CN114479386A - Super-black plastic master batch dispersed with nano carbon black, preparation method and application thereof - Google Patents
Super-black plastic master batch dispersed with nano carbon black, preparation method and application thereof Download PDFInfo
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- 239000004594 Masterbatch (MB) Substances 0.000 title claims abstract description 59
- 239000004033 plastic Substances 0.000 title claims abstract description 43
- 229920003023 plastic Polymers 0.000 title claims abstract description 43
- 229910021392 nanocarbon Inorganic materials 0.000 title claims abstract description 22
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 239000000835 fiber Substances 0.000 claims abstract description 31
- 239000000843 powder Substances 0.000 claims abstract description 23
- 229920000728 polyester Polymers 0.000 claims abstract description 16
- 239000002270 dispersing agent Substances 0.000 claims abstract description 8
- 239000011164 primary particle Substances 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 13
- 239000012752 auxiliary agent Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
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- 238000002844 melting Methods 0.000 claims description 3
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- 239000007822 coupling agent Substances 0.000 claims description 2
- 239000003431 cross linking reagent Substances 0.000 claims description 2
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- 239000000779 smoke Substances 0.000 claims description 2
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- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims 1
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
- C08J3/226—Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
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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
- 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
- D01F1/04—Pigments
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2467/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2467/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/011—Nanostructured additives
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
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Abstract
Description
技术领域technical field
本发明涉及功能纺织化纤领域,具体涉及B29技术领域,更具体地,本发明涉及一种分散有纳米炭黑的超黑塑料母粒、制备方法及其应用。The invention relates to the field of functional textile chemical fibers, in particular to the technical field of B29, and more particularly, to a super black plastic masterbatch dispersed with nanometer carbon black, a preparation method and an application thereof.
背景技术Background technique
超黑纤维是指在可见光范围内具有超高吸收率和极低反射率的纤维。因为其超高的可见光吸收率,所以超黑纤维具有极强的遮盖力。使用超黑纤维制备的服装,在拉伸时仍能保持良好的黑色,可以解决普通黑色纤维制备的织物因外力而产生的露出其他颜色的问题,因此超黑纤维市场需求量巨大,前景广阔。Ultra-black fibers refer to fibers with ultra-high absorptivity and very low reflectivity in the visible light range. Because of its ultra-high visible light absorption, the super black fiber has extremely strong covering power. Clothing made of ultra-black fiber can still maintain a good black color when stretched, which can solve the problem of exposing other colors of fabrics made of ordinary black fiber due to external force. Therefore, the market demand for ultra-black fiber is huge and has broad prospects.
超黑纤维制备工艺主要是印染加工法和原液着色法。目前,市面上大多数超黑纤维主要用印染加工方式制备,通过这种加工方式得到的纤维制品虽然色泽黑度好,但是色牢度不好,而且,印染加工过程严重污染环境,还可能影响人体的健康。原液着色法不仅不会产生工业废水,而且系统加工能耗低,更重要的是可以解决色牢度的问题。但是,这种免染聚酯纤维的黑度一直达不到印染加工的效果,主要原因是纤维母粒中炭黑的粒径和分散性的问题。原液着色法一般分为熔体直纺法和切片纺丝法。如中国专利CN111286804A公开了一种熔体直纺超黑聚酯纤维的制备方法,通过在熔体直纺过程中添加黑色色浆可以明显改善所制备的纤维黑度。但是,由于切片纺丝更加符合现在高速纺丝技术的需求,而且还具有方便品种更换、快速调整纤维中填料含量等特点,免染聚酯纤维生产一般都是切片纺丝法。所以,纺丝厂对黑色母粒提出了更高的黑度,更好的可纺性,更长的组件使用周期的要求。The preparation process of super black fiber is mainly printing and dyeing processing method and dope dyeing method. At present, most of the ultra-black fibers on the market are mainly prepared by printing and dyeing processing. Although the color and blackness of the fiber products obtained by this processing method are good, the color fastness is not good. Moreover, the printing and dyeing process seriously pollutes the environment and may affect the human health. The dope dyeing method not only does not produce industrial waste water, but also has low energy consumption for system processing, and more importantly, can solve the problem of color fastness. However, the blackness of this dye-free polyester fiber has not been able to achieve the effect of printing and dyeing, mainly due to the particle size and dispersibility of carbon black in the fiber masterbatch. The dope dyeing method is generally divided into the melt direct spinning method and the chip spinning method. For example, Chinese patent CN111286804A discloses a preparation method of melt direct spinning super black polyester fiber, and the blackness of the prepared fiber can be obviously improved by adding black color paste during the melt direct spinning process. However, because chip spinning is more in line with the needs of current high-speed spinning technology, and also has the characteristics of convenient variety replacement and rapid adjustment of filler content in fibers, the production of dye-free polyester fibers is generally chip spinning. Therefore, spinning mills have put forward higher blackness, better spinnability and longer component life cycle requirements for black masterbatch.
一般来说,纤维母粒中炭黑粒径越小,分散性越好,生产的纤维黑度就越高。如中国专利CN110885457A、CN110903611A采用原生粒径19-20nm炭黑直接添加到塑料粉中制备母粒,该母粒经过下游厂家验证,用所述母粒生产的纤维黑度得到明显提升。但是炭黑粒径越小,表面吸附能就越大,越容易发生团聚,导致炭黑在母粒中的分散性差。传统的炭黑粉体直接分散在塑料粉里的方法,无法解决纳米炭黑团聚和在母粒中分散性差的问题,不但影响可纺性和组件使用周期,还会影响纤维黑度。而传统方法制备的炭黑色浆分散剂含量高导致与塑料粉混合之后无法干燥,造成下料时螺杆打滑,无法满足生产要求。Generally speaking, the smaller the particle size of carbon black in the fiber masterbatch, the better the dispersibility, and the higher the blackness of the fiber produced. For example, in Chinese patents CN110885457A and CN110903611A, carbon black with a primary particle size of 19-20nm is directly added to plastic powder to prepare masterbatches. The masterbatches have been verified by downstream manufacturers, and the blackness of fibers produced with the masterbatches has been significantly improved. However, the smaller the particle size of carbon black, the greater the surface adsorption energy, and the easier it is to agglomerate, resulting in poor dispersibility of carbon black in the masterbatch. The traditional method of dispersing carbon black powder directly in plastic powder cannot solve the problems of nano-carbon black agglomeration and poor dispersibility in the masterbatch, which not only affects the spinnability and component service life, but also affects the fiber blackness. However, the high content of dispersant in the carbon black slurry prepared by the traditional method makes it impossible to dry after mixing with the plastic powder, resulting in the screw slipping during feeding, which cannot meet the production requirements.
因此,需要一种新型超黑母粒制备技术,解决纳米炭黑团聚和在母粒中分散性的问题。Therefore, a new preparation technology of super black masterbatch is required to solve the problems of nano-carbon black agglomeration and dispersibility in masterbatch.
发明内容SUMMARY OF THE INVENTION
针对现有技术中存在的一些问题,本发明第一个方面提供了一种分散有纳米炭黑的超黑塑料母粒,按重量份计,制备原料包括100份聚酯粉体、50-100份炭黑纳米色膏。In view of some problems existing in the prior art, the first aspect of the present invention provides an ultra-black plastic masterbatch dispersed with nano-carbon black. In parts by weight, the preparation raw materials include 100 parts of polyester powder, 50-100 parts of Parts of carbon black nano-color paste.
在一种实施方式中,所述分散有纳米炭黑的超黑塑料母粒的制备原料还包括0-10重量份助剂。In one embodiment, the raw materials for preparing the ultra-black plastic masterbatch dispersed with nano-carbon black further include 0-10 parts by weight of auxiliary agents.
在一种实施方式中,所述聚酯粉体的种类不作特别限定,可以列举的有聚苯二甲酸丁二酯、聚苯二甲酸乙二酯等。In one embodiment, the type of the polyester powder is not particularly limited, and examples thereof include polybutylene phthalate, polyethylene phthalate, and the like.
优选的,所述聚酯粉体在265℃/2.16kg的熔融指数为50-80g/10min,进一步优选为60-70g/10min。Preferably, the melt index of the polyester powder at 265°C/2.16kg is 50-80g/10min, more preferably 60-70g/10min.
优选的,所述聚酯粉体的熔点为250-270℃,例如250℃、255℃、260℃、265℃、270℃等。Preferably, the melting point of the polyester powder is 250-270°C, such as 250°C, 255°C, 260°C, 265°C, 270°C, and the like.
本申请中熔点为250-270℃的聚酯粉体对炭黑的分散性具有一定的促进作用。In this application, polyester powder with a melting point of 250-270° C. has a certain promoting effect on the dispersibility of carbon black.
在一种实施方式中,所述炭黑纳米色膏中炭黑的原生粒径为10-18nm,例如10nm、11nm、12nm、13nm、14nm、15nm、16nm、17nm、18nm。In one embodiment, the primary particle size of carbon black in the carbon black nano-color paste is 10-18 nm, such as 10 nm, 11 nm, 12 nm, 13 nm, 14 nm, 15 nm, 16 nm, 17 nm, 18 nm.
优选的,所述炭黑纳米色膏中炭黑的浓度为10-30wt%,可以列举的有10wt%、11wt%、12wt%、13wt%、14wt%、15wt%、20wt%、25wt%、30wt%等。Preferably, the concentration of carbon black in the carbon black nano-color paste is 10-30wt%, which can be listed as 10wt%, 11wt%, 12wt%, 13wt%, 14wt%, 15wt%, 20wt%, 25wt%, 30wt% %Wait.
本申请中炭黑纳米色膏中除去炭黑之外的成分不做特别限定,可以是润湿剂、分散剂、溶剂等,优选的,分散剂浓度为1-3wt%,具体成分本领域技术人员可根据实际需要进行常规选择。In this application, the components other than carbon black in the carbon black nano-color paste are not particularly limited, and can be a wetting agent, a dispersant, a solvent, etc., preferably, the concentration of the dispersant is 1-3wt%, and the specific components are skilled in the art Personnel can make routine selections according to actual needs.
在一种实施方式中,所述炭黑纳米色膏在25℃粘度为7000-8000cps。In one embodiment, the carbon black nano-color paste has a viscosity of 7000-8000 cps at 25°C.
本申请控制炭黑的原生粒径为10-18nm,在分散剂浓度较低的情况下,可以避免炭黑聚集体过大增长,使得本申请中炭黑纳米色膏中除去炭黑之外的成分种类以及炭黑纳米色膏的制备方法并不影响本申请中炭黑的分散性以及着色效果,不仅节约了不必要的成本,同时原料方便易得,提高生产效率,且以该炭黑纳米色膏的形式与本申请聚酯粉体混合造粒,得到的超黑母粒DF值低,炭黑分散更均匀,能够实现低L值的超黑纤维母粒。炭黑原生粒径过大或者过小,均会影响炭黑的分散效果,同时造成该炭黑纳米色膏的稳定性差。此外,当炭黑的原生粒径为10-18nm时,即使炭黑纳米色膏中炭黑的浓度保持在低于15wt%时,使用该塑料母粒,仍获得较好的着色效果。In the present application, the primary particle size of carbon black is controlled to be 10-18 nm. When the concentration of the dispersant is low, the excessive growth of carbon black aggregates can be avoided, so that the carbon black nano-color paste in the present application removes carbon black. The types of ingredients and the preparation method of the carbon black nano-color paste do not affect the dispersibility and coloring effect of the carbon black in the present application, which not only saves unnecessary costs, but at the same time, the raw materials are convenient and easy to obtain, and the production efficiency is improved. The form of color paste is mixed and granulated with the polyester powder of the present application, and the obtained ultra-black masterbatch has a low DF value, and the carbon black is more uniformly dispersed, which can realize the ultra-black fiber masterbatch with a low L value. If the primary particle size of carbon black is too large or too small, the dispersion effect of carbon black will be affected, and the stability of the carbon black nano-color paste will be poor at the same time. In addition, when the primary particle size of carbon black is 10-18 nm, even when the concentration of carbon black in the carbon black nano-color paste is kept below 15 wt%, the plastic masterbatch can still obtain better coloring effect.
本申请中所述助剂可以列举的有偶联剂、粘度调节剂、抗氧剂、发泡剂、表面活性剂、增塑剂、交联剂、阻燃剂、抑烟剂等,助剂的具体选择本领域技术人员可做常规选择。The auxiliary agents mentioned in this application can be listed as coupling agents, viscosity modifiers, antioxidants, foaming agents, surfactants, plasticizers, cross-linking agents, flame retardants, smoke suppressants, etc. A person skilled in the art can make routine choices.
本发明第二个方面提供了一种分散有纳米炭黑的超黑塑料母粒的制备方法,包括下面步骤:A second aspect of the present invention provides a method for preparing a super black plastic masterbatch dispersed with nano carbon black, comprising the following steps:
(1)将制备超黑塑料母粒的各原料混合后干燥;(1) drying after mixing each raw material for preparing super black plastic master batch;
(2)对步骤(1)得到的物料投入双螺杆挤出机中于250℃-270℃进行挤出造粒。(2) The material obtained in step (1) is put into a twin-screw extruder at 250°C-270°C for extrusion and granulation.
在一种实施方式中,所述分散有纳米炭黑的超黑塑料母粒的制备方法,包括下面步骤:In one embodiment, the preparation method of the ultra-black plastic masterbatch that is dispersed with nano carbon black, comprises the following steps:
(1)将制备超黑塑料母粒的各原料投入高速混合机中,加热搅拌至混合粉体干燥;(1) put each raw material for preparing super black plastic master batch into the high-speed mixer, heat and stir until the mixed powder is dried;
(2)对步骤(1)得到的物料投入双螺杆挤出机中挤出造粒:混匀的物料在双螺杆中充分塑化后经双螺杆中的分散元件剪切分散均匀,经圆孔口模挤出、水槽冷却、拉条牵引到切粒机切成长3mm±1mm,直径2.5mm±1.5mm的圆柱型颗粒;所述双螺杆挤出机配有抽真空装置,所述双螺杆挤出机的长径比不小于40:1;挤出时的工艺温度为250℃-270℃。(2) Put the material obtained in step (1) into a twin-screw extruder for extrusion and granulation: after the mixed material is fully plasticized in the twin-screw, it is uniformly sheared and dispersed by the dispersing element in the twin-screw, and the Die extrusion, water tank cooling, pulling the strands to the pelletizer to cut cylindrical pellets with a length of 3mm±1mm and a diameter of 2.5mm±1.5mm; the twin-screw extruder is equipped with a vacuum device, and the twin-screw extruder is The length-diameter ratio of the machine is not less than 40:1; the process temperature during extrusion is 250℃-270℃.
本发明第三个方面提供了一种所述分散有纳米炭黑的超黑塑料母粒在超黑纤维中的应用。A third aspect of the present invention provides an application of the super black plastic masterbatch dispersed with nano carbon black in super black fibers.
本发明与现有技术相比具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明使用湿法加料的方法提高了母粒中炭黑的分散性,折算相同浓度炭黑,本发明所述超黑塑料母粒制备的纤维Lab值中的L值相对于直接添加炭黑粉体制备的纤维L值更低;(1) the present invention uses the method for wet feeding to improve the dispersibility of carbon black in the master batch, converts the same concentration of carbon black, the L value in the fiber Lab value prepared by the ultra-black plastic master batch of the present invention is relative to the direct addition The L value of fibers prepared from carbon black powder is lower;
(2)本发明制成的20wt%炭黑浓度的超黑母粒,压滤值不高于7Mpa,在纤维中添加5wt%可实现L值不高于18,添加10wt%后L值不高于15;(2) The ultra-black masterbatch with 20wt% carbon black concentration made by the present invention has a filter press value not higher than 7Mpa, and adding 5wt% to the fiber can achieve an L value not higher than 18, and adding 10wt% L value is not high at 15;
(3)本发明解决了原生粒径小于19nm炭黑在贮存因表面吸附能过大团聚成微米级炭黑,从而影响母粒可纺性的问题,进而延长纺丝组件使用周期;(3) The present invention solves the problem that the primary particle size of carbon black is less than 19nm and the surface adsorption energy is too large to agglomerate into micron-scale carbon black in storage, thereby affecting the spinnability of the masterbatch, and then prolonging the service life of the spinning assembly;
(4)本发明所述炭黑纳米色膏中炭黑含量10-30wt%,但是分散剂含量仅在1-3wt%,避免了传统炭黑色浆分散剂含量过高,与塑料粉混合后无法完全干燥导致造粒过程中螺杆打滑的问题;(4) The carbon black content in the carbon black nano-color paste of the present invention is 10-30wt%, but the dispersant content is only 1-3wt%, which avoids the high dispersant content of the traditional carbon black paste, which cannot be mixed with plastic powder. Complete drying leads to the problem of screw slippage during granulation;
(5)本发明所述炭黑纳米色膏中炭黑含量高,导致其余原料中的有机溶剂少,高混机直接加热混合干燥时间短,节省时间和功耗,此外经实践意外发现,本申请中膏状的炭黑纳米色膏比浆状的炭黑成分制成的母粒,尤其是使用在25℃粘度为7000-8000cps的炭黑纳米色膏,压滤值低得多;(5) The carbon black content in the carbon black nano-color paste of the present invention is high, resulting in less organic solvent in the remaining raw materials, and the direct heating and mixing drying time of the high-mixer is short, saving time and power consumption. The paste-like carbon black nano-color paste in the application is much lower than the masterbatch made from the paste-like carbon black components, especially the carbon black nano-color paste with a viscosity of 7000-8000cps at 25°C, and the filter pressure value is much lower;
(6)本发明控制炭黑纳米色膏中炭黑含量和原生粒径,不但可以解决寻常炭黑纳米色膏中无法实现炭黑的解团聚问题,还可以避免贮存一段时间后,炭黑出现“返粗”现象,可更有效更稳定的储存炭黑纳米色膏,随取随用;(6) The present invention controls the carbon black content and primary particle size in the carbon black nano-color paste, which can not only solve the problem of deagglomeration of carbon black that cannot be achieved in ordinary carbon black nano-color paste, but also avoid the occurrence of carbon black after a period of storage. The phenomenon of "returning to thickening" can store carbon black nano-color paste more effectively and stably, and use it as needed;
(7)本发明是通过炭黑纳米色膏、聚酯粉体,或者添加助剂后,直接混合干燥即可进入造粒机,工艺简单,符合现在高速纺丝技术的需求,而且还具有方便品种更换、快速调整纤维中填料含量等特点。(7) In the present invention, the carbon black nano-color paste, polyester powder, or after adding auxiliary agents, can be directly mixed and dried to enter the granulator. The process is simple, which meets the needs of the current high-speed spinning technology, and also has the advantages of convenient Variety replacement, rapid adjustment of filler content in fibers, etc.
附图说明Description of drawings
图1为使用不同浓度本申请实施例1-3以及对比例1-3母粒得到的黑涤纶纤维的L值。Figure 1 shows the L values of black polyester fibers obtained by using masterbatches of Examples 1-3 and Comparative Examples 1-3 of the present application with different concentrations.
具体实施方式Detailed ways
以下通过具体实施方式说明本发明,但不局限于以下给出的具体实施例。The present invention is described below through specific embodiments, but is not limited to the specific examples given below.
实施例1Example 1
一种分散有纳米炭黑的超黑塑料母粒,按重量份计,原料如下:A super black plastic master batch dispersed with nano carbon black, by weight, the raw materials are as follows:
100份PET粉体、100份炭黑纳米色膏、1份抗氧剂。100 parts of PET powder, 100 parts of carbon black nano-color paste, 1 part of antioxidant.
其中,所述PET粉体购自江苏三房巷,牌号为CZ5011;所述炭黑纳米色膏中炭黑原生粒径为15nm,浓度为30wt%。Wherein, the PET powder was purchased from Sanfangxiang, Jiangsu, and the brand name was CZ5011; the primary particle size of carbon black in the carbon black nano-color paste was 15 nm, and the concentration was 30 wt %.
所述分散有纳米炭黑的超黑塑料母粒的制备方法如下:The preparation method of the ultra-black plastic master batch dispersed with nano carbon black is as follows:
(1)将上述各原料投入高速混合机中,加热搅拌至混合粉体干燥,除去纳米色膏的溶剂;(1) drop each above-mentioned raw material into the high-speed mixer, heat and stir until the mixed powder is dried, and remove the solvent of the nano-color paste;
(2)投入双螺杆挤出机中挤出造粒:将混匀的物料在双螺杆中充分塑化后经双螺杆中的分散元件剪切分散均匀,经圆孔口模挤出、水槽冷却、拉条牵引到切粒机切成长3mm±1mm,直径2.5mm±1.5mm的圆柱型颗粒;所述双螺杆挤出机配有抽真空装置,所述双螺杆挤出机的长径比不小于40:1;挤出时的工艺温度为260℃。(2) Put it into a twin-screw extruder for extrusion and granulation: the mixed material is fully plasticized in the twin-screw, sheared and dispersed evenly by the dispersing element in the twin-screw, extruded through a round orifice die, and cooled in a water tank , Pulled to the pelletizer to cut cylindrical pellets with a length of 3mm±1mm and a diameter of 2.5mm±1.5mm; the twin-screw extruder is equipped with a vacuum device, and the length-diameter ratio of the twin-screw extruder is different. Less than 40:1; the process temperature during extrusion is 260°C.
对比例1Comparative Example 1
一种塑料母粒,按重量份计,原料如下:A plastic masterbatch, in parts by weight, the raw materials are as follows:
100份PET粉体、30份纳米炭黑粉体、1份抗氧剂。100 parts of PET powder, 30 parts of nano-carbon black powder, 1 part of antioxidant.
其中,所述PET粉体购自江苏三房巷,牌号为CZ5011;所述纳米炭黑粉体型号与实施例中所用炭黑纳米中的炭黑一致。Wherein, the PET powder was purchased from Sanfangxiang, Jiangsu, and the brand name was CZ5011; the model of the nanometer carbon black powder was consistent with the carbon black in the carbon black nanometers used in the examples.
所述塑料母粒的制备方法同实施例1,不同之处在于,步骤(1)为:将上述各原料投入高速混合机中,充分搅拌混匀。The preparation method of the plastic masterbatch is the same as that in Example 1, except that the step (1) is as follows: put the above-mentioned raw materials into a high-speed mixer, and fully stir and mix.
将上述实施例和对比例1制备的母粒与白切粒(白色纯PET母粒)按照2:14混合,采用1400目过滤筛网测试纺丝过滤性,实施例纺丝压滤值为2.94Mpa,对比例1测试11min纺丝压滤值超标(≥10Mpa),可以说明实施例中的超黑母粒中炭黑在母粒中的分散性更好。The masterbatch prepared in the above-mentioned example and Comparative Example 1 was mixed with white cut pellets (white pure PET masterbatch) at a ratio of 2:14, and a 1400-mesh filter screen was used to test the spinning filterability. The spinning filter pressure value of the embodiment was 2.94. Mpa, the 11min spinning filter pressure value of Comparative Example 1 exceeds the standard (≥10Mpa), which can indicate that the super black masterbatch in the example has better dispersibility in the masterbatch.
实施例2Example 2
一种塑料母粒,具体实施方式同实施例1,不同之处在于,所述炭黑纳米色膏中炭黑原生粒径为10nm。A plastic master batch, the specific embodiment is the same as that of Example 1, the difference is that the primary particle size of carbon black in the carbon black nano-color paste is 10 nm.
塑料母粒的制备方法同实施例1。The preparation method of plastic masterbatch is the same as that in Example 1.
实施例3Example 3
一种塑料母粒,具体实施方式同实施例1,不同之处在于,所述炭黑纳米色膏中炭黑原生粒径为18nm。A plastic master batch, the specific embodiment is the same as that of Example 1, the difference is that the primary particle size of carbon black in the carbon black nano-color paste is 18 nm.
塑料母粒的制备方法同实施例1。The preparation method of plastic masterbatch is the same as that in Example 1.
对比例2Comparative Example 2
一种塑料母粒,具体实施方式同实施例1,不同之处在于,所述炭黑纳米色膏中炭黑原生粒径为20nm。A plastic master batch, the specific embodiment is the same as that of Example 1, the difference is that the primary particle size of carbon black in the carbon black nano-color paste is 20 nm.
塑料母粒的制备方法同实施例1。The preparation method of plastic masterbatch is the same as that in Example 1.
对比例3Comparative Example 3
一种塑料母粒,具体实施方式同实施例1,不同之处在于,所述炭黑纳米色膏中炭黑原生粒径为30nm。A plastic master batch, the specific embodiment is the same as that of Example 1, the difference is that the primary particle size of carbon black in the carbon black nano-color paste is 30 nm.
塑料母粒的制备方法同实施例1。The preparation method of plastic masterbatch is the same as that in Example 1.
将上述实施例2-3,对比例2-3制备的母粒与白切粒(白色纯PET母粒)按照2:14混合,采用1400目过滤筛网测试纺丝过滤性。The masterbatch prepared in the above Example 2-3 and Comparative Example 2-3 was mixed with white cut pellets (white pure PET masterbatch) at a ratio of 2:14, and a 1400-mesh filter screen was used to test the spinning filterability.
将上述实施例1-3,对比例1-3制备的母粒分别按照2%、4%、6%、8%和10%的重量添加量与白切粒(白色纯PET母粒)混合生产200D/96F规格的黑涤纶纤维,采用色差仪测试所生产纤维的L值,结果如表1和图1所示。The masterbatches prepared in the above-mentioned examples 1-3 and comparative examples 1-3 were mixed with white cut pellets (white pure PET masterbatch) according to the weight additions of 2%, 4%, 6%, 8% and 10%, respectively. For black polyester fibers with 200D/96F specifications, the L value of the produced fibers was tested by a colorimeter. The results are shown in Table 1 and Figure 1.
表1Table 1
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