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CN113417078B - A kind of preparation method of high shrinkage orange petal type two-component spunbond spunbond microfiber leather base fabric - Google Patents

A kind of preparation method of high shrinkage orange petal type two-component spunbond spunbond microfiber leather base fabric Download PDF

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CN113417078B
CN113417078B CN202110775639.7A CN202110775639A CN113417078B CN 113417078 B CN113417078 B CN 113417078B CN 202110775639 A CN202110775639 A CN 202110775639A CN 113417078 B CN113417078 B CN 113417078B
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shrinkage
component
fiber
spunlace
leather base
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CN113417078A (en
Inventor
钱晓明
朵永超
封严
王闻宇
秦贵昌
赵孝龙
张爱明
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JI'AN CITY SANJIANG SUPERFINE FIBER NONWOVEN CO Ltd
Shandong Qilu Chemical Textile Co ltd
Tianjin Polytechnic University
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JI'AN CITY SANJIANG SUPERFINE FIBER NONWOVEN CO Ltd
Shandong Qilu Chemical Textile Co ltd
Tianjin Polytechnic University
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    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/005Synthetic yarns or filaments
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • D01D5/088Cooling filaments, threads or the like, leaving the spinnerettes
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/22Formation of filaments, threads, or the like with a crimped or curled structure; with a special structure to simulate wool
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/10Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between yarns or filaments made mechanically
    • D04H3/11Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between yarns or filaments made mechanically by fluid jet
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06CFINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
    • D06C7/00Heating or cooling textile fabrics

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Nonwoven Fabrics (AREA)
  • Multicomponent Fibers (AREA)

Abstract

The invention discloses a preparation method of a high-shrinkage orange-petal-shaped two-component spun-bonded spunlace microfiber leather base fabric, which comprises the steps of firstly adding a hot air device and a fiber crimping device into a two-component spun-bonded/spunlace production line, and then spinning two-component composite fibers into a web; conveying the fiber web into a hot air device for thermal shrinkage treatment, and utilizing thermal shrinkage of high-shrinkage components in the two-component composite fiber to enable the two-component composite fiber to generate a cracking tendency; then the bicomponent composite fiber is separated from the fiber by a spunlace process and is mutually entangled; and conveying the spun-bonded spun-laced microfiber leather base cloth into a fiber crimping device, and performing shrinkage crimping treatment on the nonwoven cloth by using the fiber crimping device to enable the high-shrinkage component to be completely shrunk and crimped to obtain the two-component spun-bonded spun-laced microfiber leather base cloth. The method has the advantages of simple process flow, low production cost and low energy consumption, and can realize green and clean preparation of the microfiber leather base cloth by one-step method, and the prepared hollow orange petal type double-component spun-bonded spunlace leather base cloth has the characteristics of compactness, softness, stiffness and full hand feeling.

Description

一种高收缩桔瓣型双组份纺粘水刺超纤革基布的制备方法A preparation method of a high-shrinkage segmental orange-shaped two-component spunbonded spunlaced microfiber leather base cloth

技术领域technical field

本发明涉及非织造布领域,具体是一种高收缩桔瓣型双组份纺粘水刺超纤革基布的制备方法。The invention relates to the field of non-woven fabrics, in particular to a preparation method of a high-shrinkage segmental orange-shaped two-component spun-bonded spunlace microfiber leather base cloth.

背景技术Background technique

利用双组份纺粘水刺非织造技术制备的桔瓣型超细纤维非织造布解决了海岛纤维通过溶剂溶解开纤制备超细纤维非织造布而造成的环境污染问题,工艺流程简单,可制备轻薄、高强的超细纤维非织造布,可广泛应用于超纤革、过滤、擦拭等领域,特别是应用于超纤革领域可实现超纤革基布的绿色清洁化制备。申请号201710026839.6采用中空桔瓣型双组份纺粘水刺非织造布作为基布,通过超纤革贴面技术制备了纺粘长丝桔瓣型超纤革。申请号201710026836.2采用纺粘法制备桔瓣型复合长丝纤维水刺后制备纤维细度具有梯度变化的超细纤维非织造布,经聚氨酯含浸后得到桔瓣型超细纤维仿真皮革基布。The pie-shaped ultrafine fiber nonwoven fabric prepared by the two-component spunbond spunlace nonwoven technology solves the environmental pollution problem caused by the sea-island fiber dissolving and opening the ultrafine fiber nonwoven fabric. The process is simple and can be used The preparation of light, high-strength microfiber nonwoven fabric can be widely used in the fields of microfiber leather, filtration, wiping, etc., especially in the field of microfiber leather, which can realize the green and clean preparation of microfiber leather base cloth. Application No. 201710026839.6 uses hollow segmented orange-shaped two-component spunbond spunlace nonwoven fabric as the base fabric, and prepares spunbond filament segmental segmented microfiber leather through microfiber leather veneer technology. Application No. 201710026836.2 Spunbond method is used to prepare segmental-shaped composite filament fiber spunlace, and then prepare microfiber nonwoven fabric with gradient change in fiber fineness, and impregnate with polyurethane to obtain segmental-shaped ultra-fine fiber imitation leather base fabric.

但目前利用双组份纺粘水刺非织造技术制备的中空桔瓣型超细纤维非织造布应用于超纤革领域存在的不足是:桔瓣型双组份纺粘水刺超细纤维非织造布手感扁薄、丰满度、柔软度不足,因此在应用范围上受到了很大的局限。基于上述不足,桔瓣型双组份纺粘水刺非织造技术存在下述难点:(1)以PET、PA6或PP为主原料制备的中空桔瓣型双组份复合纤维无法产生卷曲,平行铺网后纤维多为平行走向,裂离开纤后纤维截面呈锲型,容易紧密堆积,制备的非织造布弹性及延展性不足;(2)中空桔瓣型复合纤维通过高压水射流裂离开纤,存在夹心开纤(非织造布表面开纤率高,中间开纤率低)的问题;(3)利用高压水刺技术开纤,存在能耗大的问题,如何降低水刺能耗,同时保证产品质量成为难点。However, the shortcomings of the hollow orange-shaped superfine fiber nonwovens prepared by two-component spunbond spunlace nonwovens in the field of microfiber leather are: The woven fabric has a flat and thin feel, insufficient fullness and softness, so its application range is greatly limited. Based on the above deficiencies, there are the following difficulties in the segmented segmental two-component spunbond spunlace nonwoven technology: (1) The segmental segmented segmental hollow hollow composite fiber prepared from PET, PA6 or PP as the main raw material cannot produce crimps, parallel After the web is laid, the fibers are mostly parallel to each other, and the cross-section of the fibers after splitting is wedge-shaped, which is easy to pack tightly, and the prepared nonwoven fabric has insufficient elasticity and ductility; , there is the problem of sandwich fiber opening (high fiber opening rate on the surface of the nonwoven fabric, low fiber opening rate in the middle); (3) using high-pressure spunlace technology to open fibers, there is a problem of high energy consumption, how to reduce the energy consumption of spunlace, and at the same time Ensuring product quality has become difficult.

因此,为解决非织造布手感扁平、丰满度、柔软度不足的问题,申请号201510422893.3的文献采用高收缩聚酯切片和锦纶6切片,HSPET为裂片部分,PA6为米字(支架)部分,重量百分比为55~65:45~35,制得沸水收缩率达10%左右的涤锦复合纤维,但支架与裂片的接触面大,支架的摩擦力小于纤维的收缩力,较难产生易收缩的效果。申请号201610355479.X的文献以改性尼龙(COPA)和聚酯(PET)为原料,经复合纺丝的方法制得以COPA为支架、PET为裂片的桔瓣型超细复合纤维,在碱减量过程中,改性尼龙与涤纶部分发生剥离,并在之后的高温染色过程中,改性尼龙进一步收缩,细旦涤纶包覆在改性尼龙纤维周围,使最终织物具有致密、挺括、丰满的效果。上述工艺应用于传统纱线织物,均需要溶剂开纤后再收缩,工艺复杂,且不利于环保。Therefore, in order to solve the problems of flat hand feeling, fullness and insufficient softness of nonwoven fabrics, the document of application number 201510422893.3 uses high-shrinkage polyester slices and nylon 6 slices, HSPET is the split part, PA6 is the rice word (bracket) part, and the weight The percentage is 55~65:45~35, and the polyester nylon composite fiber with boiling water shrinkage rate of about 10% is obtained, but the contact surface between the support and the lobes is large, and the friction force of the support is smaller than the shrinkage force of the fiber, so it is difficult to produce shrinkage. Effect. The document with the application number 201610355479.X uses modified nylon (COPA) and polyester (PET) as raw materials, and through the method of composite spinning, the orange segment ultrafine composite fiber with COPA as the support and PET as the lobes is obtained. During the dyeing process, the modified nylon and polyester parts peel off, and in the subsequent high-temperature dyeing process, the modified nylon shrinks further, and the fine-denier polyester is wrapped around the modified nylon fiber, so that the final fabric has a dense, crisp and plump texture. Effect. The above-mentioned processes are applied to traditional yarn fabrics, all of which require solvents to open the fiber and then shrink, the process is complicated, and it is not conducive to environmental protection.

发明内容Contents of the invention

针对现有技术的不足,本发明拟解决的技术问题是,提供一种高收缩桔瓣型双组份纺粘水刺超纤革基布的制备方法。Aiming at the deficiencies of the prior art, the technical problem to be solved by the present invention is to provide a method for preparing a high-shrinkage segmental-shaped two-component spunbonded spunlace microfiber leather base cloth.

本发明解决所述技术问题的技术方案是,提供一种高收缩桔瓣型双组份纺粘水刺超纤革基布的制备方法,其特征在于,该方法包括以下步骤:The technical solution of the present invention to solve the technical problem is to provide a method for preparing a high-shrinkage segmental orange-shaped two-component spunbonded spunlace microfiber leather base cloth, which is characterized in that the method comprises the following steps:

(1)在双组份纺粘/水刺生产线中加入热风装置和纤维卷缩装置;按照纺程方向,热风装置设置于成网帘的后方;纤维卷缩装置设置于压辊的后方;(1) A hot air device and a fiber crimping device are added to the two-component spunbond/spunlace production line; according to the spinning direction, the hot air device is set behind the web curtain; the fiber crimping device is set behind the press roller;

(2)双组份复合纤维纺丝成网:首先将两种聚合物通过共轭纺丝形成双组份原生丝熔体;然后经侧吹风冷却装置的冷却固化、气流牵伸装置的气流牵伸,双组份复合纤维在负压抽吸装置的作用下在成网帘上均匀铺网,形成纤维网;(2) The two-component composite fiber is spun into a web: first, the two polymers are conjugated to form a two-component raw silk melt; Stretching, the two-component composite fiber is evenly laid on the web curtain under the action of the negative pressure suction device to form a fiber web;

两种聚合物中的至少一种为高收缩聚合物,另一种为能与高收缩聚合物复合纺丝的常规聚合物;At least one of the two polymers is a high-shrinkage polymer, and the other is a conventional polymer capable of co-spinning with the high-shrinkage polymer;

(3)将步骤(2)制得的纤维网输送入热风装置中进行热收缩处理,利用双组份复合纤维中高收缩组份的热收缩使得双组份复合纤维产生裂离趋势;再经水刺工艺使双组份复合纤维裂离开纤并相互缠结,得到双组份纺粘水刺非织造布;(3) The fiber web prepared in step (2) is transported into the hot air device for thermal shrinkage treatment, and the thermal shrinkage of the high-shrinkage component in the two-component composite fiber is used to make the two-component composite fiber produce a splitting tendency; The puncture process splits the two-component composite fibers and entangles each other to obtain a two-component spunbond spunlaced nonwoven fabric;

(4)将步骤(3)制得的双组份纺粘水刺非织造布输送至纤维卷缩装置中,利用纤维卷缩装置对非织造布进行收缩卷曲处理,使得非织造布中双组份复合纤维的高收缩组份完全收缩卷曲,得到双组份纺粘水刺超纤革基布。(4) Transport the two-component spunbonded spunlace nonwoven fabric prepared in step (3) to the fiber crimping device, and use the fiber crimping device to shrink and curl the nonwoven fabric, so that the two-component spunlace nonwoven fabric in the nonwoven fabric The high-shrinkage component of the composite fiber is completely shrunk and crimped to obtain a two-component spunbonded spunlace microfiber leather base fabric.

与现有技术相比,本发明有益效果在于:Compared with the prior art, the present invention has the beneficial effects of:

(1)本发明的双组份复合纤维中的一种组分为高收缩组份,可实现后续双组份复合纤维受热收缩促进裂离,并使裂离后的高收缩组份收缩卷曲,提高非织造布丰满度、柔软度以及弹性。(1) One of the components in the two-component composite fiber of the present invention is a high-shrinkage component, which can realize the subsequent thermal shrinkage of the two-component composite fiber to promote splitting, and make the split high-shrinkage component shrink and crimp, Improve the fullness, softness and elasticity of nonwovens.

(2)本发明在成网帘后添加热风装置,通过热风装置使得双组份复合纤维中的高收缩组份的受热收缩,利用两组份的收缩率不同使双组份复合纤维产生裂离趋势,甚至部分纤维已经发生裂离,使得后续的水刺开纤工艺过程中的水刺压力随之降低,可极大地降低水刺能耗;同时又由于双组份复合纤维中两组份之间界面的相互作用力,束缚了双组份复合纤维中高收缩组份的收缩,因此双组份复合纤维中高收缩组份并没有完全充分地收缩。(2) The present invention adds a hot air device after forming a net curtain, and the high shrinkage component in the two-component composite fiber is shrunk by heat through the hot air device, and the two-component composite fiber is split by utilizing the different shrinkage rates of the two components trend, and even some fibers have been split, which reduces the spunlace pressure in the subsequent spunlace fiber opening process, which can greatly reduce the energy consumption of spunlace; at the same time, because the two components in the bicomponent composite fiber The interaction force between the interfaces restrains the shrinkage of the high-shrinkage component in the bicomponent composite fiber, so the high-shrinkage component in the bicomponent composite fiber does not fully shrink.

(3)水刺压力的降低,可大幅度降低水刺能耗,同时水刺压力降低使得非织造布中锲型的超细纤维排列相对疏松,便于后续高收缩组份的完全收缩。(3) The reduction of spunlace pressure can greatly reduce the energy consumption of spunlace. At the same time, the reduction of spunlace pressure makes the wedge-shaped microfiber arrangement in the nonwoven fabric relatively loose, which facilitates the complete shrinkage of subsequent high-shrinkage components.

(4)本发明在水刺工艺后添加纤维卷缩装置,通过纤维卷缩装置使得双组份复合纤维中的高收缩组份充分收缩卷曲,避免造成裂离后锲型的超细纤维紧密堆积,非织造布表面产生立绒的效果,同时使未裂离完全的纤维充分裂离,使非织造布具有柔软挺括、手感饱满的特点,克服了双组份纺粘水刺非织造布作为革基布在性能上的缺陷。(4) In the present invention, a fiber crimping device is added after the spunlace process, and the high-shrinkage component in the bicomponent composite fiber is fully shrunk and crimped through the fiber crimping device, so as to avoid tight accumulation of wedge-shaped ultrafine fibers after splitting , the surface of the non-woven fabric has the effect of velvet, and at the same time, the uncracked fibers are fully split, so that the non-woven fabric has the characteristics of softness, crispness and full hand feeling, which overcomes the two-component spunbonded spunlace nonwoven fabric as a leather Defects in the performance of the base cloth.

(5)本方法工艺流程简单,生产成本及能耗低,可一步法实现超纤革基布绿色清洁化的制备,制备的中空桔瓣型双组份纺粘水刺革基布具有致密、柔软、挺括、手感饱满的特点。(5) The process of the method is simple, the production cost and energy consumption are low, and the green and clean preparation of the microfiber leather base cloth can be realized in one step. Soft, crisp, and full-feeling features.

附图说明Description of drawings

图1为本发明的工艺路线示意图;Fig. 1 is a schematic diagram of the process route of the present invention;

图2为本发明实施例1的纤维网经热风装置处理后的纤维的形貌图;Fig. 2 is the topographic view of the fibers of the fiber web of Example 1 of the present invention after being treated by a hot air device;

图3为本发明实施例1制备的超纤革基布的表面微观形貌图;Fig. 3 is the surface microscopic appearance figure of the superfiber leather base cloth that the embodiment of the present invention 1 prepares;

图4为本发明实施例1制备的超纤革基布的截面微观形貌图;Fig. 4 is the cross-sectional micro-morphological figure of the microfiber leather base cloth prepared in Example 1 of the present invention;

图5为本发明对比例1的长纤的形貌图;Fig. 5 is the topography figure of the long fiber of comparative example 1 of the present invention;

图6为本发明对比例1制备的超纤革基布的表面微观形貌图;Fig. 6 is the surface microscopic topography figure of the superfiber leather base cloth that comparative example 1 of the present invention prepares;

图7为本发明对比例1制备的超纤革基布的截面微观形貌图。7 is a cross-sectional microscopic view of the microfiber leather base cloth prepared in Comparative Example 1 of the present invention.

图中,1、料斗;2、螺杆挤出机;3、计量泵;4、双组份纺丝组件;5、侧吹风冷却装置;6、气流牵伸装置;7、成网帘;8、负压抽吸装置;9、长丝纤维网;10、热风装置;11、低压水刺头;12、水抽吸装置;13、抽吸辊筒;14、高压水刺头;15、压辊;16、纤维卷缩装置;17、导辊;18、干燥箱;19、卷绕装置。In the figure, 1. Hopper; 2. Screw extruder; 3. Metering pump; 4. Two-component spinning assembly; 5. Side blowing cooling device; 6. Air drafting device; 7. Web curtain; 8. Negative pressure suction device; 9. Filament fiber web; 10. Hot air device; 11. Low-pressure spunlace head; 12. Water suction device; 13. Suction roller; 14. High-pressure spunlace head; 15. Pressure roller 16. Fiber crimping device; 17. Guide roller; 18. Drying box; 19. Winding device.

具体实施方式Detailed ways

下面给出本发明的具体实施例。具体实施例仅用于进一步详细说明本发明,不限制本申请权利要求的保护范围。Specific examples of the present invention are given below. The specific embodiments are only used to further describe the present invention in detail, and do not limit the protection scope of the claims of the present application.

本发明提供了一种高收缩桔瓣型双组份纺粘水刺超纤革基布的制备方法(简称方法),其特征在于,该方法包括以下步骤:The present invention provides a kind of preparation method (abbreviation method) of high-shrinkage segmental orange type two-component spunbonded spunlace superfiber leather base cloth, it is characterized in that, this method comprises the following steps:

(1)在双组份纺粘/水刺生产线中加入热风装置10和纤维卷缩装置16;按照纺程方向,热风装置10设置于成网帘7与水刺工艺之间,即成网帘7的后方(即纤维形成纤维网9以后的位置)、水刺工艺的前方;纤维卷缩装置16设置于压辊15与干燥箱18之间,即压辊15的后方、干燥箱18的前方;(1) Add a hot air device 10 and a fiber crimping device 16 in the two-component spunbond/spunlace production line; according to the spinning direction, the hot air device 10 is installed between the web forming curtain 7 and the spunlace process, that is, the web forming curtain 7 (that is, the position after the fibers form the fiber web 9), and the front of the spunlace process; the fiber crimping device 16 is arranged between the pressing roller 15 and the drying box 18, that is, behind the pressing roller 15 and in front of the drying box 18 ;

(2)双组份复合纤维纺丝成网:首先将两种聚合物通过共轭纺丝形成双组份原生丝熔体;然后经侧吹风冷却装置5的冷却固化、气流牵伸装置6的高速气流牵伸,双组份复合纤维在负压抽吸装置8的作用下在成网帘7上均匀铺网,形成纤维网9;(2) Two-component composite fiber is spun into a net: first, two kinds of polymers are formed into a two-component raw silk melt by conjugate spinning; Drafting by high-speed airflow, the two-component composite fiber is evenly laid on the web forming curtain 7 under the action of the negative pressure suction device 8 to form a fiber web 9;

两种聚合物中的至少一种为高收缩聚合物,另一种为能与高收缩聚合物复合纺丝的常规聚合物;At least one of the two polymers is a high-shrinkage polymer, and the other is a conventional polymer capable of co-spinning with the high-shrinkage polymer;

优选地,步骤(2)中,所述共轭纺丝是将两种聚合物切片分别导入干燥塔里进行预结晶和干燥处理,然后分别通过各自的料斗1送入各自的螺杆挤出机2内熔融成聚合物熔体,然后两种聚合物熔体经各自的熔体过滤系统过滤杂质后,再通过各自的计量泵3分别以一定的压力共同喂入双组份纺丝组件4中,在双组份纺丝组件4的喷丝板内以规律的交替排列形式从喷丝孔内挤出,形成双组份原生丝熔体;Preferably, in step (2), the conjugate spinning is to introduce the two kinds of polymer slices into the drying tower for pre-crystallization and drying treatment, and then send them into the respective screw extruders 2 through the respective hoppers 1 The two polymer melts are melted into a polymer melt, and then the two polymer melts are filtered through their respective melt filtration systems, and then fed into the two-component spinning assembly 4 through their respective metering pumps 3 at a certain pressure. In the spinneret of the two-component spinning assembly 4, it is extruded from the spinneret hole in a regular alternate arrangement to form a two-component raw silk melt;

优选地,步骤(2)中,两种聚合物的溶解度参数差值大于0.5;所述高收缩聚合物为高收缩涤纶(HSPET)、高收缩锦纶(HSPA6)、高收缩丙纶(HSPP)、高收缩聚丙烯腈(HSPAN)及其改性聚合物;常规聚合物为聚酯、聚酰胺、聚乳酸、聚丙烯、聚乙烯及其共混物、共聚物或改性聚合物;Preferably, in step (2), the solubility parameter difference of the two polymers is greater than 0.5; the high-shrinkage polymer is high-shrinkage polyester (HSPET), high-shrinkage nylon (HSPA6), high-shrinkage polypropylene (HSPP), high Shrink polyacrylonitrile (HSPAN) and its modified polymers; conventional polymers are polyester, polyamide, polylactic acid, polypropylene, polyethylene and their blends, copolymers or modified polymers;

优选地,步骤(2)中,双组份原生丝熔体中,两种聚合物熔体的体积比为5~7:3~5;双组份复合纤维中高收缩组份的收缩率为15~50%,两组份的收缩率之差大于30%;Preferably, in step (2), in the two-component raw silk melt, the volume ratio of the two polymer melts is 5-7:3-5; the shrinkage rate of the high-shrinkage component in the two-component composite fiber is 15 ~50%, the difference in shrinkage between the two components is greater than 30%;

优选地,步骤(2)中,侧吹风冷却装置5的侧吹风风温为15~28℃,风速为0.2~1m/s,相对湿度为30~90%;Preferably, in step (2), the side blowing air temperature of the side blowing cooling device 5 is 15-28°C, the wind speed is 0.2-1m/s, and the relative humidity is 30-90%;

优选地,步骤(2)中,气流牵伸装置7为管式牵伸器、宽狭缝式牵伸器或窄狭缝式牵伸器,牵伸风压力为0.1~1MPa(优选0.3~0.6MPa),牵伸速度为2000~6000m/s,温度为10~30℃,相对湿度为40~90%;Preferably, in step (2), the airflow drafting device 7 is a tubular drafter, a wide slit drafter or a narrow slit drafter, and the drafting wind pressure is 0.1-1 MPa (preferably 0.3-0.6 MPa), the drawing speed is 2000-6000m/s, the temperature is 10-30°C, and the relative humidity is 40-90%;

优选地,步骤(2)中,纤维网9的面密度为50~250g/m2Preferably, in step (2), the surface density of the fiber web 9 is 50-250 g/m 2 ;

(3)将步骤(2)制得的纤维网9输送入热风装置10中进行热收缩处理,调整热风装置10内的温度、湿度和风速,使得双组份复合纤维中的高收缩组份产生热收缩,利用双组份复合纤维中高收缩组份的热收缩使得双组份复合纤维产生裂离趋势;再经水刺工艺使双组份复合纤维裂离开纤并相互缠结,得到双组份纺粘水刺非织造布;(3) The fiber web 9 that step (2) is made is transported in the hot-air device 10 and carries out heat-shrinkage treatment, adjusts temperature, humidity and wind speed in the hot-air device 10, makes the high-shrinkage component in the two-component composite fiber produce Heat shrinkage, using the heat shrinkage of the high-shrinkage component in the two-component composite fiber to make the two-component composite fiber have a tendency to split; and then through the hydroentanglement process, the two-component composite fiber is split and entangled with each other to obtain a two-component Spunbonded spunlace nonwovens;

优选地,步骤(3)中,热风装置10内的湿度为0~60%、温度为80~180℃,风速为0.01~0.1m/s,保证风速不影响纤维网9的铺设,纤维网9在热风装置10内的停留时间≥2s;Preferably, in step (3), the humidity in the hot air device 10 is 0 to 60%, the temperature is 80 to 180° C., and the wind speed is 0.01 to 0.1 m/s, ensuring that the wind speed does not affect the laying of the fiber web 9, and the fiber web 9 The residence time in the hot air device 10 is ≥ 2s;

优选地,步骤(3)中,热风装置10中纤维网9的输送速度与成网帘7的输送速度保持一致;纤维网9在热风装置10中的输送速度提高,可提高热风装置10内的风速与温度,同时保证纤维网9在热风装置10内的停留时间≥2s。Preferably, in step (3), the conveying speed of fibrous web 9 in the hot-blast device 10 is kept consistent with the conveying speed of web curtain 7; Wind speed and temperature, while ensuring that the residence time of the fiber web 9 in the hot air device 10 is ≥ 2s.

提高热风装置10内的湿度,可降低双组份复合纤维中双组份界面之间的作用力,促进纤维的裂离。Increasing the humidity in the hot air device 10 can reduce the force between the two-component interfaces in the two-component composite fiber and promote the splitting of the fiber.

优选地,步骤(3)中,水刺裂离开纤工艺是:经低压水刺头11预刺,通过高压水刺头14利用高压水射流使双组份复合纤维裂离开纤并相互缠结。Preferably, in step (3), the hydroentanglement splitting process is as follows: the low-pressure hydroentanglement head 11 prepunctures, and the high-pressure hydroentanglement head 14 utilizes high-pressure water jets to split and defiber the two-component composite fibers and entangle each other.

优选地,步骤(3)中,水刺总压力为20~100Mpa。较低的水刺压力便可使得双组份复合纤维裂离开纤,这是由于纤维网经热风装置后,双组份复合纤维的高收缩组份受热收缩,使得纤维已经有明显的裂离趋势,甚至部分纤维已发生裂离,因此纤维网9经水刺时,较低的水刺压力就可使纤维裂离开纤。Preferably, in step (3), the total pressure of spunlace is 20-100 Mpa. The lower spunlace pressure can make the two-component composite fiber split and separate from the fiber. This is because the high-shrinkage component of the two-component composite fiber is heated and shrinks after the fiber web passes through the hot air device, so that the fiber has an obvious tendency to split , even part of the fibers have been split, so when the fiber web 9 is hydroentangled, the lower hydroentanglement pressure can cause the fibers to split and separate.

(4)将步骤(3)制得的双组份纺粘水刺非织造布通过压辊15挤出多余水分后,输送至纤维卷缩装置16中,调整非织造布在纤维卷缩装置16中的输入速度和输出速度,使非织造布的输出速度小于输入速度,保证非织造布处于松弛状态,并调整纤维卷缩装置16内的温度、湿度以及压力,利用纤维卷缩装置16对非织造布进行收缩卷曲处理,使得非织造布中双组份复合纤维的高收缩组份完全收缩卷曲;再经干燥箱18干燥后得到致密、柔软、挺括、手感饱满的双组份纺粘水刺超纤革基布。(4) After the two-component spunbonded spunlaced nonwoven fabric obtained in step (3) is squeezed out of excess water through the pressing roller 15, it is transported to the fiber crimping device 16, and the nonwoven fabric is adjusted to be in the fiber crimping device 16. The input speed and output speed in the middle make the output speed of the nonwoven fabric less than the input speed, ensure that the nonwoven fabric is in a relaxed state, and adjust the temperature, humidity and pressure in the fiber crimping device 16, and use the fiber crimping device 16 to control the nonwoven fabric. The woven fabric is subjected to shrinkage and curling treatment, so that the high-shrinkage component of the two-component composite fiber in the nonwoven fabric is completely shrunk and curled; and then dried in a drying oven 18 to obtain a dense, soft, crisp, and full-feeling two-component spunbond spunlace Microfiber leather backing.

优选地,步骤(4)中,压辊15的压力为0.1~0.5MPa。Preferably, in step (4), the pressure of the pressure roller 15 is 0.1-0.5 MPa.

优选地,步骤(4)中,纤维卷缩装置16对非织造布的收缩卷曲处理为干热收缩、湿热收缩、水浴收缩或高压水蒸汽收缩;干热收缩温度为80~180℃,湿度为0%;湿热收缩湿度为30~100%,温度为60~150℃;水浴收缩中的水浴温度为80~100℃;高压水蒸汽收缩的压力为2~10MPa。Preferably, in step (4), the shrinkage and crimping treatment of the nonwoven fabric by the fiber crimping device 16 is dry heat shrinkage, wet heat shrinkage, water bath shrinkage or high-pressure water vapor shrinkage; the dry heat shrinkage temperature is 80-180°C, and the humidity is 0%; damp heat shrinkage humidity is 30-100%, temperature is 60-150°C; water bath temperature in water-bath shrinkage is 80-100°C; pressure of high-pressure water vapor shrinkage is 2-10MPa.

优选地,步骤(4)中,非织造布的面密度为50~80g/m2,非织造布在纤维卷缩装置16中的停留时间为2~3s;非织造布的面密度为80~140g/m2,非织造布在纤维卷缩装置16中的停留时间为3~5s;非织造布的面密度≥140g/m2,非织造布在纤维卷缩装置16中的停留时间≥5s。Preferably, in step (4), the areal density of the nonwoven fabric is 50 to 80 g/m 2 , the residence time of the nonwoven fabric in the fiber crimping device 16 is 2 to 3 s; the areal density of the nonwoven fabric is 80 to 80 g/m 2 . 140g/m 2 , the residence time of the nonwoven fabric in the fiber crimping device 16 is 3 to 5s; the surface density of the nonwoven fabric is ≥140g/m 2 , and the residence time of the nonwoven fabric in the fiber crimping device 16 is ≥5s .

优选地,步骤(4)中,纤维卷缩装置16内设置有若干组导辊17;导辊17的个数≥3,导辊17沿非织造布的输送方向上下交替排布,非织造布在导辊17中呈S型路径行进;调整导辊17的速度,可调整非织造布在纤维卷缩装置16中的输入速度和输出速度以及非织造布在纤维卷缩装置16中的停留时间。Preferably, in step (4), several groups of guide rollers 17 are arranged in the fiber crimping device 16; the number of guide rollers 17 is ≥ 3, and the guide rollers 17 are alternately arranged up and down along the conveying direction of the nonwoven fabric. Travel in an S-shaped path in the guide roller 17; adjust the speed of the guide roller 17 to adjust the input speed and output speed of the nonwoven fabric in the fiber crimping device 16 and the residence time of the nonwoven fabric in the fiber crimping device 16 .

双组份纺粘水刺非织造布的开纤率为30~60%,双组份纺粘水刺超纤革基布的开纤率达到80~100%。The fiber opening rate of the two-component spunbond spunlace nonwoven fabric is 30-60%, and the fiber opening rate of the two-component spunbond spunlace microfiber leather base cloth reaches 80-100%.

与现有技术相比只要在不损害本发明效果的范围内,可以根据需要向本发明所使用的聚合物中添加功能性粒子,如通常所使用的抗静电剂、光稳定剂、抗氧化剂、耐气候稳定剂、防雾剂、防粘连剂、润滑剂、成核剂及颜料等添加剂、或其他聚合物。Compared with the prior art, as long as it does not impair the effect of the present invention, functional particles can be added to the polymer used in the present invention as required, such as commonly used antistatic agents, light stabilizers, antioxidants, Additives such as weather-resistant stabilizers, anti-fogging agents, anti-blocking agents, lubricants, nucleating agents and pigments, or other polymers.

实施例1Example 1

本实施例制备的是HSPET-PA6中空桔瓣型双组份纺粘水刺超纤革基布,具体步骤如下:In this example, the HSPET-PA6 hollow orange segment two-component spunbonded spunlace superfiber leather base fabric is prepared, and the specific steps are as follows:

(1)将热风装置10和纤维卷缩装置16加入双组份纺粘/水刺生产线中,热风装置10安装于成网帘7的后方,纤维卷缩装置16安装于压辊15的后方;(1) Add the hot air device 10 and the fiber crimping device 16 into the two-component spunbond/spunlace production line, the hot air device 10 is installed behind the web curtain 7, and the fiber crimping device 16 is installed behind the pressure roller 15;

(2)将HSPET和PA6两种聚合物切片分别导入干燥塔里进行预结晶和干燥处理,经螺杆挤压机挤压熔融、熔体过滤系统过滤后,在双组份纺丝组件4完成复合纺丝,然后经侧吹风冷却、气流牵伸,在成网帘7上均匀铺网;侧吹风温度为20℃,相对湿度为70%,风速为1m/s,牵伸压力为0.55Mpa,牵伸速度为5000m/min,纤维网面密度为160g/m2(2) Import HSPET and PA6 polymer slices into the drying tower for pre-crystallization and drying treatment respectively. After extruded and melted by a screw extruder and filtered by a melt filtration system, the compounding is completed in the two-component spinning assembly 4 Spinning, then cooled by side blowing, air drafting, and evenly laid on the netting curtain 7; the temperature of side blowing is 20°C, the relative humidity is 70%, the wind speed is 1m/s, and the drawing pressure is 0.55Mpa. The elongation speed is 5000m/min, and the surface density of the fiber web is 160g/m 2 ;

HSPET与PA6熔体的体积比为7:3,HSPET切片中添加第三单体间苯二甲酸和第四单体新戊二醇。HSPET切片的特性粘度为0.63dL/g,PA6切片的相对粘度为2.46dL/g;The volume ratio of HSPET to PA6 melt is 7:3, and the third monomer isophthalic acid and the fourth monomer neopentyl glycol are added to the HSPET chips. The intrinsic viscosity of HSPET chips is 0.63dL/g, and the relative viscosity of PA6 chips is 2.46dL/g;

(3)将纤维网输送入热风装置内,使双组份复合纤维的高收缩组份受热收缩,热风装置设置条件为温度90℃、湿度30%、风速0.05m/s,如图2,桔瓣型双组份复合纤维出现裂离趋势,部分纤维发生裂离;再经水刺工艺使双组份复合纤维裂离开纤并相互缠结,得到双组份纺粘水刺非织造布,水刺总压力为60Mpa;(3) Convey the fiber web into the hot air device, so that the high shrinkage component of the two-component composite fiber is heated and shrunk. The hot air device is set at a temperature of 90°C, a humidity of 30%, and a wind speed of 0.05m/s, as shown in Figure 2, orange The petal-shaped two-component composite fiber tends to split, and some fibers are split; then the two-component composite fiber is split and entangled with each other through the spunlace process to obtain a two-component spunbonded spunlace nonwoven fabric. The total pressure of stabbing is 60Mpa;

(4)将双组份纺粘水刺非织造布通过压辊15将水分充分挤压出去,输送入纤维卷缩装置16进行收缩处理,再经干燥箱18干燥后得到双组份纺粘水刺超纤革基布;纤维卷缩装置设定条件为水浴收缩,水浴温度为90℃,纤维卷缩装置中导辊的个数为3,非织造布在导辊上沿呈S型路径行进;(4) The two-component spunbond spunlace nonwoven fabric is fully squeezed out by the pressure roller 15, and then transported into the fiber crimping device 16 for shrinkage treatment, and then dried in the drying oven 18 to obtain a two-component spunbonded water Pricked microfiber leather base fabric; the setting condition of the fiber crimping device is water bath shrinkage, the temperature of the water bath is 90°C, the number of guide rollers in the fiber crimping device is 3, and the nonwoven fabric travels along an S-shaped path on the guide rollers ;

制备的双组份纺粘水刺超纤革基布的面密度为210g/m2,密度为0.315g/cm3,开纤率为93%,柔软度为5.3mm;由图3可以看出,革基布表面出现立绒,纤维裂离完全。由图4可以看出,双组份复合纤维已基本裂离完全,纤维收缩后未导致锲型纤维紧密堆积,纤维有一定的滑移空间,革基布的柔软度、饱满性大幅度提高。The surface density of the prepared two-component spunbonded spunlaced microfiber leather base cloth is 210g/m 2 , the density is 0.315g/cm 3 , the fiber opening rate is 93%, and the softness is 5.3mm; it can be seen from Figure 3 , The surface of the leather base fabric has a pile, and the fibers are completely separated. It can be seen from Figure 4 that the two-component composite fibers have been basically split completely, and the wedge-shaped fibers have not been closely packed after fiber shrinkage, and the fibers have a certain sliding space, and the softness and plumpness of the leather base fabric have been greatly improved.

对比例1Comparative example 1

本对比例制备的是PET-PA6中空桔瓣型双组份纺粘水刺超纤革基布,具体步骤如下:In this comparative example, a PET-PA6 hollow orange petal type two-component spunbonded spunlace microfiber leather base fabric is prepared, and the specific steps are as follows:

(1)将热风装置10和纤维卷缩装置16加入双组份纺粘/水刺生产线中,热风装置安装于成网帘7的后方,纤维卷缩装置16安装于压辊15的后方;(1) Add the hot air device 10 and the fiber crimping device 16 into the two-component spunbond/spunlace production line, the hot air device is installed behind the web curtain 7, and the fiber crimping device 16 is installed behind the pressure roller 15;

(2)将PET和PA6两种聚合物切片分别导入干燥塔里进行预结晶和干燥处理,经螺杆挤压机挤压熔融、熔体过滤系统过滤后,在双组份纺丝组件4完成复合纺丝,然后经侧吹风冷却、气流牵伸,在成网帘上均匀铺网;侧吹风温度为20℃,相对湿度为70%,风速为1m/s,牵伸压力为0.55Mpa,牵伸速度为5000m/min,纤维网面密度为160g/m2(2) Import PET and PA6 polymer slices into the drying tower for pre-crystallization and drying treatment respectively. After extruding and melting by a screw extruder and filtering by a melt filtration system, the compounding is completed in the two-component spinning assembly 4 Spinning, then cooled by side blowing, air drafting, and laying the net evenly on the web-forming curtain; the temperature of side blowing is 20°C, the relative humidity is 70%, the wind speed is 1m/s, and the drawing pressure is 0.55Mpa. The speed is 5000m/min, and the surface density of the fiber web is 160g/m 2 ;

PET与PA6熔体的体积比为7:3,PET切片的特性粘度为0.64dL/g,PA6切片的相对粘度为2.66dL/g;The volume ratio of PET to PA6 melt is 7:3, the intrinsic viscosity of PET chips is 0.64dL/g, and the relative viscosity of PA6 chips is 2.66dL/g;

(3)将纤维网输送入热风装置内,使双组份复合纤维的高收缩组份受热收缩,热风装置设置条件为温度90℃、湿度30%、风速0.05m/s,如图5,桔瓣型双组份复合纤维未出现裂离趋势;再经水刺工艺使双组份复合纤维裂离开纤并相互缠结,得到双组份纺粘水刺非织造布,水刺总压力为60Mpa;(3) Convey the fiber web into the hot air device, so that the high shrinkage component of the two-component composite fiber is heated and shrunk. The hot air device is set at a temperature of 90°C, a humidity of 30%, and a wind speed of 0.05m/s, as shown in Figure 5, orange The petal-shaped two-component composite fiber does not show a splitting tendency; the two-component composite fiber is split and entangled with each other through the spunlace process to obtain a two-component spunbonded spunlace nonwoven fabric, and the total pressure of the spunlace is 60Mpa ;

(4)将双组份纺粘水刺非织造布通过压辊15将水分充分挤压出去,输送入纤维卷缩装置进行处理,再经干燥箱18干燥后得到双组份纺粘水刺超纤革基布;纤维卷缩装置设定条件为水浴收缩,水浴温度为90℃,纤维卷缩装置中导辊的个数为3,非织造布在导辊上沿呈S型路径行进;(4) The two-component spunbonded spunlace nonwoven fabric is fully squeezed out by the pressure roller 15, and then transported to the fiber crimping device for treatment, and then dried in the drying oven 18 to obtain a two-component spunbonded spunlace nonwoven fabric. Fiber leather base fabric; the setting condition of the fiber crimping device is water bath shrinkage, the temperature of the water bath is 90°C, the number of guide rollers in the fiber crimping device is 3, and the nonwoven fabric travels along an S-shaped path on the guide rollers;

制备的双组份纺粘水刺超纤革基布的面密度为160g/m2,密度为0.37g/cm3,开纤率为34%,柔软度为3.4mm;由图6可以看出,超纤革基布表面纤维平行排列,表面纤维已基本裂离。由图7可以看出,桔瓣型双组份复合纤维通过高压水射流裂离开纤,存在夹心开纤的现象。The surface density of the prepared two-component spunbonded spunlaced microfiber leather base cloth is 160g/m 2 , the density is 0.37g/cm 3 , the fiber opening rate is 34%, and the softness is 3.4mm; it can be seen from Figure 6 , The surface fibers of the microfiber leather base cloth are arranged in parallel, and the surface fibers have basically been split. It can be seen from Figure 7 that the bicomponent composite fibers of the segmented orange shape are separated from the fibers by high-pressure water jets, and there is a phenomenon of sandwich fiber splitting.

实施例2Example 2

本实施例制备的是HSPET-PA6中空桔瓣型双组份纺粘水刺超纤革基布,具体步骤如下:In this example, the HSPET-PA6 hollow orange segment two-component spunbonded spunlace superfiber leather base fabric is prepared, and the specific steps are as follows:

(1)将热风装置和纤维卷缩装置加入双组份纺粘/水刺生产线中,热风装置安装于成网帘的后方,纤维卷缩装置安装于压辊的后方;(1) Add the hot air device and fiber crimping device to the two-component spunbond/spunlace production line, the hot air device is installed behind the web curtain, and the fiber crimping device is installed behind the pressure roller;

(2)将HSPET和PA6两种聚合物切片分别导入干燥塔里进行预结晶和干燥处理,经螺杆挤压机挤压熔融、熔体过滤系统过滤后,在双组份纺丝组件4完成复合纺丝,然后经侧吹风冷却、气流牵伸,在成网帘7上均匀铺网;侧吹风温度为25℃,相对湿度为80%,风速为1m/s,牵伸压力为0.5MPa,牵伸速度为4000m/min,纤维网面密度为120g/m2(2) Import HSPET and PA6 polymer slices into the drying tower for pre-crystallization and drying treatment respectively. After extruded and melted by a screw extruder and filtered by a melt filtration system, the compounding is completed in the two-component spinning assembly 4 Spinning, then cooled by side air blowing, air drafting, and evenly laid on the web forming curtain 7; The elongation speed is 4000m/min, and the surface density of the fiber web is 120g/m 2 ;

HSPET与PA6熔体的体积比为5:5,HSPET切片中添加第三单体间苯二甲酸和第四单体新戊二醇,HSPET切片的特性粘度为0.65dL/g,PA6切片的相对粘度为2.52dL/g;The volume ratio of HSPET to PA6 melt is 5:5, the third monomer isophthalic acid and the fourth monomer neopentyl glycol are added to HSPET chips, the intrinsic viscosity of HSPET chips is 0.65dL/g, and the relative viscosity of PA6 chips is The viscosity is 2.52dL/g;

(3)将纤维网输送入热风装置内,使双组份复合纤维的高收缩组份受热收缩,热风装置设置条件为温度100℃、湿度20%、风速0.01m/s,桔瓣型双组份复合纤维出现裂离趋势,部分纤维已经发生裂离;再经水刺工艺使双组份复合纤维裂离开纤并相互缠结,得到双组份纺粘水刺非织造布,水刺总压力为80Mpa;(3) Convey the fiber web into the hot air device, so that the high-shrinkage component of the two-component composite fiber is heated and shrunk. The hot air device is set at a temperature of 100°C, a humidity of 20%, and a wind speed of 0.01m/s. Part of the composite fiber tends to split, and some fibers have already split; then the two-component composite fiber is split and entangled with each other through the spunlace process to obtain a two-component spunbonded spunlace nonwoven fabric. The total pressure of the spunlace 80Mpa;

(4)将双组份纺粘水刺非织造布通过压辊15将水分充分挤压出去,输送入纤维卷缩装置进行收缩处理,再经干燥箱18干燥后得到双组份纺粘水刺超纤革基布;纤维卷缩装置设定条件为干热收缩,温度为120℃,纤维卷缩装置中导辊的个数为4,导辊沿双组份纺粘水刺非织造布输送方向上下交替排列;(4) The two-component spunbonded spunlace nonwoven fabric is fully squeezed out by the pressure roller 15, and then transported into the fiber crimping device for shrinkage treatment, and then dried in the drying oven 18 to obtain a two-component spunbonded spunlace nonwoven fabric. Microfiber leather base fabric; the setting condition of the fiber crimping device is dry heat shrinkage, the temperature is 120°C, the number of guide rollers in the fiber crimping device is 4, and the guide rollers are conveyed along the two-component spunbonded spunlaced nonwoven fabric The directions are arranged alternately up and down;

制备的双组份纺粘水刺超纤革基布的面密度为180g/m2,密度为0.33g/cm3,开纤率为96%,柔软度为5.8mm;纤维基本完全裂离,纤维收缩后未导致锲型纤维紧密堆积,纤维有一定的滑移空间,革基布的柔软度、饱满性大幅度提高。The surface density of the prepared two-component spunbonded spunlaced microfiber leather base cloth is 180g/m 2 , the density is 0.33g/cm 3 , the fiber opening rate is 96%, and the softness is 5.8mm; the fibers are basically completely detached, After fiber shrinkage, the wedge-shaped fibers do not accumulate tightly, and the fibers have a certain space for slipping, and the softness and plumpness of the leather base fabric are greatly improved.

对比例2Comparative example 2

本对比例制备的是HSPET-PA6中空桔瓣型双组份纺粘水刺超纤革基布,具体步骤如下:In this comparative example, HSPET-PA6 hollow orange segment type two-component spunbonded spunlace microfiber leather base fabric is prepared, and the specific steps are as follows:

(1)将HSPET和PA6两种聚合物切片分别导入干燥塔里进行预结晶和干燥处理,经螺杆挤压机挤压熔融、熔体过滤系统过滤后,在双组份纺丝组件4完成复合纺丝,然后经侧吹风冷却、气流牵伸,在成网帘7上均匀铺网;侧吹风温度为25℃,相对湿度为80%,风速为1m/s,牵伸压力为0.5MPa,牵伸速度为4000m/min,纤维网面密度为120g/m2(1) The HSPET and PA6 polymer slices are respectively introduced into the drying tower for pre-crystallization and drying treatment, extruded and melted by the screw extruder, filtered by the melt filtration system, and then compounded in the two-component spinning assembly 4 Spinning, then cooled by side air blowing, air drafting, and evenly laid on the web forming curtain 7; The elongation speed is 4000m/min, and the surface density of the fiber web is 120g/m 2 ;

HSPET与PA6熔体的体积比为5:5,HSPET切片中添加第三单体间苯二甲酸和第四单体新戊二醇,HSPET切片的特性粘度为0.65dL/g,PA6切片的相对粘度为2.52dL/g;The volume ratio of HSPET to PA6 melt is 5:5, the third monomer isophthalic acid and the fourth monomer neopentyl glycol are added to HSPET chips, the intrinsic viscosity of HSPET chips is 0.65dL/g, and the relative viscosity of PA6 chips is The viscosity is 2.52dL/g;

(2)将纤维网经水刺工艺使桔瓣型双组份复合纤维裂离开纤,并相互缠结,得到双组份纺粘水刺非织造布,水刺总压力为80Mpa;(2) Spunlace the fiber web through the spunlace process to split the segmental-shaped two-component composite fibers into fibers and entangle with each other to obtain a two-component spunbond spunlace nonwoven fabric, and the total pressure of the spunlace is 80Mpa;

(3)将双组份纺粘水刺非织造布通过压辊15将水分充分挤压出去,再经干燥箱18烘干后得到双组份纺粘水刺超纤革基布。(3) The two-component spunbonded spunlaced nonwoven fabric is fully squeezed out by the pressure roller 15, and then dried in the drying oven 18 to obtain the two-component spunbonded spunlace microfiber leather base cloth.

制备的超纤革基布的面密度为120g/m2,密度为0.38g/cm3,开纤率为36%,柔软度为3.2mm。The surface density of the prepared microfiber leather base cloth is 120 g/m 2 , the density is 0.38 g/cm 3 , the opening rate is 36%, and the softness is 3.2 mm.

实施例1、实施例2以及对比例1、对比例2的产品性能检测结果如表1和表2:The product performance testing result of embodiment 1, embodiment 2 and comparative example 1, comparative example 2 is as table 1 and table 2:

表1纤维性能Table 1 Fiber properties

检测项目Test items 实施例1Example 1 实施例2Example 2 对比例1Comparative example 1 对比例2Comparative example 2 纤维细度/(dtex)Fiber fineness/(dtex) 2.562.56 2.632.63 2.592.59 2.632.63 断裂强力/(cN/dtex)Breaking strength/(cN/dtex) 2.832.83 2.682.68 2.752.75 2.682.68 断裂伸长率/(%)Elongation at break/(%) 90.0290.02 89.4589.45 60.5460.54 89.4589.45 收缩率/(%)Shrinkage/(%) 12.5712.57 12.6312.63 1.11.1 12.6312.63

表2非织造布性能Table 2 Nonwoven properties

Figure BDA0003155151380000071
Figure BDA0003155151380000071

Figure BDA0003155151380000081
Figure BDA0003155151380000081

由表1和表2可以看出,采用高收缩聚合物切片作为桔瓣型双组份复合纤维的其中一组份,纤维受热收缩后收缩率大幅度提高,同时在双组份纺粘水刺设备的基础上,首先在成网帘后添加热风装置,通过高收缩组份受热收缩,使得纤维有裂离趋势,甚至有部分纤维裂离,后续水刺工艺过程中的水刺压力随之降低,可极大地降低水刺能耗;其次添加纤维卷缩装置,经水刺后的超细纤维非织造布通过纤维卷缩装置,利用高收缩组份的热收缩使纤维收缩卷曲,避免造成锲型的桔瓣型双组份复合纤维紧密堆积,非织造布产生立绒的效果,同时使未裂离完全的纤维充分裂离,克服了双组份纺粘水刺非织造布作为革基布在性能上的缺陷。制备的中空桔瓣型双组份纺粘水刺超纤革基布具有致密、柔软、手感饱满、挺括的特点。It can be seen from Table 1 and Table 2 that when high-shrinkage polymer chips are used as one of the components of the pie-shaped two-component composite fiber, the shrinkage rate of the fiber is greatly improved after thermal shrinkage, and at the same time, the two-component spunbond spunlace On the basis of the equipment, first add a hot air device after forming the web curtain, and the high-shrinkage component is heated and shrunk, so that the fibers tend to split, and even some fibers split, and the spunlace pressure in the subsequent spunlace process decreases accordingly. , which can greatly reduce the energy consumption of spunlace; secondly, a fiber crimping device is added, and the superfine fiber nonwoven fabric after spunlace passes through the fiber crimping device, and the heat shrinkage of the high-shrinkage component is used to shrink and curl the fiber to avoid causing wedging The orange segment type two-component composite fibers are closely packed, and the nonwoven fabric produces the effect of pile pile, and at the same time, the uncracked fibers are fully split, which overcomes the two-component spunbonded spunlace nonwoven fabric as a leather base fabric. Deficiencies in performance. The prepared hollow orange segment two-component spunbonded spunlace microfiber leather base fabric has the characteristics of compactness, softness, full hand feeling and crispness.

实施例1与对比例1相比,采用高收缩聚合物切片作为桔瓣型双组份复合纤维的其中一组份,双组份纺粘水刺非织造布受热收缩,面密度增加,密度降低14.8%,开纤率提升173.5%,柔软度提升55.9%,纤维的卷曲使得非织造布纵横强力比明显改善,断裂伸长率提高,明显改善了双组份纺粘水刺超纤革基布的蓬松度、柔软度、延展性。Example 1 Compared with Comparative Example 1, the high-shrinkage polymer chip is used as one of the components of the pie-shaped two-component composite fiber, and the two-component spunbonded spunlace nonwoven fabric shrinks when heated, the surface density increases, and the density decreases 14.8%, the opening rate increased by 173.5%, and the softness increased by 55.9%. The crimp of the fiber significantly improved the aspect ratio of the nonwoven fabric, and the elongation at break increased, which significantly improved the performance of the two-component spunbond spunlace microfiber leather base fabric. Fluffiness, softness and extensibility.

实施例2与对比例2相比,通过添加热风装置和纤维卷缩装置,桔瓣型双组份复合纤维中高收缩组份充分收缩,面密度增加,密度降低15.1%,开纤率提升166.6%,柔软度提升81.25%,纤维的卷曲使得非织造布纵横强力比明显改善,断裂伸长率提高,明显改善了双组份纺粘水刺超纤革基布的蓬松度、柔软度、延展性。Example 2 Compared with Comparative Example 2, by adding a hot air device and a fiber crimping device, the high-shrinkage component in the pie-shaped two-component composite fiber is fully shrunk, the surface density is increased, the density is reduced by 15.1%, and the fiber opening rate is increased by 166.6%. , the softness is increased by 81.25%, the curl of the fiber makes the aspect ratio of the nonwoven fabric significantly improved, the elongation at break increases, and the bulkiness, softness and ductility of the two-component spunbonded spunlace microfiber leather base fabric are significantly improved .

本发明未述及之处适用于现有技术。What is not mentioned in the present invention is applicable to the prior art.

Claims (9)

1. A preparation method of a high-shrinkage orange-peel-type two-component spun-bonded spunlace microfiber leather base fabric is characterized by comprising the following steps:
(1) A hot air device and a fiber crimping device are added in a double-component spun-bonded/spunlace production line; according to the spinning direction, the hot air device is arranged behind the net forming curtain; the fiber crimping device is arranged behind the compression roller;
(2) Spinning the two-component composite fiber into a net: firstly, forming a two-component primary silk melt by conjugate spinning of two polymers; then, cooling and solidifying by a side-blowing cooling device and air drafting by an air drafting device, and uniformly lapping the two-component composite fibers on a lapping curtain under the action of a negative pressure suction device to form a fiber web;
one of the two polymers is a high-shrinkage polymer, and the other polymer is a conventional polymer capable of being compositely spun with the high-shrinkage polymer;
(3) Conveying the fiber web prepared in the step (2) into a hot air device for thermal shrinkage treatment, and utilizing thermal shrinkage of high-shrinkage components in the two-component composite fibers to enable the two-component composite fibers to generate a cracking tendency; then, splitting the two-component composite fibers by a spunlace process, and mutually entwisting to obtain two-component spun-bonded spunlace non-woven fabric;
(4) Conveying the two-component spun-bonded spunlace non-woven fabric prepared in the step (3) into a fiber crimping device, adjusting the input speed and the output speed of the non-woven fabric in the fiber crimping device to enable the output speed of the non-woven fabric to be smaller than the input speed, ensuring that the non-woven fabric is in a loose state, and performing shrinkage crimping treatment on the non-woven fabric by using the fiber crimping device to enable high-shrinkage components of two-component composite fibers in the non-woven fabric to be completely shrunk and crimped to obtain a two-component spun-bonded spunlace leather base fabric;
the shrinkage and curling treatment of the non-woven fabric by the fiber curling device is dry heat shrinkage, damp heat shrinkage, water bath shrinkage or high-pressure steam shrinkage.
2. The method for preparing the high-shrinkage orange-peel type bicomponent spunbond spunlace microfiber leather base fabric according to claim 1, wherein in the step (2), the difference of solubility parameters of the two polymers is greater than 0.5; the conjugate spinning is that two polymer slices are respectively led into a drying tower for pre-crystallization and drying treatment, then the polymer slices are respectively sent into respective screw extruders through respective hoppers to be melted into polymer melts, then the polymer melts are filtered by respective melt filtering systems to remove impurities and then are jointly fed into a multi-component spinning assembly through respective metering pumps, and the polymer melts are extruded from spinneret holes in a spinneret plate of the multi-component spinning assembly in a regular and alternate arrangement mode to form a two-component primary yarn melt; in the two-component primary silk melt, the volume ratio of two polymer melts is 5-7.
3. The preparation method of the high-shrinkage orange-petal type two-component spun-bonded spunlace microfiber leather base cloth according to claim 1, wherein in the step (2), the high-shrinkage polymer is high-shrinkage polyester, high-shrinkage nylon, high-shrinkage polypropylene, high-shrinkage polyacrylonitrile or a modified substance thereof.
4. The preparation method of the high-shrinkage orange petal type two-component spun-bonded spunlace microfiber leather base fabric according to claim 1, wherein in the step (2), the temperature of side air blown by a side air blowing cooling device is 15-28 ℃, the air speed is 0.2-1 m/s, and the relative humidity is 30-90%; the air flow drafting device is a tubular drafting device, a wide slit type drafting device or a narrow slit type drafting device, the pressure of drafting air is 0.1-1 MPa, the temperature is 10-30 ℃, and the relative humidity is 40-90%.
5. The preparation method of the high-shrinkage orange-peel type two-component spun-bonded spunlace microfiber leather base fabric according to claim 1, wherein in the step (3), the heat shrinkage treatment process comprises the following steps: the humidity in the hot air device is 0-60%, the temperature is 80-180 ℃, the wind speed is 0.01-0.1 m/s, and the residence time of the fiber web in the hot air device is more than or equal to 2s.
6. The method for preparing a high-shrinkage orange-peel type bicomponent spunbond spunlace microfiber leather base fabric according to claim 1, wherein in the step (3), the conveying speed of the fiber web in the hot air device is the same as that of the web forming curtain;
the water jet fiber-splitting process comprises the following steps: pre-needling by a low-pressure water needling head, and splitting the two-component composite fibers by the high-pressure water needling head by using high-pressure water jet to separate the fibers and mutually entangle the fibers; the total pressure of the spunlace is 20-100 Mpa.
7. The preparation method of the high-shrinkage orange-petal type two-component spunbond spunlace microfiber leather base cloth according to claim 1, wherein in the step (4), before the two-component spunbond spunlace nonwoven cloth prepared in the step (3) is conveyed to a fiber crimping device, the two-component spunbond spunlace nonwoven cloth prepared in the step (3) is subjected to water extrusion through a compression roller; the pressure of the compression roller is 0.1-0.5 MPa.
8. The preparation method of the high-shrinkage orange-peel type two-component spunbonded spunlace microfiber leather base fabric according to claim 1, wherein in the step (4), the dry heat shrinkage temperature is 80-180 ℃, and the humidity is 0%; the humidity of the damp-heat shrinkage is 30-100%, and the temperature is 60-150 ℃; the water bath temperature in the water bath shrinkage is 80-100 ℃; the contraction pressure of the high-pressure steam is 2-10 MPa;
when the areal density of the non-woven fabric is 50-80 g/m, the residence time of the non-woven fabric in the fiber crimping device is 2-3 s; when the surface density of the non-woven fabric is 80-140 g/m, the residence time of the non-woven fabric in the fiber crimping device is 3-5 s; when the areal density of the non-woven fabric is more than or equal to 140g/m, the residence time of the non-woven fabric in the fiber crimping device is more than or equal to 5s.
9. The method for preparing the high-shrinkage orange-peel type double-component spun-bonded spunlace microfiber leather base fabric according to claim 1, wherein in the step (4), a plurality of groups of guide rollers are arranged in the fiber crimping device; the number of the guide rollers is more than or equal to 3, the guide rollers are alternately arranged up and down along the conveying direction of the non-woven fabric, and the non-woven fabric advances in the guide rollers in an S-shaped path; the speed of the guide rollers can be adjusted, and the input speed and the output speed of the non-woven fabric in the fiber crimping device and the residence time of the non-woven fabric in the fiber crimping device can be adjusted.
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