CN110746607B - Auxiliary product applied to spandex spinning oil agent and having effects of isolating and adjusting friction - Google Patents

Auxiliary product applied to spandex spinning oil agent and having effects of isolating and adjusting friction Download PDF

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CN110746607B
CN110746607B CN201911171414.XA CN201911171414A CN110746607B CN 110746607 B CN110746607 B CN 110746607B CN 201911171414 A CN201911171414 A CN 201911171414A CN 110746607 B CN110746607 B CN 110746607B
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spandex
isolating
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base material
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CN110746607A (en
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孙大超
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SHANDONG DAYI CHEMICAL CO Ltd
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/42Block-or graft-polymers containing polysiloxane sequences
    • C08G77/46Block-or graft-polymers containing polysiloxane sequences containing polyether sequences
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • C08G77/14Polysiloxanes containing silicon bound to oxygen-containing groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04Polysiloxanes
    • C08G77/14Polysiloxanes containing silicon bound to oxygen-containing groups
    • C08G77/16Polysiloxanes containing silicon bound to oxygen-containing groups to hydroxyl groups
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F11/00Chemical after-treatment of artificial filaments or the like during manufacture
    • D01F11/04Chemical after-treatment of artificial filaments or the like during manufacture of synthetic polymers
    • D01F11/08Chemical after-treatment of artificial filaments or the like during manufacture of synthetic polymers of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/37Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/643Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicon in the main chain
    • D06M15/647Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicon in the main chain containing polyether sequences
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/37Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/643Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicon in the main chain
    • D06M15/65Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicon in the main chain containing epoxy groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/70Siloxanes defined by use of the MDTQ nomenclature
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/30Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/38Polyurethanes
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2200/00Functionality of the treatment composition and/or properties imparted to the textile material
    • D06M2200/40Reduced friction resistance, lubricant properties; Sizing compositions

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  • Textile Engineering (AREA)
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Abstract

The invention discloses an auxiliary product with the functions of isolating and regulating friction, which is applied to spandex spinning oil, and relates to the technical field of functional organic silicon materials3SiO0.5)a(BMe2SiO0.5)b(CMe2SiO0.5)c(DMe2SiO0.5)d(Me2SiO)e(SiO2) f, wherein A is a mixed structure of methyl and hydroxyl, B is long-chain alkyl, C is glycidyl ether group, D is polyether group, and Me is methyl. The auxiliary agent provided by the invention is characterized in that dimethyl siloxane chain links, long-chain alkyl chain links, epoxy alkyl chain links and polyether chain links are introduced on the basis of the traditional MQ silicon resin structure, and part of active hydroxyl groups are reserved, so that the auxiliary agent and spandex fibers generate chemical bonding force, and the auxiliary agent not only provides durable intermiscibility and storage stability, but also provides antistatic property and proper strand untying tension.

Description

Auxiliary product applied to spandex spinning oil agent and having effects of isolating and adjusting friction
Technical Field
The invention relates to the technical field of functional organic silicon materials, in particular to an auxiliary agent product which is applied to spandex spinning oil and plays a role in isolating and regulating friction.
Background
The spandex spinning industry in China has been a world-wide filament-producing nation with the rapid development tendency in recent years. The matched high-end spandex spinning oil is mainly prepared by Japanese ' Songben ' (China) "bamboo ' (China), ' Golston ' oil in America. The reason is that day and beauty oil agents are unique in product quality, yield and performance.
After the domestic oil agent is applied to spandex fibers, on one hand, the isolation between the fibers is poor, and as time goes on, chemical reaction type adhesion occurs between the fibers, so that the fibers cannot be used in bundle splitting, and a large amount of spandex filaments are wasted. On the other hand, the friction between the fibers is too small, so that the spinning is loose and difficult to form. The invention provides an auxiliary product for compounding and producing a spandex spinning oil agent, aiming at the problems of oiling agents in the market, wherein the auxiliary product is 'rail yarns' and 'convex fibers' which are slightly generated, and the auxiliary product is non-spinnable due to disordered yarns.
Disclosure of Invention
The invention aims to provide an auxiliary product which is applied to a spandex spinning oil agent and has the effects of isolating and adjusting friction, so as to solve the technical problem.
An assistant product applied to spandex spinning oil agent and having the effects of isolating and adjusting friction, wherein the structure of the assistant product is (A)3SiO0.5)a(BMe2SiO0.5)b(CMe2SiO0.5)c(DMe2SiO0.5)d(Me2SiO)e(SiO2) f, wherein A is a mixed structure of methyl and hydroxyl, B is long-chain alkyl, C is glycidyl ether group, D is polyether group, and Me is methyl; wherein a, b, c, d, e and f represent the number of chain links or the degree of polymerization, a is 3-10, b is 2-5, c is 2-5, d is 2-5, e is 1-5, and f is 5-8.
The preparation process of the auxiliary agent product comprises the following steps:
firstly, dissolving silicate ester, dimethyl siloxane tetramer and hydrogen-containing double seal heads in a mixed solvent, and then dropwise adding hydrochloric acid as a catalyst to carry out hydrolytic condensation at 70-80 ℃ for 30-90min to synthesize a silicon resin base material;
step two, separating an oil phase in the mixed liquid containing the silicone base material obtained in the step one to obtain a silicone crude product, and sequentially neutralizing, filtering, washing and drying the crude product to obtain the silicone base material;
and step three, carrying out hydrosilylation reaction on the silicone resin base material, the unsaturated olefin, the allyl glycidyl ether and the unsaturated polyether according to a certain proportion and sequence, and finally separating the solvent and the low-boiling-point substance.
Preferably, the mixed solvent in the first step is prepared by mixing water, an alcohol and a benzene substance, wherein the alcohol is ethanol or propanol, and the benzene substance is one of toluene, ethylbenzene or p-xylene.
Preferably, the mass ratio of the active ingredients in the silicate ester, the water, the alcohols, the benzenes, the dimethyl siloxane tetramer, the hydrogen-containing double seal heads and the hydrochloric acid in the step one is 35-42:10-13:9-11:8-10:8.5-9.2:4-7: 2.2-2.8.
Preferably, in the first step, the hydrogen-containing double end enclosure is tetramethyldihydrodisiloxane.
Preferably, the silicate in the first step is methyl orthosilicate.
Preferably, in the second step, the filtered substance is neutralized to neutrality by using sodium hydroxide, and is washed by using distilled water, and in the second step, the solvent is distilled off under reduced pressure at 150 ℃ until no liquid is distilled off.
Preferably, the solvent is distilled off under reduced pressure in the second step at 150 ℃, until no liquid is distilled off.
As a preferable scheme, the concrete operation in the third step is that xylene is used as a solvent, the silicone resin base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether are sequentially dissolved in the xylene, and a high-activity platinum catalyst is adopted to perform catalytic reaction for 6-18h at normal temperature to prepare a crude spandex oil agent intermediate
Preferably, the mass ratio of the xylene to the silicone resin base material to the unsaturated olefin to the allyl glycidyl ether to the unsaturated polyether to the platinum catalyst is 9-11:18-22:1-3:1-3:1-3:1, wherein the mass ratio of the unsaturated olefin to the allyl glycidyl ether to the unsaturated polyether is 1:1: 1. .
Preferably, the solvent and low boiling point substance are separated in the third step by distilling the solvent and the small molecular alcohol at 80-90 deg.C and 0.10-0.15MPa after the hydrosilylation reaction.
The invention has the beneficial effects that:
1. dimethyl siloxane chain links, long-chain alkyl chain links, epoxy alkyl chain links and polyether chain links are introduced on the basis of the traditional MQ silicon resin structure, and part of active hydroxyl groups are reserved, so that the dimethyl siloxane chain links, the long-chain alkyl chain links, the epoxy alkyl chain links and the polyether chain links generate chemical bonding force with spandex fibers, and the permanent intermiscibility, the storage stability and the antistatic property and the proper bundle untying tension are provided.
2. On the basis of the traditional MQ silicon resin structure, dimethyl siloxane chain links, long-chain alkyl chain links, epoxy alkyl chain links and polyether chain links are introduced, active hydroxyl groups are reserved, products with different molar masses, densities, viscosities, softening points, toughness and tackifying performances are obtained by adjusting the proportion of M, D, Q, and the toughness adjustment of the silicon resin becomes possible.
3. The long-chain alkyl structure is introduced on the basis of the traditional MQ silicon resin structure, so that the intermediate auxiliary agent has better intermiscibility with mineral oil and other auxiliary agents, the phenomenon that surface oiling agents cannot be dissociated and migrated in the long-time storage process of fiber oiling is reflected, and the condition that spandex filaments are either deformed or adhered due to the precipitation of the surface oiling agents is prevented.
4. The introduction of the epoxy alkyl on the basis of the traditional MQ silicon resin structure is beneficial to increasing the cohesive force between the filaments, so that the filament cake is not deformed and yellowed due to long-time storage.
Drawings
FIG. 1 is a schematic view of the structure of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example one
Weighing 35mg of methyl orthosilicate, 10mg of water, 9mg of ethanol, 8mg of toluene, 8.5mg of dimethyl siloxane tetramer, 4mg of tetramethyl dihydrodisiloxane and 220mg of hydrochloric acid with the mass fraction of 1% for later use;
mixing and dissolving water, ethanol and toluene to prepare a mixed solvent, dissolving silicate ester, dimethyl siloxane tetramer and a hydrogen-containing double end enclosure in the mixed solvent, dropwise adding hydrochloric acid serving as a catalyst, and performing hydrolytic condensation at 70 ℃ for 50min to synthesize a silicon resin base material;
and (2) filtering the oil phase in the mixed liquid containing the silicone base material obtained in the first step to obtain a silicone crude product, sequentially dropwise adding a sodium hydroxide solution with the mass fraction of 1% to neutralize the crude product to be neutral, then filtering again, washing the obtained solid with distilled water for three times, 5ml each time, then putting the solid in an oven, adjusting the pressure to be 1.5Mpa and the temperature to be 150 ℃ to perform pressure distillation, and evaporating until no liquid is evaporated to obtain the silicone base material.
9mg of xylene, 18mg of silicone base, 1mg of unsaturated olefin, 1mg of allyl glycidyl ether, 1mg of unsaturated polyether and 1mg of platinum catalyst were weighed out for use.
Dissolving a silicone resin base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether in xylene in sequence, carrying out catalytic reaction for 6-18h at normal temperature by adopting a high-activity platinum catalyst to prepare a rough spandex oil agent intermediate, and distilling the xylene and micromolecular alcohol at 80 ℃ and under the pressure of 0.10Mpa after the reaction is finished to obtain the silicone resin solid material.
Example two
42mg of methyl orthosilicate, 13mg of water, 11mg of propanol, 10mg of ethylbenzene, 9.2mg of dimethyl siloxane tetramer, 7mg of tetramethyl dihydrodisiloxane and 280mg of hydrochloric acid with the mass fraction of 1% are weighed for later use;
mixing and dissolving water, propanol and ethylbenzene to prepare a mixed solvent, dissolving silicate ester, dimethyl siloxane tetramer and hydrogen-containing double end enclosure in the mixed solvent, dropwise adding hydrochloric acid serving as a catalyst, and performing hydrolytic condensation at 80 ℃ for 90min to synthesize a silicon resin base material;
and (2) filtering the oil phase in the mixed liquid containing the silicone base material obtained in the first step to obtain a silicone crude product, neutralizing the crude product to be neutral by sequentially passing through a sodium hydroxide solution with the mass fraction of 1%, then filtering again, washing the obtained solid by using distilled water for three times, wherein 5ml of the distilled water is used for each time, then putting the solid in an oven, adjusting the pressure to be 1.5Mpa and the temperature to be 150 ℃ for pressure distillation, and evaporating until no liquid is evaporated out to obtain the silicone base material.
11mg of xylene, 22mg of silicone base, 3mg of unsaturated olefin, 3mg of allyl glycidyl ether, 3mg of unsaturated polyether and 1mg of platinum catalyst were weighed out for use.
Dissolving a silicone resin base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether in xylene in sequence, carrying out catalytic reaction for 8 hours at normal temperature by adopting a high-activity platinum catalyst to prepare a rough spandex oil agent intermediate, and distilling the xylene and micromolecular alcohol at 85 ℃ and under the pressure of 0.15Mpa after the reaction is finished to obtain the silicone resin solid material.
EXAMPLE III
Weighing 37mg of methyl orthosilicate, 11mg of water, 10mg of ethanol, 9mg of p-xylene, 8.6mg of dimethyl siloxane tetramer, 4.5mg of tetramethyl dihydrodisiloxane and 230mg of hydrochloric acid with the mass fraction of 1% for later use;
mixing and dissolving water, ethanol and p-xylene to prepare a mixed solvent, dissolving silicate ester, dimethyl siloxane tetramer and a hydrogen-containing double end enclosure in the mixed solvent, dropwise adding hydrochloric acid serving as a catalyst, and performing hydrolytic condensation at 72 ℃ for 45min to synthesize a silicon resin base material;
and (2) filtering the oil phase in the mixed liquid containing the silicone base material obtained in the first step to obtain a silicone crude product, neutralizing the crude product to be neutral by sequentially passing through a sodium hydroxide solution with the mass fraction of 1%, then filtering again, washing the obtained solid by using distilled water for three times, wherein 5ml of the distilled water is used for each time, then putting the solid in an oven, adjusting the pressure to be 1.5Mpa and the temperature to be 150 ℃ for pressure distillation, and evaporating until no liquid is evaporated out to obtain the silicone base material.
10mg of xylene, 20mg of silicone base, 2mg of unsaturated olefin, 2mg of allyl glycidyl ether, 2mg of unsaturated polyether and 1mg of platinum catalyst were weighed out for use.
Dissolving a silicone resin base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether in xylene in sequence, carrying out catalytic reaction for 6-18h at normal temperature by adopting a high-activity platinum catalyst to prepare a rough spandex oil agent intermediate, and distilling the xylene and micromolecular alcohol at 85 ℃ and under the pressure of 0.13Mpa after the reaction is finished to obtain the silicone resin solid material.
Example four
Weighing 38mg of methyl orthosilicate, 12mg of water, 10mg of propanol, 9mg of p-xylene, 8.7mg of dimethyl siloxane tetramer, 5.6mg of tetramethyl dihydrodisiloxane and 260mg of hydrochloric acid with the mass fraction of 1% for later use;
mixing and dissolving water, propanol and p-xylene to prepare a mixed solvent, dissolving silicate ester, dimethyl siloxane tetramer and a hydrogen-containing double end enclosure in the mixed solvent, dropwise adding hydrochloric acid serving as a catalyst, and performing hydrolytic condensation at 75 ℃ for 40min to synthesize a silicon resin base material;
and (2) filtering the oil phase in the mixed liquid containing the silicone base material obtained in the first step to obtain a silicone crude product, neutralizing the crude product to be neutral by sequentially passing through a sodium hydroxide solution with the mass fraction of 1%, then filtering again, washing the obtained solid by using distilled water for three times, wherein 5ml of the distilled water is used for each time, then putting the solid in an oven, adjusting the pressure to be 1.5Mpa and the temperature to be 150 ℃ for pressure distillation, and evaporating until no liquid is evaporated out to obtain the silicone base material.
10mg of xylene, 20mg of silicone base, 2mg of unsaturated olefin, 2mg of allyl glycidyl ether, 2mg of unsaturated polyether and 1mg of platinum catalyst were weighed out for use.
Dissolving a silicone resin base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether in xylene in sequence, carrying out catalytic reaction for 16 hours at normal temperature by adopting a high-activity platinum catalyst to prepare a rough spandex oil agent intermediate, and distilling the xylene and micromolecular alcohol at 88 ℃ and under the pressure of 0.14Mpa after the reaction is finished to obtain the silicone resin solid material.
EXAMPLE five
Weighing 40mg of methyl orthosilicate, 12mg of water, 10mg of propanol, 9mg of ethylbenzene, 9.1mg of dimethyl siloxane tetramer, 6mg of tetramethyl dihydrodisiloxane and 270mg of hydrochloric acid with the mass fraction of 1% for later use;
mixing and dissolving water, propanol and ethylbenzene to prepare a mixed solvent, dissolving silicate ester, dimethyl siloxane tetramer and hydrogen-containing double end enclosure in the mixed solvent, dropwise adding hydrochloric acid serving as a catalyst, and performing hydrolytic condensation at 78 ℃ for 88min to synthesize a silicon resin base material;
and (2) filtering the oil phase in the mixed liquid containing the silicone base material obtained in the first step to obtain a silicone crude product, neutralizing the crude product to be neutral by sequentially passing through a sodium hydroxide solution with the mass fraction of 1%, then filtering again, washing the obtained solid by using distilled water for three times, wherein 5ml of the distilled water is used for each time, then putting the solid in an oven, adjusting the pressure to be 1.5Mpa and the temperature to be 150 ℃ for pressure distillation, and evaporating until no liquid is evaporated out to obtain the silicone base material.
10mg of xylene, 20mg of silicone base, 2mg of unsaturated olefin, 2mg of allyl glycidyl ether, 2mg of unsaturated polyether and 1mg of platinum catalyst were weighed out for use.
Dissolving a silicone resin base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether in xylene in sequence, carrying out catalytic reaction for 16 hours at normal temperature by adopting a high-activity platinum catalyst to prepare a rough spandex oil agent intermediate, and distilling the xylene and micromolecular alcohol at 87 ℃ and under the pressure of 0.14Mpa after the reaction is finished to obtain the silicone resin solid material.
EXAMPLE six
Weighing 41mg of methyl orthosilicate, 12mg of water, 10mg of ethanol, 8mg of p-xylene, 8.6mg of dimethyl siloxane tetramer, 4.5mg of tetramethyl dihydrodisiloxane and 275mg of hydrochloric acid with the mass fraction of 1% for later use;
mixing and dissolving water, ethanol and p-xylene to prepare a mixed solvent, dissolving silicate ester, dimethyl siloxane tetramer and a hydrogen-containing double end enclosure in the mixed solvent, dropwise adding hydrochloric acid serving as a catalyst, and performing hydrolytic condensation at 78 ℃ for 85min to synthesize a silicon resin base material;
and (2) filtering the oil phase in the mixed liquid containing the silicone base material obtained in the first step to obtain a silicone crude product, neutralizing the crude product to be neutral by sequentially passing through a sodium hydroxide solution with the mass fraction of 1%, then filtering again, washing the obtained solid by using distilled water for three times, wherein 5ml of the distilled water is used for each time, then putting the solid in an oven, adjusting the pressure to be 1.5Mpa and the temperature to be 150 ℃ for pressure distillation, and evaporating until no liquid is evaporated out to obtain the silicone base material.
10mg of xylene, 21mg of silicone base, 2mg of unsaturated olefin, 2mg of allyl glycidyl ether, 2mg of unsaturated polyether and 1mg of platinum catalyst were weighed out for use.
Dissolving a silicone resin base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether in xylene in sequence, carrying out catalytic reaction for 17 hours at normal temperature by adopting a high-activity platinum catalyst to prepare a rough spandex oil agent intermediate, and distilling the xylene and micromolecular alcohol at 88 ℃ and under the pressure of 0.14Mpa after the reaction is finished to obtain the silicone resin solid material.
The auxiliary agent products prepared in the first embodiment, the second embodiment, the third embodiment, the fourth embodiment, the fifth embodiment and the sixth embodiment are added into spandex products to be used as a first experimental group, a second experimental group, a third experimental group, a fourth experimental group, a fifth experimental group and a sixth experimental group respectively, and a group of spandex without addition of auxiliary agent is used as a first comparative example to measure unwinding tension, resistivity and unwinding tension after high-temperature deterioration at normal temperature of the first experimental group, the second experimental group, the third experimental group, the fourth experimental group, the fifth experimental group, the sixth experimental group and the first comparative example respectively, and the results are shown in tables 1, 2 and 3, and it can be known from tables 1, 2 and 3 that the addition of the auxiliary agent provided by the invention can effectively reduce the unwinding tension of spandex, reduce the specific resistance of the spandex and reduce the unwinding tension of the spandex after high-temperature deterioration.
TABLE 1 Effect of auxiliaries on Spandex unwinding tension
Surface unwinding tension (N) Intermediate unwinding tension (N) Inner layer unwinding tension (N)
Example one 1.87 2.07 2.55
Example two 1.88 2.09 2.56
EXAMPLE III 1.84 2.03 2.52
Example four 1.86 2.06 2.54
EXAMPLE five 1.83 2.02 2.51
EXAMPLE six 1.89 2.11 2.57
Comparative example 1 2.01 2.26 2.97
TABLE 2 Effect of auxiliaries on Spandex resistivity
Specific resistance (ohm)
Example 1 1.09*1011
Example 2 1.11*1011
Example 3 1.10*1011
Example 4 1.08*1011
Example 5 1.06*1011
Example 6 1.07*1011
Comparative example 1 1.8*1011
TABLE 3 Effect of auxiliary on the yield tension of spandex after high temperature deterioration
High temperature deterioration of surface layer and rewinding tension (N) Middle layer high temperature deterioration back winding tension (N) Inner layer high temperature deterioration back winding tension (N)
Example one 2.37 3.21 3.97
Example two 2.38 3.22 3.96
EXAMPLE III 2.35 3.23 3.93
Example four 2.33 3.2 3.94
EXAMPLE five 2.39 3.22 3.99
EXAMPLE six 2.40 3.24 3.91
Comparative example 1 3.01 4.11 4.79
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims (10)

1. An auxiliary product which is applied to a spandex spinning oil agent and has the effects of isolating and regulating friction is characterized in that the structure of the auxiliary product is (A3SiO0.5) a (BMe2SiO0.5) B (CMe2SiO0.5) C (DMe2SiO0.5) D (Me2SiO) e (SiO2) f, wherein A refers to a mixed structure of methyl and hydroxyl, B refers to long-chain alkyl, C refers to glycidyl ether group, D refers to polyether group, and Me refers to methyl; wherein a, b, c, d, e and f represent the number of chain links or the degree of polymerization, a is 3-10, b is 2-5, c is 2-5, d is 2-5, e is 1-5, and f is 5-8.
2. The auxiliary product with effects of isolating and regulating friction applied in spandex spinning oil according to claim 1, characterized in that the preparation process of the auxiliary product is as follows:
firstly, dissolving silicate ester, dimethyl siloxane tetramer and hydrogen-containing double seal heads in a mixed solvent, and then dropwise adding hydrochloric acid as a catalyst to carry out hydrolytic condensation at 70-80 ℃ for 30-90min to synthesize a silicon resin base material;
step two, separating an oil phase in the mixed liquid containing the silicone base material obtained in the step one to obtain a silicone crude product, and sequentially neutralizing, filtering, washing and drying the crude product to obtain the silicone base material;
and step three, carrying out hydrosilylation reaction on the silicone resin base material, the unsaturated olefin, the allyl glycidyl ether and the unsaturated polyether according to a certain proportion and sequence, and finally separating the solvent and the low-boiling-point substance.
3. The auxiliary agent product with effects of isolating and adjusting friction applied to spandex spin finish according to claim 2, characterized in that the mixed solvent in the first step is prepared by mixing water, alcohol and benzene, wherein the alcohol is ethanol or propanol, and the benzene is one of toluene, ethylbenzene or p-xylene.
4. The auxiliary agent product with the effects of isolating and regulating friction applied to spandex spinning oil according to claim 2, characterized in that the mass ratio of active ingredients in silicate ester, water, alcohols, benzenes, dimethyl siloxane tetramers, hydrogen-containing double heads and hydrochloric acid in the first step is 35-42:10-13:9-11:8-10:8.5-9.2:4-7: 2.2-2.8.
5. The auxiliary product with effects of isolating and regulating friction for spandex spin finish according to claim 2, wherein the hydrogen-containing double end cap in step one is tetramethyldihydrodisiloxane.
6. The adjuvant product for spandex spin finish application to provide traction control and friction control as claimed in claim 2 wherein the silicate used in step one is methyl orthosilicate.
7. The auxiliary agent product with effects of isolating and regulating friction applied to spandex spin finish according to claim 2, characterized in that in step two, sodium hydroxide is used to neutralize the filtered substance to neutrality, and distilled water is used to wash the filtered substance, and in step two, the reduced pressure solvent evaporation is performed at 150 ℃ until no liquid is evaporated.
8. The auxiliary agent product with the effects of isolating and regulating friction applied to spandex spinning oil according to claim 2, characterized in that the specific operation in step three is to use xylene as a solvent, sequentially dissolve the silicone base material, unsaturated olefin, allyl glycidyl ether and unsaturated polyether in xylene, and perform catalytic reaction for 6-18h at normal temperature by using a high-activity platinum catalyst to prepare a crude spandex oil intermediate.
9. The auxiliary product with effects of isolating and regulating friction applied to spandex spinning oil according to claim 8, wherein the mass ratio of xylene to silicone base material to unsaturated olefin to allyl glycidyl ether to unsaturated polyether to platinum catalyst is 9-11:18-22:1-3:1-3:1-3:1, wherein the mass ratio of unsaturated olefin to allyl glycidyl ether to unsaturated polyether is 1:1: 1.
10. The auxiliary agent product with effects of isolating and adjusting friction applied in spandex spin finish according to claim 2, characterized in that the specific operation of separating solvent and low-boiling-point substance in step three is distillation of solvent and small-molecule alcohol at 80-90 ℃ and 0.10-0.15Mpa after hydrosilylation reaction.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101440574A (en) * 2008-12-18 2009-05-27 宁波经济技术开发区希科新材料有限公司 Oil solution for spandex spinning by dry method, and preparation and use thereof
CN101597377A (en) * 2009-06-29 2009-12-09 山东大易化工有限公司 Compound of a kind of methyl blocking co-modified with alkyl, polyether, epoxy and phenyl polysiloxane and its production and application
KR20110079299A (en) * 2009-12-31 2011-07-07 주식회사 효성 Spin finishing oil for spandex including non-ion surfactant, manufactured method thereof and spandex thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101440574A (en) * 2008-12-18 2009-05-27 宁波经济技术开发区希科新材料有限公司 Oil solution for spandex spinning by dry method, and preparation and use thereof
CN101597377A (en) * 2009-06-29 2009-12-09 山东大易化工有限公司 Compound of a kind of methyl blocking co-modified with alkyl, polyether, epoxy and phenyl polysiloxane and its production and application
KR20110079299A (en) * 2009-12-31 2011-07-07 주식회사 효성 Spin finishing oil for spandex including non-ion surfactant, manufactured method thereof and spandex thereof

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