CN108330632A - A kind of fabric resin ironing-free technology - Google Patents
A kind of fabric resin ironing-free technology Download PDFInfo
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- CN108330632A CN108330632A CN201710031574.9A CN201710031574A CN108330632A CN 108330632 A CN108330632 A CN 108330632A CN 201710031574 A CN201710031574 A CN 201710031574A CN 108330632 A CN108330632 A CN 108330632A
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- collecting
- fabric
- ironing
- resin
- far
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- 239000004744 fabric Substances 0.000 title claims abstract description 55
- 239000011347 resin Substances 0.000 title claims abstract description 34
- 229920005989 resin Polymers 0.000 title claims abstract description 34
- 238000005516 engineering process Methods 0.000 title claims abstract description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000007921 spray Substances 0.000 claims abstract description 22
- 238000000034 method Methods 0.000 claims abstract description 15
- 230000008569 process Effects 0.000 claims abstract description 12
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000001035 drying Methods 0.000 claims abstract description 6
- 238000002425 crystallisation Methods 0.000 claims description 28
- 230000008025 crystallization Effects 0.000 claims description 28
- 230000008014 freezing Effects 0.000 claims description 11
- 238000007710 freezing Methods 0.000 claims description 11
- 238000005406 washing Methods 0.000 claims description 7
- 238000009990 desizing Methods 0.000 claims description 6
- 239000003513 alkali Substances 0.000 claims description 5
- 238000005098 hot rolling Methods 0.000 claims description 5
- 238000009992 mercerising Methods 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 81
- 230000000694 effects Effects 0.000 abstract description 10
- 238000010521 absorption reaction Methods 0.000 abstract description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 26
- 239000007789 gas Substances 0.000 description 26
- 239000001569 carbon dioxide Substances 0.000 description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 description 12
- 229920000742 Cotton Polymers 0.000 description 9
- 229940099596 manganese sulfate Drugs 0.000 description 9
- 235000007079 manganese sulphate Nutrition 0.000 description 9
- 239000011702 manganese sulphate Substances 0.000 description 9
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 9
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 description 9
- 229910052939 potassium sulfate Inorganic materials 0.000 description 9
- 235000011151 potassium sulphates Nutrition 0.000 description 9
- 238000010409 ironing Methods 0.000 description 7
- 238000003672 processing method Methods 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000004513 sizing Methods 0.000 description 3
- 239000002918 waste heat Substances 0.000 description 3
- 235000011089 carbon dioxide Nutrition 0.000 description 2
- 238000004132 cross linking Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 235000017550 sodium carbonate Nutrition 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000012224 working solution Substances 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 230000001153 anti-wrinkle effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229930002875 chlorophyll Natural products 0.000 description 1
- 235000019804 chlorophyll Nutrition 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005517 mercerization Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- 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
- D06B21/00—Successive treatments of textile materials by liquids, gases or vapours
-
- 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
- D06B23/00—Component parts, details, or accessories of apparatus or machines, specially adapted for the treating of textile materials, not restricted to a particular kind of apparatus, provided for in groups D06B1/00 - D06B21/00
- D06B23/20—Arrangements of apparatus for treating processing-liquids, -gases or -vapours, e.g. purification, filtration or distillation
-
- 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
- D06M11/51—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 sulfur, selenium, tellurium, polonium or compounds thereof
- D06M11/55—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 sulfur, selenium, tellurium, polonium or compounds thereof with sulfur trioxide; with sulfuric acid or thiosulfuric acid or their salts
- D06M11/56—Sulfates or thiosulfates other than of elements of Groups 3 or 13 of the Periodic Table
-
- 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
- D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
The invention discloses a kind of fabric resin ironing-free technologies, include to pad successively in upper resin process therein, it bakes, drying, fabric is passed into padder successively, baker, in dryer, padder, baker, collecting hood is respectively provided on dryer, the upper end of three collecting hoods is both provided with collecting pipe, the one end of collecting pipe far from collecting hood is provided with conduit, the one end of conduit far from collecting pipe is provided with wind turbine, the one end of wind turbine far from conduit is provided with collecting chamber, spray equipment is provided in collecting chamber, spray liquid in spray equipment uses liquor potassic permanganate, activated charcoal strainer is provided in collecting chamber.The present invention has the following advantages and effects：Formaldehyde gas is collected using collecting chamber, most formaldehyde gas can be sponged by wherein collecting after indoor spray liquid reacts with formaldehyde gas, can the formaldehyde gas of omission be subjected to double absorption using activated charcoal strainer simultaneously, achieve the effect that efficient process formaldehyde gas.
Description
Technical field
The present invention relates to a kind of processing method of fabric, more particularly to a kind of fabric resin ironing-free technology.
Background technology
Recently as the development of the improvement of people's living standards and dyeing and finishing processing technology, to making the pure cotton of garment material
Textile, it is proposed that crease-resistant, non-ironing and wash and wear requirement.Cotton fiber has good permeability, moisture absorption as a kind of natural fiber
Property strong, soft, the features such as wearer is comfortable, but cotton fiber is easy corrugation there is also elasticity is poor in dress and washing process
The shortcomings of, bring inconvenience to people’s lives.Therefore anti-crease finishing is carried out to cotton fabric, improves fabric elasticity, improve cotton
Fabric dry and wet state wrinkle resistance, it has also become urgent problem.
Currently, Publication No. CN1766223A, the day for announcing is Chinese patent on May 3rd, 2006《A kind of pure cotton non-ironing face fabric
Processing method》A kind of processing method of pure cotton non-ironing face fabric is disclosed, in original upper resin process and is banked up between technique
Technique is rewinded in increase, is increased alkali washing process between technique and washing process banking up, so that entire technological process is followed successively by and singe, move back
Slurry, mercerising, upper resin, rewind, bank up, alkali cleaning, washing, sizing, hot rolling, preshrunk, the processing method of this kind of pure cotton non-ironing face fabric
The advantages of be resin sizing package after rewinded again in thermostatic chamber, not only can from solved in temperature end to end, in side difference but also
This species diversity can also be eliminated from the time to large package, the cloth cover temperature after rewinding ensures that, at 30~45 DEG C, clothing can be met
Performance, and good cross-linking effect is can guarantee to reach preferable non-ironing effect；Residual can be effectively removed using alkali washing process
Excess resin in cloth, and the resin not reacted completely can be peeled off, to reach the formaldehyde for being effectively reduced cloth cover
The purpose of content.
The processing method of this kind of pure cotton non-ironing face fabric is in upper resin, the active group on molecular resin and cellulosic molecule
Hydroxyl, be combined into molecular bridge or covalent bond under certain condition, macromolecular chain adjacent in fiber be interconnected, because
And reduce the Relative sliding movement of two molecule interchains, the recovery capacity of deformation is improved, to improve the shrinkproof of fabric
Crease resistance；But in actual production processing, fabric is in upper resin, after being reacted between molecular resin and cellulosic molecule
Product also has formaldehyde gas, when process equipment it is permanent fabric is processed when, after the formaldehyde that is discharged can gradually increase
It is looped around in the side environment of shop equipment, causes the discomfort for causing body after operating personnel's inhaled formaldehyde in factory.
Invention content
It, can be to first that fabric discharges in noniron finish the object of the present invention is to provide a kind of fabric resin ironing-free technology
Aldehyde is handled.
The present invention above-mentioned technical purpose technical scheme is that：A kind of non-ironing work of fabric resin
Skill, include be followed successively by singe, desizing, mercerising, upper resin, rewind, bank up, alkali cleaning, washing, hot rolling, preshrunk technological process,
Include to pad, bake, drying successively in the upper resin process, fabric is passed into padder, baker, dryer successively
Interior, the padder, the baker are respectively provided with collecting hood on the dryer, and the upper end of three collecting hoods is respectively provided with
Have a collecting pipe, the one end of the collecting pipe far from the collecting hood is provided with conduit, the conduit far from the collecting pipe one
End is provided with wind turbine, and the one end of the wind turbine far from conduit is provided with collecting chamber, and spray equipment, institute are provided in the collecting chamber
It states the spray liquid in spray equipment and uses liquor potassic permanganate, activated charcoal strainer is provided in the collecting chamber.
By using above-mentioned technical proposal, fabric can pad fabric in resin working solution first when carrying out upper resin
In, the fabric after padding, which can then enter in baker, to be baked, and is then entered back into dryer and is dried
It is dry, it will produce certain formaldehyde gas when fabric is in by padder, baker, dryer；It is being padded at this time using setting
Machine, baker, three collecting hoods on dryer, while utilizing supravasal wind turbine dispatch formaldehyde gas, formaldehyde gas
Be fed in collecting chamber, when formaldehyde gas through collection indoor spray equipment when, formaldehyde gas can in spray liquid
Liquor potassic permanganate reacts, and the product for reacting later is the aqueous solution and carbon dioxide gas of potassium sulfate and manganese sulfate；
After having extra formaldehyde gas to omit away, formaldehyde out can will be omitted using indoor activated charcoal strainer is collected
Gas re-absorption falls, and ensures that only few or no formaldehyde gas gives off collecting chamber, finally can be realized to noniron finish
The formaldehyde of middle release is efficiently handled.
The further setting of the present invention is：Side of the collecting chamber far from the wind turbine is provided with evaporative crystallization room, institute
The temperature for stating evaporative crystallization room is 180-200 DEG C.
By using above-mentioned technical proposal, due to reacting when formaldehyde gas and the liquor potassic permanganate in spray liquid,
The product for reacting later is the aqueous solution of potassium sulfate and manganese sulfate, is passed into height when by the aqueous solution of potassium sulfate and manganese sulfate
Temperature evaporative crystallization room in after, the crystal with potassium sulfate and manganese sulfate can be precipitated in moisture evaporation, to potassium sulfate with
Manganese sulfate is recycled, the convenient spray liquid that potassium permanganate is made again；Potassium sulfate can be as the raw material of chemical fertilizer simultaneously
Use, manganese sulfate be also be agriculturally important micro first rope fertilizer, while being also the catalyst of induction biosynthesis chlorophyll.
The further setting of the present invention is：The side of the evaporative crystallization room far from the collecting chamber is provided with freezing chamber,
The indoor temperature of freezing is less than subzero 90 DEG C.
By using above-mentioned technical proposal, great amount of carbon dioxide gas is carried when being formed after in evaporative crystallization room
After vapor enters in freezing chamber, it is dry ice that carbon dioxide gas, which can be cured and form the carbon dioxide of solid, from
And realize the recycling to carbon dioxide gas, the discharge of carbon dioxide gas is reduced, the greenhouse effects in city are alleviated.
The further setting of the present invention is：The temperature of the baker is 170 DEG C, and the time baked is 60 seconds.
By using above-mentioned technical proposal, by the temperature setting of baker at 170 DEG C, the time control baked at 60 seconds,
Small is wanted to fabric strength loss so that baking in cross-linking process, readily satisfies the required higher flatness grade of textile
Number.
The further setting of the present invention is：Temperature in the dryer is 120-160 DEG C.
By using above-mentioned technical proposal, when material carries out drying and processing over there, too low or excessively high temperature can all influence
The quality of drying efficiency and finished product controls the temperature in dryer at 120-160 DEG C, so that the effect of fabric drying is more
It is good, the strength of fabric will not be influenced.
The further setting of the present invention is：It is provided with the first heat conducting pipe between the baker and the evaporative crystallization room.
By using above-mentioned technical proposal, using the first heat conducting pipe being arranged between baker and evaporative crystallization room,
Baker can will be dispersed into some temperature extra in air and pass to evaporative crystallization room by one heat conducting pipe, thus by baker
Waste heat use well, reach energy-saving and environment-friendly effect.
The further setting of the present invention is：It is provided with the second heat conducting pipe between the dryer and the evaporative crystallization room.
By using above-mentioned technical proposal, using the second heat conducting pipe being arranged between dryer and evaporative crystallization room,
The waste heat of dryer can be passed to evaporative crystallization room by two heat conducting pipes, to which the waste heat of dryer be used well,
Reach energy-saving and environment-friendly effect.
In conclusion the invention has the advantages that：Formaldehyde gas is collected using collecting chamber, wherein collecting
Indoor spray liquid can sponge most formaldehyde gas after reacting with formaldehyde gas, while utilize activated carbon mistake
The formaldehyde gas of omission can be carried out double absorption by strainer, achieve the effect that efficient process formaldehyde gas.
Description of the drawings
Fig. 1 is the process flow chart of the present invention；
Fig. 2 is that connection relation is shown between padder in the present invention, baker, dryer, collecting chamber, evaporative crystallization room, freezing chamber
It is intended to.
In figure：1, padder；2, baker；21, the first heat conducting pipe；3, dryer；31, the second heat conducting pipe；4, collecting hood；
5, collecting pipe；6, conduit；7, wind turbine；8, collecting chamber；81, spray equipment；82, activated charcoal strainer；9, evaporative crystallization room；10、
Freezing chamber.
Specific implementation mode
Below in conjunction with attached drawing, invention is further described in detail.
A kind of fabric resin ironing-free technology, referring to Fig.1, the ironing-free technology of fabric is as follows；
1, processing of singing is carried out to fabric with gassing frame；
2, desizing processing is carried out to fabric with desizing machine, it is desirable that desizing is clean, and desizing rate is 98% or more；
3, mercerization finish is carried out to fabric with mercerizing machine, it is desirable that mercerising is from point, and fabric PH is 7 or so；
4, fabric is put into the padder 1 with resin working solution, the active group and cellulosic molecule on molecular resin
Hydroxyl is combined into molecular bridge or covalent bond under certain condition, and macromolecular chain adjacent in fiber is interconnected, thus
The Relative sliding movement for reducing two molecule interchains, improves the recovery capacity of deformation, to improve the shrinkproof anti-of fabric
Wrinkle performance；
5, fabric is put into baker 2 and is baked, toasted using higher temperature, so that molecular resin is big with cellulose
It is fully condensed, is crosslinked between molecule, generate the anti-wrinkle effect mutually restrained, the wherein temperature in baker 2 is 170 DEG C, is baked
Time be 60 seconds；
6, fabric is put into dryer 3 and is dried, reduce fabric moisture, the wherein temperature in dryer 3 is 120-160
℃；
Referring to Fig.1, Fig. 2 is respectively and fixedly provided with collecting hood 4 in the upside of padder 1, baker 2, dryer 3, three collecting hoods 4
Upper end is welded with collecting pipe 5, and three one end of collecting pipe 5 far from collecting hood 4 are welded on a conduit 6；Conduit 6 is separate
One end of collecting pipe 5 has been bolted to connection wind turbine 7, and the one end of wind turbine 7 far from conduit 6 has been bolted to connection receipts
Collect room 8, wind turbine 7 enters the formaldehyde dispatch come out on padder 1, baker 2, dryer 3 in collecting chamber 8.
Spray equipment 81 is installed, spray equipment 81 includes multiple spray heads, the spray liquid in spray head in collecting chamber 8
It is reacted for liquor potassic permanganate when the air with formaldehyde passes through spray liquid：4KMnO4+6H2SO4+5HCHO=
5CO2 ↑+4MnSO4+11H2O+2K2SO4 generates solution and carbon dioxide gas with manganese sulfate and potassium sulfate；Wherein
It is further fixed on activated charcoal strainer 82 in collecting chamber 8, this kind of activated charcoal strainer 82 uses activated carbon material, when there is extra first
After aldehyde molecule is omitted away, activated charcoal strainer 82 can adsorb it, ensure only few or do not have formaldehyde gas
Give off collecting chamber 8.
Side of the collecting chamber 8 far from wind turbine 7 is fixed with evaporative crystallization room 9, and evaporative crystallization room 9 passes through pipeline with collecting chamber 8
Connection, the solution with manganese sulfate and potassium sulfate is after pipeline flows into evaporative crystallization room 9, heat temperature raising, moisture evaporation
The crystal with potassium sulfate and manganese sulfate is precipitated, the wherein temperature in evaporative crystallization room 9 is 180-200 DEG C；Simultaneously baker 2 with
The first heat conducting pipe 21 is provided between evaporative crystallization room 9, one end of the first heat conducting pipe 21 is connected in baker 2, the first heat conduction
The other end of pipe 21 is connected in evaporative crystallization room 9；The second heat conducting pipe 31 is additionally provided between dryer 3 and evaporative crystallization room 9,
One end of second heat conducting pipe 31 is connected in dryer 3, and the other end of the second heat conducting pipe 31 is connected in evaporative crystallization room 9.
Side of the evaporative crystallization room 9 far from collecting chamber 8 is fixed with freezing chamber 10, and freezing chamber 10 passes through with evaporative crystallization room 9
Pipeline is connected to, and the vapor with great amount of carbon dioxide gas is entered by pipeline in freezing chamber 10, and carbon dioxide gas is
It is dry ice that can be cured and to form the carbon dioxide of solid, to realize the recycling to carbon dioxide gas, reduces carbon dioxide
The greenhouse effects in city are alleviated in the discharge of gas；Temperature wherein in freezing chamber 10 is less than subzero 90 DEG C.
7, it is rewinded in 35 degrees Celsius of thermostatic chamber again after resin sizing package, the cloth cover temperature after rewinding is 40 DEG C；
8, it is 35 DEG C in temperature by fabric, is banked up 20 hours in the constant temperature and humidity room that humidity is 50%；
9, fabric is placed in soda ash solution, wherein the pH value of soda ash solution is 10, and the temperature of liquid is at 23 DEG C；
10, fabric is put into clear water and is washed, the temperature of clear water is at 70 DEG C；
11, fabric is passed into hot-rolling mill and carries out hot rolling, hot-rolled temperature is 105 DEG C；
12, fabric is put into preshrinking machine and carries out preshrunk.
Specific embodiment is only explanation of the invention, is not limitation of the present invention, those skilled in the art
The modification that not creative contribution can be made to the present embodiment as needed after reading this specification, but as long as in this hair
It is all protected by Patent Law in bright right.
Claims (7)
1. a kind of fabric resin ironing-free technology, include be followed successively by singe, desizing, mercerising, upper resin, rewind, bank up, alkali cleaning,
Washing, hot rolling, preshrunk technological process, it is characterised in that：Include to pad, bake, drying successively in the upper resin process,
Fabric is passed into padder successively（1）, baker（2）, dryer（3）It is interior, the padder（1）, the baker（2）, institute
State dryer（3）On be respectively provided with collecting hood（4）, three collecting hoods（4）Upper end be both provided with collecting pipe（5）, the receipts
Collector（5）Far from the collecting hood（4）One end be provided with conduit（6）, the conduit（6）Far from the collecting pipe（5）One
End is provided with wind turbine（7）, the wind turbine（7）Far from conduit（6）One end be provided with collecting chamber（8）, the collecting chamber（8）Inside set
It is equipped with spray equipment（81）, the spray equipment（81）Interior spray liquid uses liquor potassic permanganate, the collecting chamber（8）Inside set
It is equipped with activated charcoal strainer（82）.
2. a kind of fabric resin ironing-free technology according to claim 1, it is characterised in that：The collecting chamber（8）Far from institute
State wind turbine（7）Side be provided with evaporative crystallization room（9）, the evaporative crystallization room（9）Temperature be 180-200 DEG C.
3. a kind of fabric resin ironing-free technology according to claim 2, it is characterised in that：The evaporative crystallization room（9）Far
From the collecting chamber（8）Side be provided with freezing chamber（10）, the freezing chamber（10）Interior temperature is less than subzero 90 DEG C.
4. a kind of fabric resin ironing-free technology according to claim 3, it is characterised in that：The baker（2）Temperature
It it is 170 DEG C, the time baked is 60 seconds.
5. a kind of fabric resin ironing-free technology according to claim 4, it is characterised in that：The dryer（3）Interior temperature
Degree is 120-160 DEG C.
6. a kind of fabric resin ironing-free technology according to claim 5, it is characterised in that：The baker（2）With it is described
Evaporative crystallization room（9）Between be provided with the first heat conducting pipe（21）.
7. a kind of fabric resin ironing-free technology according to claim 6, it is characterised in that：The dryer（3）With it is described
Evaporative crystallization room（9）Between be provided with the second heat conducting pipe（31）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710031574.9A CN108330632A (en) | 2017-01-17 | 2017-01-17 | A kind of fabric resin ironing-free technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710031574.9A CN108330632A (en) | 2017-01-17 | 2017-01-17 | A kind of fabric resin ironing-free technology |
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| Publication Number | Publication Date |
|---|---|
| CN108330632A true CN108330632A (en) | 2018-07-27 |
Family
ID=62922751
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710031574.9A Pending CN108330632A (en) | 2017-01-17 | 2017-01-17 | A kind of fabric resin ironing-free technology |
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-
2017
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6016250A (en) * | 1984-06-08 | 1985-01-28 | Matsushita Electric Ind Co Ltd | Humidifier |
| JPH1147256A (en) * | 1997-08-04 | 1999-02-23 | Kawai Musical Instr Mfg Co Ltd | Deodorizing apparatus |
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