CN108211816A - A kind of resistance oxygen water permeable membrane and its preparation method and application - Google Patents
A kind of resistance oxygen water permeable membrane and its preparation method and application Download PDFInfo
- Publication number
- CN108211816A CN108211816A CN201711481631.XA CN201711481631A CN108211816A CN 108211816 A CN108211816 A CN 108211816A CN 201711481631 A CN201711481631 A CN 201711481631A CN 108211816 A CN108211816 A CN 108211816A
- Authority
- CN
- China
- Prior art keywords
- oxygen barrier
- water permeable
- hydrotalcite
- water
- oxygen
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D53/228—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/268—Drying gases or vapours by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0079—Manufacture of membranes comprising organic and inorganic components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
-
- 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
- C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
- C08J7/04—Coating
- C08J7/042—Coating with two or more layers, where at least one layer of a composition contains a polymer binder
- C08J7/0423—Coating with two or more layers, where at least one layer of a composition contains a polymer binder with at least one layer of inorganic material and at least one layer of a composition containing a polymer binder
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/36—Hydrophilic membranes
-
- 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
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/04—Homopolymers or copolymers of ethene
- C08J2323/06—Polyethene
-
- 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
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
-
- 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
- C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
- C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
-
- 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
- C08J2401/08—Cellulose derivatives
- C08J2401/26—Cellulose ethers
- C08J2401/28—Alkyl ethers
-
- 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
- C08J2427/00—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 a halogen; Derivatives of such polymers
- C08J2427/02—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 a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2427/04—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 a halogen; Derivatives of such polymers not modified by chemical after-treatment containing chlorine atoms
- C08J2427/06—Homopolymers or copolymers of vinyl chloride
-
- 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
- C08J2439/00—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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen; Derivatives of such polymers
- C08J2439/04—Homopolymers or copolymers of monomers containing heterocyclic rings having nitrogen as ring member
- C08J2439/06—Homopolymers or copolymers of N-vinyl-pyrrolidones
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
本发明提供了一种阻氧透水薄膜及其制备方法和应用,阻氧透水薄膜包括基底和阻氧透水层;阻氧透水层包括交替层叠的水滑石纳米片层和亲水性聚合物层;基底与阻氧透水层中的水滑石纳米片层相接,且最外层为亲水性聚合物层。实施例的结果表明,本发明阻氧透水薄膜的氧气透过量为1.128~2.783cm3·m‑2·day‑1·atm‑1低于聚丙烯薄膜的氧气透过量98.143cm3·m‑2·day‑1·atm‑1;本发明阻氧透水薄膜的水蒸气透过量为2.32cm3·m‑2·day‑1·atm‑1,高于聚丙烯薄膜的水蒸气透过量1.95cm3·m‑2·day‑1·atm‑1,本发明阻氧透水薄膜具有阻隔氧气和透过水蒸气的性能。
The invention provides an oxygen barrier and water permeable film and its preparation method and application. The oxygen barrier and water permeable film includes a substrate and an oxygen barrier and water permeable layer; the oxygen barrier and water permeable layer includes alternately laminated hydrotalcite nanosheets and hydrophilic polymer layers; The substrate is in contact with the hydrotalcite nano sheet layer in the oxygen barrier and water permeable layer, and the outermost layer is a hydrophilic polymer layer. The results of the examples show that the oxygen permeation rate of the oxygen barrier and water permeable film of the present invention is 1.128~2.783 cm 3 ·m ‑2 ·day ‑1 ·atm ‑1 which is lower than the oxygen permeation rate of the polypropylene film 98.143 cm 3 ·m ‑2 ·day ‑1 ·atm ‑1 ; the water vapor transmission rate of the oxygen barrier and water permeable film of the present invention is 2.32cm 3 ·m ‑2 ·day ‑1 ·atm ‑1 , which is higher than the water vapor transmission rate of the polypropylene film 1.95cm 3 ·m ‑2 ·day ‑1 ·atm ‑1 , the oxygen barrier and water permeable film of the present invention has the performance of blocking oxygen and permeating water vapor.
Description
技术领域technical field
本发明属于膜分离技术领域,尤其涉及一种阻氧透水薄膜及其制备方法和应用。The invention belongs to the technical field of membrane separation, and in particular relates to an oxygen barrier and water permeable membrane, a preparation method and application thereof.
背景技术Background technique
有机无机复合薄膜作为气体阻隔薄膜已经得到了越来越多的关注。有机无机复合薄膜材料具有透明性、可弯折性,阻气性能较好的特性,已被广泛用作普通密封包装材料。现有技术中有机无机复合薄膜的气体阻隔通常是基于物理阻隔作用,只能单纯地实现对气体无差别的阻隔。然而在某些领域,例如厌氧湿法发酵、空气除湿等领域,要求薄膜在具有阻氧性能的同时还需有一定的水蒸气调节性能,即水蒸气透过性能,但是现有技术中并没有同时具有阻氧透水蒸气性能的薄膜的报道。Organic-inorganic composite thin films have received increasing attention as gas barrier films. Organic-inorganic composite film materials have the characteristics of transparency, bendability, and good gas barrier properties, and have been widely used as ordinary sealing packaging materials. The gas barrier of organic-inorganic composite thin films in the prior art is usually based on physical barrier effect, which can only simply achieve indiscriminate gas barrier. However, in some fields, such as anaerobic wet fermentation, air dehumidification and other fields, it is required that the film must have certain water vapor regulation performance, that is, water vapor transmission performance, while having oxygen barrier performance, but there is no such thing in the prior art. There is no report of a film with oxygen barrier and water vapor permeability properties at the same time.
发明内容Contents of the invention
本发明提供了一种阻氧透水薄膜,本发明提供的阻氧透水薄膜同时具有氧气阻隔和水蒸气透过性能。The invention provides an oxygen-barrier water-permeable film. The oxygen-barrier water-permeable film provided by the invention has both oxygen barrier and water vapor permeability properties.
本发明提供了一种阻氧透水薄膜,包括基底和阻氧透水层;所述阻氧透水层包括交替层叠的水滑石纳米片层和亲水性聚合物层;所述基底与阻氧透水层中的水滑石纳米片层相接;所述阻氧透水薄膜的最外层为亲水性聚合物层;所述水滑石纳米片层平行于基底。The invention provides an oxygen barrier and water permeable film, comprising a substrate and an oxygen barrier and water permeable layer; the oxygen barrier and water permeable layer includes alternately laminated hydrotalcite nanosheet layers and hydrophilic polymer layers; the base and the oxygen barrier and water permeable layer The hydrotalcite nano-sheets are connected; the outermost layer of the oxygen barrier and water-permeable film is a hydrophilic polymer layer; the hydrotalcite nano-sheets are parallel to the substrate.
优选的,所述基底的材质为聚乙烯、聚丙烯或聚对苯二甲酸乙二醇酯,所述亲水性聚合物层的材质为羧甲基纤维素、羟丙基甲基纤维素、聚乙烯吡咯烷酮或聚氯乙烯。Preferably, the material of the substrate is polyethylene, polypropylene or polyethylene terephthalate, and the material of the hydrophilic polymer layer is carboxymethyl cellulose, hydroxypropyl methyl cellulose, Polyvinylpyrrolidone or polyvinyl chloride.
优选的,所述阻氧透水层的总厚度为6~9μm。Preferably, the total thickness of the oxygen barrier and water permeable layer is 6-9 μm.
优选的,每层所述亲水性聚合物层的厚度为1~6μm。Preferably, the thickness of each hydrophilic polymer layer is 1-6 μm.
优选的,所述水滑石纳米片层由水滑石纳米片组成,所述水滑石纳米片的长径比为20~200;每层所述水滑石纳米片层的厚度为4~200nm。Preferably, the hydrotalcite nanosheets are composed of hydrotalcite nanosheets, the aspect ratio of the hydrotalcite nanosheets is 20-200; the thickness of each layer of the hydrotalcite nanosheets is 4-200 nm.
本发明还提供了上述阻氧透水薄膜的制备方法,包括以下步骤:The present invention also provides a preparation method of the above-mentioned oxygen barrier and water permeable film, comprising the following steps:
(1)提供水滑石纳米片分散液和亲水性聚合物分散液;(1) Provide hydrotalcite nanosheet dispersion and hydrophilic polymer dispersion;
(2)将所述水滑石纳米片分散液和亲水性聚合物分散液交替旋涂于基底上,得到复合薄膜;(2) Alternate spin-coating the hydrotalcite nanosheet dispersion and the hydrophilic polymer dispersion on the substrate to obtain a composite film;
(3)将所述复合薄膜进行干燥,得到阻氧透水薄膜。(3) Drying the composite film to obtain an oxygen barrier and water permeable film.
优选的,所述水滑石纳米片分散液的质量浓度为0.1~1.0%;所述亲水性聚合物分散液的质量浓度为3~5%。Preferably, the mass concentration of the hydrotalcite nanosheet dispersion is 0.1-1.0%; the mass concentration of the hydrophilic polymer dispersion is 3-5%.
优选的,所述水滑石纳米片的制备方法包括:Preferably, the preparation method of described hydrotalcite nanoplate comprises:
将M2+、M3+、尿素和水混合,得到混合溶液;所述M2+包括Mg2+、Zn2+或Ni2+,所述M3+包括Fe3+、Al3+或Co3+;Mix M 2+ , M 3+ , urea and water to obtain a mixed solution; the M 2+ includes Mg 2+ , Zn 2+ or Ni 2+ , and the M 3+ includes Fe 3+ , Al 3+ or Co 3+ ;
将混合溶液进行晶化反应,将晶化反应的产物冷却至室温,得到水滑石纳米片;performing a crystallization reaction on the mixed solution, and cooling the product of the crystallization reaction to room temperature to obtain hydrotalcite nanosheets;
所述晶化反应的温度为100~120℃,所述晶化反应的时间为20~30h。The temperature of the crystallization reaction is 100-120° C., and the time of the crystallization reaction is 20-30 hours.
优选的,所述M2+与M3+的摩尔比为2~4:1;所述尿素与混合溶液中金属离子的总物质的量的比为2~4:1;所述混合溶液中尿素的浓度为0.5~1.5mol/L。Preferably, the molar ratio of M 2+ to M 3+ is 2 to 4:1; the ratio of the urea to the total amount of metal ions in the mixed solution is 2 to 4:1; The concentration of urea is 0.5-1.5mol/L.
本发明还提供了上述阻氧透水薄膜或上述制备方法制备得到的阻氧透水薄膜在分离水蒸气和氧气中的应用。The present invention also provides the application of the above oxygen barrier and water permeable film or the oxygen barrier and water permeable film prepared by the above preparation method in separating water vapor and oxygen.
本发明提供了一种阻氧透水薄膜,包括基底和阻氧透水层;所述阻氧透水层包括交替层叠的水滑石纳米片层和亲水性聚合物层;所述基底与阻氧透水层中的水滑石纳米片层相接;所述阻氧透水薄膜的最外层为亲水性聚合物层;所述水滑石纳米片层平行于基底。本发明提供的阻氧透水薄膜同时具有阻隔氧气和透过水蒸气的性能。本发明采用的水滑石纳米片平行于基底,大大延长了氧气透过的路径,从而能够将氧气阻隔在薄膜的外侧;亲水性聚合物可以吸纳大量水分子,增加基底两侧的水的渗透压,从而使得薄膜具有水蒸气通过性能。实施例的结果表明,本发明提供的阻氧透水薄膜的氧气透过量为1.128~2.783cm3·m-2·day-1·atm-1,远低于传统聚丙烯薄膜的氧气透过量98.143cm3·m-2·day-1·atm-1。可见,本发明提供的阻氧透水薄膜能够有效将氧气阻挡在薄膜的外侧,具有较好的阻氧效果;同时,本发明提供的阻氧透水薄膜的水蒸气透过量为2.327cm3·m-2·day-1·atm-1,高于传统聚丙烯薄膜基底水蒸气透过量为1.944cm3·m-2·day-1·atm-1,可见,本发明提供的阻氧透水薄膜能够有效地透过水蒸气,具有较好的水蒸气透过效果。The invention provides an oxygen barrier and water permeable film, comprising a substrate and an oxygen barrier and water permeable layer; the oxygen barrier and water permeable layer includes alternately laminated hydrotalcite nanosheet layers and hydrophilic polymer layers; the base and the oxygen barrier and water permeable layer The hydrotalcite nano-sheets are connected; the outermost layer of the oxygen barrier and water-permeable film is a hydrophilic polymer layer; the hydrotalcite nano-sheets are parallel to the substrate. The oxygen-barrier and water-permeable film provided by the invention has the properties of oxygen barrier and water vapor permeability. The hydrotalcite nanosheets used in the present invention are parallel to the substrate, which greatly prolongs the path for oxygen to pass through, so that oxygen can be blocked on the outside of the film; the hydrophilic polymer can absorb a large number of water molecules, increasing the penetration of water on both sides of the substrate pressure, so that the film has water vapor permeable properties. The results of the examples show that the oxygen permeation rate of the oxygen barrier and water permeable film provided by the present invention is 1.128~2.783 cm 3 ·m -2 ·day -1 ·atm -1 , far lower than the oxygen permeation rate of the traditional polypropylene film of 98.143 cm 3 · m -2 · day -1 · atm -1 . It can be seen that the oxygen barrier and water permeable film provided by the present invention can effectively block oxygen on the outside of the film, and has a good oxygen barrier effect; at the same time, the water vapor transmission rate of the oxygen barrier and water permeable film provided by the present invention is 2.327cm 3 ·m - 2 ·day -1 ·atm -1 , which is 1.944cm 3 ·m -2 ·day -1 ·atm -1 higher than the water vapor transmission rate of the traditional polypropylene film substrate. It can be seen that the oxygen barrier and water permeable film provided by the present invention can effectively Permeable to water vapor, has better water vapor transmission effect.
附图说明Description of drawings
图1为本发明实施例1制备的水滑石纳米片的扫描电子显微镜图;Fig. 1 is the scanning electron micrograph of the hydrotalcite nanoplate that the embodiment of the present invention 1 prepares;
图2为本发明实施例1制备得到的阻氧透水薄膜的扫描电子显微镜图;Figure 2 is a scanning electron microscope image of the oxygen barrier and water permeable film prepared in Example 1 of the present invention;
图3为本发明实施例1制备得到的阻氧透水薄膜的原子显微镜图;Fig. 3 is an atomic microscope image of the oxygen barrier and water permeable film prepared in Example 1 of the present invention;
图4为本发明实施例1制备得到的阻氧透水薄膜截面的扫描电子显微镜图;Fig. 4 is a scanning electron microscope image of the section of the oxygen barrier and water permeable film prepared in Example 1 of the present invention;
图5为本发明实施例1制备得到的阻氧透水薄膜切片的透射电子显微镜图;Fig. 5 is a transmission electron microscope image of a slice of an oxygen-barrier and water-permeable film prepared in Example 1 of the present invention;
图6为实施例1~3制备得到的阻氧透水薄膜和基底聚丙烯薄膜的氧气透过性测试结果;Figure 6 shows the oxygen permeability test results of the oxygen barrier and water permeable film and the base polypropylene film prepared in Examples 1-3;
图7为实施例1制备得到的阻氧透水薄膜和基底聚丙烯薄膜的水蒸气透过性测试结果;Fig. 7 is the water vapor permeability test result of the oxygen-barrier water-permeable film and the base polypropylene film prepared in Example 1;
图8为本发明实施例1~3制备得到的阻氧透水薄膜透过水蒸气的示意图;Fig. 8 is a schematic diagram of water vapor passing through the oxygen-barrier water-permeable film prepared in Examples 1-3 of the present invention;
图9为本发明实施例1~3制备得到的阻氧透水薄膜阻挡氧气透过的示意图。FIG. 9 is a schematic diagram of the oxygen-barrier and water-permeable films prepared in Examples 1-3 of the present invention to block oxygen transmission.
具体实施方式Detailed ways
本发明提供了一种阻氧透水薄膜,包括基底和阻氧透水层;所述阻氧透水层包括交替层叠的水滑石纳米片层和亲水性聚合物层;所述基底与阻氧透水层中的水滑石纳米片层相接;所述阻氧透水薄膜的最外层为亲水性聚合物层;所述水滑石纳米片层平行于基底。The invention provides an oxygen barrier and water permeable film, comprising a substrate and an oxygen barrier and water permeable layer; the oxygen barrier and water permeable layer includes alternately laminated hydrotalcite nanosheet layers and hydrophilic polymer layers; the base and the oxygen barrier and water permeable layer The hydrotalcite nano-sheets are connected; the outermost layer of the oxygen barrier and water-permeable film is a hydrophilic polymer layer; the hydrotalcite nano-sheets are parallel to the substrate.
在本发明中,所述基底的材质优选为聚乙烯、聚丙烯或聚对苯二甲酸乙二醇酯。所述基底的厚度优选为0.2~0.3mm,进一步优选为0.25~0.3mm。In the present invention, the material of the substrate is preferably polyethylene, polypropylene or polyethylene terephthalate. The thickness of the substrate is preferably 0.2-0.3 mm, more preferably 0.25-0.3 mm.
在本发明中,所述阻氧透水层包括交替层叠的水滑石纳米片层和亲水性聚合物层;所述基底与阻氧透水层中的水滑石纳米片层相接;所述阻氧透水薄膜的最外层为亲水性聚合物层,即所述阻氧透水薄膜的结构依次为:基底、水滑石纳米片层、亲水性聚合物层、水滑石纳米片层、……、亲水性聚合物层。In the present invention, the oxygen barrier and water permeable layer includes alternately laminated hydrotalcite nanosheets and hydrophilic polymer layers; the substrate is in contact with the hydrotalcite nanosheets in the oxygen barrier and water permeable layer; the oxygen barrier The outermost layer of the water-permeable film is a hydrophilic polymer layer, that is, the structure of the oxygen-blocking water-permeable film is as follows: substrate, hydrotalcite nanosheets, hydrophilic polymer layer, hydrotalcite nanosheets, ..., Hydrophilic polymer layer.
在本发明中,所述水滑石纳米片层和亲水性聚合物层交替层叠;本发明以一层水滑石纳米片层和一层亲水性聚合物层为一个循环单元,所述循环单元的循环次数优选为25~40次,进一步优选为30~40次,更优选为35~40次。In the present invention, the hydrotalcite nanosheets and hydrophilic polymer layers are alternately laminated; the present invention uses one layer of hydrotalcite nanosheets and one hydrophilic polymer layer as a cycle unit, and the cycle unit The number of cycles is preferably 25 to 40 times, more preferably 30 to 40 times, more preferably 35 to 40 times.
在本发明中,所述水滑石纳米片层由水滑石纳米片堆叠组成,所述水滑石纳米片的长径比优选为20~200,进一步优选为50~150,更优选为70~120;所述水滑石纳米片层的厚度优选为4~200nm,进一步优选为50~150mm,更优选为70~120mm。在本发明中,如果水滑石纳米片层厚度过大,则薄膜容易产生裂纹,其稳定性下降;如果水滑石纳米片层厚度过小,则薄膜的阻氧透水性能变差。In the present invention, the hydrotalcite nanosheet layer is composed of stacked hydrotalcite nanosheets, and the aspect ratio of the hydrotalcite nanosheets is preferably 20-200, more preferably 50-150, and more preferably 70-120; The thickness of the hydrotalcite nanosheet layer is preferably 4-200 nm, more preferably 50-150 mm, more preferably 70-120 mm. In the present invention, if the thickness of the hydrotalcite nanosheets is too large, the film is prone to cracks and its stability decreases; if the thickness of the hydrotalcite nanosheets is too small, the oxygen barrier and water permeability of the film will deteriorate.
在本发明中,所述水滑石纳米片具有大的长径比,使得水滑石纳米片大大延长了氧气透过的路径,从而能够将氧气阻隔在阻氧透水薄膜的外侧。如图9所示,氧气分子被聚合物层阻挡在薄膜外侧,难以透过。In the present invention, the hydrotalcite nanosheets have a large aspect ratio, so that the hydrotalcite nanosheets greatly prolong the oxygen permeation path, thereby blocking oxygen on the outside of the oxygen barrier and water permeable film. As shown in Figure 9, oxygen molecules are blocked by the polymer layer on the outside of the film, making it difficult to pass through.
在本发明中,所述亲水性聚合物层的材质优选为羧甲基纤维素、羟丙基甲基纤维素、聚乙烯吡咯烷酮或聚氯乙烯。在本发明中,所述亲水性聚合物层的厚度优选为1~6μm,进一步优选为2~5μm,更优选为3~4μm。In the present invention, the material of the hydrophilic polymer layer is preferably carboxymethylcellulose, hydroxypropylmethylcellulose, polyvinylpyrrolidone or polyvinyl chloride. In the present invention, the thickness of the hydrophilic polymer layer is preferably 1-6 μm, more preferably 2-5 μm, more preferably 3-4 μm.
在本发明中,所述亲水性聚合物层与薄膜外侧的水分子之间存在相互吸引作用,亲水性聚合物层能够将大量水分子吸纳在薄膜内部,增加了薄膜中基底两侧水的渗透压,从而使得薄膜具有水蒸气通过性能。如图8所示,水分子可通过聚合物层的吸附作用,进入薄膜的聚合物层,并且水滑石纳米片层中水滑石纳米片间存在着空隙,便于水分子经过水滑石片层,达到基底位置,随着水分子的积累,增加基底两侧的渗透压,进而使水分子通过基底。In the present invention, there is mutual attraction between the hydrophilic polymer layer and the water molecules on the outside of the film, and the hydrophilic polymer layer can absorb a large amount of water molecules inside the film, increasing the amount of water on both sides of the substrate in the film. osmotic pressure, so that the film has water vapor permeable properties. As shown in Figure 8, water molecules can enter the polymer layer of the film through the adsorption of the polymer layer, and there are gaps between the hydrotalcite nanosheets in the hydrotalcite nanosheets, so that the water molecules can pass through the hydrotalcite sheets to reach At the substrate position, with the accumulation of water molecules, the osmotic pressure on both sides of the substrate is increased, thereby allowing water molecules to pass through the substrate.
本发明还提供了上述技术方案所述阻氧透水薄膜的制备方法,包括以下步骤:The present invention also provides a preparation method of the oxygen barrier and water permeable film described in the above technical solution, comprising the following steps:
(1)提供水滑石纳米片分散液和亲水性聚合物分散液;(1) Provide hydrotalcite nanosheet dispersion and hydrophilic polymer dispersion;
(2)将所述水滑石纳米片分散液和亲水性聚合物分散液交替旋涂于基底上,得到复合薄膜;(2) Alternate spin-coating the hydrotalcite nanosheet dispersion and the hydrophilic polymer dispersion on the substrate to obtain a composite film;
(3)将所述复合薄膜进行干燥,得到阻氧透水薄膜。(3) Drying the composite film to obtain an oxygen barrier and water permeable film.
本发明提供了水滑石纳米片分散液。在本发明中,所述水滑石纳米片分散液的质量浓度优选为0.1~1.0%,进一步优选为0.2~0.8%,更优选为0.4~0.6%;所述水滑石纳米片分散液的溶剂优选为去离子水。本发明将水滑石纳米片和溶剂混合,得到水滑石纳米片分散液。本发明对混合的方式没有特别的限定,采用本领域技术人员所熟知的混合方式即可。The invention provides a hydrotalcite nano sheet dispersion liquid. In the present invention, the mass concentration of the hydrotalcite nanosheet dispersion is preferably 0.1 to 1.0%, more preferably 0.2 to 0.8%, more preferably 0.4 to 0.6%; the solvent of the hydrotalcite nanosheet dispersion is preferably for deionized water. The invention mixes the hydrotalcite nanosheets with a solvent to obtain a dispersion liquid of the hydrotalcite nanosheets. In the present invention, there is no particular limitation on the mixing method, and a mixing method well known to those skilled in the art can be used.
在本发明中,所述水滑石纳米片的制备方法优选包括:In the present invention, the preparation method of the hydrotalcite nanosheet preferably includes:
将M2+、M3+、尿素和水混合,得到混合溶液;所述M2+包括Mg2+、Zn2+或Ni2+,所述M3+包括Fe3+、Al3+或Co3+;Mix M 2+ , M 3+ , urea and water to obtain a mixed solution; the M 2+ includes Mg 2+ , Zn 2+ or Ni 2+ , and the M 3+ includes Fe 3+ , Al 3+ or Co 3+ ;
将混合溶液进行晶化反应,然后冷却至室温,得到水滑石纳米片;The mixed solution is subjected to a crystallization reaction, and then cooled to room temperature to obtain hydrotalcite nanosheets;
所述晶化反应的温度为100~120℃,所述晶化反应的时间为20~30h。The temperature of the crystallization reaction is 100-120° C., and the time of the crystallization reaction is 20-30 hours.
本发明将M2+、M3+、尿素和水混合,得到混合溶液。在本发明中,所述M2+优选以硝酸盐、氯化盐的形式提供;所述所述M3+优选以硝酸盐、氯化盐的形式提供。在本发明中,所述M2 +优选包括Mg2+、Zn2+或Ni2+,所述M3+优选包括Fe3+、Al3+或Co3+。在本发明中,所述混合溶液中尿素与金属离子总物质的量的摩尔比优选为2~4:1,进一步优选为2~3:1;所述金属离子中M2+与M3+的摩尔比优选为2~4:1,进一步优选为2~3:1。在本发明中,所述混合溶液中尿素的浓度优选为0.5~1.5mol/L,进一步优选为0.8~1.2mol/L。The invention mixes M 2+ , M 3+ , urea and water to obtain a mixed solution. In the present invention, the M 2+ is preferably provided in the form of nitrate or chloride; the M 3+ is preferably provided in the form of nitrate or chloride. In the present invention, the M 2+ preferably includes Mg 2+ , Zn 2+ or Ni 2+ , and the M 3+ preferably includes Fe 3+ , Al 3+ or Co 3+ . In the present invention, the molar ratio of urea to the total amount of metal ions in the mixed solution is preferably 2 to 4:1, more preferably 2 to 3:1; M 2+ and M 3+ in the metal ions The molar ratio of is preferably 2 to 4:1, more preferably 2 to 3:1. In the present invention, the concentration of urea in the mixed solution is preferably 0.5-1.5 mol/L, more preferably 0.8-1.2 mol/L.
在本发明中,所述混合优选为先将M2+、M3+和水混合,得到金属盐溶液;将尿素与水混合,得到尿素溶液,然后再将金属盐溶液与尿素溶液混合,得到混合溶液。本发明对混合的具体实施方式没有特殊要求,采用本领域技术人员所熟知的物料混合方式即可。In the present invention, the mixing is preferably to first mix M 2+ , M 3+ and water to obtain a metal salt solution; mix urea with water to obtain a urea solution, and then mix the metal salt solution and urea solution to obtain mixture. The present invention has no special requirements on the specific implementation of the mixing, and a material mixing method well known to those skilled in the art can be used.
得到混合溶液后,本发明优选将混合溶液进行晶化反应,将晶化反应的产物冷却至室温,得到水滑石纳米片。After the mixed solution is obtained, in the present invention, the mixed solution is preferably subjected to a crystallization reaction, and the product of the crystallization reaction is cooled to room temperature to obtain hydrotalcite nanosheets.
在本发明中,所述晶化反应的温度优选为100~120℃,进一步优选为105~115℃,所述晶化反应的时间优选为20~30h,进一步优选为24~26h。本发明在所述晶化过程中,混合溶液逐渐出现沉淀,生成水滑石纳米片。In the present invention, the temperature of the crystallization reaction is preferably 100-120°C, more preferably 105-115°C, and the time of the crystallization reaction is preferably 20-30h, more preferably 24-26h. In the present invention, during the crystallization process, the mixed solution gradually precipitates to generate hydrotalcite nanosheets.
在本发明中,所述冷却的方式优选为自然降温。In the present invention, the cooling method is preferably natural cooling.
本发明将晶化产物冷却至室温后,优选将晶化产物进行固液分离得到固体,然后经洗涤、干燥得到水滑石纳米片。本发明对所述固液分离的方式没有特殊要求,采用本领域技术人员所熟知的固液分离方式即可;在本发明中,所述固液分离进一步优选为离心分离,当采用离心的方式进行固液分离时,所述离心分离的转速优选为1500~2000r/min,进一步优选为1600~1800r/min,所述离心分离的时间优选为5~10min,进一步优选为6~8min。In the present invention, after the crystallization product is cooled to room temperature, the crystallization product is preferably subjected to solid-liquid separation to obtain a solid, which is then washed and dried to obtain hydrotalcite nanosheets. The present invention has no special requirements on the method of solid-liquid separation, and the solid-liquid separation method well known to those skilled in the art can be used; in the present invention, the solid-liquid separation is further preferably centrifugal separation. When performing solid-liquid separation, the rotational speed of the centrifugal separation is preferably 1500-2000r/min, more preferably 1600-1800r/min, and the time of the centrifugal separation is preferably 5-10min, more preferably 6-8min.
本发明优选采用去离子水对分离得到的固体进行洗涤。本发明对所述去离子水的用量没有特殊要求,能够将固体浸没即可。本发明对洗涤的次数没有特别要求,优选将所述固体洗涤至中性即可;在本发明中,所述洗涤的次数优选为3~5次。本发明优选通过洗涤所述固体后的洗涤溶液的pH值来判断所述固体是否为中性;当所述洗涤溶液的pH值为6.5~7.5时,所述固体即为中性。In the present invention, deionized water is preferably used to wash the separated solid. The present invention has no special requirements on the amount of deionized water, as long as the solid can be submerged. In the present invention, there is no special requirement on the number of washings, and it is preferable to wash the solid until neutral; in the present invention, the number of washings is preferably 3 to 5 times. In the present invention, it is preferred to judge whether the solid is neutral by the pH value of the washing solution after washing the solid; when the pH value of the washing solution is 6.5-7.5, the solid is neutral.
本发明优选对洗涤后的固体进行干燥。在本发明中,所述干燥的温度优选为50~70℃,进一步优选55~65℃;所述干燥的时间优选为10~15h,进一步优选12~14h。本发明对所述干燥的方式没有特殊要求,采用本领域技术人员所熟知的干燥方式即可,优选采用真空干燥或者鼓风干燥。当采用真空干燥时,所述真空干燥的压力优选为0.5~0.8个大气压。Drying of the washed solids is preferred in the present invention. In the present invention, the drying temperature is preferably 50-70°C, more preferably 55-65°C; the drying time is preferably 10-15 hours, more preferably 12-14 hours. The present invention has no special requirements on the drying method, and the drying methods known to those skilled in the art can be used, preferably vacuum drying or blast drying. When vacuum drying is adopted, the pressure of the vacuum drying is preferably 0.5-0.8 atmosphere.
本发明提供亲水性聚合物分散液。在本发明中,所述亲水性聚合物分散液的质量浓度优选为3~5%,进一步优选为4~5%;所述亲水性聚合物分散液的溶剂优选为去离子水。本发明对所述亲水性聚合物分散液的制备方法没有特别要求,采用本领域技术人员所熟知的溶液配制方法即可。The present invention provides a hydrophilic polymer dispersion. In the present invention, the mass concentration of the hydrophilic polymer dispersion is preferably 3-5%, more preferably 4-5%; the solvent of the hydrophilic polymer dispersion is preferably deionized water. The present invention has no special requirements on the preparation method of the hydrophilic polymer dispersion, and the solution preparation method known to those skilled in the art can be used.
本发明将所述水滑石纳米片分散液和亲水性聚合物分散液交替旋涂于基底上,得到复合薄膜。In the invention, the hydrotalcite nano sheet dispersion liquid and the hydrophilic polymer dispersion liquid are alternately spin-coated on the substrate to obtain a composite thin film.
在本发明中,所述旋涂优选通过旋转涂覆机完成;本发明优选使用抽真空的方法将薄膜基底吸附在旋转涂覆机上,然后将水滑石纳米片分散液和亲水性聚合物水分散液交替旋涂于基底上。在本发明中,第一层旋涂层为水滑石纳米片分散液,第二层旋涂层为亲水性聚合物水分散液,依次交替旋涂,每一层旋涂的水滑石纳米片分散液和依次旋涂的亲水性聚合物水分散液为一个循环单元,最后一层为强亲水性聚合物水分散液。在本发明中,所述循环单元的循环的次数优选为25~40次,进一步优选为30~40次,更优选为35~40次。在本发明中,当旋涂水滑石纳米片分散液时,所述旋涂的转速优选为1800~2200r/min,进一步优选2000~2200r/min;当旋涂亲水性聚合物水分散液时,所述旋涂的转速优选为4500~5500r/min,进一步优选为4800~5200r/min。本发明通过旋涂的方法,将水滑石纳米片旋涂于基底上,使水滑石纳米片具有平行于基底的有序取向结构。In the present invention, the spin coating is preferably completed by a spin coater; the present invention preferably uses a vacuum method to adsorb the film substrate on the spin coater, and then the hydrotalcite nanosheet dispersion and the hydrophilic polymer water The dispersion was alternately spin-coated on the substrate. In the present invention, the first layer of spin coating is a dispersion of hydrotalcite nanosheets, and the second layer of spin coating is an aqueous dispersion of hydrophilic polymers, which are alternately spin-coated successively, and each layer of spin-coated hydrotalcite nanosheets The dispersion liquid and the aqueous dispersion liquid of the hydrophilic polymer which are spin-coated successively constitute a circulation unit, and the last layer is the aqueous dispersion liquid of the strongly hydrophilic polymer. In the present invention, the number of cycles of the circulation unit is preferably 25 to 40 times, more preferably 30 to 40 times, and even more preferably 35 to 40 times. In the present invention, when spin-coating the hydrotalcite nanosheet dispersion, the rotational speed of the spin-coating is preferably 1800-2200r/min, more preferably 2000-2200r/min; when spin-coating the hydrophilic polymer aqueous dispersion , the rotational speed of the spin coating is preferably 4500˜5500 r/min, more preferably 4800˜5200 r/min. In the present invention, the hydrotalcite nanosheets are spin-coated on the substrate through a spin coating method, so that the hydrotalcite nanosheets have an ordered orientation structure parallel to the substrate.
所述交替旋涂前,本发明优选对所述基底进行清洗。在本发明中,所述清洗优选包括:将薄膜基底依次用丙酮、乙醇和去离子水进行超声清洗。在本发明中,所述超声清洗的超声强度优选为20000~30000Hz,进一步优选为24000~26000Hz。在本发明中,使用各溶剂进行超声清洗的时间独立地优选为20~40min,进一步优选为25~35min。本发明对超声清洗的各溶剂的用量没有特别限定,只要能够浸没薄膜基底即可。Before the alternate spin coating, the present invention preferably cleans the substrate. In the present invention, the cleaning preferably includes: ultrasonically cleaning the film substrate with acetone, ethanol and deionized water in sequence. In the present invention, the ultrasonic intensity of the ultrasonic cleaning is preferably 20000-30000 Hz, more preferably 24000-26000 Hz. In the present invention, the time for ultrasonic cleaning using each solvent is independently preferably 20 to 40 minutes, more preferably 25 to 35 minutes. In the present invention, there is no particular limitation on the amount of each solvent used in ultrasonic cleaning, as long as it can immerse the film substrate.
所述旋涂后,本发明将所述复合薄膜进行干燥,得到阻氧透水薄膜。在本发明中,所述干燥优选为自然晾干。在本发明中,所述晾干的温度优选为20~30℃,进一步优选为25℃;所述晾干的时间优选为1~3h,进一步优选为1.5~2.5h。After the spin coating, the present invention dries the composite film to obtain an oxygen barrier and water permeable film. In the present invention, the drying is preferably air drying. In the present invention, the drying temperature is preferably 20-30°C, more preferably 25°C; the drying time is preferably 1-3 hours, more preferably 1.5-2.5 hours.
下面将结合本发明中的实施例,对本发明中的技术方案进行清楚、完整地描述。显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Apparently, the described embodiments are only some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
实施例1Example 1
将Mg(NO3)2·6H2O和Al(NO3)3·9H2O溶于去离子水中,得到金属盐溶液,金属盐溶液中Mg(NO3)2·6H2O的浓度为0.4mol/L,金属盐溶液中Al(NO3)3·9H2O的浓度为0.2mol/L;将尿素溶于去离子水中,得到尿素溶液,尿素溶液的浓度为0.67mol/L。将50mL所述金属盐溶液和50mL所述尿素溶液混合,得到混合溶液。将混合溶液搅拌均匀,置于110℃的烘箱中,晶化24h,然后将反应体系自然冷却至室温,离心分离得到固体;用去离子水洗涤所述固体,至洗涤后的去离子水为中性,得到水滑石纳米片;Dissolve Mg(NO 3 ) 2 ·6H 2 O and Al(NO 3 ) 3 ·9H 2 O in deionized water to obtain a metal salt solution. The concentration of Mg(NO 3 ) 2 ·6H 2 O in the metal salt solution is 0.4mol/L, the concentration of Al(NO 3 ) 3 ·9H 2 O in the metal salt solution is 0.2mol/L; urea is dissolved in deionized water to obtain a urea solution, and the concentration of the urea solution is 0.67mol/L. 50 mL of the metal salt solution and 50 mL of the urea solution were mixed to obtain a mixed solution. Stir the mixed solution evenly, place it in an oven at 110°C, and crystallize for 24 hours, then cool the reaction system naturally to room temperature, and centrifuge to obtain a solid; wash the solid with deionized water until the deionized water after washing is medium properties, to obtain hydrotalcite nanosheets;
以去离子水为溶剂,配制质量浓度为0.5wt.%的水滑石纳米片水分散液(简写为LDH);以去离子水为溶剂,配制质量浓度为4wt.%的羧甲基纤维素水溶液(简写为CMC);With deionized water as a solvent, prepare a hydrotalcite nanosheet water dispersion (abbreviated as LDH) with a mass concentration of 0.5wt.%; with deionized water as a solvent, prepare a carboxymethyl cellulose aqueous solution with a mass concentration of 4wt.%. (abbreviated as CMC);
将聚丙烯薄膜依次用丙酮、乙醇和去离子水超声清洗30min,然后用去离子水冲洗,得到聚丙烯薄膜基底;The polypropylene film was ultrasonically cleaned with acetone, ethanol and deionized water for 30 minutes in sequence, and then rinsed with deionized water to obtain a polypropylene film substrate;
将所述薄膜基底吸附于旋转涂膜机上,将所述水滑石纳米片分散液和羧甲基纤维素水溶液先后旋涂于薄膜基底表面,循环旋涂30次,当旋涂水滑石纳米片分散液时,旋涂的转速为2000r/min,当旋涂亲水性聚合物水分散液时,旋涂的转速为5000r/min,得到复合薄膜,将所述复合薄膜从涂膜机上分离并在25℃下晾干,得到阻氧透水薄膜,简写为“(LDH/CMC)30”。Adsorb the film substrate on a spin coating machine, spin-coat the hydrotalcite nanosheet dispersion and carboxymethyl cellulose aqueous solution successively on the surface of the film substrate, spin-coat 30 times in a cycle, and when the hydrotalcite nanosheets are dispersed Liquid, the rotating speed of spin coating is 2000r/min, when spin coating hydrophilic polymer water dispersion liquid, the rotating speed of spin coating is 5000r/min, obtains composite thin film, described composite thin film is separated from film coating machine and in Dry at 25°C to obtain an oxygen barrier and water permeable film, abbreviated as "(LDH/CMC) 30 ".
实施例2Example 2
将Mg(NO3)2·6H2O和Al(NO3)3·9H2O溶于去离子水中,得到金属盐溶液,金属盐溶液中Mg(NO3)2·6H2O的浓度为0.4mol/L,金属盐溶液中Al(NO3)3·9H2O的浓度为0.2mol/L;将尿素溶于去离子水中,得到尿素溶液,尿素溶液的浓度为0.75mol/L。将50mL所述金属盐溶液和50mL所述尿素溶液混合,得到混合溶液。将混合溶液搅拌均匀,置于100℃的烘箱中,晶化26h,然后将反应体系自然冷却至室温,离心分离得到固体;使用去离子水洗涤所述固体,至洗涤后的去离子水为中性,得到水滑石纳米片;Dissolve Mg(NO 3 ) 2 ·6H 2 O and Al(NO 3 ) 3 ·9H 2 O in deionized water to obtain a metal salt solution. The concentration of Mg(NO 3 ) 2 ·6H 2 O in the metal salt solution is 0.4mol/L, the concentration of Al(NO 3 ) 3 ·9H 2 O in the metal salt solution is 0.2mol/L; urea is dissolved in deionized water to obtain a urea solution, and the concentration of the urea solution is 0.75mol/L. 50 mL of the metal salt solution and 50 mL of the urea solution were mixed to obtain a mixed solution. The mixed solution was stirred evenly, placed in an oven at 100°C, and crystallized for 26 hours, then the reaction system was naturally cooled to room temperature, and centrifuged to obtain a solid; the solid was washed with deionized water until the washed deionized water was medium properties, to obtain hydrotalcite nanosheets;
以去离子水为溶剂,配制质量浓度为0.1wt.%的水滑石纳米片水分散液,以去离子水为溶剂,配制质量浓度为3wt.%的羟丙基甲基纤维素水溶液(简写为HPMC);With deionized water as a solvent, prepare a hydrotalcite nanosheet water dispersion with a mass concentration of 0.1wt.%, and use deionized water as a solvent to prepare a 3wt.% hydroxypropyl methylcellulose aqueous solution (abbreviated as HPMC);
将聚乙烯薄膜依次用丙酮、乙醇和去离子水超声清洗30min,然后用去离子水冲洗,得到聚乙烯薄膜基底;The polyethylene film was ultrasonically cleaned with acetone, ethanol and deionized water for 30 minutes in sequence, and then rinsed with deionized water to obtain a polyethylene film substrate;
将所述薄膜基底吸附于旋转涂膜机上,将所述水滑石纳米片分散液和羟丙基甲基纤维素水溶液先后旋涂于薄膜基底表面,循环旋涂25次,当旋涂水滑石纳米片分散液时,旋涂的转速为1800r/min,当旋涂亲水性聚合物水分散液时,旋涂的转速为4500r/min,得到复合薄膜,将所述复合薄膜从涂膜机上分离并在25℃下晾干,得到阻氧透水薄膜,简写为“(LDH/HPMC)30”。Adsorb the film substrate on a spin coating machine, spin-coat the hydrotalcite nanosheet dispersion and hydroxypropyl methylcellulose aqueous solution on the surface of the film substrate successively, and spin-coat 25 times in a cycle. In the case of sheet dispersion liquid, the rotating speed of spin coating is 1800r/min, when spin coating hydrophilic polymer aqueous dispersion, the rotating speed of spin coating is 4500r/min, obtains composite film, and described composite film is separated from coating machine and dried at 25°C to obtain an oxygen barrier and water permeable film, abbreviated as "(LDH/HPMC) 30 ".
实施例3Example 3
将Mg(NO3)2·6H2O和Al(NO3)3·9H2O溶于去离子水中,得到金属盐溶液,金属盐溶液中Mg(NO3)2·6H2O的浓度为0.4mol/L,金属盐溶液中Al(NO3)3·9H2O的浓度为0.2mol/L;将尿素溶于去离子水中,得到尿素溶液,尿素溶液的浓度为0.7mol/L。将50mL所述金属盐溶液和50mL所述尿素溶液混合,得到混合溶液。将混合溶液搅拌均匀,置于110℃的烘箱中,晶化24h,然后将反应体系自然冷却至室温,离心分离得到固体;使用去离子水洗涤所述固体,至洗涤后的去离子水为中性,得到大长径比水滑石纳米片;Dissolve Mg(NO 3 ) 2 ·6H 2 O and Al(NO 3 ) 3 ·9H 2 O in deionized water to obtain a metal salt solution. The concentration of Mg(NO 3 ) 2 ·6H 2 O in the metal salt solution is 0.4mol/L, the concentration of Al(NO 3 ) 3 ·9H 2 O in the metal salt solution is 0.2mol/L; urea is dissolved in deionized water to obtain a urea solution, and the concentration of the urea solution is 0.7mol/L. 50 mL of the metal salt solution and 50 mL of the urea solution were mixed to obtain a mixed solution. Stir the mixed solution evenly, place it in an oven at 110°C, and crystallize for 24 hours, then cool the reaction system naturally to room temperature, and centrifuge to obtain a solid; wash the solid with deionized water until the deionized water after washing is medium properties, to obtain large aspect ratio hydrotalcite nanosheets;
以去离子水为溶剂,配制质量浓度为1.0wt.%的大长径比水滑石纳米片水分散液,以去离子水为溶剂,配制质量浓度为5wt.%的聚乙烯吡咯烷酮水溶液(简写为PVP);With deionized water as a solvent, prepare a water dispersion of hydrotalcite nanosheets with a large aspect ratio of 1.0wt.% in a mass concentration, and use deionized water as a solvent to prepare an aqueous solution of polyvinylpyrrolidone (abbreviated as PVP);
将聚氨酯薄膜依次用丙酮、乙醇和去离子水超声清洗30min,然后用去离子水冲洗,得到聚氨酯薄膜基底;当旋涂水滑石纳米片分散液时,旋涂的转速优选为2200r/min,当旋涂亲水性聚合物水分散液时,旋涂的转速为5500r/min;The polyurethane film is ultrasonically cleaned with acetone, ethanol and deionized water for 30min successively, and then rinsed with deionized water to obtain a polyurethane film substrate; When spin-coating the hydrophilic polymer aqueous dispersion, the spin-coating speed is 5500r/min;
将所述薄膜基底吸附于旋转涂膜机上,将所述水滑石纳米片分散液和聚氯乙烯水溶液先后旋涂于薄膜基底表面,循环旋涂40次,得到复合薄膜,将所述复合薄膜从涂膜机上分离并在30℃下晾干,得到阻氧透水薄膜,简写为“(LDH/PVP)30”。The film base is adsorbed on a spin coating machine, the hydrotalcite nanosheet dispersion and the polyvinyl chloride aqueous solution are successively spin-coated on the surface of the film base, and the spin coating is cycled 40 times to obtain a composite film, and the composite film is obtained from Separated on a film coating machine and dried at 30°C to obtain an oxygen barrier and water permeable film, abbreviated as "(LDH/PVP) 30 ".
对实施例1制备得到的水滑石纳米片使用扫描式电子显微镜进行表征,如图1所示。经测量其平均直径为641nm,平均厚度为29nm,长径比为22.1。由图1可知,本发明所得水滑石纳米片为二维层状结构,且粒径分布均匀,具有较大的长径比。由图1可知,本发明制备得到的水滑石纳米片平行放置,组成水滑石纳米片层。The hydrotalcite nanosheets prepared in Example 1 were characterized using a scanning electron microscope, as shown in FIG. 1 . The measured average diameter is 641 nm, the average thickness is 29 nm, and the aspect ratio is 22.1. It can be seen from FIG. 1 that the hydrotalcite nanosheets obtained in the present invention have a two-dimensional layered structure, and the particle size distribution is uniform and has a large aspect ratio. It can be seen from FIG. 1 that the hydrotalcite nanosheets prepared by the present invention are placed in parallel to form a hydrotalcite nanosheet layer.
对实施例1制备得到的阻氧透水薄膜使用扫描式电子显微镜进行表征,如图2所示。图2中颜色均匀表面平整,说明本发明所述方法制备得到的阻氧透水薄膜均一、完整、成膜良好。The oxygen-barrier and water-permeable film prepared in Example 1 was characterized using a scanning electron microscope, as shown in FIG. 2 . In Fig. 2, the color is uniform and the surface is smooth, which shows that the oxygen-barrier and water-permeable film prepared by the method of the present invention is uniform, complete, and film-forming is good.
对实施例1制备得到的阻氧透水薄膜使用原子显微镜进行表征,如图3所示。图3中薄膜表面平整均一,说明本发明所述方法制备得到的阻氧透水薄膜均一、完整、成膜良好。The oxygen barrier and water permeable film prepared in Example 1 was characterized by an atomic microscope, as shown in FIG. 3 . In Fig. 3, the surface of the film is even and uniform, indicating that the oxygen barrier and water permeable film prepared by the method of the present invention is uniform, complete and well formed.
对实施例1制备得到的阻氧透水薄膜的截面使用扫描式电子显微镜进行表征,如图4所示。图中颜色最深的部分为薄膜基底,中等深度的部分为阻氧透水层,较浅的部分为背景。由图4可知,本发明所得阻氧透水薄膜的结构为阻氧透水层附着在薄膜基底上,且本实施例中,阻氧透水层厚度为8μm。The cross-section of the oxygen-barrier and water-permeable film prepared in Example 1 was characterized by a scanning electron microscope, as shown in FIG. 4 . The darkest part in the picture is the film base, the middle part is the oxygen barrier and water permeable layer, and the lighter part is the background. It can be seen from FIG. 4 that the structure of the oxygen-barrier and water-permeable film obtained in the present invention is that the oxygen-barrier and water-permeable layer is attached to the film substrate, and in this embodiment, the thickness of the oxygen-barrier and water-permeable layer is 8 μm.
将本实施例所得阻氧透水薄膜进行冷冻-180℃切片,并使用透射电子显微镜对其截面进行表征,如图5所示。图中浅色的层为亲水性聚合物层,深色的层为水滑石纳米片层。经测量,本实施例所得薄膜中,亲水性聚合物层的平均厚度为204nm,水滑石纳米片层的平均厚度为67nm。The oxygen-barrier and water-permeable film obtained in this example was sliced at -180°C, and its cross-section was characterized by a transmission electron microscope, as shown in FIG. 5 . The light-colored layer in the figure is the hydrophilic polymer layer, and the dark-colored layer is the hydrotalcite nanosheet layer. It is measured that in the film obtained in this example, the average thickness of the hydrophilic polymer layer is 204 nm, and the average thickness of the hydrotalcite nanosheet layer is 67 nm.
采用GB/T 1038-2000标准对实施例1~3制备得到的阻氧透水薄膜和基底聚丙烯薄膜进行氧气透过性测试,结果如图6所示。The oxygen barrier and water permeable films prepared in Examples 1 to 3 and the base polypropylene film were tested for oxygen permeability according to the GB/T 1038-2000 standard, and the results are shown in FIG. 6 .
由图6测试结果可知,聚丙烯薄膜的氧气透过量为98.143cm3·m-2·day-1·atm-1;而本发明提供的阻氧透水薄膜的氧气透过量分别为1.128cm3·m-2·day-1·atm-1、2.783cm3·m-2·day-1·atm-1和1.857cm3·m-2·day-1·atm-1。本发明提供的阻氧透水薄膜的氧气透过量远远低于聚丙烯薄膜的氧气透过量,由此说明,本发明提供的阻氧透水薄膜能够有效将氧气阻挡在薄膜的外侧,具有较好的阻氧效果。From the test results in Figure 6, it can be seen that the oxygen transmission rate of the polypropylene film is 98.143cm 3 ·m -2 ·day -1 ·atm -1 ; while the oxygen transmission rate of the oxygen barrier and water permeable film provided by the present invention is 1.128cm 3 · m -2 ·day -1 ·atm -1 , 2.783 cm 3 ·m -2 ·day -1 ·atm -1 and 1.857 cm 3 ·m -2 ·day -1 ·atm -1 . The oxygen permeation rate of the oxygen barrier and water permeable film provided by the present invention is far lower than that of the polypropylene film, which shows that the oxygen barrier and water permeable film provided by the present invention can effectively block oxygen on the outside of the film, and has better Oxygen barrier effect.
采用GB/T 21529-2008标准对实施例1~3制备得到的阻氧透水薄膜和基底聚丙烯薄膜进行水蒸气透过性测试,结果如图7所示。The water vapor permeability test was carried out on the oxygen barrier and water permeable films prepared in Examples 1 to 3 and the base polypropylene film using the GB/T 21529-2008 standard, and the results are shown in FIG. 7 .
由图7测试结果可知,聚丙烯薄膜基底水蒸气透过量为1.95cm3·m-2·day-1·atm-1;而本发明实施例1提供的阻氧透水薄膜的水蒸气透过量为2.32cm3·m-2·day-1·atm-1。由此可知,本发明提供的阻氧透水薄膜能够有效地透过水蒸气,具有较好的水蒸气透过效果。From the test results in Figure 7, it can be seen that the water vapor transmission rate of the polypropylene film substrate is 1.95 cm 3 ·m −2 ·day −1 ·atm −1 ; while the water vapor transmission rate of the oxygen barrier and water permeable film provided in Example 1 of the present invention is 2.32cm 3 ·m -2 ·day -1 ·atm -1 . It can be seen from the above that the oxygen barrier and water permeable film provided by the present invention can effectively permeate water vapor and has a better water vapor permeation effect.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围。The above is only a preferred embodiment of the present invention, it should be pointed out that, for those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and modifications can also be made, and these improvements and modifications can also be made. It should be regarded as the protection scope of the present invention.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711481631.XA CN108211816B (en) | 2017-12-29 | 2017-12-29 | A kind of oxygen barrier water permeable film and its preparation method and application |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711481631.XA CN108211816B (en) | 2017-12-29 | 2017-12-29 | A kind of oxygen barrier water permeable film and its preparation method and application |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108211816A true CN108211816A (en) | 2018-06-29 |
| CN108211816B CN108211816B (en) | 2019-11-22 |
Family
ID=62647310
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711481631.XA Active CN108211816B (en) | 2017-12-29 | 2017-12-29 | A kind of oxygen barrier water permeable film and its preparation method and application |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108211816B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110867536A (en) * | 2019-11-19 | 2020-03-06 | 电子科技大学 | Multilayer nano film, preparation method thereof and lithium battery |
| CN112844063A (en) * | 2020-12-31 | 2021-05-28 | 浙江工业大学 | Ultrafiltration membrane constructed by high-flux black talc nanosheets and preparation method thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1461189A (en) * | 2001-03-30 | 2003-12-10 | Ooopkf“阿特兰蒂斯-帕克”公司 | Polymer film for food products |
| US20040058173A1 (en) * | 2002-09-24 | 2004-03-25 | Moulton Jeffrey D. | Barrier film with reduced dynamic coefficient of friction |
| CN102597076A (en) * | 2009-11-24 | 2012-07-18 | 花王株式会社 | Filmy material, method for producing same, and aqueous dispersion for forming filmy material |
| CN104788704A (en) * | 2015-05-02 | 2015-07-22 | 北京化工大学 | Preparation of multi-stage structured hydrotalcite and application of multi-stage structured hydrotalcite in gasbarrier packaging material |
| CN104817710A (en) * | 2015-04-30 | 2015-08-05 | 北京化工大学 | Transparent gas barrier film materials and production method thereof |
-
2017
- 2017-12-29 CN CN201711481631.XA patent/CN108211816B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1461189A (en) * | 2001-03-30 | 2003-12-10 | Ooopkf“阿特兰蒂斯-帕克”公司 | Polymer film for food products |
| US20040058173A1 (en) * | 2002-09-24 | 2004-03-25 | Moulton Jeffrey D. | Barrier film with reduced dynamic coefficient of friction |
| CN102597076A (en) * | 2009-11-24 | 2012-07-18 | 花王株式会社 | Filmy material, method for producing same, and aqueous dispersion for forming filmy material |
| CN104817710A (en) * | 2015-04-30 | 2015-08-05 | 北京化工大学 | Transparent gas barrier film materials and production method thereof |
| CN104788704A (en) * | 2015-05-02 | 2015-07-22 | 北京化工大学 | Preparation of multi-stage structured hydrotalcite and application of multi-stage structured hydrotalcite in gasbarrier packaging material |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110867536A (en) * | 2019-11-19 | 2020-03-06 | 电子科技大学 | Multilayer nano film, preparation method thereof and lithium battery |
| CN112844063A (en) * | 2020-12-31 | 2021-05-28 | 浙江工业大学 | Ultrafiltration membrane constructed by high-flux black talc nanosheets and preparation method thereof |
| CN112844063B (en) * | 2020-12-31 | 2022-05-24 | 浙江工业大学 | Ultrafiltration membrane constructed by high-flux black talc nanosheets and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108211816B (en) | 2019-11-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6095654B2 (en) | Method for manufacturing battery components | |
| CN110449032B (en) | A swelling-resistant two-dimensional SA-MXene layered nanofiltration membrane, preparation and application | |
| CN111760461B (en) | Preparation method of polyvinylidene fluoride mixed matrix membrane | |
| CN104785133B (en) | Sodium alginate-zwitterion modified graphene oxide hybrid composite membrane, preparation and application | |
| CN104194022B (en) | A kind of biodegradable high-barrier plastic film material and preparation method thereof | |
| CN105903359A (en) | Chitosan functionalized graphene oxide/polyvinylidene fluoride hybrid ultrafiltration membrane and preparation method thereof | |
| CN112007521A (en) | Preparation method of high-flux composite nanofiltration membrane | |
| CN109647234A (en) | A kind of MOF/ composite membrane of polymer preparation method and applications | |
| CN108211816B (en) | A kind of oxygen barrier water permeable film and its preparation method and application | |
| CN108993168A (en) | A kind of active layer is the organic solvent nanofiltration composite membrane and preparation method thereof of molybdenum disulfide | |
| CN110280147A (en) | A kind of swelling resistance two-dimensional layer film, preparation and application that inter-layer passages size is controllable | |
| CN111330464A (en) | Preparation method of blending modified polysulfone charged nanofiltration membrane and obtained membrane | |
| CN108097058B (en) | A kind of carbon dioxide selective permeation film and its preparation method and application | |
| WO2024168937A1 (en) | Composite membrane, preparation method therefor, and use thereof | |
| US20140315009A1 (en) | Resin composition and method for producing same | |
| CN111804161B (en) | Coated amino acid ionic liquid nanospheres/polymer hybrid membranes for CO separation | |
| CN117504626A (en) | A mixed matrix membrane for CO2 separation and preparation method thereof | |
| CN108993165B (en) | A kind of layered inorganic material organic solvent nanofiltration composite membrane and preparation method thereof | |
| CN103864977B (en) | The preparation method of a kind of many silicon linking agent and the special anionic membrane of diffusion dialysis thereof | |
| CN105617890A (en) | Layer-by-layer self-assembly chitosan positively charged composite nanofiltration membrane and preparation method thereof | |
| CN106943895B (en) | A kind of the flexible bionic bilayer polymer film and preparation method and application of acetone stimuli responsive | |
| CN111375319B (en) | Carbon dioxide separation composite membrane and preparation method and application thereof | |
| CN104525000A (en) | Preparation method of high-selectivity polyvinyl alcohol nanofiltration membrane | |
| CN107022099B (en) | Transparent oxygen-blocking and water-blocking film and preparation method thereof | |
| CN107987300B (en) | Temperature-sensitive 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 |