阅读说明：本技术 一种平整无折痕冷轧堆染色护肤宽幅天丝面料生产工艺 (Production process of smooth crease-free cold pad-batch dyeing skin-care wide tencel fabric ) 是由 欧卫国 袁志成 葛忠平 陈刚 杨莹莹 蔡云芸 杨小玲 薛鹏飞 马良益 汤蕾 张敏 于 2021-09-10 设计创作，主要内容包括：本发明公开了一种平整无折痕冷轧堆染色护肤宽幅天丝面料生产工艺,主要生产工艺流程：包括翻缝、一正一反烧毛、轧淀粉酶堆置退浆、半丝光、冷轧堆染色、无甲醛防缩与玻尿酸整理剂同浴整理、机械预缩、检验包装。产品平整无折痕,前后色差≧4级,左中右色差≧4-5级的内在质量达到GB/T22797—2009《床单》和GB/T22796—2009《被、被套》优等品指标。染整生产技术达到国内同类产品领先水平。(The invention discloses a production process of a flat crease-free cold pad-batch dyed skin-care wide tencel fabric, which mainly comprises the following production process flows: comprises the steps of seam turning, positive and negative singeing, amylase padding and stacking desizing, semi-mercerizing, cold pad-stacking dyeing, non-formaldehyde shrink-proofing and hyaluronic acid finishing agent one-bath finishing, mechanical preshrinking, inspection and packaging. The product is flat and has no crease, the front-back chromatic aberration is not less than 4, and the internal quality of the left-middle-right chromatic aberration not less than 4-5 reaches the excellent indexes of GB/T22797-2009 bed sheet and GB/T22796-2009 quilt and quilt cover. The dyeing and finishing production technology reaches the leading level of domestic similar products.)

1. A production process of a smooth crease-free cold pad-batch dyeing skin-care wide tencel fabric is characterized by comprising the following steps of: the main production process flow is as follows: seam turning → one positive and one negative singeing → rolled amylase stacking desizing → washing → drying → half mercerizing → cold pad-batch dyeing → non-formaldehyde shrink-proof and hyaluronic acid finishing agent one-bath finishing → mechanical preshrinking → inspection and packaging; the method comprises the following specific operations:

in the turning-over sewing, a circular sewing machine is used, and the thread for sewing the head is 30^s6, the stitch density is 28-32 needles/10 cm, the vertical seams on the two sides of the selvedge are 4-5 cm, and the tail is 3-5 cm;

in the half mercerizing, the half mercerizing is carried out on a full straight roll mercerizing machine containing 98 pairs, and the main process flow is as follows: cloth feeding → alkali leaching in the concentrated alkali tank → heavy padder No. 1 → alkali removal in the first alkali removal tank → heavy padder No. 2 → alkali removal in the second alkali removal tank → heavy padder No. 3 → drying → cloth dropping; wherein:

the concentrated alkali tank area of the full straight roller mercerizing machine is provided with 40 pairs of straight rollers, 1 pair of straight rollers consists of an upper rubber roller and a lower metal straight roller, wherein the No. 2 and No. 4 rubber straight rollers are spreading rollers, and the concentration of caustic soda in the concentrated alkali tank area is 90-100 g/L;

after the concentrated alkali solution is discharged from the concentrated alkali tank area, the concentrated alkali solution is subjected to expanding by an expanding roller and then enters a No. 1 heavy padder for mangling, the liquid carrying rate is 55 percent, and then the concentrated alkali solution enters a first dealkalizing tank area with 20 pairs of straight rollers, wherein No. 50, No. 52 and No. 54 rubber straight rollers are expanding rollers; after the alkali-removing groove area is discharged, the alkali-removing groove area is subjected to expanding by an expanding roller and then enters a No. 2 heavy padder for mangling, the liquid carrying rate is 55 percent, and the alkali-removing groove area enters a second alkali-removing groove area with 38 pairs of straight rollers, wherein No. 64 and No. 67 rubber straight rollers are expanding rollers;

5 and 10 groups of spray pumps are respectively installed in the first dealkalizing tank area and the second dealkalizing tank area, wherein 5 groups of spray pumps in the first dealkalizing tank area are respectively connected with 4 spray pipes, and the temperature of the spray liquid in the first dealkalizing tank area is 70-75 ℃; the second dealkalization trough area has 9 groups of spray pumps each connected with 4 spray pipes respectively, and the last 1 group of spray pumps connected with 2 spray pipes, the temperature of the spray liquid in the second dealkalization trough area is 50-55 ℃, clean water is sprayed to the straight roll spray pipes corresponding to 98 th and 97 th, and light alkali liquid is sprayed to the other spray pipes; the dilute alkali liquor flows back to the first dealkalizing tank zone from the second dealkalizing tank zone, the concentration of the dilute alkali sprayed by the straight roller spray pipes corresponding to 42 th and 41 th straight roller spray pipes reaches 40-45 g/L, and the dilute alkali liquor is recovered for later use;

after the alkali liquor is discharged from the second dealkalizing tank area, the alkali liquor enters two rows of 20 drying cylinders for drying through No. 3 heavy padder mangle, wherein the liquor carrying rate of the No. 3 heavy padder mangle is 55 percent, and the two drying cylinders at the bottom of the second row are cooling cylinders and are used for reducing the temperature of the cloth cover;

in the cropping, the pH value of the cropping is 7-8, and the moisture content is 3% -4%.

2. The production process of the flat crease-free cold pad-batch dyeing skin-care wide tencel fabric as claimed in claim 1, is characterized in that: in the cold pad-batch dyeing, the dyeing solution for dyeing grey blue consists of the following components: 1.45g/L of active red B-2BF, 2.26g/L of elegans yellow 4RFN and 6.27g/L of elegans navy blue BF-2 GF; alkali liquor composition: 30g/L of caustic soda and 12.5g/L of Alini LDR cold-stack fixation alkali; dye liquor and alkali liquor 4: 1, and when the automobile is started, adding 0.15g/L of dye reactive red B-2BF, 0.23g/L of jacetin yellow 4RFN and 1.28g/L of jacetin dark blue BF-2 GFN into a 100L rolling tank.

3. The production process of the flat crease-free cold pad-batch dyeing skin-care wide tencel fabric as claimed in claim 1, is characterized in that: in the cold pad-batch dyeing, the dyeing solution for dyeing water bath green comprises the following components: norwegian clone red ER-2 BL0.54g/L, Norwegian clone yellow ER-2R 3.2g/L, Norwegian clone blue C-5X 6.2 g/L; alkali liquor composition: 30g/L of caustic soda and 12.5g/L of Alini LDR cold-stack fixation alkali; dye liquor and alkali liquor 4: 1 volume ratio, and adding 0.06g/L of dye Nowegian clone red ER-2 BL, 0.32g/L of Nowegian clone yellow ER-2R and 1.2g/L of Nowegian clone blue C-5X in a 100L rolling tank when the automobile is started.

4. The production process of the flat crease-free cold pad-batch dyeing skin-care wide tencel fabric as claimed in claim 1, is characterized in that: in the cold pad-batch dyeing, the dyeing equipment comprises: the KUSTER uniform padder adjusts the left, middle and right pressures of the padder to be 0.30, 0.25 and 0.30MPa and the tension of a tension bracket to be 0.02MPa, when dyeing is started, the padder is started at the speed of 10m/min, pure cotton is guided for about 40m, the speed is quickly increased to be more than 40m/min, after the condition that no abnormity exists in the rolling of the cloth cover and the center, the padder speed is increased to be as fast as possible to be a normal constant speed of 75m/min, and the pure cotton is guided for about 10m and then wide tencel woven fabric is positively distributed; the mangle rolling rate is controlled to be 50-55 percent; in order to prevent the generation of seam marks, a plastic film with the length of 2.9m, the width of 0.5m and 15-20 threads is added at the circular seam type seam; after the front cloth of the wide tencel woven fabric is completely dyed, continuously feeding pure cotton wrapping cloth of about 20m, wrapping a plastic film outside the whole large-roll cloth, and moving to a stacking area for stacking at room temperature for 20-24 hours; when stacking, the cloth roll must keep rotating at a constant speed of 8-10 r/min;

5. the production process of the flat crease-free cold pad-batch dyeing skin-care wide tencel fabric as claimed in claim 1, is characterized in that: the soaping process after the cold pad-batch dyeing comprises the following steps: the method comprises the following steps of cloth feeding → first, second and third open washing, wherein the temperatures are 40 ℃, 50 ℃, 60 ℃ → fourth and fifth soaping, the temperature of the acidic low-temperature soaping agent LTS-1002 g/L, 90-95 ℃) → sixth and seventh hot water washing, the temperatures are 80 ℃, 70 ℃ → eighth neutralization, an glacial acetic acid adding system is automatically controlled, the pH is controlled to be 5-6, the temperature is 50 ℃ → ninth normal temperature water washing → tenth cold water washing in flowing manner → two groups of cylinders are dried, and the two lowermost drying cylinders in the second row are cooling cylinders and are used for reducing the temperature of a cloth cover → cloth falling.

6. The production process of the flat crease-free cold pad-batch dyeing skin-care wide tencel fabric as claimed in claim 1, is characterized in that: when the formaldehyde-free shrink-proof finishing agent and the hyaluronic acid finishing agent are finished in one bath, the working solution comprises the following components:

7. the production process of the flat crease-free cold pad-batch dyeing skin-care wide tencel fabric as claimed in claim 1, is characterized in that: the aldehyde-free low-temperature shrink-proof crease-resistant finishing agent KNITTEX FFRC is a pre-catalyzed aqueous solution of modified dimethylol dihydroxy ethylene urea containing functional magnesium salt.

8. The production process of the flat crease-free cold pad-batch dyeing skin-care wide tencel fabric as claimed in claim 1, is characterized in that: when the formaldehyde-free shrink-proof and hyaluronic acid finishing agent is finished in one bath, the fabric is fed in an open width mode, the formaldehyde-free shrink-proof and hyaluronic acid finishing agent is rolled in two times, the liquid carrying rate is 70% -75%, overfeeding is 2% -4%, needle plates are arranged, ten grids are baked by hot air, the temperature of the first grid to the second grid is 140 ℃, the temperature of the third grid to the fourth grid is 160 ℃, the temperature of the fifth grid to the ten grids is 165-170 ℃, the fabric is cooled and laid by two cylinders, and the vehicle speed is 45 m/min.

Technical Field

The invention relates to a production process of a flat crease-free cold pad-batch dyed skin-care wide tencel fabric, in particular to a dyeing and finishing production technology of a flat crease-free full-straight-roller mercerizing machine half-mercerizing, front-back chromatic aberration not less than 4 grade, left-middle-right chromatic aberration not less than 4-5 grade cold pad-batch dyeing, formaldehyde-free shrink prevention and hyaluronic acid finishing agent one-bath finishing of a wide tencel woven fabric.

Background

In the existing cold pad-batch dyeing, cloth guiding and wrapping at two ends of a fabric are respectively about 20 to 10 meters of polyester cotton cloth, and the innermost dozens of meters of the fabric of one cloth roll can have transition colors of dozens of meters because the dye concentration of a dye tank is not reached to an equilibrium point when the fabric is started initially. Meanwhile, the fabric which is originally rolled and is dozens of meters in length often has crease due to the adjustment of the rolling tension, and crease color patterns can be formed after color fixation. Because the fixing process is an exothermic reaction, multilayer water spots are easily formed on the fabric of which the outermost ring of the cloth roll is contacted with the plastic film. The fabric has color difference between the head and the tail and the middle after cold pad-batch dyeing. The head and tail fabrics with the color difference less than 4 levels can only be treated as off-grade products. The current fabric circular seam type sewing thread is 21^SAnd 6, the sewing thread is thick, the circular seam type seam head is large, and joint marks are easy to generate. The tension force during rolling is generally larger, meanwhile, the warp direction in the color fixing and stacking process is slowly contracted, the extrusion to the seam head is larger, the seam head is easy to generate the seam print, in a serious case, a seam head generates several circles of seam prints, and the fabric with the obvious seam print can only be treated as an off-grade product.

The tencel fabric is easy to generate defects such as dead crease, scratch, white spots and the like in dyeing and finishing processing. The production method of the tencel cotton-linen blended wide-width dyed woven fabric (CN107904923A) is characterized in that when semi-mercerizing is carried out on a straight-roll mercerizing machine consisting of a conventional straight-roll alkali-soaking area, a straight-roll alkali-removing area, a plain washer and the like, and when the woven fabric leaves the straight-roll area and enters the plain washer, as the vertical and back parallelism of a cloth guide roll has certain deviation, the weft direction shrinks, and the cloth cover generates mercerized wrinkles which are difficult to remove and defects of large weft direction shrinkage rate of the woven fabric. The production method of the tencel type wide woven fabric with high pilling resistance (CN109750530A) does not carry out semi-mercerization, and irregular dead folds, scratches and other defects are randomly generated on the cloth surface in the cold pad-batch dyeing process.

Disclosure of Invention

The purpose of the invention is as follows: in order to solve the defects of the prior art, the invention provides a cold pad-batch dyeing process technology for the flat crease-free wide tencel woven fabric, wherein the product performance of the cold pad-batch dyeing process technology reaches the quality indexes of the superior products of GB/T22797-2009 bed sheet and GB/T22796-2009 quilt and quilt cover.

The technical scheme is as follows: the flat crease-free wide skin-care tencel woven fabric is flat and crease-free, the front-back color difference is not less than 4 grade, the left-middle-right color difference is not less than 4-5 grade, the soaping resistance fastness is not less than 4 grade, the wet friction resistance fastness is not less than 3-4 grade, the pilling performance is not less than 4 grade, the breaking strength is not less than 280N, and the washing size change rate is-3.0% to + 0.5%.

The specification of the woven fabric grey cloth of the wide tencel (A100 type) is one of the following two types: the first had a width of 106 inches and a yarn count of 60^s×60^sA density of 200X 100 roots/inch; the second had a width of 106 inches and a yarn count of 50^s×50^sThe density was 170X 90 roots/inch.

A cold pad-batch dyeing process for a flat crease-free wide tencel woven fabric comprises the following main production process flows: seam turning → one positive reverse singeing → rolled amylase stacking desizing → water washing → drying → concentrated alkali treatment → cold pad batch dyeing → non-formaldehyde shrink-proof and hyaluronic acid finishing agent one-bath finishing → mechanical preshrinking → inspection and packaging;

when turning over the seam, a circular seam type sewing machine is used, and the thread for sewing the head is 30^sAnd 6, the stitch density is 28-32 needles/10 cm, the vertical seams on the two sides of the selvedge are 4-5 cm, and the tail is 3-5 cm.

Half mercerizing is carried out on a 98-pair full-straight-roller mercerizing machine, and the main process flow is as follows: cloth feeding → caustic soda bath in the concentrated caustic soda tank area → heavy padder No. 1 → dealkalization in the first dealkalization tank area → heavy padder No. 2 → dealkalization in the second dealkalization tank area → heavy padder No. 3 → drying → cropping.

The concentrated alkali tank area of the full straight roller mercerizing machine is provided with 40 pairs of straight rollers, 1 pair of straight rollers consists of an upper rubber roller and a lower metal straight roller, wherein the No. 2 and No. 4 rubber straight rollers are spreading rollers, and the concentration of caustic soda in the concentrated alkali tank area is 90-100 g/L;

after the concentrated alkali solution is discharged from the concentrated alkali tank area, the concentrated alkali solution is subjected to expanding by an expanding roller, enters a No. 1 heavy padder for mangling (the liquid carrying rate is 55 percent), and then enters a first alkali removal tank area with 20 pairs of straight rollers, wherein No. 50, No. 52 and No. 54 rubber straight rollers are expanding rollers; after leaving the first dealkalization groove area, the rubber is subjected to width expansion by a width expansion roller, enters a No. 2 heavy padder for mangling (the liquid carrying rate is 55 percent), and enters a second dealkalization groove area with 38 pairs of straight rollers, wherein No. 64 and No. 67 rubber straight rollers are width expansion rollers. The first and second dealkalizing tank regions are respectively provided with 5 and 10 groups of spray pumps, wherein the first dealkalizing region is provided with 5 groups of spray pumps which are respectively connected with 4 spray pipes. The temperature of the spray liquid in the first dealkalizing tank area is 70-75 ℃. The second dealkalization district has 9 groups of spray pump and each links 4 shower respectively, and 1 group of spray pump links 2 shower finally, and the second dealkalization groove district spray liquid temperature is 50 ~ 55 ℃. Clean water is sprayed to the straight-roller spray pipes corresponding to 98 th and 97 th spray pipes, and light alkali liquor is sprayed to the other spray pipes. And (3) leading the light alkali liquor to flow back to the first dealkalizing tank zone from the second dealkalizing tank zone, leading the concentration of the light alkali sprayed by the straight roller spray pipes corresponding to 42 th and 41 th straight roller spray pipes to reach 40-45 g/L, and recycling for later use. After the cloth is discharged from the second dealkalization area, the cloth is rolled by a No. 3 heavy padder (the liquid carrying rate is 55 percent) and enters two rows of 20 drying cylinders for drying, wherein the two drying cylinders at the bottom of the second row are cooling cylinders for reducing the temperature of the cloth cover; the pH value of the cropping is 7-8, and the moisture content is 3% -4%.

In the technical scheme, when cold pad-batch dyeing is carried out, the dyeing solution for dyeing grey blue consists of the following components: 1.45g/L of active red B-2BF, 2.26g/L of elegans yellow 4RFN and 6.27g/L of elegans navy blue BF-2 GF; alkali liquor composition: 30g/L of caustic soda and 12.5g/L of Alini LDR cold-stack fixation alkali; dye liquor and alkali liquor 4: 1, and when the automobile is started, adding 0.15g/L of dye reactive red B-2BF, 0.23g/L of jacetin yellow 4RFN and 1.28g/L of jacetin dark blue BF-2 GFN into a 100L rolling tank.

In the technical scheme, during cold pad-batch dyeing, the dyeing solution for dyeing water bath green comprises the following components: norwegian clone red ER-2 BL0.54g/L, Norwegian clone yellow ER-2R 3.2g/L, Norwegian clone blue C-5X 6.2 g/L; alkali liquor composition: 30g/L of caustic soda and 12.5g/L of Alini LDR cold-stack fixation alkali; dye liquor and alkali liquor 4: 1, and during the start of the process, adding 0.06g/L of dye Nowegian clone red ER-2 BL, 0.32g/L of Nowegian clone yellow ER-2R and 1.2g/L of Nowegian clone blue C-5X in a 100L rolling tank;

in this technical scheme, dyeing equipment: KUSTER evenness padder, adjusting left, middle and right pressure of padder to 0.30, 0.25 and 0.30MPa, tension of tension bracket to 0.02 MPa. When dyeing is started, the padder is started at the speed of 10m/min, pure cotton cloth guiding is carried out for about 40m, the speed is quickly increased to be more than 40m/min, after the condition that the cloth cover and the center winding are not abnormal is confirmed, the padder speed is increased to be the normal constant speed of 75m/min as fast as possible, and the pure cotton cloth guiding is continuously carried out for about 10m, and then the wide tencel woven fabric is subjected to positive cloth. The mangle rolling rate is controlled between 50 and 55 percent. In order to prevent the generation of seam marks, a plastic film with the length of 2.9m, the width of 0.5m and 15-20 threads is added at the position of a circular seam type seam. After the front cloth of the wide tencel woven fabric is completely dyed, the wide tencel woven fabric is continuously fed into pure cotton wrapping cloth of about 20m, plastic film is wrapped outside the whole large-roll cloth, and the wide tencel woven fabric is moved to a stacking area to be stacked for 20-24 hours at room temperature. When the cloth roll is stacked, the cloth roll must be kept to rotate at a constant speed of 8-10 r/min.

In the technical scheme, the soaping process after dyeing comprises the following steps: the cloth feeding → the first, second and third open washes (40 ℃, 50 ℃, 60 ℃) → the fourth and fifth soapings (the acid low-temperature soaping agent LTS-1002 g/L, 90-95 ℃) → the sixth and seventh hot washes (80 ℃, 70 ℃) → the eighth neutralization (the glacial acetic acid adding system is automatically controlled, the pH is controlled at 5-6 ℃ and 50 ℃) → the ninth normal temperature water wash → the tenth cold water wash → two sets of cylinder drying (wherein the two lowermost drying cylinders in the second row are cooling cylinders, the cloth surface temperature is reduced) → the cloth dropping.

In the technical scheme, when the formaldehyde-free shrink-proof finishing agent and the hyaluronic acid finishing agent are finished in one bath, the working solution comprises the following components:

in the technical scheme, the aldehyde-free low-temperature shrink-proof crease-resistant finishing agent KNITTEX FFRC is a pre-catalyzed aqueous solution containing functional magnesium salts of modified dimethylol dihydroxy ethylene urea.

According to the technical scheme, when the formaldehyde-free shrink-proof and hyaluronic acid finishing agent is finished in one bath, the fabric is fed in an open width mode, the formaldehyde-free shrink-proof and hyaluronic acid finishing agent is rolled in two immersion modes, the finishing liquid is finished in one bath, the liquid carrying rate is 70% -75%, 2% -4% of overfeeding is carried out on a needle plate, ten grids are baked by hot air, the temperature of the first grid to the second grid is 140 ℃, the temperature of the third grid to the fourth grid is 160 ℃, the temperature of the fifth grid to the ten grids is 165-170 ℃, two cylinders are cooled and laid, and the vehicle speed is 45 m/min.

Has the advantages that: according to the invention, the wide tencel woven fabric is subjected to half mercerization on a full-straight-roller mercerizing machine, the tencel woven fabric is fully swelled, the phenomenon of crease scratching caused by hardening of the cloth surface during cold pad-batch dyeing is effectively avoided, no crease exists on the surface of the wide tencel woven fabric, and the uniform dyeing and penetrating dyeing of the tencel woven fabric are facilitated. The wide tencel woven fabric product after cold pad-batch dyeing is flat and has no wrinkle.

The tencel woven fabric uses a thinner 30-degree circular seam type seam head^SThe fabric is drawn by pure cotton about 40m, the padder speed reaches the process set speed, the concentration of the red, yellow and blue dyes in the working solution of the KUSTER uniform padder dipping mangle is kept constant, then the wide tencel woven fabric is fed into the front fabric, and cotton wrapping cloth about 20m is rolled outside one roll of the wide tencel woven fabric. The front and back chromatic aberration of the dyed product is larger than or equal to 4 grades, and the first-grade yield of finished products is improved. The invention optimizes the left, middle and right uniform padder pressure, controls the fabric feeding tension, ensures that the left, middle and right color difference of the dyed product is not less than 4-5 grades, and uses 30^SThe/6 sewing thread has small and firm circular seam type seam head and almost no joint mark, and also improves the first-class yield of finished products. The wide tencel woven fabric is subjected to cold pad-batch dyeing by using a Norway cloned dye, and the alkali agent is mixed alkali of caustic soda and cold-batch fixation alkali, so that the effect of uniform dyeing and penetration of the tencel woven fabric is good.

The invention adopts the same bath finishing of the formaldehyde-free shrink-proof finishing agent and the hyaluronic acid finishing agent, the covalent crosslinking is generated between the formaldehyde-free shrink-proof finishing agent and the tencel fiber, and partial hydroxyl is sealed. The swelling degree of the tencel fabric is greatly reduced in the washing process. Therefore, the shrinkage rate of the wide tencel woven fabric is reduced by the formaldehyde-free shrink-proof finishing, and the anti-pilling performance of the wide tencel woven fabric is improved. After the finishing by the hyaluronic acid finishing agent, the tencel fabric is endowed with skin care performance.

Drawings

Fig. 1 is a schematic structural view of the present invention.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below so that those skilled in the art can better understand the advantages and features of the present invention, and thus the scope of the present invention will be more clearly defined. The embodiments described herein are only a few embodiments of the present invention, rather than all embodiments, and all other embodiments that can be derived by one of ordinary skill in the art without inventive faculty based on the embodiments described herein are intended to fall within the scope of the present invention.

Example 1

The width of the woven fabric of wide tencel (A100 type) is 106 inches, and the yarn count is 60^s×60^sA density of 200X 100 roots/inch;

a cold pad-batch dyeing process for a flat crease-free wide tencel woven fabric comprises the following main production process flows: seam turning → one positive and one negative singeing → rolled amylase stacking desizing → washing → drying → half mercerizing → cold pad-batch dyeing → non-formaldehyde shrink-proof and hyaluronic acid finishing agent one-bath finishing → mechanical preshrinking → inspection and packaging;

when turning over the seam, a circular seam type sewing machine is used, and the thread for sewing the head is 30^sAnd 6, the stitch density is 28-32 needles/10 cm, the vertical seams on the two sides of the selvedge are 4-5 cm, and the tail is 3-5 cm.

Half mercerizing is carried out on a 98-pair full-straight-roller mercerizing machine, and the main process flow is as follows: cloth feeding → caustic soda bath in the concentrated caustic soda tank area → heavy padder No. 1 → dealkalization in the first dealkalization tank area → heavy padder No. 2 → dealkalization in the second dealkalization tank area → heavy padder No. 3 → drying → cropping.

The concentrated alkali tank area of the full straight roller mercerizing machine is provided with 40 pairs of straight rollers, 1 pair of straight rollers consists of an upper rubber roller and a lower metal straight roller, wherein the No. 2 and No. 4 rubber straight rollers are spreading rollers, and the concentration of caustic soda in the concentrated alkali tank area is 80-90 g/L;

after the concentrated alkali solution is discharged from the concentrated alkali tank area, the concentrated alkali solution is subjected to expanding by an expanding roller, enters a No. 1 heavy padder for mangling (the liquid carrying rate is 55 percent), and then enters a first alkali removal tank area with 20 pairs of straight rollers, wherein No. 50, No. 52 and No. 54 rubber straight rollers are expanding rollers; after leaving the first dealkalization groove area, the rubber is subjected to width expansion by a width expansion roller, enters a No. 2 heavy padder for mangling (the liquid carrying rate is 55 percent), and enters a second dealkalization groove area with 38 pairs of straight rollers, wherein No. 64 and No. 67 rubber straight rollers are width expansion rollers. The first and second dealkalizing tank regions are respectively provided with 5 and 10 groups of spray pumps, wherein the first dealkalizing region is provided with 5 groups of spray pumps which are respectively connected with 4 spray pipes. The temperature of the spray liquid in the first dealkalizing tank area is 70-75 ℃. The second dealkalization district has 9 groups of spray pump and each links 4 shower respectively, and 1 group of spray pump links 2 shower finally, and the second dealkalization groove district spray liquid temperature is 50 ~ 55 ℃. Clean water is sprayed to the straight-roller spray pipes corresponding to 98 th and 97 th spray pipes, and light alkali liquor is sprayed to the other spray pipes. And (3) leading the light alkali liquor to flow back to the first dealkalizing tank zone from the second dealkalizing tank zone, leading the concentration of the light alkali sprayed by the straight roller spray pipes corresponding to 42 th and 41 th straight roller spray pipes to reach 40-45 g/L, and recycling for later use. And after the cloth is discharged from the second dealkalization area, the cloth is rolled by a No. 3 heavy padder (the liquid carrying rate is 55 percent) and enters two rows of 20 drying cylinders for drying, wherein the two drying cylinders at the bottom of the second row are cooling cylinders for reducing the temperature of the cloth cover. The pH value of the cropping is 7-8, and the moisture content is 3% -4%.

When cold pad batch dyeing is carried out, the dyeing liquid for dyeing grey blue comprises the following components: 1.45g/L of active red B-2BF, 2.26g/L of elegans yellow 4RFN and 6.27g/L of elegans navy blue BF-2 GF; alkali liquor composition: 30g/L of caustic soda and 12.5g/L of Alini LDR cold-stack fixation alkali; dye liquor and alkali liquor 4: 1, and when the automobile is started, adding 0.15g/L of dye reactive red B-2BF, 0.23g/L of jacetin yellow 4RFN and 1.28g/L of jacetin dark blue BF-2 GFN into a 100L rolling tank. Dyeing equipment: KUSTER evenness padder, adjusting left, middle and right pressure of padder to 0.30, 0.25 and 0.30MPa, tension of tension bracket to 0.02 MPa. When dyeing is started, the padder is started at the speed of 10m/min, pure cotton cloth guiding is carried out for about 40m, the speed is quickly increased to be more than 40m/min, after the condition that the cloth cover and the center winding are not abnormal is confirmed, the padder speed is increased to be the normal constant speed of 75m/min as fast as possible, and the pure cotton cloth guiding is continuously carried out for about 10m, and then the wide tencel woven fabric is subjected to positive cloth. The mangle rolling rate is controlled between 50 and 55 percent. In order to prevent the generation of seam marks, a plastic film with the length of 2.9m, the width of 0.5m and 15-20 threads is added at the position of a circular seam type seam. After the front cloth of the wide tencel woven fabric is completely dyed, continuously feeding pure cotton wrapping cloth of about 20m, wrapping a plastic film outside the whole large-roll cloth, and moving to a stacking area for stacking at room temperature for 20-24 hours; when the cloth roll is stacked, the cloth roll must be kept to rotate at a constant speed of 8-10 r/min.

The soaping process after dyeing comprises the following steps: the cloth feeding → the first, second and third open washes (40 ℃, 50 ℃, 60 ℃) → the fourth and fifth soapings (the acid low-temperature soaping agent LTS-1002 g/L, 90-95 ℃) → the sixth and seventh hot washes (80 ℃, 70 ℃) → the eighth neutralization (the glacial acetic acid adding system is automatically controlled, the pH is controlled at 5-6 ℃ and 50 ℃) → the ninth normal temperature water wash → the tenth cold water wash → two sets of cylinder drying (wherein the two lowermost drying cylinders in the second row are cooling cylinders, the cloth surface temperature is reduced) → the cloth dropping.

When the non-formaldehyde shrink-proof finishing agent and the hyaluronic acid finishing agent are finished in one bath, the working solution comprises the following components:

the aldehyde-free low-temperature shrink-proof crease-resistant finishing agent KNITTEX FFRC is a pre-catalyzed aqueous solution of modified dimethylol dihydroxy ethylene urea containing functional magnesium salt.

When the non-formaldehyde shrink-proof and hyaluronic acid finishing agent are finished in one bath, the non-formaldehyde shrink-proof and hyaluronic acid finishing agent is fed in a flat manner, the non-formaldehyde shrink-proof and hyaluronic acid finishing agent is rolled in one bath, the liquid carrying rate is 70% -75%, 2% -4% of overfeeding is carried out, ten grids are baked by hot air, wherein the temperature of the first grid to the second grid is 140 ℃, the temperature of the third grid to the fourth grid is 160 ℃, the temperature of the fifth grid to the ten grids is 165-170 ℃, two cylinders are used for cooling and doffing, and the vehicle speed is 45 m/min.

The gray blue skin care product is flat and has no crease, the color difference between the front and the back is 4 grades, the color difference between the left, the middle and the right is 4-5 grades, the soaping fastness is 4 grades, the wet rubbing fastness is 3-4 grades, the pilling performance is 4 grades, the breaking strength is 300N in the warp direction and 280N in the weft direction, and the washing size change rate is 2.9 percent in the warp direction and 2.5 percent in the weft direction.

Example 2

The width of the woven fabric of wide tencel (A100 type) is 106 inches, and the yarn count is 50^s×50^sA density of 170X 90 roots/inch;

a cold pad-batch dyeing process for a flat crease-free wide tencel woven fabric comprises the following main production process flows: seam turning → one positive and one negative singeing → rolled amylase stacking desizing → washing → drying → half mercerizing → cold pad-batch dyeing → non-formaldehyde shrink-proof and hyaluronic acid finishing agent one-bath finishing → mechanical preshrinking → inspection and packaging;

when turning over the seam, a circular seam type sewing machine is used, and the thread for sewing the head is 30^sAnd 6, the stitch density is 28-32 needles/10 cm, the vertical seams on the two sides of the selvedge are 4-5 cm, and the tail is 3-5 cm.

Half mercerizing is carried out on a 98-pair full-straight-roller mercerizing machine, and the main process flow is as follows: cloth feeding → caustic soda bath in the concentrated caustic soda tank area → heavy padder No. 1 → dealkalization in the first dealkalization tank area → heavy padder No. 2 → dealkalization in the second dealkalization tank area → heavy padder No. 3 → drying → cropping.

The concentrated alkali tank area of the full straight roller mercerizing machine is provided with 40 pairs of straight rollers, 1 pair of straight rollers consists of an upper rubber roller and a lower metal straight roller, wherein the No. 2 and No. 4 rubber straight rollers are spreading rollers, and the concentration of caustic soda in the concentrated alkali tank area is 80-90 g/L;

after the concentrated alkali solution is discharged from the concentrated alkali tank area, the concentrated alkali solution is subjected to expanding by an expanding roller, enters a No. 1 heavy padder for mangling (the liquid carrying rate is 55 percent), and then enters a first alkali removal tank area with 20 pairs of straight rollers, wherein No. 50, No. 52 and No. 54 rubber straight rollers are expanding rollers; after leaving the first dealkalization groove area, the rubber is subjected to width expansion by a width expansion roller, enters a No. 2 heavy padder for mangling (the liquid carrying rate is 55 percent), and enters a second dealkalization groove area with 38 pairs of straight rollers, wherein No. 64 and No. 67 rubber straight rollers are width expansion rollers. The first and second dealkalizing tank regions are respectively provided with 5 and 10 groups of spray pumps, wherein the first dealkalizing region is provided with 5 groups of spray pumps which are respectively connected with 4 spray pipes. The temperature of the spray liquid in the first dealkalizing tank area is 70-75 ℃. The second dealkalization district has 9 groups of spray pump and each links 4 shower respectively, and 1 group of spray pump links 2 shower finally, and the second dealkalization groove district spray liquid temperature is 50 ~ 55 ℃. Clean water is sprayed to the straight-roller spray pipes corresponding to 98 th and 97 th spray pipes, and light alkali liquor is sprayed to the other spray pipes. And (3) leading the light alkali liquor to flow back to the first dealkalizing tank zone from the second dealkalizing tank zone, leading the concentration of the light alkali sprayed by the straight roller spray pipes corresponding to 42 th and 41 th straight roller spray pipes to reach 40-45 g/L, and recycling for later use. And after the cloth is discharged from the second dealkalization area, the cloth is rolled by a No. 3 heavy padder (the liquid carrying rate is 55 percent) and enters two rows of 20 drying cylinders for drying, wherein the two drying cylinders at the bottom of the second row are cooling cylinders for reducing the temperature of the cloth cover. The pH value of the cropping is 7-8, and the moisture content is 3% -4%.

When cold pad batch dyeing is carried out, the dyeing liquid for dyeing water bath green comprises the following components: norwegian clone red ER-2 BL0.54g/L, Norwegian clone yellow ER-2R 3.2g/L, Norwegian clone blue C-5X 6.2 g/L; alkali liquor composition: 30g/L of caustic soda and 12.5g/L of Alini LDR cold-stack fixation alkali; dye liquor and alkali liquor 4: 1 volume ratio, and adding 0.06g/L of dye Nowegian clone red ER-2 BL, 0.32g/L of Nowegian clone yellow ER-2 R0.32g/L and 1.2g/L of Nowegian clone blue C-5X in a 100L rolling tank when the automobile is started. Dyeing equipment: KUSTER evenness padder, adjusting left, middle and right pressure of padder to 0.30, 0.25 and 0.30MPa, tension of tension bracket to 0.02 MPa. When dyeing is started, the padder is started at the speed of 10m/min, pure cotton cloth guiding is carried out for about 40m, the speed is quickly increased to be more than 40m/min, after the condition that the cloth cover and the center winding are not abnormal is confirmed, the padder speed is increased to be the normal constant speed of 75m/min as fast as possible, and the pure cotton cloth guiding is continuously carried out for about 10m, and then the wide tencel woven fabric is subjected to positive cloth. The mangle rolling rate is controlled between 50 and 55 percent. In order to prevent the generation of seam marks, a plastic film with the length of 2.9m, the width of 0.5m and 15-20 threads is added at the position of a circular seam type seam. After the front cloth of the wide tencel woven fabric is completely dyed, continuously feeding pure cotton wrapping cloth of about 20m, wrapping a plastic film outside the whole large-roll cloth, and moving to a stacking area for stacking at room temperature for 20-24 hours; when the cloth roll is stacked, the cloth roll must be kept to rotate at a constant speed of 8-10 r/min.

The soaping process after dyeing comprises the following steps: the cloth feeding → the first, second and third open washes (40 ℃, 50 ℃, 60 ℃) → the fourth and fifth soapings (the acid low-temperature soaping agent LTS-1002 g/L, 90-95 ℃) → the sixth and seventh hot washes (80 ℃, 70 ℃) → the eighth neutralization (the glacial acetic acid adding system is automatically controlled, the pH is controlled at 5-6 ℃ and 50 ℃) → the ninth normal temperature water wash → the tenth cold water wash → two sets of cylinder drying (wherein the two lowermost drying cylinders in the second row are cooling cylinders, the cloth surface temperature is reduced) → the cloth dropping.

When the non-formaldehyde shrink-proof finishing agent and the hyaluronic acid finishing agent are finished in one bath, the working solution comprises the following components:

the aldehyde-free low-temperature shrink-proof crease-resistant finishing agent KNITTEX FFRC is a pre-catalyzed aqueous solution of modified dimethylol dihydroxy ethylene urea containing functional magnesium salt.

When the non-formaldehyde shrink-proof and hyaluronic acid finishing agent are finished in one bath, the non-formaldehyde shrink-proof and hyaluronic acid finishing agent is fed in a flat manner, the non-formaldehyde shrink-proof and hyaluronic acid finishing agent is rolled in one bath, the liquid carrying rate is 70% -75%, 2% -4% of overfeeding is carried out, ten grids are baked by hot air, wherein the temperature of the first grid to the second grid is 140 ℃, the temperature of the third grid to the fourth grid is 160 ℃, the temperature of the fifth grid to the ten grids is 165-170 ℃, two cylinders are used for cooling and doffing, and the vehicle speed is 45 m/min.

The water-bath green skin care product disclosed by the invention is flat and free of crease, has 4 grades of front-back color difference, 4-5 grades of left-middle-right color difference, 4 grades of soaping fastness, 3-4 grades of wet-rubbing fastness, 4 grades of pilling performance, 320N grades of breaking strength in the warp direction and 290N grades of weft direction, and has the washing size change rate of-2.7% in the warp direction and-2.4% in the weft direction.