Detailed Description
In a preferred embodiment, the functional finish copolymer of the present invention comprises the following copolymerized units:
1) 40-70 mass% of acrylate modified polyurethane copolymerization units;
2) 20-30 mass% of modified casein copolymerization units;
3) 10-30 mass% of aminopolyethylene glycol acrylate copolymerized units.
In a more preferred embodiment, in the functional finishing agent copolymer, the acrylate-modified polyurethane copolymerized unit is one or more selected from hydroxyl C2-3 alkyl (meth) acrylate-modified aqueous polyurethane copolymerized units. The hydroxy C2-3 alkyl (meth) acrylate is hydroxyethyl (meth) acrylate and/or hydroxypropyl (meth) acrylate.
In a more preferred embodiment, the aminopolyethylene glycol acrylate has a weight average molecular weight of 1000 to 10000, preferably 2000 to 8000.
In a preferred embodiment, the process for preparing the functional finish copolymer of the present invention comprises the steps of:
1) Preparing acrylate modified polyurethane;
2) Preparing casein liquid;
3) Preparing amino polyethylene glycol acrylate aqueous solution;
4) Dissolving an amphoteric emulsifier and a nonionic emulsifier in water, adding 5-15% of the acrylate modified polyurethane prepared in 1), all of the casein solution prepared in 2) and 5-15% of the amino polyethylene glycol acrylate aqueous solution prepared in 3), and stirring to prepare a pre-emulsion;
5) Heating the pre-emulsion prepared in the step 4) to 50-70 ℃, dripping 30-35% of the aqueous solution of the free radical initiator, keeping the temperature basically unchanged in the dripping process, and preserving the heat for 10-50min after finishing dripping;
6) Heating to 70-90 ℃, simultaneously dripping the rest 1), 3) and the free radical initiator aqueous solution, keeping the temperature basically unchanged in the dripping process, dripping for 2-4h, keeping the temperature for 1-3h after finishing dripping, and carrying out polymerization.
In a more preferred embodiment, the incubation is continued for 20 to 40min after the end of the dropwise addition in step 5), and the temperature is raised to 75 to 85 ℃ in step 6).
In a more preferred embodiment, the amphoteric emulsifier includes, but is not limited to, one or more of C12-18 alkyl dihydroxyethyl betaine, cocamidopropyl betaine, soya amidopropyl betaine, N-dodecylalanine, N-octadecylalanine, N-dodecyl-N- (2-hydroxy-3-sulfopropylidene) dimethylammonium.
In a more preferred embodiment, the nonionic emulsifier comprises one or more of fatty alcohol polyoxyethylene ether (5-40 EO), isomeric alcohol polyoxyethylene ether (3-15 EO).
In a more preferred embodiment, the free radical initiator is one of ammonium sulfate and potassium persulfate, preferably potassium persulfate.
The functional finishing agent prepared by the invention has good stability, the moisture absorption and moisture permeability of the nylon fabric are obviously improved after the finishing agent is treated, and the nylon fabric has soft hand feeling and excellent washability.
Examples
The invention will be further illustrated with reference to the following specific examples. It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. Further, it should be understood that various changes or modifications of the present invention may be made by those skilled in the art after reading the teaching of the present invention, and such equivalents may fall within the scope of the present invention as defined in the appended claims.
In the present application,% means% by weight unless otherwise specified.
Raw materials used in the examples: the waterborne polyurethane prepolymer is Toluene Diisocyanate (TDI) polyester prepolymer (NCO content is 5.8-6.5%) and Tantawawa company; the fabric is nylon woven fabric and is sold in the market; the thickening agent is SeatexPT-20N of Shanghai Yayun science and technology, and the rest are common commercial products.
The performance measurement and the application effect in each example were measured and evaluated as follows:
1. fabric treatment process
The padding process comprises the following steps: first soaking and first rolling → 150 ℃ for 2min, dosage: 40g/L
The impregnation process comprises the following steps: impregnation (50 ℃ × 30 min) → dewatering and drying (105 ℃.) → setting (150 ℃ × 1 min), amount: 4% o.w.f
The coating process comprises the following steps:
printing a magnetic rod pressure of 40V, a speed of 30m/min and a size by adopting a flat screen magnetic rod printing small prototype:
120 meshes.
Knife coating → oven drying (150 ℃,2 min), functional finish copolymer amount: 2 percent of thickening agent and the balance of water.
2. Hydrophilicity
According to GB/T21655.1-2008. Expressed as drip diffusion time and wicking height. The shorter the drip diffusion time, the higher the wicking height indicating better hydrophilicity.
3. Moisture permeability
According to GB/T21655.1-2008. The moisture permeability is more than or equal to 8000 g/(m) 2 D) shows the moisture permeability effect, the greater the moisture permeability, the better the moisture permeability effect.
4. Washing method
Performed according to AATCC 135.
5. Hand feel evaluation
The hand feeling of the original cloth is taken as 1 point, and the average value is taken by integrating the hand feeling evaluation results of 5 persons (1-5 points, the worst point for 1 point and the best point for 5 points).
Example 1
Adding 16.5g of waterborne polyurethane prepolymer into a four-neck flask provided with a stirrer, a thermometer and a reflux condenser, heating to 65 ℃, dropwise adding 3.5g of hydroxyethyl acrylate ethanol solution, keeping the temperature for 1h after dropwise adding, adjusting the viscosity of the system by using acetone in the reaction process, cooling to 40 ℃, neutralizing by using triethylamine, reacting for 1h, and cooling to room temperature. And adding 60g of water, stirring at a high speed for water dispersion, and finally removing acetone under reduced pressure to obtain the acrylate modified waterborne polyurethane.
Adding 6.4g of casein and 25.6g of water into a four-neck flask provided with a stirrer, a thermometer and a reflux condenser, heating to 65 ℃, slowly stirring to swell the casein, adding a certain amount of triethanolamine to adjust the pH to be about =7.5, and continuously keeping the water temperature and stirring for 1h after the casein is fully swelled to be transparent liquid to obtain casein liquid.
An aqueous aminopolyethylene glycol acrylate solution was prepared by mixing 3.5g of aminopolyethylene glycol acrylate (weight average molecular weight: 8000) and 24.5g of water for subsequent use.
And adding 1.2g of dodecyl dihydroxy ethyl betaine, 1g of lauryl polyoxyethylene ether (15 EO) and 10g of deionized water into another four-neck flask, stirring for dissolving, adding 8g of the acrylic ester modified waterborne polyurethane, 32g of the casein solution and 2.8g of the amino polyethylene glycol acrylate aqueous solution, and stirring at a high speed for 30min to obtain a pre-emulsion.
Heating the pre-emulsion to 65 ℃, slowly dripping 1g of 10% potassium persulfate aqueous solution, keeping the temperature unchanged in the dripping process, finishing dripping, and keeping the temperature for 20min.
And (2) continuously heating to 78 ℃, respectively dripping 72g of acrylic acid modified waterborne polyurethane, 25.2g of amino polyethylene glycol acrylate aqueous solution and 2g of 10% potassium persulfate aqueous solution for 2 hours, keeping the temperature unchanged in the dripping process, and after the dripping is finished, carrying out heat preservation reaction for 1.5 hours to obtain the finishing agent 1.
Example 2
Adding 10.2g of waterborne polyurethane prepolymer into a four-neck flask provided with a stirrer, a thermometer and a reflux condenser, heating to 65 ℃, dropwise adding 2.5g of an ethanol solution of hydroxypropyl acrylate, keeping the temperature for 1h after dropwise adding, adjusting the viscosity of the system by using acetone in the reaction process, cooling to 40 ℃, neutralizing by using triethylamine, reacting for 1h, and cooling to room temperature. Adding 38g of water, stirring at a high speed for water dispersion, and finally removing acetone under reduced pressure to obtain the acrylate modified waterborne polyurethane.
Adding 8.5g of casein and 34g of water into a four-neck flask provided with a stirrer, a thermometer and a reflux condenser, heating to 65 ℃, slowly stirring to swell the casein, adding a certain amount of triethanolamine to adjust the pH to be about =7.5, and continuously keeping the water temperature to stir for 1h after the casein is fully swelled to be a transparent liquid to obtain a casein liquid.
9g of aminopolyethylene glycol acrylate (weight average molecular weight: 2000) and 63g of water were mixed to prepare an aminopolyethylene glycol acrylate aqueous solution for use.
And adding 1.4g of cocamidopropyl betaine, 0.9g of isomeric tridecanol polyoxyethylene ether (5 EO) and 10g of deionized water into another four-neck flask, stirring for dissolving, adding 5.07g of the acrylic ester modified waterborne polyurethane, 42.5g of the casein solution and 7.2g of the amino polyethylene glycol acrylate aqueous solution, and stirring at a high speed for 40min to obtain a pre-emulsion.
Heating the pre-emulsion to 65 ℃, slowly dripping 1g of 10% potassium persulfate aqueous solution, keeping the temperature unchanged in the dripping process, finishing dripping, and keeping the temperature for 40min.
And (3) continuously heating to 78 ℃, respectively dripping 45.63g of acrylic acid modified waterborne polyurethane, 64.8g of amino polyethylene glycol acrylate aqueous solution and 2g of 10% potassium persulfate aqueous solution for 2 hours, ensuring the temperature to be unchanged in the dripping process, and after the dripping is finished, carrying out heat preservation reaction for 2.5 hours to obtain the finishing agent 2.
Example 3
Adding 13.5g of waterborne polyurethane prepolymer into a four-neck flask provided with a stirrer, a thermometer and a reflux condenser, heating to 65 ℃, dropwise adding 2.8g of hydroxyethyl acrylate ethanol solution, keeping the temperature for 1h after dropwise adding, adjusting the viscosity of the system by using acetone in the reaction process, cooling to 40 ℃, neutralizing by using triethylamine, reacting for 1h, and cooling to room temperature. And adding 48.9g of water, stirring at a high speed for water dispersion, and finally decompressing to remove acetone to obtain the acrylate modified waterborne polyurethane.
Adding 7.5g of casein and 30g of water into a four-neck flask provided with a stirrer, a thermometer and a reflux condenser, heating to 65 ℃, slowly stirring to swell the casein, then adding a certain amount of triethanolamine to adjust the pH to be about =7.5, and continuously keeping the water temperature and stirring for 1h after the casein is fully swelled to be a transparent liquid to obtain a casein liquid.
6g of aminopolyethylene glycol acrylate (weight average molecular weight: 3400) and 42g of water were mixed to prepare an aminopolyethylene glycol acrylate aqueous solution for use.
And adding 1.4g N-dodecyl-N- (2-hydroxy-3-sulfopropylene) dimethylammonium, 1g of isomeric dodecyl polyoxyethylene ether (8 EO) and 10g of deionized water into another four-neck flask, stirring for dissolving, adding 6.52g of the acrylic modified waterborne polyurethane, 37.5g of the casein solution and 4.8g of the amino polyethylene glycol acrylate aqueous solution, and stirring at high speed for 30min to obtain a pre-emulsion.
Heating the pre-emulsion to 65 ℃, slowly dripping 1g of 10% potassium persulfate aqueous solution, keeping the temperature unchanged in the dripping process, finishing dripping, and keeping the temperature for 30min.
And continuously heating to 78 ℃, respectively dripping 58.68g of the acrylic acid modified waterborne polyurethane, 43.2g of the amino polyethylene glycol acrylate aqueous solution and 2g of 10% potassium persulfate aqueous solution for 2 hours, ensuring the temperature to be unchanged in the dripping process, and after the dripping is finished, carrying out heat preservation reaction for 3 hours to obtain the finishing agent 3.
The commercially available nylon woven fabrics were subjected to each process using the finishing agents 1 to 3 prepared in examples, and then the properties were measured. The application properties are shown in tables 1, 2 and 3.
TABLE 1 comparison of hydrophilicity and washability
In addition, the blank sample is that the fabric is treated by only adopting clear water according to the process.
TABLE 2 comparison of moisture permeability and washability
In addition, the blank sample is that the fabric is treated by only adopting clear water according to the process.
TABLE 3 Style of hand feeling
In addition, the method is characterized in that: the examples were prepared by coating processes, commercial silicone products were padded according to their product specifications, and controls were prepared by coating processes using only thickeners
As can be seen from the data in tables 1, 2 and 3, the functional finishing agent copolymer prepared by the invention has good hydrophilicity and moisture permeability, good hand feeling, excellent washability and good style after finishing the nylon fabric, is suitable for the processes of dipping, padding and coating, and has wide market prospect.