阅读说明：本技术 一种长丝无纺复合材料及其制备方法 (Filament non-woven composite material and preparation method thereof ) 是由 龚金瑞 刘维国 于 2020-12-22 设计创作，主要内容包括：本发明涉及无纺材料领域,公开了一种长丝无纺复合材料及其制备方法,该长丝无纺复合材料包括由以长丝纤维和超短纤维为原料制得的集合体。其中长丝纤维为合成纤维长丝；超短纤维为亲水性超短纤维；亲水性超短纤维分布在合成纤维长丝中,且亲水性超短纤维与合成纤维长丝相互缠结和/或亲水性超短纤维粘接固定于合成纤维长丝上。本发明以长丝和超短纤维为原料,经过聚合物纺丝及湿法成网工艺方式生产得到长丝无纺复合材料,具有高断裂强力、不易掉屑、手感柔软、吸湿性良好的特点。(The invention relates to the field of non-woven materials, and discloses a filament non-woven composite material and a preparation method thereof. Wherein the filament fibers are synthetic fiber filaments; the ultrashort fibers are hydrophilic ultrashort fibers; the hydrophilic ultrashort fibers are distributed in the synthetic fiber filament, and the hydrophilic ultrashort fibers and the synthetic fiber filament are mutually entangled and/or the hydrophilic ultrashort fibers are adhered and fixed on the synthetic fiber filament. The invention takes the long filaments and the ultrashort fibers as raw materials, and the long filament non-woven composite material is produced by polymer spinning and wet-laying processes, and has the characteristics of high breaking strength, difficult chip dropping, soft hand feeling and good hygroscopicity.)

1. A filament non-woven composite material, comprising an aggregate made of filament fibers (1) and ultra-short fibers (2) as raw materials, characterized in that: the filament fibers are synthetic fiber filaments; the ultrashort fibers are hydrophilic ultrashort fibers; the hydrophilic ultrashort fibers are distributed in the synthetic fiber filament, and the hydrophilic ultrashort fibers and the synthetic fiber filament are mutually entangled and/or the hydrophilic ultrashort fibers are adhered and fixed on the synthetic fiber filament.

2. The filament nonwoven composite of claim 1 wherein: the synthetic fiber filaments are single-component filaments or bicomponent filaments; wherein:

the single-component filament is of a C-shaped section or hollow section surface with a micropore structure; the micropores are communicated with the hollow cavity; and/or

The bicomponent filaments have two side-by-side schemes:

the first scheme is as follows: the bicomponent filament is of a parallel structure with a special-shaped section and has different melting points;

scheme II: the bicomponent filament is a hollow section radial structure.

3. The filament nonwoven composite of claim 2 wherein:

the melting point of the component with the lower melting point in the special-shaped cross section parallel structure is 110-130 ℃; or

The surface of the hollow section radiation type structure is provided with micropores; the micropores are communicated with the hollow cavity.

4. The filament nonwoven composite of claim 2 wherein: the synthetic fiber filaments are crimped filaments.

5. The filament nonwoven composite of claim 1 wherein:

the hydrophilic ultrashort fibers comprise one or more of plant pulp and cellulose fibers; and/or

The length of the hydrophilic ultrashort fibers is 2-18 mm; and/or

The official moisture regain of the hydrophilic ultrashort fibers is more than or equal to 7 percent.

6. A process for the production of a filament nonwoven composite as claimed in any of claims 1 to 5, characterized by the steps of:

(1) preparation of filament web: firstly, melting polymer slices, spinning the obtained polymer melt by a spinning device after filtering and metering, cooling and drafting the polymer melt in sequence after spinning, and then deforming the obtained filament fibers by a deforming device to enable the straight filament fibers to be in a curling state; lapping to prepare a filament fiber net;

(2) preparation of ultra-short fiber web: dispersing the ultra-short fibers in water for pulping, and removing impurities and fiber clusters in the pulp; diluting the slurry, and then carrying out wet forming by a forming machine, and dehydrating to form an ultra-short fiber net;

(3) and (3) superposing and reinforcing the fiber web: firstly, carrying out pre-spunlace on a filament fiber net; then stacking the ultra-short fiber web onto the filament fiber web; carrying out spunlace impact on the front surface and the back surface of the obtained superposed fiber web to enable the ultra-short fibers and the filament fibers to be mutually entangled and reinforced;

(4) and removing redundant water in the laminated fiber web, and finally drying to obtain the filament non-woven composite material.

7. The method of claim 6, wherein:

in the step (1): the deformation device is a mechanical deformation device; and/or

In the step (2), one or more disc mills are adopted for processing in the process of dispersing the ultrashort fibers; removing impurities and fiber clusters by using a slit filtering device; the concentration of the slurry before dilution is 1-3 wt%, and the concentration of the slurry after dilution is 0.2-0.4 wt%; the forming machine is an inclined net forming machine; and/or

In the step (3), the filament fiber net is pre-wetted and then pre-spunlaced; the pre-spunlace pressure is 30-60 bar; firstly carrying out spunlace on one surface of the laminated fiber web by adopting flat-screen spunlace, and then carrying out spunlace on the other surface of the laminated fiber web by adopting round drum spunlace; the spunlace pressure is 50-120 bar; and/or

In the step (4), redundant moisture in the laminated fiber web is removed in a vacuum suction mode; drying by hot air penetration.

8. The method of claim 6, wherein: preparing by a filament non-woven composite material production device; the filament nonwoven composite production apparatus comprises: the device comprises a spinning and web-forming unit, a wet-forming unit, a superposition conveying unit, a spunlace composite unit and a drying unit;

the spinning and web-forming unit sequentially comprises a slicing bin (101), an extruder (102), a melt metering pump (103), a spinning device (104), a cooling device (105), a drafting device (106), a deforming device (107) and a web laying device (108) according to working procedures;

the overlapping conveying unit comprises a net supporting curtain (301), a pre-wetting device (302) and a pre-hydro-entangling device (303); the net supporting curtains are connected end to form a loop capable of circularly rotating; the output end of the lapping device is connected with the input end of the net supporting curtain; a pre-wetting device and a pre-spunlace device are sequentially arranged on one side of the net supporting curtain according to the advancing direction of the net supporting curtain, and a vacuum suction device A (304) and a vacuum suction device B (305) are respectively arranged on the opposite sides of the pre-wetting device and the pre-spunlace device;

the wet-laid unit comprises a slurry preparation system, an inclined wire former (201), a forming wire (202) and a dewatering device (203); the forming nets are connected end to form a loop capable of circularly rotating, and the inclined net former and the dewatering device are sequentially arranged along the rotating direction of the forming nets; the input end of the inclined net former is connected with the output end of the slurry preparation system; the output section of the forming net is connected with a station behind the pre-spunlace device on the net supporting curtain;

the spunlace unit comprises a plurality of flat-screen spunlace heads (401), a round drum spunlace device (402) and a vacuum suction device C (403) which are arranged in front of and behind the process; the flat net spunlace head and the round drum spunlace device are used for respectively spunlacing different surfaces of the laminated fiber net; the flat net water stabs are arranged above the net supporting curtain and positioned on the inner side of the forming net; a vacuum suction device C is arranged below the net supporting curtain corresponding to each flat net water stabs; the drum spunlace device is positioned behind the output end of the net supporting curtain;

the drying unit is positioned behind the circular drum spunlace device, and a vacuum suction device D (404) is arranged in the drying unit.

9. The method of claim 8, wherein: the slurry preparation system comprises a dispersing device (204), a metering pump (208), a liquid storage device (205), a fan pump (206) and a slurry distributor (207) which are connected in sequence; and stirrers are arranged in the dispersing device and the liquid storage device.

10. The method of claim 8, wherein: the circular drum spunlace device comprises a circular drum and a plurality of circular drum spunlace heads facing the circumferential surface of the circular drum.

Technical Field

The invention relates to the field of non-woven materials, in particular to a filament non-woven composite material and a preparation method thereof.

Background

Spunlace nonwoven fabrics, also known as spunlaced nonwovens, are made by spraying high pressure fine water streams onto one or more layers of fibrous webs to entangle the fibers with each other, thereby consolidating the web. The spunlace nonwoven technology is flexible entanglement reinforcement, and does not influence the original characteristics of the fibers and damage the fibers. Therefore, the spunlace nonwoven fabric has the characteristics of soft hand feeling, good air permeability, high hygroscopicity, small strength loss and the like, and is particularly suitable for various sanitary materials.

201410565949.6 discloses a composite spunlace nonwoven fabric and a preparation method thereof, comprising a wiping layer and a non-wiping layer, wherein the wiping layer is made of 100% wood pulp paper material, and the non-wiping layer is made of 100% polyester fiber material. The non-wiping layer is formed by 100% of polyester fibers through cross lapping and spunlacing, and the wiping layer and the non-wiping layer are compounded through spunlacing. The specification states that the longitudinal and transverse strength ratio of the composite spunlace nonwoven fabric is controlled within 2: 1, and the longitudinal and transverse strength is close to each other, so that the composite spunlace nonwoven fabric is not easy to deform; the thickness is thin, no scraps are dropped, the cloth is soft after moisture absorption, and the wiping effect is good; the wear resistance is good, the wiping efficiency is improved by 20%, the service life is prolonged by 30%, and the service performance of the wiping cloth is effectively improved.

The specification describes: by adopting the technical scheme, 68.3g/m²The water absorption capacity of the wood pulp composite spunlaced nonwoven fabric is 480 percent. The scheme has the disadvantage of low water absorption capacity of the material.

The patent 201820214895.2 discloses a three-dimensional spunlace nonwoven fabric, which comprises a plurality of big convex points (2), wherein a first thin area (3) and a second thin area (4) are fixedly arranged between the adjacent big convex points (2), small holes (5) are arranged between the adjacent second thin areas (3), and the small holes (5) are arranged between the adjacent second thin areas (4). The utility model provides a three-dimensional water thorn non-woven fabrics has big bump, three gradient unevenness's structure and mesh, uses to feel plump, cleans effectually, is the clean material of ideal. Tests show that the product produced by adopting the technical scheme has a density of 70g/m²The longitudinal breaking strength of the spunlaced nonwoven fabric is 191.5N/5 x 10cm, and the transverse direction of the spunlaced nonwoven fabric isThe breaking strength was 30N/5 x 10 cm. The defects of the scheme are that the difference of the longitudinal and transverse breaking strengths of the product is large, and the transverse breaking strength is lower.

Patent 201510117516.9 discloses a production process of an ultra-thin antibacterial spunlace surgical wiping material, belonging to the technical field of textile materials, wherein mixed fibers of hydrophilic polyester fibers and viscose fibers are selected as raw materials and are sequentially fed into a long curtain, a horizontal opener and a large-bin cotton mixing box; then, carrying out layered treatment by a first fine opener and a second fine opener, feeding the raw materials treated by the first fine opener into a first cotton storage box, a first airflow cotton box, a first carding machine, a cross lapping machine and a drafting machine in sequence, and feeding the raw materials treated by the second fine opener into a second cotton storage box, a second airflow cotton box and a second carding machine in sequence; and then overlapping the two layers of raw materials, and sequentially performing a spunlace process, an antibacterial treatment process, a drying process, an online detection process, a coiling process, a foam dyeing process and a slitting process. The ultrathin antibacterial spunlace surgical wiping material disclosed by the invention has the advantages of good hygroscopicity, air permeability, sterility and comfort, and good longitudinal moisture conductivity. The disadvantage of this solution is the low breaking strength of the material.

At present, the conventional spunlace nonwoven materials on the market are mainly divided into dry-laid materials and wet-laid materials. The dry spunlace nonwoven material is mostly made by carding, netting and spunlacing of viscose, terylene and other textile short fibers (the length is generally 30-40 mm). Because short fibers are used as raw materials, the longitudinal and transverse breaking strength of the spunlace material is limited to a certain extent. The wet-laid spunlace nonwoven material is generally prepared by adopting materials such as ultra-short fibers, wood pulp and the like through wet-laid and spunlace reinforcement. Such wet spunlace nonwoven materials are most commonly used in disposable flushable hygiene articles where the breaking strength of the product is low.

In recent years, companies have utilized chemical fiber spinning principles to produce spun-bonded spunlaced nonwovens from continuous filaments laid into a web during polymer spinning and then hydroentangled. Although the breaking strength of the spun-bonded spunlace nonwoven material is high, the product has poor hygroscopicity and hard hand feeling due to the adoption of 100% chemical fiber components, is not suitable for disposable sanitary materials, and the application range of the product is influenced.

In view of the above problems in the prior art, there is a need to develop a differentiated spunlace nonwoven material with high breaking strength and good moisture absorption to meet the needs of the medical and sanitary material markets.

Disclosure of Invention

The invention provides a filament non-woven composite material and a preparation method thereof, aiming at solving the problems of low breaking strength, easy chip dropping, poor hygroscopicity of the conventional spun-bonded spunlace non-woven material, stiff hand feeling and the like of the conventional spun-bonded spunlace non-woven material.

The specific technical scheme of the invention is as follows:

in a first aspect, the present invention provides a filament nonwoven composite comprising an assembly made from filament fibers and ultra-short fibers. The filament fibers are synthetic fiber filaments; the ultrashort fibers are hydrophilic ultrashort fibers; the hydrophilic ultrashort fibers are distributed in the synthetic fiber filament, and the hydrophilic ultrashort fibers and the synthetic fiber filament are mutually entangled and/or the hydrophilic ultrashort fibers are adhered and fixed on the synthetic fiber filament.

Preferably, the synthetic fiber filaments are monocomponent filaments or bicomponent filaments.

Preferably, the monocomponent filament has a C-shaped section or a hollow section with a microporous surface. Furthermore, when the hollow surface is provided with a micropore structure, micropores on the surface of the single-component filament are communicated with the hollow.

At present, most of synthetic fiber filaments in the existing spun-bonded spunlace material are of circular structures, and the side surfaces of the filaments are smooth, so that the fibers are not only not favorably entangled, but also the water absorption and water guide performance of the spunlace material is not favorably improved. Therefore, on the basis of carrying out a large number of experimental researches, the research and development team of the invention adopts two structural modes of the C-shaped section and the hollow section with micropores on the surface, thereby solving the problems in the prior art.

When the C-shaped cross section structure is adopted, the method is equivalent to axially slotting on the outer surface of the round filament, and the surface area of the fibers is increased, so that the probability of mutual hydroentanglement among the fibers can be improved, and the stability of the material structure is facilitated; in addition, the filament surface of the C-shaped section structure is concave, which is beneficial to material water storage and rapid water guide and provides space for the entry of ultra-short fibers. When the surface micropore structure of the filament hollow belt is adopted, the surface micropores are communicated with the hollow part, so that the material is favorable for absorbing water and the diffusion of water.

The research and development team believes that the above two structures are particularly suitable for medical and sanitary materials and various cleaning materials. In actual application, the selection can be carried out according to different requirements of various products.

Preferably, the bicomponent filaments have two side-by-side schemes:

the first scheme is as follows: the bicomponent filament is of a parallel structure with a special-shaped section, namely the section of the filament is a non-circular special-shaped section, the two components are arranged in parallel, and the melting points are different.

At present, most of the existing bi-component fibers are in a skin-core structure with a circular cross section, the melting point of a skin component is lower than that of a core component, and the structure has the advantages of large skin contact area and high bonding fastness, but has the defects of stiff hand feeling of materials, smooth and straight cloth cover and unsuitability for medical and sanitary materials with soft hand feeling. Therefore, after long-term experimental research, the research and development team thinks that the problem of the prior art can be solved by adopting the filament with the special-shaped parallel structure.

Compared with the filament fiber with the circular cross section, the filament fiber with the special-shaped cross section has larger surface area, and the interval between the fibers is increased, thereby being beneficial to fiber entanglement in the spunlace process, providing space for the accommodation of the ultrashort fibers and improving the water storage performance of the material. Two components with different melting points are arranged in parallel, when the material is subjected to high-temperature heat treatment (generally at the temperature of more than 110 ℃), the low-melting-point component is melted, and the ultra-short fibers can be bonded and fixed on the surface of the low-melting-point component, so that the bonding and reinforcing effects among the fibers are achieved, and the chip falling performance of the material is improved (the ultra-short fibers are easy to fall off from an aggregate). Meanwhile, along with the melting of the low-melting-point component, single-side thermal shrinkage occurs on a single filament, so that the original straight filament is bent and deformed, the bulkiness of the material is improved, and the hand feeling of the material is improved.

Scheme II: the double-component filament is a hollow section radial structure, namely the filament is a hollow section, and the two components are arranged and distributed in a radial shape at the center.

Preferably, the surface of the hollow-section radial structure in the two components is provided with micropores; further, the micropores are communicated with the hollow.

The invention melts two different polymers, respectively filters and measures the polymers, and extrudes the polymers from a spinneret orifice to form a bicomponent fiber, and the cross section of the bicomponent fiber is in a hollow radiation type (realized by the shape design of the spinneret orifice). The fibers of the two components are arranged alternately. By adopting the section structure, when the synthetic fiber filament is impacted by high-pressure water flow, the filament fibers made of two different materials are stressed and split and stripped mutually, so that the original filament is split into a plurality of filaments (such as 16 or 32 filaments), and the original filament fiber net is separated into the superfine filament fiber net. The density of the ultra-fine filament fiber net after splitting and stripping is greatly improved, so that the ultra-short fibers are favorably intertwined with the ultra-fine filament fiber net, and the problem that the ultra-short fibers run off from the filament fiber net is solved. In addition, the radiation type bi-component fiber adopts the hollow type and surface micropore design, which is beneficial to improving the fiber opening rate of the superfine fiber in the subsequent spunlace processing, and can better improve the water absorption of the material and improve the hand feeling of the material.

Preferably, the melting point of the component with the lower melting point in the special-shaped cross section parallel structure is 110-130 ℃.

Preferably, the synthetic fiber filaments are crimped filaments.

The ultrashort fiber has short length, and the common synthetic fiber filament has smooth surface, straight appearance and lack of elasticity, and is easy to separate from each other. Therefore, the ultrashort fibers and the common synthetic fiber filaments are not easy to tangle and fall off, and a large amount of ultrashort fibers are lost. The present invention adopts the mode of deforming common synthetic fiber to endow the synthetic fiber filament with a curling shape. The synthetic fiber filament with the crimp shape enlarges the space occupied by the fiber in the transverse direction, increases the bulkiness of the synthetic fiber filament assembly, enables the fiber to shrink in the longitudinal direction and have certain elastic elongation, and increases the longitudinal deformability of the material. The arrangement can increase the probability of mutual entanglement of the synthetic fiber filament and the ultrashort fiber, thereby improving the fiber entanglement cohesive force. Meanwhile, the thickness of the material is increased, the accommodating space of the material for liquid and solid is enlarged, the moisture absorption of the material is improved, the hand feeling of the material is improved, the material is soft and fluffy, the use requirement of the disposable sanitary material is met, and multiple purposes are achieved.

Preferably, the hydrophilic ultrashort fibers include one or more of plant pulp and cellulose fibers.

The plant pulp and the cellulose fiber both have good hygroscopicity, meet the design requirements of the product, and can achieve the beneficial effects of the invention.

Preferably, the plant pulp is wood pulp;

preferably, the plant pulp is bamboo pulp;

preferably, the plant pulp is cotton pulp;

preferably, the plant pulp is hemp pulp.

Preferably, the length of the hydrophilic ultrashort fiber is 2 to 18 mm.

The length of the ultra-short fiber has great influence on the material performance, and if the length of the ultra-short fiber is too short, the fiber is easy to run off in the processing process, and the wet-process fiber net is not easy to transfer; the ultra-short fiber is too long, so that the ultra-short fiber is not easy to disperse in water, and is easy to generate flocculation in slurry, thereby affecting the product quality and the production efficiency. The research and development team of the invention determines the length of the ultrashort fiber to be a better range through repeated tests.

Preferably, the official moisture regain of the hydrophilic ultrashort fibers is more than or equal to 7 percent.

Preferably, the cellulose fibers comprise one or more combinations of natural cellulose fibers and man-made cellulose fibers.

In a second aspect, the present invention provides a method for preparing a filament nonwoven composite material, comprising the steps of:

(1) preparation of filament web: firstly, melting polymer slices, spinning the obtained polymer melt by a spinning device after filtering and metering, cooling and drafting the polymer melt in sequence after spinning, and then deforming the obtained filament fibers by a deforming device to enable the straight filament fibers to be in a curling state; and then lapping is carried out to prepare a filament fiber net.

(2) Preparation of ultra-short fiber web: dispersing the ultra-short fibers in water for pulping, and removing impurities and fiber clusters in the pulp; and diluting the slurry, carrying out wet forming by a forming machine, and dehydrating to form the ultra-short fiber web.

(3) And (3) superposing and reinforcing the fiber web: firstly, carrying out pre-spunlace on a filament fiber net; then stacking the ultra-short fiber web onto the filament fiber web; and carrying out spunlace impact on the front surface and the back surface of the obtained superposed fiber web so as to mutually entangle and reinforce the ultra-short fibers and the filament fibers.

(4) And removing redundant water in the laminated fiber web, and finally drying to obtain the filament non-woven composite material.

Preferably, in step (1): the deformation device is a mechanical deformation device.

Preferably, in step (1), the polymer is melted using an extruder, preferably a screw extruder; further preferred is a twin-screw extruder.

Preferably, in step (1), a quenching chamber is used as the cooling chamber, and cooling air is introduced from both sides simultaneously.

Preferably, in step (1), the draft is performed using a draft duct for high-speed air flow.

Preferably, in the step (2), one or more disc mills are used for processing during the dispersion of the ultra-short fibers.

The plant pulp can have more excellent dispersibility and better forming uniformity through one or more disc grinding processes.

Preferably, a slit filter device is used to remove impurities and fiber clusters.

Preferably, the concentration of the slurry before dilution is 1-3 wt%, and the concentration of the slurry after dilution is 0.2-0.4 wt%.

The concentration of the diluted slurry determines the amount of the slurry to be applied, and the molding quality and the sufficient dispersion of the ultra-short fibers should be ensured. After repeated tests, the research and development team of the invention determines that 0.2-0.4 per mill is the better range of the diluted slurry concentration, and can meet the requirement of the inclined wire former on the net.

Preferably, the former is a wire former.

The wet former is an inclined net former; the reason is as follows: the inclined net former can ensure that the ultrashort fibers have enough space to keep a suspension state, prevent flocculation and keep the bulk of the ultrashort fiber net; the hydrodynamic force generated by the speed difference of the pulp screen can be used for regulating the arrangement direction of the ultrashort fibers and regulating the strength ratio of the ultrashort fibers in the longitudinal direction and the transverse direction (MD/CD) so as to realize the uniformity of the longitudinal strength and the transverse strength.

Preferably, in the step (3), the filament fiber web is pre-wetted and then pre-spunlaced; the pre-spunlace pressure is 30-60 bar.

The filament fiber net is pre-wetted, so that the fiber net can be compacted, air in the filament fiber net is removed, and fiber opening and entanglement efficiency in pre-spunlace is improved.

In addition, the pre-hydroentangling pressure has a significant effect on the opening of bicomponent ultra-fine synthetic fibers in a filament web and the entanglement efficiency of the fibers. If the spunlace pressure is too low, the opening rate or the entanglement efficiency of the bicomponent superfine fiber is low, so that the porosity in the filament fiber web is high, and the subsequent ultra-short fiber is easy to run off after being laminated. If the pre-hydroentangling pressure is too high, the fiber opening is excessive or the material is stiff, which is also not beneficial to the superposition and reinforcement of the subsequent ultra-short fibers. The research and development team of the invention determines the pre-spunlace pressure to be in a better range through repeated tests.

Preferably, in the step (3), one side of the laminated fiber web is subjected to spunlace by adopting a flat screen spunlace, and then the other side of the laminated fiber web is subjected to spunlace by adopting a round drum spunlace; the water jet pressure is 50-120 bar.

By adopting the arrangement, the net forming curtain and the spunlace supporting curtain can be superposed and used functionally, so that the space is effectively utilized, the stroke of the superposed fiber net is shortened, and the actual production operation is convenient; the round drum spunlace can improve the fiber entanglement efficiency and is suitable for the high-speed production requirement.

Preferably, in step (4), excess moisture is removed from the laminated web by vacuum suction.

The material can be prevented from being extruded and deformed by adopting a vacuum suction dehydration mode, the thickness of the material is improved to the maximum extent, the material is ensured to have a plump hand feeling, and the hand feeling of the material is softer and more fluffy.

Preferably, in the step (4), the drying is performed by a hot air penetration method.

The hot air penetrating type drying method is high in drying efficiency, the product is soft and full, the appearance structure of the product can be kept to the maximum extent, the thickness of the material is increased, the hand feeling of the material is improved, and the material is softer and more comfortable.

In a third aspect, the present invention provides a filament nonwoven composite production apparatus comprising: the device comprises a spinning and web-forming unit, a wet-forming unit, a superposition conveying unit, a spunlace composite unit and a drying unit.

Preferably, the spunlaid unit sequentially comprises a slicing bin, an extruder, a melt metering pump, a spinning device, a cooling device, a drafting device, a deforming device and a lapping device according to the process.

Preferably, the overlapping conveying unit comprises a net supporting curtain, a pre-wetting device and a pre-spunlace device; the net supporting curtains are connected end to form a loop capable of circularly rotating; the output end of the lapping device is connected with the input end of the net supporting curtain; a pre-wetting device and a pre-spunlace device are sequentially arranged on one side of the net supporting curtain according to the advancing direction of the net supporting curtain, and a vacuum suction device A and a vacuum suction device B are respectively arranged on the opposite sides of the pre-wetting device and the pre-spunlace device.

Preferably, the wet-laid unit comprises a slurry preparation system, an inclined wire former, a forming wire and a dewatering device; the forming nets are connected end to form a loop capable of circularly rotating, and the inclined net former and the dewatering device are sequentially arranged along the rotating direction of the forming nets; the input end of the inclined net former is connected with the output end of the slurry preparation system; the output section of the forming net is connected with a station on the net supporting curtain behind the pre-spunlace device.

Preferably, the slurry preparation system comprises a dispersing device, a metering pump, a liquid storage device, a fan pump and a slurry distributor which are sequentially connected; and stirrers are arranged in the dispersing device and the liquid storage device.

Preferably, the spunlace unit comprises a plurality of flat-screen spunlace heads, a round drum spunlace device and a vacuum suction device C which are arranged in front of and behind the process; the flat net spunlace head and the round drum spunlace device are used for respectively spunlacing different surfaces of the laminated fiber net; the flat net water stabs are arranged above the net supporting curtain and positioned on the inner side of the forming net; a vacuum suction device C is arranged below the net supporting curtain corresponding to each flat net water stabs; the drum spunlace device is positioned behind the output end of the net supporting curtain;

preferably, the drying unit is positioned after the circular drum spunlace device, and a vacuum suction device D is arranged in the drying unit.

Preferably, the circular drum spunlace device comprises a circular drum and a plurality of circular drum spunlace heads facing the circumferential surface of the circular drum.

Compared with the prior art, the invention has the beneficial effects that:

(1) the synthetic fiber filament fiber net and the hydrophilic ultra-short fiber net are superposed and spunlaced for reinforcement, and the manufactured filament non-woven composite material has high breaking strength and good hygroscopicity, and can meet the use requirements in the fields of disposable sanitary materials, industrial cleaning materials and the like.

(2) According to the invention, the structure with micropores on the surface of the C-shaped section or the hollow section is adopted, so that the entanglement efficiency among fibers is enhanced; the water absorption and water diversion performance of the single-component filament non-woven composite material is improved.

(3) According to the invention, the ultrashort fibers are bonded and fixed on the surface of the synthetic fiber filament by adopting the mode of the composite fiber with the special-shaped cross section parallel bi-component structure, so that the bonding and reinforcing effects among the fibers are achieved, the chip falling performance of the material is improved, and the hand feeling of the material is also improved.

(4) The invention adopts hollow radial bi-component and the surface is provided with a micropore structure, so that the original filament fiber net is separated into the superfine fiber net through pre-spunlace, the density of the filament fiber net is improved, the entanglement effect of the ultrashort fiber is improved, the problem that the ultrashort fiber runs off in the spunlace processing is solved, the water absorption of the material is further improved, and the hand feeling of the material is improved.

(5) The invention adopts the filament deforming device in the preparation process of the filament fiber net to change the straight filaments into the curling state, thereby not only increasing the probability of mutual entanglement of the synthetic fiber filaments and the ultrashort fibers and improving the fiber entanglement cohesive force, but also increasing the material thickness, increasing the accommodating space of the material for liquid and solid, improving the moisture absorption of the material and improving the material hand feeling.

(6) The production device of the filament non-woven composite material is reasonable in design and convenient to operate, solves the problem that no special equipment for the filament non-woven composite material exists in the technical field, and provides a new equipment solution for developing new filament spunlace products.

Drawings

FIG. 1 is a schematic view of a filament nonwoven composite of the present invention;

FIG. 2 is a schematic view showing the connection of a filament nonwoven composite production apparatus of the present invention;

FIG. 3 is a schematic structural view of a C-section monocomponent filament according to the present invention;

FIG. 4 is a schematic view showing a structure of a monocomponent filament having a hollow cross-sectional surface with micro-pores according to the present invention;

FIG. 5 is a schematic structural view of a side-by-side bicomponent filament with a profiled cross section according to the present invention;

FIG. 6 is a schematic view of a hollow-section radial bicomponent filament according to the present invention.

The reference signs are: the production process comprises the following steps of (1) filament fiber 1, ultra-short fiber 2, filament non-woven composite material 3, a slicing bin 101, an extruder 102, a melt metering pump 103, a spinning device 104, a cooling device 105, a drafting device 106, a texturing device 107, a lapping device 108, an inclined wire former 201, a forming wire 202, a dewatering device 203, a dispersing device 204, a liquid storage device 205, a fan pump 206, a pulp distributor 207, a metering pump 208, a supporting wire curtain 301, a pre-wetting device 302, a pre-hydro-entangling device 303, a vacuum suction device A304, a vacuum suction device B305, a flat wire hydro-entangling head 401, a round drum hydro-entangling device 402, a vacuum suction device C403 and a vacuum suction device D404.

Detailed Description

The present invention will be further described with reference to the following examples.

General examples

A filament nonwoven composite material 3, as shown in FIG. 1, comprises an aggregate made of filament fibers 1 and ultra-short fibers 2 as raw materials. The filament fibers are synthetic fiber filaments; the ultrashort fibers are hydrophilic ultrashort fibers; the hydrophilic ultrashort fibers are distributed in the synthetic fiber filament, and the hydrophilic ultrashort fibers and the synthetic fiber filament are mutually entangled and/or the hydrophilic ultrashort fibers are adhered and fixed on the synthetic fiber filament.

Optionally, the synthetic fiber filaments are monocomponent filaments or bicomponent filaments. The single-component filament is of a C-shaped section or hollow section surface with a micropore structure; when the structure with the hollow surface provided with the micropores is adopted, the micropores on the surface of the filament are communicated with the hollow.

Optionally, the bicomponent synthetic fiber filament is of a parallel structure with a special-shaped cross section, that is, the cross section of the filament is a non-circular special-shaped cross section, the two components are arranged in parallel and have different high and low melting points, wherein the melting point of the low melting point component is 110-130 ℃. Or the synthetic fiber filament is of a hollow section radial structure, namely the filament is of a hollow section, and the two components are radially arranged at intervals in the center; micropores are formed on the surfaces of the filaments; the micropores are communicated with the hollow cavity.

Optionally, the synthetic fiber filaments are crimped filaments.

The hydrophilic ultrashort fibers comprise one or more of plant pulp and cellulose fibers; the length is 2-18 mm; the official moisture regain is more than or equal to 7 percent.

A method of making a filament nonwoven composite comprising the steps of:

(1) preparation of filament web: firstly, melting polymer slices, spinning the obtained polymer melt by a spinning device after filtering and metering, cooling and drafting the polymer melt in sequence after spinning, and deforming the obtained filament fibers by a deforming device (preferably a mechanical deforming device) to enable the straight filament fibers to be in a curling state; and then lapping is carried out to prepare a filament fiber net.

(2) Preparation of ultra-short fiber web: dispersing the ultra-short fibers in water for pulping, and processing by adopting one or more disc mills in the process of dispersing the ultra-short fibers; removing impurities and fiber clusters by using a slit filtering device; diluting the slurry, and then carrying out wet forming by a forming machine (preferably an inclined wire former), wherein the concentrations of the slurry before and after dilution are respectively 1-3 wt% and 0.2-0.4 wt%; after dewatering an ultra short web is formed.

(3) And (3) superposing and reinforcing the fiber web: prewetting the filament fiber web, and then carrying out pre-spunlace (30-60 bar) on the filament fiber web; then stacking the ultra-short fiber web onto the filament fiber web; carrying out spunlace impact on the front surface and the back surface of the superposed fiber web, specifically carrying out spunlace on one surface of the superposed fiber web by adopting flat-screen spunlace, and then carrying out spunlace on the other surface of the superposed fiber web by adopting round drum spunlace; and the spunlace pressure is 50-120 bar, so that the ultra-short fibers and the filament fibers are mutually entangled and reinforced.

(4) And removing redundant moisture in the superposed fiber web by adopting a vacuum suction mode, and finally drying by adopting a hot air penetration mode to prepare the filament non-woven composite material.

A filament nonwoven composite production apparatus, as shown in fig. 2, comprising: the device comprises a spinning and web-forming unit, a wet-forming unit, a superposition conveying unit, a spunlace composite unit and a drying unit.

The spunlaid unit sequentially comprises a slicing bin 101, an extruder 102, a melt metering pump 103, a spinning device 104, a cooling device 105, a drafting device 106, a deforming device 107 and a lapping device 108 according to the working procedures.

The overlapping conveying unit comprises a net supporting curtain 301, a pre-wetting device 302 and a pre-spunlace device 303; the net supporting curtains are connected end to form a loop capable of circularly rotating; the output end of the lapping device is connected with the input end of the net supporting curtain; a prewetting device and a prehydro-entangled device are sequentially arranged on one side of the net supporting curtain according to the advancing direction of the net supporting curtain, and a vacuum suction device A304 and a vacuum suction device B305 are respectively arranged on the opposite sides of the prewetting device and the prehydro-entangled device.

The wet-laid unit comprises a slurry preparation system, an inclined wire former 201, a forming wire 202 and a dewatering device 203. The slurry preparation system comprises a dispersing device 204, a metering pump 208, a liquid storage device 205, a fan pump 206 and a slurry distributor 207 which are connected in sequence; and stirrers are arranged in the dispersing device and the liquid storage device. The forming nets are connected end to form a loop capable of circularly rotating, and the inclined net former and the dewatering device are sequentially arranged along the rotating direction of the forming nets; the input end of the inclined net former is connected with the output end of the slurry preparation system; the output section of the forming net is connected with a station on the net supporting curtain behind the pre-spunlace device, and the superposed fiber net is positioned between the forming net and the net supporting curtain.

The spunlace unit comprises a plurality of flat-screen spunlace heads 401, a round drum spunlace device 402 and a vacuum suction device C403 which are arranged in front of and behind the process; the flat net spunlace head and the round drum spunlace device are used for respectively spunlacing different surfaces of the laminated fiber net; the flat net water stabs are arranged above the net supporting curtain and positioned on the inner side of the forming net; a vacuum suction device C is arranged below the net supporting curtain corresponding to each flat net water stabs; the drum hydro-entangled device is behind the output end of the net supporting curtain. The circular drum spunlace device comprises a circular drum and a plurality of circular drum spunlace heads facing the circumferential surface of the circular drum.

The drying unit is positioned behind the circular drum spunlace device, and a vacuum suction device D404 is arranged in the drying unit.

Example 1

The superfine filament non-woven composite material has a unit area mass of 50g/m². As shown in fig. 1, comprising a polyester/polyamide bicomponent synthetic fiber filament and an ultra-short fiber aggregate. Wherein the mass proportion of the bicomponent synthetic fiber filament is 40 percent, and the proportion of the ultra-short fiber is 60 percent; as shown in fig. 6, the cross-sectional shape of the bicomponent synthetic fiber filament is a hollow radial type, and the surface of the filament is provided with micropores communicated with the hollow. The filament fineness is 3D; the two components of Polyester (PET) and Polyamide (PA) are arranged alternately and the number of the arranged components isThe amount was 16.

The Polyester (PET)/Polyamide (PA) bicomponent synthetic fiber filament is a crimped filament; the ultrashort fibers 2 are 50% wood pulp and 50% viscose ultrashort fibers; the viscose ultrashort fiber has the specification that: 1.2D 10 mm; the wood pulp and the viscose ultrashort fibers are distributed in the polyester/polyamide bi-component synthetic fiber filament; the ultra-short wood pulp and viscose fiber is intertwined with the polyester/polyamide bi-component synthetic fiber filament.

A method for preparing superfine filament non-woven composite material comprises the following steps:

(1) production of filament webs

Respectively feeding polyester and polyamide slices into a double-screw extruder, and enabling a polymer melt to pass through a melt filter and a melt metering pump, and then to enter a quenching chamber after being sprayed out by a spinneret plate on a spinning device; then the straight filaments are changed into a curled state through a high-speed air flow drafting air channel and a mechanical deformation device; then, the filament fiber net is laid on a net supporting curtain through a lapping device to form the filament fiber net with the fineness of 3D;

(2) preparation of ultra-short fiber webs

Respectively feeding wood pulp and viscose ultrashort fibers into a pulping device, dispersing the ultrashort fibers in water, and removing impurities and fiber clusters in the pulp by using a slit filtering device; processing by adopting two disc grinding processes in the wood pulp disintegrating and dispersing process; feeding the diluted slurry into an inclined wire former through a fan pump, and dehydrating on the inclined wire former to form an ultra-short fiber net;

(3) web lamination and reinforcement

Prewetting a polyester/polyamide filament fiber net on a net supporting curtain, and then impacting by adopting high-pressure water flow to carry out prespunlace (the prespunlace pressure is 60bar) on the filament fiber net so as to open the filament fiber net into 16 superfine fibers; then stacking the ultra-short fiber web onto the filament fiber web; sending the superposed fiber web into a spunlace system, firstly carrying out spunlace on the front surface of the superposed fiber web by adopting three flat-web spunlace heads (the spunlace pressure is 55bar, 60bar and 70bar in sequence), and then carrying out spunlace on the back surface of the superposed fiber web by adopting two round-drum spunlace heads (the spunlace pressure is 75bar and 100bar in sequence), so that the ultra-short fibers and the ultra-long fibers are mutually entangled and reinforced;

(4) removing excessive water in the laminated fiber web by vacuum suction device, drying the laminated fiber web by hot air penetration, and coiling to obtain a 50g/m laminated fiber web²Superfine filament non-woven composite material.

An ultrafine filament nonwoven composite material production apparatus, as shown in fig. 2, comprising: the device comprises a spinning and web-forming unit, a superposition conveying unit, a wet-forming unit, a spunlace composite unit and a drying unit.

Wherein:

the spunlaid unit comprises two slicing bins 101, an extruder 102, a melt metering pump 103, a spinning device 104, a cooling device 105, a drafting device 106, a deforming device 107 and a lapping device 108 which are connected in parallel in sequence.

The superposition conveying unit comprises a net supporting curtain 301, a pre-wetting device 302, a pre-spunlace device 303, a vacuum suction device and six guide rollers; the net supporting curtain 301 is arranged on the frame to form a loop capable of circularly rotating; a prewetting device 302 and a prespunlace device 303 are sequentially arranged on one side of the net supporting curtain 301 according to the advancing direction of the net supporting curtain, and a vacuum suction device A and a vacuum suction device B are correspondingly arranged on the other side of the forming net.

The wet-laid unit comprises a slurry preparation system, a frame, an inclined wire former 201, a forming wire 202 and a dewatering device 203; the inclined wire former and the dewatering device are sequentially arranged on the frame along the rotation direction of the forming wire; the input end of the inclined net former is connected with the output end of the slurry preparation system; the forming net is arranged behind the pre-spunlace device on the net supporting curtain and is positioned above the filament fiber net; the laminated fiber net is positioned between the forming net and the net supporting curtain.

The spunlace unit comprises 3 flat screen spunlace heads 401, a round drum spunlace device 402, a vacuum suction device and 2 cloth guide rollers which are arranged in front of and behind the process; the flat net spunlace head and the round drum spunlace device are used for respectively spunlacing different surfaces of the laminated fiber net; the flat net water stabs 401 are arranged above the net supporting curtain 301 and are positioned on the inner side of the forming net 202; and 3 vacuum suction devices C403 are arranged below the net supporting curtain corresponding to each flat net water stabs head 401.

The slurry preparation system comprises a dispersing device 204, a liquid storage device 205, a fan pump 206 and a slurry distributor 207; a metering pump 208 is arranged between the dispersing device 204 and the liquid storage device 205; stirrers are arranged in the dispersing device 204 and the liquid storage device 205; the drum hydroentangling mechanism 402 includes a drum and 2 drum hydroentangling heads facing the circumferential surface of the drum.

Example 2

A bicomponent filament non-woven composite material with the mass per unit area of 40g/m². As shown in fig. 1, comprising a continuous bicomponent synthetic fiber filament and an ultra-short fiber aggregate; wherein the mass proportion of the bicomponent synthetic fiber filament is 50 percent, and the proportion of the ultra-short fiber is 50 percent;

the bicomponent synthetic fiber filament is a crimped filament with a fineness of 1.2D, as shown in FIG. 5, the cross-sectional shape thereof is hexagonal, and the two components are Polyethylene (PE) and polypropylene (PP) components; the two components are arranged in parallel; wherein the Polyethylene (PE) component has a melting point of 120 ℃.

The ultra-short fiber 2 is Lyocell (Lyocell, tencel) ultra-short fiber; the specification of the Lyocell ultra-short fiber is 1.2D × 8 mm; the lyocell ultra-short fibers are distributed in the bicomponent synthetic fiber filaments; the lyocell ultra-short fibers are bonded and fixed on the bicomponent synthetic fiber filament.

A method for preparing a bicomponent filament nonwoven composite material comprises the following steps:

(1) production of filament webs

Firstly, feeding polypropylene (PP) and Polyethylene (PE) slices into a double-screw extruder, and enabling a polymer melt to pass through a melt filter and a melt metering pump, and then to enter a quenching chamber after being sprayed out by a spinneret plate on a spinning device; then the straight filaments are changed into a curled state through a high-speed air flow drafting air channel and a mechanical deformation device; then, the filament fiber net is laid on a net supporting curtain through a lapping device to prepare a bicomponent filament fiber net;

(2) preparation of ultra-short fiber webs

Sending the lyocell ultra-short fiber into a pulping device, dispersing the ultra-short fiber in water, and removing impurities and fiber clusters in the pulp by adopting a slit filtering device; feeding the diluted slurry into an inclined wire former through a fan pump, and dehydrating on the inclined wire former to form an ultra-short fiber net;

(3) web lamination and reinforcement

Pre-wetting a bicomponent filament fiber net on a net supporting curtain, and then impacting by adopting high-pressure water flow to pre-spunlace the filament fiber net (the pre-spunlace pressure is 40 bar); then stacking the ultra-short fiber web onto the filament fiber web; sending the superposed fiber web into a spunlace system, firstly carrying out spunlace on the front surface of the superposed fiber web by adopting three flat-web spunlace heads (the spunlace pressure is 55bar, 65bar and 75bar in sequence), and then carrying out spunlace on the back surface of the superposed fiber web by adopting two round-drum spunlace heads (the spunlace pressure is 70bar and 110bar in sequence), so that the lyocell ultra-short fibers and the bi-component filament fibers are mutually entangled and reinforced;

(4) removing excessive water in the laminated fiber web by using a vacuum suction device, passing the laminated fiber web through a hot air penetration drying device, melting the PE component in the laminated fiber web when the drying temperature reaches above 120 ℃, bonding the ultra-short tencel fibers on the PE component of the long-filament fibers, and rolling to obtain the ultra-short tencel fibers with the weight of 40g/m²A bicomponent filament nonwoven composite.

A bicomponent filament nonwoven composite manufacturing apparatus, as shown in fig. 2, comprising: the device comprises a spinning and web-forming unit, a superposition conveying unit, a wet-forming unit, a spunlace composite unit and a drying unit.

Wherein:

the spunlaid unit comprises two slicing bins 101, an extruder 102, a melt metering pump 103, a spinning device 104, a cooling device 105, a drafting device 106, a deforming device 107 and a lapping device 108 which are connected in parallel in sequence.

The superposition conveying unit comprises a net supporting curtain 301, a pre-wetting device 302, a pre-spunlace device 303, a vacuum suction device and six guide rollers; the net supporting curtain 301 is arranged on the frame to form a loop capable of circularly rotating; a prewetting device 302 and a prespunlace device 303 are sequentially arranged on one side of the net supporting curtain 301 according to the advancing direction of the net supporting curtain, and a plurality of vacuum suction devices A and a plurality of vacuum suction devices B are correspondingly arranged on the other side of the forming net.

The wet-laid unit comprises a slurry preparation system, a frame, an inclined wire former 201, a forming wire 202 and a dewatering device 203; the inclined wire former and the dewatering device are sequentially arranged on the frame along the rotation direction of the forming wire; the input end of the inclined net former is connected with the output end of the slurry preparation system; the forming net is arranged behind the pre-spunlace device on the net supporting curtain and is positioned above the filament fiber net; the laminated fiber net is positioned between the forming net and the net supporting curtain.

The spunlace unit comprises 3 flat-screen spunlace heads 401, a round drum spunlace device 402, a vacuum suction device and two cloth guide rollers which are arranged in front of and behind the process; the flat net spunlace head and the round drum spunlace device are used for respectively spunlacing different surfaces of the laminated fiber net; the flat net water stabs 401 are arranged above the net supporting curtain 301 and are positioned on the inner side of the forming net 202; and 3 vacuum suction devices C403 are arranged below the net supporting curtain corresponding to each flat net water stabs head 401.

The slurry preparation system comprises a dispersing device 204, a liquid storage device 205, a fan pump 206 and a slurry distributor 207; a metering pump 208 is arranged between the dispersing device 204 and the liquid storage device 205; stirrers are arranged in the dispersing device 204 and the liquid storage device 205; the drum hydroentangling mechanism 402 includes a drum and 2 drum hydroentangling heads facing the circumferential surface of the drum.

Example 3

The polypropylene filament non-woven composite material has a mass per unit area of 45g/m². As shown in fig. 1, comprising continuous polypropylene (PP) filaments and ultra-short fiber assemblies; wherein, the mass ratio of the polypropylene (PP) filament is 60 percent, and the ratio of the ultra-short fiber is 40 percent. As shown in fig. 4, the polypropylene (PP) filament has a hollow cross-section and a microporous structure on the surface thereof, and the micropores on the surface of the filament are communicated with the hollow space. The polypropylene filaments are crimped filaments, and the fineness of the crimped filaments is 1.5D; the ultrashort fibers are wood pulp fibers; the wood pulp fibers are distributed in the polypropylene filaments; the wood pulp fibers are intertwined with the polypropylene filaments.

A preparation method of a polypropylene filament non-woven composite material comprises the following steps:

(1) production of filament webs

Firstly, feeding polypropylene slices into a screw extruder, and spraying a polymer melt through a melt filter and a melt metering pump and a spinneret plate on a spinning device into a quench chamber; then the straight filaments are changed into a curled state through a high-speed air flow drafting air channel and a mechanical deformation device; then, the polypropylene filament fibers are laid on a net supporting curtain through a lapping device to prepare a polypropylene filament fiber net;

(2) preparation of ultra-short fiber webs

Sending the wood pulp into a pulping device, so that the wood pulp fiber is broken and dispersed in water; processing by adopting three disc grinding processes; feeding the diluted pulp into an inclined wire former through a fan pump, and dehydrating on the inclined wire former to form a wood pulp fiber net;

(3) web lamination and reinforcement

Pre-wetting a polypropylene filament fiber net on a net supporting curtain, and then impacting by adopting high-pressure water flow to pre-spunlace the polypropylene filament fiber net (the pre-spunlace pressure is 30 bar); then stacking the ultra-short fiber web onto the filament fiber web; sending the superposed fiber web into a spunlace system, firstly carrying out spunlace on one surface of the superposed fiber web by adopting flat-web spunlace, and then carrying out spunlace on the other surface of the superposed fiber web by adopting round-drum spunlace, wherein the spunlace pressure is 50-120 bar, so that the ultra-short fibers and the long fibers are mutually entangled and reinforced;

(4) removing excessive water in the laminated fiber web by using a vacuum suction device, and drying and coiling the laminated fiber web by hot air penetration to prepare the laminated fiber web with the density of 45g/m²A polypropylene filament nonwoven composite.

A polypropylene filament nonwoven composite production apparatus, as shown in fig. 2, comprising: the device comprises a spinning and web-forming unit, a superposition conveying unit, a wet-forming unit, a spunlace composite unit and a drying unit.

Wherein:

the spunlaid unit comprises two slicing bins 101, an extruder 102, a melt metering pump 103, a spinning device 104, a cooling device 105, a drafting device 106, a deforming device 107 and a lapping device 108 which are connected in parallel in sequence.

The superposition conveying unit comprises a net supporting curtain 301, a pre-wetting device 302, a pre-spunlace device 303, a vacuum suction device and 6 guide rollers; the net supporting curtain 301 is arranged on the frame to form a loop capable of circularly rotating; a prewetting device 302 and a prespunlace device 303 are sequentially arranged on one side of the net supporting curtain 301 according to the advancing direction of the net supporting curtain, and a plurality of vacuum suction devices A and a plurality of vacuum suction devices B are correspondingly arranged on the other side of the forming net.

The wet-laid unit comprises a slurry preparation system, a frame, an inclined wire former 201, a forming wire 202 and a dewatering device 203; the inclined wire former and the dewatering device are sequentially arranged on the frame along the rotation direction of the forming wire; the input end of the inclined net former is connected with the output end of the slurry preparation system; the forming net is arranged behind the pre-spunlace device on the net supporting curtain and is positioned above the filament fiber net; the superposed fiber web is positioned between the forming net and the net supporting curtain;

the spunlace unit comprises 3 flat-screen spunlace heads 401, a round drum spunlace device 402, a vacuum suction device and 2 cloth guide rollers which are arranged in front of and behind the process; the flat net spunlace head and the round drum spunlace device are used for respectively spunlacing different surfaces of the laminated fiber net; the flat net water stabs 401 are arranged above the net supporting curtain 301 and are positioned on the inner side of the forming net 202; and 3 vacuum suction devices C403 are arranged below the net supporting curtain corresponding to each flat net water stabs head 401.

The slurry preparation system comprises a dispersing device 204, a liquid storage device 205, a fan pump 206 and a slurry distributor 207; a metering pump 208 is arranged between the dispersing device 204 and the liquid storage device 205; stirrers are arranged in the dispersing device 204 and the liquid storage device 205; the drum hydroentangling mechanism 402 includes a drum and 2 drum hydroentangling heads facing the circumferential surface of the drum.

Example 4

The difference between this example and example 3 is:

polylactic acid filament non-woven composite material with unit area mass of 60g/m². As shown in figure 1Shown, comprising continuous polylactic acid (PLA) filaments and ultrashort fiber aggregates; wherein the mass ratio of the polylactic acid (PLA) filament is 55 percent, and the mass ratio of the ultrashort fiber is 45 percent.

The polylactic acid filament is a crimped filament, as shown in fig. 3, the cross section of the filament fiber is C-shaped, and the fineness of the filament fiber is 1.2D; the ultrashort fibers are wood pulp fibers; the wood pulp fibers are distributed in the polylactic acid filaments; the wood pulp fibers are intertwined with the polylactic acid filaments.

Example 5

The difference between this example and example 3 is:

the polyamide filament non-woven composite material has a mass per unit area of 70g/m². As shown in fig. 1, comprising continuous Polyamide (PA) filaments and ultra-short fiber assemblies; wherein, the mass proportion of the Polyamide (PA) filament is 50 percent, and the proportion of the ultra-short fiber is 50 percent.

The polyamide filament is a crimped filament, as shown in figure 4, the cross section of the filament is hollow, and micropores communicated with the hollow are distributed on the surface of the filament; the fineness was 1.1D. The ultra-short fiber is bamboo pulp fiber with the specification of 1.2D 12 mm. The bamboo pulp fibers are distributed in the polyamide filaments; the bamboo pulp fibers and the polyamide filaments are intertwined with each other.

Example 6

The difference between this example and example 2 is:

a polyester filament non-woven composite material with the mass per unit area of 45g/m². As shown in fig. 1, comprising a continuous bicomponent Polyester (PET) filament and an ultra-short fiber aggregate; wherein, the mass ratio of the bicomponent Polyester (PET) filament is 60 percent, and the ratio of the ultra-short fiber is 40 percent.

The bicomponent Polyester (PET) filaments are crimped filaments, the fineness of which is 1.5D, as shown in fig. 5, the cross-sectional shape is hexagonal, the two components are a low-melting-point polyester component and a conventional polyester component, and the two components are arranged in parallel; wherein the melting point of the low-melting polyester component is 115 ℃.

The ultrashort fiber 2 is viscose ultrashort fiber; the specification of the viscose ultrashort fibers is 1.2D × 10 mm; the viscose ultra-short fibers are distributed in the polyester filament; the viscose ultrashort fibers 2 are bonded and fixed on the polyester filament.

Example 7

The difference between this example and example 3 is:

the modified polyvinyl alcohol filament non-woven composite material has a mass per unit area of 50g/m². As shown in fig. 1, comprising continuous modified polyvinyl alcohol (PVA) filaments and ultra-short fiber aggregates; wherein, the mass ratio of the polyvinyl alcohol (PVA) filament is 40 percent, and the ratio of the ultra-short fiber is 60 percent. The modified polyvinyl alcohol (PVA) filaments are protein modified polyvinyl alcohol, wherein the content of the PVA is 70%, and the content of the soybean protein is 30%.

The modified polyvinyl alcohol filament is a crimped filament, as shown in figure 3, the cross section of the filament fiber is C-shaped, and the fineness of the filament fiber is 1.5D; the ultra-short fiber is Lyocell (Lyocell, tencel) ultra-short fiber with the specification of 1.2D × 8 mm; the lyocell ultra-short fibers are distributed in modified polyvinyl alcohol (PVA) filaments; the lyocell ultra-short fibers and the modified polyvinyl alcohol filaments are intertwined with each other.

Comparative example 1

Short fiber spunlace nonwoven material with unit area mass of 50g/m². Consists of 60 percent of viscose fiber and 40 percent of polyester fiber. Wherein, the viscose fiber's specification is: 1.67dtex 38mm, the specification of the polyester fiber is 1.56dtex 38. The viscose and polyester fibers are intertwined with each other.

A method for preparing short fiber spunlace nonwoven material comprises the following steps: respectively opening and mixing viscose fibers and polyester fibers according to a proportion, and then sending the mixed fibers into a carding machine to prepare a thin fiber web; then the thin fiber net is made into a thick fiber net through a cross lapping machine and a drafting machine; then the thick fiber web is sent into a spunlace system, and the front and back surfaces of the fiber web are spunlaced by high-pressure water flow, so that the short fibers are mutually entangled and reinforced; drying and coiling to obtain the product with a density of 50g/m²Staple fiber spunlace nonwoven materials.

Comparative example 2

The wood pulp composite spunlaced nonwoven material has the mass per unit area of 56g/m². Is prepared from 53.5% wood pulp fibres and 46.5% polyesterAnd (3) fiber composition. Wherein the wood pulp is softwood pulp; the viscose specification was 1.67dtex 38 mm. The wood pulp fibers and the polyester fibers are mutually entangled; the wood pulp fibers are distributed on one surface of the material; the polyester fiber is distributed on the other side of the material more.

A preparation method of a wood pulp composite spunlace nonwoven material comprises the following steps: opening and mixing the polyester fibers according to a proportion, and then sending the mixed polyester fibers into a carding machine to prepare a polyester fiber net; superposing wood pulp paper made of wood pulp on a polyester fiber net, then sending the polyester fiber net into a spunlace machine, and adopting high-pressure water flow to respectively adopt a plurality of spunlaces on the front surface and the back surface of the superposed fiber net so as to mutually entangle and reinforce the wood pulp fiber and the polyester fiber; drying and coiling to prepare 56g/m²Wood pulp composite spunlaced nonwoven materials.

Comparative example 3

The polypropylene (PP) wood pulp spunlace composite material has the mass per unit area of 68g/m². Consists of 56% wood pulp fiber and 44% polypropylene (PP) filament. Wherein the wood pulp fiber is needle-leaved wood pulp. The wood pulp fibers and polypropylene (PP) filaments are intertwined; the wood pulp fibers are distributed on one surface of the material; the polyester fiber is distributed on the other side of the material more.

A preparation method of a polypropylene (PP) wood pulp spunlace composite material comprises the following steps: the method comprises the following steps: (1) unwinding a polypropylene (PP) non-woven fabric to obtain a bottom layer base fabric; (2) pulping wood pulp, disc-grinding, removing impurities to obtain pulp, and making into wet-process fiber web by a wet-process former; (3) superposing the wet-process fiber net on the bottom layer base cloth, and combining the wood pulp fiber with the polypropylene fiber (PP) non-woven fabric through spunlace reinforcement; then drying and coiling the mixture to prepare the 45g/m²Polypropylene (PP) wood pulp composites.

Comparative example 4

Spun-bonded spunlaced nonwoven material with the mass per unit area of 60g/m². A fiber assembly of 100% polypropylene (PP) filaments; the polypropylene filaments are intertwined with each other.

A method of making a spunbond spunlaced nonwoven material comprising the steps of: (1) feeding polypropylene (PP) slices into a hopper, and extruding and melting the PP slices by a screw extruder to obtain a melt; (2) removing impurities from the melt through a filter, and then sending the melt into a spinning system; (3) quantitatively feeding the melt into a spinning assembly by a metering pump, spraying the melt out by a spinneret plate of a spinning machine, cooling and solidifying the melt into filaments, guiding the filament bundles into a drawing nozzle, drawing the filament bundles by air flow, and lapping on a lapping machine to obtain filament fiber webs respectively; (4) the filament fiber web is sent into a spunlace mechanism for reinforcement, and is dried and coiled to prepare the spun-bonded spunlace nonwoven material.

And (3) comparing and analyzing product performance indexes:

(1) and (3) testing items: each of the materials of example 1, example 2, comparative example 1, comparative example 2, comparative example 3 and comparative example 4 was tested for the mass per unit area, breaking strength, elongation at break, water absorption rate, liquid absorption amount, chip falling rate and softness index.

(2) The test method comprises the following steps: the test methods of unit area mass, breaking strength, breaking elongation, water absorption rate and liquid absorption amount are carried out according to the regulations in FZ/T64012-2013 sanitary water spunlace nonwoven fabric; the softness index was performed according to the GB/T8942-2016 paper softness determination Standard (slit width 20 cm).

The chip drop rate index test method comprises the following steps:

cut 3 pieces of sample with dimensions 9 x 9 in.

② the sample is put into a conical flask containing 600mL deionized water, the stopper is covered tightly, and the sample is shaken at 150rpm for 5 min. Diluting 3mL of the shaken solution to 200mL with distilled water, performing suction filtration by using a mesh filter membrane, and then washing the inner wall and the edge of the filter cup by using 100mL of deionized water.

And thirdly, taking down the filter membrane to naturally dry, or drying in a30 ℃ oven.

Observation and counting by a microscope: the dried filter membrane was placed on 2 slides and the filter membrane grid lines were adjusted to lie horizontally. The number of fibers recorded at a length of 100 μm or more was observed by using a manual counter.

And (3) calculating the chip dropping rate:

wherein: ft: the total fiber number; vb: volume of solution used to soak the sample; va: volume of solution tested; a: area of the sample. The result takes two significant digits.

Comparison list of performance indexes of various materials

And (4) conclusion:

(1) example 1 is "a 50 g/m" in accordance with the present invention²The superfine filament non-woven composite material is produced with hollow PET/PA double-component hollow radial filament with micropores and through water jetting compounding with 50% wood pulp and 50% super short viscose fiber.

Comparative example 1 is a 50g/m²The short fiber spunlace nonwoven material is made by carding, lapping and spunlacing viscose and polyester short fibers. Comparative example 2 is a 56g/m²The wood pulp composite spunlaced nonwoven material is formed by combing polyester fibers into a net and then spunlacing the net and wood pulp paper. Comparative example 3 is a 68g/m²The polypropylene fiber (PP) wood pulp spunlace composite material is prepared by wet-laying wood pulp and then carrying out spunlace composite reinforcement on the wood pulp and polypropylene fiber (PP) non-woven fabric.

By comparison, under the same gram weight (unit area mass), the breaking strength of the product of the example 1 is greatly improved compared with that of the product of the comparative example 1, wherein the breaking strength in the Machine Direction (MD) is improved by 93.8 percent, and the breaking strength in the transverse direction is improved by 71.8 percent; the chip dropping rate of the product of the example 1 is improved by 25 percent compared with that of the product of the comparative example 2; compared with the product of comparative example 3, the product is improved by 41 percent, and the technical effect of the invention is achieved.

(2) Example 2 is' a 40g/m²A dual-component non-woven filament material is prepared from dual-component crimped filament with hexagonal PE/PP parallel structure and ultra-short tencel fibres through spunlacing, compounding, reinforcing, baking to fuse PE layer, and adhering ultra-short tencel fibres to dual-component filament. By comparison, the chip removal rate of the product in the example 2 is increased by 47.9% compared with that of the product in the comparative example 2, and is increased by 59% compared with that of the product in the comparative example 3.

(3) By comparison, the softness of the product in example 1 is obviously improved compared with that in comparative example 3, wherein the longitudinal softness of the material is improved by 22.6%, and the transverse softness of the material is improved by 30.8%.

(4) Comparative example 4 is a 60g/m²The spun-bonded spunlaced nonwoven material is prepared by adopting 100 Percent Polypropylene (PP) slices, spinning to form a net and then spunlacing to reinforce. By comparison, the liquid absorption of the product of example 1 of the present invention was 1.95 times that of the product of comparative example 4; compared with the product of comparative example 1, the liquid absorption is improved by 5.8%; the liquid absorption is improved by 31.9 percent compared with the product of comparative example 3.

The raw materials and equipment used in the invention are common raw materials and equipment in the field if not specified; the methods used in the present invention are conventional in the art unless otherwise specified.

The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and all simple modifications, alterations and equivalents of the above embodiments according to the technical spirit of the present invention are still within the protection scope of the technical solution of the present invention.