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CN111621141B - A slow-release chlorine dioxide-water-based polyurethane antibacterial film and preparation method thereof - Google Patents

A slow-release chlorine dioxide-water-based polyurethane antibacterial film and preparation method thereof Download PDF

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CN111621141B
CN111621141B CN202010532685.XA CN202010532685A CN111621141B CN 111621141 B CN111621141 B CN 111621141B CN 202010532685 A CN202010532685 A CN 202010532685A CN 111621141 B CN111621141 B CN 111621141B
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黄崇杏
赵辉
许承龙
黄兴强
黄丽婕
段青山
王健
赵媛
黄浩河
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Abstract

本发明公开了一种缓释型二氧化氯‑水性聚氨酯抗菌膜及其制备方法,属于抗菌材料领域,本发明制备方法包括两大步骤,第一步是水性聚氨酯分散液合成,分散液的合成原料有硬段、软段、2,2‑二羟甲基丙酸、三乙胺、丙酮和催化剂二月桂酸二丁基锡;第二步是二氧化氯‑水性聚氨酯抗菌膜制备,向分散液中加入稳定性二氧化氯水溶液,通过浇铸法制备出缓释型二氧化氯‑水性聚氨酯抗菌膜;以膜中羧酸作为与二氧化氯反应的酸性活化剂,能够生产二氧化氯气体,使膜材具有了抑菌性能,同时也通过膜中羧酸的释放来控制二氧化氯气体的释放,从而达到一定的缓释效果。

Figure 202010532685

The invention discloses a slow-release chlorine dioxide-water-based polyurethane antibacterial film and a preparation method thereof, belonging to the field of antibacterial materials. The preparation method of the invention includes two major steps. The first step is to synthesize an aqueous polyurethane dispersion. The raw materials are hard segment, soft segment, 2,2-dimethylolpropionic acid, triethylamine, acetone and catalyst dibutyltin dilaurate; the second step is the preparation of chlorine dioxide-water-based polyurethane antibacterial film, which is added to the dispersion liquid A stable chlorine dioxide aqueous solution is added, and a slow-release chlorine dioxide-water-based polyurethane antibacterial film is prepared by a casting method; the carboxylic acid in the film is used as an acid activator for reacting with chlorine dioxide, and chlorine dioxide gas can be produced to make the film The material has antibacterial properties, and at the same time, the release of chlorine dioxide gas is controlled by the release of carboxylic acid in the film, so as to achieve a certain slow-release effect.

Figure 202010532685

Description

一种缓释型二氧化氯-水性聚氨酯抗菌膜及其制备方法A slow-release chlorine dioxide-water-based polyurethane antibacterial film and preparation method thereof

技术领域technical field

本发明涉及抗菌材料领域,特别是涉及一种缓释型二氧化氯-水性聚氨酯抗菌膜及其制备方法。The invention relates to the field of antibacterial materials, in particular to a slow-release chlorine dioxide-water-based polyurethane antibacterial film and a preparation method thereof.

背景技术Background technique

抗菌膜是抗菌包装中应用最多的一种形式,主要是因为抗菌膜的制备成本低廉、应用范围广、以及抑菌效果明显,因此抗菌膜有较好的应用前景。抗菌膜的抑菌效果主要是由添加的抗菌剂决定的,不同的抗菌剂对于抗菌膜的抑菌效果有很大的影响。就抗菌剂而言,抗菌膜就可以分为有机抗菌膜、无机抗菌膜和天然抗菌膜,这些抗菌膜的抑菌效果取决于抗菌剂的种类、添加量以及膜的基材。Antibacterial film is the most widely used form of antibacterial packaging, mainly because of its low preparation cost, wide application range, and obvious bacteriostatic effect, so antibacterial film has a good application prospect. The antibacterial effect of the antibacterial film is mainly determined by the added antibacterial agent, and different antibacterial agents have a great influence on the antibacterial effect of the antibacterial film. As far as antibacterial agents are concerned, antibacterial films can be divided into organic antibacterial films, inorganic antibacterial films and natural antibacterial films.

水性聚氨酯(WPU)以水为溶剂,绿色环保无污染并且无毒副作用,开始逐渐替代聚氨酯(PU)成为更加绿色环保的合成材料。水性聚氨酯同时又具备较好的相容性、机械性能和成膜性能,可以作为膜基材使用。Water-based polyurethane (WPU) uses water as a solvent, which is environmentally friendly, pollution-free, and has no toxic side effects. It has gradually replaced polyurethane (PU) as a more green and environmentally friendly synthetic material. Waterborne polyurethane also has good compatibility, mechanical properties and film-forming properties, and can be used as a film substrate.

二氧化氯(ClO2)具有高效杀菌效果、对环境无污染以及在使用时不会有三致(致癌、致畸、致突变)物质出现等优势,因此被世界卫生组织列为安全消毒物质中的A1级产品,二氧化氯也被广泛应用于水处理、空气净化、医疗、食品保鲜等领域。在生活生产中,气态二氧化氯见光或遇热易分解,液态二氧化氯性质不稳定,相比之下,固态二氧化氯稳定性强,储运方便,且具有一定缓释效果。但固态二氧化氯仍存在一些缺陷,例如二氧化氯在缓释阶段易出现暴释现象、其释放速率难控制等,这些问题都亟需解决。目前提及控制二氧化氯释放速度的专利文献有如下几种技术方案:Chlorine dioxide (ClO 2 ) has the advantages of efficient bactericidal effect, no pollution to the environment, and no three causes (carcinogenic, teratogenic, mutagenic) substances when used, so it is listed by the World Health Organization as one of the safe disinfection substances. A1 grade product, chlorine dioxide is also widely used in water treatment, air purification, medical treatment, food preservation and other fields. In daily production, gaseous chlorine dioxide is easily decomposed when exposed to light or heat, and liquid chlorine dioxide is unstable. In contrast, solid chlorine dioxide has strong stability, convenient storage and transportation, and has a certain slow-release effect. However, solid chlorine dioxide still has some defects, such as chlorine dioxide is prone to burst release in the slow-release stage, and its release rate is difficult to control, etc. These problems need to be solved urgently. At present, the patent documents that mention controlling the release rate of chlorine dioxide have the following technical solutions:

崔健发明了一种除甲醛二氧化氯缓释凝胶的制备方法,包括将葡萄糖酸钠、胶凝剂、二氧化氯前体混合得二氧化氯凝胶体系的步骤;向前述体系中加入聚乙二醇、酸性试剂得活化的二氧化氯缓释凝胶体系的步骤;向上述体系中加入硫酸钡得到稳定的活化二氧化氯凝胶体系的步骤。Cui Jian invented a method for preparing a formaldehyde-removing chlorine dioxide slow-release gel, which includes the steps of mixing sodium gluconate, a gelling agent, and a chlorine dioxide precursor to obtain a chlorine dioxide gel system; adding a polymer The steps of obtaining an activated chlorine dioxide slow-release gel system with ethylene glycol and an acidic reagent; the steps of adding barium sulfate to the above-mentioned system to obtain a stable activated chlorine dioxide gel system.

上海海洋大学发明了一种二氧化氯缓释保鲜凝胶的制备方法,该二氧化氯缓释保鲜凝胶包括凝胶层A和凝胶层B,所述凝胶层A的制备原料包括壳聚糖、氢氧化钠水溶液和亚氯酸钠,所述凝胶层B的制备原料包括壳聚糖、乙酸水溶液、酸性物质、戊二醛水溶液;应用时,将所述凝胶层A和所述凝胶层B贴合即可。Shanghai Ocean University invented a method for preparing a chlorine dioxide sustained-release fresh-keeping gel, the chlorine dioxide sustained-release fresh-keeping gel includes a gel layer A and a gel layer B, and the preparation raw materials of the gel layer A include a shell polysaccharide, sodium hydroxide aqueous solution and sodium chlorite, the preparation raw materials of the gel layer B include chitosan, acetic acid aqueous solution, acidic substance, and glutaraldehyde aqueous solution; in application, the gel layer A and all The gel layer B can be pasted together.

青岛农业大学发明了一种微控释高效气体保鲜材料,材料包括亚氯酸钠、柠檬酸、氯化亚铁、硫酸亚铁、硫酸亚铁铵、硅胶、明胶、聚丙烯酰胺、海藻酸钠、β-环糊精、去离子水,根据其制备工艺可制备二氧化氯夹心层数为1-4层的保鲜材料。Qingdao Agricultural University invented a micro-controlled release high-efficiency gas preservation material, which includes sodium chlorite, citric acid, ferrous chloride, ferrous sulfate, ferrous ammonium sulfate, silica gel, gelatin, polyacrylamide, sodium alginate , β-cyclodextrin, deionized water, according to the preparation process thereof, a fresh-keeping material with 1-4 layers of chlorine dioxide sandwich layers can be prepared.

宁波大学发明了一种长效缓释二氧化氯保鲜剂,由片剂和粉剂组成,片剂主要由硅胶吸附剂、亚氯酸钠、微孔网络结构形成剂、离子场形成剂和水组成;粉剂主要由弱酸活化剂、硅胶吸附剂、水和粘合剂组成,然后将片剂和粉剂放入透气性无纺布包装袋中。使用时轻微挤压包装袋,放置于潮湿环境中即可。Ningbo University invented a long-acting slow-release chlorine dioxide preservative, which is composed of tablet and powder. The tablet is mainly composed of silica gel adsorbent, sodium chlorite, microporous network structure forming agent, ion field forming agent and water. ;Powder is mainly composed of weak acid activator, silica gel adsorbent, water and binder, and then put the tablet and powder into a breathable non-woven bag. When using, squeeze the packaging bag slightly and place it in a humid environment.

但是,上述研究者对二氧化氯抗菌材料的制备,大多是直接添加亚氯酸钠粉体和有机酸。亚氯酸钠是产生二氧化氯的前驱体,直接混合在材料中,在光照、高温、高湿条件下不稳定,极易分解,这在一定程度上限制了二氧化氯的产率及作用时间。However, most of the above-mentioned researchers have directly added sodium chlorite powder and organic acid to the preparation of chlorine dioxide antibacterial materials. Sodium chlorite is a precursor to generate chlorine dioxide, which is directly mixed in the material, is unstable under light, high temperature, and high humidity conditions, and is easily decomposed, which limits the yield and effect of chlorine dioxide to a certain extent. time.

发明内容SUMMARY OF THE INVENTION

本发明的目的是提供一种缓释型二氧化氯-水性聚氨酯抗菌膜及其制备方法,以解决上述现有技术存在的问题,使抗菌膜能够达到对二氧化氯的控释作用,延长其缓释时间,达到长效的抗菌保鲜效果。The object of the present invention is to provide a slow-release chlorine dioxide-water-based polyurethane antibacterial film and a preparation method thereof, so as to solve the problems existing in the above-mentioned prior art, so that the antibacterial film can achieve the controlled release effect on chlorine dioxide, prolong its Slow release time to achieve long-term antibacterial and fresh-keeping effect.

为实现上述目的,本发明提供了如下方案:For achieving the above object, the present invention provides the following scheme:

本发明提供一种缓释型二氧化氯-水性聚氨酯抗菌膜的制备方法,在水性聚氨酯分散液中加入稳定性二氧化氯水溶液,搅拌混合均匀,放入模具中,室温风干成膜,即得缓释型二氧化氯-水性聚氨酯抗菌膜;The invention provides a preparation method of a slow-release chlorine dioxide-water-based polyurethane antibacterial film. A stable chlorine dioxide aqueous solution is added to the water-based polyurethane dispersion, stirred and mixed evenly, put into a mold, and air-dried at room temperature to form a film. Slow-release chlorine dioxide-water-based polyurethane antibacterial film;

所述水性聚氨酯分散液的制备方法,包括以下步骤:The preparation method of the water-based polyurethane dispersion comprises the following steps:

在保护氛围下,加入软段和2,2-羟甲基丙酸,搅拌条件下加入丙酮,进行第一次加热,并搅拌,滴加催化剂,再加入硬段和丙酮,冷凝回流,加入三乙胺和丙酮,进行第二次加热;Under the protective atmosphere, add the soft segment and 2,2-hydroxymethylpropionic acid, add acetone under stirring, heat for the first time, and stir, add the catalyst dropwise, then add the hard segment and acetone, condense and reflux, add three Ethylamine and acetone, for the second heating;

停止加热后,冷却,滴加蒸馏水,反应,即可得到水性聚氨酯分散液。After the heating is stopped, it is cooled, and distilled water is added dropwise to react to obtain an aqueous polyurethane dispersion.

进一步地,在各原料中,异腈酸根与羟基的总摩尔比为1.4:1,所述三乙胺与2,2-二羟甲基丙酸的摩尔量比为1:1。Further, in each raw material, the total molar ratio of isocyanide to hydroxyl is 1.4:1, and the molar ratio of triethylamine to 2,2-dimethylolpropionic acid is 1:1.

进一步地,第一次加入丙酮时,所述搅拌条件的搅拌速率为150-250r/min,所述丙酮的添加量为软段摩尔量的10%-200%,且每次加入的丙酮量相同。Further, when adding acetone for the first time, the stirring rate of the stirring condition is 150-250r/min, the addition amount of the acetone is 10%-200% of the molar amount of the soft segment, and the amount of acetone added each time is the same. .

进一步地于,所述第一次加热的温度在40-50℃,加热后的搅拌时间为20-30min。Further, the temperature of the first heating is 40-50° C., and the stirring time after heating is 20-30 min.

进一步地,滴加催化剂之前,要求溶液体系呈无色透明状。Further, before dropping the catalyst, the solution system is required to be colorless and transparent.

进一步地,所述第二次加热的加热时间为1h。Further, the heating time of the second heating is 1 h.

进一步地,所述蒸馏水的滴加过程在搅拌状态下进行,所述冷却为冷却至10℃以下;Further, the dropping process of the distilled water is carried out under stirring, and the cooling is cooling to below 10°C;

在滴加蒸馏水之前,搅拌速率为900-1100r/min,滴加速度为2-3s/滴,当溶液体系呈现由稠变稀现象时,调整搅拌速率至400-600r/min。Before adding distilled water dropwise, the stirring speed is 900-1100r/min, and the dropping speed is 2-3s/drop. When the solution system shows the phenomenon from thick to thin, adjust the stirring speed to 400-600r/min.

进一步地,所述稳定性二氧化氯水溶液的添加量为水性聚氨酯分散液体积的6%-30%。Further, the added amount of the stable chlorine dioxide aqueous solution is 6%-30% of the volume of the aqueous polyurethane dispersion.

进一步地,所述催化剂为二月桂酸二丁基锡,添加量为0.25ml。Further, the catalyst is dibutyltin dilaurate, and the addition amount is 0.25ml.

进一步地,所述硬段为甲苯二异氰酸酯、异佛尔酮二异氰酸酯、二苯基甲烷二异氰酸酯、二环己基甲烷二异氰酸酯、六亚甲基二异氰酸酯中的一种或几种;所述软段为分子量是1000到3000的聚四氢呋喃,聚三亚甲基醚二醇,聚己内酯二醇,聚碳酸酯二醇中的一种或几种。Further, the hard segment is one or more of toluene diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate, dicyclohexylmethane diisocyanate, and hexamethylene diisocyanate; The segment is one or more of polytetrahydrofuran, polytrimethylene ether glycol, polycaprolactone glycol, and polycarbonate glycol with a molecular weight of 1000 to 3000.

本发明还提供一种上述的缓释型二氧化氯-水性聚氨酯抗菌膜的制备方法制备的缓释型二氧化氯-水性聚氨酯抗菌膜。The present invention also provides a slow-release chlorine dioxide-water-based polyurethane antibacterial film prepared by the above-mentioned preparation method of the slow-release chlorine dioxide-water-based polyurethane antibacterial film.

本发明公开了以下技术效果:The present invention discloses the following technical effects:

1)抗菌膜的基材选用水性聚氨酯,其具有无毒、对环境无污染、易加工等优点,相容性好、机械性能和成膜性能优良,可用于食品包装材料。1) The base material of the antibacterial film is water-based polyurethane, which has the advantages of non-toxicity, no pollution to the environment, easy processing, good compatibility, excellent mechanical properties and film-forming properties, and can be used as food packaging materials.

2)在本发明的制备工艺条件下,制备的缓释型二氧化氯/水性聚氨酯抗菌膜,其拉伸强度可达到10.0-11.8MPa,断裂伸长率为450%-530%左右,膜的水蒸气透过量为100-120g/(m2·24h),膜的氧气透过率为3.3-6.2cm3·m-2·24h-1,抗菌膜的抑菌率可达到98%以上。2) Under the preparation process conditions of the present invention, the prepared slow-release chlorine dioxide/aqueous polyurethane antibacterial film has a tensile strength of 10.0-11.8MPa, a breaking elongation of about 450%-530%, and a The water vapor transmission rate is 100-120g/(m 2 ·24h), the oxygen transmission rate of the membrane is 3.3-6.2cm 3 ·m -2 ·24h -1 , and the antibacterial rate of the antibacterial film can reach more than 98%.

3)首次以水性聚氨酯膜中羧酸为活化剂,在不添加其他酸性试剂前提下,利用ClO2-和酸在水分的激发下反应匀速生产二氧化氯气体,提高缓释效果,有效地改善二氧化氯气体在释放过程中易出现的暴释现象。3) For the first time, the carboxylic acid in the water-based polyurethane film is used as the activator, and without adding other acidic reagents, ClO 2 - and acid are used to react at a uniform speed under the excitation of water to produce chlorine dioxide gas, which improves the slow-release effect and effectively improves the The explosive release phenomenon of chlorine dioxide gas is prone to occur during the release process.

说明书附图Instruction drawings

图1为实施例1制备的缓释型二氧化氯-水性聚氨酯抗菌膜平面图;Fig. 1 is the plan view of the slow-release chlorine dioxide-water-based polyurethane antibacterial film prepared in Example 1;

图2为实施例1制备的缓释型二氧化氯-水性聚氨酯抗菌膜断面图。2 is a cross-sectional view of the slow-release chlorine dioxide-water-based polyurethane antibacterial film prepared in Example 1.

具体实施方式Detailed ways

现详细说明本发明的多种示例性实施方式,该详细说明不应认为是对本发明的限制,而应理解为是对本发明的某些方面、特性和实施方案的更详细的描述。Various exemplary embodiments of the present invention will now be described in detail, which detailed description should not be construed as a limitation of the invention, but rather as a more detailed description of certain aspects, features, and embodiments of the invention.

应理解本发明中所述的术语仅仅是为描述特别的实施方式,并非用于限制本发明。另外,对于本发明中的数值范围,应理解为还具体公开了该范围的上限和下限之间的每个中间值。在任何陈述值或陈述范围内的中间值以及任何其他陈述值或在所述范围内的中间值之间的每个较小的范围也包括在本发明内。这些较小范围的上限和下限可独立地包括或排除在范围内。It should be understood that the terms described in the present invention are only used to describe particular embodiments, and are not used to limit the present invention. Additionally, for numerical ranges in the present disclosure, it should be understood that each intervening value between the upper and lower limits of the range is also specifically disclosed. Every smaller range between any stated value or intervening value in a stated range and any other stated value or intervening value in that stated range is also encompassed within the invention. The upper and lower limits of these smaller ranges may independently be included or excluded in the range.

除非另有说明,否则本文使用的所有技术和科学术语具有本发明所述领域的常规技术人员通常理解的相同含义。虽然本发明仅描述了优选的方法和材料,但是在本发明的实施或测试中也可以使用与本文所述相似或等同的任何方法和材料。本说明书中提到的所有文献通过引用并入,用以公开和描述与所述文献相关的方法和/或材料。在与任何并入的文献冲突时,以本说明书的内容为准。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention relates. Although only the preferred methods and materials are described herein, any methods and materials similar or equivalent to those described herein can also be used in the practice or testing of the present invention. All documents mentioned in this specification are incorporated by reference for the purpose of disclosing and describing the methods and/or materials in connection with which the documents are referred. In the event of conflict with any incorporated document, the content of this specification controls.

在不背离本发明的范围或精神的情况下,可对本发明说明书的具体实施方式做多种改进和变化,这对本领域技术人员而言是显而易见的。由本发明的说明书得到的其他实施方式对技术人员而言是显而易见得的。本申请说明书和实施例仅是示例性的。It will be apparent to those skilled in the art that various modifications and variations can be made in the specific embodiments of the present invention without departing from the scope or spirit of the invention. Other embodiments will be apparent to those skilled in the art from the description of the present invention. The description and examples of the present application are only exemplary.

实施例1Example 1

1)水性聚氨酯分散液的合成:1) Synthesis of aqueous polyurethane dispersion:

将聚四氢呋喃62.9109g和2,2-二羟甲基丙酸2.4842g添加到配备有数显搅拌器、控温装置、Ar保护气的500ml圆底四口烧瓶中;将搅拌器转速调至200r/min,在搅拌时加入125ml丙酮;接入蛇形冷凝管后用聚四氟乙烯生料带缠绕接口,以保证密封性。Add 62.9109g of polytetrahydrofuran and 2.4842g of 2,2-dimethylolpropionic acid to a 500ml round-bottom four-necked flask equipped with a digital display stirrer, temperature control device, and Ar protective gas; adjust the stirring speed to 200r /min, add 125ml of acetone during stirring; after connecting the serpentine condenser tube, wrap the interface with Teflon raw material tape to ensure tightness.

通过控温装置将加热温度控制在40-50℃之间,并加热搅拌20min,当四口烧瓶内溶液呈无色透明状,5min后滴加0.25ml催化剂(二月桂酸二丁基锡),滴加催化剂5min后再加入15.54g异佛尔酮二异氰酸酯和等量丙酮;当四口烧瓶内温度达到约70℃时,冷凝管开始出现冷凝回流,冷凝回流4小时后,接着加入1.8724g的三乙胺和等量丙酮;等到加入三乙胺一小时后停止加热,待四口烧瓶内的温度降到10℃以下时,再将冷凝管取下,接上装有160ml蒸馏水的恒压漏斗,并以6ml/min的速度进行滴加(滴加之前将搅拌器转速调至1000r/min),滴加过程中烧瓶内溶液会呈现出由稠变稀现象,此时将搅拌器转速调至为500r/min,防止溶液飞溅至烧瓶内壁;等到恒压漏斗内的蒸馏水滴加结束后,再反应30min便可得到水性聚氨酯分散液,将水性聚氨酯分散液倒入丝口瓶中密封保存。The heating temperature was controlled between 40-50 °C by the temperature control device, and heated and stirred for 20 minutes. When the solution in the four-necked flask was colorless and transparent, 0.25 ml of catalyst (dibutyltin dilaurate) was added dropwise after 5 minutes. 15.54g of isophorone diisocyanate and equal amount of acetone were added to the catalyst after 5min; when the temperature in the four-necked flask reached about 70°C, the condenser tube began to condense and reflux, and after 4 hours of condensate reflux, 1.8724g of triethyl ether was then added. amine and the same amount of acetone; stop heating after adding triethylamine for one hour, and when the temperature in the four-necked flask drops below 10 °C, remove the condenser tube, connect a constant pressure funnel with 160 ml of distilled water, and use The speed of 6ml/min was added dropwise (the speed of the stirrer was adjusted to 1000r/min before dropping), and the solution in the flask would show a phenomenon of thickening and thinning during the dropping process. At this time, the speed of the stirrer was adjusted to 500r/min. min to prevent the solution from splashing to the inner wall of the flask; after the dropwise addition of the distilled water in the constant pressure funnel is completed, the aqueous polyurethane dispersion can be obtained by reacting for another 30 min, and the aqueous polyurethane dispersion is poured into a silk-mouth bottle and sealed for storage.

2)二氧化氯-水性聚氨酯抗菌膜制备:2) Preparation of chlorine dioxide-water-based polyurethane antibacterial film:

用量筒量取30ml步骤1)所制备的水性聚氨酯分散液,再添加稳定性二氧化氯水溶液2ml,二者搅拌混合均匀,并倒入水平放置的方形聚四氟乙烯模具中,在室温条件下自然风干24h成膜,得到缓释型二氧化氯-水性聚氨酯抗菌膜,其平面图如图1所示,其断面图如图2所示。Measure 30ml of the aqueous polyurethane dispersion prepared in step 1) with a measuring cylinder, add 2ml of stable aqueous solution of chlorine dioxide, stir and mix the two evenly, and pour it into a square polytetrafluoroethylene mold placed horizontally. Naturally air-dried for 24 hours to form a film to obtain a slow-release chlorine dioxide-water-based polyurethane antibacterial film.

该实施例1所制备的抗菌膜拉伸强度可达到10.5MPa,断裂伸长率为460%,膜的水蒸气透过量为112g/(m2·24h),膜的氧气透过率为4.6cm3·m-2·24h-1,抗菌膜的抑菌率可达到98%以上。The tensile strength of the antibacterial film prepared in Example 1 can reach 10.5MPa, the elongation at break is 460%, the water vapor transmission rate of the film is 112g/(m 2 ·24h), and the oxygen transmission rate of the film is 4.6cm 3 ·m -2 ·24h -1 , the antibacterial rate of the antibacterial film can reach more than 98%.

实施例2Example 2

1)水性聚氨酯分散液的合成:1) Synthesis of aqueous polyurethane dispersion:

将聚四氢呋喃48.2248g和2,2-二羟甲基丙酸3.4826g添加到配备有数显搅拌器、控温装置、Ar保护气的500ml圆底四口烧瓶中;将搅拌器转速调至200r/min,在搅拌时加入100ml的丙酮;接入蛇形冷凝管后用聚四氟乙烯生料带缠绕接口,以保证密封性。Add 48.2248g of polytetrahydrofuran and 3.4826g of 2,2-dimethylolpropionic acid to a 500ml round-bottom four-necked flask equipped with a digital display stirrer, temperature control device, and Ar protective gas; adjust the stirring speed to 200r /min, add 100ml of acetone during stirring; after connecting the serpentine condenser tube, wrap the interface with Teflon raw material tape to ensure tightness.

通过控温装置将加热温度控制在40-50℃之间,并加热搅拌20min,当四口烧瓶内溶液呈无色透明状,5min后滴加0.25ml催化剂(二月桂酸二丁基锡),滴加催化剂5min后再加入15.54g异佛尔酮二异氰酸酯和等量丙酮;当四口烧瓶内温度达到约70℃时,冷凝管开始出现冷凝回流,冷凝回流4小时后,接着加入2.6250g的三乙胺和等量丙酮;等到加入三乙胺一小时后停止加热,待四口烧瓶内的温度降到10℃以下时,再将冷凝管取下,接上装有140ml蒸馏水的恒压漏斗,并以6ml/min的速度进行滴加(滴加之前将搅拌器转速调至900r/min),滴加过程中烧瓶内溶液会呈现出由稠变稀现象,此时将搅拌器转速调至为450r/min,防止溶液飞溅至烧瓶内壁;等到恒压漏斗内的蒸馏水滴加结束后再反应30min便可得到水性聚氨酯分散液,将水性聚氨酯分散液倒入丝口瓶中密封保存。The heating temperature was controlled between 40-50 °C by the temperature control device, and heated and stirred for 20 minutes. When the solution in the four-necked flask was colorless and transparent, 0.25 ml of catalyst (dibutyltin dilaurate) was added dropwise after 5 minutes. 15.54g of isophorone diisocyanate and an equal amount of acetone were added to the catalyst after 5 minutes; when the temperature in the four-necked flask reached about 70°C, the condenser tube began to condense and reflux, and after 4 hours of condensate reflux, 2.6250g of triethyl ether was then added. amine and the same amount of acetone; stop heating one hour after adding triethylamine, and when the temperature in the four-necked flask drops below 10 °C, remove the condenser tube, connect a constant pressure funnel with 140 ml of distilled water, and use Dropwise at a speed of 6ml/min (adjust the speed of the stirrer to 900r/min before dropping), the solution in the flask will show a phenomenon of thickening and thinning during the dropping process, at this time, adjust the speed of the stirrer to 450r/min. min to prevent the solution from splashing to the inner wall of the flask; wait until the end of the dropwise addition of distilled water in the constant pressure funnel, and then react for 30 min to obtain an aqueous polyurethane dispersion, and pour the aqueous polyurethane dispersion into a silk neck bottle and seal it for storage.

2)二氧化氯-水性聚氨酯抗菌膜制备:2) Preparation of chlorine dioxide-water-based polyurethane antibacterial film:

用量筒量取50ml步骤1)所制备的水性聚氨酯分散液,再添加稳定性二氧化氯水溶液5ml,二者搅拌混合均匀,并倒入水平放置的方形聚四氟乙烯模具中,在室温条件下自然风干24h成膜,得到缓释型二氧化氯-水性聚氨酯抗菌膜。Measure 50ml of the aqueous polyurethane dispersion prepared in step 1) with a measuring cylinder, add 5ml of stable chlorine dioxide aqueous solution, stir and mix the two evenly, and pour it into a horizontal square polytetrafluoroethylene mold. Naturally air-dried for 24 hours to form a film to obtain a slow-release chlorine dioxide-water-based polyurethane antibacterial film.

该实施例2所制备的抗菌膜拉伸强度可达到11.0MPa,断裂伸长率为480%,膜的水蒸气透过量为110g/(m2·24h),膜的氧气透过率为3.6cm3·m-2·24h-1,抗菌膜的抑菌率可达到99%以上。The tensile strength of the antibacterial film prepared in Example 2 can reach 11.0MPa, the elongation at break is 480%, the water vapor transmission rate of the film is 110g/(m 2 ·24h), and the oxygen transmission rate of the film is 3.6cm 3 ·m -2 ·24h -1 , the antibacterial rate of the antibacterial film can reach more than 99%.

实施例3Example 3

1)水性聚氨酯分散液的合成:1) Synthesis of aqueous polyurethane dispersion:

将聚四氢呋喃37.2014g和2,2-二羟甲基丙酸4.2062g添加到配备有数显搅拌器、控温装置、Ar保护气的500ml圆底四口烧瓶中;将搅拌器转速调至250r/min,在搅拌时加入75ml的丙酮;接入蛇形冷凝管后用聚四氟乙烯生料带缠绕接口,以保证密封性。Add 37.2014g of polytetrahydrofuran and 4.2062g of 2,2-dimethylolpropionic acid to a 500ml round-bottom four-necked flask equipped with a digital display stirrer, temperature control device, and Ar protective gas; adjust the stirring speed to 250r /min, add 75ml of acetone during stirring; after connecting the serpentine condenser tube, wrap the interface with Teflon raw material tape to ensure tightness.

通过控温装置将加热温度控制在40-50℃之间,并加热搅拌25min,当四口烧瓶内溶液呈无色透明状,5min后滴加0.25ml催化剂(二月桂酸二丁基锡),滴加催化剂4min后再加入15.54g异佛尔酮二异氰酸酯和等量丙酮;当四口烧瓶内温度达到约70℃时,冷凝管开始出现冷凝回流,冷凝回流4小时后,接着加入3.1703g的三乙胺和等量丙酮;等到加入三乙胺一小时后停止加热,待四口烧瓶内的温度降到10℃以下时,再将冷凝管取下,接上装有120ml蒸馏水的恒压漏斗,并以6ml/min的速度进行滴加(滴加之前将搅拌器转速调至900r/min),滴加过程中烧瓶内溶液会呈现出由稠变稀现象,此时将搅拌器转速调至为500r/min,防止溶液飞溅至烧瓶内壁;等到恒压漏斗内的蒸馏水滴加结束后再反应30min便可得到水性聚氨酯分散液,将水性聚氨酯分散液倒入丝口瓶中密封保存。The heating temperature was controlled between 40-50 ℃ by the temperature control device, and heated and stirred for 25min. When the solution in the four-necked flask was colorless and transparent, 0.25ml of catalyst (dibutyltin dilaurate) was added dropwise after 5min. 15.54g of isophorone diisocyanate and an equal amount of acetone were added to the catalyst after 4min; when the temperature in the four-necked flask reached about 70°C, the condenser tube began to condense and reflux, and after 4 hours of condensate reflux, 3.1703g of triethyl ether was then added. amine and an equal amount of acetone; stop heating one hour after adding triethylamine, and when the temperature in the four-necked flask drops below 10°C, remove the condenser tube, connect a constant pressure funnel with 120ml of distilled water, and use Add dropwise at a speed of 6ml/min (adjust the speed of the stirrer to 900r/min before dropping), the solution in the flask will show a phenomenon of thickening and thinning during the dropping process, at this time, adjust the speed of the stirrer to 500r/min. min to prevent the solution from splashing to the inner wall of the flask; wait until the end of the dropwise addition of distilled water in the constant pressure funnel, and then react for 30 min to obtain an aqueous polyurethane dispersion, and pour the aqueous polyurethane dispersion into a silk neck bottle and seal it for storage.

2)二氧化氯-水性聚氨酯抗菌膜制备:2) Preparation of chlorine dioxide-water-based polyurethane antibacterial film:

用量筒量取60ml步骤1)所制备的水性聚氨酯分散液,再添加稳定性二氧化氯水溶液8ml,二者搅拌混合均匀,并倒入水平放置的方形聚四氟乙烯模具中,在室温条件下自然风干36h成膜,得到缓释型二氧化氯-水性聚氨酯抗菌膜。Measure 60ml of the aqueous polyurethane dispersion prepared in step 1) with a measuring cylinder, add 8ml of stable chlorine dioxide aqueous solution, stir and mix the two evenly, and pour it into a horizontal square PTFE mold. Naturally air-dried for 36h to form a film to obtain a slow-release chlorine dioxide-water-based polyurethane antibacterial film.

该实施例1所制备的抗菌膜拉伸强度可达到10.1MPa,断裂伸长率为450%左右,膜的水蒸气透过量为130g/(m2·24h),膜的氧气透过率为5.5cm3·m-2·24h-1,抗菌膜的抑菌率可达到99%以上。The tensile strength of the antibacterial film prepared in Example 1 can reach 10.1MPa, the elongation at break is about 450%, the water vapor transmission rate of the film is 130g/(m 2 ·24h), and the oxygen transmission rate of the film is 5.5 cm 3 ·m -2 ·24h -1 , the antibacterial rate of the antibacterial film can reach more than 99%.

对比例1Comparative Example 1

与实施例3的不同之处在于,所述的蒸馏水滴加操作改为直接混合。The difference from Example 3 is that the dropwise addition of distilled water is changed to direct mixing.

经测试,对比例1所制备的抗菌膜的水蒸气透过率为89g/(m2·24h),膜的氧气透过率为1.5cm3·m-2·24h-1,抗菌膜的抑菌率在85%以上。After testing, the water vapor transmission rate of the antibacterial film prepared in Comparative Example 1 was 89g/(m 2 ·24h), and the oxygen transmission rate of the film was 1.5cm 3 ·m -2 ·24h -1 . The bacterial rate is above 85%.

对比例2Comparative Example 2

与实施例3的不同之处在于,每次丙酮的添加量都为聚四氢呋喃添加量的3倍。The difference from Example 3 is that the amount of acetone added each time is 3 times the amount of polytetrahydrofuran added.

经测试,对比例2所制备的抗菌膜的水蒸气透过率为89g/(m2·24h),膜的氧气透过率为1.8cm3·m-2·24h-1,抗菌膜的抑菌率在88%以上。After testing, the water vapor transmission rate of the antibacterial film prepared in Comparative Example 2 was 89g/(m 2 ·24h), and the oxygen transmission rate of the film was 1.8cm 3 ·m -2 ·24h -1 . The bacterial rate is above 88%.

对比例3Comparative Example 3

与实施例3的不同之处在于,三次添加丙酮的量不等量,从第一次到第三次每次丙酮的添加量分别是聚四氢呋喃添加量的1倍、1.3倍和1.9倍。The difference from Example 3 is that the amount of acetone added three times is not equal, and the amount of acetone added each time from the first to the third time is 1, 1.3, and 1.9 times that of polytetrahydrofuran, respectively.

经测试,对比例3所制备的抗菌膜的水蒸气透过率为78g/(m2·24h),膜的氧气透过率为2.1cm3·m-2·24h-1,抗菌膜的抑菌率在80%以上。After testing, the water vapor transmission rate of the antibacterial film prepared in Comparative Example 3 was 78g/(m 2 ·24h), and the oxygen transmission rate of the film was 2.1cm 3 ·m -2 ·24h -1 . The bacterial rate is above 80%.

以上所述的实施例仅是对本发明的优选方式进行描述,并非对本发明的范围进行限定,在不脱离本发明设计精神的前提下,本领域普通技术人员对本发明的技术方案做出的各种变形和改进,均应落入本发明权利要求书确定的保护范围内。The above-mentioned embodiments are only to describe the preferred mode of the present invention, but not to limit the scope of the present invention. Without departing from the design spirit of the present invention, those of ordinary skill in the art can Variations and improvements should fall within the protection scope determined by the claims of the present invention.

Claims (7)

1. A preparation method of a slow-release chlorine dioxide-waterborne polyurethane antibacterial film is characterized in that a stable chlorine dioxide aqueous solution is added into a waterborne polyurethane dispersion liquid, the mixture is stirred and mixed evenly, the mixture is placed into a mold, and the mold is dried at room temperature to form a film, so that the slow-release chlorine dioxide-waterborne polyurethane antibacterial film is obtained;
the preparation method of the aqueous polyurethane dispersion comprises the following steps:
adding a soft segment and 2, 2-dimethylolpropionic acid in a protective atmosphere, adding acetone under the stirring condition, carrying out first heating, stirring, dropwise adding a catalyst, adding a hard segment and acetone, carrying out condensation reflux, adding triethylamine and acetone, and carrying out second heating;
stopping heating, cooling, dripping distilled water, and reacting to obtain aqueous polyurethane dispersion;
in all raw materials, the total molar ratio of isocyanic acid radical to hydroxyl is 1.4:1, and the molar weight ratio of triethylamine to 2, 2-dimethylolpropionic acid is 1: 1;
when the acetone is added for the first time, the stirring speed under the stirring condition is 150-250r/min, the adding amount of the acetone is 10-200% of the soft segment molar weight, and the amount of the acetone added each time is the same;
the dropping process of the distilled water is carried out under the stirring state, and the cooling is carried out to be below 10 ℃;
before the distilled water is dripped, the stirring speed is 900-1100r/min, the dripping speed is 2-3 s/min, and when the solution system shows the phenomenon of thickening and thinning, the stirring speed is adjusted to 400-600 r/min.
2. The method for preparing the slow-release chlorine dioxide-waterborne polyurethane antibacterial film according to claim 1, wherein the first heating temperature is 40-50 ℃, and the stirring time after heating is 20-30 min.
3. The method for preparing a sustained-release chlorine dioxide-aqueous polyurethane antibacterial film according to claim 1, wherein the solution system is required to be colorless and transparent before the catalyst is added dropwise.
4. The preparation method of the slow-release chlorine dioxide-waterborne polyurethane antibacterial film according to claim 1, wherein the second heating temperature is 40-50 ℃ and the heating time is 1 h.
5. The preparation method of the slow-release chlorine dioxide-waterborne polyurethane antibacterial film according to claim 1, wherein the addition amount of the stable chlorine dioxide aqueous solution is 6-30% of the volume of the waterborne polyurethane dispersion liquid;
the catalyst is dibutyltin dilaurate, and the addition amount of the catalyst is 0.1-0.5% of the total amount of polyurethane.
6. The preparation method of the slow-release chlorine dioxide-waterborne polyurethane antibacterial film according to claim 1, wherein the hard segment is one or more of toluene diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate, dicyclohexylmethane diisocyanate and hexamethylene diisocyanate; the soft segment is one or more of polytetrahydrofuran with molecular weight of 1000-3000, polytrimethylene ether glycol, polycaprolactone glycol and polycarbonate glycol.
7. A slow-release chlorine dioxide-waterborne polyurethane antibacterial film prepared by the preparation method of the slow-release chlorine dioxide-waterborne polyurethane antibacterial film as defined in any one of claims 1 to 6.
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