CN114351287B - Preparation method of composite drug-loaded fiber based on micro-fluid spinning - Google Patents

Preparation method of composite drug-loaded fiber based on micro-fluid spinning Download PDF

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CN114351287B
CN114351287B CN202210067004.6A CN202210067004A CN114351287B CN 114351287 B CN114351287 B CN 114351287B CN 202210067004 A CN202210067004 A CN 202210067004A CN 114351287 B CN114351287 B CN 114351287B
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CN114351287A (en
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陈宇岳
方瑛
林红
张德锁
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Suzhou University
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Abstract

本发明公开了基于微流纺复合载药纤维的制备方法,包括以下步骤:A1、取聚乙烯吡咯烷酮和海藻酸钠,分别加入水后搅拌并加热,得到聚乙烯吡咯烷酮溶液和海藻酸钠溶液;A2、将聚乙烯吡咯烷酮溶液和海藻酸钠溶液混合,再加入对乙酰氨基酚,形成混合纺丝液;A3、以混合纺丝液为芯层,以氯化钙溶液为鞘流层流,通过同轴微流体纺丝的方式制备连续的复合载药纤维。结合微流体纺丝技术和离子交联固化方法,制成排列整齐,直径均一复合载药纤维,提高了复合载药纤维的载药量,实现复合载药纤维的药物缓释效果。

The invention discloses a preparation method of composite drug-loaded fiber based on micro-flow spinning, which includes the following steps: A1. Take polyvinylpyrrolidone and sodium alginate, add water respectively, stir and heat to obtain polyvinylpyrrolidone solution and sodium alginate solution; A2. Mix polyvinylpyrrolidone solution and sodium alginate solution, and then add acetaminophen to form a mixed spinning solution; A3. Use the mixed spinning solution as the core layer and the calcium chloride solution as the sheath flow laminar flow. Continuous composite drug-loaded fibers were prepared by coaxial microfluidic spinning. Combining microfluidic spinning technology and ion cross-linking curing method, composite drug-loaded fibers with neat arrangement and uniform diameter are produced, which increases the drug-loading capacity of the composite drug-loaded fibers and achieves the sustained drug release effect of the composite drug-loaded fibers.

Description

基于微流纺复合载药纤维的制备方法Preparation method of composite drug-loaded fiber based on micro-flow spinning

技术领域Technical field

本发明涉及一种复合载药纤维,尤其涉及基于微流纺复合载药纤维的制备方法。The invention relates to a composite drug-loaded fiber, and in particular to a preparation method of a micro-flow spinning composite drug-loaded fiber.

背景技术Background technique

在药物缓、控释系统中,载体材料是很重要的组成部分之一。载体材料会影响药物的释放速率,使用不同的载体材料装载药物,就可能有不同的药物释放动力学。一般来说,合适的载体材料要具备生物相容性好,对人无毒无害,药物容易释放出来并且保证药效稳定等基本特点。In drug sustained and controlled release systems, carrier materials are one of the most important components. Carrier materials will affect the release rate of drugs. Using different carrier materials to load drugs may have different drug release kinetics. Generally speaking, a suitable carrier material must have basic characteristics such as good biocompatibility, non-toxic and harmless to humans, easy release of drugs and stable drug efficacy.

一般常用的载体材料包括可生物降解或不可生物降解型聚合物高分子材料,以及天然高分子材料。常见的载体材料有聚乳酸,聚乳酸-羟基乙酸共聚物,聚乙烯吡咯烷酮,壳聚糖,海藻酸钠等。其中聚乙烯吡咯烷酮是一种人工合成的水溶性的柔性长链的非离子型高分子化合物,具有优良的溶解性和生物相容性,同时也具有优良的生理惰性,不会参与人体的新陈代谢,无毒无害。近几十年来,越来越多的研究人员加大对它的研究,PVP的应用范围也越来越广。Commonly used carrier materials include biodegradable or non-biodegradable polymer materials and natural polymer materials. Common carrier materials include polylactic acid, polylactic acid-glycolic acid copolymer, polyvinylpyrrolidone, chitosan, sodium alginate, etc. Among them, polyvinylpyrrolidone is a synthetic water-soluble flexible long-chain non-ionic polymer compound with excellent solubility and biocompatibility. It also has excellent physiological inertness and will not participate in the metabolism of the human body. toxic free and safe. In recent decades, more and more researchers have increased their research on it, and the application range of PVP has become wider and wider.

传统的制备释药纤维的方法有干法纺丝,湿法纺丝和静电纺丝等。现有技术中使用两步去溶剂化法制备含有牛血清白蛋白BSA的明胶纳米颗粒GNP,然后利用干法纺丝制备PCL纤维,将GNP颗粒负载在纤维上,创造了一种能够携带和释放蛋白质药物系统。现有技术利用改进后的湿法纺丝技术制备了载有柠檬酸他莫昔芬TAM的聚丙烯腈PAN纤维。现有技术中还通过使用同轴静电纺丝制备了单硬脂酸甘油酯薄层作为壳层和载有盐酸小檗碱和乙基纤维素为芯层的载药纳米复合纤维。但是这些纺丝方法都存在一些局限性,干法纺丝需要高温且要求载体材料和药物要不易降解,可能会破坏药物的活性;湿法纺丝需要的凝固浴,一般是有毒的液体,对身体有伤害,需要后期去除,也可能会破坏药物分子的活性;静电纺丝一般需要高电压才能进行纺丝,而且配置纺丝液所需要的溶剂有时用的也是一些有毒性的液体,对身体有害。Traditional methods for preparing drug-releasing fibers include dry spinning, wet spinning and electrospinning. In the existing technology, a two-step desolvation method is used to prepare gelatin nanoparticles GNP containing bovine serum albumin BSA, and then dry spinning is used to prepare PCL fiber, and the GNP particles are loaded on the fiber, creating a method that can carry and release Protein drug systems. The existing technology uses improved wet spinning technology to prepare polyacrylonitrile PAN fibers loaded with tamoxifen citrate TAM. In the prior art, drug-loaded nanocomposite fibers containing a thin layer of glyceryl monostearate as the shell layer and berberine hydrochloride and ethyl cellulose as the core layer were also prepared by using coaxial electrospinning. However, these spinning methods have some limitations. Dry spinning requires high temperatures and the carrier materials and drugs must not be easily degraded, which may destroy the activity of the drugs. The coagulation bath required for wet spinning is generally a toxic liquid, which is harmful to It is harmful to the body and needs to be removed later, and it may also destroy the activity of drug molecules; electrospinning generally requires high voltage to spin, and the solvents required to configure the spinning solution sometimes use toxic liquids, which are harmful to the body. harmful.

因此需要提出一种更加简单操作,可以能减轻传统制备方法的不足并且可以保留药物缓释系统的优点的纤维的制备方法。Therefore, there is a need to propose a fiber preparation method that is simpler to operate, can alleviate the shortcomings of traditional preparation methods, and can retain the advantages of a drug sustained release system.

发明内容Contents of the invention

本发明克服了现有技术的不足,提供基于微流纺复合载药纤维的制备方法。为达到上述目的,本发明采用的技术方案为:基于微流纺复合载药纤维的制备方法,其特征在于,包括以下步骤:The present invention overcomes the shortcomings of the prior art and provides a preparation method for composite drug-loaded fibers based on micro-flow spinning. In order to achieve the above object, the technical solution adopted by the present invention is: a preparation method of composite drug-loaded fiber based on micro-flow spinning, which is characterized by including the following steps:

A1、取聚乙烯吡咯烷酮和海藻酸钠,分别加入水后搅拌并加热,得到聚乙烯吡咯烷酮溶液和海藻酸钠溶液;A1. Take polyvinylpyrrolidone and sodium alginate, add water respectively, stir and heat to obtain polyvinylpyrrolidone solution and sodium alginate solution;

A2、将聚乙烯吡咯烷酮溶液和海藻酸钠溶液混合,再加入对乙酰氨基酚,形成混合纺丝液;A2. Mix polyvinylpyrrolidone solution and sodium alginate solution, and then add acetaminophen to form a mixed spinning solution;

A3、通过微流体纺丝的方式制备连续的复合载药纤维。A3. Prepare continuous composite drug-loaded fibers through microfluidic spinning.

本发明一个较佳实施例中,以混合纺丝液为芯层,以氯化钙溶液为鞘流层流,将混合纺丝液和氯化钙溶液以不同流速同轴喷出纤维,纤维在收集装置的旋转牵引力的作用下,不断旋转牵伸出连续的纤维;通过设定收集装置的平移速率和循环次数,制备形成复合载药纤维。In a preferred embodiment of the present invention, the mixed spinning liquid is used as the core layer, and the calcium chloride solution is used as the sheath flow laminar flow. The mixed spinning liquid and calcium chloride solution are coaxially ejected into the fiber at different flow rates. Under the action of the rotational traction force of the collection device, continuous fibers are drawn out by continuous rotation; by setting the translation rate and number of cycles of the collection device, composite drug-loaded fibers are prepared and formed.

本发明一个较佳实施例中,所述聚乙烯吡咯烷酮溶液的浓度为5~15wt%,所述海藻酸钠溶液的浓度为1~2wt%,所述聚乙烯吡咯烷酮溶液和所述海藻酸钠溶液按照1:1~2的比例混合。In a preferred embodiment of the present invention, the concentration of the polyvinylpyrrolidone solution is 5-15wt%, the concentration of the sodium alginate solution is 1-2wt%, the polyvinylpyrrolidone solution and the sodium alginate solution Mix according to the ratio of 1:1~2.

本发明一个较佳实施例中,所述聚乙烯吡咯烷酮溶液的浓度为15~21wt%,所述海藻酸钠溶液的浓度为1~2wt%,所述聚乙烯吡咯烷酮溶液和所述海藻酸钠溶液按照1:1~2的比例混合。In a preferred embodiment of the present invention, the concentration of the polyvinylpyrrolidone solution is 15-21wt%, the concentration of the sodium alginate solution is 1-2wt%, the polyvinylpyrrolidone solution and the sodium alginate solution Mix according to the ratio of 1:1~2.

本发明一个较佳实施例中,所述氯化钙溶液的浓度为0.1~0.2mol/L。In a preferred embodiment of the present invention, the concentration of the calcium chloride solution is 0.1-0.2 mol/L.

本发明一个较佳实施例中,所述混合纺丝液中加入占总溶质的质量分数为0~30wt%的所述对乙酰氨基酚。In a preferred embodiment of the present invention, the acetaminophen is added to the mixed spinning liquid with a mass fraction of 0 to 30 wt% of the total solute.

本发明一个较佳实施例中,所述收集装置的旋转速度为30~50r/min,所述收集装置平移速度为3~5mm/min,循环平移一次,芯层溶液的流速为16~28mL/h,鞘流层溶液的流速为8~14mL/h。In a preferred embodiment of the present invention, the rotation speed of the collection device is 30 to 50 r/min, the translation speed of the collection device is 3 to 5 mm/min, and the translation speed is once in a cycle, and the flow rate of the core layer solution is 16 to 28 mL/min. h, the flow rate of the sheath layer solution is 8 to 14 mL/h.

一种复合载药纤维,采用上述任一项所述的基于微流纺复合载药纤维的制备方法制成,其特征在于:所述复合载药纤维为核壳纤维,聚乙烯吡咯烷酮、海藻酸钠和对乙酰氨基酚是以无定形状态均匀分散在所述复合载药纤维内,且复合载药纤维之间有氢键作用。A composite drug-loaded fiber made by any of the above-mentioned preparation methods of composite drug-loaded fiber based on micro-flow spinning, characterized in that: the composite drug-loaded fiber is core-shell fiber, polyvinylpyrrolidone, alginic acid Sodium and acetaminophen are evenly dispersed in the composite drug-loaded fiber in an amorphous state, and there are hydrogen bonds between the composite drug-loaded fibers.

本发明一个较佳实施例中,所述复合载药纤维的断裂强力与所述聚乙烯吡咯烷酮和所述对乙酰氨基酚的浓度正相关。In a preferred embodiment of the present invention, the breaking strength of the composite drug-loaded fiber is positively correlated with the concentrations of the polyvinylpyrrolidone and the acetaminophen.

本发明一个较佳实施例中,当聚乙烯吡咯烷酮溶液和对乙酰氨基酚的浓度分别在5~21wt%和0~30wt%范围内,所述复合载药纤维的乙酰氨基酚累积释放百分率与所述聚乙烯吡咯烷酮溶液和对乙酰氨基酚的浓度正相关。In a preferred embodiment of the present invention, when the concentrations of polyvinylpyrrolidone solution and acetaminophen are in the range of 5 to 21 wt% and 0 to 30 wt% respectively, the cumulative release percentage of acetaminophen of the composite drug-loaded fiber is consistent with the desired There is a positive correlation between the concentration of polyvinylpyrrolidone solution and acetaminophen.

本发明解决了背景技术中存在的缺陷,本发明具备以下有益效果:The present invention solves the defects existing in the background technology and has the following beneficial effects:

(1)本发明以聚乙烯吡咯烷酮作为对乙酰氨基酚的载体,结合微流体纺丝技术和离子交联固化方法,制成排列整齐,直径均一复合载药纤维,提高了复合载药纤维的载药量,实现复合载药纤维的药物缓释效果。(1) The present invention uses polyvinylpyrrolidone as the carrier of acetaminophen, combines microfluid spinning technology and ion cross-linking curing method to produce composite drug-loaded fibers with neat arrangement and uniform diameter, which improves the loading capacity of the composite drug-loaded fibers. dosage to achieve the drug sustained release effect of the composite drug-loaded fiber.

(2)本发明制备的复合载药纤维中聚乙烯吡咯烷酮、海藻酸钠与对乙酰氨基酚以物理形式结合,纤维组分之间有氢键作用,且对乙酰氨基酚以无定形状态均匀分散在复合纤维内,聚乙烯吡咯烷酮和海藻酸钠可以有效抑制乙酰氨基酚结晶析出,进一步提高了复合载药纤维的载药量和缓释效果。(2) In the composite drug-loaded fiber prepared by the present invention, polyvinylpyrrolidone, sodium alginate and acetaminophen are physically combined, there are hydrogen bonds between fiber components, and acetaminophen is evenly dispersed in an amorphous state In the composite fiber, polyvinylpyrrolidone and sodium alginate can effectively inhibit the crystallization of acetaminophen, further improving the drug loading capacity and sustained release effect of the composite drug-loaded fiber.

(3)本发明通过调整不同聚乙烯吡咯烷酮和海藻酸钠的浓度、调整聚乙烯吡咯烷酮和海藻酸钠之间的配比、调整微流体纺丝中混合纺丝液的输出速率、收集装置的旋转速率和平移速率,来获得较大载药量的复合载药纤维的直径、间隔和均匀度,进而获得较大的对乙酰氨基酚累计释放百分率。(3) The present invention adjusts the concentrations of different polyvinylpyrrolidone and sodium alginate, adjusts the ratio between polyvinylpyrrolidone and sodium alginate, adjusts the output rate of the mixed spinning solution in microfluidic spinning, and adjusts the rotation of the collection device. The velocity and translation rate are used to obtain the diameter, spacing and uniformity of the composite drug-loaded fiber with a larger drug load, thereby obtaining a larger cumulative release percentage of acetaminophen.

本发明中当收集装置的旋转速度为50r/min,收集装置平移速度为4mm/min,循环平移一次,芯层溶液的流速为28mL/h,鞘流层溶液的流速为14mL/h,15wt%的聚乙烯吡咯烷酮溶液与2wt%的海藻酸钠溶液按照1:2的比例混合制备的纺丝液作为芯层溶液和0.1mol/L的氯化钙溶液作为鞘流层溶液,可以通过同轴微流体纺丝连续制备纤维,在一分钟内可以生产9.42米长的微纤维,生产率达到15.7cm/s。In the present invention, when the rotation speed of the collection device is 50 r/min, the translation speed of the collection device is 4 mm/min, and the circulation translation is once, the flow rate of the core layer solution is 28 mL/h, and the flow rate of the sheath flow layer solution is 14 mL/h, 15wt% The polyvinylpyrrolidone solution and 2wt% sodium alginate solution were mixed in a ratio of 1:2 to prepare the spinning solution as the core layer solution and the 0.1mol/L calcium chloride solution as the sheath layer solution. Fluid spinning continuously prepares fibers and can produce 9.42 meters of microfibers in one minute, with a productivity of 15.7cm/s.

(4)本发明利用微流纺制备的复合载药纤维有比较大的比表面积,同时纤维内部也有孔隙可以来储存药物,纤维固化后可以很好的包封药物,也限制了药物的布朗运动,降低了药物分子间相互碰撞的几率,在一定程度上避免了药物晶核的形成,保证了复合载药纤维的载药能力和缓释效果。(4) The composite drug-loaded fiber prepared by micro-flow spinning in the present invention has a relatively large specific surface area. At the same time, there are pores inside the fiber to store drugs. After solidification, the fiber can encapsulate the drug well and limit the Brownian motion of the drug. , reduces the probability of collision between drug molecules, avoids the formation of drug crystal nuclei to a certain extent, and ensures the drug-loading capacity and sustained-release effect of the composite drug-loaded fiber.

本发明利用微流纺制备的复合载药纤维,无需使用高温,不会对载体材料或药物造成分解或破坏活性,也无需高电压纺丝,配置纺丝液的过程中不产生有毒液体。The composite drug-loaded fiber prepared by micro-flow spinning in the present invention does not require the use of high temperatures, will not cause decomposition or deactivation of carrier materials or drugs, does not require high-voltage spinning, and does not produce toxic liquids during the process of preparing the spinning solution.

附图说明Description of the drawings

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明中记载的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图;In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the drawings needed to be used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings in the following description are only These are some embodiments recorded in the present invention. For those of ordinary skill in the art, other drawings can be obtained based on these drawings without exerting creative efforts;

图1是本发明的一种基于微流纺复合载药纤维的制备流程图;Figure 1 is a flow chart for the preparation of a micro-spun composite drug-loaded fiber of the present invention;

图2是本发明的实施例一的不同PVP溶液浓度的PVP/SA/AAP复合纤维的SEM图;Figure 2 is an SEM image of PVP/SA/AAP composite fibers with different PVP solution concentrations in Example 1 of the present invention;

图3是本发明的实施例一的不同PVP溶液浓度的PVP/SA/AAP复合纤维截面的SEM图;Figure 3 is an SEM image of the cross-section of the PVP/SA/AAP composite fiber with different PVP solution concentrations in Example 1 of the present invention;

图4是本发明的实施例二的不同AAP质量分数的PVP/SA/AAP复合纤维的SEM图;Figure 4 is an SEM image of PVP/SA/AAP composite fibers with different AAP mass fractions in Example 2 of the present invention;

图5是本发明的实施例三的PVP/SA/AAP复合纤维实物图;Figure 5 is a physical diagram of the PVP/SA/AAP composite fiber according to Embodiment 3 of the present invention;

图6是本发明的实施例四的PVP、SA、AAP和AAP质量分数为0wt%、10wt%、20wt%和30wt%的PVP/SA/AAP复合纤维的红外光谱图;Figure 6 is an infrared spectrum of PVP/SA/AAP composite fibers with PVP, SA, AAP and AAP mass fractions of 0wt%, 10wt%, 20wt% and 30wt% in Example 4 of the present invention;

图7是本发明的实施例四的AAP、PVP、SA、PVP/SA复合纤维膜和PVP/SA/AAP复合纤维膜的XRD曲线图;Figure 7 is the XRD curve diagram of AAP, PVP, SA, PVP/SA composite fiber membrane and PVP/SA/AAP composite fiber membrane in Example 4 of the present invention;

图8是本发明的实施例四的PVP/SA/AAP复合纤维的力学分析图;Figure 8 is a mechanical analysis diagram of the PVP/SA/AAP composite fiber in Example 4 of the present invention;

图9是本发明的实施例五的AAP在pH=7.4的磷酸盐缓冲溶液中的标准曲线和标准曲线方程;Figure 9 is the standard curve and standard curve equation of AAP in phosphate buffer solution of pH=7.4 according to Example 5 of the present invention;

图10是本发明的实施例五的AAP在PVP/SA/AAP复合纤维中的体外释放曲线图。Figure 10 is an in vitro release curve diagram of AAP in PVP/SA/AAP composite fiber according to Example 5 of the present invention.

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.

如图1所示,示出了本发明提供的一种基于微流纺复合载药纤维的制备流程图。该基于微流纺复合载药纤维的制备方法,包括以下步骤:As shown in Figure 1, there is shown a flow chart for the preparation of a micro-spun composite drug-loaded fiber provided by the present invention. The preparation method of composite drug-loaded fiber based on micro-flow spinning includes the following steps:

A1、取聚乙烯吡咯烷酮和海藻酸钠,分别加入水后搅拌并加热,得到聚乙烯吡咯烷酮溶液和海藻酸钠溶液;A1. Take polyvinylpyrrolidone and sodium alginate, add water respectively, stir and heat to obtain polyvinylpyrrolidone solution and sodium alginate solution;

A2、将聚乙烯吡咯烷酮溶液和海藻酸钠溶液混合,再加入对乙酰氨基酚,形成混合纺丝液;A2. Mix polyvinylpyrrolidone solution and sodium alginate solution, and then add acetaminophen to form a mixed spinning solution;

A3、通过微流体纺丝的方式制备连续的复合载药纤维。实施例一A3. Prepare continuous composite drug-loaded fibers through microfluidic spinning. Embodiment 1

由于微流体纺丝是在常温常压下进行,纺丝液在整个连续纺丝的过程中除了受到注射泵的推力之外,没有受到其他外力作用,所以为了保证纺丝过程的正常进行,溶液的浓度对纺丝很重要。为了保证纤维在释药过程中只溶胀不溶解,采用离子交联方法快速固化纤维,找到合适的海藻酸钠与氯化钙浓度也很重要。因此,本实施例为了验证不同纺丝液浓度对PVP/SA/AAP复合载药纤维的成型影响。Since microfluidic spinning is carried out at normal temperature and pressure, the spinning solution is not subjected to other external forces except the thrust of the syringe pump during the entire continuous spinning process. Therefore, in order to ensure the normal progress of the spinning process, the solution The concentration is important for spinning. In order to ensure that the fiber only swells but does not dissolve during the drug release process, the ionic cross-linking method is used to quickly solidify the fiber. It is also important to find the appropriate concentrations of sodium alginate and calcium chloride. Therefore, this example is to verify the influence of different spinning solution concentrations on the shaping of PVP/SA/AAP composite drug-loaded fibers.

PVP溶液和SA溶液本身具有一定的黏度,并且随着浓度的的升高,溶液黏度也会上升。由于纺丝液流动通道比较细窄,当溶液浓度过高时,黏度也会过大,这样极易发生堵塞现象,但当溶液浓度过低时,纤维不易成型,容易发生断头。PVP solution and SA solution themselves have a certain viscosity, and as the concentration increases, the viscosity of the solution will also increase. Since the flow channel of the spinning solution is relatively narrow, when the solution concentration is too high, the viscosity will be too high, which will easily cause clogging. However, when the solution concentration is too low, the fiber will not be easy to form and breakage will easily occur.

为了能进行纺丝实验,确保纤维在纺丝过程中不会出现断丝,分别配置了5wt%、10wt%和15wt%的PVP溶液,以及1wt%和2wt%的SA溶液,且按照1:1和1:2的质量比混合得到不同浓度的混合纺丝液,实验设计样品如表1所示。其中,本实施例中氯化钙溶液的浓度选择为0.1mol/L。In order to carry out the spinning experiment and ensure that the fiber will not break during the spinning process, 5wt%, 10wt% and 15wt% PVP solutions, as well as 1wt% and 2wt% SA solutions were prepared respectively, and the ratio was 1:1. Mixed with a mass ratio of 1:2 to obtain mixed spinning solutions of different concentrations. The experimental design samples are shown in Table 1. Among them, the concentration of the calcium chloride solution in this embodiment is selected to be 0.1 mol/L.

表1实验设计样品Table 1 Experimental design samples

通过上述实验发现15wt%的PVP溶液与2wt%的SA溶液按照1:2的比例混合制备的纺丝液作为芯层溶液和0.1mol/L的氯化钙溶液作为鞘流层溶液,可以通过同轴微流体纺丝连续制备纤维,纤维基本不会发生断头。Through the above experiments, it was found that the spinning solution prepared by mixing 15wt% PVP solution and 2wt% SA solution in a ratio of 1:2 was used as the core layer solution and the 0.1mol/L calcium chloride solution was used as the sheath layer solution. axial microfluidic spinning continuously prepares fibers, and fibers are basically not broken.

当确定15wt%的PVP溶液和2wt%的SA溶液按质量比1:2的比例混合后,可以成功制备出复合纤维后,继续配置了18wt%和21wt%的PVP溶液,保持相同的SA溶液和混合比例,使用相同的同轴微流体纺丝工艺参数制备复合纤维,探究PVP溶液浓度的变化对纤维形貌的影响和后期作为药物缓释系统时对药物释放的影响。不同PVP溶液浓度的PVP/SA/AAP复合纤维表面的形貌如图2所示,其中图2a、2b和2c中分别显示为15wt%、18wt%和21wt%PVP溶液浓度的PVP/SA/AAP复合纤维的SEM图。After it was determined that 15wt% PVP solution and 2wt% SA solution were mixed in a mass ratio of 1:2, and the composite fiber could be successfully prepared, 18wt% and 21wt% PVP solutions were continued, keeping the same SA solution and Mixing ratio, use the same coaxial microfluidic spinning process parameters to prepare composite fibers, and explore the impact of changes in PVP solution concentration on fiber morphology and the impact on drug release when used as a drug sustained release system. The surface morphology of PVP/SA/AAP composite fibers with different PVP solution concentrations is shown in Figure 2, where Figures 2a, 2b and 2c show PVP/SA/AAP with 15wt%, 18wt% and 21wt% PVP solution concentrations respectively. SEM image of composite fiber.

从图2中,可以得到随着PVP含量的增加,纤维更加光滑圆润,直径为30~50μm左右。而且随着PVP含量的增加,纤维的直径变细。15wt%、18wt%和21wt%的PVP溶液浓度的PVP/SA/AAP复合纤维的直径分别是44μm、39μm和34μm。From Figure 2, it can be seen that as the PVP content increases, the fibers become smoother and rounder, with a diameter of about 30 to 50 μm. Moreover, as the PVP content increases, the diameter of the fiber becomes thinner. The diameters of PVP/SA/AAP composite fibers with PVP solution concentrations of 15wt%, 18wt% and 21wt% are 44μm, 39μm and 34μm respectively.

原因是随着PVP含量的增加,海藻酸钠的相对含量降低,在干燥过程中凝胶纤维的收缩速度减慢,收缩空隙减小,纤维表面变的更加光滑,同时海藻酸钠相对含量的降低,降低了海藻酸钠溶剂水分子之间的作用力,让纤维在干燥过程中溶剂挥发的更充分,纤维直径变细。The reason is that as the PVP content increases, the relative content of sodium alginate decreases. During the drying process, the shrinkage speed of the gel fiber slows down, the shrinkage gaps decrease, the fiber surface becomes smoother, and the relative content of sodium alginate decreases. , reducing the interaction between water molecules of the sodium alginate solvent, allowing the solvent to evaporate more fully during the drying process of the fiber, and the fiber diameter becomes thinner.

不同PVP溶液浓度的PVP/SA/AAP复合纤维内部结构如图3所示,其中图3(a-c)、3(d-f)、3(g-i)分别显示为15wt%、18wt%和21wt%PVP溶液浓度的PVP/SA/AAP复合纤维截面的SEM图。The internal structure of PVP/SA/AAP composite fibers with different PVP solution concentrations is shown in Figure 3, where Figures 3(a-c), 3(d-f), and 3(g-i) show the PVP solution concentrations of 15wt%, 18wt%, and 21wt% respectively. SEM image of the cross-section of PVP/SA/AAP composite fiber.

从图3a、图3d和图3g中,可以得到PVP/SA/AAP复合纤维内部没有明显的空腔缺陷,说明PVP、SA和AAP具有良好的相容性,可以进行均匀混合。From Figure 3a, Figure 3d and Figure 3g, it can be seen that there are no obvious cavity defects inside the PVP/SA/AAP composite fiber, indicating that PVP, SA and AAP have good compatibility and can be mixed evenly.

从图3b中,得到PVP/SA/AAP复合纤维的外部出现壳状结构,这是因为在微通道内当芯层的纺丝液与鞘流层的氯化钙溶液相遇时,SA与Ca2+的交联速率大于PVP的固化速度,所以SA的一部分在PVP组分之前在纤维的外表面上迅速形成凝胶,纤维表面具有了一层凝胶壳层,这有利于药物的包封。From Figure 3b, a shell-like structure appears on the outside of the PVP/SA/AAP composite fiber. This is because when the spinning solution in the core layer meets the calcium chloride solution in the sheath flow layer in the microchannel, SA and Ca2 + The cross-linking rate is greater than the curing speed of PVP, so part of the SA quickly forms a gel on the outer surface of the fiber before the PVP component, and the fiber surface has a gel shell, which is beneficial to the encapsulation of drugs.

同时从图3e和图3h中得到,随着PVP溶液浓度的增加,复合纤维的凝胶壳层越来越薄,由于随着PVP含量的增加,SA的相对含量降低,可以分去与Ca2+结合形成凝胶层的含量也在降低,所以纤维表面的凝胶壳层随着PVP溶液浓度的增加而变薄。从图3c、3f和3i中可以看到复合纤维内部有微小的孔径结构,这有利于药物的装载与释放,并且随着PVP溶液浓度的增加,纤维内部的孔径越多。At the same time, it can be seen from Figure 3e and Figure 3h that as the concentration of PVP solution increases, the gel shell of the composite fiber becomes thinner and thinner. As the PVP content increases, the relative content of SA decreases and can be separated from Ca2 + The content of the combined gel layer is also reduced, so the gel shell on the fiber surface becomes thinner as the concentration of the PVP solution increases. It can be seen from Figures 3c, 3f and 3i that there is a tiny pore structure inside the composite fiber, which is beneficial to the loading and release of drugs, and as the concentration of the PVP solution increases, the more pores there are inside the fiber.

实施例二Embodiment 2

本实施例探究不同AAP质量分数对复合纤维形貌的影响。不同AAP质量分数的载药PVP/SA/AAP复合纤维的SEM图。将导电胶固定在电镜台上,然后取几根上述制备的PVP/SA/AAP复合纤维粘在导电胶上,喷金90s,采用R-8100冷场扫描电镜,观察纤维的表面形貌特征。测试条件为电压3kV,电压为10mA。用液氮脆断复合纤维,采用同样的测试方法和测试条件,观察纤维的截面形貌特征。This example explores the effect of different AAP mass fractions on the morphology of composite fibers. SEM images of drug-loaded PVP/SA/AAP composite fibers with different AAP mass fractions. Fix the conductive glue on the electron microscope stage, then take several PVP/SA/AAP composite fibers prepared above and stick them on the conductive glue, spray gold for 90 seconds, and use R-8100 cold field scanning electron microscope to observe the surface morphology characteristics of the fibers. The test conditions are voltage 3kV and voltage 10mA. Use liquid nitrogen brittle fracture composite fiber and use the same testing method and testing conditions to observe the cross-sectional morphological characteristics of the fiber.

如图4所示,其中图4a、4b、4c和4d分别显示为AAP质量分数为0wt%、10wt%、20wt%和30wt%的PVP/SA/AAP复合纤维的SEM图。As shown in Figure 4, Figures 4a, 4b, 4c and 4d show SEM images of PVP/SA/AAP composite fibers with AAP mass fractions of 0wt%, 10wt%, 20wt% and 30wt% respectively.

从图4中,不同AAP质量分数的PVP/SA/AAP复合纤维表面仍然比较光滑且连续,没有明显的块状或结晶状物质析出,说明对乙酰氨基酚均匀的分散在复合纤维中。随着AAP质量分数的增加,纤维的直径略有变化,说明模型药物的加入对纤维直径的影响不大。From Figure 4, the surface of PVP/SA/AAP composite fibers with different AAP mass fractions is still relatively smooth and continuous, with no obvious block or crystalline material precipitating, indicating that acetaminophen is evenly dispersed in the composite fiber. As the mass fraction of AAP increases, the diameter of the fiber changes slightly, indicating that the addition of the model drug has little effect on the fiber diameter.

实施例三Embodiment 3

上述制备方法中,微流体纺丝工艺参数对纤维成型存在一定的影响。因此,本实施例为了探究微流体纺丝工艺参数对纤维成型的影响。In the above preparation method, the microfluidic spinning process parameters have a certain impact on fiber forming. Therefore, this example is to explore the influence of microfluidic spinning process parameters on fiber forming.

微流体纺丝机主要由微流控注射泵和纤维接收平台两大部分组成。第一部分微流控注射泵是用来控制纺丝液输出速度和输出量,主要包括:双通道注射泵、注射器、聚四氟乙烯管和同轴针头。第二部分纤维接收平台是用来接收纤维的,主要包括滚筒接收器、旋转电机、循环步进平移平台、加热器和控制面板。其中双通道注射泵可以分别独立地控制两个注射器,设置不同的推进速度,微流体纺丝装置各部件之间用聚四氟乙烯管和连接头连接。The microfluidic spinning machine mainly consists of two parts: a microfluidic syringe pump and a fiber receiving platform. The first part of the microfluidic syringe pump is used to control the output speed and volume of the spinning solution. It mainly includes: dual-channel syringe pump, syringe, polytetrafluoroethylene tube and coaxial needle. The second part of the fiber receiving platform is used to receive fibers, and mainly includes a roller receiver, a rotating motor, a cyclic stepping translation platform, a heater and a control panel. The dual-channel syringe pump can independently control the two syringes and set different propulsion speeds. The components of the microfluidic spinning device are connected with polytetrafluoroethylene tubes and connectors.

微流体纺丝机上的滚筒接收器通过不断旋转产生牵引力,一方面可以将纺丝液拉伸成纤维状,另一方面可以接收通过离子交联固化后的纤维,提供牵引力,使纤维变得更加有序。滚筒接收器的旋转速度是由旋转电机的旋转速率来决定的,所以旋转电机的旋转速率会影响纤维的直径大小。The drum receiver on the microfluidic spinning machine generates traction through continuous rotation. On the one hand, it can stretch the spinning liquid into fiber shape, and on the other hand, it can receive the fibers solidified by ion cross-linking, providing traction and making the fibers become more Orderly. The rotation speed of the drum receiver is determined by the rotation rate of the rotating motor, so the rotation rate of the rotating motor will affect the diameter of the fiber.

当转速过低时,接收器不能快速从针头牵伸出纤维,纤维无法成型,当转速过高时,接收器提供的牵引力过大,纤维会被拉断,断丝比较多。为了得到排列整齐,直径均一的纤维膜,利于后期的释药实验,让接收器以一定的平移速度循环移动,可以在滚筒上收集到规整有序,间隔均匀的纤维膜。接收器的平移速度和循环次数直接影响纤维间的间距大小和纤维膜的密度。When the rotation speed is too low, the receiver cannot quickly pull out the fiber from the needle, and the fiber cannot be formed. When the rotation speed is too high, the traction force provided by the receiver is too large, the fiber will be pulled off, and there will be more broken wires. In order to obtain neatly arranged fiber membranes with uniform diameters, which will facilitate later drug release experiments, the receiver is allowed to move cyclically at a certain translation speed, and orderly and evenly spaced fiber membranes can be collected on the drum. The translation speed and number of cycles of the receiver directly affect the spacing between fibers and the density of the fiber membrane.

纺丝液的输出速度是由注射泵的推进速度控制,需要找到合适的芯层溶液和鞘流层溶液的流速,才能得到成型良好,排布均匀的纤维。The output speed of the spinning solution is controlled by the propulsion speed of the syringe pump. It is necessary to find the appropriate flow rate of the core layer solution and the sheath layer solution to obtain well-formed and evenly arranged fibers.

因此,本实施例中微流体纺丝机通过注射泵决定的混合纺丝液的输出速率,纤维接收平台上马达的旋转速率,和循环步进平移速率来影响纤维的直径、间隔和均匀度。本实施例通过上述三个工艺参数的优化设置可以得到排列整齐、直径均一且尺寸可调的复合纤维膜。本实施例根据上述三个工艺参数设计如表2的实验方案。Therefore, in this embodiment, the microfluidic spinning machine affects the diameter, spacing and uniformity of the fibers through the output rate of the mixed spinning liquid determined by the syringe pump, the rotation rate of the motor on the fiber receiving platform, and the cycle step translation rate. In this embodiment, a composite fiber membrane with neat arrangement, uniform diameter and adjustable size can be obtained by optimizing the settings of the above three process parameters. In this embodiment, the experimental plan shown in Table 2 is designed based on the above three process parameters.

表2实验方案Table 2 Experimental plan

通过表2得到,当滚筒接收器的旋转速度为50r/min,接收器平移速度为4mm/min,循环平移一次,芯层溶液的流速为28mL/h,鞘流层溶液的流速为14mL/h时,可以得到成型良好的纤维,且可以连续制备纤维。It can be obtained from Table 2 that when the rotation speed of the drum receiver is 50r/min, the translation speed of the receiver is 4mm/min, and the cycle is translated once, the flow rate of the core layer solution is 28mL/h, and the flow rate of the sheath layer solution is 14mL/h. When, well-formed fibers can be obtained, and fibers can be produced continuously.

通过本实施例的实验方案结合上述实施例一的实验方法得到,当滚筒接收器的旋转速度为50r/min,接收器平移速度为4mm/min,循环平移一次,芯层溶液的流速为28mL/h,鞘流层溶液的流速为14mL/h,15wt%的PVP溶液与2wt%的SA溶液按照1:2的比例混合制备的纺丝液作为芯层溶液和0.1mol/L的氯化钙溶液作为鞘流层溶液,可以通过同轴微流体纺丝连续制备纤维,在一分钟内可以生产9.42米长的微纤维,生产率达到15.7cm/s。Through the experimental plan of this embodiment combined with the experimental method of the above-mentioned Example 1, it is obtained that when the rotation speed of the drum receiver is 50 r/min, the translation speed of the receiver is 4 mm/min, and the cyclic translation is performed once, the flow rate of the core layer solution is 28 mL/min. h, the flow rate of the sheath layer solution is 14mL/h, the spinning solution prepared by mixing 15wt% PVP solution and 2wt% SA solution in a ratio of 1:2 is used as the core layer solution and 0.1mol/L calcium chloride solution As a sheath layer solution, fibers can be continuously prepared through coaxial microfluidic spinning, and 9.42-meter-long microfibers can be produced in one minute with a productivity of 15.7cm/s.

同时在芯层纺丝液中加入占总溶质的质量分数为10wt%、20wt%和30wt%的AAP后,仍然可以连续制备纤维。图5是根据实施例一和实施例二优化实验方案后得到的纤维实物图,从图中可以看到纤维成型良好,并且可以进一步制备纤维阵列和纤维膜。At the same time, after adding AAP with a mass fraction of 10wt%, 20wt% and 30wt% of the total solute in the core layer spinning liquid, fibers can still be continuously produced. Figure 5 is a physical picture of the fiber obtained after optimizing the experimental plan according to Example 1 and Example 2. It can be seen from the figure that the fiber is well formed, and fiber arrays and fiber membranes can be further prepared.

实施例四Embodiment 4

本实施例通过将上述实施例制备的PVP/SA/AAP复合载药纤维进行形貌表征。In this example, the morphology of the PVP/SA/AAP composite drug-loaded fiber prepared in the above example was characterized.

(1)PVP/SA/AAP复合纤维傅立叶红外光谱(FITR)测试(1) PVP/SA/AAP composite fiber Fourier transform infrared spectroscopy (FITR) test

图6是PVP、SA、AAP和AAP质量分数为0wt%、10wt%、20wt%和30wt%的PVP/SA/AAP复合纤维的红外光谱图。Figure 6 is the infrared spectrum of PVP/SA/AAP composite fibers with mass fractions of PVP, SA, AAP and AAP of 0wt%, 10wt%, 20wt% and 30wt%.

图6a所示,PVP样品出现在3446cm-1、2956cm-1、1661cm-1和1290cm-1处的吸收峰分别对应于-CH,-CH-CH2,-C=O和-CN的伸缩振动,1423cm-1的吸收峰对应于PVP中循环CH2组的-CH的变形振动。图6b所示,SA样品出现在3423cm-1、2925cm-1、1606cm-1、1405cm-1和1025cm-1处的吸收峰分别对应于-OH、-CH、-COO、-C=O和-C-O-C-基团的伸缩振动。图6c所示,AAP样品出现在3320cm-1、1650cm-1处的吸收峰分别对应-OH和酰胺键上的-C=O的伸缩振动。As shown in Figure 6a, the absorption peaks of the PVP sample appearing at 3446cm -1 , 2956cm -1 , 1661cm -1 and 1290cm -1 respectively correspond to the stretching vibrations of -CH, -CH-CH2, -C=O and -CN. The absorption peak at 1423 cm -1 corresponds to the deformation vibration of -CH of the cyclic CH2 group in PVP. As shown in Figure 6b, the absorption peaks of the SA sample appearing at 3423cm -1 , 2925cm -1 , 1606cm -1 , 1405cm -1 and 1025cm -1 correspond to -OH, -CH, -COO, -C=O and - respectively. Stretching vibration of COC-group. As shown in Figure 6c, the absorption peaks of the AAP sample at 3320 cm -1 and 1650 cm -1 correspond to the stretching vibration of -OH and -C=O on the amide bond, respectively.

图6(e-g)所示,不同载药量的PVP/SA/AAP复合纤维的红外图谱均出现了PVP、SA和AAP的特征吸收峰,没有新的特征吸收峰出现,说明模型药物AAP与PVP,SA之间是以物理共混的形式结合,不会改变药物的理化性质,不会影响药物发挥作用。同时随着AAP含量的增加,1650cm-1处酰胺键上的-C=O特征吸收峰强度逐渐减弱,可能是对乙酰氨基酚,PVP,SA三者之间产生了氢键。As shown in Figure 6(eg), the infrared spectra of PVP/SA/AAP composite fibers with different drug loadings all show the characteristic absorption peaks of PVP, SA and AAP, and no new characteristic absorption peaks appear, indicating that the model drug AAP and PVP , SA are combined in the form of physical blending, which will not change the physical and chemical properties of the drug and will not affect the function of the drug. At the same time, as the AAP content increases, the intensity of the -C=O characteristic absorption peak on the amide bond at 1650 cm -1 gradually weakens, which may be due to hydrogen bonds between acetaminophen, PVP, and SA.

(2)PVP/SA/AAP复合纤维X射线衍射(XRD)测试(2) X-ray diffraction (XRD) test of PVP/SA/AAP composite fiber

药物如果结晶会影响药物的稳定性,生物利用度和疗效,所以在制备药物缓释系统时,要防止药物结晶。药物在聚合物基质中结晶的过程主要分为两个阶段,第一个阶段是成核,第二个阶段是晶核增长。在第一个阶段时,药物通过无规则的“布朗运动”相互碰撞会形成“二聚体”,然后这些“二聚体”会相互碰撞形成晶核。随着越来越多的药物的“二聚体”相互聚拢,就进入了晶核增长阶段。所以药物结晶,然后从聚合物中析出需要一定的时间。If the drug crystallizes, it will affect the stability, bioavailability and efficacy of the drug. Therefore, when preparing a drug sustained-release system, it is necessary to prevent drug crystallization. The process of drug crystallization in polymer matrix is mainly divided into two stages, the first stage is nucleation, and the second stage is crystal nucleation growth. In the first stage, drugs collide with each other through irregular "Brownian motion" to form "dimers", and then these "dimers" collide with each other to form crystal nuclei. As more and more "dimers" of the drug gather together, the crystal nucleus growth stage is entered. So it takes time for the drug to crystallize and then separate out of the polymer.

将制备好的载药的PVP/SA/AAP复合纤维膜在室温下储存3个月,3个月后用X射线衍射PVP/SA/AAP复合纤维膜中的AAP的分布状态,AAP,聚合物基质中的PVP和SA进行检测,图7为AAP、PVP、SA、PVP/SA复合纤维膜和PVP/SA/AAP复合纤维膜的XRD曲线图。The prepared drug-loaded PVP/SA/AAP composite fiber membrane was stored at room temperature for 3 months. After 3 months, X-ray diffraction was used to determine the distribution state of AAP, AAP, and polymer in the PVP/SA/AAP composite fiber membrane. PVP and SA in the matrix were detected. Figure 7 shows the XRD curves of AAP, PVP, SA, PVP/SA composite fiber membrane and PVP/SA/AAP composite fiber membrane.

从图7a可以得到,对乙酰氨基酚(AAP)原药在12.04°、13.76°、15.4°、16.66°、18.12°、20.3°、23.38°、24.32°、26.5°、29,22°和32.44°处出现了典型的特征衍射峰。It can be seen from Figure 7a that the original drug of acetaminophen (AAP) is at 12.04°, 13.76°, 15.4°, 16.66°, 18.12°, 20.3°, 23.38°, 24.32°, 26.5°, 29, 22° and 32.44°. Typical characteristic diffraction peaks appear.

但是在图7e可以得到载药PVP/SA/AAP复合纤维膜中没有观察到AAP原药的特征衍射峰,只观察到了与聚合物基质中PVP和SA的特征衍射峰,说明AAP是以无定型的状态分布在载药复合纤维内,也说明PVP/SA复合纤维可以有效抑制AAP的结晶。这是因为微流纺制备的纤维有比较大的比表面积,同时纤维内部也有孔隙可以来储存药物,纤维固化后可以很好的包封药物,也限制了药物的布朗运动,降低了药物分子间相互碰撞的几率,这样在一定程度上避免了药物晶核的形成。而且通过红外光谱分析中,得到AAP与PVP,SA之间会形成氢键,进一步抑制了药物结晶析出。However, as shown in Figure 7e, no characteristic diffraction peak of AAP original drug was observed in the drug-loaded PVP/SA/AAP composite fiber membrane. Only the characteristic diffraction peaks of PVP and SA in the polymer matrix were observed, indicating that AAP is in an amorphous form. The state is distributed in the drug-loaded composite fiber, which also shows that the PVP/SA composite fiber can effectively inhibit the crystallization of AAP. This is because the fibers prepared by micro-flow spinning have a relatively large specific surface area, and there are also pores inside the fibers to store drugs. After solidification, the fibers can encapsulate the drugs very well, and also limit the Brownian motion of the drugs, reducing the intermittency between drug molecules. The probability of collision with each other avoids the formation of drug crystal nuclei to a certain extent. Moreover, through infrared spectrum analysis, it was found that hydrogen bonds will be formed between AAP, PVP, and SA, further inhibiting the crystallization of the drug.

(3)PVP/SA/AAP复合纤维的力学性能测试(3) Mechanical property testing of PVP/SA/AAP composite fibers

本实施例对上述制备的PVP/SA/AAP复合纤维进行力学性能分析,如图8所示。将纤维按隔距长度200mm制样,利用Instron5967材料试验机测试复合纤维的断裂强力,每个试样测试30次,拉神速度为20mm/min取平均值作为测试结果。In this example, the mechanical properties of the PVP/SA/AAP composite fiber prepared above were analyzed, as shown in Figure 8. The fiber samples were prepared with a pitch length of 200 mm, and the breaking strength of the composite fiber was tested using an Instron5967 material testing machine. Each sample was tested 30 times, and the pulling speed was 20 mm/min. The average value was taken as the test result.

其中图8a是PVP质量分数分别为15wt%、18wt%和21wt%的PVP/SA/AAP复合纤维的断裂强力柱状图;图8b是不同PVP质量分数的复合纤维的应力应变曲线图;图8c是载药量不同的PVP/SA/AAP复合纤维的断裂强力柱状图;图8d是不同载药量PSA纤维的应力应变曲线图。Figure 8a is a histogram of breaking strength of PVP/SA/AAP composite fibers with PVP mass fractions of 15wt%, 18wt% and 21wt% respectively; Figure 8b is a stress-strain curve of composite fibers with different PVP mass fractions; Figure 8c is The breaking strength histogram of PVP/SA/AAP composite fibers with different drug loading contents; Figure 8d is the stress-strain curve of PSA fibers with different drug loading contents.

从图8a中可以得到PVP质量分数为15wt%、18wt%和21wt%的PVP/SA/AAP复合纤维的断裂强力分别是39.14±5.31MPa,44.48±5.5MPa和59.08±5.31MPa。随着PVP含量的增加,复合纤维的断裂强力增加,原因在于随着PVP含量的增加,一方面增加了PVP与SA之间的氢键,另一方面增加了PVP分子内氢键,从而提高了复合纤维的断裂强力。From Figure 8a, it can be seen that the breaking strengths of PVP/SA/AAP composite fibers with PVP mass fractions of 15wt%, 18wt% and 21wt% are 39.14±5.31MPa, 44.48±5.5MPa and 59.08±5.31MPa respectively. As the PVP content increases, the breaking strength of the composite fiber increases. The reason is that as the PVP content increases, on the one hand, the hydrogen bonds between PVP and SA are increased, and on the other hand, the intramolecular hydrogen bonds of PVP are increased, thereby improving the Breaking strength of composite fibers.

从图8b中得到PVP/SA/AAP复合纤维是一种柔性纤维,它的断裂伸长率基本都在20%以上,且随着PVP含量的增加,纤维断裂伸长率也略有增加。It can be seen from Figure 8b that the PVP/SA/AAP composite fiber is a flexible fiber, and its elongation at break is basically above 20%. As the PVP content increases, the elongation at break of the fiber also increases slightly.

从图8c中得到,随着模型药物的增加,纤维的断裂强力也略有增加,质量分数为0、10wt%、20wt%和30wt%的AAP的载药复合纤维断裂强力分别为37.27±4.17MPa、39.14±5.31MPa、39.45±5.4MPa和43.06±5.21MPa。这是因为随着AAP含量的增加,AAP小分子在纤维中均匀分布会增加纤维组分之间的分子间作用力,从而提高了复合纤维的断裂强力。It can be seen from Figure 8c that with the increase of model drug, the breaking strength of the fiber also increases slightly. The breaking strength of the drug-loaded composite fiber with mass fractions of 0, 10wt%, 20wt% and 30wt% AAP is 37.27±4.17MPa respectively. , 39.14±5.31MPa, 39.45±5.4MPa and 43.06±5.21MPa. This is because as the AAP content increases, the uniform distribution of AAP small molecules in the fiber will increase the intermolecular force between fiber components, thereby increasing the breaking strength of the composite fiber.

从图8d中可以得到,随着药物小分子的加入,会增加纤维中大分子链的滑移,复合纤维的断裂伸长率会略有增加,但AAP含量继续增大后,由于纤维组分间分子间作用力增加,复合纤维的断裂伸长率又略有下降。It can be seen from Figure 8d that with the addition of small drug molecules, the slippage of macromolecular chains in the fiber will increase, and the elongation at break of the composite fiber will increase slightly. However, as the AAP content continues to increase, due to the fiber components The intermolecular force increases, and the elongation at break of the composite fiber decreases slightly.

实施例五Embodiment 5

本实施例对上述实施例制备的PVP/SA/AAP复合纤维中AAP体外释放进行测定。This example measures the in vitro release of AAP in the PVP/SA/AAP composite fiber prepared in the above example.

图9是AAP在缓冲溶液中的标准曲线和标准曲线方程。标准曲线表明AAP浓度在0.5μg/mL-50μg/mL范围内,吸光度和浓度呈现良好的线性关系。Figure 9 is the standard curve and standard curve equation of AAP in buffer solution. The standard curve shows that the AAP concentration is in the range of 0.5μg/mL-50μg/mL, and the absorbance and concentration show a good linear relationship.

称取PVP/SA/AAP复合纤维膜置于PBS缓冲溶液中混合,分别在2h、4h、6h、8h、10h、12h、24h、26h、28h、30h、32h、34h、36h、48h、50h、52h、54h、56h、58h、60h和72h处,然后稀释,测定其在245nm处的紫外吸光度,并向缓释体系中添加等量的PBS缓冲溶液,保持溶液容量恒定,每种载药纤维作三个平行样。Weigh the PVP/SA/AAP composite fiber membrane and mix it in PBS buffer solution at 2h, 4h, 6h, 8h, 10h, 12h, 24h, 26h, 28h, 30h, 32h, 34h, 36h, 48h, 50h, respectively. 52h, 54h, 56h, 58h, 60h and 72h, and then dilute it, measure its UV absorbance at 245nm, and add an equal amount of PBS buffer solution to the sustained-release system to keep the solution volume constant. Each drug-loaded fiber is used as Three parallel samples.

根据AAP的标准曲线方程计算AAP含量,并根据以下公式计算AAP累积释放百分率,并绘制PVP/SA/AAP复合纤维的体外释放曲线。公式为:其中Q为AAP累计释放百分率,v为缓释溶液PBS的体积,vd为稀释后PBS的体积,ci为第i次换取样时释放液中药物浓度(μg/mL),A为复合载药纤维中含有的AAP质量(μg),n为取样的次数。Calculate the AAP content according to the standard curve equation of AAP, calculate the cumulative release percentage of AAP according to the following formula, and draw the in vitro release curve of the PVP/SA/AAP composite fiber. The formula is: Among them, Q is the cumulative release percentage of AAP, v is the volume of sustained-release solution PBS, v d is the volume of diluted PBS, c i is the drug concentration (μg/mL) in the release solution during the i-th sample exchange, and A is the composite load. The mass of AAP contained in medicinal fiber (μg), n is the number of sampling times.

图10是AAP在PVP/SA/AAP复合纤维中的体外释放曲线图。从图10a中可以得到,随着PVP含量的增加,PVP/SA/AAP复合纤维的累积释放百分率也在增加。原因在于随着PVP含量的增加,纤维的凝胶壳层变薄,模型药物AAP从纤维内释放的受到的阻碍减少,并且PVP是水溶性高分子聚合物,伴随着纤维壳层的减薄,PVP/SA/AAP复合纤维骨架降解的概率会增大,增加了AAP的释放途径,AAP累积释放百分率增加。并且随着PVP含量的增加,纤维的直径会变细,纤维的比表面积增大,纤维表面的载药量也会增大,纤维中的药物也就会更容易分散到PBS缓冲溶液中,药物的累积释放率也会增加。同时可以得到,三种PVP/SA/AAP复合纤维在前12小时是释放是近似于线性释放,12小时以后的释放速率较缓,近似于匀速释放。这是由于当纤维表层的AAP释放完之后,剩下的AAP只能从纤维内部向外部扩散然后再释放出来,释放速率会有所减慢。Figure 10 is the in vitro release curve of AAP in PVP/SA/AAP composite fiber. It can be seen from Figure 10a that as the PVP content increases, the cumulative release percentage of the PVP/SA/AAP composite fiber also increases. The reason is that as the PVP content increases, the gel shell of the fiber becomes thinner, and the hindrance to the release of the model drug AAP from the fiber is reduced. Moreover, PVP is a water-soluble polymer, and along with the thinning of the fiber shell, The probability of degradation of the PVP/SA/AAP composite fiber skeleton will increase, which increases the release pathway of AAP and increases the cumulative release percentage of AAP. And as the PVP content increases, the diameter of the fiber will become thinner, the specific surface area of the fiber will increase, the drug loading capacity on the fiber surface will also increase, and the drugs in the fiber will be more easily dispersed into the PBS buffer solution. The cumulative release rate will also increase. At the same time, it can be obtained that the release rate of the three PVP/SA/AAP composite fibers is approximately linear in the first 12 hours, and the release rate after 12 hours is slower, approximately uniform release. This is because after the AAP on the surface of the fiber is released, the remaining AAP can only diffuse from the inside of the fiber to the outside and then be released, and the release rate will slow down.

图10b、10c和10d分别是15wt%PVP、18wt%PVP和21wt%PVP含量的PVP/SA/AAP复合纤维的不同载药量的释放曲线图。Figures 10b, 10c and 10d are the release curves of PVP/SA/AAP composite fibers with different drug loading contents of 15wt% PVP, 18wt% PVP and 21wt% PVP respectively.

从图中可以看出,随着载药量的增加,纤维的累积释放百分率也在增加。从表3、表4和表5中得到15wt%PVP,18wt%PVP和21wt%PVP含量,AAP含量为10wt%的PVP/SA/AAP复合纤维在前12h的累积释放百分率分别是45.74%、59.86%和70.43%。AAP含量为20wt%的PVP/SA/AAP复合纤维的累积释放百分率为54.57%、72.69%和78.12%。AAP含量为30wt%的PSA复合纤维的累积释放百分率为61.11%,80%和89.72%。这是由于AAP的含量越多,分散在纤维表面的药物就越多,在前12小时内越容易被释放出来。72h后AAP含量为10wt%的PVP/SA/AAP复合纤维累积释放百分率是63.54%,71.85%和79.13%;AAP含量为20wt%的PVP/SA/AAP复合纤维累积释放百分率是70.56%,81.92%和86.96%;AAP含量为30wt%的PVP/SA/AAP复合纤维释累计释放百分率是80.85%、89.99%和97.35%。这是由于AAP的水溶性不好,包埋到纤维内部的药物不容易释放出来,所以释药速率会减慢,且AAP会与PVP之间生成氢键,抑制了AAP的结晶。当AAP含量增加时,由于PVP含量一定,产生的氢键会达到一个饱和量,这样过多的AAP就会在纤维表面结晶析出,在PBS磷酸缓冲液的冲刷下,溶解在PBS中,药物的累积释药百分率增加。It can be seen from the figure that as the drug loading increases, the cumulative release percentage of fiber also increases. From Table 3, Table 4 and Table 5, the cumulative release percentages of PVP/SA/AAP composite fiber with 15wt% PVP, 18wt% PVP and 21wt% PVP in the first 12 hours were 45.74% and 59.86 respectively. % and 70.43%. The cumulative release percentages of PVP/SA/AAP composite fibers with an AAP content of 20wt% were 54.57%, 72.69% and 78.12%. The cumulative release percentages of PSA composite fibers with an AAP content of 30wt% were 61.11%, 80% and 89.72%. This is because the greater the content of AAP, the more drugs are dispersed on the surface of the fiber and the easier it is to be released within the first 12 hours. After 72 hours, the cumulative release percentages of PVP/SA/AAP composite fibers with 10wt% AAP content were 63.54%, 71.85% and 79.13%; the cumulative release percentages of PVP/SA/AAP composite fibers with 20wt% AAP content were 70.56%, 81.92%. and 86.96%; the cumulative release percentages of the PVP/SA/AAP composite fiber with an AAP content of 30wt% are 80.85%, 89.99% and 97.35%. This is because the water solubility of AAP is not good, and the drug embedded in the fiber is not easily released, so the drug release rate will slow down, and hydrogen bonds will be formed between AAP and PVP, inhibiting the crystallization of AAP. When the AAP content increases, because the PVP content is constant, the hydrogen bonds generated will reach a saturation level, so that excess AAP will crystallize and precipitate on the surface of the fiber. Under the washing of PBS phosphate buffer, it will be dissolved in PBS and the drug will be released. The cumulative drug release percentage increases.

表3 15wt%PVP的PVP/SA/AAP复合纤维中AAP累积释放率Table 3 Cumulative release rate of AAP in PVP/SA/AAP composite fiber with 15wt% PVP

表4 18wt%PVP的PVP/SA/AAP复合纤维中AAP累积释放率Table 4 Cumulative release rate of AAP in PVP/SA/AAP composite fiber with 18wt% PVP

表5 21wt%PVP的PVP/SA/AAP复合纤维中AAP累积释放率Table 5 Cumulative release rate of AAP in PVP/SA/AAP composite fiber with 21wt% PVP

为了探究PVP/SA/AAP复合纤维的释药机理,通过5种药物释放动力学模型来拟合PVP/SA/AAP复合纤维的释药曲线图,根据相关系数R2评估适合的模型。零级释放是指药物释放速率不随时间变化而改变,即药物在释放周期内的释放速率保持恒定。In order to explore the drug release mechanism of PVP/SA/AAP composite fiber, five drug release kinetic models were used to fit the drug release curve of PVP/SA/AAP composite fiber, and the suitable model was evaluated based on the correlation coefficient R2. Zero-order release means that the drug release rate does not change with time, that is, the drug release rate remains constant during the release cycle.

一级释放是指在单位时间内释放速率与药物浓度成正比。一般认为血管外给药零级释放是理想的控释模式,一级释放是基本释放模式。骨架型的药物缓控释系统一般分为整块骨架系统,溶胀型骨架系统和溶蚀型骨架系统。Weibull模型是指药物的释放速率与扩散系数成正比,释药机理一般是扩散或骨架溶蚀。Higuchi模型一般适用于整块骨架系统,是指药物是通过骨架系统中聚合物分子网络和孔道扩散,一般聚合物降解速率远远小于药物的扩散速率。First-order release means that the release rate per unit time is proportional to the drug concentration. It is generally believed that zero-order release for extravascular administration is the ideal controlled release mode, and first-order release is the basic release mode. Matrix type drug sustained and controlled release systems are generally divided into monolithic matrix systems, swelling matrix systems and dissolution matrix systems. The Weibull model means that the release rate of a drug is proportional to the diffusion coefficient, and the drug release mechanism is generally diffusion or matrix dissolution. The Higuchi model is generally applicable to the entire framework system, which means that the drug diffuses through the polymer molecular network and pores in the framework system. Generally, the polymer degradation rate is much smaller than the diffusion rate of the drug.

Ritger-Peppas模型一般适用于溶胀型骨架系统,根据拟合曲线的斜率来判断释药机理。当斜率≤0.43时,药物的释放机理为Fickian扩散;当0.43<斜率<0.89时,药物的释放机理为非Fickian扩散;当斜率=0.89时,药物的释放机理为骨架降解。The Ritger-Peppas model is generally suitable for swelling matrix systems, and the drug release mechanism is judged based on the slope of the fitting curve. When the slope ≤ 0.43, the drug release mechanism is Fickian diffusion; when 0.43 < slope < 0.89, the drug release mechanism is non-Fickian diffusion; when the slope = 0.89, the drug release mechanism is matrix degradation.

表6、表7和表8分别是PVP含量为15wt%、18wt%和21wt%的PVP/SA/AAP复合纤维释药曲线的药物释放动力学模型的拟合。根据相关系数R2评估,PVP含量为15wt%,18wt%和21wt%的PVP/SA/AAP复合纤维释药曲线的药物释放动力学模型与Weibull模型和Ritger-Peppas模型较吻合。15wt%PVP含量的PVP/SA/AAP复合纤维的释药模型与Ritger-Peppas模型更吻合,拟合方程的斜率为0.20322,小于0.43,说明15wt%PVP含量的PVP/SA/AAP复合纤维的释药机理更接近Fickian扩散。18wt%和21wt%PVP含量的PVP/SA/AAP复合纤维的释药模型与Weibull模型更吻合,说明PVP/SA/AAP复合纤维的释药机理主要是药物的扩散和骨架溶蚀。综合说明药物从PVP/SA/AAP复合纤维中释放出来主要经历两个阶段,第一个阶段是纤维骨架发生溶胀,纤维外部的药物经Fickian扩散出来,药物的释放速率较快;第二个阶段是纤维骨架降解,纤维内部的药物扩散出来,药物的释放速率减慢。Table 6, Table 7 and Table 8 are the fitting of the drug release kinetic model of the drug release curve of PVP/SA/AAP composite fiber with PVP content of 15wt%, 18wt% and 21wt% respectively. According to the evaluation of the correlation coefficient R2, the drug release kinetic model of the PVP/SA/AAP composite fiber drug release curve with PVP content of 15wt%, 18wt% and 21wt% is consistent with the Weibull model and the Ritger-Peppas model. The drug release model of PVP/SA/AAP composite fiber with 15wt% PVP content is more consistent with the Ritger-Peppas model. The slope of the fitting equation is 0.20322, which is less than 0.43, indicating that the drug release model of PVP/SA/AAP composite fiber with 15wt% PVP content is more consistent with the Ritger-Peppas model. The drug mechanism is closer to Fickian diffusion. The drug release models of PVP/SA/AAP composite fibers with 18wt% and 21wt% PVP contents are more consistent with the Weibull model, indicating that the drug release mechanism of PVP/SA/AAP composite fibers is mainly drug diffusion and matrix dissolution. Comprehensive description: The release of drugs from PVP/SA/AAP composite fibers mainly goes through two stages. The first stage is that the fiber skeleton swells, and the drugs outside the fiber diffuse out through Fickian, and the drug release rate is faster; the second stage The fiber skeleton is degraded, the drugs inside the fiber diffuse out, and the drug release rate slows down.

表6含有15wt%PVP的PVP/SA/AAP复合纤维释药曲线药物释放动力学模型拟合Table 6 Drug release kinetic model fitting of drug release curve of PVP/SA/AAP composite fiber containing 15wt% PVP

表7含有18wt%PVP的PVP/SA/AAP复合纤维释药曲线药物释放动力学模型拟合Table 7 Drug release kinetic model fitting of drug release curve of PVP/SA/AAP composite fiber containing 18wt% PVP

表8含有21wt%PVP的PVP/SA/AAP复合纤维释药曲线药物释放动力学模型拟合Table 8 Drug release kinetic model fitting of drug release curve of PVP/SA/AAP composite fiber containing 21wt% PVP

以上依据本发明的理想实施例为启示,通过上述的说明内容,相关人员完全可以在不偏离本项发明技术思想的范围内,进行多样的变更以及修改。本项发明的技术性范围并不局限于说明书上的内容,必须要根据权利要求范围来确定技术性范围。The above is based on the ideal embodiment of the present invention. Through the above description, relevant personnel can make various changes and modifications without departing from the scope of the technical idea of the present invention. The technical scope of the present invention is not limited to the content in the description, and must be determined based on the scope of the claims.

Claims (4)

1. The preparation method of the composite drug-loaded fiber based on micro-spinning is characterized by comprising the following steps:
a1, taking polyvinylpyrrolidone and sodium alginate, respectively adding water, stirring and heating to obtain polyvinylpyrrolidone solution and sodium alginate solution; the concentration of the polyvinylpyrrolidone solution is 15-21 wt%, the concentration of the sodium alginate solution is 2wt%, and the polyvinylpyrrolidone solution and the sodium alginate solution are mixed according to the following weight ratio of 1:2, mixing in proportion;
a2, mixing a polyvinylpyrrolidone solution and a sodium alginate solution, and then adding acetaminophen to form a mixed spinning solution; adding 0-30wt% of acetaminophen into the mixed spinning solution, wherein the acetaminophen accounts for 0-30wt% of the total solute, but the acetaminophen is not included;
a3, taking the mixed spinning solution as a core layer, taking 0.1mol/L calcium chloride solution as a sheath flow laminar flow, coaxially spraying out fibers from the mixed spinning solution and the calcium chloride solution at different flow rates in a microfluid spinning mode, and continuously rotationally drafting out continuous fibers under the action of rotational traction force of a collecting device; preparing and forming continuous composite medicine carrying fibers by setting the translation rate and the circulation times of the collecting device;
the rotation speed of the collecting device is 50r/min, the translation speed of the collecting device is 4mm/min, the circulating translation is carried out once, the flow rate of the core layer solution is 28mL/h, and the flow rate of the sheath flow layer solution is 14mL/h.
2. A composite drug-loaded fiber prepared by the preparation method based on micro-fluid spinning of the composite drug-loaded fiber in claim 1, which is characterized in that:
the composite medicine carrying fiber is core-shell fiber, polyvinylpyrrolidone, sodium alginate and acetaminophen are uniformly dispersed in the composite medicine carrying fiber in an amorphous state, and hydrogen bonding is performed among the composite medicine carrying fibers.
3. A composite drug-loaded fiber as defined in claim 2, wherein: the breaking strength of the composite drug-carrying fiber is positively correlated with the concentration of the polyvinylpyrrolidone and the concentration of the acetaminophen.
4. A composite drug-loaded fiber as defined in claim 2, wherein: when the concentrations of the polyvinylpyrrolidone solution and the acetaminophen are respectively in the range of 15-21 wt% and 0-30 wt%, and the concentration of the acetaminophen is not included in the range of 0wt%; the cumulative percent acetaminophen release of the composite drug-loaded fibers is positively correlated to the concentration of the polyvinylpyrrolidone solution and acetaminophen.
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