CN106723333B - Electret superfine fiber cigarette filter tip material and preparation method thereof - Google Patents
Electret superfine fiber cigarette filter tip material and preparation method thereof Download PDFInfo
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- 239000000835 fiber Substances 0.000 title claims abstract description 50
- 235000019504 cigarettes Nutrition 0.000 title claims abstract description 49
- 239000000463 material Substances 0.000 title claims abstract description 42
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 11
- 239000004594 Masterbatch (MB) Substances 0.000 claims abstract description 10
- 239000012815 thermoplastic material Substances 0.000 claims abstract description 10
- 238000007664 blowing Methods 0.000 claims abstract description 8
- 229920001410 Microfiber Polymers 0.000 claims description 93
- 238000001816 cooling Methods 0.000 claims description 26
- 239000000203 mixture Substances 0.000 claims description 22
- 239000003658 microfiber Substances 0.000 claims description 5
- 238000001914 filtration Methods 0.000 abstract description 15
- 229920006221 acetate fiber Polymers 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000000428 dust Substances 0.000 abstract description 2
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 230000014759 maintenance of location Effects 0.000 abstract description 2
- 230000003068 static effect Effects 0.000 abstract 2
- 230000005611 electricity Effects 0.000 abstract 1
- 239000004744 fabric Substances 0.000 abstract 1
- 230000002045 lasting effect Effects 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 239000000155 melt Substances 0.000 description 9
- 238000005520 cutting process Methods 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- 241000208125 Nicotiana Species 0.000 description 3
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 125000005575 polycyclic aromatic hydrocarbon group Chemical group 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 1
- FMMWHPNWAFZXNH-UHFFFAOYSA-N Benz[a]pyrene Chemical compound C1=C2C3=CC=CC=C3C=C(C=C3)C2=C2C3=CC=CC2=C1 FMMWHPNWAFZXNH-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229960002715 nicotine Drugs 0.000 description 1
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000002166 wet spinning Methods 0.000 description 1
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- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24D—CIGARS; CIGARETTES; TOBACCO SMOKE FILTERS; MOUTHPIECES FOR CIGARS OR CIGARETTES; MANUFACTURE OF TOBACCO SMOKE FILTERS OR MOUTHPIECES
- A24D3/00—Tobacco smoke filters, e.g. filter-tips, filtering inserts; Filters specially adapted for simulated smoking devices; Mouthpieces for cigars or cigarettes
- A24D3/02—Manufacture of tobacco smoke filters
- A24D3/0229—Filter rod forming processes
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/44—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
- D01F6/46—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polyolefins
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
- D01F6/92—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyesters
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Filtering Materials (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
- Cigarettes, Filters, And Manufacturing Of Filters (AREA)
- Electrostatic Separation (AREA)
Abstract
Description
技术领域technical field
本发明涉及卷烟香烟滤嘴材料领域和非织造领域,特别涉及一种驻极超细纤维香烟滤嘴材料及其制备方法。The invention relates to the field of cigarette filter tip materials and non-woven fields, in particular to an electret superfine fiber cigarette filter tip material and a preparation method thereof.
背景技术Background technique
卷烟烟雾中包含有微粒,通常称之为焦油。焦油中含有大量的化学成分,有4000到5000种,都是烟草不完全燃烧的产物。香烟滤嘴是为了过滤烟草中的焦油等对人体有害的物质。现在常用香烟滤嘴材料为醋酸纤维香烟滤嘴,而醋酸纤维是采用湿法纺丝制得,生产工艺流程长,纺丝过程中使用的溶剂对环境有害,有三废污染。此外,醋酸纤维素纤维在滤除香烟主流烟气中的有害致癌物质(例如多环芳烃和醛类物质)的效果不是十分理想,去除多环芳烃物质的仅40%左右。Cigarette smoke contains particulates, commonly called tar. Tar contains a large number of chemical components, 4,000 to 5,000 species, which are all products of incomplete combustion of tobacco. Cigarette filters are used to filter harmful substances such as tar in tobacco. At present, the commonly used cigarette filter material is acetate fiber cigarette filter, and acetate fiber is obtained by wet spinning, the production process is long, the solvent used in the spinning process is harmful to the environment, and there are three wastes pollution. In addition, the effect of cellulose acetate fiber in filtering out harmful carcinogens (such as polycyclic aromatic hydrocarbons and aldehydes) in mainstream cigarette smoke is not very satisfactory, and only about 40% of the polycyclic aromatic hydrocarbons are removed.
卷烟滤嘴能够过滤烟雾成分,以减少焦油和尼古丁的吸入量。但是香烟装香烟滤嘴后,抽吸阻力大大增加,有毒物质就越多。如一氧化碳、苯并芘等都是在吸烟过程中,由烟草所含有机物质不完全燃烧生成的,吸烟时阻力越大,供氧越不充分,燃烧就越不完全,有毒物质的生成量也越多。纤维越细,过滤性能越好。卷烟香烟滤嘴的三种主要功能包括直接拦截、惯性压紧和扩散沉淀,最普遍的是直接拦截香烟滤嘴。过滤是一个复杂的过程,也就是说焦油小滴从烟雾中分离出来后,当它们到达香烟滤嘴材料的表面时就附着在上面。纤维越细,卷烟香烟滤嘴的过滤效率就越高,常规滤嘴所用的醋酸纤维直径在7~20μm之间。Cigarette filters filter smoke components to reduce inhalation of tar and nicotine. However, after the cigarette is equipped with a cigarette filter, the suction resistance is greatly increased, and the more toxic substances are. For example, carbon monoxide, benzopyrene, etc. are all generated by the incomplete combustion of organic substances contained in tobacco during the smoking process. more. The finer the fibers, the better the filtration performance. The three main functions of cigarette filters include direct interception, inertial compaction and diffusion deposition, the most common being direct interception of cigarette filters. Filtration is a complex process, which means that after the tar droplets are separated from the smoke, they stick to the surface of the cigarette filter material when they reach it. The finer the fiber, the higher the filtering efficiency of the cigarette filter. The diameter of the acetate fiber used in the conventional filter is between 7 and 20 μm.
发明内容SUMMARY OF THE INVENTION
为了解决现有技术中香烟过滤材料过滤效率不高的问题,本发明提供一种驻极超细纤维香烟滤嘴材料及其制备方法和制备装置。In order to solve the problem of low filtration efficiency of cigarette filter materials in the prior art, the present invention provides an electret ultrafine fiber cigarette filter tip material and a preparation method and preparation device thereof.
一种驻极超细纤维香烟滤嘴材料,为直径1-5μm的熔喷超细纤维。An electret superfine fiber cigarette filter tip material is a meltblown superfine fiber with a diameter of 1-5 μm.
进一步的,所述熔喷超细纤维由94-99重量份的热塑性材料和1-6重量份的驻极母粒制成。Further, the meltblown ultrafine fibers are made of 94-99 parts by weight of thermoplastic material and 1-6 parts by weight of electret masterbatch.
进一步的,所述熔喷超细纤维经过了驻极处理。Further, the meltblown ultrafine fibers have undergone electret treatment.
一种驻极超细纤维香烟滤嘴材料的制备方法,具体包括以下步骤:A preparation method of electret ultrafine fiber cigarette filter material, specifically comprising the following steps:
步骤S1、将94-99重量份的热塑性材料和1-6重量份的驻极母粒均匀混合,得到混合料;Step S1, uniformly mix the thermoplastic material of 94-99 parts by weight and the electret master batch of 1-6 parts by weight to obtain a mixture;
步骤S2、熔喷装置利用混合料制备熔喷超细纤维;Step S2, the melt-blown device utilizes the mixture to prepare the melt-blown ultrafine fibers;
步骤S3、冷却集束装置对熔喷装置喷出的熔喷超细纤维进行冷却和集束;Step S3, the cooling and clustering device cools and clusters the melt-blown ultrafine fibers sprayed by the melt-blowing device;
步骤S4、收集装置对熔喷超细纤维进行处理和收集,得到驻极超细纤维香烟滤嘴材料。In step S4, the collection device processes and collects the melt-blown ultrafine fibers to obtain electret ultrafine fiber cigarette filter tip materials.
进一步的,所述步骤S3的冷却集束装置包括冷风箱和帘网接收装置;所述步骤S3具体为:冷风箱对熔喷超细纤维进行冷却,冷却后的熔喷超细纤维依次落在沿着熔喷装置中熔喷模头的幅宽方向传动的帘网接收装置上,帘网接收装置对熔喷超细纤维集束得到超细纤维束。Further, the cooling and clustering device in the step S3 includes a cold air box and a curtain net receiving device; the step S3 is specifically: the cold air box cools the melt-blown ultrafine fibers, and the cooled melt-blown ultrafine fibers fall on the edge in turn. On the curtain web receiving device driven by the width direction of the melt-blown die head in the melt-blown device, the curtain web receiving device bundles the melt-blown ultra-fine fibers to obtain the ultra-fine fiber bundles.
进一步的,所述步骤S3的冷却集束装置包括冷风箱和第一集束装置;所述步骤S3具体为:所述冷风箱对熔喷装置的喷出的熔喷超细纤维进行冷却,所述第一集束装置对冷却后的熔喷超细纤维进行集束;且所述第一集束装置沿幅宽方向的宽度不小于熔喷装置中熔喷模头沿幅宽方向的宽度。Further, the cooling and clustering device in the step S3 includes a cold air box and a first clustering device; the step S3 is specifically: the cold air box cools the meltblown ultrafine fibers sprayed from the meltblown device, and the first A bundling device bundles the cooled meltblown ultrafine fibers; and the width of the first bundling device along the width direction is not less than the width of the meltblown die in the meltblown device along the width direction.
进一步的,所述熔喷超细纤维经冷却集束装置冷却和集束后,还经过驻极处理装置进行驻极处理。Further, after the melt-blown ultrafine fibers are cooled and bundled by a cooling bundle device, they are also subjected to electret treatment by an electret treatment device.
进一步的,所述驻极处理装置的驻极电压为5-20kV,驻极间隔20-60mm,驻极时间5-10s。Further, the electret voltage of the electret treatment device is 5-20kV, the electret interval is 20-60mm, and the electret time is 5-10s.
进一步的,所述步骤S1的热塑性材料为PP、PET、PA、PLA或PE中的任一种。Further, the thermoplastic material of the step S1 is any one of PP, PET, PA, PLA or PE.
本发明的有益效果是:纤维越细,卷烟香烟滤嘴的过滤效率就越高,常规滤嘴所用的醋酸纤维直径在7~20μm之间,常规的熔喷法无法制得纤维束,只能制得纤维无纺布,本发明对常规熔喷法进行了改进,通过增加冷侧吹风加速熔喷纤维的冷却,使纤维在完全冷却的情况下收集,避免熔喷纤维间的粘结,也可防止纤维在较高温度下发生解取向,熔喷纤维保留了一定的取向度,纤维强力提高。同时,将帘网由传统制备无纺布的垂直于纤网幅宽方向移动改为沿着纤网幅宽方向移动,可直接制得直径能达到1~5μm的超细纤维束,且细度均匀变化小,因而过滤效果高,能避免醋酸纤维生产中的环境污染问题。本发明对熔喷超细纤维进行驻极处理,经过特有的驻极处理,可以使熔喷超细纤维极化带上电荷,从而在不增加材料呼吸阻力的情况下,提高材料的静电吸附性能,同时电荷保持率可达2年以上,可依靠静电效应铺集为微粒尘埃,具有过滤效率高,过滤阻力低等优点。The beneficial effects of the invention are: the finer the fiber, the higher the filtering efficiency of the cigarette filter tip, the diameter of the acetate fiber used in the conventional filter tip is between 7 and 20 μm, and the conventional melt-blown method cannot obtain fiber bundles, only The fiber non-woven fabric is obtained, and the present invention improves the conventional melt-blown method, and accelerates the cooling of the melt-blown fibers by increasing the cold side air blowing, so that the fibers are collected under the condition of complete cooling, avoiding the bonding between the melt-blown fibers, and also It can prevent the fiber from de-orientation at higher temperature, the melt-blown fiber retains a certain degree of orientation, and the fiber strength is improved. At the same time, by changing the curtain web from the traditional non-woven fabric to move perpendicular to the width of the web to move along the width of the web, ultrafine fiber bundles with a diameter of 1 to 5 μm can be directly produced, and the fineness is The uniform change is small, so the filtering effect is high, and the environmental pollution problem in the production of acetate fiber can be avoided. In the present invention, the melt-blown ultra-fine fibers are electret treated, and through the special electret treatment, the melt-blown ultra-fine fibers can be polarized and charged, thereby improving the electrostatic adsorption performance of the material without increasing the breathing resistance of the material. At the same time, the charge retention rate can reach more than 2 years, and it can be spread into particulate dust by electrostatic effect, which has the advantages of high filtration efficiency and low filtration resistance.
附图说明Description of drawings
图1为冷却集束装置采用第一种实施方式时的制备装置结构示意图;FIG. 1 is a schematic structural diagram of a preparation device when the cooling and clustering device adopts the first embodiment;
图2为冷却集束装置采用第二种实施方式时的制备装置结构示意图。FIG. 2 is a schematic structural diagram of a preparation device when the cooling and clustering device adopts the second embodiment.
附图中,各标号代表的部件列表如下:In the accompanying drawings, the list of parts represented by each number is as follows:
1、熔喷装置;2、冷风箱;3、帘网接收装置;4、第一集束装置;5、收集装置;6、熔喷超细纤维;7、驻极处理装置;8、纤维通道;9、油轮;10、第二集束装置1. Melt-blown device; 2. Cold air box; 3. Curtain net receiving device; 4. First bundle device; 5. Collection device; 6. Melt-blown ultrafine fiber; 7. Electret treatment device; 8. Fiber channel; 9. Tanker; 10. The second cluster device
具体实施方式Detailed ways
以下结合附图对本发明的原理和特征进行描述,所举实例只用于解释本发明,并非用于限定本发明的范围。The principles and features of the present invention will be described below with reference to the accompanying drawings. The examples are only used to explain the present invention, but not to limit the scope of the present invention.
一种驻极超细纤维香烟滤嘴材料,为直径1-5μm的熔喷超细纤维。An electret superfine fiber cigarette filter tip material is a meltblown superfine fiber with a diameter of 1-5 μm.
所述熔喷超细纤维由94-99重量份的热塑性材料和1-6重量份的驻极母粒制成。The melt-blown microfiber is made from 94-99 parts by weight of thermoplastic material and 1-6 parts by weight of electret masterbatch.
所述熔喷超细纤维经过了驻极处理。The meltblown microfibers are electret treated.
一种驻极超细纤维香烟滤嘴材料的制备方法,具体包括以下步骤:A preparation method of electret ultrafine fiber cigarette filter material, specifically comprising the following steps:
步骤S1、将94-99重量份的热塑性材料和1-6重量份的驻极母粒均匀混合,得到混合料;Step S1, uniformly mix the thermoplastic material of 94-99 parts by weight and the electret master batch of 1-6 parts by weight to obtain a mixture;
步骤S2、熔喷装置1利用混合料制备熔喷超细纤维6;Step S2, the melt-blown device 1 utilizes the mixture to prepare the melt-blown
步骤S3、冷却集束装置对熔喷装置1喷出的熔喷超细纤维6进行冷却和集束;Step S3, the cooling and clustering device cools and clusters the melt-blown
步骤S4、收集装置5对熔喷超细纤维6进行处理和收集,得到驻极超细纤维香烟滤嘴材料。In step S4, the
冷却集束装置的第一种实施方式时,所述步骤S3的冷却集束装置包括冷风箱2和帘网接收装置3;所述步骤S3具体为:冷风箱3对熔喷超细纤维6进行冷却,冷却后的熔喷超细纤维6依次落在沿着熔喷装置1中熔喷模头的幅宽方向传动的帘网接收装置3上,对熔喷超细纤维6集束得到超细纤维束。In the first embodiment of the cooling bundling device, the cooling bundling device in step S3 includes a
所述熔喷超细纤维6经帘网接收装置3集束后,经过驻极处理装置7进行驻极处理,再经过第二集束装置10进行进一步集束,后进入收集装置5。After the melt-blown
冷却集束装置的第二种实施方式时,所述步骤S3的冷却集束装置包括冷风箱2和第一集束装置4;所述步骤S3具体为:所述冷风箱对熔喷装置1的喷出的熔喷超细纤维6进行冷却,所述第一集束装置4对冷却后的熔喷超细纤维6进行集束;且所述第一集束装置4沿幅宽方向的宽度不小于熔喷装置1中熔喷模头沿幅宽方向的宽度。In the second embodiment of the cooling clustering device, the cooling clustering device in step S3 includes a
所述熔喷超细纤维6经第一集束装置4集束后,经过驻极处理装置7进行驻极处理,后进入收集装置5。After the meltblown
所述驻极处理装置的驻极电压为5-20kV,驻极间隔20-60mm,驻极时间5-10s。The electret voltage of the electret treatment device is 5-20kV, the electret interval is 20-60mm, and the electret time is 5-10s.
所述步骤S1的热塑性材料为PP、PET、PA、PLA或PE中的任一种。The thermoplastic material of the step S1 is any one of PP, PET, PA, PLA or PE.
所述收集装置5为切断机,油轮9给熔喷超细纤维6上油后,导丝装置将熔喷超细纤维导入切断机,切断机将熔喷超细纤维6切成均匀的小段,作为驻极超细纤维香烟滤嘴材料。The
如图1和图2所示为一种驻极超细纤维香烟滤嘴材料的制备装置,包括熔喷装置1、冷却集束装置、驻极处理装置和收集装置;As shown in Figures 1 and 2, a preparation device for electret ultrafine fiber cigarette filter material, comprising a melt-blown device 1, a cooling and clustering device, an electret processing device and a collecting device;
所述熔喷装置1用于制备熔喷超细纤维6,并将熔喷超细纤维6输送至冷却集束装置;The melt-blown device 1 is used to prepare the melt-blown
所述冷却集束装置设置在熔喷装置1下方,用于对熔喷装置1喷出的熔喷超细纤维6进行冷却和集束,得到超细纤维束;The cooling and clustering device is arranged below the melt-blown device 1, and is used to cool and cluster the melt-blown
驻极处理装置用于对超细纤维束进行驻极处理;The electret treatment device is used for electret treatment of ultrafine fiber bundles;
所述收集装置用于对超细纤维束进行处理和收集,得到驻极超细纤维香烟滤嘴材料。The collecting device is used for processing and collecting the ultra-fine fiber bundles to obtain electret ultra-fine fiber cigarette filter tip materials.
如图1所示为冷却集束装置的第一种实施方式,所述冷却集束装置包括冷风箱2和帘网接收装置3;As shown in FIG. 1 , the first embodiment of the cooling bundling device includes a
所述冷风箱2设置在熔喷装置1中熔喷模头的下方,用于对熔喷装置1喷出的熔喷超细纤维6进行冷却,所述帘网接收装置3设置在冷风箱2下方,用于对冷却后的熔喷超细纤维6进行集束;所述帘网接收装置3沿着熔喷装置1中熔喷模头的幅宽方向,由远离驻极处理装置7的一端,向靠近驻极处理装置7的一端传动。The
所述帘网接收装置3内设置有抽吸装置,用于将熔喷超细纤维6吸至帘网接收装置3的上表面上。The curtain
冷却集束装置的第一种实施方式时,所述驻极处理装置和收集装置5之间还设置有第二集束装置10,用于对超细纤维束进行进一步集束。When cooling the first embodiment of the bundling device, a
如图2所示为冷却集束装置的第二种实施方式,所述冷却集束装置包括冷风箱2和第一集束装置4;所述冷风箱2设置在熔喷装置1中熔喷模头下方,用于对熔喷装置1的喷出的熔喷超细纤维6进行冷却,所述第一集束装置4设置在冷风箱2下方,用于对冷却后的熔喷超细纤维6进行集束得到超细纤维束;所述超细纤维束经过纤维通道8被输送至驻极处理装置7,超细纤维经过驻极处理后进入收集装置进行切断和收集。所述纤维通道8的作用为托持和引导纤维束,可采用托板等形式。所述第一集束装置4沿幅宽方向的宽度不小于熔喷装置1中熔喷模头沿幅宽方向的宽度,因此熔喷装置喷出的所有超细纤维均可进入集束装置4进行集束。As shown in FIG. 2, the second embodiment of the cooling and clustering device includes a
所述第一集束装置4和第二集束装置10均可采用喇叭口集束器。所述第二集束装置10、导丝装置和切断机等可采用支架等方式进行固定。Both the
实施例1Example 1
一种驻极超细纤维香烟滤嘴材料的制备方法,包括下列步骤:A preparation method of electret ultrafine fiber cigarette filter material, comprising the following steps:
步骤S1、取聚丙烯粒料96重量份、驻极母粒4重量份混合均匀,得混合料;Step S1, get 96 parts by weight of polypropylene pellets and 4 parts by weight of electret master batch and mix to obtain a mixture;
步骤S2、设置驻极超细纤维香烟滤嘴材料制备装置的四个区域温度分别为260℃,260℃,270℃,270℃,将步骤S1所得到混合料喂入螺杆挤出机的料仓,经螺杆熔融挤出机形成熔体;Step S2, set the temperature of the four regions of the electret ultrafine fiber cigarette filter material preparation device to be 260°C, 260°C, 270°C, and 270°C respectively, and feed the mixture obtained in step S1 into the silo of the screw extruder , forming a melt through a screw melt extruder;
步骤S3、熔体经计量泵后通过喷丝板喷出,在220℃、0.4MPa热风下牵伸得到熔喷超细纤维,熔喷超细纤维冷却之后利用帘网收集装置或者集束装置进行集束;Step S3, the melt is sprayed out through the spinneret after the metering pump, and the melt-blown ultrafine fibers are obtained by drawing under 220 ° C and 0.4MPa hot air, and the melt-blown ultra-fine fibers are cooled by using a curtain net collecting device or a bunching device to bundle. ;
步骤S4、对步骤S3得到的熔喷超细纤维采用高压电晕放电的方式进行驻极处理,所述驻极电压为10kV,驻极间隔30mm,驻极时间10s;Step S4, electreting the melt-blown ultrafine fibers obtained in step S3 by means of high-voltage corona discharge, the electret voltage is 10kV, the electret interval is 30mm, and the electret time is 10s;
步骤S5、将驻极处理后的熔喷超细纤维依次进行集束,上胶,成形和切断,得到驻极超细纤维香烟滤嘴材料。In step S5, the electret-treated melt-blown ultrafine fibers are sequentially bundled, sizing, shaped and cut to obtain electret ultrafine fiber cigarette filter tip materials.
本实施例所制成的驻极超细纤维香烟滤嘴材料的超细纤维平均直径能达到2μm,过滤效率达到95%。The average diameter of the ultrafine fibers of the electret ultrafine fiber cigarette filter material prepared in this embodiment can reach 2 μm, and the filtration efficiency can reach 95%.
实施例2Example 2
步骤S1、取聚丙烯粒料95重量份、驻极母粒5份混合均匀,得混合料;Step S1, get 95 parts by weight of polypropylene pellets and 5 parts by weight of electret master batch and mix to obtain a mixture;
步骤S2、设置驻极超细纤维香烟滤嘴材料制备装置的四个区域温度分别为260℃,260℃,270℃,270℃,将步骤S1所得到混合料喂入螺杆挤出机的料仓,经螺杆熔融挤出机形成熔体;Step S2, set the temperature of the four regions of the electret ultrafine fiber cigarette filter material preparation device to be 260°C, 260°C, 270°C, and 270°C respectively, and feed the mixture obtained in step S1 into the silo of the screw extruder , forming a melt through a screw melt extruder;
步骤S3、熔体经计量泵后通过喷丝板喷出,在220℃、0.4MPa热风下牵伸得到熔喷超细纤维,熔喷超细纤维冷却之后利用帘网收集装置或者集束装置进行集束;Step S3, the melt is sprayed out through the spinneret after the metering pump, and the melt-blown ultrafine fibers are obtained by drawing under 220 ° C and 0.4MPa hot air, and the melt-blown ultra-fine fibers are cooled by using a curtain net collecting device or a bunching device to bundle. ;
步骤S4、对步骤S3得到的超细纤维采用高压电晕放电的方式进行驻极处理,所述驻极电压为20kV,驻极间隔20mm,驻极时间10s;In step S4, electret treatment is performed on the ultrafine fibers obtained in step S3 by means of high-voltage corona discharge, and the electret voltage is 20kV, the electret interval is 20mm, and the electret time is 10s;
步骤S5、将熔喷驻极处理后的超细纤维依次进行集束,上胶,成形和切断,得到驻极超细纤维香烟滤嘴材料。In step S5, the superfine fibers after the melt-blown electret treatment are sequentially bundled, glued, shaped and cut to obtain electret superfine fiber cigarette filter tip materials.
本实施例所制成的驻极超细纤维香烟滤嘴材料的超细纤维平均直径为2μm,过滤效率能达到98%。The average diameter of the ultrafine fibers of the electret ultrafine fiber cigarette filter material prepared in this example is 2 μm, and the filtration efficiency can reach 98%.
实施例3Example 3
步骤S1、取PET粒料96重量份、驻极母粒4重量份混合均匀,得混合料;Step S1, get 96 parts by weight of PET pellets, 4 parts by weight of electret master batch and mix to obtain a mixture;
步骤S2、将所述混合料放入沸腾式预结晶器中,在120℃下预结晶2小时,然后放入充填干燥器中,在180℃下干燥8小时;Step S2, put the mixture into a boiling pre-crystallizer, pre-crystallize at 120°C for 2 hours, then put it into a filling dryer, and dry at 180°C for 8 hours;
步骤S3、设置驻极超细纤维香烟滤嘴材料制备装置的四个区域温度分别为270℃,270℃,280℃,285℃,将步骤S2处理后的混合料喂入螺杆挤出机的料仓,经螺杆熔融挤出机形成熔体;Step S3, set the temperature of the four regions of the electret ultrafine fiber cigarette filter material preparation device to be 270°C, 270°C, 280°C, and 285°C, respectively, and feed the mixture processed in step S2 into the material of the screw extruder. silo, the melt is formed by screw melt extruder;
步骤S4、熔体经计量泵后通过喷丝板喷出,在220℃、0.4MPa热风下牵伸得到熔喷超细纤维,熔喷超细纤维冷却之后利用帘网收集装置或者集束装置进行集束;Step S4, the melt is sprayed through a spinneret after the metering pump, and the melt-blown ultra-fine fibers are obtained by drawing at 220 ° C and 0.4 MPa hot air. After the melt-blown ultra-fine fibers are cooled, they are bundled using a curtain mesh collection device or a clustering device. ;
步骤S5、对步骤S4得到的超细纤维采用高压电晕放电的方式进行驻极处理,所述驻极电压为10kV,驻极间隔30mm,驻极时间10s;Step S5, performing electret treatment on the ultrafine fibers obtained in step S4 by means of high-voltage corona discharge, the electret voltage is 10kV, the electret interval is 30mm, and the electret time is 10s;
步骤S6、将驻极处理后的熔喷超细纤维依次进行集束,上胶,成形和切断,得到驻极超细纤维香烟滤嘴材料。In step S6, the electret-treated melt-blown ultrafine fibers are sequentially bundled, glued, shaped and cut to obtain electret ultrafine fiber cigarette filter tip materials.
本实施例所制成的驻极超细纤维香烟滤嘴材料的超细纤维平均直径为2.5μm,过滤效率能达到92%。The average diameter of the ultrafine fibers of the electret ultrafine fiber cigarette filter material prepared in this example is 2.5 μm, and the filtration efficiency can reach 92%.
实施例4Example 4
步骤S1、取PET粒料95重量份、驻极母粒5重量份混合均匀,得混合料;Step S1, get 95 parts by weight of PET pellets, 5 parts by weight of electret master batch and mix to obtain a mixture;
步骤S2、将所述混合料放入沸腾式预结晶器中,在120℃下预结晶2小时,然后放入充填干燥器中,在180℃下干燥8小时;Step S2, put the mixture into a boiling pre-crystallizer, pre-crystallize at 120°C for 2 hours, then put it into a filling dryer, and dry at 180°C for 8 hours;
步骤S3、设置驻极超细纤维香烟滤嘴材料制备装置的四个区域温度分别为270℃,270℃,280℃,285℃,将步骤S2处理后的混合料喂入螺杆挤出机的料仓,经螺杆熔融挤出机形成熔体;Step S3, set the temperature of the four regions of the electret ultrafine fiber cigarette filter material preparation device to be 270°C, 270°C, 280°C, and 285°C, respectively, and feed the mixture processed in step S2 into the material of the screw extruder. silo, the melt is formed by screw melt extruder;
步骤S4、熔体经计量泵后通过喷丝板喷出,在220℃、0.4MPa热风下牵伸得到熔喷超细纤维,熔喷超细纤维冷却之后利用帘网收集装置或者集束装置进行集束;Step S4, the melt is sprayed through a spinneret after the metering pump, and the melt-blown ultra-fine fibers are obtained by drawing at 220 ° C and 0.4 MPa hot air. After the melt-blown ultra-fine fibers are cooled, they are bundled using a curtain mesh collection device or a clustering device. ;
步骤S5、对步骤S4得到的超细纤维采用高压电晕放电的方式进行驻极处理,所述驻极电压为20kV,驻极间隔20mm,驻极时间10s;In step S5, electret treatment is performed on the ultrafine fibers obtained in step S4 by means of high-voltage corona discharge, the electret voltage is 20kV, the electret interval is 20mm, and the electret time is 10s;
步骤S6、将驻极处理后的熔喷超细纤维依次进行集束,上胶,成形和切断,得到驻极超细纤维香烟滤嘴材料。In step S6, the electret-treated melt-blown ultrafine fibers are sequentially bundled, glued, shaped and cut to obtain electret ultrafine fiber cigarette filter tip materials.
本实施例所制成的驻极超细纤维香烟滤嘴材料的超细纤维平均直径为2.5μm,过滤效率能达到94%。The average diameter of the ultrafine fibers of the electret ultrafine fiber cigarette filter material prepared in this embodiment is 2.5 μm, and the filtration efficiency can reach 94%.
以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the protection of the present invention. within the range.
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1656271A (en) * | 2002-05-20 | 2005-08-17 | 3M创新有限公司 | Method for forming spread nonwoven webs |
CN101905101A (en) * | 2010-07-30 | 2010-12-08 | 杭州电子科技大学 | A kind of preparation method of melt-blown polypropylene electret filter material |
CN104153119A (en) * | 2013-12-16 | 2014-11-19 | 多氟多化工股份有限公司 | Melt-blow non-woven material capable of effectively filtering PM 2.5 particles, preparation method and production device |
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CN102560902A (en) * | 2012-01-12 | 2012-07-11 | 天津工业大学 | Method for producing viscose cellulose spun-laid nonwoven |
CN105852208B (en) * | 2016-05-31 | 2019-06-11 | 湖北中烟工业有限责任公司 | A kind of smoke filtrate used in cigarette filter tip and its preparation method and application |
-
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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CN101905101A (en) * | 2010-07-30 | 2010-12-08 | 杭州电子科技大学 | A kind of preparation method of melt-blown polypropylene electret filter material |
CN104153119A (en) * | 2013-12-16 | 2014-11-19 | 多氟多化工股份有限公司 | Melt-blow non-woven material capable of effectively filtering PM 2.5 particles, preparation method and production device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2022036987A1 (en) * | 2020-08-17 | 2022-02-24 | 金发科技股份有限公司 | Antimicrobial melt-blown polyamide composite material and preparation method and use therefor |
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