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CN106468026A - Cotton fiber dye and its dyeing method for supercritical CO2 fluid dyeing - Google Patents

Cotton fiber dye and its dyeing method for supercritical CO2 fluid dyeing Download PDF

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Publication number
CN106468026A
CN106468026A CN201510505713.8A CN201510505713A CN106468026A CN 106468026 A CN106468026 A CN 106468026A CN 201510505713 A CN201510505713 A CN 201510505713A CN 106468026 A CN106468026 A CN 106468026A
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Prior art keywords
dyeing
dye
kettle
fluid
supercritical
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Inventor
莫崧鹰
李世豪
陈永敏
尚颂民
龙家杰
冉瑞龙
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Hong Kong Research Institute of Textiles and Apparel Ltd
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Hong Kong Research Institute of Textiles and Apparel Ltd
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Priority to CN201510505713.8A priority Critical patent/CN106468026A/en
Priority to PCT/CN2015/087662 priority patent/WO2017028306A1/en
Publication of CN106468026A publication Critical patent/CN106468026A/en
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09BORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B62/00Reactive dyes, i.e. dyes which form covalent bonds with the substrates or which polymerise with themselves
    • C09B62/02Reactive dyes, i.e. dyes which form covalent bonds with the substrates or which polymerise with themselves with the reactive group directly attached to a heterocyclic ring
    • C09B62/04Reactive dyes, i.e. dyes which form covalent bonds with the substrates or which polymerise with themselves with the reactive group directly attached to a heterocyclic ring to a triazine ring
    • C09B62/08Azo dyes
    • C09B62/085Monoazo dyes
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/38General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using reactive dyes
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/44General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/94General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using dyes dissolved in solvents which are in the supercritical state
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P3/00Special processes of dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form, classified according to the material treated
    • D06P3/58Material containing hydroxyl groups
    • D06P3/60Natural or regenerated cellulose
    • D06P3/66Natural or regenerated cellulose using reactive dyes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Coloring (AREA)

Abstract

The invention provides a method for supercritical CO2A fluid dyed cotton fiber dye and a method of dyeing the same, the method of dyeing comprising the steps of: step S1, providing a dyeing system, wherein the dyeing system comprises a dye kettle and a dyeing kettle, and the dye kettle and the dyeing kettle are communicated with each other; s2, dissolving cotton fiber dye in a fluid modifier, putting the cotton fiber dye and the fluid modifier into a dye kettle together, and closing the dye kettle; putting the fabric into a dyeing kettle, and then closing the dyeing kettle; step S3, injecting liquid carbon dioxide into the dyeing system, and heating and pressurizing the dyeing system to convert the liquid carbon dioxide into supercritical CO2Fluid and subjecting the supercritical CO2Dissolving cotton fiber dye by using a fluid; then the supercritical CO is enabled2The fluid circulates in the dye kettle and the dyeing kettle, thereby completing dyeing. The cotton fiber dye has excellent adsorption dyeing property, and the synthetic method of the cotton fiber dye is simple in process.

Description

用于超临界CO2流体染色的棉纤维染料及其染色方法Cotton fiber dye and its dyeing method for supercritical CO2 fluid dyeing

技术领域technical field

本发明涉及染料领域,尤其涉及一种用于超临界CO2流体染色的棉纤维染料及其染色方法。The invention relates to the field of dyes, in particular to a cotton fiber dye used for supercritical CO2 fluid dyeing and a dyeing method thereof.

背景技术Background technique

超临界CO2流体是一种緑色、环保的流体介质,以其代替传统水浴对纤维纺织品进行染色加工,具有环保、清洁生产的特点,以及突出的节能降耗效应,对改变传统纺织印染行业水资源消耗高、排污量大、环境污染严重等现状具有重要意义。Supercritical CO 2 fluid is a kind of green and environment-friendly fluid medium. It replaces the traditional water bath for dyeing and processing fiber textiles. It has the characteristics of environmental protection and clean production, as well as outstanding energy saving and consumption reduction effects. The status quo of high resource consumption, large amount of sewage discharge, and serious environmental pollution is of great significance.

目前采用分散染料对涤纶等合成纤维染色的研究居多,且部分已经实现工业化生产。但是目前在超临界CO2流体中直接采用分散染料对亲水性的棉、羊毛和蚕丝等天然纤维进行染色尚不能达到商业化要求。其中,棉纤维在全球纺织工业中的市场份额高达37%,是最重要的天然纤维,也是在超临界CO2流体中最难染色的天然纤维之一。目前,棉纤维主要采用三种染色途径:一是改变流体极性,但染色效果不理想;二是对天然纤维改性后染色,但降低了天然纤维原本优越的性能;三是利用在可溶于超临界CO2流体的染料母体结构中引入活性基,从而使染料可与纤维反应而固着,但其相关报导甚少。At present, most studies on dyeing polyester and other synthetic fibers with disperse dyes have been carried out, and some of them have been industrialized. However, the direct use of disperse dyes in supercritical CO 2 fluid to dye hydrophilic natural fibers such as cotton, wool and silk cannot meet the commercial requirements. Among them, cotton fiber has a market share of up to 37% in the global textile industry, is the most important natural fiber, and is also one of the most difficult natural fibers to dye in supercritical CO2 fluid. At present, cotton fibers are mainly dyed in three ways: one is to change the polarity of the fluid, but the dyeing effect is not ideal; the other is to modify and dye natural fibers, but the original superior performance of natural fibers is reduced; the third is to use soluble The introduction of active groups into the matrix structure of dyes in supercritical CO 2 fluids allows dyes to react with fibers and fix them, but there are few related reports.

此外,与传统水浴染色系统相比,超临界CO2流体属于疏水性介质;这样,在常规水浴中容易实现的(天然)纤维膨胀、染料的扩散及采用碱剂促进固色反应等在超临界CO2流体中难以实现。因而在超临界CO2流体染色过程中,如何打开纤维大分子链间的氢键,以及如何提高染料活性基与纤维上官能团的反应,是采用活性分散染料使天然棉纤维在超临界CO2流体中染色以获得满意染色效果的关键。因此,在实际生产中,往往需大量采用各类溶剂(一般为所染纺织品重量的30%~50%或以上)或其它润湿膨化剂、纤维改性剂等对亲水性天然纤维纺织品进行预处理,以帮助纤维膨化、提高染料的上染,或对纤维进行氨化改性,提高染料在纤维上的固着率,这增大了染色过程的复杂性,并提高了生产成本。In addition, compared with the traditional water-bath dyeing system, supercritical CO 2 fluid is a hydrophobic medium; thus, (natural) fiber expansion, dye diffusion and the use of alkaline agents to promote color fixation reactions, etc. Difficult to achieve in CO 2 fluid. Therefore, in the supercritical CO2 fluid dyeing process, how to open the hydrogen bond between the fiber macromolecular chains, and how to improve the reaction of the dye active group and the functional group on the fiber, is to use reactive disperse dyes to make natural cotton fibers in supercritical CO2 fluid. The key to medium dyeing to obtain satisfactory dyeing results. Therefore, in actual production, it is often necessary to use a large amount of various solvents (generally 30% to 50% or more of the weight of the dyed textiles) or other wetting bulking agents, fiber modifiers, etc. to treat hydrophilic natural fiber textiles. Pretreatment to help fiber bulking, improve dye uptake, or ammonify fiber to improve the fixation rate of dye on fiber, which increases the complexity of the dyeing process and increases the production cost.

发明内容Contents of the invention

本发明针对在常规水浴中容易实现的纤维膨胀、染料的扩散及采用碱剂促进固色反应等在超临界CO2流体中难以实现,同时,在实际生产中,往往需大量采用各类溶剂或其它润湿膨化剂、纤维改性剂等对亲水性天然纤维纺织品进行预处理,以帮助纤维膨化、提高染料的上染,或对纤维进行氨化改性,提高染料在纤维上的固着率,这增大了染色过程的复杂性,并提高了生产成本的问题,提出了一种染色过程简单的用于超临界CO2流体染色的棉纤维染料及其染色方法。The present invention aims at fiber expansion, dye diffusion and the use of alkaline agents to promote color fixation reactions, which are easy to achieve in conventional water baths, but are difficult to achieve in supercritical CO2 fluids. At the same time, in actual production, it is often necessary to use a large number of various solvents or Other wetting and bulking agents, fiber modifiers, etc. pretreat hydrophilic natural fiber textiles to help the fibers expand and improve the dyeing of dyes, or ammonify the fibers to improve the fixation rate of the dyes on the fibers , which increases the complexity of the dyeing process and increases the production cost, a cotton fiber dye and its dyeing method for supercritical CO 2 fluid dyeing with a simple dyeing process are proposed.

本发明提出解决上述技术问题的技术方案如下:The technical scheme that the present invention proposes to solve the above-mentioned technical problem is as follows:

本发明提出了一种用于超临界CO2流体染色的棉纤维染料的染色方法,包括以下步骤:The present invention proposes a kind of dyeing method that is used for the cotton fiber dyestuff of supercritical CO2fluid dyeing, comprises the following steps:

步骤S1、提供染色系统,该染色系统包括染料釜和染色釜,染料釜和染色釜互相连通;Step S1, providing a dyeing system, the dyeing system includes a dye kettle and a dye kettle, and the dye kettle and the dye kettle are connected to each other;

步骤S2、将棉纤维染料溶解于流体改性剂中,再一起投入到染料釜中,然后关闭染料釜;将织物放入到染色釜中,再关闭染色釜;Step S2, dissolving the cotton fiber dye in the fluid modifier, putting them into the dye kettle together, and then closing the dye kettle; putting the fabric into the dye kettle, and then closing the dye kettle;

步骤S3、将液态二氧化碳注入到染色系统中,再使染色系统升温和增压,使液态二氧化碳转化为超临界CO2流体,并使该超临界CO2流体溶解棉纤维染料;然后再使超临界CO2流体在染料釜、染色釜中循环,从而使超临界CO2流体携带棉纤维染料扩散到织物的棉纤维表面和内部,进而完成染色;Step S3, inject liquid carbon dioxide into the dyeing system, then heat up and pressurize the dyeing system, convert the liquid carbon dioxide into a supercritical CO2 fluid, and make the supercritical CO2 fluid dissolve the cotton fiber dye; The CO 2 fluid circulates in the dye kettle and the dyeing kettle, so that the supercritical CO 2 fluid carries the cotton fiber dye and diffuses to the surface and inside of the cotton fiber of the fabric, and then the dyeing is completed;

步骤S4、完成染色后,清洗浮色;再使染色系统降温和减压,最后,打开染色釜,取出染色后的织物。Step S4, after the dyeing is completed, the floating color is cleaned; then the dyeing system is cooled and decompressed, and finally, the dyeing kettle is opened to take out the dyed fabric.

本发明上述的染色方法中,所述染色系统还包括用于预热液态二氧化碳的预热器、用于注入液态二氧化碳的增压泵、用于使超临界CO2流体在染料釜和染色釜中循环的循环泵。In the above-mentioned dyeing method of the present invention, the dyeing system also includes a preheater for preheating liquid carbon dioxide, a booster pump for injecting liquid carbon dioxide, and a supercritical CO2 fluid in the dye kettle and the dye kettle Circulation pump for circulation.

本发明上述的染色方法中,所述染色釜具有中空且管壁布满通孔的染色轴;所述步骤S2还包括:将织物卷绕在该染色轴上。In the above-mentioned dyeing method of the present invention, the dyeing kettle has a hollow dyeing shaft whose wall is covered with through holes; the step S2 further includes: winding the fabric on the dyeing shaft.

本发明上述的染色方法中,所述步骤S3还包括:当染色系统中的温度和压力达到染色工艺所需要的温度和压力时,关闭增压泵;其中,染色工艺所需温度为80℃-100℃,所需压力为20MPa-30MPa;In the above-mentioned dyeing method of the present invention, the step S3 also includes: when the temperature and pressure in the dyeing system reach the temperature and pressure required by the dyeing process, turn off the booster pump; wherein, the temperature required by the dyeing process is 80°C- 100℃, the required pressure is 20MPa-30MPa;

然后打开循环泵,使超临界CO2流体在染料釜和染色釜中循环。Then turn on the circulation pump to circulate the supercritical CO2 fluid in the dye kettle and the dye kettle.

本发明上述的染色方法中,超临界CO2流体在染料釜和染色釜中的循环是正向循环和反向循环交替进行。In the above-mentioned dyeing method of the present invention, the circulation of the supercritical CO2 fluid in the dye kettle and the dye kettle is forward circulation and reverse circulation alternately.

本发明还提出了一种采用如上所述的染色方法染色的棉纤维染料,具有均三嗪型活性基。The present invention also proposes a cotton fiber dye dyed by the above-mentioned dyeing method, which has a s-triazine type active group.

本发明的棉纤维染料因其均三嗪型活性基,能与棉纤维发生键合反应,从而使染料固色于棉纤维上,达到染色的效果。本发明的棉纤维染料具有优秀的吸附上染特性。此外,本发明的棉纤维染料的合成方法工艺过程简单;因此,本发明的用于超临界二氧化碳流体染色的棉纤维染料及其合成方法具有非常广阔的应用前景。Because of the s-triazine active group, the cotton fiber dye of the invention can react with the cotton fiber, so that the dye can be fixed on the cotton fiber to achieve the effect of dyeing. The cotton fiber dye of the invention has excellent adsorption and dyeing properties. In addition, the synthesis method of the cotton fiber dye of the present invention has a simple process; therefore, the cotton fiber dye for supercritical carbon dioxide fluid dyeing and its synthesis method of the present invention have very broad application prospects.

附图说明Description of drawings

下面将结合附图及实施例对本发明作进一步说明,附图中:The present invention will be further described below in conjunction with accompanying drawing and embodiment, in the accompanying drawing:

图1为黄色棉纤维染料的合成路线图;Fig. 1 is the synthetic roadmap of yellow cotton fiber dye;

图2为图1所示的黄色棉纤维染料的工艺流程图;Fig. 2 is the process flow diagram of the yellow cotton fiber dye shown in Fig. 1;

图3为本发明第一实施例的黄色棉纤维染料的超临界CO2流体染色的工艺路线图;Fig. 3 is the supercritical CO of the yellow cotton fiber dyestuff of the first embodiment of the present invention The process roadmap of fluid dyeing;

图4为采用SCF-Y1染料进行超临界CO2流体染色的棉织物的第一示意图;Fig. 4 adopts SCF-Y1 dyestuff to carry out the first schematic diagram of the cotton fabric of supercritical CO2fluid dyeing;

图5为采用SCF-Y1染料进行超临界CO2流体染色的棉织物的第二示意图;Fig. 5 adopts SCF-Y1 dyestuff to carry out the second schematic diagram of the cotton fabric of supercritical CO2fluid dyeing;

图6为采用SCF-Y1染料进行超临界CO2流体染色的棉织物的第三示意图;Fig. 6 adopts SCF-Y1 dyestuff to carry out the 3rd schematic diagram of the cotton fabric of supercritical CO2fluid dyeing;

图7为采用SCF-Y1染料进行超临界CO2流体染色的棉织物的第四示意图;Fig. 7 is the 4th schematic diagram of the cotton fabric that adopts SCF-Y1 dyestuff to carry out supercritical CO 2 fluid dyeing;

图8为蓝色棉纤维染料的合成路线图;Fig. 8 is the synthetic roadmap of blue cotton fiber dyestuff;

图9为图8所示的蓝色棉纤维染料的工艺流程图;Fig. 9 is the process flow diagram of the blue cotton fiber dye shown in Fig. 8;

图10为本发明第二实施例的蓝色棉纤维染料的超临界CO2流体染色的工艺路线图;Fig. 10 is the supercritical CO of the blue cotton fiber dyestuff of the second embodiment of the present invention The process roadmap of fluid dyeing;

图11为采用SCF-B1染料进行超临界CO2流体染色并经过熨干和皂煮工艺的棉织物的示意图;Fig. 11 is the schematic diagram of the cotton fabric that adopts SCF-B1 dyestuff to carry out supercritical CO Fluid dyeing and through ironing and soaping process;

图12为采用SCF-B1染料进行超临界CO2流体染色并经过熨干和丙酮处理的棉织物的示意图;Figure 12 is a schematic diagram of a cotton fabric dyed with SCF-B1 dye by supercritical CO fluid, ironed and treated with acetone;

图13为采用SCF-B1染料进行超临界CO2流体染色并经过皂煮工艺处理的棉织物的示意图;Fig. 13 is the schematic diagram that adopts SCF-B1 dyestuff to carry out supercritical CO Fluid dyeing and process cotton fabric through soaping process;

图14为采用SCF-B1染料进行超临界CO2流体染色并经过熨干和固色工艺处理的棉织物的示意图;Fig. 14 is the schematic diagram of adopting SCF-B1 dyestuff to carry out supercritical CO Fluid dyeing and the cotton fabric that is processed through ironing and fixation process;

图15为红色棉纤维染料的合成路线图;Fig. 15 is the synthetic route figure of red cotton fiber dyestuff;

图16示出了图15所示的红色棉纤维染料的工艺流程图;Fig. 16 shows the process flow diagram of the red cotton fiber dye shown in Fig. 15;

图17为本发明第三实施例的红色棉纤维染料的超临界CO2流体染色的工艺路线图;Fig. 17 is the supercritical CO of the red cotton fiber dyestuff of the third embodiment of the present invention The process roadmap of fluid dyeing;

图18为采用SCF-R1染料进行超临界CO2流体染色的棉织物的示意图。Fig. 18 is a schematic diagram of cotton fabric dyed by supercritical CO2 fluid using SCF-R1 dye.

具体实施方式detailed description

本发明要解决的技术问题是:超临界CO2流体属于疏水性介质;这样,在常规水浴中容易实现的(天然)纤维膨胀、染料的扩散及采用碱剂促进固色反应等在超临界CO2流体中难以实现;同时,在实际生产中,往往需大量采用各类溶剂(一般为所染纺织品重量的30%~50%或以上)或其它润湿膨化剂、纤维改性剂等对亲水性天然纤维纺织品进行预处理,以帮助纤维膨化、提高染料的上染,或对纤维进行氨化改性,提高染料在纤维上的固着率,这增大了染色过程的复杂性,并提高了生产成本。本发明解决该技术问题的技术思路是:采用具有均三嗪型活性基的活性分散染料在超临界CO2流体中对棉纤维进行染色。由于活性分散染料具有均三嗪型活性基,而在超临界CO2流体中进行染色时,均三嗪型活性基会与纤维发生键合反应,从而使活性分散染料固色于棉纤维上。The technical problem to be solved in the present invention is: supercritical CO The fluid belongs to the hydrophobic medium; 2 It is difficult to realize in fluid; at the same time, in actual production, it is often necessary to use a large amount of various solvents (generally 30% to 50% or more of the weight of the dyed textile) or other wetting bulking agents, fiber modifiers, etc. Water-based natural fiber textiles are pretreated to help fiber bulking, improve dye uptake, or ammonify fibers to improve the fixation rate of dyes on fibers, which increases the complexity of the dyeing process and improves the dyeing process. production cost. The technical thinking of the present invention to solve this technical problem is: adopt the reactive disperse dye that has s-triazine type active group to dye cotton fiber in supercritical CO 2 fluid. Since the reactive disperse dye has a s-triazine active group, when dyeing in a supercritical CO2 fluid, the s-triazine active group will react with the fiber, so that the reactive disperse dye can be fixed on the cotton fiber.

在本发明中,用于超临界CO2流体染色的棉纤维染料具有均三嗪型活性基。In the present invention, the cotton fiber dyes used for supercritical CO2 fluid dyeing have s-triazine type active groups.

该棉纤维染料的合成方法包括以下步骤:The synthetic method of this cotton fiber dyestuff comprises the following steps:

步骤1、以三聚氯氰(TCT)为活性基,并将染料母体和活性基均投入到单一或混合溶剂中,使其完全溶解,从而得到反应体系;Step 1, using cyanuric chloride (TCT) as the active group, and putting the dye matrix and the active group into a single or mixed solvent to completely dissolve it, thereby obtaining a reaction system;

步骤2、将反应体系置于0℃~5℃的冰浴中,然后向反应体系中滴加三聚氯氰溶液及捕酸剂,直到反应体系的缩合反应结束;Step 2, placing the reaction system in an ice bath at 0°C to 5°C, and then adding cyanuric chloride solution and an acid scavenger dropwise to the reaction system until the condensation reaction of the reaction system ends;

步骤3、对缩合反应结束的反应体系进行稀释,经洗涤、过滤、干燥得到棉纤维染料。Step 3, diluting the reaction system after the condensation reaction, washing, filtering and drying to obtain the cotton fiber dye.

在上述合成方法中,染料母体可以为1,4-二氨基蒽醌、分散橙3或分散蓝35。当染料母体为1,4-二氨基蒽醌时,棉纤维染料为红色,记为活性分散红SCF-R1;当染料母体为分散橙3时,棉纤维染料为黄色,记为活性分散黄SCF-Y1;当染料母体为分散蓝35时,棉纤维染料为蓝色,记为活性分散蓝SCF-B1;根据三原色配色原理,通过红、黄、蓝三种颜色的棉纤维染料,便可以配出其他各种颜色的棉纤维染料。In the above synthesis method, the dye matrix can be 1,4-diaminoanthraquinone, disperse orange 3 or disperse blue 35. When the dye parent is 1,4-diaminoanthraquinone, the cotton fiber dye is red, which is recorded as reactive disperse red SCF-R1; when the dye parent is disperse orange 3, the cotton fiber dye is yellow, which is recorded as reactive disperse yellow SCF -Y1; when the dye matrix is disperse blue 35, the cotton fiber dye is blue, which is recorded as reactive disperse blue SCF-B1; according to the principle of color matching of three primary colors, cotton fiber dyes of red, yellow and blue can be formulated. Cotton fiber dyes in various other colors.

在本发明中,上述棉纤维染料的染色方法包括以下步骤:In the present invention, the dyeing method of above-mentioned cotton fiber dyestuff comprises the following steps:

步骤S1、提供染色系统,该染色系统包括染料釜和染色釜,染料釜和染色釜互相连通;Step S1, providing a dyeing system, the dyeing system includes a dye kettle and a dye kettle, and the dye kettle and the dye kettle are connected to each other;

在本实施例中,染色系统还包括用于预热液态二氧化碳的预热器、用于注入液态二氧化碳的增压泵、用于使超临界CO2流体在染料釜和染色釜中循环的循环泵。In this embodiment, the dyeing system also includes a preheater for preheating liquid carbon dioxide, a booster pump for injecting liquid carbon dioxide, and a circulation pump for circulating supercritical CO fluid in the dye kettle and the dye kettle .

步骤S2、将棉纤维染料溶解于流体改性剂中,再一起投入到染料釜中,然后关闭染料釜;将织物放入到染色釜中,再关闭染色釜;Step S2, dissolving the cotton fiber dye in the fluid modifier, putting them into the dye kettle together, and then closing the dye kettle; putting the fabric into the dye kettle, and then closing the dye kettle;

在本步骤中,染色釜具有中空且管壁布满通孔的染色轴,一般地,该染色轴为不锈钢轴,可以理解,染色轴也可以由其他材料制成。织物被卷绕在该染色轴上。In this step, the dyeing kettle has a hollow dyeing shaft whose wall is covered with through holes. Generally, the dyeing shaft is a stainless steel shaft. It can be understood that the dyeing shaft can also be made of other materials. The fabric is wound on the dyeing shaft.

步骤S3、将液态二氧化碳注入到染色系统中,再使染色系统升温和增压,使液态二氧化碳转化为超临界CO2流体,并使该超临界CO2流体溶解棉纤维染料;然后再使超临界CO2流体在染料釜、染色釜中循环,从而使超临界CO2流体携带棉纤维染料扩散到织物的棉纤维表面和内部,进而完成染色;Step S3, inject liquid carbon dioxide into the dyeing system, then heat up and pressurize the dyeing system, convert the liquid carbon dioxide into a supercritical CO2 fluid, and make the supercritical CO2 fluid dissolve the cotton fiber dye; The CO 2 fluid circulates in the dye kettle and the dyeing kettle, so that the supercritical CO 2 fluid carries the cotton fiber dye and diffuses to the surface and inside of the cotton fiber of the fabric, and then the dyeing is completed;

在本步骤中,当染色系统中的温度和压力达到染色工艺所需要的温度和压力时,则可以关闭增压泵,这里,染色工艺所需温度为80℃-100℃,所需压力为20MPa-30MPa;然后打开循环泵,使超临界CO2流体在染料釜和染色釜中循环。这里,超临界CO2流体在染料釜和染色釜中的循环是正向循环和反向循环交替进行,以促进超临界CO2流体染色的效果更加均匀。In this step, when the temperature and pressure in the dyeing system reach the temperature and pressure required by the dyeing process, the booster pump can be turned off. Here, the required temperature for the dyeing process is 80°C-100°C, and the required pressure is 20MPa -30MPa; Then turn on the circulating pump to circulate the supercritical CO2 fluid in the dye kettle and dyeing kettle. Here, the circulation of the supercritical CO2 fluid in the dye kettle and the dyeing kettle is forward circulation and reverse circulation alternately, so as to promote the dyeing effect of the supercritical CO2 fluid to be more uniform.

步骤S4、完成染色后,清洗浮色;再使染色系统降温和减压,最后,打开染色釜,取出染色后的织物。Step S4, after the dyeing is completed, the floating color is cleaned; then the dyeing system is cooled and decompressed, and finally, the dyeing kettle is opened to take out the dyed fabric.

在本步骤中,通过使染色系统降温和减压,可以将超临界CO2流体分离回收。In this step, the supercritical CO fluid can be separated and recovered by cooling down and depressurizing the dyeing system.

为了使本发明的技术目的、技术方案以及技术效果更加清楚,下面将结合附图及具体实施例对本发明做进一步详细的说明。In order to make the technical purpose, technical solution and technical effect of the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.

第一实施例first embodiment

本实施例提供了一种黄色棉纤维染料的合成方法。This embodiment provides a kind of synthetic method of yellow cotton fiber dye.

具体地,参照图1,图1为黄色棉纤维染料的合成路线,可以看到,本实施例采用分散橙3和三聚氯氰作为原料,使三聚氯氰上的一个Cl取代分散橙3的氨基上的一个H,从而合成出黄色棉纤维染料。Specifically, with reference to Fig. 1, Fig. 1 is the synthetic route of yellow cotton fiber dye, can see, present embodiment adopts disperse orange 3 and cyanuric chloride as raw material, makes a Cl on cyanuric chloride replace disperse orange 3 One H on the amino group, thus synthesizing yellow cotton fiber dye.

参照图2,图2示出了图1所示的黄色棉纤维染料的工艺流程图。With reference to Fig. 2, Fig. 2 has shown the process flowchart of the yellow cotton fiber dye shown in Fig. 1.

黄色棉纤维染料的合成方法包括:The synthetic method of yellow cotton fiber dyestuff comprises:

步骤1、以分散橙3作为染料母体,并将染料母体投入到二氧六环与水的混合溶剂中,使其完全溶解,从而得到反应体系;Step 1, using disperse orange 3 as the dye matrix, and putting the dye matrix into a mixed solvent of dioxane and water to completely dissolve it, thereby obtaining a reaction system;

在二氧六环与水的混合溶剂中,1,4-二氧六环和蒸馏水的质量比为2:1或1:(1~3);In the mixed solvent of dioxane and water, the mass ratio of 1,4-dioxane to distilled water is 2:1 or 1:(1~3);

进一步地,分散橙3采用0.001mol;这里,分散橙3与混合溶剂的质量比决定了反应速度,可以根据具体试验情况而定;Further, Disperse Orange 3 adopts 0.001mol; here, the mass ratio of Disperse Orange 3 and mixed solvent determines the reaction speed, which can be determined according to specific test conditions;

步骤2、将反应体系置于0℃~5℃的冰浴中,以三聚氯氰(TCT)作为活性基,然后向反应体系中滴加三聚氯氰溶液及捕酸剂,直到反应体系的缩合反应结束;Step 2. Place the reaction system in an ice bath at 0°C to 5°C, use cyanuric chloride (TCT) as the active group, and then add cyanuric chloride solution and acid scavenger dropwise to the reaction system until the reaction system The condensation reaction ends;

在本实施例中,捕酸剂采用0.1M的氢氧化钠。三聚氯氰与分散橙3的摩尔比为2:1。In this embodiment, 0.1M sodium hydroxide is used as the acid scavenger. The molar ratio of cyanuric chloride to disperse orange 3 is 2:1.

本步骤还包括:在向反应体系中滴加三聚氯氰溶液及捕酸剂的过程中,对反应体系进行磁力搅拌;在本实施例中,磁力搅拌的时间为3h。This step also includes: during the process of adding the cyanuric chloride solution and the acid scavenger dropwise to the reaction system, magnetic stirring is performed on the reaction system; in this embodiment, the magnetic stirring time is 3 hours.

步骤3、对缩合反应结束的反应体系进行稀释,经洗涤、过滤、干燥得到黄色棉纤维染料。Step 3, diluting the reaction system after the condensation reaction, washing, filtering and drying to obtain the yellow cotton fiber dye.

这里,为了便于之后染色效果的记录,黄色棉纤维染料记为SCF-Y1染料。Here, for the convenience of recording the dyeing effect later, the yellow cotton fiber dye is recorded as SCF-Y1 dye.

参照图3,图3为本发明第一实施例的黄色棉纤维染料的超临界CO2流体染色的工艺路线图。With reference to Fig. 3, Fig. 3 is the process roadmap of the supercritical CO2 fluid dyeing of the yellow cotton fiber dyestuff of the first embodiment of the present invention.

如图3所示,黄色棉纤维染料的超临界CO2流体染色方法包括以下步骤:As shown in Figure 3, the supercritical CO fluid dyeing method of yellow cotton fiber dye includes the following steps:

步骤S1、提供染色系统,该染色系统包括染料釜和染色釜,染料釜和染色釜互相连通;在本实施例中,染色系统还包括用于预热液态二氧化碳的预热器、用于注入液态二氧化碳的增压泵、用于使超临界CO2流体在染料釜和染色釜中循环的循环泵。Step S1, provide a dyeing system, the dyeing system includes a dye kettle and a dyeing kettle, the dye kettle and the dyeing kettle are connected to each other; in this embodiment, the dyeing system also includes a preheater for preheating liquid carbon dioxide, for injecting liquid Booster pump for carbon dioxide, circulation pump for circulating supercritical CO2 fluid in dye kettle and dyeing kettle.

步骤S2、将黄色棉纤维染料溶解于流体改性剂中,再一起投入到染料釜中,然后关闭染料釜;将织物放入到染色釜中,再关闭染色釜;Step S2, dissolving the yellow cotton fiber dye in the fluid modifier, putting them into the dye kettle together, and then closing the dye kettle; putting the fabric into the dye kettle, and then closing the dye kettle;

在本步骤中,黄色棉纤维染料为活性分散黄SCF-Y1,其掺加量为3%o.m.f;流体改性剂为甲醇,其掺加量为超临界CO2流体的10wt%。In this step, the yellow cotton fiber dyestuff is reactive disperse yellow SCF-Y1, and its admixture is 3% omf; the fluid modifier is methyl alcohol, and its admixture is 10wt% of the supercritical CO fluid.

在本步骤中,染色釜具有中空且管壁布满通孔的染色轴,一般地,该染色轴为不锈钢轴,可以理解,染色轴也可以由其他材料制成。织物被卷绕在该染色轴上。In this step, the dyeing kettle has a hollow dyeing shaft whose wall is covered with through holes. Generally, the dyeing shaft is a stainless steel shaft. It can be understood that the dyeing shaft can also be made of other materials. The fabric is wound on the dyeing shaft.

步骤S3、将液态二氧化碳注入到染色系统中,再使染色系统升温和增压,使液态二氧化碳转化为超临界CO2流体,并使该超临界CO2流体溶解黄色棉纤维染料;然后再使超临界CO2流体在染料釜、染色釜中循环,从而使超临界CO2流体携带黄色棉纤维染料扩散到织物的棉纤维表面和内部,进而完成染色;Step S3, inject liquid carbon dioxide into the dyeing system, then heat up and pressurize the dyeing system, convert the liquid carbon dioxide into a supercritical CO2 fluid, and make the supercritical CO2 fluid dissolve the yellow cotton fiber dye; then make the supercritical CO2 fluid dissolve the yellow cotton fiber dye; The critical CO 2 fluid circulates in the dye kettle and the dyeing kettle, so that the supercritical CO 2 fluid carries the yellow cotton fiber dye and diffuses to the surface and interior of the cotton fiber of the fabric, and then the dyeing is completed;

在本步骤中,当染色系统中的温度和压力达到染色工艺所需要的温度和压力时,则可以关闭增压泵,这里,染色工艺所需温度为100℃,所需压力为28MPa;然后打开循环泵,使超临界CO2流体在染料釜和染色釜中循环。这里,超临界CO2流体在染料釜和染色釜中的循环是正向循环和反向循环交替进行,以促进超临界CO2流体染色的效果更加均匀;其中,超临界CO2流体在染料釜和染色釜中循环的循环时间为90min。In this step, when the temperature and pressure in the dyeing system reach the temperature and pressure required by the dyeing process, the booster pump can be turned off. Here, the required temperature for the dyeing process is 100°C and the required pressure is 28MPa; then open Circulation pump to circulate the supercritical CO2 fluid in the dye kettle and dyeing kettle. Here, the circulation of the supercritical CO2 fluid in the dye kettle and the dyeing kettle is forward circulation and reverse circulation alternately, to promote the dyeing effect of the supercritical CO2 fluid to be more uniform; wherein, the supercritical CO2 fluid is in the dye kettle and The cycle time of the cycle in the dyeing kettle is 90min.

步骤S4、完成染色后,清洗浮色;再使染色系统降温和减压,最后,打开染色釜,取出染色后的织物。Step S4, after the dyeing is completed, the floating color is cleaned; then the dyeing system is cooled and decompressed, and finally, the dyeing kettle is opened to take out the dyed fabric.

如图4-7所示,图4-图7为采用不同SCF-Y1染料进行超临界CO2流体染色的棉织物的示意图。As shown in Figures 4-7, Figures 4-7 are schematic diagrams of cotton fabrics dyed with supercritical CO2 fluid using different SCF-Y1 dyes.

这里,图4所采用的SCF-Y1染料的合成方法中,1,4-二氧六环和蒸馏水的质量比为1:1;图5所采用的SCF-Y1染料的合成方法中,1,4-二氧六环和蒸馏水的质量比为1:2;图6所采用的SCF-Y1染料的合成方法中,1,4-二氧六环和蒸馏水的质量比为1:3;图7所采用的SCF-Y1染料的合成方法中,1,4-二氧六环和蒸馏水的质量比为3:1。Here, in the synthetic method of the SCF-Y1 dye that Fig. 4 adopts, the mass ratio of 1,4-dioxane and distilled water is 1:1; In the synthetic method of the SCF-Y1 dye that Fig. 5 adopts, 1, The mass ratio of 4-dioxane and distilled water is 1:2; in the synthetic method of SCF-Y1 dye adopted in Fig. 6, the mass ratio of 1,4-dioxane and distilled water is 1:3; Fig. 7 In the synthetic method of the SCF-Y1 dye used, the mass ratio of 1,4-dioxane to distilled water is 3:1.

第二实施例second embodiment

本实施例提供了一种蓝色棉纤维染料的合成方法。This embodiment provides a kind of synthetic method of blue cotton fiber dye.

具体地,参照图8,图8为蓝色棉纤维染料的合成路线,可以看到,本实施例采用分散蓝35和三聚氯氰作为原料,使三聚氯氰上的一个Cl取代分散蓝35的羟基上的一个H,从而合成出蓝色棉纤维染料。Specifically, referring to Fig. 8, Fig. 8 is a synthetic route of blue cotton fiber dye, as can be seen, the present embodiment adopts disperse blue 35 and cyanuric chloride as raw materials, so that a Cl on cyanuric chloride replaces disperse blue One H on the hydroxyl group of 35, thereby synthesizing the blue cotton fiber dye.

参照图9,图9示出了图8所示的蓝色棉纤维染料的工艺流程图。Referring to FIG. 9, FIG. 9 shows a process flow diagram of the blue cotton fiber dye shown in FIG. 8.

蓝色棉纤维染料的合成方法包括:The synthetic method of blue cotton fiber dyestuff comprises:

步骤1、以分散蓝35作为染料母体,并将染料母体投入到四氢呋喃与水的混合溶剂中,使其完全溶解,从而得到反应体系;Step 1. Use disperse blue 35 as the dye matrix, and put the dye matrix into a mixed solvent of tetrahydrofuran and water to completely dissolve it, thereby obtaining a reaction system;

在四氢呋喃与水的混合溶剂中,四氢呋喃与蒸馏水的质量比为3:1;In the mixed solvent of tetrahydrofuran and water, the mass ratio of tetrahydrofuran and distilled water is 3:1;

进一步地,分散蓝35采用0.001mol;这里,分散蓝35与混合溶剂的比例决定了反应速度,可以根据具体试验情况而定;Further, disperse blue 35 adopts 0.001mol; here, the ratio of disperse blue 35 and mixed solvent determines the reaction speed, which can be determined according to specific test conditions;

步骤2、将反应体系置于0℃~5℃的冰浴中,以三聚氯氰(TCT)作为活性基,然后向反应体系中滴加三聚氯氰溶液及捕酸剂,直到反应体系的缩合反应结束;Step 2. Place the reaction system in an ice bath at 0°C to 5°C, use cyanuric chloride (TCT) as the active group, and then add cyanuric chloride solution and acid scavenger dropwise to the reaction system until the reaction system The condensation reaction ends;

在本实施例中,捕酸剂采用0.1M的氢氧化钠。三聚氯氰与分散蓝35的摩尔比为2:1。In this embodiment, 0.1M sodium hydroxide is used as the acid scavenger. The molar ratio of cyanuric chloride to disperse blue 35 is 2:1.

本步骤还包括:在向反应体系中滴加三聚氯氰溶液及捕酸剂的过程中,对反应体系进行磁力搅拌;在本实施例中,磁力搅拌的时间为3h。This step also includes: during the process of adding the cyanuric chloride solution and the acid scavenger dropwise to the reaction system, magnetic stirring is performed on the reaction system; in this embodiment, the magnetic stirring time is 3 hours.

步骤3、对缩合反应结束的反应体系进行稀释,经洗涤、过滤、干燥得到蓝色棉纤维染料。Step 3, diluting the reaction system after the condensation reaction, washing, filtering and drying to obtain the blue cotton fiber dye.

这里,为了便于之后染色效果的记录,蓝色棉纤维染料记为SCF-B1染料。Here, in order to facilitate the recording of the dyeing effect later, the blue cotton fiber dye is recorded as SCF-B1 dye.

参照图10,图10为本发明第二实施例的蓝色棉纤维染料的超临界CO2流体染色的工艺路线图。Referring to FIG. 10 , FIG. 10 is a process roadmap of supercritical CO 2 fluid dyeing of blue cotton fiber dyes according to the second embodiment of the present invention.

如图10所示,蓝色棉纤维染料的超临界CO2流体染色方法包括以下步骤:As shown in Figure 10, the supercritical CO2 fluid dyeing method of blue cotton fiber dye includes the following steps:

步骤S1、提供染色系统,该染色系统包括染料釜和染色釜,染料釜和染色釜互相连通;在本实施例中,染色系统还包括用于预热液态二氧化碳的预热器、用于注入液态二氧化碳的增压泵、用于使超临界CO2流体在染料釜和染色釜中循环的循环泵。Step S1, provide a dyeing system, the dyeing system includes a dye kettle and a dyeing kettle, the dye kettle and the dyeing kettle are connected to each other; in this embodiment, the dyeing system also includes a preheater for preheating liquid carbon dioxide, for injecting liquid Booster pump for carbon dioxide, circulation pump for circulating supercritical CO2 fluid in dye kettle and dyeing kettle.

步骤S2、将蓝色棉纤维染料溶解于流体改性剂中,再一起投入到染料釜中,然后关闭染料釜;将织物放入到染色釜中,再关闭染色釜;Step S2, dissolving the blue cotton fiber dye in the fluid modifier, putting them into the dye kettle together, and then closing the dye kettle; putting the fabric into the dye kettle, and then closing the dye kettle;

在本步骤中,蓝色棉纤维染料为活性分散蓝SCF-B1,其掺加量为2%o.m.f;流体改性剂为甲醇,其掺加量为超临界CO2流体的10wt%。In this step, the blue cotton fiber dye is reactive disperse blue SCF-B1, and its admixture is 2% omf; the fluid modifier is methyl alcohol, and its admixture is 10wt% of the supercritical CO fluid.

在本步骤中,染色釜具有中空且管壁布满通孔的染色轴,一般地,该染色轴为不锈钢轴,可以理解,染色轴也可以由其他材料制成。织物被卷绕在该染色轴上。In this step, the dyeing kettle has a hollow dyeing shaft whose wall is covered with through holes. Generally, the dyeing shaft is a stainless steel shaft. It can be understood that the dyeing shaft can also be made of other materials. The fabric is wound on the dyeing shaft.

步骤S3、将液态二氧化碳注入到染色系统中,再使染色系统升温和增压,使液态二氧化碳转化为超临界CO2流体,并使该超临界CO2流体溶解蓝色棉纤维染料;然后再使超临界CO2流体在染料釜、染色釜中循环,从而使超临界CO2流体携带蓝色棉纤维染料扩散到织物的棉纤维表面和内部,进而完成染色;Step S3, injecting liquid carbon dioxide into the dyeing system, then heating and pressurizing the dyeing system, converting the liquid carbon dioxide into a supercritical CO2 fluid, and making the supercritical CO2 fluid dissolve the blue cotton fiber dye; and then using The supercritical CO 2 fluid circulates in the dye kettle and the dyeing kettle, so that the supercritical CO 2 fluid carries the blue cotton fiber dye and diffuses to the surface and inside of the cotton fiber of the fabric, and then the dyeing is completed;

在本步骤中,当染色系统中的温度和压力达到染色工艺所需要的温度和压力时,则可以关闭增压泵,这里,染色工艺所需温度为100℃,所需压力为30MPa;然后打开循环泵,使超临界CO2流体在染料釜和染色釜中循环。这里,超临界CO2流体在染料釜和染色釜中的循环是正向循环和反向循环交替进行,以促进超临界CO2流体染色的效果更加均匀;其中,超临界CO2流体在染料釜和染色釜中循环的循环时间为120min。In this step, when the temperature and pressure in the dyeing system reach the temperature and pressure required by the dyeing process, the booster pump can be turned off. Here, the required temperature for the dyeing process is 100°C and the required pressure is 30MPa; then open Circulation pump to circulate the supercritical CO2 fluid in the dye kettle and dyeing kettle. Here, the circulation of the supercritical CO2 fluid in the dye kettle and the dyeing kettle is forward circulation and reverse circulation alternately, to promote the dyeing effect of the supercritical CO2 fluid to be more uniform; wherein, the supercritical CO2 fluid is in the dye kettle and The cycle time of the cycle in the dyeing kettle is 120min.

步骤S4、完成染色后,清洗浮色;再使染色系统降温和减压,最后,打开染色釜,取出染色后的织物。Step S4, after the dyeing is completed, the floating color is cleaned; then the dyeing system is cooled and decompressed, and finally, the dyeing kettle is opened to take out the dyed fabric.

如图11-14所示,图11-14为采用SCF-B1染料进行超临界CO2流体染色并经过清洗浮色工艺的棉织物的示意图。As shown in Figures 11-14, Figures 11-14 are schematic diagrams of cotton fabrics dyed with SCF-B1 dyes in supercritical CO 2 fluid and washed and floated.

这里,图11所示的棉织物采用了熨干和皂煮工艺处理,图12所示的棉织物采用了熨干和丙酮处理;图13所示的棉织物仅采用了皂煮工艺处理,图14所示的棉织物采用了熨干和固色工艺处理;Here, the cotton fabric shown in Figure 11 was treated with ironing and soaping, the cotton fabric shown in Figure 12 was ironed and treated with acetone; the cotton fabric shown in Figure 13 was only treated with soaping, and the cotton fabric shown in Figure 13 was only treated with soaping. The cotton fabric shown in 14 has been treated with iron drying and color fixing;

第三实施例third embodiment

本实施例提供了一种红色棉纤维染料的合成方法。This embodiment provides a kind of synthetic method of red cotton fiber dye.

具体地,参照图15,图15为红色棉纤维染料的合成路线,可以看到,本实施例采用1,4-二氨基蒽醌和三聚氯氰作为原料,使三聚氯氰上的一个Cl取代1,4-二氨基蒽醌的一个氨基上的H,或者使两个三聚氯氰上的Cl分别取代1,4-二氨基蒽醌的两个氨基的H,从而合成出红色棉纤维染料。Specifically, referring to Fig. 15, Fig. 15 is a synthesis route of red cotton fiber dye, it can be seen that this embodiment adopts 1,4-diaminoanthraquinone and cyanuric chloride as raw materials to make one on cyanuric chloride Cl replaces the H on one amino group of 1,4-diaminoanthraquinone, or replaces the H on the two amino groups of 1,4-diaminoanthraquinone with Cl on two cyanuric chlorides, thereby synthesizing red cotton Fiber dye.

参照图16,图16示出了图15所示的红色棉纤维染料的工艺流程图。Referring to FIG. 16, FIG. 16 shows a process flow diagram of the red cotton fiber dye shown in FIG. 15.

红色棉纤维染料的合成方法包括:The synthetic method of red cotton fiber dyestuff comprises:

步骤1、以1,4-二氨基蒽醌(即分散紫1)作为染料母体,并将染料母体投入到1,4-二氧六环与水的混合溶剂中,使其完全溶解,从而得到反应体系;Step 1, using 1,4-diaminoanthraquinone (i.e. disperse violet 1) as the dye matrix, and putting the dye matrix into a mixed solvent of 1,4-dioxane and water to completely dissolve it, thereby obtaining reaction system;

在1,4-二氧六环与水的混合溶剂中,1,4-二氧六环与蒸馏水的质量比为4:1;In the mixed solvent of 1,4-dioxane and water, the mass ratio of 1,4-dioxane to distilled water is 4:1;

进一步地,1,4-二氨基蒽醌采用0.001mol;这里,1,4-二氨基蒽醌与混合溶剂的比例决定了反应速度,可以根据具体试验情况而定;Further, 0.001mol is used for 1,4-diaminoanthraquinone; here, the ratio of 1,4-diaminoanthraquinone to the mixed solvent determines the reaction speed, which can be determined according to specific test conditions;

步骤2、将反应体系置于0℃~5℃的冰浴中,以三聚氯氰(TCT)作为活性基,然后向反应体系中滴加三聚氯氰溶液及捕酸剂,直到反应体系的缩合反应结束;Step 2. Place the reaction system in an ice bath at 0°C to 5°C, use cyanuric chloride (TCT) as the active group, and then add cyanuric chloride solution and acid scavenger dropwise to the reaction system until the reaction system The condensation reaction ends;

在本实施例中,捕酸剂采用0.1M的氢氧化钠。三聚氯氰与1,4-二氨基蒽醌的摩尔比为1:3。In this embodiment, 0.1M sodium hydroxide is used as the acid scavenger. The molar ratio of cyanuric chloride to 1,4-diaminoanthraquinone is 1:3.

本步骤还包括:在向反应体系中滴加三聚氯氰溶液及捕酸剂的过程中,对反应体系进行磁力搅拌;在本实施例中,磁力搅拌的时间为2.5h。This step also includes: during the process of adding the cyanuric chloride solution and the acid scavenger dropwise to the reaction system, magnetic stirring is performed on the reaction system; in this embodiment, the magnetic stirring time is 2.5 hours.

步骤3、对缩合反应结束的反应体系进行稀释,经洗涤、过滤、干燥得到红色棉纤维染料。Step 3, diluting the reaction system after the condensation reaction, washing, filtering and drying to obtain the red cotton fiber dye.

这里,为了便于之后染色效果的记录,红色棉纤维染料记为SCF-R1染料。Here, in order to facilitate the recording of the dyeing effect later, the red cotton fiber dye is recorded as SCF-R1 dye.

参照图17,图17为本发明第三实施例的红色棉纤维染料的超临界CO2流体染色的工艺路线图。Referring to Fig. 17, Fig. 17 is a process roadmap of supercritical CO 2 fluid dyeing of red cotton fiber dyes according to the third embodiment of the present invention.

如图17所示,红色棉纤维染料的超临界CO2流体染色方法包括以下步骤:As shown in Figure 17, the supercritical CO2 fluid dyeing method of red cotton fiber dye includes the following steps:

步骤S1、提供染色系统,该染色系统包括染料釜和染色釜,染料釜和染色釜互相连通;在本实施例中,染色系统还包括用于预热液态二氧化碳的预热器、用于注入液态二氧化碳的增压泵、用于使超临界CO2流体在染料釜和染色釜中循环的循环泵。Step S1, provide a dyeing system, the dyeing system includes a dye kettle and a dyeing kettle, the dye kettle and the dyeing kettle are connected to each other; in this embodiment, the dyeing system also includes a preheater for preheating liquid carbon dioxide, for injecting liquid Booster pump for carbon dioxide, circulation pump for circulating supercritical CO2 fluid in dye kettle and dyeing kettle.

步骤S2、将红色棉纤维染料溶解于流体改性剂中,再一起投入到染料釜中,然后关闭染料釜;将织物放入到染色釜中,再关闭染色釜;Step S2, dissolving the red cotton fiber dye in the fluid modifier, putting them into the dye kettle together, and then closing the dye kettle; putting the fabric into the dye kettle, and then closing the dye kettle;

在本步骤中,红色棉纤维染料为活性分散红SCF-R1,其掺加量为3%o.m.f;流体改性剂为甲醇,其掺加量为超临界CO2流体的10wt%。In this step, the red cotton fiber dye is reactive disperse red SCF-R1, and its admixture is 3% omf; the fluid modifier is methanol, and its admixture is 10wt% of the supercritical CO fluid.

在本步骤中,染色釜具有中空且管壁布满通孔的染色轴,一般地,该染色轴为不锈钢轴,可以理解,染色轴也可以由其他材料制成。织物被卷绕在该染色轴上。In this step, the dyeing kettle has a hollow dyeing shaft whose wall is covered with through holes. Generally, the dyeing shaft is a stainless steel shaft. It can be understood that the dyeing shaft can also be made of other materials. The fabric is wound on the dyeing shaft.

步骤S3、将液态二氧化碳注入到染色系统中,再使染色系统升温和增压,使液态二氧化碳转化为超临界CO2流体,并使该超临界CO2流体溶解红色棉纤维染料;然后再使超临界CO2流体在染料釜、染色釜中循环,从而使超临界CO2流体携带红色棉纤维染料扩散到织物的棉纤维表面和内部,进而完成染色;Step S3, inject liquid carbon dioxide into the dyeing system, then heat up and pressurize the dyeing system, convert the liquid carbon dioxide into a supercritical CO2 fluid, and make the supercritical CO2 fluid dissolve the red cotton fiber dye; then make the supercritical CO2 fluid dissolve the red cotton fiber dye; The critical CO 2 fluid circulates in the dye kettle and the dyeing kettle, so that the supercritical CO 2 fluid carries the red cotton fiber dye and diffuses to the surface and interior of the cotton fiber of the fabric, and then completes the dyeing;

在本步骤中,当染色系统中的温度和压力达到染色工艺所需要的温度和压力时,则可以关闭增压泵,这里,染色工艺所需温度为120℃,所需压力为28MPa;然后打开循环泵,使超临界CO2流体在染料釜和染色釜中循环。这里,超临界CO2流体在染料釜和染色釜中的循环是正向循环和反向循环交替进行,以促进超临界CO2流体染色的效果更加均匀;其中,超临界CO2流体在染料釜和染色釜中循环的循环时间为120min。In this step, when the temperature and pressure in the dyeing system reach the temperature and pressure required by the dyeing process, the booster pump can be turned off. Here, the required temperature for the dyeing process is 120°C and the required pressure is 28MPa; then open Circulation pump to circulate the supercritical CO2 fluid in the dye kettle and dyeing kettle. Here, the circulation of the supercritical CO2 fluid in the dye kettle and the dyeing kettle is forward circulation and reverse circulation alternately, to promote the dyeing effect of the supercritical CO2 fluid to be more uniform; wherein, the supercritical CO2 fluid is in the dye kettle and The cycle time of the cycle in the dyeing kettle is 120min.

步骤S4、完成染色后,清洗浮色;再使染色系统降温和减压,最后,打开染色釜,取出染色后的织物。Step S4, after the dyeing is completed, the floating color is cleaned; then the dyeing system is cooled and decompressed, and finally, the dyeing kettle is opened to take out the dyed fabric.

如图18所示,图18为采用SCF-R1染料进行超临界CO2流体染色的棉织物的示意图。As shown in Fig. 18, Fig. 18 is a schematic diagram of cotton fabric dyed with SCF-R1 dye by supercritical CO2 fluid.

从图4-7、11-14、18可以看到,将SCF-Y1染料、SCF-B1染料以及SCF-R1染料应用于超临界CO2流体染色中是可行的;并且SCF-Y1染料、SCF-B1染料以及SCF-R1染料在超临界CO2流体中对棉纤维表现出非常优秀的吸附上染特性,且可在80℃的较低温度条件下实现对棉纤维的上染和反应固着。As can be seen from Figures 4-7, 11-14, and 18, it is feasible to apply SCF-Y1 dyes, SCF-B1 dyes and SCF-R1 dyes to supercritical CO2 fluid dyeing; and SCF-Y1 dyes, SCF -B1 dyes and SCF-R1 dyes showed excellent adsorption and dyeing properties on cotton fibers in supercritical CO 2 fluid, and could achieve dyeing and reactive fixation on cotton fibers at a relatively low temperature of 80°C.

本发明的棉纤维染料因其均三嗪型活性基,能与棉纤维发生键合反应,从而使染料固色于棉纤维上,达到染色的效果。本发明的棉纤维染料具有优秀的吸附上染特性。此外,本发明的棉纤维染料的合成方法工艺过程简单;因此,本发明的用于超临界二氧化碳流体染色的棉纤维染料及其合成方法具有非常广阔的应用前景。Because of the s-triazine active group, the cotton fiber dye of the invention can react with the cotton fiber, so that the dye can be fixed on the cotton fiber to achieve the effect of dyeing. The cotton fiber dye of the invention has excellent adsorption and dyeing properties. In addition, the synthesis method of the cotton fiber dye of the present invention has a simple process; therefore, the cotton fiber dye for supercritical carbon dioxide fluid dyeing and its synthesis method of the present invention have very broad application prospects.

本文所描述和要求权利的发明并不限于此中所公开的具体实施方案的范围,因为这些实施方案只用于本发明几个方面的说明。任何等价的实施方案均将是在本发明的范围内。确实,本领域技术人员从前面所描述可理解在本文所示和所描述的实施方案外可有各种修改。这些修改也在所附权利要求书的范围内。The invention described and claimed herein is not to be limited in scope by the specific embodiments disclosed therein, since these embodiments serve only as illustrations of several aspects of the invention. Any equivalent embodiments are intended to be within the scope of this invention. Indeed, those skilled in the art will appreciate from the foregoing description that various modifications and variations of the embodiments shown and described herein are possible. Such modifications are also within the scope of the appended claims.

Claims (6)

1.一种用于超临界CO2流体染色的棉纤维染料的染色方法,其特征在于,包括以下步骤:1. a kind of dyeing method that is used for supercritical CO The cotton fiber dyestuff of fluid dyeing, it is characterized in that, may further comprise the steps: 步骤S1、提供染色系统,该染色系统包括染料釜和染色釜,染料釜和染色釜互相连通;Step S1, providing a dyeing system, the dyeing system includes a dye kettle and a dye kettle, and the dye kettle and the dye kettle are connected to each other; 步骤S2、将棉纤维染料溶解于流体改性剂中,再一起投入到染料釜中,然后关闭染料釜;将织物放入到染色釜中,再关闭染色釜;Step S2, dissolving the cotton fiber dye in the fluid modifier, putting them into the dye kettle together, and then closing the dye kettle; putting the fabric into the dye kettle, and then closing the dye kettle; 步骤S3、将液态二氧化碳注入到染色系统中,再使染色系统升温和增压,使液态二氧化碳转化为超临界CO2流体,并使该超临界CO2流体溶解棉纤维染料;然后再使超临界CO2流体在染料釜、染色釜中循环,从而使超临界CO2流体携带棉纤维染料扩散到织物的棉纤维表面和内部,进而完成染色;Step S3, inject liquid carbon dioxide into the dyeing system, then heat up and pressurize the dyeing system, convert the liquid carbon dioxide into a supercritical CO2 fluid, and make the supercritical CO2 fluid dissolve the cotton fiber dye; The CO 2 fluid circulates in the dye kettle and the dyeing kettle, so that the supercritical CO 2 fluid carries the cotton fiber dye and diffuses to the surface and inside of the cotton fiber of the fabric, and then the dyeing is completed; 步骤S4、完成染色后,清洗浮色;再使染色系统降温和减压,最后,打开染色釜,取出染色后的织物。Step S4, after the dyeing is completed, the floating color is cleaned; then the dyeing system is cooled and decompressed, and finally, the dyeing kettle is opened to take out the dyed fabric. 2.根据权利要求1所述的染色方法,其特征在于,所述染色系统还包括用于预热液态二氧化碳的预热器、用于注入液态二氧化碳的增压泵、用于使超临界CO2流体在染料釜和染色釜中循环的循环泵。2. dyeing method according to claim 1, is characterized in that, described dyeing system also comprises the preheater that is used for preheating liquid carbon dioxide, is used to inject the booster pump of liquid carbon dioxide, is used to make supercritical CO2 Circulation pump for circulating fluid in dye tank and dye tank. 3.根据权利要求1所述的染色方法,其特征在于,所述染色釜具有中空且管壁布满通孔的染色轴;所述步骤S2还包括:将织物卷绕在该染色轴上。3 . The dyeing method according to claim 1 , wherein the dyeing kettle has a hollow dyeing shaft whose wall is covered with through holes; the step S2 further comprises: winding the fabric on the dyeing shaft. 4 . 4.根据权利要求2所述的染色方法,其特征在于,所述步骤S3还包括:当染色系统中的温度和压力达到染色工艺所需要的温度和压力时,关闭增压泵;其中,染色工艺所需温度为80℃-100℃,所需压力为20MPa-30MPa;4. The dyeing method according to claim 2, characterized in that, said step S3 also includes: when the temperature and pressure in the dyeing system reach the temperature and pressure required by the dyeing process, closing the booster pump; wherein, the dyeing The temperature required for the process is 80°C-100°C, and the required pressure is 20MPa-30MPa; 然后打开循环泵,使超临界CO2流体在染料釜和染色釜中循环。Then turn on the circulation pump to circulate the supercritical CO2 fluid in the dye kettle and the dye kettle. 5.根据权利要求4所述的染色方法,其特征在于,超临界CO2流体在染料釜和染色釜中的循环是正向循环和反向循环交替进行。5. dyeing method according to claim 4 is characterized in that, supercritical CO The circulation of fluid in dye still and dyeing still is that forward circulation and reverse circulation carry out alternately. 6.一种采用如权利要求1-5任意一项的染色方法染色的棉纤维染料,其特征在于,具有均三嗪型活性基。6. A cotton fiber dye dyed by the dyeing method according to any one of claims 1-5, characterized in that it has a s-triazine active group.
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