CN102492179B - Sodium alginate-based slurry, printing sizing agent and preparation methods thereof - Google Patents

Sodium alginate-based slurry, printing sizing agent and preparation methods thereof Download PDF

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CN102492179B
CN102492179B CN 201110398843 CN201110398843A CN102492179B CN 102492179 B CN102492179 B CN 102492179B CN 201110398843 CN201110398843 CN 201110398843 CN 201110398843 A CN201110398843 A CN 201110398843A CN 102492179 B CN102492179 B CN 102492179B
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sodium alginate
slurry
viscosity modifier
printing
viscosity
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CN102492179A (en
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林国芳
张羡文
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Shenzhen Fuanna Bedding And Furnishing Co Ltd
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Shenzhen Fuanna Bedding And Furnishing Co Ltd
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Abstract

The invention discloses sodium alginate-based slurry, a printing sizing agent and preparation methods thereof. The sodium alginate-based slurry is made from the following ingredients in percentage by weight: 3-6% of sodium alginate, 0.04-0.06% of monosodium orthophosphate, 0.1-0.25% of disodium hydrogen phosphate, 0.5-1.5% of reserve salt, 2-3% of sodium bicarbonate, 2-4% of sodium sulphate, 7-10% of carbamide and 17-21% of soft water. The printing sizing agent is prepared by mixing the following ingredients in percentage by weight: 75-95% of sodium alginate-based slurry and 5-25% of viscosity modifier. With the adoption of color paste prepared from the printing sizing agent disclosed by the invention, the big flat meshwork printing quality can be improved, the printing effect can still be ensured after a vehicle speed is increased, the vehicle speed can be increased by 30% to 50%, the production efficiency can be increased by 100%, and the benefit is remarkably increased.

Description

A kind of sodium alginate base slurry, concentrator and preparation method thereof
[technical field]
The present invention relates to the high-speed square screen reactive printing technology in the dyeing and finishing of textiles chemistry, relate in particular to a kind of sodium alginate base slurry, concentrator and preparation method thereof.
[background technology]
the general cross-peen return of PLATE SCREAM PRINTING is 160CM, stamp is scraped the rear hauling of slurry, because the little terylene silk net of screen frame also has Xiao Xu distortion (diagram), affect printing effect but be unlikely, and there is no special dark special rich and gaudy color in traditional product, but the cross-peen return is after to be 250CM above, because the terylene silk net plane reaches 9 square metres, because terylene silk net itself has certain elasticity, mostly color is rich and gaudy and lead at present the product of trend of the market, deep, with traditional paste formula, for rheological and the shearing modulus of guaranteeing mill base reaches the printing requirement, mill base viscosity can be very large, twine, adhesion between mill base and fabric, can produce when wanting hauling screen frame lifted reset and plain net in the middle of part also be bonded on fabric, when separating in both moments, twine produces certain resilience, because pulling up with resilience, the band mill base gets rid of color dot, affect the production efficiency of stamp and the visual appearance of fabric.
along with the gradation of the raising man textile fabric stamp of living standards of the people is more and more abundanter, the color lightness, purity, the degree of depth all can further improve, and human consumer's pursuit is the product of seamless, return newly developed is the product of the above return of 250CM * 250CM, what plain net was used is all the high-strength polyester silk screen, the plane reaches 9 square metres, with traditional paste formula, clinging power between twine and mill base and fabric can make can produce when wanting hauling screen frame lifted reset and the net in the middle of also be bonded on fabric, the certain band mill base of twine generation pulls up with resilience and gets rid of look when both separate, color dot can be ejected into and produce time point on the pattern of other colors, the lines fluffing is not bright and clean, large-area color lump is can not level dyeing etc. bad, affect the visual appearance of printed fabric.Along with the depth contrast gradient of the color of fabric is increasing, the rich and gaudy dark product of color gets more and more, dye dosage can surpass the 10-50% that dyestuff power is divided consumption, and mill base viscosity can increase 10-15%, also can affect fineness and the effect of stamp with the large plain net of common mill base seal.
[summary of the invention]
The technical problem to be solved in the present invention is to provide a kind of concentrator that can guarantee large PLATE SCREAM PRINTING quality and preparation method thereof.
Another technical problem that will solve of the present invention is to provide a kind of sodium alginate base slurry that can prepare above-mentioned concentrator and preparation method thereof.
In order to solve the problems of the technologies described above, the technical solution used in the present invention is that a kind of sodium alginate base is starched, and is composed of the following components by weight percentage:
Sodium alginate 3-6%;
SODIUM PHOSPHATE, MONOBASIC 0.04-0.06%;
Sodium phosphate dibasic 0.1-0.25%;
Reserve salt 0.5-1.5%;
Sodium bicarbonate 2-3%;
Sodium sulfate anhydrous.min(99) 2-4%;
Urea 7-10%;
Soft water 17-21%.
The aqueous solution of described sodium alginate is when quality-volumetric concentration is 50g/L, and kinetic viscosity is 150pa.s-200pa.s, and described reserve salt is reservehao S.
The preparation method's of above-mentioned sodium alginate base slurry technical scheme comprises the following steps:
Take raw material by above-mentioned weight percent;
Soft water is added beater tup, starts stirrer, successively add raw material and stir in the following order:
1, Sodium sulfate anhydrous.min(99), 2, urea, 3, SODIUM PHOSPHATE, MONOBASIC phosphorus and Sodium phosphate dibasic, 4, sodium alginate;
Add sodium bicarbonate and reserve salt, after stirring, standing more than 2 hours;
Above pulping process, slurry temperature remain on below 40 ℃.
A kind of technical scheme of sodium alginate concentrator is, and is composed of the following components by weight percentage:
Sodium alginate base slurry: 75-95%;
Viscosity modifier: 5-25%;
Wherein, described sodium alginate base slurry is above-mentioned sodium alginate base slurry;
Wherein, viscosity modifier is mixed by following component by weight percentage:
Turpentine 10-30%;
Thickening material 2-4%;
Emulsifying agent 5-7%;
Soft water 17-21%.
Described thickening material is LYOPRINT RT-BC dyeing and printing auxiliary, and emulsifying agent is the 400H dyeing and printing auxiliary.
Above-mentioned sodium alginate concentrator preparation method's technical scheme comprises the following steps:
Weight percent by above-mentioned sodium alginate concentrator takes sodium alginate base slurry and viscosity modifier; Add viscosity modifier in sodium alginate base slurry, drop into beater tup and stir, place more than 2 hours, the pulping process slurry temperature remains on below 50 ℃.
The preparation method of above-described sodium alginate concentrator comprises the preparation process of viscosity modifier:
Weight percent by above-mentioned viscosity modifier takes raw material;
Soft water is added beater tup, start stirrer, add successively emulsifying agent, thickening material to stir;
Add turpentine, and stir, place more than 2 hours;
Above pulping process, slurry temperature remain on below 50 ℃.
The mill base of concentrator modulation of the present invention can improve large PLATE SCREAM PRINTING quality, and after the raising speed of a motor vehicle, printing effect still can be guaranteed, and can increase substantially production efficiency and the economic benefit of stamp.
[embodiment]
Below by embodiment, the present invention is further set forth:
In following examples, sodium alginate dyes the carrier of cellulosic fibre as the printing paste major ingredient on reactive dyestuffs, and the aqueous solution of sodium alginate is when quality-volumetric concentration 50g/L, and kinetic viscosity is 150pa.s-200pa.s, the clean brilliant product in Qingdao; The effect of SODIUM PHOSPHATE, MONOBASIC and Sodium phosphate dibasic is to prevent that reactive dyestuffs are hydrolyzed increase in dissolved state, smart grand Instr Ltd. product; The effect of reservehao S is to prevent from dying the function that keeps the dye activity group, Shangyu city Norcent Chemicals on reactive dyestuffs are in various carriers; Sodium bicarbonate guarantees to dye cellulosic fibre on reactive dyestuffs are under alkaline condition abundant Xinghua chemical product as alkaline agent; The effect of Sodium sulfate anhydrous.min(99) is to make the short fixation of dying of dying cellulosic fibre on reactive dyestuffs, abundant Xinghua chemical product; Urea is as the solubilizing agent of reactive dyestuffs, the surperficial solubilizing agent of cellulosic fibre.
Thickening material is dyeing and printing auxiliary: LYOPRINT RT-BC, producer: HUNTSMAN; Emulsifying agent is dyeing and printing auxiliary 400H, the DIC of producer.
The equipment of using in following examples and apparatus:
1. stirrer:
Use for laboratory: the portable agitato of adjustable speed motor (0-2000rpm), can stir the 2kg slurry;
Batch production is used: the stirrer that the 2000rpm stepless speed-change motor drives.
2. metering outfit:
Precision is the electronic scale of 0.1g, the large electronic scales that industrial production is used (in the suitable scope of weighing), viscometer, special pH test paper or potentiometer
3. charge apparatus: stainless steel cask or the plastic tank of 1L measuring cup, 50kg capacity, scoop, bailer.
One, preparation sodium alginate base slurry in the laboratory:
1, take raw material according to the weight percent in table 1.
2, Jia Shui: add required soft water (supercarbonate content is less than 25mg/L (CaCO3), the hardness water less than 50mg/L (CaCO3)) in beater tup.
3, start stirrer: the paddle of stirrer is placed in container center, the height at the distance bucket end is the diameter (L) of 0.5L---1L times of blade, mixing speed transfers to 1440r/min, should be set as: should be 2.8L---4L in the bucket footpath if diameter of propeller blade is L, the distance of blade and container bottom is 0.5L---1L, allows oar form advection in whipping process and does not form turbulent flow.And blade can not stir near liquid level and form too much foam.
4, be sequentially added into (when stirrer power is sufficient, can directly add raw material) of dissolving in advance well in soft water: 1) Sodium sulfate anhydrous.min(99), 2) urea, 3) SODIUM PHOSPHATE, MONOBASIC phosphorus and Sodium phosphate dibasic.
5, add sodium alginate (the kinetic viscosity 150pa.s-200pa.s of sodium alginate under quality-volumetric concentration 50g/L condition), the rotating speed of stirrer transfers to the 800r/min left and right, slowly add sodium alginate powdery concentrator to continue to stir to the whirlpool center, it is repeatedly even that rotating speed transfers 1440r/min to stir.
6, stirrer is transferred to 800r/min and is added in advance dissolving good sodium bicarbonate and reserve salt, and rotating speed transfers to>and 1600r/min is stirred to evenly.
7, standing: in pulping process, slurry temperature remains on below 40 ℃, and slurry stirred rear placement more than 2 hours, guaranteed the homogeneity of slurry
8, survey pH value and viscosity: check the pH value of modulated good slurry with accurate PH test paper or potentiometer, with the viscosity under NDJ-4 rotational viscosimeter measurement slurry room temperature condition.
Table 1: sodium alginate base slurry embodiment 1-6 and Comparative Examples component concentration and physical property table
Figure BDA0000116394510000061
One, prepare viscosity modifier in the laboratory:
1, take raw material according to the weight percent in table 2.
2, Jia Shui: add required soft water in beater tup.
3, start stirrer: the paddle of stirrer is placed in container center, the height at the distance bucket end is the diameter (L) of 0.5L---1L times of blade, the start mixing speed transfers to 1440r/min, blade position is set as: if diameter of propeller blade is L, the bucket footpath should be 2.8L---4L, the distance of blade and container bottom is 0.5L---1L, allows oar form advection in whipping process and does not form turbulent flow.And oar can not stir the too much foam of formation near liquid level.
4, be sequentially added into emulsifying agent, thickening material: the rotating speed of stirrer transfers to about 1000r/min, slowly adds emulsifing thickener to the whirlpool center, and rotating speed accent>1600r/min is stirred to evenly
5, add turpentine: the rotating speed of stirrer transfers to about 1000r/min, slowly adds turpentine to the whirlpool center, preliminary evenly after, rotating speed transfers 1500r/min to be stirred to evenly.
6 is standing:
The pulping process slurry temperature remains on below 50 ℃, places after 2 hours, guarantees the homogeneity of slurry
6, survey pH value and viscosity: check the pH value of modulated good slurry with accurate PH test paper or potentiometer, measure the viscosity of slurry with viscometer.
Table 2: the component concentration of the embodiment 1-6 of viscosity modifier and physical property table
Three, target slurry (the active PLATE SCREAM PRINTING slurry of high speed) preparation:
1 is mixed corresponding viscosity modifier embodiment 1-6 in the slurry embodiment 1-6 of the sodium alginate base in table 1 and table 2, obtains target slurry embodiment 1-6, and sodium alginate base slurry is pressed table 3 with the weight ratio of viscosity modifier.
2, drop into raw material, the rotating speed of stirrer is transferred from low speed to high speed, and rotating speed transfers to>and 1600r/min is stirred to evenly.
3, standing: in pulping process, slurry temperature remains on below 50 ℃, places after 2 hours, guarantees the homogeneity of slurry
4, survey pH value and viscosity: check the pH value of modulated good slurry with accurate PH test paper or potentiometer, the slurry of each embodiment was respectively surveyed pH value and viscosity in 2 hours, 24 hours, 48 hours in placement.
The component concentration of the embodiment 1-6 of table 3 target slurry and physical property table
Figure BDA0000116394510000082
As seen from the above table, add viscosity modifier in sodium alginate base slurry, the viscosity degradation ratio is rule comparatively, and PH guarantees thixotropic property good in slurry and reach in reasonable interval, reaches to control viscosity and reduce being stained with property, makes slurry sticking and smooth and be not stained with.Because the constant lubricant viscosity that added of the amount of sodium alginate in slurry has reduced, illustrate that this slurry is adding shearing stress disposed slurry viscosity along with stress and shearing rate increase and reduce, after shearing stress is eliminated, viscosity is replied as before, be a good reactive printing slurry, the stamp speed of a motor vehicle increase shearing rate of doctor increases, and size performance is stable, be not stained with the edge of a knife, do not drag slurry, receive slurry clean, stabilised efficiency improves.
In large PLATE SCREAM PRINTING or will enhance productivity in conventional stamp, the speed of a motor vehicle when improving stamp is a key, guarantees printing effect and will improve the speed of a motor vehicle, and a kind of viscosity appropriateness be arranged, the mill base that rheological and thixotropy well and not are stained with, improve production efficiency and product quality.
Use that concentrator of the present invention is starched by the sodium alginate base and viscosity modifier is mixed by a certain percentage, the ratio of adjusting sodium alginate base slurry and viscosity modifier according to the depth of printed color obtains the suitable concentrator of viscosity.
Concentrator suitable viscosity of the present invention, glue and be not stained with, thixotropic property is high, the mill base that modulates with this concentrator, carry and dye material on fabric the time, be not stained with stamp instrument and fabric, effective must avoid that traditional concentrator easily occurs in printing technology to drag slurry to scrape unclean because being stained with the edge of a knife, because being stained with net and traction.When traditional printing paste can adhesive tape prints to mill base on cloth cover and pulls up stamp not bright and clean, the color lump of lines produce moire and inhomogeneous, the moire effect incomplete, withered pen displacement, heterochromaticly stain according to legend or be infected with the bad defective such as Bai Di and produce, having produced bad defective must stop and look into, parking eliminating etc. affects the work of efficient and loses time, after the mill base of concentrator modulation of the present invention improves the speed of a motor vehicle, printing effect still can be guaranteed, the speed of a motor vehicle can improve 30% to 50%, production efficiency can improve 100%, and remarkable benefit improves.
Concentrator acid and alkali-resistance of the present invention and ionogen performance are good, have the stronger carrying capacity that gets, and dyestuff is anchored on fiber by various effects.Dye yield is high, saves dyestuff.This concentrator is sticking and smooth but be not stained with, dispersing property is good, can make and dye the material Uniform Dispersion and accurately be fixed on the certain position of fabric and not imbibition, easily producing stream when having avoided using traditional concentrator oozes, the not bright and clean or breakthrough of hachure, large color lump Dry Sack is uneven, and the disadvantages such as color dot make the decorative pattern clear-cut.Mill base with concentrator modulation of the present invention, make composition complexity, the abundant picture proof of element just can ideally print to existing printing equipment and become possibility on cloth, be unlikely to excessively to delete element or the color of original picture proof, the more design inspiration of Designers and freedom of creation can access performance.
Analytical table 1:
By upper table Data Comparison, target slurry: embodiment 1 is identical with turpentine content in embodiment 3, sodium alginate base slurry: embodiment 3 and embodiment 1 (sodium alginate) content are than 1.67, viscosity ratio: be 9.21,9.3,9.44, target slurry: embodiment 3 is 1.67 with embodiment 1 (sodium alginate) content than also, but viscosity ratio is 7.14,6.93,6.94, and viscosity modifier is described, and effect is remarkable to the adjusting amplitude modulation of viscosity is stable.
Analytical table 2:
Figure BDA0000116394510000111
By upper table Data Comparison, target slurry: embodiment 2 is identical with sodium alginate content in embodiment 5, the content of turpentine: embodiment 2 is 3 times of embodiment 5, and target slurry: embodiment 2 and embodiment 5 viscosity ratio: be 1.03,1.01,1.05, viscosity is consistent.Illustrate in the target slurry turpentine embodiment concentration (10g/100g) with interior this scope in, viscosity amplitude modulation is stable.
The viscosity ratio of target slurry and sodium alginate base slurry: embodiment 2 is 0.576,0.645,0.605; Embodiment 5 is 0.557,0.637,0.577, illustrates that viscosity modifier is transferred the adjusting of viscosity to reach 50% web stabilization and effect is remarkable.
Analytical table 3:
Figure BDA0000116394510000121
By upper table Data Comparison, target slurry: embodiment 4 is identical with sodium alginate content in embodiment 6, the content of turpentine: embodiment 6 is 3 times of embodiment 4, and target slurry: embodiment 6 and embodiment 4 viscosity ratio: be 1.03,1.04,1.01, viscosity is consistent.Illustrate in the target slurry turpentine embodiment concentration (10g/100g) with interior this scope in, viscosity amplitude modulation is stable.
The viscosity ratio of target slurry and sodium alginate base slurry: embodiment 4 is 0.477,0.472,0.507; Embodiment 6 is 0.491,0.492,0.513, illustrates that viscosity modifier reaches 50% to the adjusting amplitude modulation of viscosity, and is stable and effect is remarkable.
Analytical table 4:
Figure BDA0000116394510000131
By upper table Data Comparison, different embodiment, the different time pH value is stable, has reflected that the target slurry is stable, guarantees stable production process.

Claims (3)

1. a sodium alginate concentrator, is characterized in that, and is composed of the following components by weight percentage:
Sodium alginate base slurry: 75-95%;
Viscosity modifier: 5-25%;
Described sodium alginate base slurry is composed of the following components by weight percentage:
Figure FDA0000337247261
Wherein, viscosity modifier is mixed by following component by weight percentage:
Figure FDA0000337247262
2. the preparation method of a sodium alginate concentrator claimed in claim 1, is characterized in that, comprises the following steps:
201) weight percent by claim 1 sodium alginate concentrator takes sodium alginate base slurry and viscosity modifier;
202) add viscosity modifier in sodium alginate base slurry, drop into beater tup and stir, place more than 2 hours, the pulping process slurry temperature remains on below 50 ℃.
3. the preparation method of sodium alginate concentrator according to claim 5, is characterized in that, comprises the preparation process of viscosity modifier:
301) weight percent by claim 1 viscosity modifier takes raw material;
302) soft water is added beater tup, start stirrer, add successively emulsifying agent, thickening material to stir;
303) add turpentine, and stir, place more than 2 hours;
Above pulping process, slurry temperature remain on below 50 ℃.
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CN102634999A (en) * 2012-04-17 2012-08-15 青岛聚大洋海藻工业有限公司 Sodium alga acid printing paste and preparation process thereof
CN104313905A (en) * 2014-11-04 2015-01-28 苏州艾宸服饰有限公司 Printing method for men's garment fabrics
CN105780550A (en) * 2014-12-22 2016-07-20 常熟市虹桥印染有限公司 Printing method of polyester-cotton fabric
CN107201680A (en) * 2016-03-10 2017-09-26 新乡景弘印染有限公司 A kind of thermal transfer printing method
CN107190526A (en) * 2016-03-10 2017-09-22 新乡景弘印染有限公司 A kind of production method of stamp jeans
CN107059435B (en) * 2017-04-28 2019-07-23 昌邑富润纺织科技有限公司 A kind of pure cotton fabric exempts from decatize printing method
CN107254788B (en) * 2017-06-28 2020-05-22 山东洁晶集团股份有限公司 Method for rapidly preparing sodium alginate raw paste with target viscosity for printing and dyeing by one-step method

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JP2003246946A (en) * 2002-02-26 2003-09-05 Upepo & Maji Inc Water-based ink for printing fabric by ink jet method
CN101328684B (en) * 2008-07-31 2010-09-08 章传兴 Real silk and real silk intimating digit printing process
CN102154851A (en) * 2011-06-03 2011-08-17 江西博大化工有限公司 Phosphate starch printing paste and preparation method thereof

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Denomination of invention: Sodium alginate based paste, printing paste and its preparation method

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