CN110565384A - Preparation method of special oiling agent for vortex spun-bonded adhesive fiber - Google Patents
Preparation method of special oiling agent for vortex spun-bonded adhesive fiber Download PDFInfo
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- CN110565384A CN110565384A CN201910697548.9A CN201910697548A CN110565384A CN 110565384 A CN110565384 A CN 110565384A CN 201910697548 A CN201910697548 A CN 201910697548A CN 110565384 A CN110565384 A CN 110565384A
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Abstract
The invention relates to a preparation method of a special oiling agent for vortex spun-bonded adhesive fibers, belonging to the technical field of textile auxiliaries. According to the invention, maleic anhydride is used as a bridging agent, diethanolamine is grafted to polypropylene wax to be used as an antistatic auxiliary agent, so that the antistatic auxiliary agent has good antistatic effect and thermal stability, low foam, low toxicity, excellent emulsifying property and wetting property, and excellent decontamination and foaming capabilities, and the antistatic auxiliary agent prepared by grafting waterborne polyurethane has good lasting antistatic effect, good washing resistance and good compatibility, thereby improving the mechanical strength of viscose fiber; the prepared antistatic auxiliary agent is a nonionic antistatic auxiliary agent, has no electric charge and small polarity, usually has longer lipophilic group and has good compatibility with resin.
Description
Technical Field
the invention relates to a preparation method of a special oiling agent for vortex spun-bonded adhesive fibers, belonging to the technical field of textile auxiliaries.
Background
Vortex spinning is different from ring spinning and rotor spinning, and the yarn forming principle is as follows: the fed sliver is drafted by a four-roller (or five-roller) drafting device to obtain a parallel fiber bundle with a set yarn count, and the fiber bundle is sucked into a nozzle by means of negative pressure. The front end of the fiber bundle is pulled by the tail end of the yarn being formed to enter the yarn withdrawal tube; under the action of the axial component force of the high-speed vortex, a part of fibers in the rear end of the fiber bundle are inverted at the inlet of the yarn-withdrawing pipe. The reverse fiber exposed in the rotary airflow ejected from the nozzle is twisted on the yarn tail along with the rotation of the airflow to form true twisted yarn output. The wrapping angle and the revolving angle of the fiber bundle on the spindle can be adjusted according to the process.
The high-speed rotary machine parts such as spindles, steel wire rings and the like in the vortex spinning non-ring spinning are twisted into yarns by rotating vortex, and compared with mechanical twisting, the efficiency is obviously improved. The rotary vortex only realizes the twisting action and does not influence the yarn number, high-speed spinning can be realized based on the principle, the highest spinning speed of the vortex spinning of Jiangsu Shixiang textile company can reach 500m/min, and the single-spindle yield is more than 24 times of that of ring spinning. Because the fiber is subjected to the action of air-jet vortex and take-up roller to form true twist, the twisting mode can not be replaced by other spinning machines, and the yarn-forming structure is more compact.
Compared with the traditional ring spinning and novel rotor spinning, the vortex spinning technology has the following characteristics:
(1) the production efficiency is high;
(2) The spinning process is short;
(3) The labor is minimum;
(4) The quality control means of the vortex spinning machine is advanced;
(5) Vortex spun yarns are distinctive;
(6) the production cost is low.
The viscose fiber is cellulose fiber obtained by extracting and remolding fiber molecules from natural wood cellulose by taking wood pulp as a raw material, and belongs to one of regenerated cellulose fibers. The viscose fiber has good hygroscopicity, meets the physiological requirements of human skin, and has the characteristics of smoothness, coolness, air permeability, static resistance, ultraviolet resistance, gorgeous color and good dyeing fastness. It has the nature of cotton, the quality of silk. The fabric is widely applied to the fields of various underwear, textile, clothes, non-woven fabrics and the like.
The surface of the natural fiber is provided with a layer of natural grease, and the natural fiber has good textile performance. After the viscose fiber is formed, the surface of the viscose fiber is free of grease after the impurities are removed through the procedures of washing, desulfurization and the like, the viscose fiber cannot be directly spun, and oiling treatment is carried out on the surface of the fiber through an oiling procedure. The oil used by most enterprises at present is imported oil, and viscose fiber is oiled by the imported oil to endow the fiber with good surface performance, so that the spinning requirements of common ring spinning, compact siro spinning and low-speed vortex spinning can be met.
The oil agent is an important chemical agent for the post-treatment of viscose fibers, and can increase the softness and smoothness of the fibers, improve the hand feeling of the fibers, reduce the electrostatic effect of the fibers, reduce the friction coefficient of the fibers and increase the cohesive force of the fibers, thereby improving the spinning spinnability and the yarn quality. The viscose fiber has the following requirements on oil agent: the oil solution is convenient to use and can be uniformly adsorbed on the surface of viscose fiber, so that the fiber is not wound and does not stick to a roller in the spinning process and has excellent cohesive force; endows the fiber with a certain antistatic effect, and can reduce the generation of electrostatic phenomenon in the spinning process as much as possible; the stability of the oil solution emulsion is good, and the oil solution emulsion is not layered after being stored for 24 hours; a certain thermal stability is required. In the drying process, the oil film is not deteriorated due to high temperature, sticky, yellow and volatile, and is beneficial to improving whiteness; the oil solution emulsion has less foam and no corrosion to metal.
The oil content of the fiber is strictly controlled, the fiber cannot meet the requirements of a spinning process when the oil content is too low, and the fiber is stuck to a roller during spinning when the oil content is too high, so that the spinning processing is difficult. The oil content is also related to the climate condition and the air humidity, and is controlled to be higher in winter. The oil content of the fiber is related to the concentration of the oil solution bath, the circulation amount of the oil bath, the temperature of the bath, the water content of the fiber during oiling, the high-pressure rolling process after leaving the oil bath and the drying temperature. The oil content is generally controlled between 0.2mg/100g and 0.7mg/100 g. The row mark requirement is between 0.15mg/100g and 0.30mg/100 g.
Most of oil agents used by viscose fiber manufacturers at present are imported oil agents, and indexes such as friction coefficient, cohesive force, specific resistance and the like of fibers using the oil agents can meet the requirements of traditional ring spinning and compact siro spinning; the novel spinning has no roving process like vortex spinning, the surface property requirement of fiber raw materials is high when the bobbin yarns are directly drawn to post-spinning, and the surface property of the fibers given by the currently used oil agent can still meet the requirement of low-speed vortex spinning.
the vortex spinning yarn principle is different from the traditional ring spinning, when the ring spun yarn is twisted, the inner layer and the outer layer of the single yarn have the same twist; the inner layer of the vortex spinning single yarn is formed by longitudinally and linearly arranging a plurality of fibers in a staggered mode without twist, and the outer layer of fibers has twist and wraps the inner layer of fibers. Therefore, the strength of the vortex spun single yarn is lower than that of the ring spun single yarn, and the vortex spinning has higher requirement on the surface property of the fiber raw material in high-speed spinning: if the friction coefficient is lower, the fibers are well combed without entanglement in the vortex spinning cotton carding process, the neps are less, the coarse and fine details of the finished yarn are less, the shearing number is less, and the efficiency is improved; the low specific resistance ensures that the static electricity of the fiber is less in the carding, drawing and drawing processes, and the surface of the sliver is smooth and is not easy to hang flower; the outer layer fiber does not slip in the twisting process due to a certain cohesive force, the fiber strength is enhanced, the yarn is not broken during forming, the efficiency is improved, and the yarn quality is improved.
The friction coefficient, specific resistance, fluffiness and cohesion of the fiber are key parameters in spinning, for example, the fiber is required to be easy to open, easy to comb, free from static electricity and damage the fiber in the blowing-carding process, so that the fiber is required to have lower friction coefficient and specific resistance, and the fiber is less in sliver neps through combing; the cotton carding, drawing and drawing processes require that fibers have certain fluffiness and cohesion to keep the circular section of the cotton sliver; the yarn forming process from sliver spinning to single yarn spinning requires that the fibers have certain cohesive force, so that the outer layer fibers do not slip and the inner layer fibers are better wrapped. Therefore, the development of special oiling agents for vortex spun-bonded viscose fibers is necessary to endow the fibers with surface properties suitable for vortex spinning, and the preparation method has wide application prospects.
disclosure of Invention
the technical problems to be solved by the invention are as follows: aiming at the problems of poor yarn evenness and low strength of surface properties of fibers endowed by the original oil, the preparation method of the special oil for vortex spinning viscose is provided.
in order to solve the technical problems, the invention adopts the technical scheme that:
(1) Stirring a polypropylene wax oil bath to obtain a melt, mixing the melt, maleic anhydride, diisobutyl phthalate and absolute ethyl alcohol, continuously stirring for 10-20 min to obtain a reactant, adding diisobutyl phthalate into the reactant, stirring for reaction to obtain a mixture, placing the mixture in a pressure reduction device, distilling under reduced pressure to obtain a semi-finished product, washing and soaking the semi-finished product, and drying to obtain a graft;
(2) Taking a graft, 3-chloropropene, methyl methacrylate, cumene hydroperoxide, tetraethylenepentamine, sodium phosphate and deionized water, mixing the graft, the sodium phosphate and the deionized water, stirring to obtain a mixed solution, adding the 3-chloropropene, the methyl methacrylate and the cumene hydroperoxide into the mixed solution, continuously stirring for 20-30 min at the temperature of 30-35 ℃ to obtain a mixed solution A, adding the tetraethylenepentamine into the mixed solution A, and continuously stirring for 3-4 h to obtain the antistatic auxiliary agent;
(3) Mixing polyethylene glycol biscyule silicate, polyethylene glycol monooleate, mineral oil, an antistatic auxiliary agent, a stearic acid emulsifier AE-96 and deionized water, and stirring to obtain the special oiling agent for the vortex spun-bonded viscose fiber.
the oil bath stirring treatment step in the step (1) is as follows: and (3) carrying out oil-bath stirring on the polypropylene wax for 1-2 h under the nitrogen atmosphere at the temperature of 190-200 ℃ and the stirring speed of 100-150 r/min.
The ratio of the melt, the maleic anhydride, the diisobutyl phthalate and the absolute ethyl alcohol in the step (1) is respectively as follows: respectively weighing 20-30 parts of melt, 2-6 parts of maleic anhydride, 0.3-0.5 part of diisobutyl phthalate and 80-100 parts of absolute ethyl alcohol according to parts by weight.
The stirring reaction step in the step (1) is as follows: adding diisobutyl phthalate into the reactant, and stirring and reacting for 1-2 h at the stirring speed of 200-300 r/min.
The reduced pressure distillation step in the step (1) comprises the following steps: and (3) placing the mixture in a pressure reduction device, and carrying out reduced pressure distillation for 2-3 h under the reduced pressure of 2000-3000 Pa.
The washing, soaking and drying treatment steps in the step (1) are as follows: adding absolute ethyl alcohol into the semi-finished product, soaking for 10-12 hours, performing suction filtration to obtain a precipitate, soaking the precipitate for 3-5 hours by using the absolute ethyl alcohol, filtering to obtain a filter residue, drying the filter residue in an oven at the temperature of 70-80 ℃ for 4-5 hours, and cooling to room temperature.
the graft, 3-chloropropene, methyl methacrylate, cumene hydroperoxide, tetraethylenepentamine, sodium phosphate and deionized water in the step (2) are respectively in the following proportion: respectively weighing 20-30 parts of graft, 1-10 parts of 3-chloropropene, 1-10 parts of methyl methacrylate, 0.2-0.4 part of cumene hydroperoxide, 0.3-0.6 part of tetraethylenepentamine, 1-3 parts of sodium phosphate and 40-60 parts of deionized water according to parts by weight.
The stirring treatment step in the step (2) is as follows: and mixing the graft, sodium phosphate and deionized water, and stirring for 10-15 min at a stirring speed of 100-200 r/min.
The polyethylene glycol biscriester, the polyethylene glycol monooleate, the mineral oil, the antistatic auxiliary agent, the stearic acid emulsifier AE-96 and the deionized water in the proportion of the step (3) are respectively as follows: respectively weighing 10-20 parts of polyethylene glycol biscyule silicate, 10-20 parts of polyethylene glycol monooleate, 5-10 parts of mineral oil, 5-10 parts of antistatic auxiliary agent, 1-10 parts of stearic acid emulsifier AE-96 and 50-80 parts of deionized water according to parts by weight.
The stirring treatment step in the step (3) is as follows: mixing polyethylene glycol biscy silicate, polyethylene glycol monooleate, mineral oil, an antistatic auxiliary agent, stearic acid emulsifier AE-96 and deionized water, and stirring for 3-5 hours at the temperature of 60-70 ℃ and the stirring speed of 200-260 r/min.
Compared with other methods, the method has the beneficial technical effects that:
(1) according to the invention, maleic anhydride is used as a bridging agent, diethanolamine is grafted to polypropylene wax to be used as an antistatic auxiliary agent, so that the antistatic auxiliary agent has good antistatic effect and thermal stability, low foam, low toxicity, excellent emulsifying property and wetting property, and excellent decontamination and foaming capabilities, and the antistatic auxiliary agent prepared by grafting waterborne polyurethane has good lasting antistatic effect, good washing resistance and good compatibility, thereby improving the mechanical strength of viscose fiber; the prepared antistatic auxiliary agent is a nonionic antistatic auxiliary agent, has no electric charge and small polarity, usually has longer lipophilic group and has good compatibility with resin;
(2) The method adopts a melt grafting method to graft maleic anhydride on polypropylene wax, further utilizes the maleic anhydride in a graft as a bridging agent to graft micromolecule diethanolamine, and utilizes carbonyl on the maleic anhydride and amino of the diethanolamine to carry out amidation reaction; the non-ionic antistatic auxiliary agent generally contains an oxyethylene structure and polar groups such as hydroxyl, carboxyl or amino; the antistatic agent has no electric charge, has lone pair electrons, shows weak polarity, and has smaller polarity than an ionic antistatic auxiliary agent, so the antistatic effect is not good in ionic type; generally, the nonionic antistatic auxiliary agent has a longer lipophilic group, has good compatibility with resin, low toxicity, good processability and good thermal stability;
(3) the invention takes non-ionic surfactant as main body, combines smoothing agent, emulsifier and antistatic auxiliary agent prepared by maleic anhydride grafting, prepares special oil agent for vortex spinning viscose fiber, fiber absorbs a layer of smoothing agent after oiling, and friction can occur between hydrophobic groups sliding mutually; the longer the hydrophobic group is, the easier the hydrophobic group slides, the smaller the friction is, and the best effect is achieved when the number of carbon atoms is 16-18; hydrophobic groups in the prepared antistatic auxiliary agent are adsorbed on the surface of the fiber, and hydrophilic groups tend to air to form a hydrophilic film which can prevent static electricity; adding a proper emulsifier into the oil agent to emulsify and uniformly disperse water-insoluble oil agent components in water, reducing the tension between two interfaces, promoting the solution to be stable and facilitating the oiling of fibers;
(4) According to the invention, the antistatic auxiliary agent is grafted by the waterborne polyurethane, and the waterborne polyurethane has good film forming property and high bonding strength to textiles, can endow the textiles with soft and plump handfeel, and improves the wear resistance, wrinkle resistance, rebound resilience, permeability, heat resistance and the like of the textiles, so that the treated viscose fibers have good physical and mechanical properties and antistatic effects.
Detailed Description
The preparation method comprises the steps of subjecting polypropylene wax to oil bath stirring for 1-2 hours at the temperature of 190-200 ℃ and the stirring speed of 100-150 r/min under the nitrogen atmosphere to obtain a melt, weighing 20-30 parts by weight of the melt, 2-6 parts by weight of maleic anhydride, 0.3-0.5 part by weight of diisobutyl phthalate and 80-100 parts by weight of absolute ethyl alcohol respectively, mixing maleic anhydride and the melt, continuing stirring for 10-20 minutes to obtain a reactant, adding diisobutyl phthalate into the reactant, stirring and reacting for 1-2 hours at the stirring speed of 200-300 r/min to obtain a mixture, placing the mixture in a pressure reduction device, carrying out reduced pressure distillation for 2-3 hours under the reduced pressure of 2000-3000 Pa to obtain a semi-finished product, adding absolute ethyl alcohol into the semi-finished product, soaking for 10-12 hours, carrying out suction filtration to obtain a precipitate, soaking and precipitating with absolute ethyl alcohol for 3-5 hours, filtering to obtain a filter residue, placing the filter residue in an oven at the temperature of 70-80 ℃ to dry for 4-5 hours, cooling to room temperature to obtain a graft; respectively weighing 20-30 parts of graft, 1-10 parts of 3-chloropropene, 1-10 parts of methyl methacrylate, 0.2-0.4 part of cumene hydroperoxide, 0.3-0.6 part of tetraethylenepentamine, 1-3 parts of sodium phosphate and 40-60 parts of deionized water according to parts by weight, mixing the graft, the sodium phosphate and the deionized water, stirring at the stirring speed of 100-200 r/min for 10-15 min to obtain a mixed solution, adding the 3-chloropropene, the methyl methacrylate and the cumene hydroperoxide into the mixed solution, continuously stirring at the temperature of 30-35 ℃ for 20-30 min to obtain a mixed solution A, adding the tetraethylenepentamine into the mixed solution A, and continuously stirring for 3-4 h to obtain the antistatic auxiliary agent; respectively weighing 10-20 parts of polyethylene glycol crescent silicate, 10-20 parts of polyethylene glycol monooleate, 5-10 parts of mineral oil, 5-10 parts of antistatic auxiliary agent, 1-10 parts of stearic acid emulsifier AE-96 and 50-80 parts of deionized water according to parts by weight, mixing the polyethylene glycol crescent silicate, the polyethylene glycol monooleate, the mineral oil, the antistatic auxiliary agent, the stearic acid emulsifier AE-96 and the deionized water, and stirring for 3-5 hours at the temperature of 60-70 ℃ and the stirring speed of 200-260 r/min to obtain the special oiling agent for the vortex spun-bonded viscose fibers.
Example 1
The polypropylene wax is stirred for 1 hour in an oil bath under the atmosphere of nitrogen at the temperature of 190 ℃ and the stirring speed of 100r/min, obtaining a melt, respectively weighing 20 parts of the melt, 2 parts of maleic anhydride, 0.3 part of diisobutyl phthalate and 80 parts of absolute ethyl alcohol according to parts by weight, mixing the maleic anhydride and the melt, continuously stirring for 10min, to obtain a reactant, adding diisobutyl phthalate into the reactant, stirring and reacting for 1h at the stirring speed of 200r/min, obtaining a mixture, putting the mixture into a pressure reduction device, reducing the pressure to 2000Pa, carrying out reduced pressure distillation for 2h, adding anhydrous ethanol into the semi-finished product, soaking for 10 hr, vacuum filtering to obtain precipitate, soaking in anhydrous ethanol for 3 hr, filtering to obtain filter residue, drying the filter residue in an oven at 70 deg.C for 4h, and cooling to room temperature to obtain graft; respectively weighing 20 parts of graft, 1 part of 3-chloropropene, 1 part of methyl methacrylate, 0.2 part of cumene hydroperoxide, 0.3 part of tetraethylenepentamine, 1 part of sodium phosphate and 40 parts of deionized water according to parts by weight, mixing the graft, the sodium phosphate and the deionized water, stirring for 10min at the stirring speed of 100r/min to obtain a mixed solution, adding the 3-chloropropene, the methyl methacrylate and the cumene hydroperoxide into the mixed solution, continuously stirring for 20min at the temperature of 30 ℃ to obtain a mixed solution A, adding the tetraethylenepentamine into the mixed solution A, and continuously stirring for 3h to obtain the antistatic auxiliary agent; respectively weighing 10 parts of polyethylene glycol bilaminar silicate, 10 parts of polyethylene glycol monooleate, 5 parts of mineral oil, 5 parts of antistatic auxiliary agent, 1 part of stearic acid emulsifier AE-96 and 50 parts of deionized water according to parts by weight, mixing the polyethylene glycol bilaminar silicate, the polyethylene glycol monooleate, the mineral oil, the antistatic auxiliary agent, the stearic acid emulsifier AE-96 and the deionized water, and stirring for 3 hours at the temperature of 60 ℃ and the stirring speed of 200r/min to obtain the special oiling agent for the vortex spinning viscose fibers.
example 2
Stirring polypropylene wax in oil bath for 1h under nitrogen atmosphere at 195 ℃ and the stirring speed of 125r/min, obtaining a melt, respectively weighing 25 parts of the melt, 4 parts of maleic anhydride, 0.4 part of diisobutyl phthalate and 90 parts of absolute ethyl alcohol according to parts by weight, mixing the maleic anhydride and the melt, continuously stirring for 15min, to obtain a reactant, adding diisobutyl phthalate into the reactant, stirring and reacting for 1h at the stirring speed of 250r/min, to obtain a mixture, putting the mixture into a pressure reduction device, reducing the pressure to 2500Pa, carrying out reduced pressure distillation for 2h, adding anhydrous ethanol into the semi-finished product, soaking for 11 hr, vacuum filtering to obtain precipitate, soaking with anhydrous ethanol for 4 hr, filtering to obtain filter residue, drying the filter residue in an oven at 75 deg.C for 4h, and cooling to room temperature to obtain graft; respectively weighing 25 parts of graft, 5 parts of 3-chloropropene, 5 parts of methyl methacrylate, 0.3 part of cumene hydroperoxide, 0.5 part of tetraethylenepentamine, 2 parts of sodium phosphate and 50 parts of deionized water according to parts by weight, mixing the graft, the sodium phosphate and the deionized water, stirring for 12min at the stirring speed of 150r/min to obtain a mixed solution, adding the 3-chloropropene, the methyl methacrylate and the cumene hydroperoxide into the mixed solution, continuously stirring for 25min at the temperature of 33 ℃ to obtain a mixed solution A, adding the tetraethylenepentamine into the mixed solution A, and continuously stirring for 3h to obtain the antistatic auxiliary agent; respectively weighing 15 parts of polyethylene glycol bilaminar silicate, 15 parts of polyethylene glycol monooleate, 8 parts of mineral oil, 8 parts of antistatic auxiliary agent, 5 parts of stearic acid emulsifier AE-96 and 65 parts of deionized water according to parts by weight, mixing the polyethylene glycol bilaminar silicate, the polyethylene glycol monooleate, the mineral oil, the antistatic auxiliary agent, the stearic acid emulsifier AE-96 and the deionized water, and stirring for 4 hours at the temperature of 65 ℃ and the stirring speed of 230r/min to obtain the special oiling agent for the vortex spinning viscose.
example 3
Stirring polypropylene wax in oil bath for 2 hours at the temperature of 200 ℃ and the stirring speed of 150r/min under the nitrogen atmosphere, obtaining a melt, respectively weighing 30 parts of the melt, 6 parts of maleic anhydride, 0.5 part of diisobutyl phthalate and 100 parts of absolute ethyl alcohol according to parts by weight, mixing the maleic anhydride and the melt, continuously stirring for 20min, to obtain a reactant, adding diisobutyl phthalate into the reactant, stirring and reacting for 2 hours at the stirring speed of 300r/min, obtaining a mixture, putting the mixture into a pressure reduction device, reducing the pressure to 3000Pa, carrying out reduced pressure distillation for 3h, adding anhydrous ethanol into the semi-finished product, soaking for 12 hr, vacuum filtering to obtain precipitate, soaking in anhydrous ethanol for 5 hr, filtering to obtain filter residue, drying the filter residue in an oven at 80 deg.C for 5h, and cooling to room temperature to obtain graft; respectively weighing 30 parts of graft, 10 parts of 3-chloropropene, 10 parts of methyl methacrylate, 0.4 part of cumene hydroperoxide, 0.6 part of tetraethylenepentamine, 3 parts of sodium phosphate and 60 parts of deionized water according to parts by weight, mixing the graft, the sodium phosphate and the deionized water, stirring for 15min at the stirring speed of 200r/min to obtain a mixed solution, adding the 3-chloropropene, the methyl methacrylate and the cumene hydroperoxide into the mixed solution, continuously stirring for 30min at the temperature of 35 ℃ to obtain a mixed solution A, adding the tetraethylenepentamine into the mixed solution A, and continuously stirring for 4h to obtain the antistatic auxiliary agent; respectively weighing 20 parts of polyethylene glycol bilaminar silicate, 20 parts of polyethylene glycol monooleate, 10 parts of mineral oil, 10 parts of antistatic auxiliary agent, 10 parts of stearic acid emulsifier AE-96 and 80 parts of deionized water according to parts by weight, mixing the polyethylene glycol bilaminar silicate, the polyethylene glycol monooleate, the mineral oil, the antistatic auxiliary agent, the stearic acid emulsifier AE-96 and the deionized water, and stirring for 5 hours at the temperature of 70 ℃ and the stirring speed of 260r/min to obtain the special oiling agent for the vortex spun-bonded viscose fibers.
Comparative example: the special oiling agent for vortex spinning viscose fiber produced by Dongguan company.
After oiling the viscose fiber, the special oiling agents prepared in the embodiments and the comparative examples are detected, and the detection is as follows:
determination of the oil content of the fiber: soxhlet extraction is adopted, the oil on the fiber is extracted into a distillation flask by using ether by utilizing the property that the oil can be dissolved in an ether organic solvent, and the obtained liquid is evaporated and dried to obtain the oil which is not easy to volatilize.
Determination of the coefficient of friction of the fibers: firstly, the oiled viscose fiber is manually made into a fiber roller, and the fibers on the fiber roller cannot be entangled with each other and cannot be curled. Then, friction coefficient test is carried out on the oiled viscose staple fibers by adopting a winch method, and the tester is a YG151 type fiber friction coefficient tester, and the initial tension is 0.2 cN. When measuring the dynamic friction coefficient, the rotating speed of the fiber roller is set to be 30 r/min; when the static friction coefficient is measured, the fiber roller is kept still, the handle of the torsion balance is slowly and manually rotated at a constant speed, the rotation of the handle is immediately stopped when sudden slippage occurs between the fiber and the fiber roller, and the reading on the torsion balance when the pointer begins to deflect is read. And randomly selecting 5 fibers from each fiber sample to test the friction coefficient, wherein each fiber is tested twice, and the average value is taken as the test result.
Fiber mass specific resistance test: the method comprises the following steps: randomly extracting 50g of the fiber sample, loosening by hands, balancing for more than 4 hours under a standard atmospheric condition, and weighing 3 parts of test sample, 15g of each part, by using a balance with the precision of 0.01g for use in testing; according to the standard GB/T14342-1993, during testing, the fiber measuring box is taken out of the case, the pressing block is taken out by a special hook of the instrument, a weighed fiber sample is uniformly filled into the box by tweezers, then the pressing block is pushed in, then the fiber measuring box is put into the instrument, and the handle is rotated until the fiber measuring box is not shaken.
the specific test results are shown in table 1.
Table 1 comparative table of property characterization
Detecting items | example 1 | Example 2 | Example 3 | Comparative example |
Oil content of fiber/mg/100 fiber | 0.20 | 0.21 | 0.22 | 0.7 |
Coefficient of friction | 0.118 | 0.123 | 0.115 | 0.291 |
Fiber mass specific resistance/108Ω•g/cm2 | 7.8 | 7.9 | 7.6 | 9.5 |
As can be seen from Table 1, the oil solution special for vortex spinning viscose fibers prepared by the invention has good oil content, friction coefficient and fiber mass specific resistance.
Claims (10)
1. A preparation method of special oiling agent for vortex spun-bonded adhesive fiber is characterized by comprising the following specific preparation steps:
(1) Stirring a polypropylene wax oil bath to obtain a melt, mixing the melt, maleic anhydride, diisobutyl phthalate and absolute ethyl alcohol, continuously stirring for 10-20 min to obtain a reactant, adding diisobutyl phthalate into the reactant, stirring for reaction to obtain a mixture, placing the mixture in a pressure reduction device, distilling under reduced pressure to obtain a semi-finished product, washing and soaking the semi-finished product, and drying to obtain a graft;
(2) Taking a graft, 3-chloropropene, methyl methacrylate, cumene hydroperoxide, tetraethylenepentamine, sodium phosphate and deionized water, mixing the graft, the sodium phosphate and the deionized water, stirring to obtain a mixed solution, adding the 3-chloropropene, the methyl methacrylate and the cumene hydroperoxide into the mixed solution, continuously stirring for 20-30 min at the temperature of 30-35 ℃ to obtain a mixed solution A, adding the tetraethylenepentamine into the mixed solution A, and continuously stirring for 3-4 h to obtain the antistatic auxiliary agent;
(3) Mixing polyethylene glycol biscyule silicate, polyethylene glycol monooleate, mineral oil, an antistatic auxiliary agent, a stearic acid emulsifier AE-96 and deionized water, and stirring to obtain the special oiling agent for the vortex spun-bonded viscose fiber.
2. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the oil bath stirring treatment step in the step (1) is as follows: and (3) carrying out oil-bath stirring on the polypropylene wax for 1-2 h under the nitrogen atmosphere at the temperature of 190-200 ℃ and the stirring speed of 100-150 r/min.
3. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the ratio of the melt, the maleic anhydride, the diisobutyl phthalate and the absolute ethyl alcohol in the step (1) is respectively as follows: respectively weighing 20-30 parts of melt, 2-6 parts of maleic anhydride, 0.3-0.5 part of diisobutyl phthalate and 80-100 parts of absolute ethyl alcohol according to parts by weight.
4. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the stirring reaction step in the step (1) is as follows: adding diisobutyl phthalate into the reactant, and stirring and reacting for 1-2 h at the stirring speed of 200-300 r/min.
5. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the reduced pressure distillation step in the step (1) comprises the following steps: and (3) placing the mixture in a pressure reduction device, and carrying out reduced pressure distillation for 2-3 h under the reduced pressure of 2000-3000 Pa.
6. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the washing, soaking and drying treatment steps in the step (1) are as follows: adding absolute ethyl alcohol into the semi-finished product, soaking for 10-12 hours, performing suction filtration to obtain a precipitate, soaking the precipitate for 3-5 hours by using the absolute ethyl alcohol, filtering to obtain a filter residue, drying the filter residue in an oven at the temperature of 70-80 ℃ for 4-5 hours, and cooling to room temperature.
7. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the graft, 3-chloropropene, methyl methacrylate, cumene hydroperoxide, tetraethylenepentamine, sodium phosphate and deionized water in the step (2) are respectively in the following proportion: respectively weighing 20-30 parts of graft, 1-10 parts of 3-chloropropene, 1-10 parts of methyl methacrylate, 0.2-0.4 part of cumene hydroperoxide, 0.3-0.6 part of tetraethylenepentamine, 1-3 parts of sodium phosphate and 40-60 parts of deionized water according to parts by weight.
8. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the stirring treatment step in the step (2) is as follows: and mixing the graft, sodium phosphate and deionized water, and stirring for 10-15 min at a stirring speed of 100-200 r/min.
9. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the polyethylene glycol biscriester, the polyethylene glycol monooleate, the mineral oil, the antistatic auxiliary agent, the stearic acid emulsifier AE-96 and the deionized water in the proportion of the step (3) are respectively as follows: respectively weighing 10-20 parts of polyethylene glycol biscyule silicate, 10-20 parts of polyethylene glycol monooleate, 5-10 parts of mineral oil, 5-10 parts of antistatic auxiliary agent, 1-10 parts of stearic acid emulsifier AE-96 and 50-80 parts of deionized water according to parts by weight.
10. The preparation method of the special oiling agent for the vortex spun-bonded adhesive fiber according to claim 1, which is characterized in that: the stirring treatment step in the step (3) is as follows: mixing polyethylene glycol biscy silicate, polyethylene glycol monooleate, mineral oil, an antistatic auxiliary agent, stearic acid emulsifier AE-96 and deionized water, and stirring for 3-5 hours at the temperature of 60-70 ℃ and the stirring speed of 200-260 r/min.
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Cited By (2)
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CN111851075A (en) * | 2020-08-11 | 2020-10-30 | 沈阳新意精细助剂有限公司 | Preparation method of vortex spinning viscose oil agent |
CN114197210A (en) * | 2021-12-21 | 2022-03-18 | 赛得利(福建)纤维有限公司 | Hydrophobically modified viscose fiber and preparation method thereof |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN111851075A (en) * | 2020-08-11 | 2020-10-30 | 沈阳新意精细助剂有限公司 | Preparation method of vortex spinning viscose oil agent |
CN114197210A (en) * | 2021-12-21 | 2022-03-18 | 赛得利(福建)纤维有限公司 | Hydrophobically modified viscose fiber and preparation method thereof |
CN114197210B (en) * | 2021-12-21 | 2024-03-19 | 赛得利(福建)纤维有限公司 | Hydrophobically modified viscose fiber and preparation method thereof |
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