Patent Application
20240271359
The present invention relates to a method of scouring a textile product and a method of scouring a textile product to produce a scouring-treated textile product.
Cotton is one of highly evaluated natural fibers, and is composed of pure cellulose (88 to 96.5 weight %) and other non-cellulose impurities such as waxes, pectins, hemicelluloses, and proteins. A wax having an amount of 0.4 to 1 weight % and being mainly present in the outermost layer of an unbleached cotton fiber is a material that most affects the hydrophilicity of cotton. Unbleached cotton fibers are subjected to a treatment called scouring, whereby natural hydrophobic impurities are removed and the hydrophilicity of the cotton is improved.
Generally, cotton product woven fabrics are produced by interlacing warp yarns/weft yarns. Therefore, first, producing a woven fabric starts with dividing grey yarns into warp yarns and weft yarns. Grey yarns divided into warp yarns and weft yarns are passed through various steps. Finally, the woven fabric, put on a weaving machine and finished, is inspected and subjected to a finishing step. The main steps for cotton product production are respective steps of spinning, sizing, weaving, desizing/scouring/bleaching, dyeing, and finishing. Among these steps, in respective steps of sizing, desizing/scouring, and dyeing, a large amount of water is used, and at the same time, a large amount of wastewater is discharged. It is known that the amount of wastewater discharged when clothes are produced is 20% of the world's wastewater. Reduction in the environmental load is a worldwide main issue and an environmentally friendly producing step that addresses such a wastewater problem is required.
In addition, in the above scouring step for cotton product production, a scouring method in which an organic solvent is used is known. However, an increase in the amount of the organic solvent used is not preferable in terms of reducing the environmental load, and similar to the above wastewater problem, it is necessary to reduce the amount of the organic solvent used to implement an environmentally friendly producing step.
In addition, it is known to perform fiber processing using supercritical carbon dioxide. The supercritical state can be expressed as a state of exceeding a critical temperature (Tc) and a critical pressure (Tp) unique to each compound. A fluid in this state is called a supercritical fluid, and has properties intermediate between a gas and a liquid. As shown in
As described above, in a textile product scouring step, it is desirable to realize a step of producing an environmentally friendly textile product using a solvent in place of conventionally used water or an organic solvent.
An object of the present invention is to realize a step of producing an environmentally friendly textile product using a solvent in place of conventionally used water or an organic solvent in a textile product scouring step.
The inventors conducted extensive studies in order to address the above problem, and as a result, found that the above problem can be addressed using a supercritical state carbon dioxide as a solvent in place of conventionally used water or an organic solvent, and completed the present invention. From the above features (1) to (5) of supercritical carbon dioxide, when supercritical carbon dioxide is used as a solvent in a scouring step, it is possible to realize a producing step in which no wastewater is generated, and no organic solvent is used or the amount used is reduced.
Specific aspects of the present invention are as follows.
In the method of the present invention, it is possible to realize a step of producing an environmentally friendly textile product using a solvent in place of conventionally used water or an organic solvent in a textile product scouring step.
In the present invention, “scouring” means a treatment for removing some or all substances such as oils, pastes, and natural fiber-derived waxes adhered to a textile product. In the present invention, when a numerical range is expressed using “X to Y”, the range includes the numerical values at both ends.
Hereinafter, a method of scouring a textile product and a method of scouring a textile product to produce a scouring-treated textile product according to the present invention will be described.
One embodiment of the present invention is a method of scouring a textile product, including a step (a) of bringing a fluid containing supercritical carbon dioxide into contact with the textile product to remove some or all substances adhered to the surface of the textile product. In addition, another embodiment of the present invention is a method of scouring a textile product to produce a scouring-treated textile product, including a step (a′) of bringing a fluid containing supercritical carbon dioxide into contact with the textile product before a scouring treatment to remove some or all substances adhered to the surface of the textile product before the scouring treatment.
In the present embodiment, the textile product is not particularly limited, and examples thereof include fibers, yarns, and fabrics. Examples of fibers include tows before they become yarns. The yarns are not particularly limited, and examples thereof include spun yarns, filament yarns, and mixed twisted yarns and blended yarns obtained by mixing and twisting them. Examples of fabrics include woven fabrics and knit fabrics using yarns, non-woven fabrics, and felts. In the method of the present embodiment, it is preferable to use a yarn or a fabric as a textile product.
The type of yarn is not particularly limited, and for example, natural fibers, for examples, vegetable fibers such as cotton and linen, and animal fibers such as silk and wool, and chemical fibers, for example, synthetic fibers such as polyester and acrylic, semi-synthetic fibers such as acetate, triacetate, and promix, regenerated fibers such as rayon, polynosic, cupra, and lyocell, and inorganic fibers such as glass fibers, metal fibers, and carbon fibers can be used. Two or more types of these yarns that are blended or twisted together may be used. In addition, these yarns may be single yarns, two ply yarns, three ply yarns or four or more twisted yarns. In the present embodiment, the textile product preferably contains a cotton yarn or a cotton fabric because it is suitable for producing towels. When the textile product contains a cotton yarn or a cotton fabric, and is subjected to scouring, some or all of the hydrophobic impurities present on the surface of the cotton are removed, the hydrophilicity of the cotton is improved, and thus it is possible to improve the water wettability of the textile product.
In the present embodiment, treatment conditions when a fluid containing supercritical carbon dioxide is brought into contact with the textile product are not particularly limited, and in order to perform sufficient scouring, a temperature of 20 to 150° C., 25 to 130° C., or 30 to 110° ° C. can be used, a pressure of 3 to 40 MPa, 5 to 30 MPa, or 8 to 25 MPa can be used, and a time of 1 to 800 minutes, 5 to 600 minutes, or 10 to 300 minutes can be used. The step of bringing a fluid containing supercritical carbon dioxide into contact with a textile product can be performed according to a continuous treatment.
In the present embodiment, when the scouring step is performed according to a continuous treatment, the rate of supercritical carbon dioxide flowing into a treatment container is not particularly limited, and in order to perform sufficient scouring, the flow rate is preferably 0.1 to 10 ml/min, more preferably 0.3 to 8 ml/min, and most preferably 0.5 to 6 ml/min per 1 g of fibers.
In the present embodiment, some or all substances adhered to the surface of the textile product can be removed by scouring the textile product. Examples of substances adhered to the surface of the textile product include non-cellulose impurities such as oils, pastes, waxes, pectins, hemicelluloses, and proteins and combinations of two or more thereof.
In the present embodiment, the fluid containing supercritical carbon dioxide may further contain a co-solvent. When the fluid contains a co-solvent, it is possible to further improve removability of substances adhered to the surface of the textile product than when a fluid containing no co-solvent is used, and particularly, when the textile product contains a cotton yarn or a cotton fabric, it is possible to further improve the water wettability of the textile product. The co-solvent is not particularly limited, and may include at least one selected from the group consisting of ethanol, methanol, acetone, and tetrahydrofuran. In order to improve removability of substances adhered to the surface of the textile product, the co-solvent is preferably an alcohol such as ethanol and methanol or tetrahydrofuran, and more preferably ethanol.
In the present embodiment, when a co-solvent is used, the co-solvent can be transferred as a liquid into the treatment container separately from the supercritical carbon dioxide.
When a co-solvent is used, the proportion (mol %) of the co-solvent with respect to supercritical carbon dioxide is not particularly limited, and in order to improve removability of substances adhered to the surface of the textile product, the proportion is preferably 1 to 20 mol %, more preferably 3 to 15 mol %, and most preferably 5 to 10 mol %.
In the present embodiment, when the scouring step is performed according to a continuous treatment and a co-solvent is used, the rate of the co-solvent flowing into the treatment container is not particularly limited, and in order to perform sufficient scouring, the flow rate is preferably 0.05 to 10 ml/min, more preferably 0.08 to 8 ml/min, and most preferably 0.1 to 5 ml/min per 1 g of fibers.
In the present embodiment, the fluid containing supercritical carbon dioxide may further contain a surfactant. When the fluid contains a surfactant, it is possible to further improve removability of substances adhered to the surface of the textile product than when a fluid containing no surfactant is used, and particularly, when the textile product contains a cotton yarn or a cotton fabric, it is possible to further improve the water wettability of the textile product.
In the present embodiment, the fluid containing supercritical carbon dioxide may further contain a co-solvent and a surfactant. When the fluid contains both a co-solvent and a surfactant, it is possible to further significantly improve removability of substances adhered to the surface of the textile product than when a fluid containing neither a co-solvent nor a surfactant, a fluid containing only a co-solvent, or a fluid containing only a surfactant is used, and particularly, when the textile product contains a cotton yarn or a cotton fabric, it is possible to significantly improve the water wettability of the textile product.
The surfactant is not particularly limited, and nonionic surfactants such as polyoxyethylene lauryl ether, fatty alcohol ethoxylate, and glycerin fatty acid ester, cationic surfactants such as distearyldimethylammonium chloride, and benzalkonium chloride, and anionic surfactants such as sulfate ester salts and phosphate ester salts can be used, and one of these surfactants or combinations of two or more thereof can be used. As the surfactant, a nonionic surfactant is preferable and polyoxyethylene lauryl ether is more preferable in consideration of low toxicity.
In the present embodiment, when a surfactant is used, it can be directly added into the treatment container separately from the supercritical carbon dioxide. In addition, when a surfactant and a co-solvent are used in combination, the surfactant is added to the co-solvent in advance, and the co-solvent to which the surfactant is added can be transferred as a liquid into the treatment container separately from the supercritical carbon dioxide.
When a surfactant is used, the proportion (g/L) of the surfactant(g) with respect to the entire solvent containing supercritical carbon dioxide or solvent containing supercritical carbon dioxide and a co-solvent (L) in the treatment container is not particularly limited, and in order to improve removability of substances adhered to the surface of the textile product, the proportion is preferably 0.2 to 15 g/L, more preferably 0.3 to 10 g/L, and most preferably 0.5 to 5 g/L. In the present embodiment, during the treatment with supercritical carbon dioxide, the proportion (g/L) of the surfactant in the treatment container can be maintained within the above numerical range.
In the present embodiment, the method may further include a step of irradiating the textile product before a scouring treatment with an electron beam before the step (a) or (a′). When the textile product before a scouring treatment is irradiated with an electron beam, it is possible to decompose some or all substances adhered to the surface of the textile product (such as the above non-cellulose impurities). Thereby, during a subsequent treatment with a fluid containing supercritical carbon dioxide, it is possible to more efficiently remove the substances from the surface of the textile product.
In the step of irradiating the electron beam, the electron beam irradiation dose is not particularly limited, and is preferably 1 to 500 kGy, more preferably 10 to 400 kGy, and most preferably 30 to 300 kGy in order to maintain the strength of the fiber to be irradiated, and the electron beam irradiation time is not particularly limited, and is preferably 0.1 to 5 seconds, more preferably 0.5 to 3 seconds, and most preferably 1 to 2 seconds.
In the present embodiment, the weight loss (%) of the textile product before and after the scouring treatment is not particularly limited, and may be 0.1 to 20%, 1 to 10%, or 2 to 5%. The weight loss (%) of the textile product before and after the scouring treatment can be calculated based on Formula (1) described in 3.1. of examples to be described below.
In the present embodiment, the water wettability (s, seconds) of the textile product after the scouring treatment is performed is not particularly limited, and may be 1 to 11,000 s, 3 to 1,200 s, 3 to 1,100 s, 3 to 1,000 s, 3 to 100 s, or 5 to 20 s. The water wettability (%) of the textile product after the scouring treatment is performed can be calculated based on the method described in 3.2. of examples to be described below.
The textile product after the scouring treatment obtained by the method according to the present embodiment exhibits a large weight loss (%) and high water wettability.
The method of the present embodiment can be used as a scouring step which is one fiber processing step, and can also be used in combination with other fiber processing steps of spinning, weaving, sizing, desizing/bleaching, dyeing, and finishing.
Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to the content described in the examples.
Unbleached cotton pile fabrics (commercially available from IZAWA TOWEL Co., Ltd.) were prepared. The following Table 1 shows specifications of woven fabrics.
1 g of the above woven fabric was cut to a size of 4 cm×6 cm, and the ends of the cut woven fabric were sewn in order to prevent the yarn loss. The woven fabric with the sewn ends was pre-dried in a drying oven (DX302, commercially available from Yamato Scientific Co., Ltd.) at 105° C. for 1 hour. In addition, nonionic surfactants having a chemical structure represented by the following Formula (1): polyoxyethylene lauryl ether (99.0%), ethanol (99.8%), methanol (99.8%), acetone (99.8%), tetrahydrofuran (99.8%), and sodium hydroxide (99.8%) (all commercially available from Nacalai Tesque, Inc.) were prepared.
2.1. Treatment with Alkaline Aqueous Solution (Conventional Treatment Method)
1 g (Wa1) of the pre-dried woven fabric shown in the above 1. was scoured using sodium hydroxide and the above nonionic surfactant: polyoxyethylene lauryl ether at 100° C. for 120 minutes, and at a liquid ratio 1:50. The scouring was performed using a mixture containing 10 g/L of NaOH and 1.4 g/L of a surfactant (hereinafter referred to as “alkaline scoring 1”), a mixture containing 30 g/L of NaOH and 4.2 g/L of a surfactant (hereinafter referred to as “alkaline scoring 2”), or a mixture containing 30 g/L of NaOH and 30 g/L of a surfactant (hereinafter referred to as “alkaline scoring 3”) as shown in Table 3 below. The scoured woven fabric was washed with water at 30° C. for 10 minutes, then post-dried in an oven at 105° C. for 60 minutes, and the weight (g, Wa2) of the post-dried woven fabric was measured.
2.2. Treatment with Organic Solvent (Conventional Treatment Method)
0.5 g (Wo1) of the pre-dried woven fabric shown in the above 1. was put into a sealed glass container containing 240 ml of different media such as water, ethanol, methanol, acetone, tetrahydrofuran (THF), or hexane (1.2 g of the above nonionic surfactant: contains or does not contain polyoxyethylene lauryl ether), as shown in Table 3 below, and scoured using a water shaking bath (BW400, commercially available from Yamato Scientific Co., Ltd.) at 50° C. for 480 minutes. The scoured woven fabric was washed with water for 10 minutes, and then washed with acetone at room temperature for 10 minutes, and post-dried in an oven at 105° C. for 60 minutes, and the weight (g, Wo2) of the post-dried woven fabric was measured.
2.3. Dewaxing with Supercritical Carbon Dioxide
The device used in the treatment with supercritical carbon dioxide is shown in
1 g (Wc1) of the pre-dried woven fabric shown in the above 1. and a stirrer tip were put into the high-pressure container, the high-pressure container was installed in an oven SCF-Sro, and the temperature of the oven was set to 100° C. A liquefied carbon dioxide was injected into the high-pressure container at 5 ml/min for 480 minutes using a liquid transfer pump. In addition, as shown in Tables 2 and 4 below, only a co-solvent or a co-solvent containing 5, 10, or 20 g/L of the above nonionic surfactant: polyoxyethylene lauryl ether was injected into the high-pressure container at 1 ml/min and 20 MPa. In addition, as shown in the following Table 4, when only a surfactant was added without injecting a co-solvent and supercritical carbon dioxide was used, 9.6 g (4 g/L) of a surfactant was directly added to the high-pressure container before carbon dioxide flowed out. As described above, when a co-solvent contained a surfactant, the concentration of the surfactant in the mixture containing supercritical carbon dioxide and the co-solvent was estimated to be 0.83, 1.7, and 3.3 g/L. A magnetic stirrer installed in the high-pressure container was operated at 100 rpm during the treatment with supercritical carbon dioxide. After the treatment with supercritical carbon dioxide under conditions of 100° C., 20 MPa, and 480 minutes, the high-pressure container was depressurized to atmospheric pressure. Then, the woven fabric after the treatment with supercritical carbon dioxide was taken out, washed with sufficient water for 10 minutes, and washed with sufficient acetone at room temperature for 10 minutes, and then post-dried in an oven at 105° C. for 60 minutes. Then, the weight (Wc2) of the post-dried woven fabric was measured.
2.4. Dewaxing with Supercritical Carbon Dioxide in Combination with Electron Beam Irradiation
Electron beam irradiation was performed using an electron beam irradiation device EPS-750 (commercially available from NHV Corporation) at atmospheric atmosphere and an acceleration voltage of 750 keV, as shown in Table 5 below, at an absorbed dose of 50, 100, or 200 kGy. Regarding the device used in the treatment with supercritical carbon dioxide, the liquid transfer pump that transfers carbon dioxide or a co-solvent, the carbon dioxide supply source and the like, those described in the above 2.3.1. were used.
1 g (We1) of the pre-dried woven fabric shown in the above 1. was put into the electron beam irradiation device, and as shown in Table 5 below, the woven fabric was irradiated with an electron beam at a dose of 50, 100, or 200 kGy. As described above, the woven fabric irradiated with an electron beam or the woven fabric not irradiated with an electron beam (1 g (We1) of the pre-dried woven fabric shown in the above 1.) and a stirrer tip were put into the high-pressure container, the high-pressure container was installed in an oven SCF-Sro, and the temperature of the oven was set to 100° C. The liquefied carbon dioxide was injected into the high-pressure container using a liquid transfer pump at 5 ml/min for 120, 240, or 480 minutes (the flow rate of carbon dioxide: 600, 1,200, or 2,400 ml). In addition, as shown in Table 5 below, only a co-solvent (methanol), or a co-solvent containing 5, 10, or 20 g/L of the above nonionic surfactant: polyoxyethylene lauryl ether, was injected into the high-pressure container at 1 ml/min and 20 MPa. In addition, as shown in the following Table 5, when only a surfactant was added without injecting a co-solvent and supercritical carbon dioxide was used, 9.6 g (4 g/L) of a surfactant was directly added to the high-pressure container before carbon dioxide flowed out. As described above, when a co-solvent contained a surfactant, the concentration of the surfactant in the mixture containing supercritical carbon dioxide and a co-solvent was estimated to be 3.3 g/L. A magnetic stirrer installed in the high-pressure container was operated at 5 rpm during the treatment with supercritical carbon dioxide. After the treatment with supercritical carbon dioxide under conditions of 100° C., 20 MPa, and 120, 240, or 480 minutes, the high-pressure container was depressurized to atmospheric pressure. Then, the woven fabric after the treatment with supercritical carbon dioxide was taken out, washed with sufficient acetone at room temperature for 10 minutes and washed with sufficient water at 100° C. for 10 minutes, and then post-dried in an oven at 105° C. for 60 minutes. Then, the weight (We2) of the post-dried woven fabric was measured.
In order to confirm the extent to which waxes and other impurities were removed from the woven fabric according to each treatment described in the above 2., the weight loss (%) of the woven fabric was calculated based on the following Formula (1).
Here, Wx1 was the weight of the woven fabric before the treatment and after drying, and Wx2 was the weight of the woven fabric after the treatment with an alkali (x=a), an organic solvent (x=0), supercritical carbon dioxide (x=c), or electron beam irradiation and supercritical carbon dioxide (x=e) and after post-drying (each weight described in the above 2.).
The water wettability of the woven fabric was measured according to a water immersion test (EN14697: 2005 standardization) under standard laboratory conditions (20±2° C., relative humidity of 65±2%). The time from when the woven fabric was placed on the surface of water until the woven fabric was completely immersed in water was recorded. If the woven fabric had excellent water wettability (short water wettability time), the woven fabric had excellent water absorption accordingly, and for example, was suitable for use as a towel.
The surface condition of each woven fabric was observed using a field emission scanning electron microscope (FE-SEM JSM-701F, commercially available from JEOL Ltd.). Before observation was performed, the surface of the woven fabric was precoated with 75A gold using fine coating sputtering (FINECOAT JFC-1100E, commercially available from JEOL Ltd.) for 1 minute.
The change in weight of the unbleached cotton pile fabric and its improvement in water wettability described in the above 3.1. and 3.2. were main criteria for determining effectiveness of the woven fabric dewaxing and washing process. In the present invention, the method of using supercritical carbon dioxide to extract impurities from cotton and various other conventional dewaxing methods were applied, and the type of impurities that could be removed by each method and how impurities affected the absorbency of the fabric was investigated.
4.1. Dewaxing with Supercritical Carbon Dioxide
Table 2 shows the results obtained by performing the treatment with supercritical carbon dioxide using various co-solvents. Table 2 shows the results of no treatment and the treatment with pure supercritical carbon dioxide together. In addition, Table 3 shows the results of the above alkaline scorings 1 to 3 and the treatment with various organic solvents, which are conventional treatment methods.
As shown in the results in Table 2, it was found that, although the woven fabric had no significant change in weight when treated with pure supercritical carbon dioxide, the water wettability exhibited an immersion time of 10,800 seconds, and the water wettability was more improved than that of the untreated woven fabric (an immersion time of 14,400 seconds). When treated with pure supercritical carbon dioxide, the amount of an organic solvent could be significantly reduced and the environmental load could be sufficiently reduced so that the method was thought to be a beneficial scouring method. In addition, as shown in the results in Table 2, it was found that, when the treatment with supercritical carbon dioxide using a co-solvent was performed, the water wettability was further improved. This is thought to be caused by the fact that, when a co-solvent having polarity shown in Table 2 was added, the polarity of the entire solvent containing supercritical carbon dioxide increased, the cotton was likely to swell, and the wax on the surface of cotton was likely to dissolve in the solvent. In particular, it was found that, when the treatment with supercritical carbon dioxide using an alcohol such as methanol or ethanol or tetrahydrofuran as a co-solvent was performed, the water wettability was significantly improved. In addition, it was found that, comparing the results in Table 2 with the results of conventional treatment methods in Table 3, the water wettability after the treatment with supercritical carbon dioxide using methanol, ethanol, or tetrahydrofuran as a co-solvent (for 1,080 seconds, 970 seconds, or 1,080 seconds) was better than the water wettability after the treatment with ethanol, methanol, or tetrahydrofuran without using supercritical carbon dioxide (for 1,200 seconds). Based on the results, it was found that, when an alcohol such as methanol or ethanol or tetrahydrofuran was used as a co-solvent for supercritical carbon dioxide, it was possible to significantly improve the water wettability while reducing the amount of the organic solvent and reducing the environmental load. Regarding the results, it was speculated that an alcohol such as methanol or ethanol was more likely to swell the cotton. In addition, as shown in the results in Tables 2 and 3, it was found that the water wettability after the treatment with supercritical carbon dioxide using acetone as an co-solvent maintained the same level as the water wettability after the treatment with acetone without using supercritical carbon dioxide, it was possible to achieve excellent water wettability while reducing the amount of an organic solvent and reducing the environmental load.
Table 4 shows the results obtained by the treatment with supercritical carbon dioxide using a surfactant. Table 4 shows cases in which only a surfactant was added to supercritical carbon dioxide and cases in which both a surfactant and a co-solvent were added.
As shown in Table 4, it was found that, when the treatment with supercritical carbon dioxide to which only a surfactant was added was performed, the weight loss of the woven fabric was significantly increased to 2.6%, the immersion time was shortened to 10 seconds, and favorable water wettability was exhibited. That is, it was found that, comparing the treatment with pure supercritical carbon dioxide and the treatment with supercritical carbon dioxide containing a co-solvent shown in Table 2, when the treatment with supercritical carbon dioxide to which only a surfactant was added was performed, the water wettability was further improved. Regarding the results, it was speculated that the surfactant had amphipathic properties, lipophilic groups of the surfactant were adsorbed to the wax on the fibers and incorporated into micelles, and additionally, according to the function of hydrophilic groups of the surfactant, the wax-incorporated micelles were stably dispersed in the solution, and the wax was removed from the fiber. In addition, as shown in Table 4, it was found that, when the treatment with supercritical carbon dioxide containing both a co-solvent and a surfactant was performed, a very good dewaxing effect was obtained, and the results of the woven fabric weight loss of 1.9% to 3.5% and the water wettability for 6.5 seconds to 30 seconds were obtained. Accordingly, it was found that, when the treatment with supercritical carbon dioxide in combination with a co-solvent and a surfactant was performed, improvement in the water wettability was obtained, and particularly, when methanol was used as a co-solvent, a very good synergistic effect was obtained regardless of the concentration (g/L) of the surfactant. Regarding the results, it was thought that the co-solvent increased the polarity of supercritical carbon dioxide, swelling of cotton fibers was promoted, and the co-solvent could improve the solubility of supercritical carbon dioxide in the surfactant.
Summarizing the results shown in Tables 2 and 4,
4.2. Dewaxing with Supercritical Carbon Dioxide in Combination with Electron Beam Irradiation
Table 5 shows the results obtained by performing a treatment by changing the electron beam irradiation dose, and the amounts of supercritical carbon dioxide, a co-solvent (methanol), and a surfactant. Table 5 also shows the results without a treatment with supercritical carbon dioxide. In addition,
As shown in the results in Table 5, it was found that, as the dose of the electron beam increased, the value of the weight loss (%) increased, and the water wettability was improved (the value (s) of the water wettability decreased). This was thought to be caused by the fact that, when electron beam irradiation was performed before the treatment with supercritical carbon dioxide, hydrophobic impurities on the surface of the cotton were decomposed, and it was possible to improve removability of the wax and pectin during the treatment with supercritical carbon dioxide. Therefore, it was thought that, according to electron beam irradiation, it was possible to shorten the treatment time with supercritical carbon dioxide and reduce the energy used. In addition, as shown in the results in Table 5, it was found that, when the treatment with supercritical carbon dioxide using a co-solvent (methanol) was performed, the value of the weight change (%) was larger and the water wettability was more improved than the treatment with pure supercritical carbon dioxide was performed. In addition, it was found that, when the treatment with supercritical carbon dioxide using a surfactant was performed and when the treatment with supercritical carbon dioxide in combination with a co-solvent and a surfactant was performed, the value of the weight change (%) was larger and the water wettability was more improved than when the treatment with supercritical carbon dioxide using a co-solvent (methanol) was performed. In addition, as shown in the results in
| Number | Date | Country | Kind |
|---|---|---|---|
| 2021-102928 | Jun 2021 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2022/022291 | 6/1/2022 | WO |
