CN111499999B - A kind of polyvinyl alcohol sponge with high elongation rate and preparation method thereof - Google Patents
A kind of polyvinyl alcohol sponge with high elongation rate and preparation method thereof Download PDFInfo
- Publication number
- CN111499999B CN111499999B CN202010491547.1A CN202010491547A CN111499999B CN 111499999 B CN111499999 B CN 111499999B CN 202010491547 A CN202010491547 A CN 202010491547A CN 111499999 B CN111499999 B CN 111499999B
- Authority
- CN
- China
- Prior art keywords
- polyvinyl alcohol
- solution
- sponge
- high elongation
- elongation rate
- 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.)
- Active
Links
- 239000004372 Polyvinyl alcohol Substances 0.000 title claims abstract description 126
- 229920002451 polyvinyl alcohol Polymers 0.000 title claims abstract description 126
- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 238000003756 stirring Methods 0.000 claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000006243 chemical reaction Methods 0.000 claims abstract description 25
- 239000008367 deionised water Substances 0.000 claims abstract description 20
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 20
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 17
- 239000004088 foaming agent Substances 0.000 claims abstract description 16
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims abstract description 11
- 150000002148 esters Chemical class 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims abstract description 10
- 229920002678 cellulose Polymers 0.000 claims abstract description 9
- 239000001913 cellulose Substances 0.000 claims abstract description 9
- 230000008014 freezing Effects 0.000 claims abstract description 5
- 238000007710 freezing Methods 0.000 claims abstract description 5
- 238000004090 dissolution Methods 0.000 claims abstract description 3
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical group COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 claims description 21
- 229920002749 Bacterial cellulose Polymers 0.000 claims description 19
- 239000005016 bacterial cellulose Substances 0.000 claims description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 18
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical group CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 15
- 229910021389 graphene Inorganic materials 0.000 claims description 8
- 238000003760 magnetic stirring Methods 0.000 claims description 7
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 239000004020 conductor Substances 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 3
- 239000006230 acetylene black Substances 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 239000002041 carbon nanotube Substances 0.000 claims description 3
- 229910021393 carbon nanotube Inorganic materials 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052737 gold Inorganic materials 0.000 claims description 3
- 239000010931 gold Substances 0.000 claims description 3
- 229910002804 graphite Inorganic materials 0.000 claims description 3
- 239000010439 graphite Substances 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims description 3
- 229910052709 silver Inorganic materials 0.000 claims description 3
- 239000004332 silver Substances 0.000 claims description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 6
- 238000005187 foaming Methods 0.000 abstract description 4
- 238000010257 thawing Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 24
- 239000011148 porous material Substances 0.000 description 22
- 229910000019 calcium carbonate Inorganic materials 0.000 description 12
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 8
- 229920002554 vinyl polymer Polymers 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 4
- 229920002472 Starch Polymers 0.000 description 3
- 238000004132 cross linking Methods 0.000 description 3
- 239000008107 starch Substances 0.000 description 3
- 235000019698 starch Nutrition 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- XCCHQGIGHCRZOS-KBKZQPOHSA-N (4as,5as,6s,12ar)-1,6,10,11,12a-pentahydroxy-6-methyl-3,12-dioxo-4,4a,5,5a-tetrahydrotetracene-2-carboxamide Chemical compound C1=CC=C2[C@@](C)(O)[C@@H](C[C@@H]3[C@](C(O)=C(C(N)=O)C(=O)C3)(O)C3=O)C3=C(O)C2=C1O XCCHQGIGHCRZOS-KBKZQPOHSA-N 0.000 description 1
- 101100221122 Caenorhabditis elegans cmt-1 gene Proteins 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- DHKHKXVYLBGOIT-UHFFFAOYSA-N acetaldehyde Diethyl Acetal Natural products CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 description 1
- 125000002777 acetyl group Chemical class [H]C([H])([H])C(*)=O 0.000 description 1
- 125000003158 alcohol group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 231100000206 health hazard Toxicity 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002071 nanotube Substances 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
- C08J9/14—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
- C08J9/141—Hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/28—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2201/00—Foams characterised by the foaming process
- C08J2201/04—Foams characterised by the foaming process characterised by the elimination of a liquid or solid component, e.g. precipitation, leaching out, evaporation
- C08J2201/048—Elimination of a frozen liquid phase
- C08J2201/0484—Elimination of a frozen liquid phase the liquid phase being aqueous
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/14—Saturated hydrocarbons, e.g. butane; Unspecified hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2205/00—Foams characterised by their properties
- C08J2205/04—Foams characterised by their properties characterised by the foam pores
- C08J2205/044—Micropores, i.e. average diameter being between 0,1 micrometer and 0,1 millimeter
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2329/00—Characterised 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
- C08J2329/02—Homopolymers or copolymers of unsaturated alcohols
- C08J2329/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2401/00—Characterised by the use of cellulose, modified cellulose or cellulose derivatives
- C08J2401/02—Cellulose; Modified cellulose
- C08J2401/04—Oxycellulose; Hydrocellulose
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/24—Acids; Salts thereof
- C08K3/26—Carbonates; Bicarbonates
- C08K2003/265—Calcium, strontium or barium carbonate
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/001—Conductive additives
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
- C08K3/042—Graphene or derivatives, e.g. graphene oxides
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
本发明公开了一种具有高拉伸率的聚乙烯醇海绵及其制备方法。该方法包括:将聚乙烯醇、纤维素、碳酸盐与去离子水混合后,封闭条件下搅拌至溶解完全,得到均一的聚乙烯醇溶液;将乳化剂和酯类的混合物加入聚乙烯醇溶液中,搅拌至反应完全,得到白色粘稠状溶液;在白色粘稠状溶液中加入发泡剂后,使用强力搅拌器搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;将发泡后溶液倒入模具中,进行冻融后得到具有高拉伸率的聚乙烯醇海绵。与现有聚乙烯醇海绵制作过程相比,本方法使用的冻融法具有易控制、环保性好,资源浪费少,避免了甲醛对人类健康的危害等优点。
The invention discloses a polyvinyl alcohol sponge with high elongation rate and a preparation method thereof. The method comprises: after mixing polyvinyl alcohol, cellulose, carbonate and deionized water, stirring under closed conditions until the dissolution is complete, to obtain a homogeneous polyvinyl alcohol solution; adding the mixture of emulsifier and ester to the polyvinyl alcohol In the solution, stir until the reaction is complete to obtain a white viscous solution; after adding a foaming agent to the white viscous solution, use a strong stirrer to stir until bubbles of uniform size are generated in the solution to obtain a foamed solution; After foaming, the solution is poured into a mold, and after freezing and thawing, a polyvinyl alcohol sponge with high elongation rate is obtained. Compared with the existing production process of polyvinyl alcohol sponge, the freeze-thaw method used in this method has the advantages of easy control, good environmental protection, less waste of resources, and avoiding the harm of formaldehyde to human health.
Description
技术领域technical field
本发明属于高分子材料领域,具体是一种具有高拉伸率的聚乙烯醇海绵及其制备方法。The invention belongs to the field of polymer materials, in particular to a polyvinyl alcohol sponge with high elongation rate and a preparation method thereof.
背景技术Background technique
聚乙烯醇(Polyvinyl Alcohol,PVA)海绵由众多高分子链交联的网孔状结构构成。聚乙烯醇具有很强的亲水性,因此其可以吸附并储存大量的水分,且在吸水后保持一定的机械强度。此外,聚乙烯醇是高分子材料,重量轻,将其做成多孔海绵结构,还可应用于隔热和隔音等领域。Polyvinyl Alcohol (PVA) sponge is composed of a network structure cross-linked by numerous polymer chains. Polyvinyl alcohol has strong hydrophilicity, so it can absorb and store a large amount of water, and maintain a certain mechanical strength after absorbing water. In addition, polyvinyl alcohol is a polymer material with light weight. It can be made into a porous sponge structure and can also be used in fields such as heat insulation and sound insulation.
现有的聚乙烯醇海绵主要是聚乙烯醇缩甲醛海绵。在资源和环保方面,聚乙烯醇缩甲醛海绵的制备一般使用淀粉作辅助发泡剂,待海绵固化成型后,再将多余的淀粉洗掉。这种制备方法需要消耗大量的水,导致资源的浪费和环境的污染。在海绵力学性能方面,若海绵中的淀粉未能完全洗掉,则海绵在使用过程中容易被腐蚀。此外,在制备过程中,反应条件难以精确控制。若升温速度过快,则缩醛度过高,会导致海绵结块、抱团,形成紧密物料,网孔状结构难以良好地形成,使得反应物难以再继续相互作用。这样得到的聚乙烯醇缩甲醛海绵的拉伸性能较差,拉伸率一般在200-300%,且海绵结构在反复拉伸过程中容易被破坏。在人身健康方面,上述制备方法使用甲醛,因此产物中不可避免的含有游离态的甲醛,无论对制备实验人员还是产品使用人员,都会造成潜在的健康危害。Existing polyvinyl alcohol sponges are mainly polyvinyl formal sponges. In terms of resources and environmental protection, starch is generally used as an auxiliary foaming agent for the preparation of polyvinyl formal sponge. After the sponge is solidified and formed, the excess starch is washed away. This preparation method needs to consume a large amount of water, resulting in waste of resources and environmental pollution. In terms of the mechanical properties of the sponge, if the starch in the sponge is not completely washed off, the sponge is easily corroded during use. In addition, during the preparation process, the reaction conditions are difficult to precisely control. If the heating rate is too fast, the acetal is too high, which will cause the sponge to agglomerate and clump together to form a tight material, and it is difficult to form a mesh-like structure well, making it difficult for the reactants to continue to interact. The polyvinyl formal sponge thus obtained has poor tensile properties, the elongation rate is generally 200-300%, and the sponge structure is easily damaged during repeated stretching. In terms of human health, the above preparation method uses formaldehyde, so the product inevitably contains free formaldehyde, which will cause potential health hazards to both the preparation experimenter and the product user.
发明内容SUMMARY OF THE INVENTION
针对现有技术的不足,本发明拟解决的技术问题是,提供一种具有高拉伸率的聚乙烯醇海绵及其制备方法。In view of the deficiencies of the prior art, the technical problem to be solved by the present invention is to provide a polyvinyl alcohol sponge with high elongation rate and a preparation method thereof.
本发明解决所述方法技术问题的技术方案是,提供一种具有高拉伸率的聚乙烯醇海绵的制备方法,其特征在于该方法包括如下步骤:The technical solution of the present invention to solve the technical problem of the method is to provide a method for preparing a polyvinyl alcohol sponge with high elongation rate, which is characterized in that the method comprises the following steps:
(1)将聚乙烯醇、纤维素、碳酸盐与去离子水混合后,封闭条件下搅拌至溶解完全,得到均一的聚乙烯醇溶液;(1) after polyvinyl alcohol, cellulose, carbonate are mixed with deionized water, stir to dissolve completely under closed condition, obtain homogeneous polyvinyl alcohol solution;
(2)将乳化剂和酯类的混合物加入步骤1)得到的聚乙烯醇溶液中,搅拌至反应完全,得到白色粘稠状溶液;(2) adding the mixture of emulsifier and esters to the polyvinyl alcohol solution obtained in step 1), stirring until the reaction is complete, to obtain a white viscous solution;
(3)在步骤2)得到的白色粘稠状溶液中加入发泡剂后,使用强力搅拌器搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) after adding a foaming agent in the white viscous solution obtained in step 2), use a strong stirrer to stir until bubbles of uniform size are generated in the solution, and obtain a solution after foaming;
(4)将步骤3)得到的发泡后溶液倒入模具中,进行冻融后得到具有高拉伸率的聚乙烯醇海绵。(4) Pour the foamed solution obtained in step 3) into a mold, and freeze and thaw to obtain a polyvinyl alcohol sponge with a high elongation rate.
步骤1)中,反应温度为80-100℃;所述纤维素为细菌纤维素;聚乙烯醇、纤维素、碳酸钙与去离子水的质量比为42-46:2-4:8-12:240-260;聚乙烯醇的分子量为135000-300000。In step 1), the reaction temperature is 80-100 ° C; the cellulose is bacterial cellulose; the mass ratio of polyvinyl alcohol, cellulose, calcium carbonate and deionized water is 42-46:2-4:8-12 : 240-260; the molecular weight of polyvinyl alcohol is 135000-300000.
步骤2)中,反应温度为70-80℃;所述乳化剂采用OP-10;所述酯类为碳酸二甲酯;乳化剂与酯类的体积比为2-4:4-5,且混合物的质量是聚乙烯醇溶液和混合物的质量之和的16-17%;搅拌使用磁力搅拌或安装有螺旋桨的强力搅拌器进行搅拌。In step 2), the reaction temperature is 70-80 ° C; the emulsifier is OP-10; the ester is dimethyl carbonate; the volume ratio of the emulsifier to the ester is 2-4:4-5, and The mass of the mixture is 16-17% of the sum of the mass of the polyvinyl alcohol solution and the mixture; stirring is performed using a magnetic stirrer or a powerful stirrer equipped with a propeller.
步骤3)中,反应温度为30-40℃,搅拌转速为1500-2000r/min。所述发泡剂为正戊烷;发泡剂的质量为白色粘稠状溶液和发泡剂的质量之和的5-6%。In step 3), the reaction temperature is 30-40° C., and the stirring speed is 1500-2000 r/min. The foaming agent is n-pentane; the mass of the foaming agent is 5-6% of the sum of the mass of the white viscous solution and the foaming agent.
步骤4)中,冻融是将具有发泡后溶液的模具在-40℃至-50℃的冷冻干燥机中冷冻4-12h后,再在室温下融化2-3h。In step 4), freeze-thaw is to freeze the mold with the foamed solution in a freeze dryer at -40°C to -50°C for 4-12 hours, and then thaw at room temperature for 2-3 hours.
在步骤1)的原料中加入导电物质,可制得具有高拉伸率的聚乙烯醇导电海绵;所述导电物质为铜、铝、金、银、镍、石墨、乙炔黑、石墨烯、碳纳米管或MXene中的至少一种。A conductive material is added to the raw material in step 1) to obtain a polyvinyl alcohol conductive sponge with high elongation; the conductive material is copper, aluminum, gold, silver, nickel, graphite, acetylene black, graphene, carbon At least one of nanotubes or MXenes.
本发明解决所述聚乙烯醇海绵技术问题的技术方案是,提供一种所述的制备方法得到的具有高拉伸率的聚乙烯醇海绵。The technical solution of the present invention to solve the technical problem of the polyvinyl alcohol sponge is to provide a polyvinyl alcohol sponge with high elongation obtained by the preparation method.
与现有技术相比,本发明有益效果在于:Compared with the prior art, the beneficial effects of the present invention are:
(1)与现有聚乙烯醇海绵制作过程相比,本方法使用的冻融法具有易控制、环保性好,资源浪费少,避免了甲醛对人类健康的危害等优点。(1) Compared with the existing polyvinyl alcohol sponge production process, the freeze-thaw method used in this method has the advantages of easy control, good environmental protection, less waste of resources, and avoiding the harm of formaldehyde to human health.
(2)与现有聚乙烯醇海绵制作过程相比,本方法制备得到的海绵可控性好,力学拉伸性能可大于300%,且聚乙烯醇海绵的拉伸率、气孔大小以及电阻率都可以通过改变制备参数进行调节。例如,在配方中通过控制加入了细菌纤维素含量,可以调整海绵的拉伸率;通过控制去离子水的含量可以对海绵气孔进行调整,得到不同持水能力的海绵;在海绵中加入不同量的导电物质可以得到不同导电率的柔性电极。(2) Compared with the existing production process of polyvinyl alcohol sponge, the sponge prepared by this method has good controllability, mechanical tensile properties can be greater than 300%, and the elongation rate, pore size and resistivity of the polyvinyl alcohol sponge All can be adjusted by changing the preparation parameters. For example, by controlling the content of bacterial cellulose in the formula, the stretch rate of the sponge can be adjusted; by controlling the content of deionized water, the pores of the sponge can be adjusted to obtain sponges with different water holding capacities; adding different amounts to the sponge flexible electrodes with different conductivity can be obtained.
附图说明Description of drawings
图1为本发明的聚乙烯醇海绵的结构示意图;Fig. 1 is the structural representation of polyvinyl alcohol sponge of the present invention;
图2为本发明实施例1的电镜图;Fig. 2 is the electron microscope picture of the embodiment of the present invention 1;
图3为本发明实施例3的应力-应变图;图中,1为气孔;2为聚乙烯醇骨架。Figure 3 is a stress-strain diagram of Example 3 of the present invention; in the figure, 1 is a pore; 2 is a polyvinyl alcohol skeleton.
具体实施方式Detailed ways
下面给出本发明的具体实施例。具体实施例仅用于进一步详细说明本发明,不限制本申请权利要求的保护范围。Specific embodiments of the present invention are given below. The specific embodiments are only used to further illustrate the present invention in detail, and do not limit the protection scope of the claims of the present application.
本发明提供了一种具有高拉伸率的聚乙烯醇海绵的制备方法(简称方法),其特征在于该方法包括以下步骤:The invention provides a preparation method (method for short) of a polyvinyl alcohol sponge with high elongation rate, which is characterized in that the method comprises the following steps:
(1)将聚乙烯醇(PVA)、纤维素、碳酸盐与去离子水混合后,在封闭条件下在80-100℃温度中磁力搅拌1-2h至溶解完全,得到均一的乳白色聚乙烯醇溶液;(1) After mixing polyvinyl alcohol (PVA), cellulose, carbonate and deionized water, magnetic stirring at 80-100°C for 1-2h under closed conditions to complete dissolution to obtain a uniform milky white polyethylene alcohol solution;
步骤1)中,封闭条件是采用锡纸或保鲜薄膜封闭容器防止水分蒸发。In step 1), the sealing condition is to use tin foil or fresh-keeping film to seal the container to prevent moisture from evaporating.
步骤1)中,所述碳酸盐包括碳酸钙、碳酸钾或碳酸钠等(优选碳酸钙)。In step 1), the carbonate includes calcium carbonate, potassium carbonate or sodium carbonate (preferably calcium carbonate).
步骤1)中,所述纤维素为细菌纤维素(BC);聚乙烯醇、细菌纤维素、碳酸盐与去离子水的质量比为42-46:2-4:8-12:240-260(优选45:6:10:250);聚乙烯醇的分子量为135000-300000;BC可以增加聚乙烯醇海绵的持水性能和抗张性能;碳酸盐可以促进聚乙烯醇与碳酸二甲酯的反应速率。In step 1), the cellulose is bacterial cellulose (BC); the mass ratio of polyvinyl alcohol, bacterial cellulose, carbonate and deionized water is 42-46:2-4:8-12:240- 260 (preferably 45:6:10:250); the molecular weight of polyvinyl alcohol is 135000-300000; BC can increase the water retention and tensile properties of polyvinyl alcohol sponge; carbonate can promote polyvinyl alcohol and dimethyl carbonate The reaction rate of the ester.
(2)将步骤1)得到的聚乙烯醇溶液降温至70-80℃(优选70℃、76℃),将乳化剂和酯类的混合物一次性加入聚乙烯醇溶液中,磁力搅拌2-3h(优选2h)至反应完全,得到白色粘稠状溶液;(2) Cool the polyvinyl alcohol solution obtained in step 1) to 70-80°C (preferably 70°C, 76°C), add the mixture of emulsifier and esters to the polyvinyl alcohol solution at one time, and stir magnetically for 2-3h (preferably 2h) to complete the reaction to obtain a white viscous solution;
步骤2)中,所述乳化剂采用OP-10,用于加大聚乙烯醇与碳酸二甲酯的融合程度;所述酯类为碳酸二甲酯(DMC);In step 2), described emulsifier adopts OP-10, is used for increasing the fusion degree of polyvinyl alcohol and dimethyl carbonate; Described ester is dimethyl carbonate (DMC);
步骤2)中,乳化剂与碳酸二甲酯的体积比为2-4:4-5(优选3:5),且混合物的质量是聚乙烯醇溶液和混合物的质量之和的16-17%;碳酸二甲酯与聚乙烯醇进行缩聚反应,为聚乙烯醇海绵搭建骨架。In step 2), the volume ratio of emulsifier and dimethyl carbonate is 2-4:4-5 (preferably 3:5), and the mass of the mixture is 16-17% of the sum of the mass of the polyvinyl alcohol solution and the mixture ; The polycondensation reaction of dimethyl carbonate and polyvinyl alcohol is carried out to build a skeleton for the polyvinyl alcohol sponge.
步骤2)中,聚乙烯醇与碳酸二甲酯的反应温度过高,碳酸二甲酯挥发,导致剩余聚乙烯醇过多;温度过低,反应不充分。碳酸二甲酯与聚乙烯醇反应过程中更优选地是使用安装有螺旋桨的强力搅拌器进行搅拌,避免因搅拌不完全导致的反应不充分。In step 2), the reaction temperature of polyvinyl alcohol and dimethyl carbonate is too high, and the dimethyl carbonate volatilizes, resulting in too much remaining polyvinyl alcohol; the temperature is too low, and the reaction is insufficient. In the reaction process of dimethyl carbonate and polyvinyl alcohol, it is more preferable to use a strong stirrer equipped with a propeller for stirring, so as to avoid insufficient reaction caused by incomplete stirring.
(3)将步骤2)得到的白色粘稠状溶液降温至30-40℃(优选30℃),加入发泡剂后,使用安装有螺旋桨的强力搅拌器快速、剧烈搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution obtained in step 2) is cooled to 30-40°C (preferably 30°C), after adding the foaming agent, use a powerful stirrer equipped with a propeller to quickly and vigorously stir until the solution is uniform in size the bubbles to obtain the foamed solution;
步骤3)中,所述发泡剂为正戊烷;发泡剂的质量为白色粘稠状溶液和发泡剂的质量之和的5-6%,且发泡温度在33-38℃之间。In step 3), the foaming agent is n-pentane; the quality of the foaming agent is 5-6% of the sum of the mass of the white viscous solution and the foaming agent, and the foaming temperature is between 33-38 ° C. between.
步骤3)中,搅拌转速为1500-2000r/min,转速的大小会影响海绵的网孔结构的大小与均匀程度。In step 3), the stirring rotation speed is 1500-2000 r/min, and the size of the rotation speed will affect the size and uniformity of the mesh structure of the sponge.
(4)将步骤3)得到的发泡后溶液倒入模具中,进行2-4次(优选3次)冻融后得到具有高拉伸率的聚乙烯醇海绵。(4) Pour the foamed solution obtained in step 3) into a mold, and freeze and thaw for 2-4 times (preferably 3 times) to obtain a polyvinyl alcohol sponge with a high elongation rate.
冻融的具体过程是将具有发泡后溶液的模具在-40℃至-50℃的冷冻干燥机中冷冻4-12h(优选7h)后,再在室温下融化2-3h(优选2h);冻融的特征是温度容易控制;冷冻是为了使聚乙烯醇与碳酸二甲酯反应生成的碳酸聚乙烯醇脂聚合物发生物理交联;融化是为了检验碳酸聚乙烯醇脂聚合物是否完全发生物理交联;多次冻融是为了保证碳酸聚乙烯醇脂聚合物完全发生物理交联。The specific process of freezing and thawing is to freeze the mold with the foamed solution in a freeze dryer at -40°C to -50°C for 4-12h (preferably 7h), and then thaw it at room temperature for 2-3h (preferably 2h); The characteristic of freezing and thawing is that the temperature is easy to control; freezing is to make the polyvinyl carbonate polymer generated by the reaction of polyvinyl alcohol and dimethyl carbonate physically cross-linked; thawing is to test whether the polyvinyl carbonate polymer has completely occurred. Physical cross-linking; multiple freeze-thaw cycles are to ensure complete physical cross-linking of the polyvinyl carbonate polymer.
优选地,在步骤1)的原料中加入导电物质,最终可制得具有高拉伸率的聚乙烯醇导电泡沫;所述导电物质为铜、铝、金、银、镍、石墨、乙炔黑、石墨烯、碳纳米管(CNT)或MXene中的至少一种;导电物质的加入量与导电率相关。Preferably, a conductive substance is added to the raw material in step 1), and finally a polyvinyl alcohol conductive foam with high elongation can be obtained; the conductive substance is copper, aluminum, gold, silver, nickel, graphite, acetylene black, At least one of graphene, carbon nanotube (CNT) or MXene; the added amount of the conductive substance is related to the conductivity.
本发明同时提供了一种所述制备方法得到的具有高拉伸率的聚乙烯醇海绵。The present invention also provides a polyvinyl alcohol sponge with high elongation obtained by the preparation method.
由图1可以看出,聚乙烯醇与碳酸二甲酯发生酯化反应,然后经过发泡剂发泡产生大量气孔,可以为储存水分提供空间。It can be seen from Figure 1 that polyvinyl alcohol and dimethyl carbonate undergo an esterification reaction, and then a large number of pores are generated by foaming with a foaming agent, which can provide space for storing moisture.
下面的实施例和对比例中,气孔直径采用金相显微镜WYJ-55XA测量得到。拉伸率采用联工万能试验机CMT-1按照标准GB/T 528-2009测试得到,所有样品均裁成5mm×15mm×2mm的哑铃状。电阻率采用晶格JG2511C电阻率四探针测试仪测量得到。In the following examples and comparative examples, the pore diameter was measured by metallographic microscope WYJ-55XA. The elongation rate was measured by Liangong universal testing machine CMT-1 according to the standard GB/T 528-2009, and all samples were cut into dumbbell shapes of 5mm×15mm×2mm. The resistivity was measured with a lattice JG2511C resistivity four-probe tester.
实施例1Example 1
(1)将10g聚乙烯醇(分子量为145000)、0.6g细菌纤维素、3g碳酸钙与100ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的乳白色聚乙烯醇溶液;(1) Place 10g of polyvinyl alcohol (molecular weight 145000), 0.6g of bacterial cellulose, 3g of calcium carbonate and 100ml of deionized water in a beaker, place a stirring bar of appropriate size, then seal it with tin foil, and stir magnetically at 95°C Stir and dissolve in a water bath for 1.5h to obtain a uniform milky white polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为12.64-18.04μm,拉伸率为318%的聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze-thaw is frozen in a freeze dryer at -45°C for 7 hours, and then thawed at room temperature for 2 hours) to obtain a pore diameter of 12.64 -18.04 μm, polyvinyl alcohol sponge with 318% elongation.
由图2可以看出,实施例1制备出的海绵与海绵的结构示意图(图1)一致,含有多孔结构的聚乙烯醇海绵;As can be seen from Figure 2, the sponge prepared in Example 1 is consistent with the structural representation of the sponge (Figure 1), and contains a polyvinyl alcohol sponge with a porous structure;
对比例1Comparative Example 1
(1)将10g聚乙烯醇(分子量为145000)、0g细菌纤维素、3g碳酸钙与100ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的乳白色聚乙烯醇溶液;(1) Place 10g of polyvinyl alcohol (molecular weight 145000), 0g of bacterial cellulose, 3g of calcium carbonate and 100ml of deionized water in a beaker, place a stirring bar of appropriate size, then seal it with tin foil, and magnetically stir the water bath at 95°C Stir and dissolve in the pot for 1.5h to obtain a uniform milky white polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为12.64-18.04μm、拉伸率为180%的聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze-thaw is frozen in a freeze dryer at -45°C for 7 hours, and then thawed at room temperature for 2 hours) to obtain a pore diameter of 12.64 -18.04 μm, 180% elongation polyvinyl alcohol sponge.
对比例2Comparative Example 2
(1)将10g聚乙烯醇(分子量为145000)、0.3g细菌纤维素、3g碳酸钙与100ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的乳白色聚乙烯醇溶液;(1) Place 10g polyvinyl alcohol (molecular weight 145000), 0.3g bacterial cellulose, 3g calcium carbonate and 100ml deionized water in a beaker, place a stirring bar of appropriate size, then seal with tin foil, and stir magnetically at 95°C Stir and dissolve in a water bath for 1.5h to obtain a uniform milky white polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为12.64-18.04μm、拉伸率为260%的聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze-thaw is frozen in a freeze dryer at -45°C for 7 hours, and then thawed at room temperature for 2 hours) to obtain a pore diameter of 12.64 -18.04 μm, 260% elongation polyvinyl alcohol sponge.
对比例3Comparative Example 3
(1)将10g聚乙烯醇(分子量为145000)、0.9g细菌纤维素、3g碳酸钙与100ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的乳白色聚乙烯醇溶液;(1) Put 10g of polyvinyl alcohol (molecular weight 145000), 0.9g of bacterial cellulose, 3g of calcium carbonate and 100ml of deionized water in a beaker, place a stirring bar of appropriate size, then seal it with tin foil, and stir magnetically at 95°C Stir and dissolve in a water bath for 1.5h to obtain a uniform milky white polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为12.64-18.04μm、拉伸率为280%的聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze-thaw is frozen in a freeze dryer at -45°C for 7 hours, and then thawed at room temperature for 2 hours) to obtain a pore diameter of 12.64 -18.04 μm, 280% elongation polyvinyl alcohol sponge.
将实施例1、对比例1、对比例2和对比例3进行比较,可以看出:细菌纤维素的量会影响聚乙烯醇海绵的拉伸率,细菌纤维素含量太低会导致聚乙烯醇海绵的强度不足,进而导致其拉伸率较小;但细菌纤维素含量太高,聚乙烯醇海绵的强度过大,从而降低聚乙烯醇海绵的拉伸率。By comparing Example 1, Comparative Example 1, Comparative Example 2 and Comparative Example 3, it can be seen that: the amount of bacterial cellulose can affect the stretch rate of the polyvinyl alcohol sponge, and the bacterial cellulose content is too low to cause polyvinyl alcohol. The strength of the sponge is insufficient, resulting in a small elongation rate; however, if the bacterial cellulose content is too high, the strength of the polyvinyl alcohol sponge is too large, thereby reducing the elongation rate of the polyvinyl alcohol sponge.
实施例2Example 2
(1)将10g聚乙烯醇(分子量为145000)、0.6g细菌纤维素、3g碳酸钙与110ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的乳白色聚乙烯醇溶液;(1) Place 10g of polyvinyl alcohol (molecular weight 145000), 0.6g of bacterial cellulose, 3g of calcium carbonate and 110ml of deionized water in a beaker, place a stirring bar of appropriate size, then seal it with tin foil, and stir magnetically at 95°C Stir and dissolve in a water bath for 1.5h to obtain a uniform milky white polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为9.97-11.92μm、拉伸率为322%的聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze-thaw in a freeze dryer at -45°C for 7 hours, and then thaw at room temperature for 2 hours) to obtain a pore diameter of 9.97 - 11.92 μm, 322% elongation polyvinyl alcohol sponge.
实施例3Example 3
将10g聚乙烯醇(分子量为145000)、0.6g细菌纤维素、3g碳酸钙与120ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的乳白色聚乙烯醇溶液;Place 10g of polyvinyl alcohol (molecular weight 145000), 0.6g of bacterial cellulose, 3g of calcium carbonate and 120ml of deionized water in a beaker, place a stirring bar of appropriate size, then seal it with tin foil, and place it in a magnetic stirring water bath at 95°C. Stir and dissolve for 1.5h to obtain a uniform milky white polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为8.68-9.17μm、拉伸率为332%的聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze-thaw is frozen in a freeze dryer at -45°C for 7 hours, and then thawed at room temperature for 2 hours) to obtain a pore diameter of 8.68 - 9.17 μm, 332% elongation polyvinyl alcohol sponge.
由图3可以看出,本实施例得到的聚乙烯醇海绵的拉伸性能高于300%。It can be seen from FIG. 3 that the tensile properties of the polyvinyl alcohol sponge obtained in this example are higher than 300%.
将实施例1、实施例2和实施例3进行比较,可以看出:随着去离子水的量的增加,聚乙烯醇海绵气孔的直径逐渐减小。从气孔形成原理可得出:去离子水的量会影响聚乙烯醇溶液的粘稠度,进而会影响体系液体的流动性与气孔的强度,最后会影响海绵气孔的直径。经过多次实验得出:去离子水的量不可以超过一定范围,若太大,气孔壁强度太小,发生塌泡现象;若太小,气孔壁强度太大,导致生成大量的死泡或者气孔不均匀。Comparing Example 1, Example 2 and Example 3, it can be seen that: with the increase of the amount of deionized water, the diameter of the pores of the polyvinyl alcohol sponge gradually decreases. From the formation principle of pores, it can be concluded that the amount of deionized water will affect the viscosity of the polyvinyl alcohol solution, which will then affect the fluidity of the system liquid and the strength of the pores, and finally affect the diameter of the pores of the sponge. After many experiments, it is concluded that the amount of deionized water should not exceed a certain range. If it is too large, the strength of the pore wall will be too small, resulting in collapse of bubbles; The pores are uneven.
实施例4Example 4
(1)将10g聚乙烯醇(分子量为145000)、0.6g细菌纤维素、3g碳酸钙、4ml石墨烯溶液与100ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的聚乙烯醇溶液;(1) After placing 10g polyvinyl alcohol (molecular weight 145000), 0.6g bacterial cellulose, 3g calcium carbonate, 4ml graphene solution and 100ml deionized water in a beaker, place a stirring bar of appropriate size, and then seal it with tin foil, Stir and dissolve in a magnetic stirring water bath at 95°C for 1.5h to obtain a homogeneous polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为12.96-18.75μm、拉伸率为298%、电阻率为2.68x10-4Ω·m的导电聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze and thaw in a freeze-drier at -45°C for 7 hours, and then thaw at room temperature for 2 hours) to obtain a pore diameter of 12.96 -18.75μm, elongation 298%, electrical resistivity 2.68x10 -4 Ω·m conductive polyvinyl alcohol sponge.
实施例5Example 5
(1)将10g聚乙烯醇(分子量为145000)、0.6g细菌纤维素、3g碳酸钙、5ml石墨烯溶液与100ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的聚乙烯醇溶液;(1) After placing 10g polyvinyl alcohol (molecular weight 145000), 0.6g bacterial cellulose, 3g calcium carbonate, 5ml graphene solution and 100ml deionized water in a beaker, place a stirring bar of appropriate size, and then seal it with tin foil, Stir and dissolve in a magnetic stirring water bath at 95°C for 1.5h to obtain a homogeneous polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour the mixed 10ml emulsifier OP-10 and 14ml dimethyl carbonate into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reaction is White and viscous, remove the magnetic stirrer;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(3) the white viscous solution was cooled to 36 ℃, 12ml of foaming agent n-pentane was added, and a strong stirrer was used to stir at a rotating speed of 1500r/min until bubbles of uniform size were generated in the solution, and the foamed solution was obtained;
(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为13.12-18.95μm、拉伸率为241%、电阻率为1.43x10-4Ω·m的导电聚乙烯醇海绵。(4) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze and thaw for 7 hours in a freeze dryer at -45°C, and then thaw at room temperature for 2 hours) to obtain a pore diameter of 13.12 -18.95μm, 241% elongation, 1.43x10 -4 Ω·m electrical resistivity conductive polyvinyl alcohol sponge.
实施例6Example 6
(1)将10g聚乙烯醇(分子量为145000)、0.6g细菌纤维素、3g碳酸钙、6ml石墨烯溶液与100ml去离子水放置于烧杯后,放置适当大小的搅拌子,然后使用锡纸封闭,在95℃磁力搅拌水浴锅中搅拌溶解1.5h,得到均一的聚乙烯醇溶液;(1) After placing 10g polyvinyl alcohol (molecular weight 145000), 0.6g bacterial cellulose, 3g calcium carbonate, 6ml graphene solution and 100ml deionized water in a beaker, place a stirring bar of appropriate size, and then seal it with tin foil, Stir and dissolve in a magnetic stirring water bath at 95°C for 1.5h to obtain a homogeneous polyvinyl alcohol solution;
(2)将聚乙烯醇溶液降温至76℃,将适量混合后的10ml乳化剂OP-10与14ml碳酸二甲酯一次性倒入装有聚乙烯醇溶液的烧杯中,并搅拌2h至溶液反应为白色粘稠状,取出磁力搅拌子;(2) Cool the polyvinyl alcohol solution to 76°C, pour 10ml of emulsifier OP-10 and 14ml of dimethyl carbonate mixed in an appropriate amount into the beaker containing the polyvinyl alcohol solution at one time, and stir for 2h until the solution reacts It is white and viscous, take out the magnetic stirring bar;
(3)将白色粘稠状溶液降温至36℃,加入12ml发泡剂正戊烷,使用强力搅拌机以1500r/min的转速搅拌至溶液中产生大小均匀的气泡,得到发泡后溶液;(4)将发泡后溶液倒入模具中,反复进行3次冻融(冻融为在-45℃的冷冻干燥机中冷冻7h后,再在室温下融化2h)后,得到气孔直径为13.31-19.25μm、拉伸率为226%、电阻率为4.12x10-5Ω·m的导电聚乙烯醇海绵。(3) the white viscous solution is cooled to 36 ℃, 12ml of foaming agent n-pentane is added, and a strong mixer is used to stir at a rotating speed of 1500r/min until bubbles of uniform size are generated in the solution, and the foamed solution is obtained; (4) ) Pour the foamed solution into the mold, and repeat freeze-thaw three times (freeze-thaw in a freeze-drier at -45°C for 7 hours, and then thaw at room temperature for 2 hours) to obtain a pore diameter of 13.31-19.25 A conductive polyvinyl alcohol sponge with μm, elongation rate of 226%, and resistivity of 4.12x10 -5 Ω·m.
将实施例4、实施例5和实施例6进行比较,可以看出:石墨烯的含量会影响导电海绵的导电性,石墨烯的含量越高,电阻率越小;但加入导电物质的同时会影响海绵的孔径与拉伸性能,加入过多的导电物质会使海绵内部的交联键数量减少,从而使其拉伸性能大幅度降低。可见,在制作聚乙烯醇导电海绵时需要综合考虑加入各种物质的含量。By comparing Example 4, Example 5 and Example 6, it can be seen that: the content of graphene can affect the conductivity of the conductive sponge, and the higher the content of graphene, the smaller the resistivity; Affecting the pore size and tensile properties of the sponge, adding too much conductive material will reduce the number of cross-linking bonds inside the sponge, thereby greatly reducing the tensile properties. It can be seen that the content of various substances needs to be comprehensively considered when making the polyvinyl alcohol conductive sponge.
表1Table 1
表1为上述所有实施例和对比例的数据总结。综上所述,与传统的聚乙烯醇海绵相比,使用相同的聚乙烯醇、发泡剂、交联剂用量时,本发明提供的方法制备的聚乙烯醇海绵拉伸率得到提高,制作方法更为简单、环保,且聚乙烯醇海绵的气孔直径大小与拉伸率、电阻率均可根据使用环境进行灵活调整。Table 1 summarizes the data for all of the above examples and comparative examples. To sum up, compared with the traditional polyvinyl alcohol sponge, when the same dosage of polyvinyl alcohol, foaming agent and crosslinking agent is used, the elongation rate of the polyvinyl alcohol sponge prepared by the method provided by the present invention is improved, and the The method is simpler and more environmentally friendly, and the pore diameter, elongation rate and resistivity of the polyvinyl alcohol sponge can be flexibly adjusted according to the use environment.
本发明未述及之处适用于现有技术。What is not described in the present invention applies to the prior art.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010491547.1A CN111499999B (en) | 2020-06-02 | 2020-06-02 | A kind of polyvinyl alcohol sponge with high elongation rate and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010491547.1A CN111499999B (en) | 2020-06-02 | 2020-06-02 | A kind of polyvinyl alcohol sponge with high elongation rate and preparation method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN111499999A CN111499999A (en) | 2020-08-07 |
| CN111499999B true CN111499999B (en) | 2022-06-21 |
Family
ID=71870392
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010491547.1A Active CN111499999B (en) | 2020-06-02 | 2020-06-02 | A kind of polyvinyl alcohol sponge with high elongation rate and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111499999B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115304812B (en) * | 2022-08-22 | 2023-05-09 | 福州大学 | A kind of TAT polypeptide modified MXene/aminated bacterial cellulose electromagnetic shielding composite material and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020114826A1 (en) * | 2001-02-21 | 2002-08-22 | Drury Thomas J. | PVA sponge with low durometer skin silicone |
| CN104830002A (en) * | 2015-04-10 | 2015-08-12 | 徐禄贵 | Polyvinyl alcohol spongy material and production method thereof |
| CN104962096A (en) * | 2015-07-13 | 2015-10-07 | 深圳职业技术学院 | Preparation method of polyvinyl alcohol foamed plastics |
| CN108630462A (en) * | 2018-05-22 | 2018-10-09 | 中南林业科技大学 | Nanofiber-based integrated film ultracapacitor of one kind and preparation method thereof |
-
2020
- 2020-06-02 CN CN202010491547.1A patent/CN111499999B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020114826A1 (en) * | 2001-02-21 | 2002-08-22 | Drury Thomas J. | PVA sponge with low durometer skin silicone |
| CN104830002A (en) * | 2015-04-10 | 2015-08-12 | 徐禄贵 | Polyvinyl alcohol spongy material and production method thereof |
| CN104962096A (en) * | 2015-07-13 | 2015-10-07 | 深圳职业技术学院 | Preparation method of polyvinyl alcohol foamed plastics |
| CN108630462A (en) * | 2018-05-22 | 2018-10-09 | 中南林业科技大学 | Nanofiber-based integrated film ultracapacitor of one kind and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN111499999A (en) | 2020-08-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN113088078B (en) | MXene/polyimide nanofiber aerogel and preparation method and application thereof | |
| CN110746939B (en) | A kind of composite phase change material with PVA as skeleton material and preparation method thereof | |
| CN104167302B (en) | Preparation method for grapheme/melamine resin hollow ball composite material | |
| CN111841457B (en) | A kind of metal ion/zirconium phosphate aerogel and its preparation method and composite phase change energy storage material | |
| CN105176198A (en) | Preparation method and use method of high-concentration silver nano-wire stabilized ink used for storage | |
| CN111584805A (en) | Preparation method of water-based clay mineral/polyvinyl alcohol crosslinked nano coating composite diaphragm | |
| CN101671196B (en) | Preparation method of carbon foam heat insulating material added with potassium hexatitanate whiskers | |
| CN108630462A (en) | Nanofiber-based integrated film ultracapacitor of one kind and preparation method thereof | |
| CN107722332A (en) | The preparation method of polyvinyl alcohol micropore expanded material | |
| CN111499999B (en) | A kind of polyvinyl alcohol sponge with high elongation rate and preparation method thereof | |
| CN109830668A (en) | The method that lithium ion battery silicon-carbon cathode material is prepared using carbon nanotube | |
| CN115850787A (en) | Recyclable aramid nanofiber aerogel, and preparation method and application thereof | |
| CN105489910A (en) | Preparation method of electrolyte flake for thermal battery | |
| CN113150360B (en) | Method for Promoting the Dispersion of Nanofillers by Utilizing the Stretching Effect of Pore Wall of Polymer Foaming Material | |
| CN114773684A (en) | A chemically cross-linked cellulose-based composite foam and its preparation method and application | |
| CN110156000A (en) | A kind of multistage dispersion method of graphene | |
| CN107353426B (en) | A kind of preparation method of polymer opening material and opening material | |
| CN106117741A (en) | A kind of polyethylene composite foam material and preparation method thereof | |
| CN104448303A (en) | Ethylene-vinyl acetate copolymer/polyaniline composite conductive material and preparation method thereof | |
| CN103342869A (en) | Modified carbon black/PVA (polyvinyl alcohol) film and preparation method thereof | |
| CN108219453B (en) | A kind of preparation method of three-dimensional porous grapheme/polyaniline composite material | |
| CN107337750B (en) | A kind of expandable poly-styrene and preparation method thereof | |
| CN1884373A (en) | Preparation of low density(0.03-0.2g/cm3)conductive polyurethane foam material containing carbon nanometer tube | |
| CN102863645B (en) | A kind of supercritical CO2 prepares the method for highly functional foamed polymer material | |
| CN116987305A (en) | Metal-doped multiwall carbon nanotube type biodegradable conductive film and preparation method thereof |
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 | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |