WO2019148577A1 - Method for preparing microcapsule containing pure polyamine and microdroplet forming device thereof - Google Patents
Method for preparing microcapsule containing pure polyamine and microdroplet forming device thereof Download PDFInfo
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- WO2019148577A1 WO2019148577A1 PCT/CN2018/078099 CN2018078099W WO2019148577A1 WO 2019148577 A1 WO2019148577 A1 WO 2019148577A1 CN 2018078099 W CN2018078099 W CN 2018078099W WO 2019148577 A1 WO2019148577 A1 WO 2019148577A1
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- polyamine
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/06—Making microcapsules or microballoons by phase separation
- B01J13/14—Polymerisation; cross-linking
- B01J13/16—Interfacial polymerisation
Definitions
- the invention belongs to the field of microencapsulation, and in particular to a method for preparing microcapsules containing pure polyamines and a microdroplet device thereof.
- the microencapsulation technique is a technique for producing microcapsules containing a protective shell material and various functional core materials that are wrapped. These core materials become solid before being wrapped, and they become solid after being wrapped, so the use and disposal of these materials is more convenient after microencapsulation. When the substance is wrapped, it is isolated from the environment, which reduces its volatilization, masks its odor, enhances its stability, protects its active ingredients, and controls its release. Microencapsulation technology has been extensively and deeply studied by the academic community since its invention, and it has also been widely used in industry. Microcapsules can perform different functions depending on the permeability of the capsule wall.
- the microcapsules can be used to store various functional substances, such as repair liquid (US6518330B2), phase change energy storage material, flame retardant, etc.; and when the microcapsule wall has In the case of modulating permeability, it can be used as a carrier for sustained release or controlled release, such as drugs, antifouling agents, corrosion inhibitors and the like.
- repair liquid US6518330B2
- phase change energy storage material phase change energy storage material
- flame retardant etc.
- modulating permeability it can be used as a carrier for sustained release or controlled release, such as drugs, antifouling agents, corrosion inhibitors and the like.
- microencapsulation techniques In order to meet the demand for the preparation of microcapsules containing different functions, various microencapsulation techniques have been developed over the past few decades.
- the conventional microencapsulation method can be roughly classified into three types according to the difference in the manner of generating small droplets/small particles for wrapping and the manner of forming the shell material, that is, physical methods, physicochemical compounding methods, and chemical methods. Among them, in-situ polymerization and interfacial polymerization are the two methods used most in the chemical method.
- the droplets in the emulsion can be
- the shell monomer in the system is encapsulated by polymer deposition on the oil/water interface.
- organic polyamines are widely used as curing agents or chain extenders for epoxy resins, polyureas, nylons, and the like.
- organic polyamines can be dissolved in most polar or weakly polar solvents, such as water, benzene, toluene, and the like. Therefore, there is no way to emulsify a pure organic polyamine in a solvent to form a stable emulsion.
- organic polyamines can react with many of the shell monomers used today or can affect their reaction, this high activity is also a reason for their microcapsules being very challenging.
- the researchers In addition to the use of hollow tubes to load polyamines to prepare self-healing materials, the researchers also prepared various other carriers to load polyamine curing agents, such as hollow polyurea resin (PUF) microcapsules, hollow glass beads (US9522843B2), and Hollow polypropylene cyanide nanofibers. After the preparation of these microcarriers, the polyamine-based curing agent is then loaded in these carriers. During the loading process, depending on the actual situation, you can choose to use vacuum to speed up the loading process. Although the above methods can be used to load polyamines for self-healing purposes, these methods are relatively complex. Li (Li) and others claimed that they successfully wrapped the polyether polyamine, Jeffamine D230, by solvent evaporation.
- the two-component epoxy-amine self-repairing system based on the microcapsules and epoxy microcapsules showed a good repairing effect in the self-repairing epoxy resin.
- the content of amine in the finally obtained microcapsules is very low. After optimizing the wrapping conditions, the highest content is only about 20% by weight.
- researchers also used the Pickering emulsion method to encapsulate pure polyamines. Although microspheres containing polyamines were prepared, they obtained solid microspheres rather than microcapsules having a core-shell structure. At the same time, they did not further prepare self-healing materials based on such microcapsules to verify the applicability of the prepared pure polyamine-containing microcapsules.
- Li (Li) et al. and Yi et al. successfully encapsulated aqueous solutions of polyamines rather than pure polyamines. Since the microcapsule wall prepared by this method is very fragile, these researchers did not even remove the water in the microcapsule before further use of the microcapsule.
- Chen et al. successfully encapsulated aqueous solutions of diethylenetriamine (DETA) and triethylenetetramine (TETA) using a second complex emulsion produced by a very complex and sophisticated microfluidic device. Through the fine control of the microencapsulation process, this method can prepare microcapsules with uniform dimensions and uniform thickness of the capsule wall.
- DETA diethylenetriamine
- TETA triethylenetetramine
- the thermal stability of the polyacrylic acid capsule wall used is relatively good, the water in the capsule can be completely removed using a vacuum. Nevertheless, since the capsule wall of the capsule is thick and the original capsule contains a large proportion of moisture, the polyamine content in the final microcapsule is relatively low. In addition, self-healing epoxy resins prepared using such microcapsules are less than ideal for repairing fracture toughness because of the relatively high epoxy crosslink density cured using DETA or TETA.
- the object of the present invention is to overcome the above problems and to provide a method for preparing microcapsules containing pure polyamines and a microdroplet device thereof, which can complete the preparation of pure polyamine microcapsules and provide a preparation for pure polyamines.
- a new method and a corresponding micro-dropletization device can well complete the micro-dropletization of pure polyamines.
- a method of preparing microcapsules containing pure polyamines comprising the following preparation steps:
- the reaction solution described in the step (1) is a mixture of a diisocyanate monomer/prepolymer, a surfactant, a catalyst, and a nonpolar or weakly polar solvent which is insoluble or only slightly soluble in the polyamine.
- the weight ratio of diisocyanate monomer/prepolymer, surfactant and catalyst in each solute is 4-8:0.05-1:0-1, and each solute is insoluble or only slightly soluble in polyamine at 50ml.
- the non-polar or weakly polar solvent is combined, and the configured reaction solution is placed in a normal temperature environment and stirred at a rate of 80-180 r/min.
- the diisocyanate monomer/prepolymer includes any one or more of hexamethylene diisocyanate, 4,4′-dicyclohexylmethane diisocyanate, isophorone diisocyanate, and toluene diisocyanate.
- the composition may be formed by any one of hexamethylene diisocyanate, 4,4'-dicyclohexylmethane diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate or toluene diisocyanate. a prepolymer dissolved in the reaction solution;
- the surfactant is selected to be a surfactant capable of promoting the formation of an inverse emulsion
- the catalyst comprises any one of triethylenediamine, 2,4,6-tris(dimethylaminomethyl)phenol or dibutyltin dilaurate capable of promoting the reaction of a polyamine with an isocyanate monomer/prepolymer;
- Non-polar or weakly polar solvents which are insoluble or only slightly soluble in polyamines include liquid aliphatic hydrocarbons having from 6 to 18 carbon atoms, cycloalkanes such as cyclohexane, cycloheptane, cyclooctane, cyclodecane. Any one or a mixture of any one or more of decalin.
- the micro-droplet treatment in the step (2) is performed by using a micro-droplet device;
- the polyamine includes any one of an ethylenediamine polycondensate, a polyether amine, a fatty amine, a polyacrylamine, and an aromatic amine.
- the polyamine includes any one of an ethylenediamine polycondensate, a polyether amine, a fatty amine, a polyacrylamine, and an aromatic
- the heating method in step (3) is:
- step (4) The cleaning process in step (4) is:
- a cleaning agent is added to the preliminary microcapsules, and the mixture is stirred uniformly, and then allowed to stand until the solid precipitates, and the supernatant is removed, and the cleaning agent is repeatedly added for cleaning 3-6 times until the supernatant is clarified; Then, the clarified supernatant is removed, and the washed microcapsules are placed in the air until the cleaning agent is completely volatilized to obtain pure microcapsules;
- the cleaning agent is a non-polar solvent, and the most preferred cleaning agent is pure cyclohexane.
- a micro-dropleting device for preparing microcapsules containing pure polyamines comprising a crude Teflon tube, inserted into a fine Teflon tube at any position except the ends of the first and last ends of the Teflon tube, and separately connected thereto Pumping device on the thick Teflon tube and the fine Teflon tube; wherein the pumping device connected to the thick Teflon tube is used for pumping out the co-current phase, and pumping out with the fine Teflon tube
- the device uses and pumps out a polyamine.
- the number of the fine Teflon tubes is one or more, and each of the fine Teflon tubes is independently connected with a pumping device, and the pumping device is a syringe or a metering pump;
- the phase is a solution in which a surfactant and a nonpolar or weakly polar solvent which is insoluble or only slightly soluble in the polyamine are mixed in a weight-to-volume ratio of 0.05-1 g: 50 ml.
- a micro-dropleting device for preparing microcapsules containing pure polyamines comprising a pumping device, a flat metal needle connected to the pumping device and vertically disposed, a metal conductor disposed directly below the flat metal needle, and a positive electrode
- a high-voltage power supply is connected between the flat metal needles and the negative electrode and the metal conductor; the distance between the flat metal needle and the metal conductor is 10-50 cm, and the voltage of the high-voltage power source is 5-15 KV.
- a micro-dropletting device for preparing microcapsules containing pure polyamines comprising a pressure tank with two conduits inserted at the top, one of which extends into the bottom of the pressure tank and the other conduit is placed on top of the pressure tank An atomizing nozzle connected to a conduit extending into the bottom of the pressure tank, and a gas cylinder connected to a conduit disposed at the top of the pressure tank; wherein the compressed gas in the gas cylinder is any non-acid gas.
- the present invention has the following advantages and beneficial effects:
- the method of the invention provides a brand-new idea, breaks through the bottleneck of the existing polyamine microcapsules, can well complete the production of pure polyamine microcapsules, and promotes the development of enterprises and industries. .
- the micro-dropletization device of the present invention has three different composition structures, and provides different setting modes for the enterprise, thereby facilitating selection according to actual needs during use, and greatly improving the flexibility of product use.
- Figure 1 is a schematic view showing the structure of a first micro-dropletizing apparatus of the present invention.
- FIG. 2 is a schematic view showing the structure of a second micro-dropleting device of the present invention.
- Fig. 3 is a schematic view showing the structure of a third micro-dropleting device of the present invention.
- This embodiment discloses a method for preparing a microcapsule containing a pure polyamine, comprising the following preparation steps:
- the reaction solution is prepared by mixing a diisocyanate monomer/prepolymer, a surfactant, a catalyst, and a non-polar or weakly polar solvent which cannot dissolve or only dissolve a polyamine in a small amount, wherein each solute has two
- the weight ratio of isocyanate monomer/prepolymer, surfactant and catalyst is 6:0.05:0, and each solute is matched with 50ml of non-polar or weakly polar solvent which cannot dissolve or only dissolve the polyamine in a small amount.
- the configured reaction solution was placed in a normal temperature environment and stirred at a rate of 80-180 r/min.
- the catalyst may not be used, that is, when the weight ratio of the catalyst therein is zero.
- the use of the catalyst is to further increase the formation speed of the outer shell of the polyamine droplets after entering the reaction solution, thereby further ensuring the rapid formation of the microcapsules.
- the diisocyanate monomer/prepolymer includes any one or more of hexamethylene diisocyanate, 4,4′-dicyclohexylmethane diisocyanate, isophorone diisocyanate, and toluene diisocyanate.
- the composition may be formed by any one of hexamethylene diisocyanate, 4,4'-dicyclohexylmethane diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate or toluene diisocyanate. a prepolymer dissolved in the reaction solution;
- the surfactant is selected to be a surfactant capable of promoting the formation of an inverse emulsion which is a polyoxyethylene polyhydroxystearate or a sorbitan fatty acid ester, the most preferred being span 80.
- the catalyst comprises any one of triethylenediamine, 2,4,6-tris(dimethylaminomethyl)phenol or dibutyltin dilaurate capable of promoting the reaction of a polyamine with an isocyanate monomer/prepolymer;
- Non-polar or weakly polar solvents which are insoluble or only slightly soluble in polyamines include liquid aliphatic hydrocarbons having from 6 to 18 carbon atoms, cycloalkanes such as cyclohexane, cycloheptane, cyclooctane, cyclodecane. Any one or a mixture of any one or more of decalin.
- the micro-droplet treatment is performed by using a micro-droplet device;
- the polyamine includes any one or more of an ethylenediamine polycondensate, a polyether amine, a fatty amine, a polyacrylamide, and an aromatic amine. mixture.
- the shell encloses the inner pure polyamine to prevent the internal polyamine from continuing to react with the diisocyanate monomer/prepolymer, thereby forming the desired polyamine microcapsules.
- the heating method is:
- the cleaning process is:
- a cleaning agent is added to the preliminary microcapsules, and the mixture is stirred uniformly, and then allowed to stand until the solid precipitates, and the supernatant is removed, and the cleaning agent is repeatedly added for cleaning 3-6 times until the supernatant is clarified; Then, the clarified supernatant is removed, and the washed microcapsules are placed in the air until the cleaning agent is completely volatilized to obtain pure microcapsules;
- the cleaning agent is a non-polar solvent, and the most preferred cleaning agent is pure cyclohexane.
- the content of the amine in the microcapsules produced by the method is about 80% by weight, and the thermal stability of the shell of the microcapsules is relatively good, and the thermal decomposition temperature is above 200 degrees Celsius.
- Embodiment 1 differs from Embodiment 1 only in that:
- the weight ratio of diisocyanate monomer/prepolymer, surfactant to catalyst in each solute was 8:1:1.
- the stirring speed at the time of heating the reaction solution to which the polyamine droplets were added was 250 r/min.
- Embodiment 1 differs from Embodiment 1 only in that:
- the weight ratio of the diisocyanate monomer/prepolymer, surfactant and catalyst in each solute was 6:0.6:0.5.
- the stirring speed at the time of heating the reaction solution to which the polyamine droplets were added was 225 r/min.
- this embodiment discloses a micro-dropleting device for preparing microcapsules containing pure polyamines, including a thick Teflon tube 2, inserted into the crude Teflon tube 2 except for the ends of the first and last ends. a fine Teflon tube 3, and a pumping device 1 separately connected to the thick Teflon tube 2 and the fine Teflon tube 3; wherein, the pumping device 1 connected to the thick Teflon tube 2 The pumping device 1 for pumping out the co-current phase and connected to the fine Teflon tube 3 is used to pump out the polyamine.
- the number of the fine Teflon tubes 3 is one or more, and each of the fine Teflon tubes 3 is independently connected with a pumping device 1 , and the pumping device 1 is a syringe or a metering pump;
- the flow phase is a solution in which a surfactant and a nonpolar or weakly polar solvent which is insoluble or only slightly soluble in the polyamine are mixed in a weight-to-volume ratio of 0.05-1 g: 50 ml.
- the liquid flow rate in the crude Teflon tube and the fine Teflon tube is controlled by the pumping device, and during the pumping process, the liquid flow rate in the crude Teflon tube is greater than that in the fine Teflon tube.
- the flow rate is such that the polyamine can become a microdroplet during the flow.
- a micro-dropleting device for preparing microcapsules containing pure polyamines includes a pumping device 1, a flat metal needle 4 connected to the pumping device 1 and vertically disposed, and disposed at the flat metal a metal conductor 6 directly under the needle 4, and a high-voltage power source 5 in which the positive-electrode metal needle 4 is connected and the negative electrode is connected to the metal conductor 6; the distance between the flat metal needle 4 and the metal conductor 6 is 10-50 cm, and the high voltage The voltage of the power source 5 is 5-15 KV.
- the polyamine will be charged when passing through the flat metal needle, and will approach the metal conductor under the action of the electric field, and then drip into the carrier disposed above the metal conductor to form microcapsules.
- the upper planar area of the metal conductor can be changed.
- the size of the microdroplets it can be done by adjusting the pumping speed or the voltage value of the high voltage power supply.
- a micro-dropleting apparatus for preparing microcapsules containing pure polyamines includes a pressure tank 8 with two conduits inserted at the top, one of which extends into the bottom of the pressure tank 8, and the other The conduit is disposed at the top of the pressure tank 8, an atomizing nozzle 9 connected to the conduit extending into the bottom of the pressure tank 8, and a gas cylinder 7 connected to the conduit disposed at the top of the pressure tank 8; wherein the gas tank 7
- the compressed gas is any non-acid gas.
- the compressed gas in the gas tank adopts a non-acid gas, which can ensure that the gas does not react with the polyamine, thereby ensuring the purity of the polyamine.
- the polyamine enters the atomizing nozzle through a conduit under the pressure of air pressure, and is micro dropletized by the atomizing nozzle.
- the size of the microdroplets can be changed by adjusting the size of the atomizing nozzle and the pressure of the cylinder.
- the present invention can be well implemented.
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Abstract
Description
本发明属于微胶囊化领域,具体是指一种制备含纯多元胺的微胶囊的方法及其微液滴化装置。The invention belongs to the field of microencapsulation, and in particular to a method for preparing microcapsules containing pure polyamines and a microdroplet device thereof.
微胶囊化技术是一种制造含有保护性壳材和被包裹的各种不同功能芯材的微胶囊的技术。这些芯材无论在被包裹之前是什么形态,被包裹之后就变成了固态,因此微胶囊化之后对这些物质的使用和处置都会更加方便。物质被包裹起来后,其与外界环境隔绝,这样能减少其挥发,遮掩其气味,增强其稳定性,保护其活性成分,以及控制其释放。微胶囊化技术自其被发明以来就已经被学术界进行了广泛且深入地研究,同时其在工业界也被广泛地应用。根据囊壁通透性的不同,微胶囊可以发挥不同的功能。当微胶囊囊壁密封性比较好的时候,微胶囊可以用来存储各种不同功能的物质,如修复液(US6518330B2),相变储能材料,阻燃剂等;而当微胶囊囊壁具有可以调控的通透性的时候,其可以用作缓释或可控释放的载体,释放诸如药物、防污剂、缓蚀剂等。The microencapsulation technique is a technique for producing microcapsules containing a protective shell material and various functional core materials that are wrapped. These core materials become solid before being wrapped, and they become solid after being wrapped, so the use and disposal of these materials is more convenient after microencapsulation. When the substance is wrapped, it is isolated from the environment, which reduces its volatilization, masks its odor, enhances its stability, protects its active ingredients, and controls its release. Microencapsulation technology has been extensively and deeply studied by the academic community since its invention, and it has also been widely used in industry. Microcapsules can perform different functions depending on the permeability of the capsule wall. When the microcapsule wall is relatively tight, the microcapsules can be used to store various functional substances, such as repair liquid (US6518330B2), phase change energy storage material, flame retardant, etc.; and when the microcapsule wall has In the case of modulating permeability, it can be used as a carrier for sustained release or controlled release, such as drugs, antifouling agents, corrosion inhibitors and the like.
为了满足制备含有不同功能微胶囊的需求,在过去几十年里已经开发出了各种不同的微胶囊化技术。根据产生用于包裹的小液滴/小颗粒方式的不同及生成壳材方式的不同,传统的微胶囊化方法可以大致分为三类,即物理方法、物理化学复合法和化学方法。其中原位聚合和界面聚合是化学法中被使用得最多的两种方法,在这两种方法中,不管是水包油还是油包水,当形成稳定的乳液之后,乳液中的液滴可以被体系中形壳单体经聚合沉积于油/水界面而被包裹起来。In order to meet the demand for the preparation of microcapsules containing different functions, various microencapsulation techniques have been developed over the past few decades. The conventional microencapsulation method can be roughly classified into three types according to the difference in the manner of generating small droplets/small particles for wrapping and the manner of forming the shell material, that is, physical methods, physicochemical compounding methods, and chemical methods. Among them, in-situ polymerization and interfacial polymerization are the two methods used most in the chemical method. In these two methods, whether it is oil-in-water or water-in-oil, when a stable emulsion is formed, the droplets in the emulsion can be The shell monomer in the system is encapsulated by polymer deposition on the oil/water interface.
然而,迄今虽说微胶囊化包裹技术已经非常多样化了,但是还是有些物质没有办法用现存的方法来包裹,比如说多元胺。作为含有两个或两个以上氨基的一类化合物,有机多元胺作为环氧树脂、聚脲、尼龙等的固化剂或者扩链剂而被广泛使用。但是由于其分子结构中既有憎水部分也有亲水部分,有机多 元胺几乎可以溶于绝大多数极性或者弱极性溶剂中,比如说水、苯、甲苯等。因此没有办法将纯的有机多元胺在某种溶剂中进行乳化,形成稳定的乳液。此外,由于有机多元胺能与现今使用的很多形壳单体反应或者能影响其反应,这种高活性也是其微胶囊化非常具有挑战性的一个原因。However, although the microencapsulation technology has been very diverse so far, there are still some materials that cannot be wrapped by existing methods, such as polyamines. As a class of compounds containing two or more amino groups, organic polyamines are widely used as curing agents or chain extenders for epoxy resins, polyureas, nylons, and the like. However, since the molecular structure has both hydrophobic and hydrophilic moieties, organic polyamines can be dissolved in most polar or weakly polar solvents, such as water, benzene, toluene, and the like. Therefore, there is no way to emulsify a pure organic polyamine in a solvent to form a stable emulsion. In addition, because organic polyamines can react with many of the shell monomers used today or can affect their reaction, this high activity is also a reason for their microcapsules being very challenging.
因为多元胺对环氧基及异氰酸酯基都具有很高的活性,所以将多元胺进行包裹进而制备自修复材料已经被尝试了很长一段时间。在自修复领域,基于微胶囊化的环氧-胺自修复体系及基于微胶囊化的异氰酸酯-胺快速自修复体系已经吸引了越来越多的关注。为了制造上述的自修复材料,学术界为多元胺的微胶囊化进行了大量的努力。除了利用空心管道装载多元胺制备自修复材料外,研究者也制备其他各种载体来装载多元胺类固化剂,比如说空心聚脲醛树脂(PUF)微胶囊、空心玻璃微珠(US9522843B2)、及空心聚丙烯氰纳米纤维。在制备出这些微载体之后,然后再在这些载体中装载多元胺类固化剂。在装载的过程中,根据实际情况可以选择使用真空来加速装载进程。虽然出于自修复目的可以使用上述的方法来装载多元胺,但是这些方法相对来说都比较复杂。李(Li)等人声称他们利用溶剂挥发法,成功包裹了聚醚多元胺,即Jeffamine D230。同时基于该微胶囊及环氧微胶囊的双组份环氧-胺自修复体系在自修复环氧树脂中表现出了良好的修复效果。但是据他们的报导,在最终得到的微胶囊中胺的含量非常低。在优化了包裹条件后,最高的含量也只有大概20wt%。科研人员也使用了皮克林(Pickering)乳液法来包裹纯多元胺。虽然制备出了含有多元胺的微球,但是他们得到的是实心微球而不是具有核-壳结构的微胶囊。同时他们也没有进一步制备基于这种微胶囊的自修复材料来验证所制备的含纯多元胺微胶囊的应用性。利用多元胺在水和低极性碳水化合物溶剂中的分配规则,李(Li)等人及易(Yi)等人成功包裹了多元胺的水溶液,而非纯多元胺。由于利用这种方法所制备的微胶囊囊壁非常脆弱,这些研究者在进一步使用这种微胶囊之前,甚至没有将微胶囊中的水去除。陈(Chen)等人利用一种非常复杂且精密的微流体装置产生的二次复乳液,成功包裹了二乙烯三胺(DETA)及三乙烯四胺(TETA)的水溶液。经过对微胶囊化过程的精细控制,这种方法可以 制备出尺度均一、囊壁厚度均匀的微胶囊。由于所使用的聚丙烯酸囊壁的热稳定比较好,可以使用真空将胶囊中的水完全去除。尽管如此,由于这种胶囊的囊壁较厚且原始胶囊中含有较大比例的水分,最终微胶囊中的多元胺含量也相对来说比较低。此外,因为使用DETA或者TETA固化的环氧交联密度比较高,利用这种微胶囊制备的自修复环氧树脂对断裂韧性的修复不太理想。Since polyamines have high activity for both epoxy groups and isocyanate groups, it has been tried for a long time to encapsulate polyamines to prepare self-healing materials. In the field of self-repair, microencapsulated epoxy-amine self-healing systems and microencapsulated isocyanate-amine rapid self-healing systems have attracted more and more attention. In order to manufacture the self-healing materials described above, a great deal of effort has been made in the academic community for the microencapsulation of polyamines. In addition to the use of hollow tubes to load polyamines to prepare self-healing materials, the researchers also prepared various other carriers to load polyamine curing agents, such as hollow polyurea resin (PUF) microcapsules, hollow glass beads (US9522843B2), and Hollow polypropylene cyanide nanofibers. After the preparation of these microcarriers, the polyamine-based curing agent is then loaded in these carriers. During the loading process, depending on the actual situation, you can choose to use vacuum to speed up the loading process. Although the above methods can be used to load polyamines for self-healing purposes, these methods are relatively complex. Li (Li) and others claimed that they successfully wrapped the polyether polyamine, Jeffamine D230, by solvent evaporation. At the same time, the two-component epoxy-amine self-repairing system based on the microcapsules and epoxy microcapsules showed a good repairing effect in the self-repairing epoxy resin. However, according to their report, the content of amine in the finally obtained microcapsules is very low. After optimizing the wrapping conditions, the highest content is only about 20% by weight. Researchers also used the Pickering emulsion method to encapsulate pure polyamines. Although microspheres containing polyamines were prepared, they obtained solid microspheres rather than microcapsules having a core-shell structure. At the same time, they did not further prepare self-healing materials based on such microcapsules to verify the applicability of the prepared pure polyamine-containing microcapsules. Using the rules for the partitioning of polyamines in water and low-polarity carbohydrate solvents, Li (Li) et al. and Yi et al. successfully encapsulated aqueous solutions of polyamines rather than pure polyamines. Since the microcapsule wall prepared by this method is very fragile, these researchers did not even remove the water in the microcapsule before further use of the microcapsule. Chen et al. successfully encapsulated aqueous solutions of diethylenetriamine (DETA) and triethylenetetramine (TETA) using a second complex emulsion produced by a very complex and sophisticated microfluidic device. Through the fine control of the microencapsulation process, this method can prepare microcapsules with uniform dimensions and uniform thickness of the capsule wall. Since the thermal stability of the polyacrylic acid capsule wall used is relatively good, the water in the capsule can be completely removed using a vacuum. Nevertheless, since the capsule wall of the capsule is thick and the original capsule contains a large proportion of moisture, the polyamine content in the final microcapsule is relatively low. In addition, self-healing epoxy resins prepared using such microcapsules are less than ideal for repairing fracture toughness because of the relatively high epoxy crosslink density cured using DETA or TETA.
由上可以看出,现在还没有一种方法,能制备出具有核-壳结构、芯材含量较高、且芯材成份可控的含纯多元胺的微胶囊。另外,对于这种含多元胺的微胶囊,还存在着一种两难处境,即在这种微胶囊的自修复应用中,我们希望所包裹的胺活性越高越好,但是利用传统的方法在制备这种微胶囊的过程中,活性越高的胺其越难被包裹。如此看来,如果我们想包裹纯多元胺,我们需要探索开发一种新的方法来实现其包裹。在这个发明中,我们描述了一种将T型结微流体装置与界面聚合联合使用的复合方法来实现纯多元胺的微胶囊化。As can be seen from the above, there is currently no method for preparing a microcapsule containing a pure polyamine having a core-shell structure, a high core material content, and a controllable core material composition. In addition, there is a dilemma for such polyamine-containing microcapsules, that is, in the self-healing application of the microcapsules, we hope that the higher the activity of the encapsulated amine, the better, but using the conventional method In the process of preparing such microcapsules, the more active the amine, the more difficult it is to be encapsulated. So it seems that if we want to wrap pure polyamines, we need to explore a new way to implement their packages. In this invention, we describe a composite process using a T-junction microfluidic device in combination with interfacial polymerization to achieve microencapsulation of pure polyamines.
发明内容Summary of the invention
本发明的目的在于克服上述问题,提供一种制备含纯多元胺的微胶囊的方法及其微液滴化装置,能够完成对纯多元胺微胶囊的制备,为纯多元胺的制备提供了一种全新的方法,并提供了相应的微液滴化装置,能够很好的完成对纯多元胺的微液滴化。The object of the present invention is to overcome the above problems and to provide a method for preparing microcapsules containing pure polyamines and a microdroplet device thereof, which can complete the preparation of pure polyamine microcapsules and provide a preparation for pure polyamines. A new method and a corresponding micro-dropletization device can well complete the micro-dropletization of pure polyamines.
本发明的目的通过下述技术方案实现:The object of the invention is achieved by the following technical solution:
一种制备含纯多元胺的微胶囊的方法,包括以下制备步骤:A method of preparing microcapsules containing pure polyamines, comprising the following preparation steps:
(1)配置反应溶液,并对反应溶液进行持续搅拌;(1) arranging the reaction solution, and continuously stirring the reaction solution;
(2)对多元胺进行微液滴化处理,并将微液滴化后的多元胺微液滴加入反应溶液中;(2) micro-droplet treatment of the polyamine, and the micro-dropletized polyamine droplets are added to the reaction solution;
(3)将加入了多元胺液滴的反应溶液加热到40-60℃,并调整搅拌速度以保持对反应溶液的持续搅拌,并在搅拌2-6小时后得到初制微胶囊;(3) heating the reaction solution to which the polyamine droplets are added to 40-60 ° C, and adjusting the stirring speed to maintain continuous stirring of the reaction solution, and obtaining the preliminary microcapsules after stirring for 2-6 hours;
(4)用清洗剂对初制微胶囊进行清洗,并在干燥后得到成品微胶囊。(4) The primary microcapsules are washed with a cleaning agent, and after drying, the finished microcapsules are obtained.
步骤(1)中所述的反应溶液由二异氰酸酯单体/预聚体、表面活性剂、催化剂以及不能溶解或只能微量溶解多元胺的非极性或弱极性溶剂混合而成,其中, 每份溶质中二异氰酸酯单体/预聚体、表面活性剂和催化剂的重量比为4-8:0.05-1:0-1,而每份溶质则与50ml不能溶解或只能微量溶解多元胺的非极性或弱极性溶剂相配合,将配置好的反应溶液放置在常温的环境中并以80-180r/min的速度进行搅拌。The reaction solution described in the step (1) is a mixture of a diisocyanate monomer/prepolymer, a surfactant, a catalyst, and a nonpolar or weakly polar solvent which is insoluble or only slightly soluble in the polyamine. The weight ratio of diisocyanate monomer/prepolymer, surfactant and catalyst in each solute is 4-8:0.05-1:0-1, and each solute is insoluble or only slightly soluble in polyamine at 50ml. The non-polar or weakly polar solvent is combined, and the configured reaction solution is placed in a normal temperature environment and stirred at a rate of 80-180 r/min.
所述二异氰酸酯单体/预聚体包括六亚甲基二异氰酸酯、4,4'-二环己基甲烷二异氰酸酯、异氟尔酮二异氰酸酯和甲苯二异氰酸酯中的任意一种或任意一种以上的组合物,或者是由六亚甲基二异氰酸酯、4,4'-二环己基甲烷二异氰酸酯、异氟尔酮二异氰酸酯、二苯基甲烷二异氰酸酯或甲苯二异氰酸酯中任意一种生成的可溶于反应液溶液的预聚体;The diisocyanate monomer/prepolymer includes any one or more of hexamethylene diisocyanate, 4,4′-dicyclohexylmethane diisocyanate, isophorone diisocyanate, and toluene diisocyanate. The composition may be formed by any one of hexamethylene diisocyanate, 4,4'-dicyclohexylmethane diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate or toluene diisocyanate. a prepolymer dissolved in the reaction solution;
所述表面活性剂则选择能够促进形成反相乳液的表面活性剂;The surfactant is selected to be a surfactant capable of promoting the formation of an inverse emulsion;
所述催化剂包括能促进多元胺与异氰酸酯单体/预聚体反应的三乙烯二胺、2,4,6-三(二甲氨基甲基)苯酚或二月桂酸二丁基锡中的任意一种;The catalyst comprises any one of triethylenediamine, 2,4,6-tris(dimethylaminomethyl)phenol or dibutyltin dilaurate capable of promoting the reaction of a polyamine with an isocyanate monomer/prepolymer;
不能溶解或只能微量溶解多元胺的非极性或弱极性的溶剂包括含6-18个碳原子的液态脂肪烃,环烷烃如环己烷、环庚烷、环辛烷、环癸烷、十氢化萘中的任意一种或任意一种以上的混合物。Non-polar or weakly polar solvents which are insoluble or only slightly soluble in polyamines include liquid aliphatic hydrocarbons having from 6 to 18 carbon atoms, cycloalkanes such as cyclohexane, cycloheptane, cyclooctane, cyclodecane. Any one or a mixture of any one or more of decalin.
步骤(2)中的微液滴化处理则是选用微液滴化装置完成;所述的多元胺包括乙二胺缩聚物、聚醚胺、脂肪胺、聚丙烯胺以及芳香胺中的任意一种或任意一种以上的混合物。The micro-droplet treatment in the step (2) is performed by using a micro-droplet device; the polyamine includes any one of an ethylenediamine polycondensate, a polyether amine, a fatty amine, a polyacrylamine, and an aromatic amine. Kind or a mixture of any one or more.
步骤(3)中的加热方式为:The heating method in step (3) is:
(31)将加入了多元胺液滴的反应溶液加热到40℃,以200-250r/min的搅拌速度搅拌1小时;(31) The reaction solution to which the polyamine droplets were added was heated to 40 ° C, and stirred at a stirring speed of 200-250 r / min for 1 hour;
(32)将温度提升到50℃,以200-250r/min的搅拌速度搅拌2小时;(32) Raise the temperature to 50 ° C, and stir at a stirring speed of 200-250 r / min for 2 hours;
(33)将温度提升到60℃,以200-250r/min的搅拌速度搅拌2小时后得到初制微胶囊。(33) The temperature was raised to 60 ° C, and the preliminary microcapsules were obtained by stirring at a stirring speed of 200-250 r/min for 2 hours.
步骤(4)中的清洗过程为:The cleaning process in step (4) is:
首先,在初制微胶囊中加入清洗剂,并将其搅拌均匀后静置,直至固体沉淀后去除上清液,并重复加入清洗剂对其清洗3-6次,直至上清液澄清为止;接 着,去除澄清的上清液,并将清洗后的微胶囊置于空气中,直至清洗剂完全挥发后即得到了纯净的微胶囊;First, a cleaning agent is added to the preliminary microcapsules, and the mixture is stirred uniformly, and then allowed to stand until the solid precipitates, and the supernatant is removed, and the cleaning agent is repeatedly added for cleaning 3-6 times until the supernatant is clarified; Then, the clarified supernatant is removed, and the washed microcapsules are placed in the air until the cleaning agent is completely volatilized to obtain pure microcapsules;
该清洗剂为非极性溶剂,最优的清洗剂则为纯环己烷。The cleaning agent is a non-polar solvent, and the most preferred cleaning agent is pure cyclohexane.
一种制备含纯多元胺的微胶囊的微液滴化装置,包括粗特氟龙管,插入粗特氟龙管除首尾两端外任意位置处的细特氟龙管,以及分别单独连接在粗特氟龙管和细特氟龙管上的泵出装置;其中,与粗特氟龙管相连接的泵出装置用于泵出共流相,与细特氟龙管相连接的泵出装置用与泵出多元胺。A micro-dropleting device for preparing microcapsules containing pure polyamines, comprising a crude Teflon tube, inserted into a fine Teflon tube at any position except the ends of the first and last ends of the Teflon tube, and separately connected thereto Pumping device on the thick Teflon tube and the fine Teflon tube; wherein the pumping device connected to the thick Teflon tube is used for pumping out the co-current phase, and pumping out with the fine Teflon tube The device uses and pumps out a polyamine.
作为优选,所述细特氟龙管的数量为一个或一个以上,每个细特氟龙管上均独立连接有一个泵出装置,且该泵出装置为注射器或定量泵;所述共流相是由表面活性剂以及不能溶解或只能微量溶解多元胺的非极性或弱极性的溶剂以0.05-1g:50ml的重量体积比混合而成的溶液。Preferably, the number of the fine Teflon tubes is one or more, and each of the fine Teflon tubes is independently connected with a pumping device, and the pumping device is a syringe or a metering pump; The phase is a solution in which a surfactant and a nonpolar or weakly polar solvent which is insoluble or only slightly soluble in the polyamine are mixed in a weight-to-volume ratio of 0.05-1 g: 50 ml.
一种制备含纯多元胺的微胶囊的微液滴化装置,包括泵出装置,与泵出装置相连接且竖直设置的平口金属针头,设置在平口金属针头正下方的金属导体,以及正极平口金属针头相连接、负极与金属导体相连接的高压电源;所述平口金属针头与金属导体之间的间距为10-50cm,高压电源的电压为5-15KV。A micro-dropleting device for preparing microcapsules containing pure polyamines, comprising a pumping device, a flat metal needle connected to the pumping device and vertically disposed, a metal conductor disposed directly below the flat metal needle, and a positive electrode A high-voltage power supply is connected between the flat metal needles and the negative electrode and the metal conductor; the distance between the flat metal needle and the metal conductor is 10-50 cm, and the voltage of the high-voltage power source is 5-15 KV.
一种制备含纯多元胺的微胶囊的微液滴化装置,包括顶部插有两根导管的压力罐,其中一根导管伸入压力罐的底部,另一根导管设置在压力罐的顶部,与伸入压力罐底部的导管相连接的雾化喷头,以及与设置在压力罐的顶部的导管相连接的气罐;其中气罐中的压缩气体为任意一种非酸性气体。A micro-dropletting device for preparing microcapsules containing pure polyamines, comprising a pressure tank with two conduits inserted at the top, one of which extends into the bottom of the pressure tank and the other conduit is placed on top of the pressure tank An atomizing nozzle connected to a conduit extending into the bottom of the pressure tank, and a gas cylinder connected to a conduit disposed at the top of the pressure tank; wherein the compressed gas in the gas cylinder is any non-acid gas.
本发明与现有技术相比,具有以下优点及有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:
(1)本发明的方法提供了一种全新的思路,突破了现有多元胺微胶囊的制作瓶颈,能够很好的完成纯多元胺微胶囊的制作,很好的促进了企业与行业的发展。(1) The method of the invention provides a brand-new idea, breaks through the bottleneck of the existing polyamine microcapsules, can well complete the production of pure polyamine microcapsules, and promotes the development of enterprises and industries. .
(2)本发明的微液滴化装置有三种不同的组成结构,为企业提供了不同的设置方式,进而便于使用时根据实际需求进行选择,大大的提高了产品使用的灵活性。(2) The micro-dropletization device of the present invention has three different composition structures, and provides different setting modes for the enterprise, thereby facilitating selection according to actual needs during use, and greatly improving the flexibility of product use.
图1为本发明的第一种微液滴化装置的结构示意图。Figure 1 is a schematic view showing the structure of a first micro-dropletizing apparatus of the present invention.
图2为本发明的第二种微液滴化装置的结构示意图。2 is a schematic view showing the structure of a second micro-dropleting device of the present invention.
图3为本发明的第三种微液滴化装置的结构示意图。Fig. 3 is a schematic view showing the structure of a third micro-dropleting device of the present invention.
附图标记说明:1、泵出装置;2、粗特氟龙管;3、细特氟龙管;4、平口金属针头;5、高压电源;6、金属导体;7、气罐;8、压力罐;9、雾化喷头。DESCRIPTION OF REFERENCE NUMERALS: 1, pumping device; 2, thick Teflon tube; 3, fine Teflon tube; 4, flat metal needle; 5, high voltage power supply; 6, metal conductor; 7, gas tank; Pressure tank; 9, atomizing nozzle.
下面结合实施例对本发明作进一步的详细说明,但本发明的实施方式不限于此。The present invention will be further described in detail below with reference to the embodiments, but the embodiments of the present invention are not limited thereto.
实施例1Example 1
本实施例公开了一种制备含纯多元胺的微胶囊的方法,包括以下制备步骤:This embodiment discloses a method for preparing a microcapsule containing a pure polyamine, comprising the following preparation steps:
(1)配置反应溶液,并对反应溶液进行持续搅拌;(1) arranging the reaction solution, and continuously stirring the reaction solution;
所述的反应溶液由二异氰酸酯单体/预聚体、表面活性剂、催化剂以及不能溶解或只能微量溶解多元胺的非极性或弱极性溶剂混合而成,其中,每份溶质中二异氰酸酯单体/预聚体、表面活性剂和催化剂的重量比为6:0.05:0,而每份溶质则与50ml不能溶解或只能微量溶解多元胺的非极性或弱极性溶剂相配合,将配置好的反应溶液放置在常温的环境中并以80-180r/min的速度进行搅拌。The reaction solution is prepared by mixing a diisocyanate monomer/prepolymer, a surfactant, a catalyst, and a non-polar or weakly polar solvent which cannot dissolve or only dissolve a polyamine in a small amount, wherein each solute has two The weight ratio of isocyanate monomer/prepolymer, surfactant and catalyst is 6:0.05:0, and each solute is matched with 50ml of non-polar or weakly polar solvent which cannot dissolve or only dissolve the polyamine in a small amount. The configured reaction solution was placed in a normal temperature environment and stirred at a rate of 80-180 r/min.
其中,催化剂可以不使用,即催化剂在其中的重量比为0时。催化剂的使用是为了进一步的提高多元胺微液滴在进入反应溶液后外壳的形成速度,进而能够更好的确保微胶囊的迅速形成。Among them, the catalyst may not be used, that is, when the weight ratio of the catalyst therein is zero. The use of the catalyst is to further increase the formation speed of the outer shell of the polyamine droplets after entering the reaction solution, thereby further ensuring the rapid formation of the microcapsules.
所述二异氰酸酯单体/预聚体包括六亚甲基二异氰酸酯、4,4'-二环己基甲烷二异氰酸酯、异氟尔酮二异氰酸酯和甲苯二异氰酸酯中的任意一种或任意一种以上的组合物,或者是由六亚甲基二异氰酸酯、4,4'-二环己基甲烷二异氰酸酯、异氟尔酮二异氰酸酯、二苯基甲烷二异氰酸酯或甲苯二异氰酸酯中任意一种生成的可溶于反应液溶液的预聚体;The diisocyanate monomer/prepolymer includes any one or more of hexamethylene diisocyanate, 4,4′-dicyclohexylmethane diisocyanate, isophorone diisocyanate, and toluene diisocyanate. The composition may be formed by any one of hexamethylene diisocyanate, 4,4'-dicyclohexylmethane diisocyanate, isophorone diisocyanate, diphenylmethane diisocyanate or toluene diisocyanate. a prepolymer dissolved in the reaction solution;
所述表面活性剂则选择能够促进形成反相乳液的表面活性剂,该表面活性剂为聚氧乙烯聚羟基硬脂酸酯或失水山梨糖醇脂肪酸酯,其中最优的为span 80。The surfactant is selected to be a surfactant capable of promoting the formation of an inverse emulsion which is a polyoxyethylene polyhydroxystearate or a sorbitan fatty acid ester, the most preferred being span 80.
所述催化剂包括能促进多元胺与异氰酸酯单体/预聚体反应的三乙烯二胺、2,4,6-三(二甲氨基甲基)苯酚或二月桂酸二丁基锡中的任意一种;The catalyst comprises any one of triethylenediamine, 2,4,6-tris(dimethylaminomethyl)phenol or dibutyltin dilaurate capable of promoting the reaction of a polyamine with an isocyanate monomer/prepolymer;
不能溶解或只能微量溶解多元胺的非极性或弱极性的溶剂包括含6-18个碳原子的液态脂肪烃,环烷烃如环己烷、环庚烷、环辛烷、环癸烷、十氢化萘中的任意一种或任意一种以上的混合物。Non-polar or weakly polar solvents which are insoluble or only slightly soluble in polyamines include liquid aliphatic hydrocarbons having from 6 to 18 carbon atoms, cycloalkanes such as cyclohexane, cycloheptane, cyclooctane, cyclodecane. Any one or a mixture of any one or more of decalin.
(2)对多元胺进行微液滴化处理,并将微液滴化后的多元胺微液滴加入反应溶液中;(2) micro-droplet treatment of the polyamine, and the micro-dropletized polyamine droplets are added to the reaction solution;
微液滴化处理则是选用微液滴化装置完成;所述的多元胺包括乙二胺缩聚物、聚醚胺、脂肪胺、聚丙烯胺以及芳香胺中的任意一种或任意一种以上的混合物。The micro-droplet treatment is performed by using a micro-droplet device; the polyamine includes any one or more of an ethylenediamine polycondensate, a polyether amine, a fatty amine, a polyacrylamide, and an aromatic amine. mixture.
多元胺在被微液滴化成微液滴后进入反应溶液后,将迅速的与二异氰酸酯单体/预聚体进行反应,微液滴表面的多元胺与二异氰酸酯单体/预聚体反应形成壳体以对内部的纯多元胺进行包裹,避免内部的多元胺继续与二异氰酸酯单体/预聚体反应,进而形成了所需要的多元胺微胶囊。After the polyamine is converted into micro droplets into the reaction solution, it will react rapidly with the diisocyanate monomer/prepolymer, and the polyamine on the surface of the microdroplet reacts with the diisocyanate monomer/prepolymer. The shell encloses the inner pure polyamine to prevent the internal polyamine from continuing to react with the diisocyanate monomer/prepolymer, thereby forming the desired polyamine microcapsules.
(3)将加入了多元胺液滴的反应溶液加热到40-60℃,并调整搅拌速度以保持对反应溶液的持续搅拌,并在搅拌2-6小时后得到初制微胶囊;(3) heating the reaction solution to which the polyamine droplets are added to 40-60 ° C, and adjusting the stirring speed to maintain continuous stirring of the reaction solution, and obtaining the preliminary microcapsules after stirring for 2-6 hours;
加热方式为:The heating method is:
(31)将加入了多元胺液滴的反应溶液加热到40℃,以200r/min的搅拌速度搅拌1小时;(31) The reaction solution to which the polyamine droplets were added was heated to 40 ° C, and stirred at a stirring speed of 200 r / min for 1 hour;
(32)将温度提升到50℃,以200r/min的搅拌速度搅拌2小时;(32) Raise the temperature to 50 ° C, and stir at a stirring speed of 200 r / min for 2 hours;
(33)将温度提升到60℃,以200r/min的搅拌速度搅拌2小时后得到初制微胶囊。(33) The temperature was raised to 60 ° C, and the preliminary microcapsules were obtained by stirring at a stirring speed of 200 r / min for 2 hours.
(4)用清洗剂对初制微胶囊进行清洗,并在干燥后得到成品微胶囊。(4) The primary microcapsules are washed with a cleaning agent, and after drying, the finished microcapsules are obtained.
清洗过程为:The cleaning process is:
首先,在初制微胶囊中加入清洗剂,并将其搅拌均匀后静置,直至固体沉淀后去除上清液,并重复加入清洗剂对其清洗3-6次,直至上清液澄清为止;接着,去除澄清的上清液,并将清洗后的微胶囊置于空气中,直至清洗剂完全挥 发后即得到了纯净的微胶囊;First, a cleaning agent is added to the preliminary microcapsules, and the mixture is stirred uniformly, and then allowed to stand until the solid precipitates, and the supernatant is removed, and the cleaning agent is repeatedly added for cleaning 3-6 times until the supernatant is clarified; Then, the clarified supernatant is removed, and the washed microcapsules are placed in the air until the cleaning agent is completely volatilized to obtain pure microcapsules;
该清洗剂为非极性溶剂,最优的清洗剂则为纯环己烷。The cleaning agent is a non-polar solvent, and the most preferred cleaning agent is pure cyclohexane.
通过该方法制作的微胶囊中胺的含量大概为80wt%,且微胶囊的壳体的热稳定性比较好,热分解温度在200摄氏度以上。The content of the amine in the microcapsules produced by the method is about 80% by weight, and the thermal stability of the shell of the microcapsules is relatively good, and the thermal decomposition temperature is above 200 degrees Celsius.
实施例2Example 2
本实施例与实施例1的不同点仅在于:This embodiment differs from
每份溶质中二异氰酸酯单体/预聚体、表面活性剂和催化剂的重量比为8:1:1。The weight ratio of diisocyanate monomer/prepolymer, surfactant to catalyst in each solute was 8:1:1.
在加热加入了多元胺液滴的反应溶液时的搅拌速度为250r/min。The stirring speed at the time of heating the reaction solution to which the polyamine droplets were added was 250 r/min.
实施例3Example 3
本实施例与实施例1的不同点仅在于:This embodiment differs from
每份溶质中二异氰酸酯单体/预聚体、表面活性剂和催化剂的重量比为6:0.6:0.5。The weight ratio of the diisocyanate monomer/prepolymer, surfactant and catalyst in each solute was 6:0.6:0.5.
在加热加入了多元胺液滴的反应溶液时的搅拌速度为225r/min。The stirring speed at the time of heating the reaction solution to which the polyamine droplets were added was 225 r/min.
实施例4Example 4
如图1所示,本实施例公开了一种制备含纯多元胺的微胶囊的微液滴化装置,包括粗特氟龙管2,插入粗特氟龙管2除首尾两端外任意位置处的细特氟龙管3,以及分别单独连接在粗特氟龙管2和细特氟龙管3上的泵出装置1;其中,与粗特氟龙管2相连接的泵出装置1用于泵出共流相,与细特氟龙管3相连接的泵出装置1用与泵出多元胺。As shown in FIG. 1 , this embodiment discloses a micro-dropleting device for preparing microcapsules containing pure polyamines, including a
所述细特氟龙管3的数量为一个或一个以上,每个细特氟龙管3上均独立连接有一个泵出装置1,且该泵出装置1为注射器或定量泵;所述共流相是由表面活性剂以及不能溶解或只能微量溶解多元胺的非极性或弱极性的溶剂以0.05-1g:50ml的重量体积比混合而成的溶液。The number of the
粗特氟龙管和细特氟龙管中的液体流速均通过泵出装置来进行控制,且在泵出的过程中,粗特氟龙管中的液体流速大于细特氟龙管中的液体流速,以确保多元胺能够在流动的过程中成为微液滴。The liquid flow rate in the crude Teflon tube and the fine Teflon tube is controlled by the pumping device, and during the pumping process, the liquid flow rate in the crude Teflon tube is greater than that in the fine Teflon tube. The flow rate is such that the polyamine can become a microdroplet during the flow.
实施例5Example 5
如图2所示,一种制备含纯多元胺的微胶囊的微液滴化装置,包括泵出装置1,与泵出装置1相连接且竖直设置的平口金属针头4,设置在平口金属针头4正下方的金属导体6,以及正极平口金属针头4相连接、负极与金属导体6相连接的高压电源5;所述平口金属针头4与金属导体6之间的间距为10-50cm,高压电源5的电压为5-15KV。As shown in FIG. 2, a micro-dropleting device for preparing microcapsules containing pure polyamines includes a
多元胺在通过平口金属针头时将会带电,并在电场作用下向金属导体靠近,进而滴落在设置在金属导体上方设置的承载装置中,形成微胶囊。若要调整微液滴的滴落范围则可以改变金属导体的上平面面积,若要调整微液滴的大小则可以通过调整泵出速度或高压电源的电压值来完成。The polyamine will be charged when passing through the flat metal needle, and will approach the metal conductor under the action of the electric field, and then drip into the carrier disposed above the metal conductor to form microcapsules. To adjust the drip range of the microdroplets, the upper planar area of the metal conductor can be changed. To adjust the size of the microdroplets, it can be done by adjusting the pumping speed or the voltage value of the high voltage power supply.
实施例6Example 6
如图3所示,一种制备含纯多元胺的微胶囊的微液滴化装置,包括顶部插有两根导管的压力罐8,其中一根导管伸入压力罐8的底部,另一根导管设置在压力罐8的顶部,与伸入压力罐8底部的导管相连接的雾化喷头9,以及与设置在压力罐8的顶部的导管相连接的气罐7;其中气罐7中的压缩气体为任意一种非酸性气体。As shown in FIG. 3, a micro-dropleting apparatus for preparing microcapsules containing pure polyamines includes a
气罐中的压缩气体采用非酸性气体,可以很好的保证该气体不会与多元胺进行反应,进而确保了多元胺纯净性。多元胺在气压的压力下通过导管进入雾化喷头,并由雾化喷头进行微液滴化喷出。通过调整雾化喷头型号以及气罐压力大小均可以改变微液滴的大小。The compressed gas in the gas tank adopts a non-acid gas, which can ensure that the gas does not react with the polyamine, thereby ensuring the purity of the polyamine. The polyamine enters the atomizing nozzle through a conduit under the pressure of air pressure, and is micro dropletized by the atomizing nozzle. The size of the microdroplets can be changed by adjusting the size of the atomizing nozzle and the pressure of the cylinder.
如上所述,便可很好的实现本发明。As described above, the present invention can be well implemented.
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| CN201820188887.5 | 2018-02-02 | ||
| CN201820188887.5U CN208320758U (en) | 2018-02-02 | 2018-02-02 | A kind of microlayer model makeup of pure polyamine is set |
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