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CN101736440B - Manufacturing method of dyeable alginate fiber - Google Patents

Manufacturing method of dyeable alginate fiber Download PDF

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CN101736440B
CN101736440B CN2010100115204A CN201010011520A CN101736440B CN 101736440 B CN101736440 B CN 101736440B CN 2010100115204 A CN2010100115204 A CN 2010100115204A CN 201010011520 A CN201010011520 A CN 201010011520A CN 101736440 B CN101736440 B CN 101736440B
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alginate
stainable
alginate fiber
fiber
polyamide
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CN101736440A (en
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朱平
张传杰
胡四军
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Qingdao Tianyi Lignin New Material Technology Co ltd
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Wuhan University of Science and Engineering WUSE
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Abstract

The invention discloses a method for manufacturing dyeable alginate fibers. Adding a water-soluble dendrimer compound into an alginate fiber spinning solution, and carrying out solidification, drafting, washing and post-treatment by adopting wet spinning equipment and technology to obtain the alginate fiber with excellent dyeing property, wherein the content of the dendrimer in the alginate fiber is 1-10%. Compared with the existing alginate fiber production technology, the method has the advantages that the prepared alginate fiber can be dyed by direct dyes and reactive dyes under the salt-free condition, has high dye uptake which can generally reach more than 80 percent, and is 10-15 times higher than that of the alginate fiber produced by the prior art. In addition, the alginate fiber prepared by the method has good color fastness, especially excellent wet processing fastness, and reaches more than grade 4.

Description

可染海藻酸盐纤维的制造方法Manufacturing method of dyeable alginate fiber

技术领域 technical field

本发明涉及可染海藻酸盐纤维的制造方法,特别涉及通过在纺丝溶液中添加树状大分子染色改性剂,经湿法纺丝制造可染海藻酸盐纤维的方法。The invention relates to a method for manufacturing dyeable alginate fibers, in particular to a method for manufacturing dyeable alginate fibers by wet spinning by adding a dendrimer dyeing modifier to a spinning solution.

背景技术 Background technique

海藻酸盐纤维是以天然海藻中提取的多糖为原料,水溶性的金属盐溶液为凝固浴,通过湿法纺丝生产工艺得到的新型纤维。海藻中积累了海洋中丰富的矿物质,并含有碳水化合物、氨基酸、脂肪及各种维生素等成分,可以激活细胞的新陈代谢,具有消炎、止痒的功能,使得海藻酸盐纤维对人体皮肤有自然养护、保湿、美容的功效,同时对皮肤病治疗也具有特殊用途。另外,海藻酸盐纤维还具有良好的生物可降解、生物相容性和优异的吸湿性、阻燃性和电磁屏蔽能力,使得海藻酸盐纤维非常适合用于生产高档服装和内衣面料、防护服以及装饰用纺织品和医用纺织品。但是海藻酸盐纤维目前主要用于生产医用敷料,这是由于其耐盐和耐碱性能比较差,传统的染色工艺难以实现海藻酸盐纤维的染色,限制了其在多个领域的应用。因此,如何实现海藻酸盐纤维的染色成为海藻酸盐纤维研究领域迫在眉睫的问题,目前鲜见这方面的报道。Alginate fiber is a new type of fiber obtained by wet spinning production process with polysaccharide extracted from natural seaweed as raw material and water-soluble metal salt solution as coagulation bath. Seaweed has accumulated rich minerals in the ocean, and contains carbohydrates, amino acids, fats and various vitamins, which can activate the metabolism of cells and have the functions of anti-inflammatory and anti-itching, making alginate fiber have a natural effect on human skin. It has the effects of maintenance, moisturizing, and beauty, and it also has special uses for skin disease treatment. In addition, alginate fiber also has good biodegradability, biocompatibility, excellent hygroscopicity, flame retardancy and electromagnetic shielding ability, making alginate fiber very suitable for the production of high-grade clothing and underwear fabrics, protective clothing As well as decorative textiles and medical textiles. However, alginate fiber is currently mainly used in the production of medical dressings. This is due to its poor salt and alkali resistance. Traditional dyeing processes are difficult to dye alginate fiber, which limits its application in many fields. Therefore, how to realize the dyeing of alginate fibers has become an urgent problem in the field of alginate fiber research, and there are few reports on this aspect at present.

发明内容 Contents of the invention

本发明的任务在于提供一种可染海藻酸盐纤维的制造方法。The task of the present invention is to provide a kind of manufacture method of dyeable alginate fiber.

其技术解决方案是:Its technical solutions are:

一种可染海藻酸盐纤维的制造方法,步骤是将水溶性的树状大分子化合物添加到海藻酸盐水溶液中,采用湿法纺丝设备和工艺,经凝固、牵伸、水洗和后处理,得到可染海藻酸盐纤维。A kind of manufacturing method of dyeable alginate fiber, the step is to add water-soluble dendrimer compound to alginate aqueous solution, adopt wet spinning equipment and process, through coagulation, drafting, washing and post-treatment , to obtain dyeable alginate fiber.

上述水溶性的树状大分子化合物在可染海藻酸盐纤维中的含量为1%~10%,以重量百分数计。The content of the above-mentioned water-soluble dendritic macromolecular compound in the dyeable alginate fiber is 1%-10%, calculated by weight percentage.

上述水溶性的树状大分子化合物是聚酰胺-胺类的树枝状大分子化合物,所选用的聚酰胺-胺类的树枝状大分子化合物优选1.0代~4.0代聚酰胺-胺树状大分子化合物中的任意一种。The above-mentioned water-soluble dendrimer compound is a polyamide-amine dendrimer compound, and the selected polyamide-amine dendrimer compound is preferably 1.0 generation to 4.0 generation polyamide-amine dendrimer compound any of the compounds.

上述可染海藻酸盐纤维的制造方法具体包括如下步骤:The manufacture method of above-mentioned dyeable alginate fiber specifically comprises the following steps:

a称取适量的聚酰胺-胺树状大分子化合物,将其溶解于蒸馏水中;a Weigh an appropriate amount of polyamide-amine dendrimers and dissolve it in distilled water;

b选取适量的海藻酸盐溶于步骤a所获取的聚酰胺-胺树状大分子水溶液中,制得质量百分比浓度为3%~8%的海藻酸盐纤维纺丝溶液;其中,聚酰胺-胺树状大分子化合物对海藻酸盐的质量百分比为1%~10%;b Select an appropriate amount of alginate to dissolve in the polyamide-amine dendrimer aqueous solution obtained in step a to prepare an alginate fiber spinning solution with a concentration of 3% to 8% by mass; wherein, polyamide- The mass percentage of the amine dendrimer compound to the alginate is 1% to 10%;

c选取适量凝固剂溶于水中制得质量百分比浓度为2%~10%的凝固剂水溶液,作为纺丝用凝固浴;c Select an appropriate amount of coagulant to dissolve in water to prepare an aqueous coagulant solution with a mass percent concentration of 2% to 10%, as a coagulation bath for spinning;

d将步骤b制取的海藻酸盐纤维纺丝溶液经过滤和脱泡后,在压力作用下进入步骤c制取的凝固浴中凝固,再经牵伸、水洗和干燥后得到可染海藻酸盐纤维。d. After filtering and defoaming the alginate fiber spinning solution prepared in step b, enter the coagulation bath prepared in step c under pressure to coagulate, and then draw, wash and dry to obtain dyeable alginic acid salt fiber.

上述步骤b中,海藻酸盐的溶解温度是20℃~40℃,并在此温度下机械搅拌2~6小时。In the above step b, the dissolution temperature of the alginate is 20° C. to 40° C., and mechanical stirring is performed at this temperature for 2 to 6 hours.

上述步骤c中,所述凝固剂是氯化钙、氯化钡、氯化铝、硫酸铜试剂中的任意一种或几种的组合。In the above step c, the coagulant is any one or a combination of calcium chloride, barium chloride, aluminum chloride, and copper sulfate reagents.

上述步骤d中:海藻酸盐纤维纺丝溶液的脱泡工艺是减压脱泡12~24h或静置脱泡24~36h;凝固浴的温度是25℃~60℃;纤维的牵伸采用三段牵伸工艺,每段牵伸1.1~2.2倍;纤维的水洗温度是20℃~50℃,烘干温度是40℃~80℃。In the above step d: the defoaming process of the alginate fiber spinning solution is vacuum defoaming for 12-24 hours or standing for defoaming for 24-36 hours; the temperature of the coagulation bath is 25°C-60°C; Sectional drawing process, each section is drawn 1.1 to 2.2 times; the fiber washing temperature is 20°C to 50°C, and the drying temperature is 40°C to 80°C.

上述步骤b中,所述海藻酸盐优选海藻酸钠或海藻酸钾。In the above step b, the alginate is preferably sodium alginate or potassium alginate.

本发明的有益技术效果是:The beneficial technical effect of the present invention is:

1.本发明实现了海藻酸盐纤维的染色,不仅有助于推动海藻酸盐纤维在服用和装饰用纺织品领域的应用,开发出各种功能性的纺织服装,满足人们生活的多元化需求;而且有助于加速我国纺织行业的产品升级和更新换代,提高产品的附加值和市场竞争力,促进我国纺织行业的可持续发展。1. The invention realizes the dyeing of alginate fibers, which not only helps to promote the application of alginate fibers in the field of clothing and decorative textiles, but also develops various functional textile garments to meet the diversified needs of people's lives; Moreover, it will help accelerate the product upgrading and replacement of my country's textile industry, improve the added value and market competitiveness of products, and promote the sustainable development of my country's textile industry.

2.海藻酸盐水溶液是由海藻酸盐溶于水中制取,在现有技术中可直接作为海藻酸盐纤维纺丝溶液,然后采用湿法纺丝设备和工艺等处理即可得到海藻酸盐纤维,但是用此法制取的海藻酸盐纤维染色性能较差。本发明创造性的在海藻酸盐纤维纺丝溶液中添加树状大分子染色改性剂,利用现有海藻酸盐纤维的生产工艺,制造了染色性能优异的海藻酸盐纤维。该方法简单易行,且操作工艺可控,可根据纤维的染色工艺要求调整染色改性剂的用量。2. The aqueous solution of alginate is prepared by dissolving alginate in water. In the prior art, it can be directly used as an alginate fiber spinning solution, and then treated with wet spinning equipment and processes to obtain alginate fiber, but the dyeing performance of the alginate fiber prepared by this method is poor. The present invention creatively adds a dendritic macromolecular dyeing modifier to the alginate fiber spinning solution, and utilizes the existing production process of the alginate fiber to manufacture the alginate fiber with excellent dyeing performance. The method is simple and easy, and the operation process is controllable, and the dosage of the dyeing modifier can be adjusted according to the requirements of the fiber dyeing process.

3.本发明制造的海藻酸盐纤维,具有很高的上染率,一般可以达到80%以上,比现有技术生产的海藻酸盐纤维的上染率提高10~15倍。另外,纤维的色牢度较好,尤其是湿处理牢度优异,达到4级以上。3. The alginate fiber produced by the present invention has a very high dye uptake rate, which can generally reach more than 80%, which is 10-15 times higher than that of the alginate fiber produced in the prior art. In addition, the color fastness of the fiber is good, especially the wet fastness is excellent, reaching above grade 4.

4.本发明制造的可染海藻酸盐纤维采用直接染料或活性染料染色,与传统的染色工艺相比,本发明制造的海藻酸盐纤维的染色无需使用盐促染和碱剂固色,缩短了工艺流程。4. The dyeable alginate fibers manufactured by the present invention are dyed with direct dyes or reactive dyes. Compared with the traditional dyeing process, the dyeing of the alginate fibers manufactured by the present invention does not need to use salt to promote dyeing and alkali agent to fix the color, shortening the process flow.

具体实施方式 Detailed ways

下面结合具体实施例对本发明作进一步说明。The present invention will be further described below in conjunction with specific examples.

实施例1Example 1

称取1.2克第二代(2.0代)的聚酰胺-胺树状大分子化合物溶于960ml蒸馏水中,然后加入40克海藻酸钠,在25℃机械搅拌4小时得到质量百分比浓度为4%的海藻酸钠纤维纺丝溶液,然后经过滤、减压脱泡14h得到海藻酸钠纤维纺丝原液。在压力作用下,海藻酸钠纺丝原液经计量泵、喷丝头进入温度为30℃,质量百分比浓度为4%的氯化钙水溶液凝固浴中,凝固后再对其进行牵伸处理,纤维的牵伸采用三段牵伸工艺,每段牵伸1.5~1.8倍,然后经水洗、干燥后得到可染海藻酸钠纤维。上述步骤中,纤维的水洗温度是40℃,烘干温度是60℃。Weigh 1.2 grams of polyamidoamine dendrimers of the second generation (2.0 generations) and dissolve them in 960 ml of distilled water, then add 40 grams of sodium alginate, and mechanically stir at 25° C. for 4 hours to obtain a concentration of 4% by mass. The sodium alginate fiber spinning solution was filtered and defoamed under reduced pressure for 14 hours to obtain the sodium alginate fiber spinning solution. Under the action of pressure, the sodium alginate spinning stock solution enters the coagulation bath of calcium chloride aqueous solution with a temperature of 30°C and a concentration of 4% by mass through the metering pump and spinneret, and then it is drawn after solidification, and the fiber The drafting adopts three-stage drafting process, and each stage is drawn by 1.5 to 1.8 times, and then washed and dried to obtain dyeable sodium alginate fibers. In the above steps, the fiber washing temperature is 40°C, and the drying temperature is 60°C.

实施例2Example 2

称取2.0克第二代(2.0代)的聚酰胺-胺树状大分子化合物,溶于950ml蒸馏水中,得到聚酰胺-胺树状大分子水溶液,然后向聚酰胺-胺树状大分子水溶液中加入50克海藻酸钠,在30℃下机械搅拌3.5h得到质量百分比浓度为5%的海藻酸钠纤维纺丝溶液,将上述海藻酸钠纤维纺丝溶液过滤、减压脱泡16h得到海藻酸钠纤维纺丝原液。在压力作用下,海藻酸钠纤维纺丝原液经计量泵、喷丝头进入温度为40℃,质量百分比浓度为5%的氯化钡水溶液凝固浴中凝固,然后依次经过牵伸、水洗、干燥后得到可染海藻酸钠纤维。上述步骤中,纤维的牵伸采用三段牵伸工艺,每段牵伸1.6~1.9倍,纤维的水洗温度是40℃,烘干温度是60℃。Take by weighing the polyamide-amine dendrimer compound of the second generation (2.0 generation) of 2.0 grams, be dissolved in 950ml distilled water, obtain polyamide-amine dendrimer aqueous solution, then add polyamide-amine dendrimer aqueous solution Add 50 grams of sodium alginate to the mixture, stir mechanically at 30°C for 3.5 hours to obtain a sodium alginate fiber spinning solution with a concentration of 5% by mass, filter the above-mentioned sodium alginate fiber spinning solution, and defoam under reduced pressure for 16 hours to obtain seaweed Sodium acid fiber spinning dope. Under the action of pressure, the sodium alginate fiber spinning stock solution enters the coagulation bath of barium chloride aqueous solution with a temperature of 40°C and a concentration of 5% by mass through the metering pump and spinneret, and then is drawn, washed, and dried in sequence. Then get dyeable sodium alginate fiber. In the above steps, the fiber is drawn using a three-stage drawing process, and each stage is drawn by 1.6 to 1.9 times. The fiber washing temperature is 40°C, and the drying temperature is 60°C.

实施例3Example 3

称取3.6克第二代(2.0代)的聚酰胺-胺树状大分子化合物溶于940mL蒸馏水中,然后加入60克海藻酸钠,在35℃机械搅拌3.5h得到质量百分比浓度为6%的海藻酸钠纤维纺丝溶液,然后经过滤、减压脱泡18h得到海藻酸钠纤维纺丝原液。在压力作用,海藻酸钠纤维纺丝原液经计量泵、喷丝头进入温度为45℃,质量百分比浓度为6%的氯化铝水溶液凝固浴中,经凝固、牵伸、水洗、干燥后得到可染海藻酸钠纤维。上述步骤中,纤维的牵伸采用三段牵伸工艺,每段牵伸1.7~2.0倍,纤维的水洗温度是45℃,烘干温度是65℃。Weigh 3.6 grams of the second-generation (2.0 generation) polyamide-amine dendrimers and dissolve them in 940 mL of distilled water, then add 60 grams of sodium alginate, and stir mechanically at 35° C. for 3.5 hours to obtain a polyamide-amine dendrimer with a mass percentage concentration of 6%. The sodium alginate fiber spinning solution was filtered and defoamed under reduced pressure for 18 hours to obtain the sodium alginate fiber spinning solution. Under the action of pressure, the sodium alginate fiber spinning stock solution enters the coagulation bath of aluminum chloride aqueous solution with a temperature of 45°C and a mass percentage concentration of 6% through a metering pump and a spinneret, and is obtained after coagulation, drawing, washing and drying. Sodium alginate fiber can be dyed. In the above steps, the fiber is drawn using a three-stage drawing process, each stage is drawn 1.7 to 2.0 times, the fiber washing temperature is 45°C, and the drying temperature is 65°C.

实施例4Example 4

称取5.6克第二代(2.0代)的聚酰胺-胺树状大分子化合物溶于930mL蒸馏水中,然后加入70克海藻酸钠,在40℃机械搅拌3h得到质量百分比浓度为7%的海藻酸钠纤维纺丝溶液,然后经过滤、减压脱泡19h得到海藻酸钠纤维纺丝原液。在压力作用,海藻酸钠纤维纺丝原液经计量泵、喷丝头进入温度为50℃,质量百分比浓度为7%的氯化钙水溶液凝固浴中,经凝固、牵伸、水洗、干燥后得到可染海藻酸钠纤维。上述步骤中,纤维的牵伸采用三段牵伸工艺,每段牵伸1.8~2.1倍,纤维的水洗温度是50℃,烘干温度是70℃。Weigh 5.6 grams of the second-generation (2.0 generation) polyamide-amine dendrimers and dissolve them in 930 mL of distilled water, then add 70 grams of sodium alginate, and stir mechanically at 40°C for 3 hours to obtain seaweed with a mass percentage concentration of 7%. sodium alginate fiber spinning solution, and then filtered and defoamed under reduced pressure for 19 hours to obtain the sodium alginate fiber spinning solution. Under the action of pressure, the sodium alginate fiber spinning dope enters the coagulation bath of calcium chloride aqueous solution with a temperature of 50°C and a mass percentage concentration of 7% through a metering pump and a spinneret, and is obtained after coagulation, drawing, washing and drying. Sodium alginate fiber can be dyed. In the above steps, the fiber is drawn using a three-stage drawing process, each stage is drawn 1.8 to 2.1 times, the fiber washing temperature is 50°C, and the drying temperature is 70°C.

实施例5Example 5

称取8克第二代(2.0代)的聚酰胺-胺树状大分子化合物溶于920mL蒸馏水中,然后加入80克海藻酸钠,在40℃机械搅拌4h得到质量百分比浓度为8%的海藻酸钠纤维纺丝溶液,然后经过滤、减压脱泡22h得到海藻酸钠纤维纺丝原液。在压力作用,海藻酸钠纤维纺丝原液经计量泵、喷丝头进入温度为50℃,质量百分比浓度为8%的氯化钙水溶液凝固浴中,经凝固、牵伸、水洗、干燥后得到可染海藻酸钠纤维。上述步骤中,纤维的牵伸采用三段牵伸工艺,每段牵伸1.8~2.2倍,纤维的水洗温度是50℃,烘干温度是80℃。Weigh 8 grams of the second-generation (2.0 generation) polyamide-amine dendrimers and dissolve them in 920 mL of distilled water, then add 80 grams of sodium alginate, and stir mechanically at 40°C for 4 hours to obtain seaweed with a mass percentage concentration of 8%. sodium alginate fiber spinning solution, and then filtered and defoamed under reduced pressure for 22 hours to obtain the sodium alginate fiber spinning solution. Under the action of pressure, the sodium alginate fiber spinning stock solution enters the coagulation bath of calcium chloride aqueous solution with a temperature of 50 °C and a mass percentage concentration of 8% through a metering pump and a spinneret, and is obtained after coagulation, drawing, washing and drying. Sodium alginate fiber can be dyed. In the above steps, the fiber is drawn using a three-stage drawing process, each stage is drawn 1.8 to 2.2 times, the fiber washing temperature is 50°C, and the drying temperature is 80°C.

上述实施例中,我们选用第二代(2.0代)聚酰胺-胺树状大分子化合物,当然,我们也可以选用第一代(1.0代)、第三代(3.0代)或第四代(4.0代)聚酰胺-胺树状大分子化合物,用以达到相同或相近似的技术效果。In the above-mentioned embodiment, we select the second generation (2.0 generation) polyamide-amine dendrimers for use, of course, we can also select the first generation (1.0 generation), the third generation (3.0 generation) or the fourth generation ( 4.0 generation) polyamide-amine dendrimers to achieve the same or similar technical effects.

上述实施例中,聚酰胺-胺树状大分子化合物与海藻酸钠的加入顺序也可以变换,即先向蒸馏水中加入海藻酸钠制取海藻酸钠水溶液,然后向海藻酸钠水溶液中加入水溶性的聚酰胺-胺树状大分子化合物。In the above examples, the order of adding the polyamide-amine dendrimer compound and sodium alginate can also be changed, that is, first add sodium alginate to distilled water to prepare a sodium alginate aqueous solution, and then add water-soluble sodium alginate to the sodium alginate aqueous solution. non-toxic polyamide-amine dendrimers.

上述实施例中,脱泡工艺可以在减压条件下脱泡12~24h,也可以静置脱泡24~36h。In the above-mentioned embodiments, the degassing process can be degassed under reduced pressure for 12-24 hours, or left standing for 24-36 hours.

有必要指出的是,上述实施例只用于对本发明进一步说明,不能理解为对本发明保护范围的限制,从事该领域的技术人员根据上述发明内容的指导,对本发明所做出的一些非本质性的改进和调整仍属于本发明的保护范围。It must be pointed out that the above-mentioned embodiments are only used to further illustrate the present invention, and should not be interpreted as limiting the protection scope of the present invention. Those skilled in the art will make some non-essential aspects of the present invention according to the guidance of the above-mentioned content of the invention. Improvements and adjustments still belong to the protection scope of the present invention.

普通海藻酸盐纤维和实施例1、2、3、4、5所得到的可染海藻酸盐纤维的性能如表1所示。The properties of common alginate fibers and the dyeable alginate fibers obtained in Examples 1, 2, 3, 4, and 5 are shown in Table 1.

表1普通和可染海藻酸盐纤维的性能Table 1 Properties of ordinary and dyeable alginate fibers

Figure G2010100115204D00041
Figure G2010100115204D00041

注:1.纤维的染色工艺如下:Note: 1. The fiber dyeing process is as follows:

称取0.04克活性染料(活性艳红K-2G,活性黄K-RN,活性艳蓝P-3R)加入到100克水中搅拌溶解,在60℃下投入2克海藻酸盐纤维,染色30min。然后在90℃的水中煮洗10min,再用冷水洗5min,在80℃烘干或者晾干。Weigh 0.04 g of reactive dyes (reactive brilliant red K-2G, reactive yellow K-RN, reactive brilliant blue P-3R) into 100 g of water, stir and dissolve, add 2 g of alginate fiber at 60°C, and dye for 30 minutes. Then boil and wash in 90°C water for 10 minutes, then wash in cold water for 5 minutes, and dry at 80°C or dry in the air.

2.参照国家标准《GB/T 3921-2008纺织品色牢度试验耐皂洗色牢度》测试纤维的水洗色牢度。实施例1、2、3、4、5所得海藻酸盐纤维对活性艳红K-2G、活性黄K-RN和活性艳蓝P-3R的皂洗色牢度均达到或超过4级。2. Refer to the national standard "GB/T 3921-2008 Textile Color Fastness Test Color Fastness to Soaping" to test the color fastness to washing of the fiber. The color fastness to soaping of the alginate fibers obtained in Examples 1, 2, 3, 4 and 5 to reactive brilliant red K-2G, reactive yellow K-RN and reactive brilliant blue P-3R all reached or exceeded grade 4.

Claims (7)

1. the manufacturing approach of a stainable alginate fibers; It is characterized in that: water miscible dendrimer compound is added in the alginate aqueous solution; Adopt wet spinning equipment and technology, through solidify, drawing-off, washing and post processing, obtain stainable alginate fibers;
The content of above-mentioned water miscible dendrimer compound in stainable alginate fibers is 1%~10%, by weight percentage;
The dendritic macromole compound that above-mentioned water miscible dendrimer compound is the polyamide-amide class.
2. the manufacturing approach of stainable alginate fibers according to claim 1 is characterized in that the polyamide-amide class dendritic macromole compound of being selected for use is any one in the 1.0 generation~4.0 generation polyamide-amide dendrimer compounds.
3. the manufacturing approach of stainable alginate fibers according to claim 2 is characterized in that may further comprise the steps:
A takes by weighing an amount of polyamide-amide dendrimer compound, and it is dissolved in the distilled water;
B chooses an amount of alginate and is dissolved in the polyamide-amide dendrimer aqueous solution that step a obtained, and makes mass percent concentration and be 3%~8% alginate fibre spinning solution; Wherein, polyamide-amide dendrimer compound is 1%~10% to the mass percent of alginate;
It is 2%~10% aqueous coagulant solution that c chooses an amount of coagulating agent mass percent concentration that makes soluble in water, uses coagulating bath as spinning;
The alginate fibre spinning solution that d produces step b through filter and deaeration after, get under pressure in the coagulating bath that step c produces and solidify, after drawing-off, washing and drying, obtain stainable alginate fibers again.
4. the manufacturing approach of stainable alginate fibers according to claim 3 is characterized in that among the step b, and the solution temperature of alginate is 20 ℃~40 ℃, and under this temperature mechanical agitation 2~6 hours.
5. the manufacturing approach of stainable alginate fibers according to claim 3 is characterized in that among the step c, and said coagulating agent is any one or a few the combination in calcium chloride, barium chloride, aluminium chloride, the copper sulphate reagent.
6. the manufacturing approach of stainable alginate fibers according to claim 3, it is characterized in that in the said steps d: the deaeration technology of alginate fibre spinning solution is vacuum deaerator 12~24h or standing and defoaming 24~36h; The temperature of coagulating bath is 25 ℃~60 ℃; Three sections draft process are adopted in the drawing-off of fiber, 1.1~2.2 times of every section drawing-offs; The washing temperature of fiber is 20 ℃~50 ℃, and bake out temperature is 40 ℃~80 ℃.
7. the manufacturing approach of stainable alginate fibers according to claim 3 is characterized in that among the step b, and said alginate is sodium alginate or potassium alginate.
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