CN113338060A - Energy-saving short-process health-care functional dyeing method for home textile fabric - Google Patents
Energy-saving short-process health-care functional dyeing method for home textile fabric Download PDFInfo
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- CN113338060A CN113338060A CN202110900224.8A CN202110900224A CN113338060A CN 113338060 A CN113338060 A CN 113338060A CN 202110900224 A CN202110900224 A CN 202110900224A CN 113338060 A CN113338060 A CN 113338060A
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
- D06P1/38—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using reactive dyes
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- 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
- D06B17/00—Storing of textile materials in association with the treatment of the materials by liquids, gases or vapours
- D06B17/02—Storing of textile materials in association with the treatment of the materials by liquids, gases or vapours in superimposed, i.e. stack-packed, form; J-boxes
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- 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
- D06B7/00—Mercerising, e.g. lustring by mercerising
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
- D06P1/44—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
- D06P1/46—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders using compositions containing natural macromolecular substances or derivatives thereof
- D06P1/48—Derivatives of carbohydrates
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
- D06P1/44—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
- D06P1/64—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders using compositions containing low-molecular-weight organic compounds without sulfate or sulfonate groups
- D06P1/651—Compounds without nitrogen
- D06P1/65106—Oxygen-containing compounds
- D06P1/65118—Compounds containing hydroxyl groups
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P3/00—Special processes of dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form, classified according to the material treated
- D06P3/58—Material containing hydroxyl groups
- D06P3/60—Natural or regenerated cellulose
- D06P3/66—Natural or regenerated cellulose using reactive dyes
Abstract
The invention discloses an energy-saving short-flow health-care functional dyeing method of home textile fabric, which comprises the following steps: in the mercerizing step, the frequency of washing and removing alkali is reduced, and wet cropping is realized, so that water and energy are saved; cold pad batch dyeing: the wet cropping enters a dye liquor padder of a cold rolling pile, the dye liquor comprises reactive dye or a mixture of the reactive dye and tea polyphenol, monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin, citronella oil or menthol and an ethanol water solution, salt and an alkaline agent are not required to be added into the dye liquor, and the dyeing and the after finishing are carried out synchronously in one bath through the cold rolling pile process, so that the dyeing and the finishing with the mosquito-repelling, cool-feeling and antibacterial composite functions are completed in one step, the processing flow is shortened, and the energy is saved.
Description
Technical Field
The invention relates to the technical field of textile fabric processing, in particular to an energy-saving short-process health-care function dyeing method for home textile fabric.
Background
The printing and dyeing processing of the home textile fabric currently comprises pretreatment (including desizing, boiling, bleaching and mercerizing), dyeing and after-finishing (including functional finishing), and the traditional printing and dyeing processing currently has the disadvantages of long flow, high energy consumption and water consumption, more discharged wastewater and influence on the survival of printing and dyeing processing enterprises. With the improvement of the requirements of environmental protection and energy conservation, the method has a limited standard for the discharge amount of printing and dyeing wastewater and indexes of national places, and the short-flow energy conservation and emission reduction of printing and dyeing processing is a development direction.
The high-end home textile fabric is generally a pure cotton fabric, the dyeing effect and luster of the fabric can be improved by the pre-treatment mercerization of the printing and dyeing processing of the pure cotton fabric, the mercerization uses concentrated alkali, a multi-lattice (6-lattice) water washing tank is required to remove alkali after the mercerization is finished, then the acid neutralization is carried out, and finally the drying, water consumption and energy consumption are realized. The dyeing of the pure cotton fabric generally adopts reactive dyes, the reactive dyes need to be subjected to covalent reaction with cotton cellulose in an alkaline environment for fixation, cold pad-batch dyeing is energy-saving, an alkaline agent needs to be added into a padding dye solution, and the problem that the dyes are easy to hydrolyze exists. After finishing such as antibiosis, mosquito repelling, deodorization and the like is generally carried out after dyeing, finishing equipment is added, and the flow steps of printing and dyeing processing are added.
Disclosure of Invention
The invention aims to provide an energy-saving short-flow health-care function dyeing method for home textile fabric, which solves one or more of the problems in the prior art.
The invention provides an energy-saving short-flow health-care functional dyeing method of home textile fabric, which comprises the following steps:
mercerizing: the alkali removing process in the mercerizing step comprises 1 alkali removing box, after the mercerizing step is finished, the pH value of wet cropping is 8-10, and the liquid carrying rate of the wet cropping is 60-70%;
cold pad batch dyeing: and the wet cropping enters a dye liquor padder of a cold rolling stack, and the dye liquor comprises 5-50 g/L of reactive dye or a mixture of the reactive dye and tea polyphenol, 20-60g/L of monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin, 0.1-5g/L of citronella oil or menthol and ethanol water solution.
In some embodiments, a clip mercerizer is used in the mercerizing step, the mercerizing step is flat-width cloth feeding → first padding alkali solution → cloth stretching roller → second padding alkali solution → cloth clip chain expanding → diluted alkali leaching → alkali removing box, the concentration of the padding alkali solution is 220-240g/L, the concentration of the diluted alkali is 5-10%, and the length of the cloth clip chain is 20-30 m.
In some embodiments, the reactive dyes include Norwegian clone blue FN-R, Norwegian clone red FN-2BL, and Norwegian clone yellow FN-2R.
In some embodiments, in the cold pad-batch dyeing step, the dye liquor is emulsified by a high shear emulsifier, the rotation speed of the high shear emulsifier is 1000r/min, and the emulsification time is 5 min.
In some embodiments, the volume ratio of water to ethanol in the aqueous ethanol solution is from 9:1 to 1: 1.
In some embodiments, in the cold pad-batch dyeing step, the padder has a vehicle speed of 60-70 m/min, a mangle rolling rate of 65-85%, and a room-temperature sealing stacking time of 16-24 h.
In some embodiments, the mercerization step further comprises an enzyme desizing step and a p-theasaponin scouring and bleaching treatment step.
In some embodiments, in the enzyme desizing step, high-concentration amylase with the concentration of 5g/L is used, the treatment temperature is 40-60 ℃, and the treatment time is 12-24 h; in the boiling and bleaching treatment step of the aloha tea saponin, aloha tea saponin with the concentration of 8g/L is used, the treatment temperature is 80-90 ℃, and the treatment time is 50-60 min.
In some embodiments, the mass ratio of the reactive dye to the tea polyphenol in the mixture of reactive dye and tea polyphenol is 1:1 to 9: 1.
The invention has the beneficial effects that:
1. according to the invention, the number of alkali removal and water washing after mercerization is reduced, and the mercerization is carried out in the alkali removal box with 1 grid, acid washing neutralization and drying are removed, so that the cold pad-batch reactive dye liquor padder is used, the traditional mercerization process is reduced, water and energy are saved, and the problems of energy consumption and water consumption are solved;
2. the mercerized fabric is alkaline, so that an alkaline agent is not required to be added into the dyeing solution, and the problems that the utilization rate and the color fastness are influenced due to the hydrolysis of the dye in the dyeing solution in an alkaline environment are solved;
3. besides the reactive dye or tea polyphenol, monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin, citronella oil or menthol, ethanol and water are added into the dye liquor, so that the using amount of water in a rolling groove is reduced, the concentration of the reactive dye is equivalently increased, the dyed color depth value is favorably improved, the problem of water consumption in dyeing is solved, and the dye is saved;
4. the monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin similar colorless active dye is anchored on the cotton fabric through covalent bond;
in 16-24 hours of the sealed stacking, the active dye, the monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin and the cotton fiber complete covalent reaction and fixation, the citronella oil or menthol and tea polyphenol dissolved in the ethanol enter the cavity of the cyclodextrin in the stacking process of the sealed stacking, and the slow release effect is achieved;
and the cold pad batch finishes dyeing and mosquito-repelling cool-feeling antibacterial composite functional finishing, and the dyeing and the after-finishing are carried out in one bath synchronously, so that the processing flow is shortened, and the energy is saved.
Detailed Description
The present invention will be further described with reference to the following examples. The following examples are only for illustrating the performance of the present invention more clearly and are not limited to the following examples.
Example 1
Enzyme desizing: in the step of enzyme desizing, high-concentration amylase with the concentration of 5g/L is used, the treatment temperature is 40 ℃, and the treatment time is 24 hours;
boiling and bleaching the alopeia saponin: in the boiling and bleaching treatment step of the aloha tea saponin, aloha tea saponin with the concentration of 8g/L is used, the treatment temperature is 80 ℃, and the treatment time is 60 min.
Mercerizing: the mercerizing step comprises the steps of open width cloth feeding → first padding alkali liquor → a cloth stretching roller → second padding alkali liquor → cloth clamp chain expanding → leaching dilute alkali → 1 lattice alkali removal box, wherein the concentration of the padding alkali liquor is 220g/L, and the concentration of the dilute alkali is 5%.
After the mercerization step is finished, the pH value of the wet cropping is 9.5, and the liquid carrying rate is 60%.
The mercerization process reduces the number of alkali removal and water washing times after mercerization, removes acid washing neutralization and drying, and enters a cold-rolling pile reactive dye liquor padder only when the number of alkali removal boxes is reduced to 1, so that the traditional mercerization process is reduced, water and energy are saved, and the problems of energy consumption and water consumption are solved.
Cold pad batch dyeing:
the cold pad-batch dyeing process comprises the steps of enabling the wet cropping cloth to enter a dye solution padder of a cold pad-batch, enabling the dye solution to comprise a reactive dye with the concentration of 10 g/L, monochlorotriazine-vinyl sulfone double-active group-beta-cyclodextrin with the concentration of 40g/L, citronella oil with the concentration of 1g/L and an ethanol water solution (V water: V ethanol =6: 1), enabling the reactive dye to comprise Novak clone blue FN-R, Novak clone red FN-2BL and Novak clone yellow FN-2R, and emulsifying the dye solution through a high-shear emulsifying machine, wherein the rotating speed of the high-shear emulsifying machine is 1000R/min, and the emulsifying time is 5 min;
the dyeing equipment adopts a KUSTER uniform padder, the speed of the padder is 60 m/min, the mangle liquor rate is 65%, and the room-temperature sealing stacking time is 24 h.
In the mercerizing process, the mercerized fabric is alkaline, so that an alkaline agent is not required to be added into a dyeing solution, and the problems that the dye in the dyeing solution is hydrolyzed in an alkaline environment to influence the utilization rate and the color fastness are solved.
Besides the reactive dye, monochlorotriazine-vinyl sulfone double-active group-beta-cyclodextrin, citronella oil, ethanol and water are added into the dye liquor, so that the use amount of water in a rolling tank is reduced, the concentration of the reactive dye is equivalently increased, the dyed color depth value is favorably improved, the problem of water consumption in dyeing is solved, and the dye is saved; the monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin similar colorless active dye is anchored on the cotton fabric through covalent bond; in the sealed stacking for 20 hours, the covalent reaction and fixation of the reactive dye, the monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin and the cotton fiber are completed, the citronella oil dissolved in the ethanol is dissolved, and a cavity of the cyclodextrin is also added in the sealed stacking; and the cold pad batch finishes dyeing and mosquito-repelling cool-feeling antibacterial composite functional finishing, and dyeing and after-finishing are carried out synchronously, so that the processing flow is shortened, and the energy is saved.
The mercerizing step selects a mercerizing machine with a flat width, a caustic soda solution padding machine, a cloth stretching roller, a cloth clip chain type expanding device, a leaching alkali device, a dealkalizing steam box and the like.
The mercerizing machine adopts a vertical three-roller open width padding machine, two padding and two rolling are carried out, and the number of the padding and the rolling is two. A plurality of guide rollers are arranged in the padding tank to increase the dipping time of the fabric in the alkali liquor, which can generally reach about 20 s. The soaking and rolling tank is provided with an interlayer which can be filled with cold water to cool the alkali liquor in the tank. A communicating pipe is arranged between the two leaching tanks so as to facilitate the flow of alkali liquor.
The pressure of the first soaking and rolling groove is smaller, and the first soaking and rolling groove can be pressurized by a lever, so that the fabric is provided with more alkali liquor, and the action of the alkali liquor and the cellulose is facilitated.
The pressure of the second soaking and rolling tank is high, and an oil pump can be used for pressurizing, so that the amount of alkali liquor carried by the fabric is low, the rolling residual rate is less than 65%, the washing and the alkali removal are convenient, and the alkali consumption is reduced.
In order to prolong the alkali carrying time of the fabric, meet the requirement of full penetration and reaction of alkali to the fabric and simultaneously prevent the fabric from shrinking after swelling, more than ten iron hollow cloth stretching rollers which are alternately arranged up and down are arranged above the frame between the two padding tanks, and the diameter is 460-500 mm. Generally, the operation is passive, and the operation is active.
To prevent the fabric from shrinking, the wrap angle surface of the fabric along the cloth stretching roller should be larger, and the linear speed of the back groove should be larger than that of the front groove. Thus, the warp direction of the fabric has certain tension to prevent shrinkage; and the weft direction utilizes the friction resistance to prevent shrinkage.
The clip expanding device is composed of two annular clip chains with the length of about 20-30m, the clip chains are placed on the two annular tracks, the distance can be adjusted through a screw rod, clips are fully distributed on the clip chains, the clip edges are gripped to play a role in expanding, and the clip discs at the two ends respectively play a role in clip loading and clip unloading of the fabric.
And (4) after the fabric is subjected to amplitude expanding operation 1/3 on the clip chain, leaching and removing alkali by a leaching and liquid-absorbing device. The leaching device sprays hot water or dilute alkali on the whole width of the fabric from the upper part of the fabric, and then the hot water or dilute alkali is sucked by a pipette which is tightly attached to the lower part of the fabric and is connected with a vacuum pump, and the surface of the pipette is full of small holes.
The method is to adopt vacuum liquid absorption to strengthen the liquid exchange in the fabric when the fabric is in a stretching state. And the weak alkali solution sucked by the pipette is sequentially discharged into each weak alkali tank below the machine, and then the weak alkali solution in the weak alkali tank and the weak alkali solution from the dealkalizing steam box are respectively conveyed to the leaching device by each pump according to the principle of gradual countercurrent leaching.
And finally, in order to further wash off the caustic soda on the fabric, after the fabric is subjected to tenter rinsing, the fabric enters an alkali removal box with high alkali washing efficiency, and the alkali removal box is only set to be 1 lattice. The alkali removing box is a stainless steel closed box, and a box cover can be hung so as to facilitate cloth penetration or fault treatment; the upper and lower parts in the box are respectively provided with an iron cloth guide roller row, the upper row is active, and the lower row is passive; water sealing ports are arranged at the inlet and the outlet to prevent steam in the box from escaping; the bottom of the box is filled with water to wash off alkali, the bottom of the box is inclined, so that the alkali liquor can flow backwards from the back of the box against the direction of the fabric, and a direct steam pipe is arranged between the fabric layers to spray steam to the fabric, so that part of the steam is condensed into water on the fabric and permeates into the fabric, thereby playing the roles of diluting the alkali liquor and raising the temperature.
Example 2
Enzyme desizing: in the step of enzyme desizing, high-concentration amylase with the concentration of 5g/L is used, the treatment temperature is 60 ℃, and the treatment time is 12 hours;
boiling and bleaching the alopeia saponin: in the boiling and bleaching treatment step of the tea saponin, the tea saponin with the concentration of 8g/L is used, the treatment temperature is 90 ℃, and the treatment time is 50 min;
mercerizing: the mercerizing step comprises the steps of open width cloth feeding → first padding alkali liquor → a cloth stretching roller → second padding alkali liquor → cloth clamp chain expanding → leaching dilute alkali → 1 lattice alkali removal box, wherein the concentration of the padding alkali liquor is 230g/L, and the concentration of the dilute alkali is 8%.
After the mercerization step is finished, the pH value of the wet cropping is 10, and the liquid carrying rate is 70%.
The mercerization process reduces the number of alkali removal and water washing times after mercerization, removes acid washing neutralization and drying, and enters a cold-rolling pile reactive dye liquor padder only when the number of alkali removal boxes is reduced to 1, so that the traditional mercerization process is reduced, water and energy are saved, and the problems of energy consumption and water consumption are solved.
Cold pad batch dyeing:
the cold pad-batch dyeing process comprises the step of enabling the wet cropping cloth to enter a dye solution padder of a cold pad-batch, wherein the dye solution comprises a reactive dye with the concentration of 30g/L, a tea polyphenol dye with the concentration of 20g/L, monochlorotriazine-vinyl sulfone double-active group-beta-cyclodextrin with the concentration of 40g/L, menthol with the concentration of 2g/L, an ethanol water solution and an ethanol water solution (V water: V ethanol =5: 1), wherein the reactive dye comprises Norwegian clone blue FN-R, Norwegian clone red FN-2BL and Norwegian clone yellow FN-2R, a dyeing device selects KUSTER (KUSTER uniform padder), the speed of the padder is 65m/min, the mangle rate is 85%, and the room-temperature sealing stacking time is 20 h.
In the mercerizing process, the mercerized fabric is alkaline, so that an alkaline agent is not required to be added into a dyeing solution, and the problems that the dye in the dyeing solution is hydrolyzed in an alkaline environment to influence the utilization rate and the color fastness are solved.
Besides the reactive dye and the tea polyphenol dye, monochlorotriazine-vinyl sulfone double-active group-beta-cyclodextrin, citronella oil, ethanol and water are added into the dye liquor, so that the using amount of water in a mangle is reduced, the concentration of the dye is equivalently increased, the dyeing depth value is favorably improved, the problem of water consumption in dyeing is solved, and the dye is saved; the monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin similar colorless active dye is anchored on the cotton fabric through covalent bond; in 24 hours of the sealed stacking, the active dye, the monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin and the cotton fiber complete covalent reaction and fixation, and the menthol and the tea polyphenol dissolved in the ethanol enter a cavity of the cyclodextrin in the sealed stacking; and the cold pad batch finishes dyeing and mosquito-repelling cool-feeling antibacterial composite functional finishing, and dyeing and after-finishing are carried out synchronously, so that the processing flow is shortened, and the energy is saved.
The fabrics obtained in example 1 and example 2 were subjected to color fastness tests according to GB/T3921-:
the test results are given in the following table:
the fabrics obtained by the processes of the embodiments 1 and 2 meet the requirements of national standards, and due to the improvement of the processes, the traditional mercerization process is reduced, water and energy are saved, and the problems of energy consumption and water consumption are solved.
The mosquito repelling rate of example 1 was tested; the example 2 was tested for cool feeling, bacteriostatic rate and mosquito repellent rate, with the following test standards:
the cooling effect Qmax is measured according to GB/T35263-2017 detection and evaluation of cooling performance at the moment of textile contact, and the larger the value is, the more heat is taken away, and the more obvious the cooling effect is.
The bacteriostasis rate is evaluated according to GB/T20944.3-2008 'antibacterial performance of textiles' third part: measured by the oscillatory method.
The mosquito repelling rate is measured according to the GB/T30126-2013 mosquito-proof textile test standard.
The test results are given in the following table:
item | Example 1 | Example 2 |
Mosquito repelling rate (%) | 76.8 | 70.5 |
Bacteriostasis rate (Staphylococcus aureus (%) | 99.8 | |
Cool feeling Qmax | 0.21 |
In the embodiments 1 and 2, the cold pad batch is adopted to finish the dyeing and mosquito-repellent cool antibacterial composite functional finishing, the dyeing and the after-finishing are carried out synchronously, the processing flow is shortened, and the energy is saved. In example 1, the citronella oil is added to realize the compound function of repelling mosquitoes, and in example 2, the menthol and the tea polyphenol are added to realize the multiple compound functions of repelling mosquitoes, inhibiting bacteria, cooling and the like.
The above description is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, various changes and modifications can be made without departing from the inventive concept of the present invention, and these should also be construed as being within the scope of the present invention.
Claims (9)
1. An energy-saving short-flow health-care functional dyeing method for home textile fabric is characterized by comprising the following steps:
mercerizing: the alkali removing process in the mercerizing step comprises 1 alkali removing box, after the mercerizing step is finished, the pH value of wet cropping is 8-10, and the liquid carrying rate of the wet cropping is 60-70%;
cold pad batch dyeing: and the wet cropping enters a dye liquor padder of a cold rolling stack, and the dye liquor comprises 5-50 g/L of reactive dye or a mixture of the reactive dye and tea polyphenol, 20-60g/L of monochlorotriazine-vinyl sulfone double active group-beta-cyclodextrin, 0.1-5g/L of citronella oil or menthol and ethanol water solution.
2. The energy-saving short-process health-care functional dyeing method of home textile fabric according to claim 1, characterized in that a cloth-clip mercerizer is used in the mercerizing step, the mercerizing step is flat cloth feeding → first padding alkali solution → a cloth roller → second padding alkali solution → cloth clip chain widening → leaching dilute alkali → an alkali removal box, the concentration of the padding alkali solution is 220-240g/L, the concentration of the dilute alkali is 5-10%, and the length of the cloth clip chain is 20-30 m.
3. The energy-saving short-process health-care functional dyeing method of home textile fabric according to claim 1, characterized in that the reactive dyes comprise Norwegian clone blue FN-R, Norwegian clone red FN-2BL and Norwegian clone yellow FN-2R.
4. The energy-saving short-process health-care functional dyeing method of home textile fabric according to claim 1, characterized in that in the cold pad-batch dyeing step, the dye liquor is emulsified by a high shear emulsifying machine, the rotating speed of the high shear emulsifying machine is 1000r/min, and the emulsifying time is 5 min.
5. The energy-saving short-process health-care functional dyeing method of home textile fabric according to claim 1, characterized in that the volume ratio of water to ethanol in the ethanol aqueous solution is 9:1-1: 1.
6. The energy-saving short-flow health-care functional dyeing method of home textile fabric according to claim 1, characterized in that in the cold pad-batch dyeing step, the speed of a padder is 60-70 m/min, the mangle expression is 65-85%, and the room-temperature sealing stacking time is 16-24 h.
7. The energy-saving short-process health-care functional dyeing method of home textile fabric according to any one of claims 1 to 6, characterized in that the mercerization step further comprises an enzyme desizing step and a p-theasaponin scouring and bleaching treatment step.
8. The energy-saving short-process health-care functional dyeing method of home textile fabric according to claim 7, characterized in that in the enzyme desizing step, high-concentration amylase with the concentration of 5g/L is used, the treatment temperature is 40-60 ℃, and the treatment time is 12-24 h; in the boiling and bleaching treatment step of the aloha tea saponin, aloha tea saponin with the concentration of 8g/L is used, the treatment temperature is 80-90 ℃, and the treatment time is 50-60 min.
9. The energy-saving short-process health-care functional dyeing method of home textile fabric according to claim 1, characterized in that in the mixture of the reactive dye and the tea polyphenol, the mass ratio of the reactive dye to the tea polyphenol is 1:1-9: 1.
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CN112813708A (en) * | 2021-02-20 | 2021-05-18 | 江南大学 | Salt-free less-water circulating dyeing method for cellulose textile reactive dye |
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CN115928438B (en) * | 2022-11-21 | 2023-12-22 | 江苏南星家纺有限公司 | Hypnotizing sweat stain-preventing headrest fabric and preparation method thereof |
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