CN105899717A - Copolymerized aramid dope-dyed yarn and method for preparing same - Google Patents
Copolymerized aramid dope-dyed yarn and method for preparing same Download PDFInfo
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- CN105899717A CN105899717A CN201480071976.6A CN201480071976A CN105899717A CN 105899717 A CN105899717 A CN 105899717A CN 201480071976 A CN201480071976 A CN 201480071976A CN 105899717 A CN105899717 A CN 105899717A
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- cation
- pigment
- yarn
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- cyano group
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/04—Pigments
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/06—Dyes
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/60—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides
- D01F6/605—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides from aromatic polyamides
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/78—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
- D01F6/80—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyamides
- D01F6/805—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyamides from aromatic copolyamides
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2401/00—Physical properties
- D10B2401/20—Physical properties optical
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Polyamides (AREA)
- Artificial Filaments (AREA)
Abstract
The present invention relates to a copolymerized aramid dope-dyed yarn and a method for preparing the same. When a copolymerized aramid yarn is prepared by adding terephthaloyl dichloride to an organic solvent in which an aromatic diamine having a cyano group is dissolved, followed by a reaction, to polymerize a polymerization solution containing a copolymerized aramid polymer, and then spinning and solidifying the polymerization solution, a copolymerized aramid dope-dyed yarn is prepared by adding a dye having a cation during the polymerization process of the polymerization solution containing the copolymerized aramid polymer. Deterioration in the polymerization degree of the copolymerized aramid polymer or deterioration in the dissolubility of the polymerization solution due to the addition of the dye to the polymerization solution can be effectively prevented. Further, according to the copolymerized aramid dope-dyed yarn and the method, when a copolymerized aramid polymer having a cyano(-CN) group and a dye having a cation are bonded by a hydrogen bond to form a liquid crystal during the polymerization process of the polymerization solution containing the copolymerized aramid polymer, the behavior together with a main chain of the copolymerized aramid polymer is possible, thereby enhancing the color strength, color fastness to light, and color fastness to washing of the copolymerized aramid doped-dyed yarn.
Description
Technical field
The present invention relates to a kind of copolymer aramid solution dyeing yarn and preparation method thereof, more particularly, to one
Plant when utilizing spinning nozzle that the polymeric solution comprising copolymer aramid polymer carries out spinning by being polymerized
In solution, mixing has the pigment of cation and has intensity of colour and the look of excellence without using sulfuric acid to prepare
The method of the copolymer aramid solution dyeing yarn of fastness.
Background technology
Aromatic polyamide is commonly called aramid fiber, passes through amide groups (-CONH) including having wherein phenyl ring
The p-aramid fiber of the structure that straight line connects and the meta virtue with the attachment structure different from described p-aramid fiber
Synthetic fibre.
Described p-aramid fiber has characteristic such as high intensity, high resiliency and the lower shrinkage of excellence.Due to contraposition
Aramid fiber has the Thin cable that sufficiently high intensity makes thickness prepared therefrom be about 5mm can promote two tons
Vehicle, be therefore widely used in the various application of shellproof and aerospace advanced industry.
Additionally, aramid fiber meeting carbonization and blackening more than 500 DEG C, therefore in the field needing high-fire resistance energy
Also focus is become.
Korean patent registration No. 10-0910537 that the preparation method of aramid fiber has had the applicant
In illustrate fully.According to this registration patent, mixed by dissolving aromatic diamine preparation in polymer solvent
Close solution, then by adding aromatic diacid in above-mentioned solution to prepare aramid fiber polymeric compound.Hereafter,
It is dissolved in sulfuric acid solvent to prepare spinning solution by described aramid fiber polymeric compound, by this spinning solution spinning,
Carry out the most successively solidifying, cleaning and drying process, be thus finally completed aramid fiber.
But, if preparing aramid fiber, the aramid fiber polymeric compound system of solid state according to above-mentioned operation
Standby and it is dissolved in again to prepare spinning solution in sulfuric acid solvent, then it is carried out spinning.Cause
This, manufacture process becomes complicated, harmful, and can cause the most durable due to the corrosion of equipment
Property reduce problem.
Additionally, due to there is the aramid fiber polymeric compound of high chemical resistance for dissolving and remove after spinning
Sulfuric acid solvent often result in environmental pollution, it suitably should be processed after usage.For processing
The expense of this type of sulfuric acid consumed generally reduces the economic advantages of aramid fiber.
In order to solve the problems referred to above, Korean patent registration No. 10-171994 discloses one and directly utilizes copolymerization
Aramid fiber polymeric solution as spinning solution because of the method preparing aramid fiber without sulfuric acid solvent.
More specifically, in above-mentioned routine techniques, aramid fiber is by joining it by paraphthaloyl chloride
In be dissolved with in the organic solvent of p-phenylenediamine and cyano group p-phenylenediamine so that it is react with preparation comprise copolymerization
The polymeric solution of aramid fiber polymeric compound, then carries out spinning to this polymeric solution and prepared by solidification.
But, described routine techniques brings following problem: although prepared copolymer aramid fibers has not
The advantage using sulfuric acid solvent, but due to highly crystalline performance, there is the dyeability of deterioration.
In order to solve the problems referred to above, Korean patent registration No. 10-067338 discloses one and prepares copolymer aramid
The method of fiber, when the method includes preparing copolymer aramid fibers, using polyvinylpyrrolidone as amorphous
Property polymer joins in polymeric solution, and this copolymer aramid fibers is by joining it by paraphthaloyl chloride
In be dissolved with in the organic solvent of p-phenylenediamine and cyano group p-phenylenediamine, make them react so that comprising
The polymeric solution polymerization of copolymer aramid polymer, then, carries out spinning and solidification preparation to it.But,
Although improve the dyeability of prepared copolymer aramid fibers, the method still relates to deteriorating polymeric solution
Solubility and the problem of fastness of dyeing.
As another routine techniques, have been carried out the preparation method of a kind of copolymer aramid solution dyeing yarn,
The method includes: when preparing copolymer aramid fibers, and adding will not be by the cyano group of hydrogen bond with copolymer aramid
The specific pigment that (-CN) is bonded, does not the most comprise the pigment of cation, and this copolymer aramid fibers is by will be to benzene
Dimethyl chloride is added thereto in the organic solvent being dissolved with p-phenylenediamine and cyano group p-phenylenediamine so that it is anti-
Should so that comprise copolymer aramid polymer polymeric solution polymerization, then this polymeric solution is carried out spinning and
Solidification preparation.But, the method brings the degree of polymerization of such as copolymer aramid polymer to reduce, polymeric solution
Solubility reduce and many problems of color fastness deterioration of prepared solution dyeing yarn.
Summary of the invention
Technical problem
The copolymerization aromatics that it is an object of the present invention to provide a kind of intensity of colour with excellence and color fastness gathers
Acid amides solution dyeing yarn and a kind of solubility in the degree of polymerization reduction with polymeric solution that are preventing copolymer aramid
The method preparing this copolymer aramid solution dyeing yarn while reduction.
Technical scheme
To achieve these goals, the invention provides a kind of method for preparing copolymer aramid yarn, bag
Include: when preparing copolymer aramid yarn, in the polymerization process of the polymeric solution containing copolymer aramid polymer
Add content be copolymer aramid polymer weight 0.1 weight % (wt.%) to 5 weight % have sun from
The pigment of son, this copolymer aramid yarn has the virtue of cyano group by paraphthaloyl chloride is added thereto dissolving
In the organic solvent of fragrant race diamines so that it is reaction is so that the polymerization comprising copolymerization aramid polymer is molten
Liquid is polymerized, and then this polymeric solution carries out spinning and solidification preparation.
Beneficial effect
According to the present invention, owing to joining in polymeric solution by pigment, copolymer aramid can be effectively prevented
The degree of polymerization of polymer reduces or the solubility of polymeric solution reduces.
Additionally, according to the present invention, in comprising the polymerization process of polymeric solution of copolymer aramid polymer,
The copolymer aramid polymer with cyano group (-CN) and the pigment with cation are by hydrogen bonding, and have
The pigment of cation is had to be bonded by ionic bond with the cyano group (-CN) on the main chain being positioned at copolymer aramid polymer,
And the line position common with main chain can be shown in the forming process of liquid crystal, thus improve described copolymerization
Intensity of colour, color fastness to light and the color fastness to washing of aramid fiber solution dyeing yarn.
Detailed description of the invention
Hereinafter, will be described in the present invention.
The embodiment of invention described below is presented to assist in understanding this as illustrative embodiment
Bright but be not specially limited claimed subject matter of the present invention.Additionally, those of ordinary skill in the art is come
Say and be apparent that and can carry out various modifications and variations in the technical spirit of the present invention and scope.Therefore,
The present invention includes the invention described in claim and all modifications in its equivalency range and modification.
First, in the present invention, inorganic salts are dissolved in organic solvent;Then it is added thereto to have
The aromatic diamine of cyano group (CN-).
Wherein, the aromatic diamine described in cyano group (CN-) can include the mol ratio with 1:9 to 9:1
The p-phenylenediamine dissolved and the solution of cyano group p-phenylenediamine, or the solution of single cyano group-p-phenylenediamine.
Described organic solvent can include such as, METHYLPYRROLIDONE (NMP), N, N-dimethyl second
Acid amides (DMAC), hexamethyl phosphoramide (HMPA), N, N, N ', N '-tetramethylurea (TMU), N, N-diformazan
Base formamide (DMF) or their mixture.
Adding inorganic salts is the degree of polymerization in order to increase aromatic polyamide, and inorganic salts can include such as alkali
Metal halide salt or alkaline earth metal halide salt, such as CaCl2, LiCl, NaCl, KCl, LiBr and KBr,
They can be individually or with more than two of which being added in combination.
Preferably, the addition of inorganic salts is the 2wt.% to 5wt.% of weight of described organic solvent.
Then, paraphthaloyl chloride join described in comprise the aromatic diamine with cyano group organic solvent
In mole identical with the mole of the aromatic diamine with cyano group added and be dissolved in wherein.
Copolymer aramid polymer is comprised with preparation additionally, added in described organic solvent by the pigment with cation
Polymeric solution.
The described pigment with cation has following typical structure, but is not limited thereto.
There is azo alkaline as C.I. alkali blue 64, the C.I. of pigment precursor (a coloring matter base)
Red 22.
C.I. alkali blue 64
The most alkaline red 22
There is azine and the azo compound C.I. basic black 2 as pigment precursor.
C.I. basic black 2
There is azine and the piperazine compound C.I. basic black 7 as pigment precursor.
C.I. basic black 7
There is piperazine as the C.I. alkali blue 10 of pigment precursor, C.I. alkali blue 12, C.I. Blue 74.
C.I. alkali blue 10
C.I. alkali blue 12
C.I. Blue 74
There is thiazine as the C.I. alkali blue 24 of pigment precursor, C.I. alkali blue 25.
C.I. alkali blue 24
C.I. alkali blue 25
There is anthraquinone as the C.I. alkali blue 47 of pigment precursor, C.I. alkali blue 22.
C.I. alkali blue 47
C.I. alkali blue 22
Have that bisazo is red 32 as the C.I. alkalescence of pigment precursor, C.I. alkali red 1:1 11.
The most alkaline red 32
C.I. alkali red 1:1 11
There is the phthalocyanine C.I. alkali blue 140 as pigment precursor.
C.I. alkali blue 140
Preferably, there is described in the weight that addition is copolymer aramid polymer of the pigment of cation
0.1wt.% to 5wt.%.If described addition is less than 0.1wt.%, intensity of colour is weak, and if addition surpasses
Crossing 5wt.%, the physical property of fiber can deteriorate.
Then, the polymeric solution of above-mentioned preparation is directly being used as spinning solution and to pass through spinning nozzle
After being extruded, fragrant to prepare thread copolymerization by the polymeric solution using coagulator solidification to be extruded
Synthetic fibre solution dyeing yarn.
In the polymerization process of the described polymeric solution comprising copolymer aramid polymer, when introducing have cloudy from
When the pigment of son replaces the pigment with cation, cyano group (-CN) has strong electronegativity, thus to having the moon
The anion sulfo group of the pigment of ion shows repulsive force.Therefore, the pigment with anion can not deposit
On polymer but discharge together with solvent, do not show face in coloring level in level of pollution
Look and intensity of colour, color fastness to light and the color fastness to washing of copolymer aramid solution dyeing yarn is had the most bad
Change.
The example of the described pigment with anion is as follows.
C.I. alkalescence acid blue 25
C.I. alkalescence azogeramine 38
C.I. alkalescence acid black 60
It is any that the copolymer aramid solution dyeing yarn of the present invention can include having above in the pigment of cation
A kind of more than or two of which combination.
Described there is cation pigment can be have cation pigment, have cation dyestuff or
The pigment with cation and the mixture of the dyestuff with cation.
Can be comprised by prepared according to the methods of the invention copolymer aramid solution dyeing yarn and there is cation
Pigment, therefore there is the excellent intensity of colour of at least 50 and the excellent color fastness to light of 4 grades to 5 grades
And color fastness to washing.Additionally, described copolymer aramid polymer does not shows the reduction of the degree of polymerization, therefore have
There is the high intensity of 28g/d to 35g/d.
Hereinafter, the present invention will be more fully described with reference to embodiment and comparative example.
Embodiment 1
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor including described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. basic black 2 (relative to the weight of copolymer aramid polymer) of chlorine and 0.3wt.% comprises copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 2
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the cyano group p-phenylenediamine of 100mol% the most in the reactor and dissolve with system
Standby mixed solution.
Then, in the reactor including described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 22 (relative to the weight of copolymer aramid polymer) of chlorine and 1.5wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 3
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor including described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 64 (relative to the weight of copolymer aramid polymer) of chlorine and 3wt.% comprises copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 4
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the cyano group p-phenylenediamine of 100mol% the most in the reactor and dissolve with system
Standby mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
C.I. red 22 (relative to the weight of copolymer aramid polymer) of alkalescence of chlorine and 4.9wt.% comprise copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 5
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. basic black 7 (relative to the weight of copolymer aramid polymer) of chlorine and 0.3wt.% comprises copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 6
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. Blue 74 (relative to the weight of copolymer aramid polymer) of chlorine and 1.5wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 7
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 24 (relative to the weight of copolymer aramid polymer) of chlorine and 3wt.% comprises copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 8
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 25 (relative to the weight of copolymer aramid polymer) of chlorine and 4.9wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 9
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 47 (relative to the weight of copolymer aramid polymer) of chlorine and 1.5wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 10
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
C.I. red 32 (relative to the weight of copolymer aramid polymer) of alkalescence of chlorine and 3wt.% comprise copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 11
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali red 1:1 11 (relative to the weight of copolymer aramid polymer) of chlorine and 4.9wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 12
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 140 (relative to the weight of copolymer aramid polymer) of chlorine and 0.3wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 13
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 10 (relative to the weight of copolymer aramid polymer) of chlorine and 0.3wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Embodiment 14
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. alkali blue 12 (relative to the weight of copolymer aramid polymer) of chlorine and 3wt.% comprises copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Comparative example 1
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, add in the reactor comprising described mixed solution the paraphthaloyl chloride of 100mol% with
Preparation comprises the polymeric solution of copolymer aramid polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Fiber.
By adding the above-mentioned dye (C.I. of 0.2g in the distilled water of 100ml and the glacial acetic acid of 1.2ml
Alkalescence red 22) prepare basic-dyeable fibre, the copolymer aramid fibers of 0.5g prepared as described above is injected and comprises this
In the dye bath of basic-dyeable fibre, and dye 1 hour at 100 DEG C, then it be carried out and be dried.
The intensity of colour of the copolymer aramid dyed yarn prepared by evaluation, fast light and color fastness to washing, and its result
Illustrate in Table 1.
Comparative example 2
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the cyano group p-phenylenediamine of 100mol% the most in the reactor and dissolve with system
Standby mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The polyvinyl pyridine (relative to the weight of copolymer aramid polymer) of chlorine and 57wt.% comprises copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Fiber.
By adding the above-mentioned dye (C.I. of 0.2g in the distilled water of 100ml and the glacial acetic acid of 1.2ml
Alkalescence red 22) prepare basic-dyeable fibre, the copolymer aramid fibers of 0.5g prepared as described above is injected and comprises this
In the dye bath of basic-dyeable fibre, and dye 1 hour at 100 DEG C, then it be carried out and be dried.
The intensity of colour of the copolymer aramid dyed yarn prepared by evaluation, fast light and color fastness to washing, and its result
Illustrate in Table 1.
Comparative example 3
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. acid blue 25 (relative to the weight of copolymer aramid polymer) of chlorine and 0.3wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Comparative example 4
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. azogeramine 38 (relative to the weight of copolymer aramid polymer) of chlorine and 2wt.% comprises copolymerization with preparation
The polymeric solution of aramid fiber polymeric compound.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
Comparative example 5
The CaCl of 3wt.% will be comprised2METHYLPYRROLIDONE (NMP) organic solvent nitrogen injection atmosphere
Under reactor in, introduce the p-phenylenediamine of 50mol% and the cyano group of 50mol% the most in the reactor
P-phenylenediamine also dissolves to prepare mixed solution.
Then, in the reactor comprising described mixed solution, it is simultaneously introduced the paraphenylene terephthalamide of 100mol%
The C.I. acid black 60 (relative to the weight of copolymer aramid polymer) of chlorine and 4wt.% comprises copolymerization virtue with preparation
The polymeric solution of synthetic fibre polymer.
Hereafter, after being extruded by polymeric solution by spinning nozzle, air gap and coagulator order are by spinning
Silk spinning head, thus form the multifilament that line density is 3,000 danier.The pressure of filament spinning component is 2,800psi
And spinning speed is 600mpm (m/min).
Hereafter, cleaning multifilament, then the drying drum of the temperature by being set as 150 DEG C is dried and stretches institute
The multifilament cleaned.The multifilament of drawn through Overheating Treatment and winding, thus prepares copolymer aramid at 250 DEG C
Solution dyeing yarn.
The intensity of colour of copolymer aramid solution dyeing yarn prepared by evaluation, fast light and color fastness to washing, and its
Result illustrates in Table 1.
[table 1]
The intensity of colour and the color fastness that illustrate in table 1 above are evaluated by following method.
Intensity of colour
Intensity of colour determines by measuring color according to KS K 0205.More specifically, aramid fiber is intensive
Be wound on the little card of a size of 7.5cm width and 6.5cm length, then utilize spectrophotometer
(Konica-Minolta CM-3600d) measures the color of aramid fiber under d 65 illuminant with the visual angles of 10 degree.
Herein, the value measured is the mean value that three values measured at diverse location calculate.
Blue tristimulus value(s)
Green tristimulus value(s)
Red tristimulus value(s)
λ: wavelength
K: absorption coefficient
S: scattering coefficient
R: reflectivity
Color fastness to light
Color fastness to light measures according to 206KS K 0700, and color changes based on utilizing spectrophotometer
The mensuration of the color variation grades of KS K ISO 105-A05 determines.
Color fastness to washing
Color fastness to washing measures according to KS K ISO 105-C06, and the face of the textile material after testing
Discoloration mensuration based on the color variation grades utilizing spectrophotometer KS K ISO 105-A05 determines.
Commercial Application
Copolymer aramid solution dyeing yarn according to the present invention can effectively serve as protective gloves or protection
The raw material of clothes.
Claims (13)
1. a copolymer aramid solution dyeing yarn, this copolymer aramid solution dyeing yarn is by by paraphenylene terephthalamide
Chlorine is added thereto in the organic solvent dissolving the aromatic diamine with cyano group so that it is reaction is so that comprising
The polymeric solution polymerization of copolymer aramid polymer, then, carries out spinning and solidification is made this polymeric solution
It is standby,
Wherein, described yarn comprises the pigment with cation, thus has the intensity of colour of more than 50.
2. yarn as claimed in claim 1, wherein, described in there is cation the content of pigment be described
The 0.1wt.% to 5wt.% of the weight of copolymer aramid polymer.
3. yarn as claimed in claim 1, wherein, the color fastness to light of described yarn is 4 grades to 5 grades.
4. yarn as claimed in claim 1, wherein, the color fastness to washing of described yarn is 4 grades to 5 grades.
5. yarn as claimed in claim 1, wherein, described in have the pigment of cation be selected from C.I. alkali
Property black 2, C.I. alkali blue 22, C.I. alkali blue 64, C.I. alkalescence is red 22, C.I. basic black 7, C.I. alkalescence
Indigo plant 10, C.I. alkali blue 12, C.I. Blue 74, C.I. alkali blue 24, C.I. alkali blue 25, C.I. alkalescence
Blue 47, C.I. alkalescence is red 32, at least one in C.I. alkali red 1:1 11 and C.I. alkali blue 140.
6. yarn as claimed in claim 1, wherein, described in have the pigment of cation be to have cation
Pigment, there is the dyestuff of cation and there is the pigment of cation and there is dyestuff mixed of cation
Compound.
7. for the method preparing copolymer aramid yarn, including: paraphthaloyl chloride is added thereto molten
In the organic solvent of the aromatic diamine that solution has cyano group;It is made to react so that comprising copolymer aramid polymer
Polymeric solution polymerization, then, this polymeric solution is carried out spinning and solidification,
Wherein, in the polymerization process of the described polymeric solution comprising copolymer aramid polymer, addition has sun
The pigment of ion.
8. method as claimed in claim 7, wherein, described in there is cation the addition of pigment be
The 0.1wt.% to 5wt.% of the weight of described copolymer aramid polymer.
9. method as claimed in claim 7, wherein, described in have the pigment of cation be selected from C.I.
Basic black 2, C.I. alkali blue 22, C.I. alkali blue 64, C.I. alkalescence is red 22, C.I. basic black 7, C.I.
Alkali blue 10, C.I. alkali blue 12, C.I. Blue 74, C.I. alkali blue 24, C.I. alkali blue 25, C.I.
Alkali blue 47, C.I. alkalescence is red 32, at least one in C.I. alkali red 1:1 11 and C.I. alkali blue 140.
10. method as claimed in claim 7, wherein, described in have the pigment of cation be to have sun
The pigment of ion, there is the dyestuff of cation and there is the pigment of cation and there is the dyestuff of cation
Mixture.
11. methods as claimed in claim 7, wherein, described dissolving has cyano group in organic solvent
Aromatic diamine by p-phenylenediamine and cyano group p-phenylenediamine that mol ratio is 1:9 to 9:1 have been dissolved in
Prepared by machine solvent.
12. methods as claimed in claim 7, wherein, described dissolving has cyano group in organic solvent
Aromatic diamine by cyano group p-phenylenediamine being separately dissolved in organic solvent preparation.
13. methods as claimed in claim 7, wherein, paraphthaloyl chloride with the virtue with cyano group
The mole that the mole of fragrant race diamines is identical is added thereto dissolves the having of aromatic diamine with cyano group
In machine solvent.
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KR20130166398 | 2013-12-30 | ||
PCT/KR2014/012809 WO2015102297A1 (en) | 2013-12-30 | 2014-12-24 | Copolymerized aramid dope-dyed yarn and method for preparing same |
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US (1) | US20180195207A1 (en) |
EP (1) | EP3091107B1 (en) |
JP (1) | JP6185184B2 (en) |
KR (1) | KR102070137B1 (en) |
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CN108841199A (en) * | 2018-05-31 | 2018-11-20 | 韩学民 | A kind of production technology of phthalocyanine blue series dyes alkali blue 140 |
CN109183179A (en) * | 2018-09-19 | 2019-01-11 | 超美斯新材料(淮安)有限公司 | A kind of preparation method of meta-aramid colored fibre |
CN109594177A (en) * | 2019-02-22 | 2019-04-09 | 江苏工匠服饰科技有限公司 | A kind of inflaming retarding fabric and preparation method thereof |
CN112281244A (en) * | 2020-11-23 | 2021-01-29 | 蓝星(成都)新材料有限公司 | Preparation method of stock solution dyed aramid 1414 fibers |
CN115821417A (en) * | 2021-09-17 | 2023-03-21 | 中国石油化工股份有限公司 | Preparation method of copolymerized self-coloring aramid fiber and copolymerized self-coloring aramid fiber |
CN116988184A (en) * | 2023-07-21 | 2023-11-03 | 江苏新视界先进功能纤维创新中心有限公司 | Polymer coloring method, spinning color paste, spinning solution and colored fiber |
CN117004018A (en) * | 2023-08-22 | 2023-11-07 | 江苏新视界先进功能纤维创新中心有限公司 | Polymer coloring method, spinning solution and colored fiber |
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Publication number | Priority date | Publication date | Assignee | Title |
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JP7342068B2 (en) * | 2020-06-30 | 2023-09-11 | 住友化学株式会社 | Composition |
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Also Published As
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JP2017504731A (en) | 2017-02-09 |
BR112016015170B1 (en) | 2022-01-18 |
KR102070137B1 (en) | 2020-01-28 |
EP3091107A1 (en) | 2016-11-09 |
JP6185184B2 (en) | 2017-08-23 |
US20180195207A1 (en) | 2018-07-12 |
WO2015102297A1 (en) | 2015-07-09 |
BR112016015170A2 (en) | 2017-08-08 |
CN105899717B (en) | 2018-01-19 |
KR20150079425A (en) | 2015-07-08 |
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EP3091107B1 (en) | 2019-02-13 |
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