, raise the temperature of the prepolymer to 270 ℃, control the pressure to 10kPa, and react for 3 hours.
(4) Removing monomers from final polymer by disc evaporator, controlling the temperature to 280 deg.C, absolute pressure to 0.1kPa, reacting for 0.5h, and obtaining melt with number average molecular weight 25000-45000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the monomers to a spinning system for spinning, wherein the spinning temperature is 280 ℃, and obtaining the functionalized anion polyamide 6-66 copolymer fiber.
Example 7
The difference from example 1 is that the final polymerization and the dealkylation are carried out simultaneously, the temperature is raised to 260 ℃ after the end of the pre-polymerization, the pressure is controlled to be 0.1kPa, the reaction is carried out for 7 hours, and the number average molecular weight of the melt after the final polymerization and the dealkylation is 15000-30000.
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a compatibilizer modifier treated anion generator, namely adding 5g of Qixite nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form a suspension, adjusting the pH to 3.5 by hydrochloric acid, adding 1mL of 3-aminopropyl trimethoxy silane, and magnetically stirring at 800rpm for 12 hours to uniformly disperse Qixite in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotating speed is 5000rpm for 5min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 3 times. And collecting bottom sediment obtained by the last centrifugation, and drying the sediment in vacuum at 80 ℃ for 12 hours to obtain the silane functionalized Qizhongshi nano particles.
(2) Compounding 100kg caprolactam, 2kg deionized water, 0.4kg PTA, 0.2kg SEED and 1kg silane functionalized Qiyte were blended and stirred at 80℃for 2h.
(3) The prepolymerization reaction is carried out firstly, the temperature of the raw materials is raised to 240 ℃, the absolute pressure is controlled to be 0.2MPa, and the prepolymer is obtained after the reaction for 5 hours.
(4) Polycondensation and deallocation, namely heating the prepolymer to 260 ℃, controlling the pressure to 0.1kPa, reacting for 7 hours, and finally polymerizing and deallocation, wherein the number average molecular weight of the melt after the deallocation is 15000-30000.
(5) And (3) spinning, namely directly conveying the melt after the removal of the single to a spinning system for spinning, wherein the spinning temperature is 260 ℃, and obtaining the functionalized anion polyamide 6 fiber.
Example 8
A preparation method of a melt-spun anion polyamide fiber comprises the following steps:
(1) Preparing a compatibilizer modifier treated anion generator, namely adding 3g of Qixite nano particles with the particle size of 200nm into 100mL of absolute ethyl alcohol to form a suspension, adjusting the pH to 5 by hydrochloric acid, adding 2mL of 3-aminopropyl trimethoxysilane, and magnetically stirring at 500rpm for 8 hours to uniformly disperse Qixite in the mixed solution. And (3) after stirring, carrying out centrifugal washing on the mixed solution, wherein the centrifugal rotation speed is 10000rpm for 3min, pouring out supernatant after centrifugation, taking out bottom sediment, adding absolute ethyl alcohol, continuously carrying out centrifugal washing, and repeating the steps for 4 times. And collecting bottom sediment obtained by the last centrifugation, and vacuum drying at 60 ℃ for 10 hours to obtain the silane functionalized Qizhongshi nano particles.
(2) The ingredients were 100kg caprolactam, 4kg deionized water, 0.6kg acetic acid, 0.2kg talc and 1kg silane functionalized Qiyaku blended and stirred at 80℃for 2h.
(3) The polycondensation reaction comprises the steps of pre-polymerizing, heating raw materials to 260 ℃, controlling the absolute pressure to 3MPa, reacting for 2 hours, controlling the number average molecular weight of the pre-polymerized melt to 15000, then final polymerizing, heating the pre-polymer to 280 ℃, controlling the pressure to 80kPa, reacting for 2 hours, and controlling the number average molecular weight of the final polymerized melt to 30000.
(4) The process of removing monomers includes removing monomers from final polymer by combination of disc evaporator and cage evaporator, controlling temp. to 240 deg.C, absolute pressure to 0.05kPa, reacting for 0.1h, and obtaining melt with number average molecular weight of 45000.
(5) Spinning, namely directly granulating the melt after the single removal to obtain slices.
Comparative example 4
The difference from example 1 is that the step (4) of the singulation process is not performed. As a result, the fiber is difficult to form during spinning and cannot be spun.
Performance testing
The fibers obtained in each of the above examples and comparative examples were subjected to performance testing using GB/T14344-2008. The results are shown in the following table.
Table 1 fiber index for each example and comparative example
From the table above, it can be seen that:
(1) From examples 2,3 and 4, various options and combinations of the negative ion generating agent and the modifying agent are known. From examples 2, 5, and 6, the polyamide melt direct spinning process according to the present invention is applicable to a variety of polyamide materials, including but not limited to polyamide 6, polyamide 56, and polyamide 6-66 copolymers. As is clear from examples 1 and 7, the dealkylation treatment may be performed after the completion of the final polymerization or may be performed simultaneously with the final polymerization.
(2) As is clear from comparative example 1, example 1 and example 2, under the same polymerization conditions, the amount of negative ions generated by the fiber is the lowest, only 1090 negative ions per cm 3, and the amount of negative ions generated by the fiber is obviously improved from 1wt% to 5wt% along with the addition of the functional negative ion generating agent, which means that the functional negative ion generating agent has a direct effect on the amount of negative ions generated by the fiber and has no obvious effect on the relative molecular mass and strength of the fiber within the range.
(3) As is clear from comparative example 2 and example 1, the amount of the functionalized anion generator added was low and the anion generating effect of the fiber was poor under the same conditions. As is clear from comparative example 3 and example 1, when the addition amount of the functionalized anion generator exceeds the range, the strength of the fiber is significantly reduced because the introduction of the inorganic auxiliary agent damages the orientation of the molecular weight to some extent, and the crystallinity of the polymer is affected, resulting in a reduction in strength, indicating that the excessively high addition amount of the functionalized anion generator adversely affects the performance of the direct spinning fiber. However, when the addition amount of the functional negative ion generating agent exceeds the range, the method can be adopted, and melt after the removal of the monomers is not input into a spinning system, so that the functional master batch is obtained.
(4) As is clear from comparative example 4 and example 1, under the same conditions, the melt which is not subjected to the removal of the monomers is not spun directly after being fed into the spinning system, and the fiber is difficult to form, because the removed melt contains about 8wt% of caprolactam monomer, and the existence of the caprolactam monomer causes stress concentration of the melt during the fiber forming, so that the monofilament is broken. Therefore, the monomer removal system plays a vital role in the direct spinning process of the polyamide melt.
The present invention is not limited to the preferred embodiments, and the present invention is described above in any way, but is not limited to the preferred embodiments, and any person skilled in the art will appreciate that the present invention is not limited to the embodiments described above, while the above disclosure is directed to various equivalent embodiments, which are capable of being modified or varied in several ways, any simple modification, equivalent changes and variation of the above embodiments according to the technical principles of the present invention will still fall within the scope of the present invention.

Claims (10)

1.一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,包括以下步骤:1. A method for preparing melt-spinnable anionic polyamide fiber, characterized in that it comprises the following steps: (1)将聚合单体与助剂共混,依次进行预聚、终聚反应;所述助剂包括开环剂、封端剂、稳定剂和经过增容改性剂处理的负离子发生剂;(1) mixing the polymerization monomers with the auxiliary agents, and sequentially performing prepolymerization and final polymerization reactions; the auxiliary agents include a ring-opening agent, an end-capping agent, a stabilizer, and a negative ion generator treated with a volume-increasing modifier; (2)在终聚反应的同时或终聚反应结束后,用圆盘蒸发器、笼式蒸发器的一种或两种组合进行单体脱除,得到脱单后熔体;(2) During or after the final polymerization reaction, the monomer is removed by using a disc evaporator, a cage evaporator or a combination of both to obtain a melt after monomer removal; (3)脱单后熔体直接切粒得切片或直接纺丝,制得负离子聚酰胺纤维。(3) After stripping, the melt is directly pelletized to obtain slices or directly spun to produce negative ion polyamide fibers. 2.根据权利要求1所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,聚酰胺为聚酰胺6、聚酰胺56、聚酰胺610、聚酰胺6-66共聚物或聚酰胺6-10共聚物。2. The method for preparing a melt-spinnable anionic polyamide fiber according to claim 1, characterized in that the polyamide is polyamide 6, polyamide 56, polyamide 610, polyamide 6-66 copolymer or polyamide 6-10 copolymer. 3.根据权利要求1所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,步骤(1)的开环剂添加量为聚合单体的1-4wt%;封端剂为醋酸、苯甲酸、对苯二甲酸、癸二胺、乙二酸及其同系物中的一种或多种,添加量为聚合单体的0.2-0.6wt%;稳定剂为SEED、水杨酸、二苯甲酮系苯并三唑系、碳酸钙和滑石粉中的一种或多种,添加量为聚合单体的0.1-0.5wt%;增容改性剂处理的负离子发生剂的添加量为聚合单体的1-5wt%。3. The method for preparing a melt-spinnable anionic polyamide fiber according to claim 1 is characterized in that the amount of the ring-opening agent added in step (1) is 1-4wt% of the polymerized monomer; the end-capping agent is one or more of acetic acid, benzoic acid, terephthalic acid, decanediamine, oxalic acid and their homologues, and the amount added is 0.2-0.6wt% of the polymerized monomer; the stabilizer is one or more of SEED, salicylic acid, benzophenone series benzotriazole series, calcium carbonate and talcum powder, and the amount added is 0.1-0.5wt% of the polymerized monomer; the amount of the anionic generator treated with a volume-increasing modifier is 1-5wt% of the polymerized monomer. 4.根据权利要求1或3所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,步骤(1)的负离子发生剂为奇冰石、电气石、蛋白石、奇才石中的一种或多种,粒径为100-300 nm;增容改性剂为3-氨丙基三乙氧基硅烷、3-氨丙基三甲氧基硅烷、3-异氰酸丙基三乙氧基硅烷中的一种或几种。4. A method for preparing a melt-spinnable anion polyamide fiber according to claim 1 or 3, characterized in that the anion generator in step (1) is one or more of quartz, tourmaline, opal, and quartz, with a particle size of 100-300 nm; the volume-increasing modifier is one or more of 3-aminopropyltriethoxysilane, 3-aminopropyltrimethoxysilane, and 3-isocyanatepropyltriethoxysilane. 5.根据权利要求4所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,增容改性剂的质量为负离子发生剂的0.02-2倍。5. The method for preparing a melt-spinnable anion polyamide fiber according to claim 4, characterized in that the mass of the volume-increasing modifier is 0.02-2 times that of the anion generator. 6.根据权利要求1所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,步骤(1)的负离子发生剂的处理方法为:将负离子发生剂分散在无水乙醇中,调pH至酸性;加入增容改性剂,分散均匀;离心、收集固相、干燥,得功能化改性负离子发生剂。6. The method for preparing a melt-spinnable anion polyamide fiber according to claim 1, characterized in that the treatment method of the anion generator in step (1) is: dispersing the anion generator in anhydrous ethanol and adjusting the pH to acidic; adding a volume-increasing modifier and dispersing it evenly; centrifuging, collecting the solid phase, and drying to obtain a functionalized modified anion generator. 7.根据权利要求6所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,pH为3-5;离心为转速3000-10000 rpm下离心3-10 min,重复3-5次;干燥为50-80 ℃真空干燥6-12 h。7. The method for preparing a melt-spinnable anionic polyamide fiber according to claim 6, characterized in that the pH is 3-5; the centrifugation is performed at a speed of 3000-10000 rpm for 3-10 min, repeated 3-5 times; and the drying is performed at 50-80°C vacuum drying for 6-12 h. 8.根据权利要求1所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,步骤(1)预聚的条件为:温度190-260 ℃,绝对压力0.1-3 MPa,时间2-10 h。8. The method for preparing a melt-spinnable anionic polyamide fiber according to claim 1, characterized in that the prepolymerization conditions in step (1) are: temperature 190-260°C, absolute pressure 0.1-3 MPa, and time 2-10 h. 9.根据权利要求1所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,步骤(1)终聚的条件为:温度220-280 ℃,绝对压力0.05-100 kPa,时间2-10 h。9. The method for preparing a melt-spinnable anionic polyamide fiber according to claim 1, characterized in that the conditions for final polymerization in step (1) are: temperature 220-280°C, absolute pressure 0.05-100 kPa, and time 2-10 h. 10.根据权利要求1或8或9所述的一种可熔体直纺的负离子聚酰胺纤维的制备方法,其特征在于,步骤(2)脱单的条件为:温度240-280 ℃,绝对压力0.05-10 kPa,时间0.1-4 h;脱单后熔体数均分子量25000-45000。10. A method for preparing melt-spinnable anionic polyamide fibers according to claim 1, 8 or 9, characterized in that the conditions for removing the single atoms in step (2) are: temperature 240-280°C, absolute pressure 0.05-10 kPa, time 0.1-4 h; and the number average molecular weight of the melt after removing the single atoms is 25000-45000.
CN202410220344.7A 2024-02-28 2024-02-28 Preparation method of melt-spun anion polyamide fiber Pending CN119663473A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202410220344.7A CN119663473A (en) 2024-02-28 2024-02-28 Preparation method of melt-spun anion polyamide fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202410220344.7A CN119663473A (en) 2024-02-28 2024-02-28 Preparation method of melt-spun anion polyamide fiber

Publications (1)

Publication Number Publication Date
CN119663473A true CN119663473A (en) 2025-03-21

Family

ID=94999451

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202410220344.7A Pending CN119663473A (en) 2024-02-28 2024-02-28 Preparation method of melt-spun anion polyamide fiber

Country Status (1)

Country Link
CN (1) CN119663473A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103061038A (en) * 2012-12-14 2013-04-24 浙江理工大学 Tourmaline electret polylactic acid melt-blown non-woven cloth and manufacture method
CN108192092A (en) * 2017-12-30 2018-06-22 常州恒利宝纳米新材料科技有限公司 A kind of graphene oxide, tourmaline powder, polyamide 6 composite material and preparation method thereof
CN109208149A (en) * 2017-07-05 2019-01-15 上海水星家用纺织品股份有限公司 The method for weaving of Strange ice stone fiber home textile fabric
CN111575825A (en) * 2020-03-20 2020-08-25 浙江恒澜科技有限公司 Method for preparing functionalized nylon 6 fibers based on melt direct spinning technology
CN113429591A (en) * 2021-06-08 2021-09-24 由吉春 Functional master batch, polymer material, preparation method and post-treatment method thereof
CN114990888A (en) * 2022-06-10 2022-09-02 王应剑 Easily-cleaned antibacterial negative ion mattress and preparation method thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103061038A (en) * 2012-12-14 2013-04-24 浙江理工大学 Tourmaline electret polylactic acid melt-blown non-woven cloth and manufacture method
CN109208149A (en) * 2017-07-05 2019-01-15 上海水星家用纺织品股份有限公司 The method for weaving of Strange ice stone fiber home textile fabric
CN108192092A (en) * 2017-12-30 2018-06-22 常州恒利宝纳米新材料科技有限公司 A kind of graphene oxide, tourmaline powder, polyamide 6 composite material and preparation method thereof
CN111575825A (en) * 2020-03-20 2020-08-25 浙江恒澜科技有限公司 Method for preparing functionalized nylon 6 fibers based on melt direct spinning technology
CN113429591A (en) * 2021-06-08 2021-09-24 由吉春 Functional master batch, polymer material, preparation method and post-treatment method thereof
CN114990888A (en) * 2022-06-10 2022-09-02 王应剑 Easily-cleaned antibacterial negative ion mattress and preparation method thereof

Similar Documents

Publication Publication Date Title
CN108192092B (en) A kind of graphene oxide, tourmaline powder, polyamide 6 composite material and preparation method thereof
CN105295028B (en) A kind of graphene in-situ modified poly-lactam composite and preparation method and application
CN107385542B (en) A kind of preparation method and application of the nylon compound resin and its fiber that POSS grafted graphene oxide is modified
CN111393633B (en) Caprolactam polymerization method capable of realizing direct melt processing
CN114351276A (en) High-strength para-aramid fiber and preparation method thereof
CN111607838A (en) Slow-release aromatic polyester fiber and preparation method thereof
CN116024818A (en) A kind of sizing agent and its preparation method and application
CN119663473A (en) Preparation method of melt-spun anion polyamide fiber
CN118222075A (en) A polylactic acid nanocomposite material with full stereocomposite crystal and preparation method thereof
CN106750271A (en) The preparation method of nano silicon reinforced nylon 6 composite
CN111363141B (en) A kind of continuous hydrolysis polymerization method of green recycling caprolactam
CN109761816A (en) One birdss of the same feather flock together (hydroxyl) to penylene benzo diimidazole-benzoxazoles PBIO liquid crystal copolymer and monomer, preparation and application
CN118326549B (en) A method for preparing plant-derived aerogel fiber
CN109161187A (en) A kind of high-wearing feature graphene nylon 6 composite material preparation method
CN108059720B (en) Graphene oxide, sericite and polyamide 6 composite material and preparation method thereof
CN118773763A (en) Nylon fiber containing herb and trace elements and preparation method thereof
CN113845647B (en) Preparation method of special material for producing in-situ polymerized antibacterial polyester flat filaments
JPS59130315A (en) Continuous liquid phase process for melt spinning acrylonitrile polymer
CN106866957B (en) A kind of preparation method of nanometer of copper ion differentiation slices of caprone
CN105399893B (en) Preparation method of acrylate polymer/montmorillonite composite particles for toughening makrolon
CN113831727A (en) Graphene modified polyamide composite material and preparation method thereof
JPH0333730B2 (en)
CN116180261A (en) A kind of high-strength yarn for polyamide 56 airbag yarn and its preparation method
CN116554462B (en) Antistatic polyamide composite material and preparation method thereof
CN112745657B (en) Anti-slip thermoplastic polyurethane composite material and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination