CN108950839B - A kind of production method for removing the ultra-fine wiping non-dust cloth of white mark - Google Patents
A kind of production method for removing the ultra-fine wiping non-dust cloth of white mark Download PDFInfo
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- CN108950839B CN108950839B CN201810894620.2A CN201810894620A CN108950839B CN 108950839 B CN108950839 B CN 108950839B CN 201810894620 A CN201810894620 A CN 201810894620A CN 108950839 B CN108950839 B CN 108950839B
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- reverse osmosis
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- 239000004744 fabric Substances 0.000 title claims abstract description 144
- 239000000428 dust Substances 0.000 title claims abstract description 119
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 87
- 239000002131 composite material Substances 0.000 claims abstract description 10
- 239000004952 Polyamide Substances 0.000 claims abstract description 9
- 229920002647 polyamide Polymers 0.000 claims abstract description 9
- 238000007670 refining Methods 0.000 claims description 72
- 238000001223 reverse osmosis Methods 0.000 claims description 66
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 34
- 239000003513 alkali Substances 0.000 claims description 20
- 238000013022 venting Methods 0.000 claims description 19
- 239000003795 chemical substances by application Substances 0.000 claims description 16
- 239000002253 acid Substances 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 12
- 239000002585 base Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 10
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- 238000004513 sizing Methods 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 8
- 238000010521 absorption reaction Methods 0.000 claims description 5
- 238000007664 blowing Methods 0.000 claims description 5
- 238000002485 combustion reaction Methods 0.000 claims description 5
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 239000008367 deionised water Substances 0.000 claims description 5
- 229910021641 deionized water Inorganic materials 0.000 claims description 5
- 238000009826 distribution Methods 0.000 claims description 5
- 239000003814 drug Substances 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 5
- 239000003345 natural gas Substances 0.000 claims description 5
- 230000003252 repetitive effect Effects 0.000 claims description 5
- 230000002000 scavenging effect Effects 0.000 claims description 5
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- 238000005213 imbibition Methods 0.000 abstract description 4
- 239000012466 permeate Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 229910001948 sodium oxide Inorganic materials 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04B—KNITTING
- D04B1/00—Weft knitting processes for the production of fabrics or articles not dependent on the use of particular machines; Fabrics or articles defined by such processes
- D04B1/14—Other fabrics or articles characterised primarily by the use of particular thread materials
- D04B1/16—Other fabrics or articles characterised primarily by the use of particular thread materials synthetic threads
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
- B08B3/08—Cleaning involving contact with liquid the liquid having chemical or dissolving effect
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
- B08B3/10—Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
- D06B15/00—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours
- D06B15/09—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours by jets of gases
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
- D06B15/00—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours
- D06B15/10—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours by use of centrifugal force
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
- D06B3/00—Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating
- D06B3/10—Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of fabrics
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06C—FINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
- D06C7/00—Heating or cooling textile fabrics
- D06C7/02—Setting
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M11/00—Treating 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
- D06M11/32—Treating 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
- D06M11/36—Treating 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
- D06M11/38—Oxides or hydroxides of elements of Groups 1 or 11 of the Periodic Table
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B2203/00—Details of cleaning machines or methods involving the use or presence of liquid or steam
- B08B2203/007—Heating the liquid
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M2101/00—Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
- D06M2101/16—Synthetic fibres, other than mineral fibres
- D06M2101/30—Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D06M2101/32—Polyesters
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M2101/00—Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
- D06M2101/16—Synthetic fibres, other than mineral fibres
- D06M2101/30—Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D06M2101/34—Polyamides
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2331/00—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
- D10B2331/02—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyamides
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2331/00—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
- D10B2331/04—Fibres 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]
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
Abstract
The invention belongs to non-dust cloth production technical field more particularly to a kind of production methods for removing the ultra-fine wiping non-dust cloth of white mark.The dustless cloth non-dust cloth ontology of the super wear resistance is cross-woven using polyamide composite filaments, has good wearability and water imbibition.In addition, the non-dust cloth may be implemented to panel or accurate chip wiping, and white mark residual is not left.In addition, this goes the production method technological design of the ultra-fine wiping non-dust cloth of white mark reasonable, working condition is easy to control, and production efficiency is higher, is suitble to promote the use of.
Description
Technical field
The invention belongs to non-dust cloth production technical field more particularly to a kind of production sides for removing the ultra-fine wiping non-dust cloth of white mark
Method.
Background technique
Non-dust cloth soft surface is easy to wipe sensing surface, and friction does not take off fiber, has good water imbibition and cleaning effect
Rate.The cleaning of product and packaging are completed in Superclean workshop.The optional edge sealing of non-dust cloth generally has: cold sanction, laser edge bonding, ultrasonic wave
Edge sealing.
Common non-dust cloth is usually to wash bright and beautiful composite yarn using the 8:2 or 7:3 of 75D/36F and produce, the cleaning of product and
Packaging is completed in Superclean workshop, and can be widely applied to semiconductor fab production line, and LCD shows class product line, accurate
Instrument production line, optical articles production line, in Medical Devices production line and dust-free workshop, client's is main during use
Purpose is that panel or accurate chip wiping are remained without white mark, then the wiping effect to non-dust cloth proposes very strict requirements, is
Cope with the requirement.
In order to solve the above-mentioned technical problem, the present invention devises a kind of production method for removing the ultra-fine wiping non-dust cloth of white mark,
The dustless cloth non-dust cloth ontology of the super wear resistance is cross-woven using polyamide composite filaments, has good wearability and water suction
Property.In addition, the non-dust cloth may be implemented to panel or accurate chip wiping, and white mark residual is not left.In addition, this goes white mark
The production method technological design of ultra-fine wiping non-dust cloth is reasonable, and working condition is easy to control, and production efficiency is higher, and suitable popularization makes
With.
Summary of the invention
In order to overcome defect present in background technique, the technical solution adopted by the present invention to solve the technical problems is:
A kind of production method for removing the ultra-fine wiping non-dust cloth of white mark, the steps include:
(1), section is refined.By the polyamide composite filaments of 75D/36F by the circle of 38-42 needle compile it is woven caused by non-dust cloth and super
It is that 1:8-10 is added in refining cylinder that drainage, which is crossed, according to weight ratio, and the water temperature in control refining cylinder is opened within the scope of 55-75 DEG C
Begin that medicament is added, dosages distribution is more than 1-2 grams of refining agent to be added in drainage, while every liter is more than in drainage for every liter in refining cylinder
It is added 3-6 grams of sodium hydroxide, to be stirred continuously in refining agent and sodium hydroxide adding procedure, and control refining agent and hydroxide
Sodium adds completion in 10 minutes；Then temperature is risen to 110-120 DEG C with 1.5-3 DEG C per minute of heating rate, refines cylinder
Interior pressure is 1.0-2.0kg, refines the non-dust cloth in cylinder and is rotated with 60-80 rpms, and keeps the temperature 60-80 minutes；Then with
After the temperature refined in cylinder is reduced to 75 DEG C by the speed per minute for being reduced to 1.0-1.5 DEG C, overflow is carried out 10 minutes with more than drainage,
Then it carries out cloth and moves venting to be more than drainage；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is
8-10:1 will refine the temperature in cylinder and control within the scope of 35-45 DEG C, be initially added into acid, and acid proportion is anti-for every liter in refining cylinder
It permeates and 0.5-1 grams of acid is added in water, refine the non-dust cloth in cylinder and after rotation 10-15 minutes, then carried out with 60-80 rpms
Cloth moves venting reverse osmosis water；Then reverse osmosis water being added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 8-10:1,
The temperature in cylinder will be refined to control within the scope of 55-75 DEG C, the non-dust cloth in cylinder is refined and rotated with 60-80 rpms, started
White mark remover and alkali is added, white mark remover proportion is 4-6 grams of white mark remover of addition in every liter of reverse osmosis water in refining cylinder,
Alkali proportion controls white mark remover and alkali and adds in 10 minutes to be added 1-2 grams of alkali in every liter of reverse osmosis water in refining cylinder
It completes, temperature is then risen to 85-100 DEG C with 1.5-3 DEG C per minute of heating rate, refining in-cylinder pressure is 1.0-2.0kg,
It refines the non-dust cloth in cylinder to rotate with 60-80 rpms, and keeps the temperature 20-30 minutes；Then to be reduced to 2.0-2.5 DEG C per minute
Speed the temperature refined in cylinder is reduced to 75 DEG C after, carries out overflow 10 minutes with reverse osmosis water, it is anti-then to carry out the dynamic venting of cloth
Permeate water；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 10-15:1, is refined in cylinder
Non-dust cloth after rotation 10-20 minutes, carries out overflow 10-20 minutes with reverse osmosis water, then venting reverse osmosis with 60-80 rpms
It is permeable；
(2), it is dehydrated.Centrifugal dehydration is carried out to the non-dust cloth after refining, revolving speed is 700-800 rpms, time 20-
35 minutes；
(3), it is formed.Forming machine is 8 sections, is heated with combustion of natural gas, whole controllable base weight, thickness and breadth, sizing
Temperature is 160-170 DEG C, and it is 30-45 meters per minute that host, which drives non-dust cloth forward speed, is compressed above non-dust cloth in forming machine
The linear velocity of roller operation is 1-1.1 times of non-dust cloth forward speed, compresses the line of roller operation in forming machine below non-dust cloth
Speed is 1-1.1 times of non-dust cloth forward speed, is formed breadth 165-175 meters, and the base weight of non-dust cloth is 165-200 grams after sizing
Every square metre, the thickness of non-dust cloth is greater than 0.4 millimeter, and the water absorption of non-dust cloth is greater than 300 milliliters every square metre；
(4), it cuts.It is carried out using ultrasonic wave hilted broadsword mode or the mode of flanging；
(5), clean.Cleaning the piece number is 6000-10000 piece/vehicle, and every length and width are 9 inches, and deionized water 600- is added
800 kilograms, temperature is 25-45 DEG C, and scavenging period is to be dried after 5-15 minutes, repetitive operation 2-5 times, and drying temperature is
60-65 DEG C, blowing hot-air is blown a cold wind over 10-15 minutes after 25-30 minutes, that is, is prepared into the ultra-fine wiping non-dust cloth of white mark.
It is according to the present invention it is a kind of go white mark it is ultra-fine wiping non-dust cloth production method, the dustless cloth of the super wear resistance without
Dirt cloth ontology is cross-woven using polyamide composite filaments, has good wearability and water imbibition.In addition, the non-dust cloth can be with
It realizes to panel or accurate chip wiping, and does not leave white mark residual.In addition, this goes the production of the ultra-fine wiping non-dust cloth of white mark
Rationally, working condition is easy to control, and production efficiency is higher for method and process design, is suitble to promote the use of.
Specific embodiment
A kind of specific embodiment one, production method for removing the ultra-fine wiping non-dust cloth of white mark, the steps include:
(1), section is refined.By the polyamide composite filaments of 75D/36F by the circle of 38-42 needle compile it is woven caused by non-dust cloth and super
It is that 1:8 is added in refining cylinder that drainage, which is crossed, according to weight ratio, and the water temperature in control refining cylinder is initially added within the scope of 55 DEG C
Medicament, dosages distribution are more than 1 gram of refining agent to be added in drainage, while every liter is more than that hydrogen-oxygen is added in drainage for every liter in refining cylinder
Change 3 grams of sodium, to be stirred continuously in refining agent and sodium hydroxide adding procedure, and control refining agent and sodium hydroxide at 10 minutes
Interior addition is completed；Then temperature is risen to 110 DEG C with 1.5 DEG C of heating rate per minute, refining in-cylinder pressure is 1.0kg, essence
It refines the non-dust cloth in cylinder to rotate with 60 rpms, and keeps the temperature 60 minutes；Then it will be refined with the speed for being reduced to 1.0 DEG C per minute
After temperature in cylinder is reduced to 75 DEG C, with being more than that drainage carries out overflow 10 minutes, then carry out cloth and move venting to be more than drainage；Then to
The weight ratio of refining cylinder addition reverse osmosis water, reverse osmosis water and non-dust cloth is 8:1, will refine the temperature in cylinder and control at 35 DEG C
In range, it is initially added into acid, acid proportion refines the non-dust cloth in cylinder for 0.5 gram of acid is added in every liter of reverse osmosis water in refining cylinder
With 60 rpms after rotation 10-15 minutes, then carries out cloth and move venting reverse osmosis water；Then it is added to refining cylinder reverse osmosis
The weight ratio of water, reverse osmosis water and non-dust cloth is 8:1, will refine the temperature in cylinder and controls within the scope of 55 DEG C, refines in cylinder
Non-dust cloth is rotated with 60 rpms, is initially added into white mark remover and alkali, and white mark remover proportion is anti-for every liter in refining cylinder
It permeates and 4 grams of white mark remover is added in water, alkali proportion controls white mark to be added 1 gram of alkali in every liter of reverse osmosis water in refining cylinder
Remover and alkali add completion in 10 minutes, and temperature is then risen to 85 DEG C with 1.5 DEG C of heating rate per minute, refine cylinder
Interior pressure is 1.0kg, refines the non-dust cloth in cylinder and is rotated with 60 rpms, and keeps the temperature 20 minutes；Then to be reduced to per minute
After the temperature refined in cylinder is reduced to 75 DEG C by 2.0 DEG C of speed, overflow is carried out 10 minutes with reverse osmosis water, then carries out the dynamic row of cloth
Remove reverse osmosis water；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 10:1, is refined in cylinder
Non-dust cloth with 60 rpms rotation after ten minutes, carry out overflow 10 minutes with reverse osmosis water, then venting reverse osmosis water；
(2), it is dehydrated.Centrifugal dehydration is carried out to the non-dust cloth after refining, revolving speed is 700 rpms, and the time is 20 minutes；
(3), it is formed.Forming machine is 8 sections, is heated with combustion of natural gas, whole controllable base weight, thickness and breadth, sizing
Temperature is 160 DEG C, and it is 30 meters per minute that host, which drives non-dust cloth forward speed, compresses roller operation in forming machine above non-dust cloth
Linear velocity be 1 times of non-dust cloth forward speed, the linear velocity for compressing roller operation in forming machine below non-dust cloth is non-dust cloth
1 times of forward speed is formed 165 meters of breadth, and the base weight of non-dust cloth is 165 grams every square metre after sizing, and the thickness of non-dust cloth is big
In 0.4 millimeter, the water absorption of non-dust cloth is greater than 300 milliliters every square metre；
(4), it cuts.It is carried out using ultrasonic wave hilted broadsword mode；
(5), clean.Cleaning the piece number is 6000/vehicle, and every length and width are 9 inches, is added 600 kilograms of deionized water, temperature
It is 25 DEG C, scavenging period is to be dried after 5 minutes, repetitive operation 2 times, and drying temperature is 60 DEG C, blowing hot-air after-blow in 25 minutes
Cold wind 10 minutes, that is, it is prepared into the ultra-fine wiping non-dust cloth of white mark.
A kind of specific embodiment two, production method for removing the ultra-fine wiping non-dust cloth of white mark, the steps include:
(1), section is refined.By the polyamide composite filaments of 75D/36F by the circle of 38-42 needle compile it is woven caused by non-dust cloth and super
It is that 1:9 is added in refining cylinder that drainage, which is crossed, according to weight ratio, and the water temperature in control refining cylinder is initially added within the scope of 65 DEG C
Medicament, dosages distribution are more than 1.5 grams of refining agent to be added in drainage, while every liter is more than that hydrogen is added in drainage for every liter in refining cylinder
It 4 grams of sodium oxide molybdena, to be stirred continuously in refining agent and sodium hydroxide adding procedure, and control refining agent and sodium hydroxide at 10 points
Addition is completed in clock；Then temperature is risen to 115 DEG C with 2 DEG C of heating rate per minute, refining in-cylinder pressure is 1.5kg, essence
It refines the non-dust cloth in cylinder to rotate with 70 rpms, and keeps the temperature 70 minutes；Then it will be refined with the speed for being reduced to 1.2 DEG C per minute
After temperature in cylinder is reduced to 75 DEG C, with being more than that drainage carries out overflow 10 minutes, then carry out cloth and move venting to be more than drainage；Then to
The weight ratio of refining cylinder addition reverse osmosis water, reverse osmosis water and non-dust cloth is 9:1, will refine the temperature in cylinder and control at 40 DEG C
In range, it is initially added into acid, acid proportion refines the non-dust cloth in cylinder for 0.8 gram of acid is added in every liter of reverse osmosis water in refining cylinder
After being rotated 12 minutes with 70 rpms, then carries out cloth and move venting reverse osmosis water；Then reverse osmosis water is added to refining cylinder, instead
The weight ratio for permeating water and non-dust cloth is 9:1, will refine the temperature in cylinder and controls within the scope of 65 DEG C, refines the non-dust cloth in cylinder
It is rotated with 70 rpms, is initially added into white mark remover and alkali, white mark remover proportion is every liter of reverse osmosis water in refining cylinder
Middle 5 grams of addition white mark remover, alkali proportion controls white mark removal to be added 1.5 grams of alkali in every liter of reverse osmosis water in refining cylinder
Agent and alkali add completion in 10 minutes, and temperature is then risen to 90 DEG C with 2 DEG C of heating rate per minute, refine in-cylinder pressure
It for 1.2kg, refines the non-dust cloth in cylinder and is rotated with 70 rpms, and keep the temperature 25 minutes；Then to be reduced to 2.2 DEG C per minute
After the temperature refined in cylinder is reduced to 75 DEG C by speed, overflow is carried out 10 minutes with reverse osmosis water, is then carried out cloth and is moved venting reverse osmosis
It is permeable；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 13:1, is refined dustless in cylinder
After cloth is rotated 18 minutes with 70 rpms, overflow is carried out 18 minutes with reverse osmosis water, then venting reverse osmosis water；
(2), it is dehydrated.Centrifugal dehydration is carried out to the non-dust cloth after refining, revolving speed is 750 rpms, and the time is 30 minutes；
(3), it is formed.Forming machine is 8 sections, is heated with combustion of natural gas, whole controllable base weight, thickness and breadth, sizing
Temperature is 165 DEG C, and it is 35 meters per minute that host, which drives non-dust cloth forward speed, compresses roller operation in forming machine above non-dust cloth
Linear velocity be 1.1 times of non-dust cloth forward speed, it is dustless for compressing the linear velocity of roller operation in forming machine below non-dust cloth
1.1 times of cloth forward speed are formed breadth 165-175 meters, and the base weight of non-dust cloth is 180 grams every square metre after sizing, non-dust cloth
Thickness be greater than 0.4 millimeter, the water absorption of non-dust cloth is greater than 300 milliliters every square metre；
(4), it cuts.It is carried out using ultrasonic wave hilted broadsword mode；
(5), clean.Cleaning the piece number is 8000/vehicle, and every length and width are 9 inches, is added 800 kilograms of deionized water, temperature
It is 35 DEG C, scavenging period is to be dried after 10 minutes, repetitive operation 3 times, and drying temperature is 62 DEG C, blowing hot-air after-blow in 28 minutes
Cold wind 12 minutes, that is, it is prepared into the ultra-fine wiping non-dust cloth of white mark.
A kind of specific embodiment three, production method for removing the ultra-fine wiping non-dust cloth of white mark, the steps include:
(1), section is refined.By the polyamide composite filaments of 75D/36F by the circle of 38-42 needle compile it is woven caused by non-dust cloth and super
It is that 1:9 is added in refining cylinder that drainage, which is crossed, according to weight ratio, and the water temperature in control refining cylinder is initially added within the scope of 75 DEG C
Medicament, dosages distribution are more than 2 grams of refining agent to be added in drainage, while every liter is more than that hydrogen-oxygen is added in drainage for every liter in refining cylinder
Change 6 grams of sodium, to be stirred continuously in refining agent and sodium hydroxide adding procedure, and control refining agent and sodium hydroxide at 10 minutes
Interior addition is completed；Then temperature is risen to 120 DEG C with 3 DEG C of heating rate per minute, refining in-cylinder pressure is 2.0kg, refining
Non-dust cloth in cylinder is rotated with 80 rpms, and keeps the temperature 80 minutes；Then cylinder will be refined with the speed for being reduced to 1.5 DEG C per minute
After interior temperature is reduced to 75 DEG C, with being more than that drainage carries out overflow 10 minutes, then carry out cloth and move venting to be more than drainage；Then to essence
The weight ratio of refining cylinder addition reverse osmosis water, reverse osmosis water and non-dust cloth is 10:1, will refine the temperature in cylinder and control in 45 DEG C of models
In enclosing, it is initially added into acid, acid proportion refines the non-dust cloth in cylinder for 1 gram of acid is added in every liter of reverse osmosis water in refining cylinder with 80
Rpm rotation 15 minutes after, then carry out cloth move venting reverse osmosis water；Then reverse osmosis water is added to refining cylinder, it is reverse osmosis
The weight ratio of water and non-dust cloth be 10:1, will refine cylinder in temperature control within the scope of 75 DEG C, refine cylinder in non-dust cloth with
80 rpms of rotations are initially added into white mark remover and alkali, and white mark remover proportion is in every liter of reverse osmosis water in refining cylinder
Be added 6 grams of white mark remover, alkali proportion for 2 grams of alkali are added in every liter of reverse osmosis water in refining cylinder, and control white mark remover and
Alkali adds completion in 10 minutes, and temperature is then risen to 100 DEG C with 3 DEG C of heating rate per minute, and refining in-cylinder pressure is
2.0kg is refined the non-dust cloth in cylinder and is rotated with 80 rpms, and keeps the temperature 30 minutes；Then to be reduced to 2.5 DEG C of speed per minute
After the temperature refined in cylinder is reduced to 75 DEG C by degree, overflow is carried out 10 minutes with reverse osmosis water, and it is reverse osmosis then to carry out the dynamic venting of cloth
Water；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 15:1, refines the non-dust cloth in cylinder
After twenty minutes with 80 rpms of rotations, overflow is carried out 20 minutes with reverse osmosis water, then venting reverse osmosis water；
(2), it is dehydrated.Centrifugal dehydration is carried out to the non-dust cloth after refining, revolving speed is 800 rpms, and the time is 35 minutes；
(3), it is formed.Forming machine is 8 sections, is heated with combustion of natural gas, whole controllable base weight, thickness and breadth, sizing
Temperature is 170 DEG C, and it is 45 meters per minute that host, which drives non-dust cloth forward speed, compresses roller operation in forming machine above non-dust cloth
Linear velocity be 1.1 times of non-dust cloth forward speed, it is dustless for compressing the linear velocity of roller operation in forming machine below non-dust cloth
1.1 times of cloth forward speed are formed 175 meters of breadth, and the base weight of non-dust cloth is 200 grams every square metre after sizing, the thickness of non-dust cloth
Degree is greater than 0.4 millimeter, and the water absorption of non-dust cloth is greater than 300 milliliters every square metre；
(4), it cuts.It is carried out by the way of flanging；
(5), clean.Cleaning the piece number is 10000/vehicle, and every length and width are 9 inches, is added 800 kilograms of deionized water, temperature
Degree is 45 DEG C, and scavenging period is to be dried after 15 minutes, repetitive operation 5 times, after drying temperature is 65 DEG C, blowing hot-air 30 minutes
It blows a cold wind over 15 minutes, that is, is prepared into the ultra-fine wiping non-dust cloth of white mark.
It is according to the present invention it is a kind of go white mark it is ultra-fine wiping non-dust cloth production method, the dustless cloth of the super wear resistance without
Dirt cloth ontology is cross-woven using polyamide composite filaments, has good wearability and water imbibition.In addition, the non-dust cloth can be with
It realizes to panel or accurate chip wiping, and does not leave white mark residual.In addition, this goes the production of the ultra-fine wiping non-dust cloth of white mark
Rationally, working condition is easy to control, and production efficiency is higher for method and process design, is suitble to promote the use of.
Obviously, the above embodiments are merely examples for clarifying the description, and does not limit the embodiments.It is right
For those of ordinary skill in the art, can also make on the basis of the above description it is other it is various forms of variation or
It changes.There is no necessity and possibility to exhaust all the enbodiments.And it is extended from this it is obvious variation or
It changes still within the protection scope of the invention.
Claims (1)
1. a kind of production method for removing the ultra-fine wiping non-dust cloth of white mark, it is characterised in that the steps include:
(1) section is refined, non-dust cloth and hyperfiltration caused by the circle volume that the polyamide composite filaments of 75D/36F are passed through 38-42 needle is woven
Water is that 1:8-10 is added in refining cylinder according to weight ratio, and the water temperature in control refining cylinder starts to add within the scope of 55-75 DEG C
Enter medicament, dosages distribution is more than 1-2 grams of refining agent to be added in drainage, while every liter is more than to be added in drainage for every liter in refining cylinder
It 3-6 grams of sodium hydroxide, to be stirred continuously in refining agent and sodium hydroxide adding procedure, and control refining agent and sodium hydroxide exists
It adds and completes in 10 minutes；Then temperature is risen to 110-120 DEG C with 1.5-3 DEG C per minute of heating rate, refines cylinder internal pressure
Power is 1.0-2.0kg, refines the non-dust cloth in cylinder and is rotated with 60-80 rpms, and keeps the temperature 60-80 minutes；Then with every point
After the temperature refined in cylinder is reduced to 75 DEG C by the speed that clock is reduced to 1.0-1.5 DEG C, with being more than that drainage carries out overflow 10 minutes, then
It carries out cloth and moves venting to be more than drainage；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 8-
10:1 will refine the temperature in cylinder and control within the scope of 35-45 DEG C, be initially added into acid, and acid proportion is every liter of reverse osmosis in refining cylinder
Permeable 0.5-1 grams of middle addition acid, the non-dust cloth in cylinder is refined with 60-80 rpms and after rotation 10-15 minutes, then carries out cloth
Dynamic venting reverse osmosis water；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 8-10:1, will
The temperature refined in cylinder controls within the scope of 55-75 DEG C, refines the non-dust cloth in cylinder and is rotated with 60-80 rpms, starts to add
Enter white mark remover and alkali, white mark remover proportion is 4-6 grams of white mark remover of addition in every liter of reverse osmosis water in refining cylinder, alkali
Proportion controls white mark remover and alkali and has added in 10 minutes to be added 1-2 grams of alkali in every liter of reverse osmosis water in refining cylinder
At temperature then being risen to 85-100 DEG C with 1.5-3 DEG C per minute of heating rate, refining in-cylinder pressure is 1.0-2.0kg, essence
It refines the non-dust cloth in cylinder to rotate with 60-80 rpms, and keeps the temperature 20-30 minutes；Then to be reduced to 2.0-2.5 DEG C per minute
After the temperature refined in cylinder is reduced to 75 DEG C by speed, overflow is carried out 10 minutes with reverse osmosis water, is then carried out cloth and is moved venting reverse osmosis
It is permeable；Then reverse osmosis water is added to refining cylinder, the weight ratio of reverse osmosis water and non-dust cloth is 10-15:1, refines the nothing in cylinder
Dirt cloth after rotation 10-20 minutes, carries out overflow 10-20 minutes with reverse osmosis water, then venting is reverse osmosis with 60-80 rpms
Water；
(2), it is dehydrated, centrifugal dehydration is carried out to the non-dust cloth after refining, revolving speed is 700-800 rpms, and the time is 20-35 points
Clock；
(3), be formed: forming machine is 8 sections, is heated with combustion of natural gas, whole controllable base weight, thickness and breadth, setting temperature
It is 160-170 DEG C, it is 30-45 meters per minute that host, which drives non-dust cloth forward speed, compresses roller in forming machine above non-dust cloth
The linear velocity of operation is 1-1.1 times of non-dust cloth forward speed, compresses the linear velocity of roller operation in forming machine below non-dust cloth
It is 1-1.1 times of non-dust cloth forward speed, is formed breadth 165-175 meters, the base weight of non-dust cloth is often put down after sizing for 165-200 grams
Square rice, the thickness of non-dust cloth are greater than 0.4 millimeter, and the water absorption of non-dust cloth is greater than 300 milliliters every square metre；
(4), it cuts, is carried out using ultrasonic wave hilted broadsword mode or the mode of flanging；
(5), clean, cleaning the piece number is 6000-10000 piece/vehicle, and every length and width are 9 inches, and deionized water 600-800 thousand is added
Gram, temperature is 25-45 DEG C, and scavenging period is to be dried after 5-15 minutes, repetitive operation 2-5 times, drying temperature 60-65
DEG C, blowing hot-air is blown a cold wind over 10-15 minutes after 25-30 minutes, that is, is prepared into the ultra-fine wiping non-dust cloth of white mark.
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| CN111705403A (en) * | 2020-06-18 | 2020-09-25 | 龙钜超洁净科技（苏州）有限公司 | Preparation method of soft wear-resistant purification wiping dust-free cloth |
| CN112981680A (en) * | 2021-03-10 | 2021-06-18 | 苏州柯林赛思超净科技有限公司 | Manufacturing process of wear-resistant soft composite dust-free cloth |
| CN115125655B (en) * | 2022-07-15 | 2024-05-24 | 广东硕源科技股份有限公司 | Island microfiber low-cost dust-free wiping cloth and manufacturing method thereof |
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| CN104005169B (en) * | 2013-06-14 | 2016-01-13 | 营口三鑫合纤有限公司 | A kind of polyester-nylon composite superfine fibre high density non-dust cloth and preparation method thereof |
| CN104074043B (en) * | 2014-06-27 | 2016-03-30 | 广东硕源科技股份有限公司 | A kind of high convergency high-effective dust-removing non-dust cloth and production method thereof |
| CN106958070B (en) * | 2016-01-08 | 2019-04-23 | 龙钜超洁净科技（苏州）有限公司 | A kind of super wear resistance non-dust cloth and preparation method thereof |
| CN106968106B (en) * | 2017-06-01 | 2019-06-18 | 龙钜超洁净科技（苏州）有限公司 | A kind of low soft flocks non-dust cloth procedure for producing of super abrasive |
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