CN100348631C - Acid dye dyeable polyacrylonitrile resin production method - Google Patents
Acid dye dyeable polyacrylonitrile resin production method Download PDFInfo
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- CN100348631C CN100348631C CNB2004100538538A CN200410053853A CN100348631C CN 100348631 C CN100348631 C CN 100348631C CN B2004100538538 A CNB2004100538538 A CN B2004100538538A CN 200410053853 A CN200410053853 A CN 200410053853A CN 100348631 C CN100348631 C CN 100348631C
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Abstract
The present invention relates to a method for producing acid dye dyeable polyacrylonitrile resin, which adopts water as a medium for suspension polymerization. The polymerization monomers comprise acrylonitrile, flexible modified polymerization second monomers and dyeing modified third polymerization monomers; the total amount of all polymerization monomers is taken for calculating that the charge amount of the second polymerization monomers is from 5 wt% to 15 wt%, the charge amount of the third polymerization monomers is from 1.0 wt% to 5.0 wt%, the input concentration of the total polymerization monomers is from 10 % to 50 %, reaction temperature is from 50 DEG C to 100 DEG C, and reaction time is from 1 hour to 20 hours; the third polymerization monomer is a compound which has the structural formula, wherein n is an integer from 2 to 6, R1 is a hydrogen atom or alkyl of C1 to C4, R2 and R3 are respectively an alkyl of C1 to C4, X is sulfate radical or formylic radical, m is 2 when the X is the sulfate radical, and m is 1 when the X is the formylic radical. The third polymerization monomer adopted by the present invention has a high reactivity ratio, and the third polymerization monomer has sufficient content in resin under general polymerizing condition to make the resin have high dyeing saturation value.
Description
Technical field
The present invention relates to a kind of manufacture method of acid-dyeable polyacrylonitrile resin.
Background technology
The important use of polyacrylonitrile resin is as the spinning material of making polyacrylonitrile fibre (acrylic fibers), simple polyacrylonitrile resin dyeing behavior is very poor, so as in the polyacrylonitrile resin of spinning material except second comonomer that adds flexible modification, also must add the 3rd comonomer that 5～15wt% is used for dyeing, modifying.General polyacrylonitrile resin mostly adopts methylpropene sodium sulfonate as the 3rd monomer, and it has good dyeability for cationic dyestuff.Although cationic dyestuff has abundant, the bright in luster and colour fastness advantages of higher of color, but because the performance of acrylic fibers exactly likes wool, acrylic fibers and wool blended, the mixed fabric of knitting occupy very big ratio in acrylic fibers post-treatment product, and wool should adopt matching stain to dye, blending, mix the fabric knit and force acrylic fibers and wool to carry out " with bathing " to dye, this polyacrylonitrile resin the 3rd comonomer that just requires to be used for to make this acrylic fibers can be fit to the dyeing of matching stain.In the prior art, industrial be considered to effect preferably the 3rd monomer that adopted of acid-dyeable polyacrylonitrile resin be compound with following general formula:
Wherein n is 2～8 integer, R
1Be the alkyl of hydrogen atom or C1～C6, R
2And R
3Respectively the do for oneself alkyl of C1～C6 opens as the Japanese Patent spy that clear 56-21842, spy open clear 55-8604, the spy opens clear 48-7888 and introduces.
Yet this 3rd monomeric defective is that reactivity ratio is on the low side in it and vinyl cyanide and the common copolymerization system of forming of flexible modification second monomer commonly used, it is difficult for the content that reaches enough in resin under general polymerizing condition, so that the dyeing saturation value of resin is lower, thereby influences the color and luster and the dye uptake of fiber.Although this can recently solve by improving the 3rd monomeric feeding intake, this obviously can improve production cost, and makes that the control difficulty of each co-monomer content increases in the resin.Also the someone attempts acid to be contained be dipped in the fiber by in spinning process fiber being handled with acid, thereby improves the color and luster degree and the dye uptake of acid-dyeable polyacrylonitrile fibre.The Japanese Patent spy opens the report that clear 55-8604 and the clear 48-7888 of Te Kai all have this type of research contents.But adopting this method to have another drawback, is very difficult because acid is contained equably be dipped in the fiber, and acidiferous inhomogeneous just can causing produces phenomenons such as hickie, specking after the dyeing keratin-fiber in the fiber.
Summary of the invention
The invention provides a kind of manufacture method of acid-dyeable polyacrylonitrile resin, the technical problem that it will solve is to make the 3rd monomer of dyeing, modifying have higher reactivity ratio, the 3rd monomer just has enough content in the resin that obtains under general polymerizing condition, makes the resin that makes have ideal acid dyeing saturation value.
Below be the technical scheme that the present invention solves the problems of the technologies described above:
A kind of manufacture method of acid-dyeable polyacrylonitrile resin, it is that medium carries out suspension polymerization that this method adopts water, polymerization single polymerization monomer comprises second comonomer of vinyl cyanide, flexible modification and the 3rd monomer of dyeing, modifying, is that 5～15wt%, the 3rd monomeric charging capacity are 1.0～5.0wt% in the charging capacity of all polymerization single polymerization monomer total amount second comonomers.The monomeric input concentration of total polymerization is 10～50%, and temperature of reaction is 50～100 ℃, and the reaction times is 1～20 hour.The initiator that reaction is used is water miscible Oxidizing and Reducing Agents, and the chain-transfer agent of molecular weight of being used to adjust is thio-alcohol or different alkanols compound.
Second comonomer of flexible modification is taken from a kind of in methyl acrylate, ethyl propenoate, methyl methacrylate, Jia Jibingxisuanyizhi, vinyl acetate, acrylamide, Methacrylamide, vinylbenzene, vinylchlorid or the vinylidene chloride.
The 3rd monomer of dyeing, modifying is the compound with following structural formula:
Wherein n is 2～6 integer, R
1Be the alkyl of hydrogen atom or C1～C4, R
2And R
3Respectively the do for oneself alkyl of C1～C4, X is sulfate radical or formate, m=2 when X is sulfate radical; M=1 when X is formate.
In technique scheme:
Monomeric input concentration is preferably 30～50%; Temperature of reaction is preferably 60～70 ℃; Reaction times is preferably 3～6 hours.
Oxygenant can be ammonium persulphate, Potassium Persulphate, hydrogen peroxide or sodium chlorate in the initiator, and reductive agent can be Sodium Pyrosulfite, sodium bisulfite, S-WAT, xitix or trolamine.
Chain-transfer agent can be Virahol or dodecyl mercaptans.
Described initiator amount is generally 0.05～5wt% in all polymerization single polymerization monomer total amounts, is preferably 0.2～1.0wt%.
Most of process of the present invention and prior art are basic identical, its key is to have adopted a kind of very ideal the 3rd monomer, this compound is compared with existing the 3rd monomer has structurally increased a strong electron-withdrawing group group, the existence of this group can not influence it and dye the performance of seat as matching stain, but can accelerate the copolymerization rate that this monomer and vinyl cyanide carry out radical polymerization greatly.Therefore this 3rd monomer has higher unexpectedly poly-rate in above-described copolymerization system, and this has just guaranteed that it just has enough content in resin under general polymerizing condition, thereby makes resin have higher acid dyeing saturation value.In addition, after the 3rd monomeric reactivity ratio suitably improved, it more reached unanimity with the vinyl cyanide and the second monomeric rate of gathering unexpectedly, and this makes that each co-monomer content is easy to recently be controlled by feeding intake in the resin, made the easier operation of polymerization process like this.These all make the present invention that substantial progress has compared with prior art been arranged.
Below will the invention will be further described by specific embodiment.
As previously mentioned, the present invention compared with prior art its key distinction is characterised in that and has increased a salt forming group on the 3rd monomeric structure, other each several part and the prior art of technical scheme are basic identical, and those skilled in the art are very familiar to this.Therefore in embodiment and comparative example, the contriver will give an example to this distinguishing characteristics emphatically, and those skilled in the art should know by inference, and after other situation and condition variation, therefore effect of the present invention will can not be affected.
Embodiment
[embodiment 1～8]
In the reactor that has reflux exchanger, electric mixer and electric heating temperature controller, be that medium carries out suspension polymerization with water.
Selecting vinyl acetate between to for plastic for use is second monomer, and the weight ratio that feeds intake of control vinyl cyanide and vinyl acetate between to for plastic is 92: 8, selects the 3rd required monomer for use and determines its charging capacity by required feed ratio, and it is 1 listed that concrete the 3rd monomer that adopts of each embodiment and charging capacity thereof see Table;
The total monomer input concentration is 30%;
Selecting initiator for use is the redox system of being made up of Oxidizing and Reducing Agents, and wherein oxygenant is a sodium chlorate, and reductive agent is a Sodium Pyrosulfite.The oxygenant add-on is counted 0.5wt% with all polymerization single polymerization monomer total amounts, and the add-on of reductive agent is to determine at 1.5: 1 with the mol ratio of reductive agent and oxygenant.
In reactor, drop into reaction mass by the above mode of forming to drip charging that feeds intake, and, add an amount of chain-transfer agent dodecyl mercaptans according to the molecular weight of product requirement.Control reaction temperature is 60 ℃, and the reaction times is 4 hours.After reaction finishes reaction mixture is filtered, washs, then in vacuum drying oven in 80 ℃ dry 4 hours down, obtain white powder acrylic resin product.
[comparative example 1～3]
Change the 3rd monomer and determine its charging capacity by required feed ratio, all the other are with embodiment 1～8.It is 1 listed that concrete the 3rd monomer that adopts of each comparative example and charging capacity thereof see Table.
The dyeing saturation value of the 3rd monomer content and resin sees Table 2 in the polyacrylonitrile resin that transformation efficiency in polyreaction of each embodiment and comparative example the 3rd monomer, reaction make.
Wherein, transformation efficiency is defined as:
The 3rd monomeric content is measured with the method for nucleus magnetic resonance in the polymkeric substance;
The measuring method of dyeing saturation value (the dyestuff gram number that dyes on the 100 gram polymers) is: adopt matching stain Sandolan BLUE MF-GL (Clariant provides), maximum absorption wavelength is 628nm, and bath raio is 1/100, PH=4.5～5.5 (acetic acid adjusting).Dyeing is 40 ℃ of initial temperatures, and heat-up rate is 1.0 ℃/min, to 100 ℃ of constant temperature dyeings 3 hours, naturally cools to room temperature then, washing.Measure the dyeing absorbancy and the absorbancy of raffinate afterwards that dyes of stoste before respectively with spectrophotometer, and obtain the dyeing saturation value S of polypropylene acrylic fibers resin according to the dyeing saturation value formula.
K1 in the formula: the slope of standard working curve
A1: the absorbancy of stoste before the dyeing
A2: the absorbancy of raffinate after the dyeing
B: polymeric weight
From the data of table 1 and table 2 as can be seen, comparative example 1 and embodiment 2, comparative example 2 and embodiment 3, comparative example 3 and embodiment 4 are except the 3rd monomer is different, and other polymerizing condition is identical, but the result of embodiment acquisition is significantly better than the comparative example of correspondence.
Table 1.
| The 3rd monomer | The 3rd monomeric charge amount (wt%) | |
| Embodiment 1 | Methacrylic acid N, silomate base ethyl ester vitriol | 1.0 |
| Embodiment 2 | The same | 2.0 |
| Embodiment 3 | The same | 2.5 |
| Embodiment 4 | The same | 3.0 |
| Embodiment 5 | The same | 5.0 |
| Embodiment 6 | Methacrylic acid N, N diethylin ethyl ester formate | 1.0 |
| Embodiment 7 | The same | 3.0 |
| Embodiment 8 | The same | 5.0 |
| Comparative example 1 | Methacrylic acid N, silomate base ethyl ester | 2.0 |
| Comparative example 2 | The same | 2.5 |
| Comparative example 3 | The same | 3.0 |
Table 2.
| The 3rd monomer conversion (%) | The 3rd monomer content (wt%) in the resin | The resin dyeing saturation value | |
| Embodiment 1 | 86.4 | 0.864 | 3.08 |
| Embodiment 2 | 88.5 | 1.77 | 4.42 |
| Embodiment 3 | 91.2 | 2.28 | 7.34 |
| Embodiment 4 | 92.3 | 2.77 | 8.09 |
| Embodiment 5 | 95.8 | 4.79 | 9.86 |
| Embodiment 6 | 85.4 | 0.854 | 2.98 |
| Embodiment 7 | 89.6 | 2.69 | 7.95 |
| Embodiment 8 | 92.4 | 4.62 | 9.57 |
| Comparative example 1 | 65.5 | 1.31 | 3.47 |
| Comparative example 2 | 67.2 | 1.68 | 4.26 |
| Comparative example 3 | 70.3 | 2.11 | 6.87 |
Claims (6)
1, a kind of manufacture method of acid-dyeable polyacrylonitrile resin, it is that medium carries out suspension polymerization that this method adopts water, polymerization single polymerization monomer comprises vinyl cyanide, second comonomer of flexible modification and the 3rd monomer of dyeing, modifying, charging capacity in all polymerization single polymerization monomer total amount second comonomers is 5～15wt%, the 3rd monomeric charging capacity is 1.0～5.0wt%, the monomeric input concentration of total polymerization is 10～50%, temperature of reaction is 50～100 ℃, reaction times is 1～20 hour, the initiator that reaction is used is water miscible Oxidizing and Reducing Agents, oxygenant is an ammonium persulphate, Potassium Persulphate, hydrogen peroxide or sodium chlorate, reductive agent is a Sodium Pyrosulfite, sodium bisulfite, S-WAT, xitix or trolamine, initiator amount is counted 0.05～5wt% with all polymerization single polymerization monomer total amounts, the chain-transfer agent of molecular weight of being used to adjust is thio-alcohol or different alkanols compound, second comonomer of flexible modification is taken from methyl acrylate, ethyl propenoate, methyl methacrylate, Jia Jibingxisuanyizhi, vinyl acetate, acrylamide, Methacrylamide, vinylbenzene, a kind of in vinylchlorid or the vinylidene chloride, the 3rd monomer that it is characterized in that dyeing, modifying is the compound with following structural formula:
Wherein n is 2～6 integer, R
1Be the alkyl of hydrogen atom or C1～C4, R
2And R
3Respectively the do for oneself alkyl of C1～C4, X is sulfate radical or formate, m=2 when X is sulfate radical; M=1 when X is formate.
2, the manufacture method of acid-dyeable polyacrylonitrile resin according to claim 1 is characterized in that described monomeric input concentration is 30～50%.
3, the manufacture method of acid-dyeable polyacrylonitrile resin according to claim 1 is characterized in that in described temperature of reaction be 60～70 ℃.
4, the manufacture method of acid-dyeable polyacrylonitrile resin according to claim 1 is characterized in that in the described reaction times be 3～6 hours.
5, the manufacture method of acid-dyeable polyacrylonitrile resin according to claim 1 is characterized in that at described chain-transfer agent be Virahol or dodecyl mercaptans.
6, the manufacture method of acid-dyeable polyacrylonitrile resin according to claim 1 is characterized in that counting 0.2～1.0wt% at described initiator amount with all polymerization single polymerization monomer total amounts.
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| CN100348631C true CN100348631C (en) | 2007-11-14 |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS49395A (en) * | 1972-04-17 | 1974-01-05 | ||
| CA963989A (en) * | 1970-12-28 | 1975-03-04 | Monsanto Company | Acrylic fibers having improved hot-wet properties |
| CN1037179A (en) * | 1988-04-19 | 1989-11-15 | 成都科技大学 | Preparation of modified polyvinyl fibre by chemical method |
| CN1231005A (en) * | 1996-09-20 | 1999-10-06 | 英特拉技术公司 | Process for improving polyamide, acrylic, aramid, cellulosic and polyester properties, and modified polymers produced thereby |
| CN1304417A (en) * | 1998-04-03 | 2001-07-18 | 索罗蒂亚公司 | Polyacrylonitrile particles by surfmer polymerization and sodium removal by chemical exhcnage |
| CN1304419A (en) * | 1998-04-03 | 2001-07-18 | 索罗蒂亚公司 | Polyacrylonitrile polymer treatment |
| CN1432086A (en) * | 2000-06-02 | 2003-07-23 | 德意志戴斯达纺织品及染料两合公司 | Method for coloring acrylic fibers |
-
2004
- 2004-08-19 CN CNB2004100538538A patent/CN100348631C/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA963989A (en) * | 1970-12-28 | 1975-03-04 | Monsanto Company | Acrylic fibers having improved hot-wet properties |
| JPS49395A (en) * | 1972-04-17 | 1974-01-05 | ||
| CN1037179A (en) * | 1988-04-19 | 1989-11-15 | 成都科技大学 | Preparation of modified polyvinyl fibre by chemical method |
| CN1231005A (en) * | 1996-09-20 | 1999-10-06 | 英特拉技术公司 | Process for improving polyamide, acrylic, aramid, cellulosic and polyester properties, and modified polymers produced thereby |
| CN1304417A (en) * | 1998-04-03 | 2001-07-18 | 索罗蒂亚公司 | Polyacrylonitrile particles by surfmer polymerization and sodium removal by chemical exhcnage |
| CN1304419A (en) * | 1998-04-03 | 2001-07-18 | 索罗蒂亚公司 | Polyacrylonitrile polymer treatment |
| CN1432086A (en) * | 2000-06-02 | 2003-07-23 | 德意志戴斯达纺织品及染料两合公司 | Method for coloring acrylic fibers |
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