CN103642065A - Process of regenerating nylon 6 and nylon 66 from waste carpet by selective dissolving-precipitating method - Google Patents
Process of regenerating nylon 6 and nylon 66 from waste carpet by selective dissolving-precipitating method Download PDFInfo
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- 239000002699 waste material Substances 0.000 title claims abstract description 31
- 229920002292 Nylon 6 Polymers 0.000 title claims abstract description 30
- 229920002302 Nylon 6,6 Polymers 0.000 title claims abstract description 29
- 238000000034 method Methods 0.000 title claims abstract description 27
- 230000001172 regenerating effect Effects 0.000 title claims abstract 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000001556 precipitation Methods 0.000 claims abstract description 10
- 239000002244 precipitate Substances 0.000 claims description 30
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 28
- 239000008367 deionised water Substances 0.000 claims description 26
- 229910021641 deionized water Inorganic materials 0.000 claims description 26
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 18
- 239000000835 fiber Substances 0.000 claims description 16
- 239000000706 filtrate Substances 0.000 claims description 15
- 238000006243 chemical reaction Methods 0.000 claims description 10
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 9
- 235000019253 formic acid Nutrition 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 8
- 239000003153 chemical reaction reagent Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000000047 product Substances 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims 3
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- 230000035484 reaction time Effects 0.000 claims 1
- 150000003462 sulfoxides Chemical class 0.000 claims 1
- 238000004064 recycling Methods 0.000 abstract description 14
- 239000004677 Nylon Substances 0.000 abstract description 4
- 229920001778 nylon Polymers 0.000 abstract description 4
- 239000003960 organic solvent Substances 0.000 abstract description 3
- 239000003795 chemical substances by application Substances 0.000 abstract description 2
- 230000001376 precipitating effect Effects 0.000 abstract description 2
- 238000004821 distillation Methods 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 5
- 238000010992 reflux Methods 0.000 description 4
- 239000002861 polymer material Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- -1 polyhexamethylene adipate Polymers 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000002174 Styrene-butadiene Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000011115 styrene butadiene Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
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- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
本发明涉及一种选择性溶解-沉淀方法从废旧尼龙中再生尼龙6和尼龙66的工艺。其特征是利用不同的有机溶剂选择性的溶解尼龙6和尼龙66,以水作为沉淀剂,从有机溶剂中再生获得尼龙6和尼龙66的工艺。本发明具有操作简单、回收利用率高等特点,可以有效的回收利用废旧地毯中尼龙6和尼龙66,避免资源浪费,同时也为废旧地毯的工业化回收利用探索了新工艺。The invention relates to a process for regenerating nylon 6 and nylon 66 from waste nylon by a selective dissolution-precipitation method. It is characterized in the process of using different organic solvents to selectively dissolve nylon 6 and nylon 66, and using water as a precipitating agent to regenerate nylon 6 and nylon 66 from organic solvents. The invention has the characteristics of simple operation and high recycling rate, can effectively recycle nylon 6 and nylon 66 in waste carpets, avoid waste of resources, and also explores a new process for industrial recycling of waste carpets.
Description
技术领域technical field
本发明涉及一种利用有机溶剂选择性溶解废旧地毯,以去离子水为沉淀剂,获得尼龙6和尼龙66的工艺。属于高分子聚合物回收应用技术领域。The invention relates to a process for selectively dissolving waste carpets with an organic solvent and using deionized water as a precipitating agent to obtain nylon 6 and nylon 66. The invention belongs to the technical field of high molecular polymer recycling application.
背景技术Background technique
高分子材料具有良好的功能性和实用性,从而促进了高分子材料的迅速发展,高分子材料带给人们生活方便的同时也引发了严重的废旧聚合物的污染问题,因此通过技术处理最大限度的回收再生废旧聚合物,保持社会可持续发展,使废旧聚合物实现再资源化引起了人们的广泛关注。Polymer materials have good functionality and practicability, which promotes the rapid development of polymer materials. While polymer materials bring convenience to people's lives, they also cause serious pollution problems of waste polymers. The recycling of waste polymers, maintaining the sustainable development of society, and realizing the recycling of waste polymers have aroused widespread concern.
尼龙地毯是最早大量使用的化纤类地毯,具有耐磨性、强度高和耐酸碱等优异特征。废旧尼龙地毯主要由尼龙6(聚己内酰胺)和尼龙66(聚己二酸己二胺)纤维构成的绒面,聚丙烯衬层,填充了大量的碳酸钙的丁苯胶乳胶黏剂组成。目前废旧地毯的处理方法主要包括填埋回收、能量回收、材料回收和化学回收。随着社会倡导环境保护、绿色经济、循环经济和可持续发展的理念的不断发展,从废旧地毯中再生尼龙6和尼龙66用于循环利用越来越受到大家的重视。Nylon carpet is the earliest chemical fiber carpet used in large quantities. It has excellent characteristics such as wear resistance, high strength and acid and alkali resistance. The waste nylon carpet is mainly composed of suede made of nylon 6 (polycaprolactam) and nylon 66 (polyhexamethylene adipate) fibers, polypropylene lining, and styrene-butadiene latex adhesive filled with a large amount of calcium carbonate. At present, the treatment methods of waste carpet mainly include landfill recycling, energy recovery, material recovery and chemical recovery. With the continuous development of the concept of environmental protection, green economy, circular economy and sustainable development advocated by the society, the recycling of nylon 6 and nylon 66 from waste carpets has attracted more and more attention.
发明内容Contents of the invention
本发明的主要目的是提供一种化学循环的工艺从废旧地毯中再生获得尼龙6和尼龙66,能将废旧地毯中的有效的成分(尼龙6和尼龙66)实现再资源化利用。该工艺具有回收利用率高、再生产品质量高、工艺操作简单等优点,可以有效的实现资源的循环利用,降低尼龙地毯的生产成本,具有工业化推广的前景。The main purpose of the present invention is to provide a chemical recycling process to regenerate nylon 6 and nylon 66 from waste carpets, which can realize recycling of effective components (nylon 6 and nylon 66) in waste carpets. The process has the advantages of high recycling rate, high quality of recycled products, simple process operation, etc., can effectively realize the recycling of resources, reduce the production cost of nylon carpet, and has the prospect of industrialization promotion.
本发明具体采用如下的技术方案:The present invention specifically adopts the following technical solutions:
一种选择性溶解-沉淀方法从废旧地毯中再生尼龙6和尼龙66的工艺,其特征主要包括如下步骤:A kind of selective dissolution-precipitation method regenerates the technique of nylon 6 and nylon 66 from waste and old carpet, its feature mainly comprises the following steps:
(1).将废旧地毯粉碎、筛分处理获得粗纤维。(1). Crush and sieve waste carpets to obtain crude fibers.
(2).将处理后的粗纤维和溶剂二甲基亚砜按质量比1:8~10混合,在110℃~130℃下加热搅拌,恒温60分钟。(2). Mix the treated crude fiber and solvent dimethyl sulfoxide at a mass ratio of 1:8-10, heat and stir at 110°C-130°C, and keep the temperature constant for 60 minutes.
(3).然后趁热过滤,并且用热的二甲基亚砜冲洗未溶解的残留物,然后向所得的滤液中加入去离子水,可以看到有沉淀析出,沉淀为尼龙6,再过滤出沉淀,用去离子水洗涤三次,干燥。(3). Then filter while it is hot, and rinse the undissolved residue with hot dimethyl sulfoxide, then add deionized water to the obtained filtrate, you can see that there is precipitation, the precipitate is nylon 6, and then filter The precipitate was washed three times with deionized water and dried.
(4).将步骤3中剩余的残留物和甲酸按照质量比1:10~15混合,在室温下搅拌60分钟。(4). Mix the remaining residue in step 3 and formic acid in a mass ratio of 1:10-15, and stir at room temperature for 60 minutes.
(5).过滤,然后向所得的滤液中加入去离子水,可以看到有沉淀析出,沉淀为尼龙66,再过滤出沉淀,用去离子水洗涤三次,干燥。(5). Filtrate, then add deionized water to the obtained filtrate, it can be seen that there is a precipitate, which is nylon 66, then filter the precipitate, wash with deionized water three times, and dry.
(6).收集反应中使用的试剂,蒸馏分离,重复循环利用。(6). The reagents used in the reaction are collected, separated by distillation, and recycled repeatedly.
本发明的优点:能将废旧地毯再生转化为有价值的资源,不仅有效的缓解了废旧聚合物的污染问题,而且有利于社会的可持续发展;工艺简单,回收利用率高,回收再生产品质量高;充分实现了废旧资源的再资源化利用,能耗低,符合环保要求;回收再生过程中用到的二甲基亚砜、甲酸和去离子水可以通过蒸馏的方式分离,循环利用,降低了生产成本,具有工业化应用的前景。The advantages of the present invention: it can regenerate waste carpets into valuable resources, which not only effectively alleviates the pollution of waste polymers, but also contributes to the sustainable development of society; the process is simple, the recycling rate is high, and the quality of recycled products is high. High; fully realize the recycling of waste resources, low energy consumption, in line with environmental protection requirements; dimethyl sulfoxide, formic acid and deionized water used in the recycling process can be separated by distillation and recycled, reducing The production cost is reduced, and it has the prospect of industrial application.
具体实施方式Detailed ways
实施例1Example 1
将废旧地毯粉碎、筛分处理获得粗纤维。在顶部装有冷凝回流装置的50ml的三口烧瓶中按质量比1:8将处理后的粗纤维与二甲基亚砜混合,加热搅拌,温度控制在110℃~130℃,恒温60分钟,然后过滤,并用热的二甲基亚砜冲洗残留物,向所得的滤液中添加适量去离子水,有沉淀析出,沉淀为尼龙6,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。同时将残留物与甲酸按质量比1:10在室温下混合搅拌60分钟,然后过滤,向滤液中添加适量的去离子水,有沉淀析出,沉淀为尼龙66,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。收集反应中使用的试剂,蒸馏分离,重复循环利用。尼龙6的产率为13.62%,尼龙66的产率为56.58%。The waste carpets are crushed and sieved to obtain crude fibers. In a 50ml three-necked flask equipped with a condensing reflux device on the top, mix the treated crude fiber with dimethyl sulfoxide at a mass ratio of 1:8, heat and stir, and control the temperature at 110°C to 130°C, and keep the temperature constant for 60 minutes, then Filter, and wash the residue with hot dimethyl sulfoxide, add an appropriate amount of deionized water to the obtained filtrate, a precipitate is precipitated, and the precipitate is nylon 6, filter the precipitate, wash with deionized water three times, and then vacuum at 60 ° C Let dry for 12 hours. At the same time, the residue and formic acid were mixed and stirred at room temperature for 60 minutes at a mass ratio of 1:10, then filtered, and an appropriate amount of deionized water was added to the filtrate, and a precipitate was precipitated, which was nylon 66. The precipitate was filtered and washed with deionized water three times, and then dried under vacuum at 60 °C for 12 hours. The reagents used in the reaction are collected, separated by distillation, and recycled repeatedly. The yield of nylon 6 was 13.62%, and that of nylon 66 was 56.58%.
实施例2Example 2
将废旧地毯粉碎、筛分处理获得粗纤维。在顶部装有冷凝回流装置的50ml的三口烧瓶中按质量比1:10将处理后的粗纤维与二甲基亚砜混合,加热搅拌,温度控制在110℃~130℃,恒温60分钟,然后过滤,并用热的二甲基亚砜冲洗残留物,向所得的滤液中添加适量去离子水,有沉淀析出,沉淀为尼龙6,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。同时将残留物与甲酸按质量比1:10在室温下混合搅拌60分钟,然后过滤,向滤液中添加适量的去离子水,有沉淀析出,沉淀为尼龙66,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。收集反应中使用的试剂,蒸馏分离,重复循环利用。尼龙6的产率为14.06%,尼龙66的产率为57.17%。The waste carpets are crushed and sieved to obtain crude fibers. In a 50ml three-neck flask equipped with a condensing reflux device on the top, mix the treated crude fiber with dimethyl sulfoxide at a mass ratio of 1:10, heat and stir, and control the temperature at 110°C to 130°C for 60 minutes at a constant temperature, then Filter, and wash the residue with hot dimethyl sulfoxide, add an appropriate amount of deionized water to the obtained filtrate, a precipitate is precipitated, and the precipitate is nylon 6, filter the precipitate, wash with deionized water three times, and then vacuum at 60 ° C Let dry for 12 hours. At the same time, the residue and formic acid were mixed and stirred at room temperature for 60 minutes at a mass ratio of 1:10, then filtered, and an appropriate amount of deionized water was added to the filtrate, and a precipitate was precipitated, which was nylon 66. The precipitate was filtered and washed with deionized water three times, and then dried under vacuum at 60 °C for 12 hours. The reagents used in the reaction are collected, separated by distillation, and recycled repeatedly. The yield of nylon 6 was 14.06%, and that of nylon 66 was 57.17%.
实施例3Example 3
将废旧地毯粉碎、筛分处理获得粗纤维。在顶部装有冷凝回流装置的50ml的三口烧瓶中按质量比1:8将处理后的粗纤维与二甲基亚砜混合,加热搅拌,温度控制在110℃~130℃,恒温60分钟,然后过滤,并用热的二甲基亚砜冲洗残留物,向所得的滤液中添加适量去离子水,有沉淀析出,沉淀为尼龙6,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。同时将残留物与甲酸按质量比1:15在室温下混合搅拌60分钟,然后过滤,向滤液中添加适量的去离子水,有沉淀析出,沉淀为尼龙66,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。收集反应中使用的试剂,蒸馏分离,重复循环利用。尼龙6的产率为13.95%,尼龙66的产率为58.06%。The waste carpets are crushed and sieved to obtain crude fibers. In a 50ml three-necked flask equipped with a condensing reflux device on the top, mix the treated crude fiber with dimethyl sulfoxide at a mass ratio of 1:8, heat and stir, and control the temperature at 110°C to 130°C, and keep the temperature constant for 60 minutes, then Filter, and wash the residue with hot dimethyl sulfoxide, add an appropriate amount of deionized water to the obtained filtrate, a precipitate is precipitated, and the precipitate is nylon 6, filter the precipitate, wash with deionized water three times, and then vacuum at 60 ° C Let dry for 12 hours. At the same time, the residue and formic acid were mixed and stirred at room temperature for 60 minutes at a mass ratio of 1:15, then filtered, and an appropriate amount of deionized water was added to the filtrate, and a precipitate was precipitated, which was nylon 66. The precipitate was filtered and washed with deionized water three times, and then dried under vacuum at 60 °C for 12 hours. The reagents used in the reaction are collected, separated by distillation, and recycled repeatedly. The yield of nylon 6 was 13.95%, and that of nylon 66 was 58.06%.
实施例4Example 4
将废旧地毯粉碎、筛分处理获得粗纤维。在顶部装有冷凝回流装置的50ml的三口烧瓶中按质量比1:10将处理后的粗纤维与二甲基亚砜混合,加热搅拌,温度控制在110℃~130℃,恒温60分钟,然后过滤,并用热的二甲基亚砜冲洗残留物,向所得的滤液中添加适量去离子水,有沉淀析出,沉淀为尼龙6,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。同时将残留物与甲酸按质量比1:15在室温下混合搅拌60分钟,然后过滤,向滤液中添加适量的去离子水,有沉淀析出,沉淀为尼龙66,过滤沉淀,用去离子水洗涤三次,然后在60℃下真空干燥12小时。收集反应中使用的试剂,蒸馏分离,重复循环利用。尼龙6的产率为14.46%,尼龙66的产率为58.62%。The waste carpets are crushed and sieved to obtain crude fibers. In a 50ml three-neck flask equipped with a condensing reflux device on the top, mix the treated crude fiber with dimethyl sulfoxide at a mass ratio of 1:10, heat and stir, and control the temperature at 110°C to 130°C for 60 minutes at a constant temperature, then Filter, and wash the residue with hot dimethyl sulfoxide, add an appropriate amount of deionized water to the obtained filtrate, a precipitate is precipitated, and the precipitate is nylon 6, filter the precipitate, wash with deionized water three times, and then vacuum at 60 ° C Let dry for 12 hours. At the same time, the residue and formic acid were mixed and stirred at room temperature for 60 minutes at a mass ratio of 1:15, then filtered, and an appropriate amount of deionized water was added to the filtrate, and a precipitate was precipitated, which was nylon 66. The precipitate was filtered and washed with deionized water three times, and then dried under vacuum at 60 °C for 12 hours. The reagents used in the reaction are collected, separated by distillation, and recycled repeatedly. The yield of nylon 6 was 14.46%, and that of nylon 66 was 58.62%.
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Cited By (6)
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CN105367818A (en) * | 2015-11-08 | 2016-03-02 | 韶关市连邦环保新材料股份有限公司 | Method for preparing pure product nylon 6 by taking nylon 6 waste material as raw material |
CN105713229A (en) * | 2016-03-31 | 2016-06-29 | 武汉纺织大学 | Method for separating nylon 66 and nylon 6 in polyamide thermal barrier strips |
CN110423377A (en) * | 2019-08-27 | 2019-11-08 | 上海松沅环境修复技术有限公司 | A kind of preparation method of high-purity nylon reworked material |
CN112356338A (en) * | 2020-10-09 | 2021-02-12 | 满遵连 | Waste carpet recycling processing method |
WO2022001054A1 (en) * | 2020-06-30 | 2022-01-06 | 金发科技股份有限公司 | Polyamide recycling process and polyamide obtained by recycling process |
CN114591531A (en) * | 2022-01-28 | 2022-06-07 | 苏州大学 | A method for preparing porous microspheres from waste nylon 6 fabrics |
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