[go: up one dir, main page]

CN117487223A - A kind of preparation method of shellac resin and PVA composite film - Google Patents

A kind of preparation method of shellac resin and PVA composite film Download PDF

Info

Publication number
CN117487223A
CN117487223A CN202311761428.3A CN202311761428A CN117487223A CN 117487223 A CN117487223 A CN 117487223A CN 202311761428 A CN202311761428 A CN 202311761428A CN 117487223 A CN117487223 A CN 117487223A
Authority
CN
China
Prior art keywords
pva
shellac resin
composite film
shellac
preparing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202311761428.3A
Other languages
Chinese (zh)
Inventor
冀浩博
张敏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kunming Metallurgy College
Original Assignee
Kunming Metallurgy College
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kunming Metallurgy College filed Critical Kunming Metallurgy College
Priority to CN202311761428.3A priority Critical patent/CN117487223A/en
Publication of CN117487223A publication Critical patent/CN117487223A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2329/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
    • C08J2329/02Homopolymers or copolymers of unsaturated alcohols
    • C08J2329/04Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2393/00Characterised by the use of natural resins; Derivatives thereof
    • C08J2393/02Shellac

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

The invention relates to a preparation method of a shellac resin and PVA composite film, which comprises the following steps of (1) preparing shellac resin emulsion; (2) preparing an aqueous PVA solution; (3) blending to form a film; according to the invention, the ultraviolet resin and the PVA are adopted to prepare the composite film through the aqueous phase physical blending method, the compactness of the ultraviolet resin film is improved by adding the PVA, and the compactness, the tensile strength and the elongation at break of the composite film are also improved along with the increase of the PVA content, so that the degree of chemical reaction of the ultraviolet resin and the PVA is low, and the ultraviolet resin and the PVA have certain physical compatibility. And along with the increase of PVA content, the contact angle of the composite film is continuously reduced, the hygroscopicity of the composite film is continuously enhanced, and further, the composite film has better hydrophilicity, the composite film and the composite film have larger degree of physical blending, and the shellac resin is more stable in the solution.

Description

一种紫胶树脂与PVA复合膜的制备方法A kind of preparation method of shellac resin and PVA composite film

技术领域Technical field

本发明属于风电设备运行、维护技术领域,具体涉及一种紫胶树脂与PVA复合膜的制备方法。The invention belongs to the technical field of wind power equipment operation and maintenance, and specifically relates to a preparation method of a shellac resin and PVA composite film.

背景技术Background technique

紫胶作为一种由紫胶虫在吸取植物汁液后分泌出的天然无毒可降解且具有特殊性能的天然树脂混合物,其在制药领域的应用历史悠久。然而紫胶树脂本身的机械性能较差,长期贮存时容易发生聚合等老化反应。因此,在使用前绝大多数情况下会采用另外一种物质对其改性,改善其物理性与机械性的同时,着重改善其亲水类性能,进一步拓展紫胶作为药用天然高分子材料的应用范围。Shellac is a natural, non-toxic, degradable and special-property natural resin mixture secreted by lac insects after sucking plant sap. It has a long history of application in the pharmaceutical field. However, the mechanical properties of shellac resin itself are poor, and aging reactions such as polymerization are prone to occur during long-term storage. Therefore, in most cases, another substance will be used to modify it before use. While improving its physical and mechanical properties, it also focuses on improving its hydrophilic properties and further expanding the use of shellac as a medicinal natural polymer material. scope of application.

PVA具有良好的亲水性能和成膜柔韧性,且医药级PVA是一种极安全的高分子有机物,对身体无毒、无副作用,具有良好的生物相容性。由此可以看出,PVA与紫胶树脂在性质上具有互补性。正好可以将其用作改善紫胶树脂的备选材料,在紫胶树脂中掺入PVA制备复合膜,研究复合膜的亲水性等方面的情况,以便扩展二者的适用性。PVA has good hydrophilic properties and film-forming flexibility, and pharmaceutical-grade PVA is an extremely safe polymer organic substance that is non-toxic to the body, has no side effects, and has good biocompatibility. It can be seen from this that PVA and shellac resin are complementary in nature. It can be used as an alternative material to improve the shellac resin. PVA is mixed into the shellac resin to prepare a composite membrane, and the hydrophilicity of the composite membrane is studied to expand the applicability of the two.

发明内容Contents of the invention

针对上述问题,本发明提供一种紫胶树脂与PVA复合膜的制备方法。In view of the above problems, the present invention provides a preparation method of a shellac resin and PVA composite film.

具体技术方案是:一种紫胶树脂与PVA复合膜的制备方法,包括如下步骤:The specific technical solution is: a preparation method of a shellac resin and PVA composite film, including the following steps:

(1)制备紫胶树脂乳液:将紫胶树脂在无水乙醇中溶解,过滤,除去醇不溶物,滤液以5mL/min的速度加入高速剪切的去离子水中,制备成紫胶树脂乳液,备用;(1) Preparation of shellac resin emulsion: Dissolve shellac resin in absolute ethanol, filter, and remove alcohol-insoluble matter. The filtrate is added to high-speed sheared deionized water at a speed of 5 mL/min to prepare shellac resin emulsion. spare;

(2)制备PVA水溶液:将PVA溶于90℃的去离子水中,然后冷却至室温,制得PVA水溶液,备用;(2) Prepare PVA aqueous solution: Dissolve PVA in deionized water at 90°C, and then cool to room temperature to prepare a PVA aqueous solution for later use;

(3)共混成膜:将上述制备得到的紫胶树脂乳液与PVA水溶液于50℃的水浴中混合并搅拌2h,然后转移至旋转蒸发仪中旋转蒸发1h,以回收部分溶剂乙醇,旋蒸后将混合液转移到室温下继续搅拌24h,并去除混合液表面气泡,最后将液体倒入培养皿中,于30℃的电热恒温培养箱内干燥24h,待混合液的溶剂乙醇和水充分挥发,混合液干燥成紫胶树脂与PVA复合膜后将其揭起,制得紫胶树脂与PVA复合膜。(3) Blending film formation: Mix the shellac resin emulsion and PVA aqueous solution prepared above in a water bath at 50°C and stir for 2 hours, and then transfer to a rotary evaporator to rotary evaporate for 1 hour to recover part of the solvent ethanol. After rotary evaporation Transfer the mixture to room temperature and continue stirring for 24 hours, and remove bubbles on the surface of the mixture. Finally, pour the liquid into a petri dish and dry it in an electric constant-temperature incubator at 30°C for 24 hours until the solvents of the mixture, ethanol and water, are fully evaporated. The mixed liquid is dried into a shellac resin and PVA composite film and then lifted up to obtain a shellac resin and PVA composite film.

进一步,步骤(1)中紫胶树脂与无水乙醇的质量比为5:194.1。Further, the mass ratio of shellac resin and absolute ethanol in step (1) is 5:194.1.

进一步,步骤(1)中高速剪切的剪切速率>1000r/min。Furthermore, the shear rate of high-speed shearing in step (1) is >1000r/min.

进一步,步骤(1)中紫胶树脂滤液与去离子水的体积比为2:1。Further, the volume ratio of the shellac resin filtrate and deionized water in step (1) is 2:1.

进一步,步骤(2)中PVA与去离子水的质量比为1:30。Further, the mass ratio of PVA and deionized water in step (2) is 1:30.

进一步,步骤(3)中PVA在复合膜中的质量分数控制为50%。Further, in step (3), the mass fraction of PVA in the composite film is controlled to 50%.

本发明的有益效果:本发明采用紫胶树脂与PVA通过水相物理共混法制备复合膜,PVA的加入提高了紫胶树脂膜的致密性,且随着PVA含量的增加,复合膜的致密性、拉伸强度、断裂伸长率也随之提高,二者发生化学反应的程度较低,紫胶树脂与PVA具有一定的物理相容性。而且随着PVA含量的增加,复合膜的接触角不断减小,复合膜吸湿性不断增强,进一步印证了复合膜具有较好的亲水性,且二者的复合具有较大程度的物理共混,紫胶树脂在其溶液中较稳定。Beneficial effects of the present invention: The present invention uses shellac resin and PVA to prepare a composite film through an aqueous physical blending method. The addition of PVA improves the density of the shellac resin film, and as the PVA content increases, the density of the composite film increases. The properties, tensile strength, and elongation at break also increase. The degree of chemical reaction between the two is relatively low. Shellac resin and PVA have certain physical compatibility. Moreover, as the PVA content increases, the contact angle of the composite film continues to decrease, and the hygroscopicity of the composite film continues to increase, which further confirms that the composite film has better hydrophilicity, and the combination of the two has a greater degree of physical blending , Shellac resin is relatively stable in its solution.

附图说明Description of drawings

图1是本发明不同PVA质量分数下复合膜的外观形态图;其中:(a)PVA比例为0%;(b)PVA比例为10%;(c)PVA比例为20%;(d)PVA比例为30%;(e)PVA比例为40%;(f)PVA比例为50%;(g)PVA比例为100%;图中黑色为背景色;Figure 1 is a diagram of the appearance of the composite film under different PVA mass fractions of the present invention; wherein: (a) the PVA proportion is 0%; (b) the PVA proportion is 10%; (c) the PVA proportion is 20%; (d) PVA The proportion is 30%; (e) the PVA proportion is 40%; (f) the PVA proportion is 50%; (g) the PVA proportion is 100%; black is the background color in the picture;

图2为本发明不同PVA质量分数下复合膜的水静滴接触角形态图;(a)PVA比例为10%;(b)PVA比例为20%;(c)PVA比例为30%;(d)PVA比例为40%;(e)PVA比例为50%;Figure 2 is a morphological diagram of the water droplet contact angle of the composite film under different PVA mass fractions of the present invention; (a) PVA proportion is 10%; (b) PVA proportion is 20%; (c) PVA proportion is 30%; (d) ) PVA proportion is 40%; (e) PVA proportion is 50%;

图3为本发明不同PVA质量分数下复合膜的吸湿等温线;Figure 3 is the moisture absorption isotherm of the composite film under different PVA mass fractions of the present invention;

图4为本发明紫胶树脂乳液与PVA水溶液的共混溶液图。Figure 4 is a blended solution diagram of the shellac resin emulsion and PVA aqueous solution of the present invention.

具体实施方式Detailed ways

为了使本发明所解决的技术问题、技术方案更加清楚明白,以下结合附图及实施例,对本发明进一步详细说明。应当理解,此处所描述的具体实施例仅仅用于解释本发明,并不用于限定本发明。In order to make the technical problems and technical solutions solved by the present invention clearer, the present invention will be further described in detail below with reference to the drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention and are not intended to limit the present invention.

实施例1:PVA在复合膜中的质量分数为10%。Example 1: The mass fraction of PVA in the composite film is 10%.

(1)制备紫胶树脂乳液:将18g紫胶树脂加入900mL无水乙醇中,搅拌溶解后,过滤除去醇不溶物,滤液经蠕动泵以5ml/min的速度加入高速剪切(剪切速率为1000r/min)的去离子水中,紫胶树脂滤液与去离子水体积比为2:1,制备成紫胶树脂乳液,备用;(1) Preparation of shellac resin emulsion: Add 18g of shellac resin to 900mL of absolute ethanol. After stirring and dissolving, filter to remove alcohol-insoluble matter. The filtrate is added to high-speed shear at a speed of 5ml/min through a peristaltic pump (the shear rate is 1000r/min) in deionized water, the volume ratio of the shellac resin filtrate to the deionized water is 2:1, prepare a shellac resin emulsion for later use;

(2)制备PVA水溶液:将2gPVA溶于90℃的60mL去离子水中,然后冷却至室温,制得PVA水溶液,备用;(2) Prepare PVA aqueous solution: Dissolve 2g PVA in 60 mL deionized water at 90°C, and then cool to room temperature to prepare a PVA aqueous solution for later use;

(3)共混成膜:将上述制备得到的紫胶树脂乳液与PVA水溶液按照紫胶树脂与PVA质量比为9:1时的体积比(约30:2)置于50℃的水浴中混合并搅拌2h后,转移至旋转蒸发仪中旋转蒸发1h,以回收部分溶剂乙醇,然后转移到室温下继续搅拌24h,并去除混合液表面气泡,最后将液体倒入培养皿中,于30℃的电热恒温培养箱内干燥24h,待混合液的溶剂乙醇和水充分挥发,混合液干燥成紫胶树脂与PVA复合膜后将其揭起,制得紫胶树脂与PVA复合膜。(3) Blending film formation: Place the shellac resin emulsion and PVA aqueous solution prepared above in a water bath at 50°C and mix according to the volume ratio (about 30:2) when the mass ratio of shellac resin to PVA is 9:1. After stirring for 2 hours, transfer to a rotary evaporator for 1 hour to recover part of the solvent ethanol, and then transfer to room temperature to continue stirring for 24 hours and remove bubbles on the surface of the mixture. Finally, pour the liquid into a petri dish and heat it with electric heating at 30°C. Dry in a constant-temperature incubator for 24 hours. After the solvents ethanol and water of the mixed solution are fully evaporated, the mixed solution is dried into a shellac resin and PVA composite film and then peeled off to prepare a shellac resin and PVA composite film.

实施例2:PVA在复合膜中的质量分数为20%。Example 2: The mass fraction of PVA in the composite film is 20%.

(1)制备紫胶树脂乳液:将12g紫胶树脂加入600mL无水乙醇中,搅拌溶解后,过滤除去醇不溶物,滤液经蠕动泵以5ml/min的速度加入高速剪切(剪切速率为1000r/min)的去离子水中,紫胶树脂滤液与去离子水体积比为2:1,制备成紫胶树脂乳液,备用;(1) Preparation of shellac resin emulsion: Add 12g of shellac resin to 600mL of absolute ethanol, stir and dissolve, filter to remove alcohol-insoluble matter, and add the filtrate to high-speed shear at a speed of 5ml/min through a peristaltic pump (the shear rate is 1000r/min) in deionized water, the volume ratio of the shellac resin filtrate to the deionized water is 2:1, and prepare a shellac resin emulsion for later use;

(2)制备PVA水溶液:将3gPVA溶于90℃的90mL去离子水中,然后冷却至室温,制得PVA水溶液,备用;(2) Prepare PVA aqueous solution: Dissolve 3g PVA in 90 mL deionized water at 90°C, and then cool to room temperature to prepare a PVA aqueous solution for later use;

(3)共混成膜:将上述制备得到的紫胶树脂乳液与PVA水溶液按照紫胶树脂与PVA质量比为8:2时的体积比(约20:3)置于50℃的水浴中混合并搅拌2h后,转移至旋转蒸发仪中旋转蒸发1h,以回收部分溶剂乙醇,然后转移到室温下继续搅拌24h,并去除混合液表面气泡,最后将液体倒入培养皿中,于30℃的电热恒温培养箱内干燥24h,待混合液的溶剂乙醇和水充分挥发,混合液干燥成紫胶树脂与PVA复合膜后将其揭起,制得紫胶树脂与PVA复合膜。(3) Blending film formation: Place the shellac resin emulsion and PVA aqueous solution prepared above in a water bath at 50°C and mix according to the volume ratio (approximately 20:3) when the mass ratio of shellac resin to PVA is 8:2. After stirring for 2 hours, transfer to a rotary evaporator for 1 hour to recover part of the solvent ethanol. Then transfer to room temperature to continue stirring for 24 hours and remove air bubbles on the surface of the mixture. Finally, pour the liquid into a petri dish and heat it with electric heating at 30°C. Dry in a constant-temperature incubator for 24 hours. After the solvents ethanol and water of the mixed solution are fully evaporated, the mixed solution is dried into a shellac resin and PVA composite film and then peeled off to prepare a shellac resin and PVA composite film.

实施例3:PVA在复合膜中的质量分数为30%。Example 3: The mass fraction of PVA in the composite film is 30%.

(1)制备紫胶树脂乳液:将9.3g紫胶树脂加入465mL无水乙醇中,搅拌溶解后,过滤除去醇不溶物,滤液经蠕动泵以5ml/min的速度加入高速剪切(剪切速率为1000r/min)的去离子水中,紫胶树脂滤液与去离子水体积比为2:1,制备成紫胶树脂乳液,备用;(1) Preparation of shellac resin emulsion: Add 9.3g of shellac resin to 465mL of absolute ethanol. After stirring and dissolving, filter to remove alcohol-insoluble matter. The filtrate is added to high-speed shear (shear rate) through a peristaltic pump at a speed of 5ml/min. (1000r/min) in deionized water, the volume ratio of the shellac resin filtrate to the deionized water is 2:1, prepare a shellac resin emulsion for later use;

(2)制备PVA水溶液:将4gPVA溶于90℃的120mL去离子水中,然后冷却至室温,制得PVA水溶液,备用;(2) Prepare PVA aqueous solution: Dissolve 4g PVA in 120mL deionized water at 90°C, and then cool to room temperature to prepare a PVA aqueous solution for later use;

(3)共混成膜:将上述制备得到的紫胶树脂乳液与PVA水溶液按照紫胶树脂与PVA质量比为7:3时的体积比(约31:8)置于50℃的水浴中混合并搅拌2h后,转移至旋转蒸发仪中旋转蒸发1h,以回收部分溶剂乙醇,然后转移到室温下继续搅拌24h,并去除混合液表面气泡,最后将液体倒入培养皿中,于30℃的电热恒温培养箱内干燥24h,待混合液的溶剂乙醇和水充分挥发,混合液干燥成紫胶树脂与PVA复合膜后将其揭起,制得紫胶树脂与PVA复合膜。(3) Blending film formation: Place the shellac resin emulsion and PVA aqueous solution prepared above in a water bath at 50°C and mix according to the volume ratio (approximately 31:8) when the mass ratio of shellac resin to PVA is 7:3. After stirring for 2 hours, transfer to a rotary evaporator for 1 hour to recover part of the solvent ethanol. Then transfer to room temperature to continue stirring for 24 hours and remove air bubbles on the surface of the mixture. Finally, pour the liquid into a petri dish and heat it with electric heating at 30°C. Dry in a constant-temperature incubator for 24 hours. After the solvents ethanol and water of the mixed solution are fully evaporated, the mixed solution is dried into a shellac resin and PVA composite film and then peeled off to prepare a shellac resin and PVA composite film.

实施例4:PVA在复合膜中的质量分数为40%。Example 4: The mass fraction of PVA in the composite film is 40%.

(1)制备紫胶树脂乳液:将7.5g紫胶树脂加入375mL无水乙醇中,搅拌溶解后,过滤除去醇不溶物,滤液经蠕动泵以5ml/min的速度加入高速剪切(剪切速率为1000r/min)的去离子水中,紫胶树脂滤液与去离子水体积比为2:1,制备成紫胶树脂乳液,备用;(1) Preparation of shellac resin emulsion: Add 7.5g of shellac resin to 375mL of absolute ethanol. After stirring and dissolving, filter to remove alcohol-insoluble matter. The filtrate is added to high-speed shear (shear rate) through a peristaltic pump at a speed of 5ml/min. (1000r/min) in deionized water, the volume ratio of the shellac resin filtrate to the deionized water is 2:1, prepare a shellac resin emulsion for later use;

(2)制备PVA水溶液:将5gPVA溶于90℃的150mL去离子水中,然后冷却至室温,制得PVA水溶液,备用;(2) Prepare PVA aqueous solution: Dissolve 5g PVA in 150 mL deionized water at 90°C, and then cool to room temperature to prepare a PVA aqueous solution for later use;

(3)共混成膜:将上述制备得到的紫胶树脂乳液与PVA水溶液按照紫胶树脂与PVA质量比为3:2时的体积比(约5:2)置于50℃的水浴中混合并搅拌2h,然后转移到室温下继续搅拌24h后,转移至旋转蒸发仪中旋转蒸发1h,以回收部分溶剂乙醇,并去除混合液表面气泡,最后将液体倒入培养皿中,于30℃的电热恒温培养箱内干燥24h,待混合液的溶剂乙醇和水充分挥发,混合液干燥成紫胶树脂与PVA复合膜后将其揭起,制得紫胶树脂与PVA复合膜。(3) Blending film formation: Place the shellac resin emulsion and PVA aqueous solution prepared above in a water bath at 50°C and mix according to the volume ratio (approximately 5:2) when the mass ratio of shellac resin to PVA is 3:2. Stir for 2 hours, then transfer to room temperature and continue stirring for 24 hours, then transfer to a rotary evaporator to rotate and evaporate for 1 hour to recover part of the solvent ethanol and remove bubbles on the surface of the mixed solution. Finally, pour the liquid into a petri dish and heat it with electric heating at 30°C. Dry in a constant-temperature incubator for 24 hours. After the solvents ethanol and water of the mixed solution are fully evaporated, the mixed solution is dried into a shellac resin and PVA composite film and then peeled off to prepare a shellac resin and PVA composite film.

实施例5:PVA在复合膜中的质量分数为50%。Example 5: The mass fraction of PVA in the composite film is 50%.

(1)制备紫胶树脂乳液:将6g紫胶树脂加入300mL无水乙醇中,搅拌溶解后,过滤除去醇不溶物,滤液经蠕动泵以5ml/min的速度加入高速剪切(剪切速率为1000r/min)的去离子水中,紫胶树脂滤液与去离子水体积比为2:1,制备成紫胶树脂乳液,备用;(1) Preparation of shellac resin emulsion: Add 6g of shellac resin to 300mL of absolute ethanol. After stirring and dissolving, filter to remove alcohol-insoluble matter. The filtrate is added to high-speed shear at a speed of 5ml/min through a peristaltic pump (the shear rate is 1000r/min) in deionized water, the volume ratio of the shellac resin filtrate to the deionized water is 2:1, and prepare a shellac resin emulsion for later use;

(2)制备PVA水溶液:将6gPVA溶于90℃的180mL去离子水中,然后冷却至室温,制得PVA水溶液,备用;(2) Prepare PVA aqueous solution: Dissolve 6g PVA in 180 mL deionized water at 90°C, and then cool to room temperature to prepare a PVA aqueous solution for later use;

(3)共混成膜:将上述制备得到的紫胶树脂乳液与PVA水溶液按照紫胶树脂与PVA质量比为1:1时的体积比(约5:3)置于50℃的水浴中混合并搅拌2h后,转移至旋转蒸发仪中旋转蒸发1h,以回收部分溶剂乙醇,然后转移到室温下继续搅拌24h,并去除混合液表面气泡,最后将液体倒入培养皿中,于30℃的电热恒温培养箱内干燥24h,待混合液的溶剂乙醇和水充分挥发,混合液干燥成紫胶树脂与PVA复合膜后将其揭起,制得紫胶树脂与PVA复合膜。(3) Blending film formation: Place the shellac resin emulsion and PVA aqueous solution prepared above in a water bath at 50°C and mix according to the volume ratio (about 5:3) when the mass ratio of shellac resin to PVA is 1:1. After stirring for 2 hours, transfer to a rotary evaporator for 1 hour to recover part of the solvent ethanol. Then transfer to room temperature to continue stirring for 24 hours and remove air bubbles on the surface of the mixture. Finally, pour the liquid into a petri dish and heat it with electric heating at 30°C. Dry in a constant-temperature incubator for 24 hours. After the solvents ethanol and water of the mixed solution are fully evaporated, the mixed solution is dried into a shellac resin and PVA composite film and then peeled off to prepare a shellac resin and PVA composite film.

试验例1:不同PVA质量分数下复合膜的外观形态Test Example 1: Appearance of composite membranes under different PVA mass fractions

在复合膜制备过程中,为减小紫胶树脂与PVA复合膜的厚度差异,紫胶树脂乳液与PVA水溶液的共混物在浓度相同时,投入培养皿中的液面高度均控制在10±1mm。混合液按照上述制备步骤最终干燥、成膜后,不同PVA质量分数下的膜外观形态如图1所示,图1中(a)、(b)、(c)、(d)、(e)、(f)、(g)的PVA质量分数分别为0%、10%、20%、30%、40%、50%、100%,图中黑色是背景色。从图1可以看出,随着PVA含量的增加,复合膜的颜色在逐渐变浅,这是由于PVA成膜后的无色透明性所致;同时,随着PVA含量的增加,紫胶树脂成膜后的均匀性随之提高,但会有少量紫胶树脂析出而存在局部聚集,表现为斑点状,说明以水为介质将紫胶树脂膜与PVA共混成膜时,二者不会完全混合均匀,这也是二者的亲水性差异所致。During the preparation process of the composite membrane, in order to reduce the thickness difference between the shellac resin and the PVA composite membrane, when the blends of the shellac resin emulsion and the PVA aqueous solution have the same concentration, the liquid level height put into the petri dish is controlled at 10± 1mm. After the mixture is finally dried and formed into a film according to the above preparation steps, the appearance of the film under different PVA mass fractions is shown in Figure 1. In Figure 1 (a), (b), (c), (d), (e) The PVA mass fractions of (f) and (g) are 0%, 10%, 20%, 30%, 40%, 50%, and 100% respectively. Black is the background color in the figure. It can be seen from Figure 1 that as the PVA content increases, the color of the composite film gradually becomes lighter, which is due to the colorless transparency of PVA after film formation; at the same time, as the PVA content increases, the color of the shellac resin The uniformity after film formation is improved, but a small amount of shellac resin will precipitate and cause local aggregation, which appears as spots, indicating that when water is used as the medium to blend the shellac resin film and PVA to form a film, the two will not be completely Mix evenly, which is also due to the difference in hydrophilicity between the two.

另外,经过对复合膜成品进行拉伸后发现,复合膜的韧性也随着PVA含量的增加而增大,相应其拉伸强度、断裂伸长率也随之提高。In addition, after stretching the finished composite film, it was found that the toughness of the composite film also increased with the increase in PVA content, and accordingly its tensile strength and elongation at break also increased.

试验例2:不同PVA质量分数下复合膜的水静滴接触角测定Test Example 2: Measurement of water droplet contact angle of composite films under different PVA mass fractions

将不同PVA质量分数的复合膜置于接触角仪载玻片上,测定各膜与去离子水的静滴接触角,测试结果如图2所示,图2中(a)、(b)、(c)、(d)、(e)的PVA质量分数分别为10%、20%、30%、40%、50%。从图2可以看出,随着PVA含量的增加,接触角在不断减小,PVA含量为50%时接触角最小,为16.87°,此时复合膜的亲水性最佳,润湿性最好。表明PVA的加入,使得紫胶树脂膜的亲水性增加了,且随着PVA加入量的增加,复合膜的亲水性正比例增加。The composite membranes with different PVA mass fractions were placed on the glass slide of the contact angle meter, and the sessile contact angle between each membrane and deionized water was measured. The test results are shown in Figure 2, (a), (b), ( The PVA mass fractions of c), (d), and (e) are 10%, 20%, 30%, 40%, and 50% respectively. It can be seen from Figure 2 that as the PVA content increases, the contact angle continues to decrease. When the PVA content is 50%, the contact angle is the smallest at 16.87°. At this time, the composite membrane has the best hydrophilicity and the best wettability. good. It shows that the addition of PVA increases the hydrophilicity of the shellac resin membrane, and as the amount of PVA added increases, the hydrophilicity of the composite membrane increases in proportion.

试验例3:不同PVA质量分数下复合膜的吸湿等温线测定Test Example 3: Determination of moisture absorption isotherms of composite films under different PVA mass fractions

将制得不同PVA质量分数的复合膜样品置于恒定温度下、可控湿度的环境中一定时间,让样品吸收足够的水汽,直至达到平衡,然后将样品置放入干燥箱,设定箱内温度为70℃,干燥约3h,直到测定样品干重恒定为止,得到样品干重w0The composite film samples prepared with different PVA mass fractions are placed in an environment with constant temperature and controlled humidity for a certain period of time, allowing the samples to absorb enough water vapor until equilibrium is reached, and then the samples are placed in a drying box and set in the box. The temperature is 70°C and dried for about 3 hours until the dry weight of the measured sample is constant, and the dry weight w 0 of the sample is obtained.

将上述烘干之后的样品分别放入干燥器中,每种干燥器装有不同种类的饱和溶液,每种饱和溶液可提供特定的相对湿度;每份样品均于干燥器放置10天,直到获得恒定的质量为止,记为湿重w1The above dried samples were placed into desiccators respectively. Each desiccator was filled with different types of saturated solutions. Each saturated solution can provide a specific relative humidity; each sample was placed in the desiccator for 10 days until the obtained Until the mass is constant, it is recorded as wet weight w 1 .

干燥器内的饱和溶液种类分别为:①氯化镁饱和溶液,其相对湿度为32.8%,即aw=0.328;②重铬酸钠饱和溶液,其相对湿度为54.4%,即aw=0.544;③氯化钠饱和溶液,其相对湿度为75.3%,即aw=0.753;④氯化钾饱和溶液,其相对湿度为84.3%,即aw=0.843;⑤硝酸钾饱和溶液,其相对湿度为93.7%,即aw=0.937;⑥蒸馏水,其相对湿度为100.0%,即aw=1.00。The types of saturated solutions in the dryer are: ① Magnesium chloride saturated solution, its relative humidity is 32.8%, that is, a w = 0.328; ② Sodium dichromate saturated solution, its relative humidity is 54.4%, that is, a w = 0.544; ③ The relative humidity of a saturated solution of sodium chloride is 75.3%, that is, a w = 0.753; ④ The relative humidity of a saturated solution of potassium chloride is 84.3%, that is, a w = 0.843; ⑤ The relative humidity of a saturated solution of potassium nitrate is 93.7 %, that is, a w = 0.937; ⑥ Distilled water, its relative humidity is 100.0%, that is, a w = 1.00.

每个复合膜样品在每种相对湿度条件下测定3次,取平均值。记录下每种相对湿度条件下的复合膜恒重,并用式(1)来计算含水量ω。Each composite film sample was measured three times under each relative humidity condition and the average value was taken. Record the constant weight of the composite film under each relative humidity condition, and use formula (1) to calculate the moisture content ω.

根据不同湿度条件下的ω值绘制膜的吸湿等温线,得到不同PVA质量分数下复合膜的吸湿等温线如图3所示。从图3可以看出,不含PVA时的纯紫胶树脂膜其吸湿性最差,其吸湿性随湿度的增加其吸水率呈下降趋势;而PVA含量为10%-50%的复合膜随湿度的增加其吸收率呈上升趋势,且在湿度为100%时表现出最强的吸水性,而且PVA含量为50%的复合膜吸水性最优,这一特性为复合膜在人造皮肤材料领域提供了可能性。The moisture absorption isotherm of the film is drawn according to the ω value under different humidity conditions, and the moisture absorption isotherm of the composite film under different PVA mass fractions is obtained, as shown in Figure 3. As can be seen from Figure 3, the pure shellac resin film without PVA has the worst hygroscopicity, and its hygroscopicity shows a downward trend as the humidity increases; while the composite film with a PVA content of 10%-50% decreases as the humidity increases. The absorption rate shows an upward trend with the increase of humidity, and shows the strongest water absorption when the humidity is 100%, and the composite film with a PVA content of 50% has the best water absorption. This characteristic makes the composite film useful in the field of artificial skin materials. Possibilities are provided.

综上所述,紫胶树脂与PVA可以通过水相物理共混法进行共混成膜,PVA的加入提高了紫胶树脂膜的致密性,且随着PVA含量的增加,复合膜的致密性、拉伸强度、断裂伸长率也随之提高,二者发生化学反应的程度较低,紫胶树脂与PVA具有一定的物理相容性。In summary, shellac resin and PVA can be blended to form a film through aqueous physical blending. The addition of PVA improves the density of the shellac resin film, and as the PVA content increases, the density and density of the composite film decrease. The tensile strength and elongation at break also increase, and the degree of chemical reaction between the two is relatively low. Shellac resin and PVA have certain physical compatibility.

而且,随着PVA含量的增加,复合膜的接触角不断减小,复合膜吸湿性不断增强,进一步印证了复合膜具有较好的亲水性,且二者的复合具有较大程度的物理共混,紫胶树脂在其溶液中较稳定。Moreover, as the PVA content increases, the contact angle of the composite film continues to decrease, and the hygroscopicity of the composite film continues to increase, which further confirms that the composite film has better hydrophilicity, and the combination of the two has a greater degree of physical commonality. Mixed, shellac resin is relatively stable in its solution.

以上通过具体的和优选的实施例详细的描述了本发明,但本领域技术人员应该明白,本发明并不局限于以上所述实施例,凡在本发明的精神和原则之内,所做的任何修改、等同替换等,均应包含在本发明的保护范围之内。The present invention has been described in detail through specific and preferred embodiments. However, those skilled in the art should understand that the present invention is not limited to the above-described embodiments. Anything within the spirit and principles of the present invention can be made. Any modifications, equivalent substitutions, etc. shall be included in the protection scope of the present invention.

Claims (6)

1.一种紫胶树脂与PVA复合膜的制备方法,其特征在于,包括如下步骤:1. A method for preparing a shellac resin and PVA composite film, which is characterized in that it includes the following steps: (1)制备紫胶树脂乳液:将紫胶树脂在无水乙醇中溶解,过滤,除去醇不溶物,滤液以5mL/min的速度加入高速剪切的去离子水中,制备成紫胶树脂乳液,备用;(1) Preparation of shellac resin emulsion: Dissolve shellac resin in absolute ethanol, filter, and remove alcohol-insoluble matter. The filtrate is added to high-speed sheared deionized water at a speed of 5 mL/min to prepare shellac resin emulsion. spare; (2)制备PVA水溶液:将PVA溶于90℃的去离子水中,然后冷却至室温,制得PVA水溶液,备用;(2) Prepare PVA aqueous solution: Dissolve PVA in deionized water at 90°C, and then cool to room temperature to prepare a PVA aqueous solution for later use; (3)共混成膜:将上述制备得到的紫胶树脂乳液与PVA水溶液于50℃的水浴中混合并搅拌2h,然后转移至旋转蒸发仪中旋转蒸发1h,以回收部分溶剂乙醇,旋蒸后将混合液转移到室温下继续搅拌24h,并去除混合液表面气泡,最后将液体倒入培养皿中,于30℃的电热恒温培养箱内干燥24h,待混合液的溶剂乙醇和水充分挥发,混合液干燥成紫胶树脂与PVA复合膜后将其揭起,制得紫胶树脂与PVA复合膜。(3) Blending film formation: Mix the shellac resin emulsion and PVA aqueous solution prepared above in a water bath at 50°C and stir for 2 hours, and then transfer to a rotary evaporator to rotary evaporate for 1 hour to recover part of the solvent ethanol. After rotary evaporation Transfer the mixture to room temperature and continue stirring for 24 hours, and remove bubbles on the surface of the mixture. Finally, pour the liquid into a petri dish and dry it in an electric constant-temperature incubator at 30°C for 24 hours until the solvents of the mixture, ethanol and water, are fully evaporated. The mixed liquid is dried into a shellac resin and PVA composite film and then lifted up to obtain a shellac resin and PVA composite film. 2.根据权利要求1所述的一种紫胶树脂与PVA复合膜的制备方法,其特征在于,步骤(1)中紫胶树脂与无水乙醇的质量比为5:194.1。2. A method for preparing a shellac resin and PVA composite film according to claim 1, characterized in that the mass ratio of shellac resin and absolute ethanol in step (1) is 5:194.1. 3.根据权利要求1所述的一种紫胶树脂与PVA复合膜的制备方法,其特征在于,步骤(1)中高速剪切的剪切速率>1000r/min。3. A method for preparing a shellac resin and PVA composite film according to claim 1, characterized in that the shear rate of high-speed shearing in step (1) is >1000 r/min. 4.根据权利要求1所述的一种紫胶树脂与PVA复合膜的制备方法,其特征在于,步骤(1)中紫胶树脂滤液与去离子水的体积比为2:1。4. A method for preparing a shellac resin and PVA composite membrane according to claim 1, wherein the volume ratio of the shellac resin filtrate and deionized water in step (1) is 2:1. 5.根据权利要求1所述的一种紫胶树脂与PVA复合膜的制备方法,其特征在于,步骤(2)中PVA与去离子水的质量比为1:30。5. A method for preparing a shellac resin and PVA composite membrane according to claim 1, characterized in that the mass ratio of PVA to deionized water in step (2) is 1:30. 6.根据权利要求1所述的一种紫胶树脂与PVA复合膜的制备方法,其特征在于,步骤(3)中PVA在复合膜中的质量分数控制为50%。6. A method for preparing a shellac resin and PVA composite film according to claim 1, characterized in that in step (3), the mass fraction of PVA in the composite film is controlled to 50%.
CN202311761428.3A 2023-12-20 2023-12-20 A kind of preparation method of shellac resin and PVA composite film Pending CN117487223A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202311761428.3A CN117487223A (en) 2023-12-20 2023-12-20 A kind of preparation method of shellac resin and PVA composite film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202311761428.3A CN117487223A (en) 2023-12-20 2023-12-20 A kind of preparation method of shellac resin and PVA composite film

Publications (1)

Publication Number Publication Date
CN117487223A true CN117487223A (en) 2024-02-02

Family

ID=89669328

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202311761428.3A Pending CN117487223A (en) 2023-12-20 2023-12-20 A kind of preparation method of shellac resin and PVA composite film

Country Status (1)

Country Link
CN (1) CN117487223A (en)

Similar Documents

Publication Publication Date Title
CN106390765B (en) A kind of doping covalent organic framework material prior-alcohol-permeacomposite composite membrane and preparation method
CN101212036A (en) Microporous polymer isolating film for Li-ion battery and method for producing the same
CN102532572B (en) Preparation method of quaternized chitosan anion hybrid membrane doped with positive polystyrene latex
CN117487223A (en) A kind of preparation method of shellac resin and PVA composite film
CN104525000A (en) Preparation method of high-selectivity polyvinyl alcohol nanofiltration membrane
CN116041773A (en) Micro-nano-scale strong three-dimensional interpenetrating network polyvinylidene fluoride hydrophobic membrane and preparation method thereof
CN113150625B (en) PVOH emulsion for PE coating film and preparation method thereof
CN102908915B (en) Preparation method of diffusion and dialysis membrane for alkali recovery
Luo et al. Modulating the internal porosity of organogel electrolyte via pore-forming agent for low temperature resistant and flexible quasi-solid supercapacitors
CN111234253A (en) Preparation method of nano metal organic framework material
CN101579538B (en) Preparation method of silk fibroin/nanometer SiO2 blend film
CN1792420A (en) Porous film made of polyunsymfluoroethylene, and its prepn. method
CN110818931A (en) Blending dehumidification film and preparation method thereof
CN108376791B (en) A kind of organic-inorganic composite proton exchange membrane containing double proton conductor and preparation method thereof
RU2529187C1 (en) Proton-conducting composite polymer material
CN107151339B (en) Method for constructing composite anionic membrane by introducing binuclear morpholine ionic liquid into pyridine functionalized polyvinyl alcohol
CN113174138B (en) A kind of artificial skin film containing lamellar liquid crystal and its preparation method and application
CN118930912A (en) A method for preparing a sodium alginate hydrogel film containing nitrogen-doped carbon dots
CN105013331B (en) Method for preparing PDMS/PVDF blend pervaporation membrane by using membrane casting solution
JPH0424087B2 (en)
CN116062742A (en) Preparation method of metal ion crosslinked nano film
CN109173745B (en) A kind of hollow fiber ultrafiltration membrane and preparation method thereof
CN113372576A (en) Polyacid-polyaniline-glycerol-polyvinyl alcohol composite gel and preparation method thereof
CN1055875C (en) Hydrophilic osmotic evaporating and separating membrane and its preparing method
RU2845771C1 (en) Method of producing an ion-conducting membrane based on polyvinyl alcohol cross-linked with 2,5-diformylfuran

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination