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CN109880016A - Method for continuous preparation of water-in-oil high internal phase emulsion and polymer porous material - Google Patents

Method for continuous preparation of water-in-oil high internal phase emulsion and polymer porous material Download PDF

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CN109880016A
CN109880016A CN201910004584.2A CN201910004584A CN109880016A CN 109880016 A CN109880016 A CN 109880016A CN 201910004584 A CN201910004584 A CN 201910004584A CN 109880016 A CN109880016 A CN 109880016A
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phase
water
emulsion
porous material
oil
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CN109880016B (en
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章圣苗
周策
朱芸
陈建定
张晓宇
王彦华
乔敏
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East China University of Science and Technology
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East China University of Science and Technology
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Abstract

本发明涉及连续制备油包水型高内相乳液以及聚合物多孔材料的方法。以乳化剂溶于疏水性单体后所得溶液作为油相;以含电解质和引发剂的水溶液作为水相;将油相和水相分别持续加入到双螺杆挤出机中,通过双螺杆剪切作用,让油相和水相充分乳化形成乳液;油相和水相充分乳化形成乳液后,引发剂引发乳液中的疏水性单体,获得具有孔结构,且孔结构形貌可调的聚合物多孔材料。与现有技术相比,本发明方法简单易行,可用于连续生产高内相乳液,并获得具有特殊孔结构多孔材料。

The present invention relates to a method for continuously preparing a water-in-oil type high internal phase emulsion and a polymeric porous material. The solution obtained by dissolving the emulsifier in the hydrophobic monomer is used as the oil phase; the aqueous solution containing the electrolyte and the initiator is used as the water phase; the oil phase and the water phase are continuously added into the twin-screw extruder, and sheared by the twin-screw The oil phase and the water phase are fully emulsified to form an emulsion; after the oil phase and the water phase are fully emulsified to form an emulsion, the initiator initiates the hydrophobic monomer in the emulsion to obtain a polymer with a pore structure and adjustable pore structure and morphology Porous material. Compared with the prior art, the method of the invention is simple and feasible, can be used for continuous production of high internal phase emulsion, and obtains porous materials with special pore structure.

Description

The method for continuously preparing water-in-oil type High Internal Phase Emulsion and polymer porous material
Technical field
The invention belongs to lotion preparation and porous material preparation technical fields, more particularly, to a kind of continuous preparation oil packet The method of water type High Internal Phase Emulsion and polymer porous material.
Background technique
High Internal Phase Emulsion, that is, disperse phase volume accounts for the lotion that total emulsion volume score is more than or equal to 74.05%.It is wide It is general to be applied to food, fuel, oil plant recycling, cosmetics and field of porous materials.High Internal Phase Emulsion is usually by accounting for continuous phase 5- 50% nonionic emulsifier is stabilizer.Also there is nanoparticle to stablize the report of High Internal Phase Emulsion recently.High Internal Phase Emulsion is logical Often under the action of stabilizer, it is prepared by being gradually added dropwise to dispersed phase in the continuous phase in emulsifying.Its emulsifying manner Including mechanical stirring, magnetic agitation, emulsification pretreatment, ultrasonic emulsification etc..However these emulsifying manner are clearance-type, i.e. lotion is One kettle, one kettle or one bottle one bottle preparation, be unfavorable for the stabilization of product emulsion performance.So far, continuous large scale preparation lotion has become For emulsion technology field problem urgently to be resolved.
In recent years, the polymer porous material as made from High Internal Phase Emulsion template is even more because its unique hole is tied The characteristics such as structure, high porosity and low-density, excite wide spread interest in multiple fields, they act not only as microelectronics work The bracket of 3D cell culture, the catalyst in synthesis chemistry and reactant etc. in low-k matrix, organizational project in industry Carrier, be also used as preparing the template of inorganic porous material.During High Internal Phase Emulsion template prepares porous material, Performance between emulsion intercalation method and product emulsion batch is unified particularly significant.
The stability of High Internal Phase Emulsion is emphasis concerned by people, it is influenced by many factors.So far, lotion phase The formation for lotion such as component, emulsifier property and dosage, emulsion dispersion phase volume fraction, preparation temperature, electrolyte concentration And the influence of stability has been reported that more.Surface is studied, in order to stablize High Internal Phase Emulsion, emulsifier allows for quick adsorption Onto liquid-liquid interface, one layer of firm interfacial film is formed, and can be effectively reduced the interfacial tension of two-phase interface in lotion.Cream The stabilization of liquid belongs to dynamic stabilization, it is stabilized by the mutually exclusive power between interior phase drop.Have been generally acknowledged that nonionic Type emulsifier realizes the stabilization of HIPE by the repulsion benefit on spatial position.It is high interior mutually newborn when to prepare stable Water-In-Oil Liquid generally requires a kind of nonionic emulsifier of low hydrophilic lipophilic balance, such as sorbitol monooleate (Span80, HLB= 4.3) etc..In addition, electrolyte also also plays important role in terms of High Internal Phase Emulsion stability.The presence of electrolyte can be with The interaction for weakening emulsifier and aqueous solution makes them in water-oil interface to increase the interaction between emulsifier It arranges more orderly.Therefore water-oil interface film strength can be enhanced in the addition of electrolyte, increases the elasticity modulus of lotion and apparent Yield stress, and then improve emulsion intercalation method.On the other hand, dissolution of the electrolyte also by reduction aqueous solution in oily phase Degree improves the stability of High Internal Phase Emulsion so that Ostwald be inhibited to cure effect.Although the research of High Internal Phase Emulsion is more, But its emulsifying manner is still limited to the production method of the clearance-types such as mechanical stirring, magnetic agitation, emulsification pretreatment, ultrasonic emulsification, no Conducive to the stabilization of product emulsion performance, therefore, continuous large scale preparation emulsion technology is still to be developed.
Chinese patent CN102838774B discloses a kind of total with styrene, acrylic acid, methyl methacrylate three block The water-in-oil type High Internal Phase Emulsion of polymers macromolecular stabilizer is presoma, prepares low-density by being freeze-dried this physics mode The method of polymer porous material.Steps are as follows: styrene, acrylic acid, methyl methacrylate triblock copolymer are added Into organic solvent, stirring and dissolving forms polymer solution, using the solution as oily phase, by certain density electrolyte aqueous solution It is slowly added dropwise in oily phase as water phase, is formed under the action of mechanical stirring and only have the stable water-in-oil type of polymer macromolecule Lotion is directly fixed pattern with liquid nitrogen frozen, then pass through freeze-drying after placing a period of time at room temperature by High Internal Phase Emulsion Low-density polymeric porous material is formed after place to go water and organic solvent.
Chinese patent CN102838773B discloses a kind of total with styrene, acrylic acid, methyl methacrylate three block The stable water-in-oil type High Internal Phase Emulsion of polymers nanoparticle be presoma, by be freeze-dried this physics mode prepare it is ultralow The method of density polymers porous material.Steps are as follows: electrolyte is added to styrene, acrylic acid, methyl methacrylate In triblock copolymer nanoparticle aqueous dispersions, it is used as water phase after matter stirring and dissolving to be electrolysed, is then poured slowly into water phase In oily phase, water-in-oil type High Internal Phase Emulsion is formed under the action of magnetic agitation.Place one section at room temperature to High Internal Phase Emulsion After time, it is freeze-dried to form low-density polymeric porous material.
Chinese patent CN102391416A discloses one kind in inorganic nano-particle titanium dioxide stabilised oil-in-water height Phase emulsion, and the method that hydrophilic polymer porous material is obtained as matrix polymerization using this lotion.Steps are as follows: by water-soluble mono Body, water-soluble cross-linker, electrolyte, initiator are added in the aqueous dispersions of nano-titanium dioxide, and stirring and dissolving is then dripped again Hydrophobic organic solvent is added, stirring forms emulsion oil-in-water.Heating causes monomer reaction in lotion and obtains hydrophilic polymer Object porous material.
Above-mentioned three patents be all study before present inventor about the preparation of water-in-oil type High Internal Phase Emulsion and The related patents of polymer porous material preparation, emulsifying manner of above-mentioned three patents are still limited to the production method of clearance-type, no It can continuous large scale preparation lotion.
On the other hand, from nineteen thirty-five, Italian Roberto Colombo and Carlo Pasqutti is developed respectively first Out in the same direction and counter rotation twin screw extruder after, by more than 80 years continuously improve and it is perfect, double screw extruder has obtained considerable Development, be widely used at present Polymer Processing industry and other industry.Although twin-screw extrusion is in Polymer Processing Be used widely with modified field, but its in the application of lotion preparation field, there is not been reported.
Summary of the invention
It is an object of the present invention to overcome the above-mentioned drawbacks of the prior art and provide a kind of continuous preparation oil packets The method of water type High Internal Phase Emulsion and polymer porous material.
The present invention realizes continuous preparation and the polyalcohol stephanoporate of water-in-oil type High Internal Phase Emulsion using double screw extruder The continuous preparation of material.
The purpose of the present invention can be achieved through the following technical solutions:
Present invention firstly provides a kind of methods that continuous extrusion prepares water-in-oil type High Internal Phase Emulsion, comprising the following steps:
Acquired solution is as oily phase after being dissolved in hydrophobic monomer using emulsifier;
Using the aqueous solution containing electrolyte as water phase;
It is mutually continuously added into oily in double screw extruder feed opening with water phase, by twin-screw shear action, allows respectively Water phase is mutually sufficiently mixed with oil, is emulsified, can be obtained water-in-oil type High Internal Phase Emulsion in discharge outlet.
Further, the emulsifier is selected from one of following substance or a variety of: Span80, Span60, polyglycereol alkene Base succinate or HypermerT96.
Further, the hydrophobic monomer is selected from one of following substance or a variety of: styrene, divinylbenzene, 2-Hydroxyethyl methacrylate, 2-EHA, 2-Ethylhexyl Methacrylate, lauryl acrylate, acrylic acid Tetradecane base ester, lauryl methacrylate, butyl acrylate, methacrylic acid tetradecane base ester, Glycidyl methacrylate Glyceride or ethylene glycol dimethacrylate.
Further, the electrolyte is selected from one or both of sodium chloride or calcium chloride.
Further, mass fraction of the emulsifier in oily phase is 5%~30%.
Further, mass fraction of the electrolyte in water phase is 0.5%~3%.
Further, the oil is mutually continuously added into twin-screw respectively and squeezes with the ratio of water phase 1:40~1:3 by volume Out in machine.
Further, the screw speed of the double screw extruder is 50~350 rpms, and oil is mutually and water phase is in double spiral shells Temperature in bar extruder is controlled at 20~50 DEG C, and preferably 30~40 DEG C.
Further, initiator is also contained in the water phase, the initiator is in potassium peroxydisulfate or ammonium persulfate One or two, the initiator amount are the 1%~3% of hydrophobic monomer quality.
In addition the purpose of initiator is, so that containing initiator in last water-in-oil type High Internal Phase Emulsion, exist in this way Under suitable initiation conditions, the hydrophobic monomer in initiator initiation lotion can use, and then can obtain with pore structure, And the adjustable polymer porous material of pore structure.
The present invention also provides a kind of preparation methods of polymer porous material, comprising the following steps:
Acquired solution is as oily phase after being dissolved in hydrophobic monomer using emulsifier;
Using the aqueous solution containing electrolyte and initiator as water phase;
It is mutually continuously added into oily in double screw extruder feed opening with water phase, by twin-screw shear action, allows respectively Water phase is mutually sufficiently mixed with oil, is emulsified, can be obtained water-in-oil type High Internal Phase Emulsion in discharge outlet;
Oily initiator causes the hydrophobic monomer in lotion mutually and after the fully emulsified formation lotion of water phase, and obtaining has hole Structure, and the adjustable polymer porous material of pore structure.
Further, the initiator is selected from one or both of potassium peroxydisulfate or ammonium persulfate, and the initiator is used Amount is the 1%~3% of hydrophobic monomer quality.
Further, initiator, which causes the condition of the hydrophobic monomer acquisition polymer porous material in lotion, is: by institute It obtains lotion and is heated to 60~90 DEG C, preferably 70~80 DEG C.
Cause the hydrophobic monomer in polymerization High Internal Phase Emulsion, after reaction obtains white solid, uses elution aqueous solvent, second The mixture of alcohol or water and ethyl alcohol washs solid product, and the porous material with certain pore size can be obtained after drying.
Further, the emulsifier is selected from one of following substance or a variety of: Span80, Span60, polyglycereol alkene Base succinate or HypermerT96.
Further, the hydrophobic monomer is selected from one of following substance or a variety of: styrene, divinylbenzene, 2-Hydroxyethyl methacrylate, 2-EHA, 2-Ethylhexyl Methacrylate, lauryl acrylate, acrylic acid Tetradecane base ester, lauryl methacrylate, butyl acrylate, methacrylic acid tetradecane base ester, Glycidyl methacrylate Glyceride or ethylene glycol dimethacrylate.
Further, the electrolyte is selected from one or both of sodium chloride or calcium chloride.
Further, mass fraction of the emulsifier in oily phase is 5%~30%.
Further, mass fraction of the electrolyte in water phase is 0.5%~3%.
Further, the oil is mutually continuously added into twin-screw respectively and squeezes with the ratio of water phase 1:40~1:3 by volume Out in machine.
Further, the screw speed of the double screw extruder is 50~350 rpms, and oil is mutually and water phase is in double spiral shells Temperature in bar extruder is controlled at 20~50 DEG C, and preferably 30~40 DEG C.
The present invention passes through adjusting screw rod revolving speed and barrel temperature, the continuous interior mutually cream of the height for obtaining dispersed phase drop size adjustable Liquid.Method of the invention is simple and easy, is suitble to continuous production, obtains dispersed phase drop size and its adjustable high interior mutually cream of distribution Liquid.
By the dispersed phase drop size of optical microscope inspection High Internal Phase Emulsion, using scanning electron microscope (SEM, S- 3400N, JEOL) pattern of bulk polymer porous material is observed, and it is close to utilize digital display solid body densitometer (EDS-300) to measure its Degree.The quality of bulk polymer open-cell material is measured using the gentle vernier caliper in day respectively and volume and calculates porosity.
The spies such as the dispersed phase drop size of lotion, the aperture of porous material obtained by the method for the present invention, the density of porous material Property have controllability.
The present invention utilizes good charging performance possessed by double screw extruder, mixing plasticizing capacity, extrusion stability The features such as, in conjunction with its positive position conveying characteristic to material, double screw extruder is used in lotion for the first time and is continuously prepared, especially On the lasting emulsifying process of High Internal Phase Emulsion.
Compared with prior art, method of the invention is simple and easy, is suitble to continuous production High Internal Phase Emulsion and its polymer Porous material, while twin-screw extrusion function provides enough dispersions, distributed rendering, better temperature control, and has good Good self-cleaning, therefore, the water-in type High Internal Phase Emulsion and polymer porous material quality of the method for the present invention preparation are higher, work Skill stability is more preferable.
Detailed description of the invention
Fig. 1 is the optical microscope of 1 gained lotion of embodiment;
Fig. 2 is the scanning electron microscope (SEM) photograph of 1 gained porous material of embodiment;
Fig. 3 is the optical microscope of 2 gained lotion of embodiment;
Fig. 4 is the scanning electron microscope (SEM) photograph of 2 gained porous material of embodiment;
Fig. 5 is the optical microscope of 3 gained lotion of embodiment;
Fig. 6 is the scanning electron microscope (SEM) photograph of 3 gained porous material of embodiment;
Fig. 7 is the optical microscope of 4 gained lotion of embodiment;
Fig. 8 is the scanning electron microscope (SEM) photograph of 4 gained porous material of embodiment.
Specific embodiment
The present invention is described in detail with specific embodiment below in conjunction with the accompanying drawings.
Embodiment 1
To weigh 100 grams of Spans 80, it is added in the mixture of 1600 grams of styrene and 400 grams of divinylbenzenes, gained has Machine solution is oily phase.It weighs 300 grams of sodium chloride and 100 grams of potassium peroxydisulfates is added in 8000 grams of distilled water, acquired solution is Water phase.30 DEG C mutually are separately heated to water phase by oily, then oil is mutually and water phase is according to the feed rate of volume ratio 1:3, passes through perseverance Stream pump is added in the double screw extruder that cylinder temperature is arranged in 30 DEG C, twin-screw revolving speed is 350 rpms.Water phase is mutually passed through with oil Cross twin-screw shearing after, at extruder discharging mouth out be High Internal Phase Emulsion.Gained High Internal Phase Emulsion is heated to 70 DEG C, Cause the monomer in polymerization High Internal Phase Emulsion, reaction obtains white solid, uses elution aqueous solvent, ethyl alcohol or their mixture Solid product is washed, arrives the porous material with certain pore size after drying.
By the dispersed phase drop size of optical microscope inspection High Internal Phase Emulsion, High Internal Phase Emulsion obtained by the present embodiment Optical microscope is as shown in Figure 1, as can be seen from FIG. 1, the resulting lotion of the present embodiment divides aqueous phase droplets average diameter to be 48 Micron.
Using the pattern of scanning electron microscope (SEM, S-3400N, JEOL) observation porous material, the present embodiment gained porous material Scanning electron microscope (SEM) photograph as shown in Fig. 2, can be calculated according to fig. 2, the aperture of resulting porous material is 47 microns.
The quality of gained porous material is measured using the gentle vernier caliper in day respectively and volume and calculates porosity, this reality The porosity for applying the resulting porous material of example is 77%.
Embodiment 2
To weigh 600 grams of Spans 60,1600 grams of 2-Hydroxyethyl methacrylate and 400 ethylene glycol dimethacrylates are added In the mixture of ester, gained organic solution is oily phase.It weighs 300 grams of sodium chloride and 300 grams of potassium peroxydisulfates is added to 10000 grams In distilled water, acquired solution is water phase.30 DEG C mutually are separately heated to water phase by oily, then oil is mutually and water phase is according to volume ratio 1: 4 feed rate is added to the twin-screw that cylinder temperature is arranged in 30 DEG C, twin-screw revolving speed is 100 rpms by constant flow pump and squeezes Out in machine.Water phase and oil mutually after twin-screw is sheared, at extruder discharging mouth out be High Internal Phase Emulsion.By gained height Internal phase emulsions are heated to 70 DEG C, cause the monomer in polymerization High Internal Phase Emulsion, and reaction obtains white solid, use elution solvent Water, ethyl alcohol or their mixture wash solid product, arrive the porous material with certain pore size after drying.
By the dispersed phase drop size of optical microscope inspection High Internal Phase Emulsion, High Internal Phase Emulsion obtained by the present embodiment Optical microscope is as shown in figure 3, as can be seen from FIG. 3, the resulting lotion of the present embodiment divides aqueous phase droplets average diameter to be 25 Micron.
Using the pattern of scanning electron microscope (SEM, S-3400N, JEOL) observation porous material, the present embodiment gained porous material Scanning electron microscope (SEM) photograph as shown in figure 4, can be calculated according to Fig. 4, the aperture of resulting porous material is 27 microns.
The quality of gained porous material is measured using the gentle vernier caliper in day respectively and volume and calculates porosity, this reality The porosity for applying the resulting porous material of example is 82%.
Embodiment 3
To weigh 200 grams of polyglycereol alkenyl succinic acid esters and 100 grams of HypermerT96,1600 grams of acrylic acid 2- second are added In the mixture of the own ester of base and 400 grams of divinylbenzenes, gained organic solution is oily phase.Weigh 200 grams of sodium chloride and 300 grams of mistakes Potassium sulfate is added in 10000 grams of distilled water, and acquired solution is water phase.30 DEG C mutually are separately heated to water phase by oily, then Oily phase and water phase are added to cylinder temperature by constant flow pump and are arranged in 30 DEG C, twin-screw revolving speed according to the feed rate of volume ratio 1:40 For in 150 rpms of double screw extruders.Water phase and oil are mutually after twin-screw is sheared, at extruder discharging mouth out It is High Internal Phase Emulsion.Gained High Internal Phase Emulsion is heated to 70 DEG C, causes the monomer in polymerization High Internal Phase Emulsion, reaction obtains White solid washs solid product using elution aqueous solvent, ethyl alcohol or their mixture, certain to having after drying The porous material in aperture.
By the dispersed phase drop size of optical microscope inspection High Internal Phase Emulsion, High Internal Phase Emulsion obtained by the present embodiment Optical microscope is as shown in figure 5, as can be seen from FIG. 5, the resulting lotion of the present embodiment divides aqueous phase droplets average diameter to be 74 Micron.
Using the pattern of scanning electron microscope (SEM, S-3400N, JEOL) observation porous material, the present embodiment gained porous material Scanning electron microscope (SEM) photograph as shown in fig. 6, can be calculated according to Fig. 6, the aperture of resulting porous material is 68 microns.
The quality of gained porous material is measured using the gentle vernier caliper in day respectively and volume and calculates porosity, this reality The porosity for applying the resulting porous material of example is 96%.
Embodiment 4
To weigh 400 grams of Spans 80,1600 grams of glycidyl methacrylate and 400 grams of dimethacrylate second are added In the mixture of diol ester, gained organic solution is oily phase.It weighs 50 grams of sodium chloride and 100 grams of potassium peroxydisulfates is added to 10000 Gram distilled water in, acquired solution is water phase.30 DEG C mutually are separately heated to water phase by oily, then oil is mutually and water phase is according to volume Feed rate than 1:5 is added to the twin-screw that cylinder temperature is arranged in 30 DEG C, twin-screw revolving speed is 50 rpms by constant flow pump In extruder.Water phase and oil mutually after twin-screw is sheared, at extruder discharging mouth out be High Internal Phase Emulsion.By gained High Internal Phase Emulsion is heated to 70 DEG C, causes the monomer in polymerization High Internal Phase Emulsion, and reaction obtains white solid, uses elution solvent Water, ethyl alcohol or their mixture wash solid product, arrive the porous material with certain pore size after drying.
By the dispersed phase drop size of optical microscope inspection High Internal Phase Emulsion, High Internal Phase Emulsion obtained by the present embodiment Optical microscope is as shown in fig. 7, as can be seen from FIG. 7, the resulting lotion of the present embodiment divides aqueous phase droplets average diameter to be 30 Micron.
Using the pattern of scanning electron microscope (SEM, S-3400N, JEOL) observation porous material, the present embodiment gained porous material Scanning electron microscope (SEM) photograph as shown in figure 8, can be calculated according to Fig. 8, the aperture of resulting porous material is 32 microns.
The quality of gained porous material is measured using the gentle vernier caliper in day respectively and volume and calculates porosity, this reality The porosity for applying the resulting porous material of example is 81%.
The above description of the embodiments is intended to facilitate ordinary skill in the art to understand and use the invention. Person skilled in the art obviously easily can make various modifications to these embodiments, and described herein general Principle is applied in other embodiments without having to go through creative labor.Therefore, the present invention is not limited to the above embodiments, ability Field technique personnel announcement according to the present invention, improvement and modification made without departing from the scope of the present invention all should be of the invention Within protection scope.

Claims (10)

1.一种连续挤出制备油包水型高内相乳液的方法,其特征在于,包括以下步骤:1. a method for preparing water-in-oil type high internal phase emulsion by continuous extrusion, is characterized in that, comprises the following steps: 以乳化剂溶于疏水性单体后所得溶液作为油相;The solution obtained after the emulsifier is dissolved in the hydrophobic monomer is used as the oil phase; 以含电解质的水溶液作为水相;The aqueous solution containing electrolyte is used as the water phase; 将油相和水相分别持续加入到双螺杆挤出机中,通过双螺杆剪切作用,让油相和水相充分乳化形成乳液。The oil phase and the water phase are continuously added to the twin-screw extruder, and the oil phase and the water phase are fully emulsified to form an emulsion through the shearing action of the twin-screw. 2.根据权利要求1所述的一种连续挤出制备油包水型高内相乳液的方法,其特征在于,所述乳化剂选自以下物质中的一种或多种:Span80、Span60、聚甘油烯基丁二酸酯或HypermerT96;2. a kind of method for preparing water-in-oil high internal phase emulsion by continuous extrusion according to claim 1, is characterized in that, described emulsifier is selected from one or more in following material: Span80, Span60, Polyglyceryl alkenyl succinate or Hypermer T96; 所述疏水性单体选自以下物质中的一种或多种:苯乙烯、二乙烯基苯、甲基丙烯酸2-羟乙酯、丙烯酸2-乙基己酯、甲基丙烯酸2-乙基己酯、丙烯酸月桂酯、丙烯酸十四烷基酯、甲基丙烯酸月桂酸酯、丙烯酸丁酯、甲基丙烯酸十四烷基酯、甲基丙烯酸缩水甘油酯或二甲基丙烯酸乙二醇酯。The hydrophobic monomer is selected from one or more of the following: styrene, divinylbenzene, 2-hydroxyethyl methacrylate, 2-ethylhexyl acrylate, 2-ethyl methacrylate Hexyl, lauryl acrylate, myristyl acrylate, laurate methacrylate, butyl acrylate, myristyl methacrylate, glycidyl methacrylate or ethylene glycol dimethacrylate. 3.根据权利要求1所述的一种连续挤出制备油包水型高内相乳液的方法,其特征在于,所述乳化剂在油相中的质量分数为5%~30%,所述电解质在水相中的质量分数为0.5%~3%,所述油相和水相按体积比1:40~1:3的比例分别持续加入到双螺杆挤出机中。3. The method for preparing a water-in-oil high internal phase emulsion by continuous extrusion according to claim 1, wherein the mass fraction of the emulsifier in the oil phase is 5% to 30%, and the The mass fraction of the electrolyte in the water phase is 0.5% to 3%, and the oil phase and the water phase are continuously added to the twin-screw extruder in a volume ratio of 1:40 to 1:3, respectively. 4.根据权利要求1所述的一种连续挤出制备油包水型高内相乳液的方法,其特征在于,所述双螺杆挤出机的螺杆转速为50~350转每分钟,油相和水相在双螺杆挤出机中的温度控制在20~50℃。4. a kind of method for preparing water-in-oil high internal phase emulsion by continuous extrusion according to claim 1, is characterized in that, the screw speed of described twin-screw extruder is 50~350 revolutions per minute, oil phase The temperature of the water phase and the water phase in the twin-screw extruder is controlled at 20-50°C. 5.根据权利要求1所述的一种连续挤出制备油包水型高内相乳液的方法,其特征在于,所述水相中还含有引发剂,所述引发剂选自过硫酸钾或过硫酸铵中的一种或两种,所述引发剂用量为疏水性单体质量的1%~3%。5. a kind of method for preparing water-in-oil high internal phase emulsion by continuous extrusion according to claim 1, is characterized in that, also contains initiator in described water phase, and described initiator is selected from potassium persulfate or One or two kinds of ammonium persulfate, and the dosage of the initiator is 1% to 3% of the mass of the hydrophobic monomer. 6.一种聚合物多孔材料的制备方法,其特征在于,6. a preparation method of polymer porous material, is characterized in that, 以乳化剂溶于疏水性单体后所得溶液作为油相;The solution obtained after the emulsifier is dissolved in the hydrophobic monomer is used as the oil phase; 以含电解质和引发剂的水溶液作为水相;The aqueous solution containing electrolyte and initiator is used as the water phase; 将油相和水相分别持续加入到双螺杆挤出机中,通过双螺杆剪切作用,让油相和水相充分乳化形成乳液;The oil phase and the water phase are continuously added to the twin-screw extruder, and the oil phase and the water phase are fully emulsified to form an emulsion through the shearing action of the twin-screw; 油相和水相充分乳化形成乳液后,引发剂引发乳液中的疏水性单体,获得具有孔结构,且孔结构可调的聚合物多孔材料。After the oil phase and the water phase are sufficiently emulsified to form an emulsion, the initiator initiates the hydrophobic monomer in the emulsion to obtain a polymer porous material with pore structure and adjustable pore structure. 7.根据权利要求1所述的一种聚合物多孔材料的制备方法,其特征在于,所述乳化剂在油相中的质量分数为5%~30%,所述电解质在水相中的质量分数为0.5%~3%,所述油相和水相按体积比1:40~1:3的比例分别持续加入到双螺杆挤出机中,所述引发剂用量为疏水性单体质量的1%~3%。7 . The method for preparing a polymer porous material according to claim 1 , wherein the mass fraction of the emulsifier in the oil phase is 5% to 30%, and the mass fraction of the electrolyte in the water phase is 5% to 30% . The fraction is 0.5% to 3%, the oil phase and the water phase are continuously added to the twin-screw extruder in a volume ratio of 1:40 to 1:3, and the amount of the initiator is 30% of the mass of the hydrophobic monomer. 1% to 3%. 8.根据权利要求6所述一种聚合物多孔材料的制备方法,其特征在于,所述引发剂选自过硫酸钾或过硫酸铵中的一种或两种;8. The preparation method of a polymeric porous material according to claim 6, wherein the initiator is selected from one or both of potassium persulfate or ammonium persulfate; 所述电解质选自氯化钠或氯化钙中的一种或两种;The electrolyte is selected from one or both of sodium chloride or calcium chloride; 所述乳化剂选自以下物质中的一种或多种:Span80、Span60、聚甘油烯基丁二酸酯或HypermerT96;The emulsifier is selected from one or more of the following substances: Span80, Span60, polyglyceryl alkenyl succinate or HypermerT96; 所述疏水性单体选自以下物质中的一种或多种:苯乙烯、二乙烯基苯、甲基丙烯酸2-羟乙酯、丙烯酸2-乙基己酯、甲基丙烯酸2-乙基己酯、丙烯酸月桂酯、丙烯酸十四烷基酯、甲基丙烯酸月桂酸酯、丙烯酸丁酯、甲基丙烯酸十四烷基酯、甲基丙烯酸缩水甘油酯或二甲基丙烯酸乙二醇酯。The hydrophobic monomer is selected from one or more of the following: styrene, divinylbenzene, 2-hydroxyethyl methacrylate, 2-ethylhexyl acrylate, 2-ethyl methacrylate Hexyl, lauryl acrylate, myristyl acrylate, laurate methacrylate, butyl acrylate, myristyl methacrylate, glycidyl methacrylate or ethylene glycol dimethacrylate. 9.根据权利要求6所述的一种聚合物多孔材料的制备方法,其特征在于,所述双螺杆挤出机的螺杆转速为50~350转每分钟,油相和水相在双螺杆挤出机中的温度控制在20~50℃。9 . The method for preparing a polymer porous material according to claim 6 , wherein the screw speed of the twin-screw extruder is 50-350 rpm, and the oil phase and the water phase are extruded in the twin-screw extruder. 10 . The temperature in the discharge machine is controlled at 20 to 50 °C. 10.根据权利要求6所述的一种聚合物多孔材料的制备方法,其特征在于,引发剂引发乳液中的疏水性单体获得聚合物多孔材料的条件是:将所得乳液加热至60~90℃。10 . The method for preparing a polymer porous material according to claim 6 , wherein the conditions for obtaining the polymer porous material by initiating the hydrophobic monomer in the emulsion by the initiator are: heating the obtained emulsion to a temperature of 60-90 ℃. 11 . °C.
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