TWI521107B - Preparing method of polysaccharide fiber - Google Patents
Preparing method of polysaccharide fiber Download PDFInfo
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- TWI521107B TWI521107B TW103126370A TW103126370A TWI521107B TW I521107 B TWI521107 B TW I521107B TW 103126370 A TW103126370 A TW 103126370A TW 103126370 A TW103126370 A TW 103126370A TW I521107 B TWI521107 B TW I521107B
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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
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
- D01F2/02—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from solutions of cellulose in acids, bases or salts
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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
- D01F9/00—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
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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
- D01F1/06—Dyes
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
- D06P5/00—Other features in dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form
- D06P5/13—Fugitive dyeing or stripping dyes
- D06P5/137—Fugitive dyeing or stripping dyes with other compounds
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Description
本發明是有關於一種多醣類纖維的製備方法,且特別是有關於一種再生多醣類纖維的製備方法。 The present invention relates to a method for preparing a polysaccharide fiber, and more particularly to a method for preparing a regenerated polysaccharide fiber.
近年來,科學家積極開發透過將現有的高分子材料進行溶解,製作成再生纖維以取代天然纖維的消耗。再生纖維可以廣泛應用於各種產業中,如家飾紡織品、光學薄膜、可撓式電子顯示器、化妝品、醫學藥品與食品添加物等。在再生纖維的製程上,通常利用各種化學或物理的方法,來使得再生纖維具有各種不同的機能以符合市場的需求,其例如透氣、吸濕性佳、易染色、抗靜電、抗菌等。 In recent years, scientists have actively developed the production of recycled fibers to replace the consumption of natural fibers by dissolving existing polymer materials. Recycled fibers can be used in a wide variety of industries, such as home textiles, optical films, flexible electronic displays, cosmetics, medical drugs and food additives. In the process of reclaiming fibers, various chemical or physical methods are generally used to make the regenerated fibers have various functions to meet the market demand, such as gas permeability, moisture absorption, easy dyeing, antistatic, antibacterial and the like.
在紡織業中,又以廢棉織品的處理為研究重點。由於纖維素纖維同時具有柔軟性與吸濕性,故相當適合作為不織布的原料。目前纖維素不纖布是使用甲基氧化嗎啉(N-methylmorpholine N-oxide,NMMO)作為纖維素的溶劑。然而,使用NMMO來溶解纖維素不僅需要高溫,還需要經過繁複的成形過程,進而提高其 製備成本。因此,亟需一種製程簡易且可於室溫下進行的再生纖維的製備方法。 In the textile industry, the treatment of waste cotton fabrics is the focus of research. Since cellulose fibers have both flexibility and hygroscopicity, they are quite suitable as raw materials for nonwoven fabrics. At present, cellulose non-fibrous cloth is a solvent using cellulose as N-methylmorpholine N-oxide (NMMO). However, the use of NMMO to dissolve cellulose requires not only high temperatures, but also a complicated forming process to increase its Preparation costs. Therefore, there is a need for a process for preparing recycled fibers which is simple in process and can be carried out at room temperature.
本發明提供一種多醣類纖維的製備方法,其具有製程簡單的優點。 The invention provides a preparation method of polysaccharide fiber, which has the advantages of simple process.
本發明提出一種多醣類纖維的製備方法,其包括以下步驟。首先,提供多醣類材料。接著,將多醣類材料與離子液體混合,以形成多醣溶液。然後,將多醣溶液與成形液混合,以形成多醣成形物。接著,對多醣成形物進行均質化處理,以形成多醣均質物。然後,將多醣均質物乾燥,以形成多醣類纖維。 The present invention provides a method for preparing a polysaccharide fiber, which comprises the following steps. First, a polysaccharide material is provided. Next, the polysaccharide material is mixed with the ionic liquid to form a polysaccharide solution. Then, the polysaccharide solution is mixed with the molding liquid to form a polysaccharide shaped product. Next, the polysaccharide shaped product is homogenized to form a polysaccharide homogenate. The polysaccharide homogenate is then dried to form a polysaccharide fiber.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,將多醣類材料與離子液體於室溫下混合,以形成多醣溶液。 In an embodiment of the present invention, in the method for producing a polysaccharide fiber, a polysaccharide material and an ionic liquid are mixed at room temperature to form a polysaccharide solution.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,均質化處理是使用高速攪拌均質機作處理,以形成多醣均質物,且將多醣均質物乾燥後,所形成之多醣類纖維呈不織布型態。 In an embodiment of the present invention, in the method for preparing the polysaccharide fiber, the homogenization treatment is performed by using a high-speed stirring homogenizer to form a polysaccharide homogenate, and the polysaccharide homogenate is dried to form a large amount. The saccharide fiber is in a non-woven fabric.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,均質化處理步驟是使用乳化均質機作處理,以形成多醣均質物,且將多醣均質物乾燥後,所形成之多醣類纖維呈薄膜型態。 In an embodiment of the present invention, in the method for preparing a polysaccharide fiber, the homogenization treatment step is performed by using an emulsifier homogenizer to form a polysaccharide homogenate, and the polysaccharide homogenate is dried. The saccharide fiber is in a film form.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,多醣類材料包括含纖維素材料、含甲殼素材料或含澱粉材料。 In an embodiment of the invention, in the method for preparing the polysaccharide fiber, the polysaccharide material comprises a cellulose-containing material, a chitin-containing material or a starch-containing material.
在本發明的一實施例中,上述的多醣類纖維的製備方法 中,含纖維素材料包括木漿、竹、麻、稻桿、椰殼、甘蔗或棉織品。 In an embodiment of the present invention, the method for preparing the above polysaccharide fiber Among the cellulose-containing materials include wood pulp, bamboo, hemp, rice straw, coconut shell, sugar cane or cotton.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,含甲殼素材料包括蝦殼、蟹殼、昆蟲甲殼或烏賊軟骨。 In an embodiment of the invention, in the method for preparing the polysaccharide fiber, the chitin-containing material comprises a shrimp shell, a crab shell, an insect shell or a squid cartilage.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,含澱粉材料包括植物之種子、塊莖或塊根。 In an embodiment of the invention, in the method for preparing the polysaccharide fiber, the starch-containing material comprises seeds, tubers or roots of the plant.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,離子液體由陽離子及陰離子組成。陽離子包括式(1)所示的結構:
其中R1至R5為H或碳原子數為1至8的烴基;該陰離子為選自Cl-、Br-、I-、CH3COO-及HCOO-以及PO4 3-中的一者。 Wherein R 1 to R 5 are H or a hydrocarbon group having 1 to 8 carbon atoms; and the anion is one selected from the group consisting of Cl - , Br - , I - , CH 3 COO - and HCOO - and PO 4 3- .
在本發明的一實施例中,上述的多醣類纖維的製備方法中,離子液體包括1-乙基-3-甲基咪唑醋酸鹽(1-ethyl-3-methylimidazolium acetate,[EMIM]OAc)。 In an embodiment of the present invention, in the method for preparing the polysaccharide fiber, the ionic liquid comprises 1-ethyl-3-methylimidazolium acetate ([EMIM]OAc). .
在本發明的一實施例中,上述的多醣類纖維的製備方法中,成形液包括第一溶劑以及第二溶劑。第一溶劑包括水、甲醇、乙醇、丙酮或其組合。第二溶劑包括離子液體、二甲亞碸(dimethyl sulfoxide,DMSO)、二甲基乙醯胺(dimethylacetamide,DMAc)或 其組合。 In an embodiment of the invention, in the method for producing a polysaccharide fiber, the molding liquid includes a first solvent and a second solvent. The first solvent includes water, methanol, ethanol, acetone, or a combination thereof. The second solvent includes an ionic liquid, dimethyl sulfoxide (DMSO), dimethylacetamide (DMAc) or Its combination.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,不織布型態之多醣類纖維的平均纖維直徑為13μm至30μm。 In an embodiment of the present invention, in the method for producing a polysaccharide fiber, the non-woven fabric type polysaccharide fiber has an average fiber diameter of from 13 μm to 30 μm.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,薄膜型態之多醣類纖維的平均纖維直徑為0.080μm至0.200μm。 In an embodiment of the present invention, in the method for producing a polysaccharide fiber, the film-type polysaccharide fiber has an average fiber diameter of from 0.080 μm to 0.200 μm.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,將多醣類材料與離子液體混合更包括加熱至60℃至80℃。 In an embodiment of the invention, in the method for preparing the polysaccharide fiber, mixing the polysaccharide material with the ionic liquid further comprises heating to 60 ° C to 80 ° C.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,均質化處理為3至5分鐘。 In an embodiment of the present invention, in the method for producing the polysaccharide fiber, the homogenization treatment is 3 to 5 minutes.
在本發明的一實施例中,上述的多醣類纖維的製備方法中,多醣類材料更包括反應性染料,且將多醣溶液與成形液混合後,反應性染料與多醣類材料分離,以形成不具有反應性染料之多醣成形物。 In an embodiment of the present invention, in the method for preparing a polysaccharide fiber, the polysaccharide material further comprises a reactive dye, and after the polysaccharide solution is mixed with the molding liquid, the reactive dye is separated from the polysaccharide material. To form a polysaccharide shaped article that does not have a reactive dye.
基於上述,本發明的實施例所提出之多醣類纖維的製備方法中,使用於室溫下呈液體的離子液體。因此,可於室溫下將多醣類材料與離子液體混合,以提高製程的便利性。此外,視需要,可將多醣成形物經過不同之均質化處理,以得到不織布型態或薄膜型態之多醣類纖維。另外,在本發明的實施例之多醣類纖維的製備方法中,還可將反應性染料與多醣類材料分離,且不需經過離心處理即可得到脫色後的再生多醣類纖維。 Based on the above, in the method for producing a polysaccharide fiber proposed in the examples of the present invention, an ionic liquid which is liquid at room temperature is used. Therefore, the polysaccharide material can be mixed with the ionic liquid at room temperature to improve the convenience of the process. Further, the polysaccharide molded article may be subjected to different homogenization treatments as needed to obtain a polysaccharide fiber of a non-woven fabric type or a film type. Further, in the method for producing a polysaccharide fiber according to the embodiment of the present invention, the reactive dye may be separated from the polysaccharide material, and the decolorized regenerated polysaccharide fiber may be obtained without subjecting to centrifugation.
為讓本發明的上述特徵和優點能更明顯易懂,下文特舉 實施例,並配合所附圖式作詳細說明如下。 In order to make the above features and advantages of the present invention more apparent, the following is a special The embodiments are described in detail below in conjunction with the drawings.
S100~S500‧‧‧步驟 S100~S500‧‧‧Steps
圖1是根據本發明一實施例之多醣類纖維的製備方法的流程圖。 1 is a flow chart showing a method of preparing a polysaccharide fiber according to an embodiment of the present invention.
圖1是根據本發明一實施例之多醣類纖維的製備方法的流程圖。請參照圖1,首先,進行步驟S100,提供多醣類材料。在本實施例中,多醣類材料例如是含纖維素材料、含甲殼素材料或含澱粉材料。在自然界中,纖維素的含量居首。含纖維素材料例如是木漿、竹、麻、稻桿、椰殼、甘蔗或棉織品。含甲殼素材料例如是蝦殼、蟹殼、昆蟲甲殼或烏賊軟骨。甲殼素為僅次於纖維素的第二大天然高分子材料,且甲殼素具有良好生物相容性、吸溼性、更有優越的抗菌、防臭等的功能。含澱粉材料例如是植物之種子、塊莖或塊根,然本發明不限於此。 1 is a flow chart showing a method of preparing a polysaccharide fiber according to an embodiment of the present invention. Referring to Fig. 1, first, step S100 is performed to provide a polysaccharide material. In the present embodiment, the polysaccharide material is, for example, a cellulose-containing material, a chitin-containing material or a starch-containing material. In the natural world, the content of cellulose ranks first. The cellulose-containing material is, for example, wood pulp, bamboo, hemp, rice straw, coconut shell, sugar cane or cotton. The chitin-containing material is, for example, a shrimp shell, a crab shell, an insect shell or a squid cartilage. Chitin is the second largest natural polymer material second only to cellulose, and chitin has good biocompatibility, hygroscopicity, and superior antibacterial and deodorant functions. The starch-containing material is, for example, a seed, tuber or root of a plant, but the invention is not limited thereto.
在本實施例中,可使用物理力量將上述多醣類材料細微化,其例如粉碎或研磨等方式,然本發明不限於此。一般來說,多醣類材料的分子結構中通常具有多個氫鍵提供者(hydrogen bond donor)以及氫鍵接受者(hydrogen bond acceptor)。舉例而言,在本實施例之多醣類材料中,氫鍵提供者為羥基中的氫原子,而氫鍵接受者為羥基中的氧原子。如此一來,多醣類材料不僅分子 內部廣泛存在氫鍵,而具有一定程度的分子內極性,多醣類材料之分子與分子間亦容易產生氫鍵,此將使得多醣類材料在常規的溶劑(例如水和大多數有機溶劑等)中難以溶解。 In the present embodiment, the above polysaccharide material may be finely ground using physical strength, such as pulverization or grinding, but the invention is not limited thereto. Generally, a polysaccharide material generally has a plurality of hydrogen bond donors and a hydrogen bond acceptor in its molecular structure. For example, in the polysaccharide material of the present embodiment, the hydrogen bond provider is a hydrogen atom in the hydroxyl group, and the hydrogen bond acceptor is an oxygen atom in the hydroxyl group. As a result, polysaccharide materials are not only molecules Hydrogen bonds are widely present inside, and have a certain degree of intramolecular polarity. Hydrogen bonds are easily generated between molecules and molecules of polysaccharide materials, which will make polysaccharide materials in conventional solvents (such as water and most organic solvents, etc.). It is difficult to dissolve.
在本實施例中,請參照圖1之步驟S200,將上述多醣類材料與離子液體混合,以形成多醣溶液。詳細而言,離子液體中的陽離子及陰離子能夠與多醣類材料中的氧原子和氫原子進行相互作用,因此能破壞多醣類材料分子間的氫鍵,進而充分溶解多醣類材料,而形成多醣溶液。在本實施例中,上述多醣溶液為澄清溶液,然本發明不限於此。 In the present embodiment, referring to step S200 of FIG. 1, the above polysaccharide material is mixed with an ionic liquid to form a polysaccharide solution. In detail, the cation and anion in the ionic liquid can interact with the oxygen atom and the hydrogen atom in the polysaccharide material, thereby breaking the hydrogen bond between the molecules of the polysaccharide material, thereby fully dissolving the polysaccharide material, and A polysaccharide solution is formed. In the present embodiment, the above polysaccharide solution is a clear solution, but the invention is not limited thereto.
在本實施例中,離子液體由陽離子及陰離子組成。陽離子可包括式(1)所示的結構:
在本實施例中,R1至R5可為H或碳原子數為1至8的烴基。在本實施例中,陰離子可選自Cl-、Br-、I-、CH3COO-及HCOO-以及PO4 3-中的一者。 In the present embodiment, R 1 to R 5 may be H or a hydrocarbon group having 1 to 8 carbon atoms. In this embodiment, the anion may be selected from one of Cl - , Br - , I - , CH 3 COO - and HCOO - and PO 4 3- .
在一實施例中,離子液體例如是1-乙基-3-甲基咪唑醋酸鹽([EMIM]OAc),其結構如下式(2)所示。 In one embodiment, the ionic liquid is, for example, 1-ethyl-3-methylimidazolium acetate ([EMIM]OAc), and its structure is represented by the following formula (2).
特別說明的是,陰離子為CH3COO-的離子液體(如上所述的1-乙基-3-甲基咪唑醋酸鹽)與陰離子為其他種類(例如Cl-)的離子液體相比,陰離子為CH3COO-的離子液體可在較低的溫度下溶解同等量的多醣類材料,因此可減少溶解時所使用的能量。 In particular, an ionic liquid having an anion of CH 3 COO − (1-ethyl-3-methylimidazolium acetate as described above) and an anion having an anion of an ionic liquid of another species (for example, Cl − ) are The ionic liquid of CH 3 COO - can dissolve the same amount of polysaccharide material at a lower temperature, thereby reducing the energy used in dissolution.
值得一提的是,上述離子液體於室溫下仍呈液體狀。因此,可直接於室溫下將上述多醣類材料與離子液體混合。然而,在其他實施例中,也可在步驟S200中透過加熱的方式,加速多醣類材料之溶解速率。加熱的溫度例如是60℃至80℃,然本發明不限於此。 It is worth mentioning that the above ionic liquid is still liquid at room temperature. Therefore, the above polysaccharide material can be mixed with the ionic liquid directly at room temperature. However, in other embodiments, the dissolution rate of the polysaccharide material may also be accelerated by means of heating in step S200. The heating temperature is, for example, 60 ° C to 80 ° C, but the invention is not limited thereto.
請參照圖1之步驟S300,將上述多醣溶液與成形液混合,以形成多醣成形物。在本實施例中,成形液可包括第一溶劑以及第二溶劑。第一溶劑例如是水、甲醇、乙醇、丙酮或其組合。第二溶劑例如是上述任一種離子液體、二甲亞碸(DMSO)、二甲基乙醯胺(DMAc)或其組合,然本發明不限於此。 Referring to step S300 of Fig. 1, the above polysaccharide solution is mixed with a molding liquid to form a polysaccharide shaped product. In the present embodiment, the molding liquid may include a first solvent and a second solvent. The first solvent is, for example, water, methanol, ethanol, acetone or a combination thereof. The second solvent is, for example, any of the above ionic liquids, dimethyl hydrazine (DMSO), dimethyl acetamide (DMAc), or a combination thereof, but the invention is not limited thereto.
值得一提的是,在步驟S300後所形成之多醣成形物的分子間填充著第一溶劑(例如為水)與第二溶劑(例如為離子液體)。因此,在步驟S300後,多醣成形物為凝膠狀而尚未有足夠的時間可形成結晶,使得其分子間的作用力較為薄弱。 It is worth mentioning that the first embodiment of the polysaccharide formed after step S300 is filled with a first solvent (for example, water) and a second solvent (for example, an ionic liquid). Therefore, after the step S300, the polysaccharide shaped product is gel-like and there is not enough time to form crystals, so that the force between the molecules is weak.
接著,請參照圖1之步驟S400,對多醣成形物進行均質化處理,以形成多醣均質物。由於多醣成形物尚未形成結晶,故可藉物理力量輕易地將多醣成形物均質化,上述物理力量例如是攪拌或超音波震盪。均質化處理之時間例如為3至5分鐘,然本 發明不限於此。然後,請參照圖1之步驟S500,將上述多醣均質物乾燥,以形成多醣類纖維。在本實施例中,上述乾燥方式例如是將多醣均質物抽氣過濾後,再放置24小時陰乾,然本發明不限於此。 Next, referring to step S400 of Fig. 1, the polysaccharide molded product is homogenized to form a polysaccharide homogenate. Since the polysaccharide shaped product has not yet formed crystals, the polysaccharide shaped body can be easily homogenized by physical force such as stirring or ultrasonic vibration. The time of homogenization treatment is, for example, 3 to 5 minutes, The invention is not limited to this. Then, referring to step S500 of Fig. 1, the above polysaccharide homogenate is dried to form a polysaccharide fiber. In the present embodiment, the drying method is, for example, that the polysaccharide homogenate is suction-filtered and then left to stand for 24 hours, but the present invention is not limited thereto.
值得一提的是,在本實施例中,可視需要選擇不同的均質處理方式。舉例而言,可使用高速攪拌均質機處理上述多醣成形物,以形成多醣均質物。接著,將多醣均質物乾燥後,可形成不織布型態之多醣類纖維。此不織布型態之多醣類纖維的平均纖維直徑可為13μm至30μm。在一實施例中,上述多醣類纖維的平均纖維直徑為15μm,然本發明不限於此。又或者,可使用乳化均質機處理上述多醣成形物,以形成多醣均質物。接著,將上述多醣均質物乾燥並經過壓製後,可形成半透明薄膜型態之多醣類纖維。此薄膜型態之多醣類纖維的平均纖維直徑可為0.080μm至0.200μm。 It is worth mentioning that in this embodiment, different homogeneous processing modes can be selected as needed. For example, the above polysaccharide shaped article can be treated using a high speed agitation homogenizer to form a polysaccharide homogenate. Next, after drying the polysaccharide homogenate, a polysaccharide fiber of a non-woven fabric type can be formed. The non-woven fabric type polysaccharide fiber may have an average fiber diameter of from 13 μm to 30 μm. In one embodiment, the above polysaccharide fibers have an average fiber diameter of 15 μm, but the invention is not limited thereto. Alternatively, the polysaccharide shaped article may be treated with an emulsification homogenizer to form a polysaccharide homogenate. Next, the polysaccharide homogenate is dried and pressed to form a translucent film-type polysaccharide fiber. The film type polyester fiber may have an average fiber diameter of from 0.080 μm to 0.200 μm.
進行以上所有步驟S100至S500後,即可完成本實施例之多醣類纖維的製備。 After all the above steps S100 to S500 are carried out, the preparation of the polysaccharide fiber of the present embodiment can be completed.
值得一提的是,在一實施例中,多醣類材料更可包括反應性染料。反應性染料是由染料母體與連接基所構成的,此反應性染料可與多醣類材料的多種官能基之間形成化學鍵結。使用在多醣類材料的反應性染料之染料母體例如為偶氮、蒽醌、酞菁等。上述反應性染料之連接基例如為均三嗪、乙烯碸、喹噁啉、嘧啶等。在本發明一實施例之多醣類纖維的製備方法中,將含反應性 染料之多醣溶液與成形液混合後,可將反應性染料與多醣類材料分離,使反應性染料進入第一溶劑中,以形成脫色之多醣成形物。 It is worth mentioning that in an embodiment, the polysaccharide material may further comprise a reactive dye. The reactive dye is composed of a dye precursor and a linking group which forms a chemical bond with a plurality of functional groups of the polysaccharide material. The dye precursor of the reactive dye used in the polysaccharide material is, for example, azo, hydrazine, phthalocyanine or the like. The linking group of the above reactive dye is, for example, a s-triazine, a vinyl hydrazine, a quinoxaline, a pyrimidine or the like. In the method for preparing a polysaccharide fiber according to an embodiment of the present invention, reactivity is included After the dye solution of the dye is mixed with the molding liquid, the reactive dye can be separated from the polysaccharide material, and the reactive dye can be introduced into the first solvent to form a decolored polyester shaped article.
以下,藉由數個實驗例來詳細說明上述實施例所提出之多醣類纖維的製備及其特性。然而,下列實驗例並非用以限制本發明。 Hereinafter, the preparation of the polysaccharide fibers proposed in the above examples and their characteristics will be described in detail by way of several experimental examples. However, the following experimental examples are not intended to limit the invention.
為了證明本發明之多醣類纖維的製備方法可製備多醣類纖維且製程簡單,特別作以下多個實例。 In order to prove that the preparation method of the polysaccharide fiber of the present invention can prepare a polysaccharide fiber and the process is simple, the following examples are particularly made.
首先,將木漿或棉織品粉碎。接著,於60℃至80℃下,以[EMIM]OAc作為溶劑,配製5重量%至10重量%之纖維素黏液。然後,將20克之纖維素黏液倒出或是擠入1升之水中,形成纖維素成形物。接著,使用高速攪拌均質機,以10000rpm至26000rpm之轉速,將纖維素成形物均質化處理3至5分鐘,形成纖維素均質物。最後,將此纖維素均質物抽氣過濾後,再放置24小時陰乾,即可得到纖維素不織布。此纖維素不織布的平均纖維直徑為15μm。 First, the wood pulp or cotton fabric is pulverized. Next, 5 to 10% by weight of the cellulose slime is prepared at 60 ° C to 80 ° C using [EMIM]OAc as a solvent. Then, 20 g of the cellulose slime was poured out or squeezed into 1 liter of water to form a cellulose formed product. Next, the cellulose molded product was homogenized by a high-speed stirring homogenizer at a number of revolutions of 10,000 rpm to 26,000 rpm for 3 to 5 minutes to form a cellulose homogenate. Finally, the cellulose homogenate was suction filtered, and then left to stand for 24 hours to obtain a cellulose non-woven fabric. This cellulose nonwoven fabric had an average fiber diameter of 15 μm.
首先,將1克的黑白報紙剪成2cmx2cm的尺寸,並將其浸泡於1%的氫氧化鈉水溶液中1小時,以將油墨去除。接著,使用20克之[EMIM]OAc於80℃下溶解4小時後,可得到纖維素黏 液。隨後,將此纖維素黏液倒入高速攪拌均質機中,以10000rpm至26000rpm之轉速,進行均質處理5分鐘。最後,經由抽氣過濾收集,並陰乾24小時後,即可得到纖維素不織布。此纖維素不織布的平均纖維直徑為20μm。 First, 1 gram of black and white newspaper was cut into a size of 2 cm x 2 cm, and it was immersed in a 1% aqueous sodium hydroxide solution for 1 hour to remove the ink. Then, after 20 g of [EMIM]OAc was dissolved at 80 ° C for 4 hours, cellulose adhesion was obtained. liquid. Subsequently, the cellulose slime was poured into a high-speed stirring homogenizer, and homogenized for 5 minutes at a rotational speed of 10,000 rpm to 26,000 rpm. Finally, it was collected by suction filtration and dried for 24 hours to obtain a cellulose non-woven fabric. This cellulose non-woven fabric had an average fiber diameter of 20 μm.
首先,準備1克的甲殼素粉末。接著,使用20克之[EMIM]OAc於80℃下溶解8小時後,可得到甲殼素黏液。隨後,將此甲殼素黏液倒入高速攪拌均質機中,以10000rpm至26000rpm之轉速,進行均質處理5分鐘。最後,經由抽氣過濾收集,並陰乾24小時後,即可得到甲殼素不織布。此甲殼素不織布的平均纖維直徑為30μm。 First, 1 gram of chitin powder was prepared. Next, after 20 g of [EMIM]OAc was dissolved at 80 ° C for 8 hours, a chitin mucilage was obtained. Subsequently, the chitin mucilage was poured into a high-speed stirring homogenizer, and homogenization was carried out for 5 minutes at a rotation speed of 10,000 rpm to 26,000 rpm. Finally, it was collected by suction filtration and dried for 24 hours to obtain a chitin non-woven fabric. This chitin nonwoven fabric had an average fiber diameter of 30 μm.
分別使用NMMO與[EMIM]OAc來溶解含5重量%之纖維素的木漿漿板與純棉染色纖維織品。溶解溫度為80℃;溶解時間為8小時。根據以下公式來計算其聚合度:聚合度=(總分子量)/(1單位之分子量)*100%。此外,以溶解前之木漿漿板與純棉染色纖維織品的聚合度為基準,計算溶解後之木漿漿板與純棉染色纖維織品的保持率,也就是說,將溶解前之木漿漿板與純棉染色纖維織品的保持率當作100%,根據以下公式來計算其保持率:保持率=(溶解前之多醣類材料的聚合度)/(溶解後之多醣類材料的聚合 度)*100%。將其結果示於下表一。 NMMO and [EMIM]OAc were used to dissolve wood pulp board and cotton dyed fiber fabric containing 5% by weight of cellulose, respectively. The dissolution temperature was 80 ° C; the dissolution time was 8 hours. The degree of polymerization was calculated according to the following formula: degree of polymerization = (total molecular weight) / (molecular weight of 1 unit) * 100%. In addition, based on the degree of polymerization of the wood pulp board and the pure cotton dyed fiber fabric before dissolution, the retention rate of the dissolved wood pulp board and the pure cotton dyed fiber fabric is calculated, that is, the wood pulp before dissolution is calculated. The retention rate of the pulp board and the cotton dyed fiber fabric is regarded as 100%, and the retention ratio is calculated according to the following formula: retention ratio = (degree of polymerization of the polysaccharide material before dissolution) / (polysaccharide material after dissolution) polymerization Degree) *100%. The results are shown in Table 1 below.
應先說明的是,多醣類材料溶解後之聚合度愈大,表示多醣類材料在此溶劑中愈能保持其結構,亦即,保持率愈大。由表一的結果可知,在同樣的溶解溫度與溶解時間下,以[EMIM]OAc作為溶劑,纖維素被破壞的程度較以NMMO來得小,具體而言,前者的保持率可達後者的保持率兩倍以上。因此,在工業上使用NMMO溶解纖維素之製程中,一般會額外加入保護劑來防止纖維素降解。在本發明的多醣類纖維的製備方法中,使用離子液體來處理纖維素,纖維素的降解程度可較使用NMMO的纖維素降解程度大幅下降,故不需要額外加入保護劑。 It should be noted that the greater the degree of polymerization after dissolution of the polysaccharide material, the more the polysaccharide material retains its structure in the solvent, that is, the greater the retention. From the results of Table 1, it can be seen that under the same dissolution temperature and dissolution time, with [EMIM]OAc as the solvent, the degree of cellulose destruction is smaller than that of NMMO. Specifically, the retention rate of the former can be maintained by the latter. The rate is more than twice. Therefore, in the process of industrially using NMMO to dissolve cellulose, an additional protective agent is generally added to prevent cellulose degradation. In the method for producing a polysaccharide fiber of the present invention, an ionic liquid is used to treat cellulose, and the degree of degradation of cellulose can be greatly reduced as compared with the degree of degradation of cellulose using NMMO, so that no additional protective agent is required.
以下特別作一些實驗例來比較以本發明之多醣類纖維的製備方法製得之纖維素不織布與市售不織布的吸水倍率。吸水倍率量測的詳細步驟如下。首先,秤量空茶包之重量T(克),將稱重後之空茶包作為盛裝樣品的工具。接著,秤量表二所示樣品之重量S(克),將稱重後之樣品放入茶包內。隨後,將上述裝有樣品之 茶包浸於蒸餾水中5分鐘,並夾起懸吊5分鐘。待多餘的水分滴完後,秤量茶包和樣品吸水後之總重量W(克)。根據下列公式計算吸水倍率:吸水倍率=(W-(T+S)-T*W0)/S,其中,W0(克)為1克茶包的吸水量。並將其計算結果列於表二。 In the following, some experimental examples were specifically made to compare the water absorption ratios of the cellulose non-woven fabric obtained by the preparation method of the polysaccharide fiber of the present invention and a commercially available nonwoven fabric. The detailed steps of the water absorption rate measurement are as follows. First, weigh the weight T (gram) of the empty tea bag, and use the empty tea bag after weighing as a tool for holding the sample. Next, the weight S (gram) of the sample shown in Table 2 is weighed, and the weighed sample is placed in a tea bag. Subsequently, the above-mentioned tea bag containing the sample was immersed in distilled water for 5 minutes, and suspended for 5 minutes. After the excess water has been dripped, weigh the total weight W (g) of the tea bag and the sample after absorbing water. The water absorption ratio was calculated according to the following formula: water absorption ratio = (W - (T + S) - T * W 0 ) / S, where W 0 (gram) is the water absorption amount of 1 gram of tea bag. The calculation results are listed in Table 2.
比較例1為一般市售之聚丙烯(polypropene,PP)不織布,比較例2為使用NMMO作為溶劑所製得之木漿纖維素不織布,實驗例1為使用[EMIM]OAc作為溶劑所製得之木漿纖維素不織布,而實驗例2為使用[EMIM]OAc作為溶劑所製得之棉織品纖維素不織布。由表二之結果可知,使用[EMIM]OAc作出之再生纖維不織布之吸水倍率比目前市售的PP不織布優異(約大於兩倍)。此外,使用[EMIM]OAc作出之再生纖維不織布之吸水倍率與目前使用NMMO作為溶劑的纖維素不織布相當。 Comparative Example 1 is a commercially available polypropylene (PP) nonwoven fabric, and Comparative Example 2 is a wood pulp cellulose nonwoven fabric obtained by using NMMO as a solvent. Experimental Example 1 was prepared using [EMIM]OAc as a solvent. Wood pulp cellulose was not woven, and Experimental Example 2 was a cotton cellulose non-woven fabric obtained by using [EMIM]OAc as a solvent. As is apparent from the results of Table 2, the water absorption ratio of the recycled fiber nonwoven fabric made using [EMIM]OAc is superior to that of the currently commercially available PP nonwoven fabric (about more than twice). Further, the water absorption ratio of the regenerated fiber nonwoven fabric made using [EMIM]OAc is comparable to the cellulose non-woven fabric currently using NMMO as a solvent.
值得一提的是,透過肉眼觀察,在上述實驗例2中,以[EMIM]OAc溶解具反應性染料(偶氮與均三嗪)染色之棉纖維可幫助棉纖維脫色,進而可得到白色之再生纖維素纖維。相反地,以NMMO溶解具反應性染料染色之棉纖維,所得到的是粉紅色之再生纖維素纖維。 It is worth mentioning that, by visual observation, in the above Experimental Example 2, the cotton fiber dyed with the reactive dye (azo and s-triazine) dissolved in [EMIM]OAc can help the cotton fiber to be decolored, and thus the white color can be obtained. Regenerated Cellulose Fiber. Conversely, cotton fibers dyed with reactive dyes were dissolved in NMMO to give pink regenerated cellulose fibers.
綜上所述,本發明的實施例所提出之多醣類纖維的製備 方法中,使用於室溫下呈液體的離子液體。因此,可於室溫下將多醣類材料與離子液體混合,以提高製程的便利性。此外,使用上述離子液體作為溶劑,還可使多醣類材料之結構保有良好的保持率。視需要,還可將多醣成形物經過不同之均質化處理,以得到不織布型態或薄膜型態之再生多醣類纖維,且不織布型態之再生多醣類纖維可具有較市售的PP不織布優異的吸水倍率。另外,在本發明的實施例之多醣類纖維的製備方法中,還可將反應性染料與多醣類材料分離,且不需經過離心處理即可得到脫色後的再生多醣類纖維。 In summary, the preparation of the polysaccharide fiber proposed in the examples of the present invention In the method, an ionic liquid which is liquid at room temperature is used. Therefore, the polysaccharide material can be mixed with the ionic liquid at room temperature to improve the convenience of the process. Further, by using the above ionic liquid as a solvent, the structure of the polysaccharide material can be maintained at a good retention rate. If necessary, the polysaccharide shaped product may be subjected to different homogenization treatment to obtain a regenerated polysaccharide fiber of a non-woven fabric type or a film type, and the non-woven fabric type regenerated polysaccharide fiber may have a commercially available PP non-woven fabric. Excellent water absorption ratio. Further, in the method for producing a polysaccharide fiber according to the embodiment of the present invention, the reactive dye may be separated from the polysaccharide material, and the decolorized regenerated polysaccharide fiber may be obtained without subjecting to centrifugation.
雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明的精神和範圍內,當可作些許的更動與潤飾,故本發明的保護範圍當視後附的申請專利範圍所界定者為準。 Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention, and any one of ordinary skill in the art can make some changes and refinements without departing from the spirit and scope of the present invention. The scope of the invention is defined by the scope of the appended claims.
S100~S500‧‧‧步驟 S100~S500‧‧‧Steps
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