CN106012296A - Composite non-woven filter material and preparation method thereof - Google Patents

Composite non-woven filter material and preparation method thereof Download PDF

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Publication number
CN106012296A
CN106012296A CN201610454570.7A CN201610454570A CN106012296A CN 106012296 A CN106012296 A CN 106012296A CN 201610454570 A CN201610454570 A CN 201610454570A CN 106012296 A CN106012296 A CN 106012296A
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Prior art keywords
polyester
polyamide
fiber
preparation
complex nonwoven
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CN106012296B (en
Inventor
王洪
孙尚泽
裘春湖
李越徽
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ZHEJIANG YANPAI FILTRATION TECHNOLOGY CO., LTD.
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ZHEJIANG YANPAI FILTRATION TECHNOLOGY Co Ltd
Donghua 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
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/42Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties characterised by the use of certain kinds of fibres insofar as this use has no preponderant influence on the consolidation of the fleece
    • D04H1/4382Stretched reticular film fibres; Composite fibres; Mixed fibres; Ultrafine fibres; Fibres for artificial leather
    • 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
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/44Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling
    • D04H1/46Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres
    • 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
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/44Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling
    • D04H1/46Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres
    • D04H1/492Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties the fleeces or layers being consolidated by mechanical means, e.g. by rolling by needling or like operations to cause entanglement of fibres by fluid jet
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/32Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond
    • D06M11/36Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond with oxides, hydroxides or mixed oxides; with salts derived from anions with an amphoteric element-oxygen bond
    • D06M11/38Oxides or hydroxides of elements of Groups 1 or 11 of the Periodic Table
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/21Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/244Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of halogenated hydrocarbons
    • D06M15/256Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of halogenated hydrocarbons containing fluorine
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/21Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/263Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of unsaturated carboxylic acids; Salts or esters thereof
    • D06M15/277Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of unsaturated carboxylic acids; Salts or esters thereof containing fluorine
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/37Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/643Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicon in the main chain
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/30Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/32Polyesters
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/30Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/34Polyamides
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2200/00Functionality of the treatment composition and/or properties imparted to the textile material
    • D06M2200/10Repellency against liquids
    • D06M2200/12Hydrophobic properties
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2331/00Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
    • D10B2331/02Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyamides
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2331/00Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
    • D10B2331/04Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyesters, e.g. polyethylene terephthalate [PET]

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nonwoven Fabrics (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Abstract

The invention discloses a composite non-woven filter material and a preparation method thereof. The composite non-woven filter material is characterized in that bent channel pore structures are formed on the fiber surfaces due to needle punching and spunlace reinforcement; each fiber simultaneously comprises two polymer ingredients, namely, polyester and polyamide, and the two polymer ingredients are distributed irregularly in an island manner in fibers. The preparation method comprises steps as follows: a polyester/polyamide blended filament fiber net is prepared with a spun-bonding forming process, reinforced through needle punching and then soaked in an acidic or alkaline solution, and parts of polyester or polyamide ingredients on the fiber surfaces are corroded, so that rough structures are formed on the fiber surfaces; spunlace reinforcement is further performed, treating solutions on the fiber surfaces are washed away, hydrophobic finishing is performed, and the composite non-woven filter material can be prepared. The prepared filter material has a good hydrophobic effect and is also endowed with higher mechanical performance and better size stability by the filament fibers.

Description

A kind of complex nonwoven filtering material and preparation method thereof
Technical field
The present invention relates to a kind of complex nonwoven filtering material and preparation method thereof, particularly fiber surface has one Determine hydrophobic polyester/polyamide blended spun-bonded continuous yarn acupuncture/spun lacing composite nonwoven material and the preparation side thereof of roughness Method.
Background technology
Along with pollutant emission index is improved constantly by country, to as sack cleaner main filtration function group The structure of the needled punched nonwoven material of part and performance propose the highest requirement.Sack cleaner is as efficiently The smoke gas treatment systems such as cleaner is widely used in power plant, metallurgy, waste incineration.Filtrate is to affect pocket type Cleaner unit service life and the most important factor of efficiency of dust collection, owing to the condition such as equipment, production technology limits, state Interior filtrate technology lags behind abroad for a long time.It addition, China's coal-burning boiler used equipment is more, coal variety is various, The factors such as the technological literacy of incomplete combustion and fireman cause fire coal boiler fume high temperature, high concentration and complexity Etc. special flue gas operating mode.Therefore, the Novel filter material seeking applicable China present situation is to solve current sack cleaner to answer By one of effective way of a difficult problem.It is known that filtration flue gas often contains substantial amounts of water vapour, in discharge During easily form dew condensation phenomenon on filter bag surface, thus have impact on the ash-removal effect of filter bag, reduce filter bag Filter efficiency and improve filtration resistance, have an effect on the service life of filter bag.It is thus desirable to improve the hydrophobic of filtrate Effect, alleviates dew condensation phenomenon.
The hydrophobicity of material surface depends primarily on two factors: one is the surface energy of material;Two is material surface Roughness.Many studies have shown that, having micro-nano coarse structure surface is the major reason forming hydrophobic effect. Material surface is carried out illumination, additive, electric treatment etc., improves the roughness of material surface, can be necessarily More preferable hydrophobicity is obtained in degree.
The patent of invention of Application No. CN201510299456, discloses a kind of nano-tube/line modified fibre The new method on surface, is successively heated to reflux fiber in organic solvent and deionized water, after then processing Fiber is placed in plasma generating device process, then the fiber after processing immerses further in organic solvent and locates Reason, can make the roughness of fiber surface dramatically increase, improve the hydrophobicity of fiber, improve fibre efficiently The resistant to hydrolysis ability of dimension.
Terylene (polyester) and nylon (polyamide) are conventional fibrous materials, are also important weaving filter materials Material fibrous raw material.Utilize polyester and the incompatibility of polyamide both polymer, be made into skin-core structure Bicomponent fibre, or Fructus Citri tangerinae lobe fiber type fibrillation become superfine fibre, is the most ripe industrial skill Art, but it is less to make the research application in terms of blended fiber after being blended by two kinds of polymer melts.
The patent of invention of Application No. 201410026134.0, disclose a kind of modified poly ester blended fiber and Preparation method, described blended fiber prepared with polyamide blended melt spinning by modified poly ester, and blended fiber is often For acid-dyeable dark color under normal temperature and pressure, overcome conventional modified polyester complex fiber dyeing uniformity difference Shortcoming.
It addition, polyester and polyamide show different stability in acid-base solution, alkaline solution can be used Polyester is carried out alkali decrement treatment, it would however also be possible to employ acid solution carries out surface etch to polyamide.Such as, Shen Please number be the patent of invention of 201210348404.0, disclose a kind of blended fiber and production method thereof, this be altogether After combined filament woven into fabric, under the conditions of aqueous slkali, carry out stripping property process the dissolution copolymerization getting rid of in fiber Ester, makes the Fypro in blended fiber form micro hole construction, gives the water-absorbing fast-drying performance that fabric is good.
In sum, on the basis of existing technology, in spunbond forming process, polyester and polyamide two kinds are gathered Polymer melt prepares polyester/polyamide blend filament after being blended, after preliminary acupuncture, and recycling polyester and polyamide Different stability in acid-base solution, partial etching falls the polyester of fiber surface or polyamide component and makes fibre Dimension table face is roughened, then is reinforced further by fibre web by spun lacing and washed away the acid-alkali treatment liquid of fiber surface, Prepare hydrophobic polyester/polyamide blended long filament filtrate, be used as Anti-dew flue filtering material, not disclosed report Road.
Summary of the invention
Hydrophobic polyester/polyamide that the technical problem to be solved is to provide a kind of fiber surface coarse is common Mixed long filament filtrate and preparation method thereof, to solve the deficiencies in the prior art.
For solving the problems referred to above, the invention provides a kind of complex nonwoven filtering material, particularly fiber surface There is the hydrophobic polyester/polyamide blended spun-bonded continuous yarn non-woven filter material of certain roughness, it is characterised in that Fiber surface is because reinforcing through acupuncture and spun lacing and have bending channel aperture structure;Every in non-woven filter material Root fiber includes the polyester in island shape random and two kinds of polymer component of polyamide simultaneously.
Preferably, its surface density is 150~250g/m2, Air permenbility is 25~40L/ (m2S), contact angle is 110 °~130 °, the average diameter of polyester/polyamide blend filament is 15~35 μm, fiber surface coarse Degree is 0.025~0.1 μm.
Preferably, described polyester and polyamide can be homopolymer, it is also possible to be copolymer.
Preferably, the differences in viscosity of described polyester and polyamide is not more than 300Pa s.
Preferably, in every fiber, the percentage by weight of polyester and polyamide is 1/99~99/1.
It is highly preferred that the percentage by weight of polyester and polyamide is 40/60~60/40 in every fiber.
Preferably, raw material, in addition to polyester and polyamide blended resin, also includes that epoxy resin, maleic anhydride connect At least one in branch polymer, polyester-polyamide copolymer is as compatilizer.
It is highly preferred that the percentage by weight that described compatilizer is in the fibre is 1.0~5.0wt%.
The present invention also provided for the preparation method of a kind of complex nonwoven filtering material, it is characterised in that concrete Step is as follows:
The first step: polyester and polyamide are dried;
Second step: the polyester of drying, polyamide and/or compatilizer are proportionally added into product line of spinning viscose Screw extruder in, carry out polyester/spunbond shaping of amide blend filament;
3rd step: above-mentioned spunbond forming polyester/polyamide blended filament web is transported to acupuncture unit and carries out 1 The main pinprick reinforcement of road pre-needling and 2 roads;
4th step: be sent to subtract by the above-mentioned polyester/polyamide blend filament non-woven material through pinprick reinforcement Carrying out decrement treatment in amount treatment trough, partial etching falls polyester or the polyamide component of fiber surface, makes fiber Rough surface;
5th step: the above-mentioned polyester/polyamide blend filament non-woven material through decrement treatment is sent to spun lacing Machine is reinforced, and washes away the treatment fluid of fiber surface simultaneously;
6th step: the polyester/polyamide blend filament non-woven material the 5th step prepared is sent in dehydrator and dried Dry, obtain the non-woven filtrate of polyester/polyamide blend filament that fiber surface is coarse.
Preferably, after in the described first step, polyester and polyamide section are dried, its water content is not more than 40ppm。
Preferably, described second step spunbond process is: each district temperature of extruder: a district 150~180 DEG C, two District 180~270 DEG C, three districts 270~330 DEG C, four districts 320~340 DEG C;Die head temperature 300~320 DEG C;Side-blown Air temperature is 10~25 DEG C;Drawing air speed is 500~900m/s.
Preferably, described 3rd step needling process is: bestock 2000-3000 piece of pre-needling machine/m, adopts With lower thorn formula pricker movement locus, punch frequency is 300-600 thorn/min;First and the main acupuncture of second divide Cai Yong not go up thorn formula and lower thorn formula acupuncture movement locus, needle plate bestock 4000-6000 piece/m, punch frequency For 800-1200 thorn/min.
Preferably, the decrement process in described 4th step uses the polyamide of acid solution etching fiber surface to become Point, its treatment conditions are: pH value is 2~5, and temperature is 40~90 DEG C, and the time is 1~5min;Or Using the polyester component of alkaline solution etching fiber surface, its treatment conditions are: NaOH weight percent concentration It is 0.5~2.0wt%, temperature 80~90 DEG C, the time 1~5min.
It is highly preferred that add semi-annular jade pendant base succinate, butyl naphthalene sulfonate, middle carbon alcohol phosphoric acid in described treatment fluid At least one in ester, capryl alcohol polyoxyethylene ether is as penetrating agent, and its weight percent concentration is 1.0~2.5 Wt%.
Preferably, in described 5th step, water jet process condition is: spun lacing number of channels is 2~4 roads, and liquid drugs injection pressure is 70~100Bar.
Preferably, the temperature dried in described 6th step is 100~150 DEG C.
Preferably, the polyester/polyamide blend filament spunlace non-woven material obtained by described 5th step is being dried Take a step forward and be impregnated in the hydrophobic finishing liquid containing low-surface energy substance, carry out hydrophobic Final finishing.
It is highly preferred that the low-surface energy substance in described hydrophobic finishing liquid is politef, flourine-containing acrylate ester, Fluorine carbon phosphate ester, any one of polydimethylsiloxane and silicon fluoride apoplexy due to endogenous wind, its weight hundred in dressing liquid Proportion by subtraction concentration is 1.5~3.0wt%.
The polymer melt that polyester and polyamide two kinds have different acid-base reaction characteristic is blended by the present invention, passes through Spunbond forming technology prepares polyester/polyamide blend filament fleece, certain by giving fibre web after pinprick reinforcement Mechanical property, be then dipped in weak acid or weak caustic solution, partial etching falls the polyester of fiber surface Or polyamide component, thus form coarse structure at fiber surface.Spun lacing is reinforced further, washes simultaneously The treatment fluid of fiber surface, carries out hydrophobic Final finishing the most again, obtain fiber surface coarse and be coated with thin The polyester/polyamide blend filament non-woven material of water finishing agent.This invented technology technology path integrated level is high, Raw material sources are wide, have obvious technical advantage.Made shaggy hydrophobic polyester/polyamide filaments Non-woven filtrate, can show more preferable hydrophobic effect, when being used as flue filtering material, shows preferably Anti-dew effect.Meanwhile, filament fiber also gives the higher mechanical property of filtrate and more preferable dimensional stability.
Detailed description of the invention
For making the present invention become apparent, hereby with preferred embodiment, it is described in detail below.
Embodiment 1
The first step: the COPET that cut into slices by water-soluble polyester (Changzhou synthetic material company limited) and relative viscosity are It is 30 that the polyamide PA6 (Mei Da nylon chips limited company of Xinhui of Guangdong Province) of 3.48 dries water content ppm。
Second step: the polyester dried and polyamide section are joined spunbond production according to the ratio of 40: 60 In the screw extruder hopper of line, set each district temperature of extruder as 150 DEG C of a district, two 180 DEG C of districts, Three 270 DEG C of districts, four 320 DEG C of districts, die head temperature 300 DEG C, the temperature of cross air blasting is 25 DEG C, drawing air Speed is 500m/s, carries out the spunbond shaping of polyester/polyamide blend filament.
3rd step, is transported to acupuncture unit by above-mentioned spunbond forming polyester/polyamide blended filament web and carries out 1 The main pinprick reinforcement of road pre-needling and 2 roads.Wherein, the 2000 pieces/m of bestock of pre-needling machine, use lower thorn Formula pricker movement locus, punch frequency is 300 thorns/min.First and the main acupuncture of second are respectively adopted thorn Formula and lower thorn formula acupuncture movement locus, 4000 pieces/m of needle plate bestock, punch frequency is 800 thorns/min.
4th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through pinprick reinforcement into decrement Carrying out decrement treatment in treatment trough, alkaline solution treatment conditions are: the weight percent concentration of NaOH is 0.5 Wt%, temperature 80 DEG C, time 1min, make fiber surface be roughened.
5th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through decrement treatment into spun-laced machine Reinforcing, wash away the alkali treatment fluid of fiber surface simultaneously, water jet process condition is: 2 road spun lacing, first The liquid drugs injection pressure of road and second water jet is respectively 70Bar and 90Bar.
6th step, the polyester/polyamide blend filament non-woven material the 5th step prepared is sent in dehydrator and is dried Dry, the temperature of dehydrator is 100 DEG C, obtains the non-woven filter of polyester/polyamide blend filament that fiber surface is coarse Material, its surface density is 150g/m2, Air permenbility is 40L/ (m2S), contact angle is 110 °, fibre diameter Being 35 μm, fiber surface roughness is 0.025 μm.
Embodiment 2
The first step: by polyester slice BRN-204 (China PetroChemical Corporation) andWater content is dried in Copolyamides copolyamide (Shanghai Ah's Kerma (unit of kinetic energy) Chemical Co., Ltd.) section For 20ppm.
Second step: the polyester dried and copolyamide resin slicer are joined spunbond life according to the ratio of 60: 40 Produce in the screw extruder hopper of line, set each district temperature of extruder as 180 DEG C of a district, two 270 DEG C of districts, Three 320 DEG C of districts, four 330 DEG C of districts, die head temperature 320 DEG C, the temperature of cross air blasting is 15 DEG C, drawing-off sky The speed of gas is 900m/s, carries out the spunbond shaping of polyester/polyamide blend filament.
3rd step, is transported to acupuncture unit by above-mentioned spunbond forming polyester/polyamide blended filament web and carries out 1 The main pinprick reinforcement of road pre-needling and 2 roads.Wherein, the 2000 pieces/m of bestock of pre-needling machine, use lower thorn Formula pricker movement locus, punch frequency is 600 thorns/min.First and the main acupuncture of second are respectively adopted thorn Formula and lower thorn formula acupuncture movement locus, 4000 pieces/m of needle plate bestock, punch frequency is 1200 thorns/min.
4th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through pinprick reinforcement into decrement Carrying out decrement treatment in treatment trough, acid solution treatment conditions are: pH value is 2, and temperature is 40 DEG C, the time For 2min, partial etching falls the copolyamide composition of fiber surface, makes fiber surface be roughened.
5th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through alkali decrement treatment into spun lacing Machine is reinforced, and washes away the treatment fluid of fiber surface simultaneously, and water jet process condition is: 4 road spun lacing, each road The liquid drugs injection pressure of water jet is respectively 70, and 80,90 and 100Bar.
6th step, the polyester/polyamide blend filament non-woven material the 5th step prepared is sent in dehydrator and is dried Dry, the temperature of dehydrator is 120 DEG C, and the polyester/polyamide blend filament obtaining fiber surface coarse is non-woven Filtrate, its surface density is 180g/m2, Air permenbility is 30L/ (m2S), contact angle is 115 °, and fiber is straight Footpath is 18 μm, and fiber surface roughness is 0.030 μm.
Embodiment 3
The first step: the COPET that cut into slices by water-soluble polyester (Changzhou synthetic material company limited) and relative viscosity are It is 30 that the polyamide PA6 (Mei Da nylon chips limited company of Xinhui of Guangdong Province) of 3.48 dries water content ppm。
Second step: the polyester dried and polyamide section are joined spunbond production according to the ratio of 40: 60 In the screw extruder hopper of line, set each district temperature of extruder as 150 DEG C of a district, two 180 DEG C of districts, Three 270 DEG C of districts, four 320 DEG C of districts, die head temperature 300 DEG C, the temperature of cross air blasting is 10 DEG C, drawing air Speed is 500m/s, carries out the spunbond shaping of polyester/polyamide blend filament.
3rd step, is transported to acupuncture unit by above-mentioned spunbond forming polyester/polyamide blended filament web and carries out 1 The main pinprick reinforcement of road pre-needling and 2 roads.Wherein, the 3000 pieces/m of bestock of pre-needling machine, use lower thorn Formula pricker movement locus, punch frequency is 300 thorns/min.First and the main acupuncture of second are respectively adopted thorn Formula and lower thorn formula acupuncture movement locus, 6000 pieces/m of needle plate bestock, punch frequency is 800 thorns/min.
4th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through pinprick reinforcement into decrement Carrying out decrement treatment in treatment trough, alkaline solution treatment conditions are: the weight percent concentration of NaOH is 2.0 Wt%, temperature 90 DEG C, time 5min, partial etching falls the polyester components of fiber surface, makes fiber surface Roughening.
5th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through alkali decrement treatment into spun lacing Machine is reinforced, and washes away the treatment fluid of fiber surface simultaneously, and water jet process condition is: 2 road spun lacing, and first The liquid drugs injection pressure of road and second water jet is respectively 70Bar and 90Bar.
6th step, enters one by the polyester/polyamide blend filament spunlace non-woven material obtained by described 5th step Step is impregnated in the politef hydrophobic finishing liquid that weight percent concentration is 3.0wt%, carries out hydrophobic rear whole Reason.
7th step, the polyester/polyamide blend filament non-woven material the 6th step prepared is sent in dehydrator and is dried Dry, the temperature of dehydrator is 150 DEG C, obtains the non-woven filter of polyester/polyamide blend filament that fiber surface is coarse Material, its surface density is 150g/m2, Air permenbility is 37L/ (m2S), contact angle is 125 °, fibre diameter Being 32 μm, fiber surface roughness is 0.05 μm.
Embodiment 4
The first step: be by polyester slice BRN-204 (China PetroChemical Corporation) and the trade mark It is 30ppm that the polyamide PA66 (China Shenma Group Co., Ltd.) of FYR25BCL dries water content.
Second step: the polyester dried and copolyamide resin slicer are joined spunbond life according to the ratio of 90: 10 Produce in the screw extruder hopper of line, be simultaneously introduced the epoxy resin that weight percent concentration is 1.0wt% CYD-011 (Ba Ling petrochemical industry chemical company), sets each district temperature of extruder as 180 DEG C of a district, 2nd district 270 DEG C, three 300 DEG C of districts, four 3320 DEG C of districts, die head temperature 320 DEG C, the temperature of cross air blasting is 15 DEG C, leads The speed stretching air is 800m/s, carries out the spunbond shaping of polyester/polyamide blend filament.
3rd step, is transported to acupuncture unit by above-mentioned spunbond forming polyester/polyamide blended filament web and carries out 1 The main pinprick reinforcement of road pre-needling and 2 roads.Wherein, the 2500 pieces/m of bestock of pre-needling machine, use lower thorn Formula pricker movement locus, punch frequency is 400 thorns/min.First and the main acupuncture of second are respectively adopted thorn Formula and lower thorn formula acupuncture movement locus, 5000 pieces/m of needle plate bestock, punch frequency is 1000 thorns/min.
4th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through pinprick reinforcement into decrement Carrying out decrement treatment in treatment trough, alkaline solution treatment conditions are: the weight percent concentration of NaOH is 2.0 Wt%, temperature 90 DEG C, time 5min, partial etching falls the polyester components of fiber surface, makes fiber surface Roughening.
5th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through alkali decrement treatment into spun lacing Machine is reinforced, and washes away the treatment fluid of fiber surface simultaneously, and water jet process condition is: 4 road spun lacing, each road The liquid drugs injection pressure of water jet is respectively 70, and 80,90 and 100Bar.
6th step, enters one by the polyester/polyamide blend filament spunlace non-woven material obtained by described 5th step Step is impregnated in the polydimethylsiloxane hydrophobic finishing liquid that weight percent concentration is 1.5wt%, carries out hydrophobic Final finishing.
7th step, the polyester/polyamide blend filament non-woven material the 6th step prepared is sent in dehydrator and is dried Dry, the temperature of dehydrator is 140 DEG C, and the polyester/polyamide blend filament obtaining fiber surface coarse is non-woven Filtrate, its surface density is 250g/m2, Air permenbility is 28L/ (m2S), contact angle is 125 °, and fiber is straight Footpath is 20 μm, and fiber surface roughness is 0.035 μm.
Embodiment 5
The first step: by polyester slice that the trade mark is SB500 (Sinopec Yizheng Fiber Optical plant Co., Ltd) and Relative viscosity is that PA6 (Mei Da nylon chips limited company of the Xinhui of Guangdong Province) drying of 3.48 is to water content For 30ppm.
Second step: the polyester dried and polyamide section are joined spunbond production according to the ratio of 10: 90 In the screw extruder hopper of line, set each district temperature of extruder as 150 DEG C of a district, two 180 DEG C of districts, Three 270 DEG C of districts, four 320 DEG C of districts, die head temperature 300 DEG C, the temperature of cross air blasting is 10 DEG C, and drawing-off is empty The speed of gas is 900m/s, carries out the spunbond shaping of polyester/polyamide blend filament.
3rd step, is transported to acupuncture unit by above-mentioned spunbond forming polyester/polyamide blended filament web and carries out 1 The main pinprick reinforcement of road pre-needling and 2 roads.Wherein, the 3000 pieces/m of bestock of pre-needling machine, use lower thorn Formula pricker movement locus, punch frequency is 600 thorns/min.First and the main acupuncture of second are respectively adopted thorn Formula and lower thorn formula acupuncture movement locus, 6000 pieces/m of needle plate bestock, punch frequency is 1200 thorns/min.
4th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through pinprick reinforcement into decrement Carrying out decrement treatment in treatment trough, acid solution treatment conditions are: pH value is 2, and capryl alcohol polyoxyethylene ether oozes The weight percent concentration of agent is 2.5wt% thoroughly, and temperature is 90 DEG C, and the time is 5min, and partial etching falls fibre The polyamide component in dimension table face, makes fiber surface be roughened.
5th step, sends the above-mentioned polyester/polyamide blend filament non-woven material through decrement treatment into spun-laced machine Reinforcing, wash away the treatment fluid of fiber surface simultaneously, water jet process condition is: 4 road spun lacing, each road water The liquid drugs injection pressure of tartar is respectively 70, and 80,90 and 100Bar.
6th step, enters one by the polyester/polyamide blend filament spunlace non-woven material obtained by described 5th step Step be impregnated in the flourine-containing acrylate ester hydrophobic finishing liquid that weight percent concentration is 3.0wt%, carry out hydrophobic after Arrange.
7th step, the polyester/polyamide blend filament non-woven material the 6th step prepared is sent in dehydrator and is dried Dry, the temperature of dehydrator is 140 DEG C, and the polyester/polyamide blend filament obtaining fiber surface coarse is non-woven Filtrate, its surface density is 250g/m2, Air permenbility is 25L/ (m2S), contact angle is 130 °, and fiber is straight Footpath is 15 μm, and fiber surface roughness is 0.1 μm.

Claims (18)

1. a complex nonwoven filtering material, it is characterised in that fiber surface is because reinforcing through acupuncture and spun lacing and have There is bending channel aperture structure;Every fiber in non-woven filter material includes in island shape random simultaneously Polyester and two kinds of polymer component of polyamide.
2. complex nonwoven filtering material as claimed in claim 1, it is characterised in that its surface density is 150~250g/m2, Air permenbility is 25~40L/ (m2S), contact angle is 110 °~130 °, polyester/polyamides The average diameter of amine blend filament is 15~35 μm, and the roughness of fiber surface is 0.025~0.1 μm.
3. complex nonwoven filtering material as claimed in claim 1, it is characterised in that described polyester and polyamide Can be homopolymer, it is also possible to be copolymer.
4. complex nonwoven filtering material as claimed in claim 1, it is characterised in that described polyester and polyamide Differences in viscosity be not more than 300Pa s.
5. complex nonwoven filtering material as claimed in claim 1, it is characterised in that in every fiber polyester and The percentage by weight of polyamide is 1/99~99/1.
6. complex nonwoven filtering material as claimed in claim 5, it is characterised in that in every fiber polyester and The percentage by weight of polyamide is 40/60~60/40.
7. complex nonwoven filtering material as claimed in claim 1, it is characterised in that raw material is except polyester and gathers Outside amide blending resin, also include epoxy resin, maleic anhydride grafted polymer, polyester-polyamide copolymer In at least one as compatilizer.
8. complex nonwoven filtering material as claimed in claim 7, it is characterised in that described compatilizer is at fiber In weight percent concentration be 1.0wt%~5.0wt%.
9. a preparation method for the complex nonwoven filtering material described in claim 1-8 any one, its feature exists In, specifically comprise the following steps that
The first step: polyester and polyamide are dried;
Second step: the polyester of drying, polyamide and/or compatilizer are proportionally added into product line of spinning viscose Screw extruder in, carry out the spunbond shaping of polyester/polyamide blend filament;
3rd step: above-mentioned spunbond forming polyester/polyamide blended filament web is transported to acupuncture unit and carries out 1 The main pinprick reinforcement of road pre-needling and 2 roads;
4th step: be sent to subtract by the above-mentioned polyester/polyamide blend filament non-woven material through pinprick reinforcement Carrying out decrement treatment in amount treatment trough, partial etching falls polyester or the polyamide component of fiber surface, makes fiber Rough surface;
5th step: the above-mentioned polyester/polyamide blend filament non-woven material through decrement treatment is sent to spun lacing Machine is reinforced, and washes away the treatment fluid of fiber surface simultaneously;
6th step: the polyester/polyamide blend filament non-woven material the 5th step prepared is sent in dehydrator and dried Dry, obtain the non-woven filtrate of polyester/polyamide blend filament that fiber surface is coarse.
10. the preparation method of complex nonwoven filtering material as claimed in claim 9, it is characterised in that described the After in one step, polyester and polyamide section are dried, its water content is not more than 40ppm.
The preparation method of 11. complex nonwoven filtering materials as claimed in claim 9, it is characterised in that described Two step spunbond process are: each district temperature of extruder: a district 150~180 DEG C, two districts 180~270 DEG C, 3rd district 270~330 DEG C, four districts 320~340 DEG C;Die head temperature 300~320 DEG C;Cross air blasting temperature is 10~25 DEG C;Lead Stretching air velocity is 500~900m/s.
The preparation method of 12. complex nonwoven filtering materials as claimed in claim 9, it is characterised in that described Three step needling processes are: bestock 2000-3000 piece of pre-needling machine/m, use lower thorn formula pricker motion rail Mark, punch frequency is 300-600 thorn/min;First and the main acupuncture of second are respectively adopted thorn formula and lower thorn Formula acupuncture movement locus, needle plate bestock 4000-6000 piece/m, punch frequency is 800-1200 thorn/min.
The preparation method of 13. polyester/polyamide blend filament filtering materials as claimed in claim 9, its feature exists In, the decrement process in described 4th step uses the polyamide component of acid solution etching fiber surface, and it processes Condition is: pH value is 2~5, and temperature is 40~90 DEG C, and the time is 1~5min;Or employing alkaline solution Etching fiber surface polyester component, its treatment conditions are: NaOH weight percent concentration be 0.5~ 2.0wt%, temperature 80~90 DEG C, the time 1~5min.
The preparation method of 14. complex nonwoven filtering materials as claimed in claim 13, it is characterised in that in institute State addition semi-annular jade pendant base succinate, butyl naphthalene sulfonate, middle carbon alcohol phosphate ester, capryl alcohol polyoxyethylene ether in treatment fluid In at least one as penetrating agent, its weight percent concentration is 1.0~2.5wt%.
The preparation method of 15. complex nonwoven filtering materials as claimed in claim 9, it is characterised in that described In five steps, the process conditions of spun lacing are: spun lacing number of channels is 2~4 roads, and liquid drugs injection pressure is 70~100Bar.
The preparation method of 16. complex nonwoven filtering materials as claimed in claim 9, it is characterised in that described The temperature dried in six steps is 100~150 DEG C.
The preparation method of 17. complex nonwoven filtering materials as claimed in claim 9, it is characterised in that described Polyester/polyamide blend filament spunlace non-woven material obtained by five steps is impregnated into the most further containing low In the hydrophobic finishing liquid of surface energy substance, carry out hydrophobic Final finishing.
The preparation method of 18. complex nonwoven filtering materials as claimed in claim 17, it is characterised in that described Low-surface energy substance in hydrophobic finishing liquid is politef, flourine-containing acrylate ester, fluorine carbon phosphate ester, poly-two Any one of methylsiloxane and silicon fluoride apoplexy due to endogenous wind, its weight percent concentration in dressing liquid be 1.5~ 3.0wt%.
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CN111501201A (en) * 2020-04-20 2020-08-07 陕西科技大学 Super-hydrophobic split-type superfine fiber non-woven fabric and preparation method thereof
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CN114875578A (en) * 2022-04-08 2022-08-09 南通大学 Degradable online spunlace composite filter material and preparation method thereof

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