CN114699999B - Preparation method of core-shell silica microspheres based on microfluidic liquid drops - Google Patents
Preparation method of core-shell silica microspheres based on microfluidic liquid drops Download PDFInfo
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 120
- 239000011258 core-shell material Substances 0.000 title claims abstract description 55
- 239000007788 liquid Substances 0.000 title claims abstract description 44
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000004005 microsphere Substances 0.000 claims abstract description 33
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 33
- 238000000034 method Methods 0.000 claims abstract description 31
- 239000002243 precursor Substances 0.000 claims abstract description 30
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000000243 solution Substances 0.000 claims description 40
- 238000004945 emulsification Methods 0.000 claims description 32
- GHBFNMLVSPCDGN-UHFFFAOYSA-N rac-1-monooctanoylglycerol Chemical compound CCCCCCCC(=O)OCC(O)CO GHBFNMLVSPCDGN-UHFFFAOYSA-N 0.000 claims description 19
- 239000004205 dimethyl polysiloxane Substances 0.000 claims description 17
- 235000013870 dimethyl polysiloxane Nutrition 0.000 claims description 17
- 230000004048 modification Effects 0.000 claims description 17
- 238000012986 modification Methods 0.000 claims description 17
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 claims description 17
- -1 polydimethylsiloxane Polymers 0.000 claims description 16
- DKNPRRRKHAEUMW-UHFFFAOYSA-N Iodine aqueous Chemical compound [K+].I[I-]I DKNPRRRKHAEUMW-UHFFFAOYSA-N 0.000 claims description 12
- 239000007864 aqueous solution Substances 0.000 claims description 12
- 229910052731 fluorine Inorganic materials 0.000 claims description 9
- 238000003860 storage Methods 0.000 claims description 9
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 8
- 239000011737 fluorine Substances 0.000 claims description 8
- ZDHXKXAHOVTTAH-UHFFFAOYSA-N trichlorosilane Chemical compound Cl[SiH](Cl)Cl ZDHXKXAHOVTTAH-UHFFFAOYSA-N 0.000 claims description 8
- 239000005052 trichlorosilane Substances 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- 239000011259 mixed solution Substances 0.000 claims description 6
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 5
- 238000003682 fluorination reaction Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 4
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims description 3
- 238000002835 absorbance Methods 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 3
- 239000007924 injection Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000006185 dispersion Substances 0.000 claims 1
- CXQXSVUQTKDNFP-UHFFFAOYSA-N octamethyltrisiloxane Chemical compound C[Si](C)(C)O[Si](C)(C)O[Si](C)(C)C CXQXSVUQTKDNFP-UHFFFAOYSA-N 0.000 claims 1
- 238000004987 plasma desorption mass spectroscopy Methods 0.000 claims 1
- 239000004540 pour-on Substances 0.000 claims 1
- 238000005516 engineering process Methods 0.000 abstract description 11
- 239000003921 oil Substances 0.000 abstract description 7
- WWZKQHOCKIZLMA-UHFFFAOYSA-N Caprylic acid Natural products CCCCCCCC(O)=O WWZKQHOCKIZLMA-UHFFFAOYSA-N 0.000 abstract description 4
- 235000012239 silicon dioxide Nutrition 0.000 abstract description 3
- 239000004094 surface-active agent Substances 0.000 abstract description 2
- 239000005635 Caprylic acid (CAS 124-07-2) Substances 0.000 abstract 2
- 230000001804 emulsifying effect Effects 0.000 abstract 2
- 229960002446 octanoic acid Drugs 0.000 abstract 2
- 125000005456 glyceride group Chemical group 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 6
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241001391944 Commicarpus scandens Species 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- OBETXYAYXDNJHR-UHFFFAOYSA-N alpha-ethylcaproic acid Natural products CCCCC(CC)C(O)=O OBETXYAYXDNJHR-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000012377 drug delivery Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- POVQBCXZUZAICL-UHFFFAOYSA-N methoxy trimethyl silicate Chemical compound [Si](OC)(OC)(OC)OOC POVQBCXZUZAICL-UHFFFAOYSA-N 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 238000000206 photolithography Methods 0.000 description 1
- 229920002120 photoresistant polymer Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 239000003361 porogen Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
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- 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
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- B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
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Abstract
Description
技术领域Technical field
本发明涉及一种基于微流控液滴的核壳二氧化硅微球制备方法,属于微流控微液技术领域。The invention relates to a method for preparing core-shell silica microspheres based on microfluidic droplets, and belongs to the technical field of microfluidic microfluids.
背景技术Background technique
随着微纳米技术的发展,核壳二氧化硅微球广泛应用于药物递送、生物传感等领域,在材料学中具有广阔的发展前景。核壳二氧化硅微球的制备方法多种多样。二氧化硅微球传统的制备方法是将乳化法与溶胶凝胶法相结合,但是该方法所需仪器设备庞大,制备的微球单分散性较差,在应用于微球尺寸要求严格的研究时,难以满足实验要求。检索发现,公开号为CN108341415A的中国专利公开了一种大孔二氧化硅核壳微球的制备方法,该方法制备的二氧化硅核壳微球具有大孔结构,是采用无孔微球与有机单体、交联剂、致孔剂反应改性无孔硅胶微球获得,所制备的微球尺寸是1~3μm,用于生物大分子的快速分离分析。CN110433882A公开一种毛细管液滴微流控装置及单粒柱塞制备方法,该装置是用毛细管制成的微流控装置,以四甲氧基硅氧烷、聚乙二醇、乙酸和氨水混合溶液为分散相制备毛细管柱塞。With the development of micro-nano technology, core-shell silica microspheres are widely used in drug delivery, biosensing and other fields, and have broad development prospects in materials science. There are various methods for preparing core-shell silica microspheres. The traditional preparation method of silica microspheres is to combine the emulsification method and the sol-gel method. However, this method requires huge equipment and the prepared microspheres have poor monodispersity. When used in research with strict microsphere size requirements, , it is difficult to meet the experimental requirements. The search found that the Chinese patent with publication number CN108341415A discloses a method for preparing macroporous silica core-shell microspheres. The silica core-shell microspheres prepared by this method have a macroporous structure and use non-porous microspheres and Non-porous silica microspheres are obtained by modifying the reaction of organic monomers, cross-linking agents, and porogens. The size of the prepared microspheres is 1 to 3 μm, and can be used for rapid separation and analysis of biological macromolecules. CN110433882A discloses a capillary droplet microfluidic device and a method for preparing a single-particle plunger. The device is a microfluidic device made of capillary tubes, and is mixed with tetramethoxysiloxane, polyethylene glycol, acetic acid and ammonia water. The solution is a dispersed phase to prepare a capillary plunger.
液滴微流控技术形成的液滴具有高度单分散性,逐渐发展为微球制备的新方法。液滴微流控技术根据芯片装置几何形状的不同可分为:共流(co-flow)、交叉流(cross-flow)、流动聚焦(flow focusing)以及梯度乳化装置(step emulsification)。其中,梯度乳化法主要依靠通道几何形状和表面张力来形成单分散液滴,是一个自发过程。当分散相进入平行化副通道末端时受到四周通道壁的约束力,靠近副通道连接的储液池(连续相所处位置)时,流体受表面张力的作用变为舌状。舌状流体进入储液池后被不断填充为灯泡状,灯泡状流体与仍在副通道的分散相之间的普拉斯压力差不断增大,最终灯泡状流体颈部断裂形成液滴。目前,基于微流控液滴的梯度乳化法制备核壳二氧化硅微球还未发现。The droplets formed by droplet microfluidic technology are highly monodispersed and have gradually developed into a new method for the preparation of microspheres. Droplet microfluidic technology can be divided into co-flow, cross-flow, flow focusing and step emulsification devices according to the different geometry of the chip device. Among them, the gradient emulsification method mainly relies on channel geometry and surface tension to form monodispersed droplets, which is a spontaneous process. When the dispersed phase enters the end of the parallelized secondary channel, it is restrained by the surrounding channel walls. When it approaches the liquid reservoir connected to the secondary channel (where the continuous phase is located), the fluid becomes tongue-shaped due to surface tension. After the tongue-shaped fluid enters the liquid reservoir, it is continuously filled into a bulb shape. The Plas pressure difference between the bulb-shaped fluid and the dispersed phase still in the secondary channel continues to increase, and finally the neck of the bulb-shaped fluid breaks to form a droplet. At present, the preparation of core-shell silica microspheres based on the gradient emulsification method of microfluidic droplets has not yet been discovered.
发明内容Contents of the invention
本发明所要解决的技术问题是,克服现有技术的不足而提供一种基于微流控液滴的核壳二氧化硅微球制备方法,该方法将微流控技术用于微球制备,所制备的微球尺寸均一,具有高度单分散性。The technical problem to be solved by the present invention is to overcome the shortcomings of the existing technology and provide a method for preparing core-shell silica microspheres based on microfluidic droplets. This method uses microfluidic technology for the preparation of microspheres. The prepared microspheres are uniform in size and highly monodisperse.
本发明提供一种基于微流控液滴的核壳二氧化硅微球制备方法,包括以下步骤:The invention provides a method for preparing core-shell silica microspheres based on microfluidic droplets, which includes the following steps:
步骤1、制备微流控芯片(即梯度乳化装置)——采用聚二甲基硅氧烷(PDMS)浇筑在梯度乳化装置模板和无图案的空模板上,加热定型后取下,空白聚二甲基硅氧烷在上、梯度乳化通道在下进行封接后,打孔、等离子体清洗,最后封接至玻璃片上;Step 1. Prepare the microfluidic chip (i.e. gradient emulsification device) - use polydimethylsiloxane (PDMS) to pour it on the template of the gradient emulsification device and an empty template without pattern, remove it after heating and setting, and leave a blank polydimethylsiloxane After sealing with methylsiloxane on the upper side and gradient emulsification channel on the lower side, holes are drilled, plasma cleaned, and finally sealed on the glass sheet;
步骤2、通道修饰——将修饰液注入梯度乳化装置的通道内,修饰一定时间后,去除修饰液;Step 2. Channel modification - Inject the modification liquid into the channel of the gradient emulsification device. After modification for a certain period of time, remove the modification liquid;
步骤3、通道内液滴的生成以及微球的制备——将二氧化硅前体溶液与辛癸酸甘油酯按照体积比10~50:1的比例溶于乙酸乙酯中(乙酸乙酯作为溶剂,其加入量为使二氧化硅前体溶液与辛癸酸甘油酯两者互溶即可),混合均匀构成分散相,分散相以一定的流速注入梯度乳化装置内中,分散相在梯度乳化装置的通道内破裂成液滴,液滴流进装有连续相的储液池中,静置一段时间后,固化成微球;Step 3. Generation of droplets in the channel and preparation of microspheres - Dissolve the silica precursor solution and glyceryl octanoate in ethyl acetate at a volume ratio of 10 to 50:1 (ethyl acetate is used as Solvent, the amount added is enough to make the silica precursor solution and octanoic acid glyceryl ester mutually soluble), mix evenly to form a dispersed phase, the dispersed phase is injected into the gradient emulsification device at a certain flow rate, and the dispersed phase is in the gradient emulsification The channels of the device break into droplets, and the droplets flow into the liquid reservoir containing the continuous phase. After standing for a period of time, they solidify into microspheres;
步骤4、收集微球于马弗炉中于800℃下煅烧2小时,得到基于微流控液滴的核壳二氧化硅微球。Step 4: Collect the microspheres and calcine them in a muffle furnace at 800°C for 2 hours to obtain core-shell silica microspheres based on microfluidic droplets.
本发明通过微流控技术形成微液滴,液滴具有高度单分散性,并且后续固化成微球时,微球粒径分布小,同时利用二氧化硅前体溶液与辛癸酸甘油酯在有无乙酸乙酯存在下的互溶性得到具有核壳结构的微球,制备了具有不同核壳厚度的二氧化硅微球。所制备的核壳二氧化硅微球未观察到孔状结构,尺寸在200μm左右,具有吸附功能,能够吸附碘水溶液中的碘离子。The present invention forms micro droplets through microfluidic technology. The droplets have a high degree of monodispersity, and when they are subsequently solidified into microspheres, the microsphere particle size distribution is small. At the same time, the silicon dioxide precursor solution and glyceryl octanoate are used in the Microspheres with core-shell structure were obtained through mutual solubility in the presence or absence of ethyl acetate, and silica microspheres with different core-shell thicknesses were prepared. The prepared core-shell silica microspheres have no pore structure and are about 200 μm in size. They have an adsorption function and can adsorb iodine ions in an iodine aqueous solution.
本发明利用梯度乳化装置制备核壳二氧化硅微球,与传统的核壳二氧化硅微球制备方法通过界面反应,所制得的核壳壁薄、易破相比,本发明通过两试剂间相分离实现核壳结构制备,核壳厚度可通过改变两试剂间含量进行调节。The present invention uses a gradient emulsification device to prepare core-shell silica microspheres. Compared with the traditional preparation method of core-shell silica microspheres through interface reaction, the core-shell wall produced is thin and easy to break. Phase separation realizes the preparation of core-shell structure, and the core-shell thickness can be adjusted by changing the content between the two reagents.
作为本发明进一步优化的技术方案如下:As the technical solution for further optimization of the present invention is as follows:
所述步骤1中,梯度乳化装置由一个分散相主通道、七个平行化副通道和一个装载连续相的储液池构成,所述主通道与注射泵的注射针头可插拔连接,所述主通道与副通道的入口相连,所述副通道的出口与储液池相连,本发明设计了合适的梯度乳化装置,在一定程度上增大了装置的通量;所述梯度乳化装置所用的材料为聚二甲基硅氧烷(PDMS)。In the step 1, the gradient emulsification device consists of a dispersed phase main channel, seven parallel secondary channels and a liquid storage tank loaded with the continuous phase. The main channel is pluggably connected to the injection needle of the syringe pump. The main channel is connected to the inlet of the secondary channel, and the outlet of the secondary channel is connected to the liquid storage tank. The present invention designs a suitable gradient emulsification device, which increases the flux of the device to a certain extent; the gradient emulsification device uses The material is polydimethylsiloxane (PDMS).
本发明的微流控芯片为梯度乳化装置,同时集成了七个平行化副通道,提高了装置的通量。The microfluidic chip of the present invention is a gradient emulsification device and integrates seven parallel secondary channels, which improves the throughput of the device.
进一步的,所述储液池内装有连续相,所述连续相为氟碳油。Further, the liquid storage tank is equipped with a continuous phase, and the continuous phase is fluorocarbon oil.
进一步的,所述修饰液为含氟三氯硅烷与电子氟化液(FC 40)组成的混合溶液,所述混合溶液含有3体积%的含氟三氯硅烷及97体积%的电子氟化液。采用含氟三氯硅烷、电子氟化液构成的修饰液,能够改变PDMS通道表面的疏水性,防止液滴粘黏在通道上。Further, the modification liquid is a mixed solution composed of fluorine-containing trichlorosilane and electronic fluorination liquid (FC 40). The mixed solution contains 3 volume % of fluorine-containing trichlorosilane and 97 volume % of electronic fluorination liquid. . The modification liquid composed of fluorine-containing trichlorosilane and electronic fluoride liquid can change the hydrophobicity of the PDMS channel surface and prevent droplets from sticking to the channel.
所述步骤3中,由于副通道末端连接储液池区域分散相尖端的拉普拉斯压力差不断增大,分散相在副通道末端连接储液池区域破裂成液滴,流进盛满连续相的储液池中,以氟碳油为连续相,液滴静置30~40 min后,二氧化硅前体溶液随着乙酸乙酯的挥发固化得到二氧化硅微球。In step 3, due to the increasing Laplace pressure difference at the tip of the dispersed phase in the area connected to the liquid reservoir at the end of the secondary channel, the dispersed phase breaks into droplets in the area connected to the liquid reservoir at the end of the secondary channel and flows into a continuous In the liquid storage tank of the phase, fluorocarbon oil is used as the continuous phase. After the droplets stand for 30 to 40 minutes, the silica precursor solution solidifies with the volatilization of ethyl acetate to obtain silica microspheres.
本发明的二氧化硅微球具有核壳结构,以二氧化硅前体溶液、辛癸酸甘油酯和乙酸乙酯为分散相形成液滴,再通过乙酸乙酯的挥发使二氧化硅前体溶液和辛癸酸甘油酯不互溶得到核壳结构,其中二氧化硅微球为壳,辛癸酸甘油酯为核。The silica microspheres of the present invention have a core-shell structure. Silica precursor solution, octyl glyceryl ester and ethyl acetate are used as dispersed phases to form droplets, and then the silica precursor is evaporated through the volatilization of ethyl acetate. The solution and octanoic acid glyceryl are immiscible to form a core-shell structure, in which silica microspheres are the shell and octanoic acid glyceryl ester is the core.
进一步的,所述液滴具有单分散性,固化后的二氧化硅微球也具有单分散性。Furthermore, the liquid droplets have monodispersity, and the cured silica microspheres also have monodispersity.
进一步的,所述核壳二氧化硅微球可通过调节分散相中二氧化硅前体溶液和辛癸酸甘油酯的体积比,制备得到不同核壳厚度的二氧化硅微球,分散相中二氧化硅前体溶液和辛癸酸甘油酯的体积比分别为10:1、20:1、30:1、40:1、50:1。Further, the core-shell silica microspheres can be prepared with different core-shell thicknesses by adjusting the volume ratio of the silica precursor solution and glyceryl octanoate in the dispersed phase. The volume ratios of the silica precursor solution and glyceryl octanoate are 10:1, 20:1, 30:1, 40:1, and 50:1 respectively.
进一步的,所述二氧化硅前体溶液的制备方法如下:以正硅酸四乙酯为硅源,将2.7 g 0.01 M 盐酸溶液、3 g 乙醇溶液和5.2 g 正硅酸四乙酯混合,搅拌30 min。Further, the preparation method of the silica precursor solution is as follows: using tetraethyl orthosilicate as the silicon source, mix 2.7 g 0.01 M hydrochloric acid solution, 3 g ethanol solution and 5.2 g tetraethyl orthosilicate, Stir for 30 minutes.
本发明通过液滴微流控技术中的梯度乳化法形成单分散液滴,以二氧化硅前体溶液和辛癸酸甘油酯在乙酸乙酯的存在下互溶作为分散相,以氟碳油作为连续相,形成尺寸均一的液滴,静置后乙酸乙酯挥发会导致二氧化硅前体溶液与辛癸酸甘油酯不互溶,同时氟碳油中的表面活性剂与二氧化硅前体溶液反应使液滴固化,因此形成了具有核壳结构的二氧化硅微球。在此基础上,改变了分散相中二氧化硅前体溶液与辛癸酸甘油酯的含量,得到了具有不同核壳厚度的二氧化硅微球。The present invention forms monodisperse droplets through the gradient emulsification method in droplet microfluidic technology. Silica precursor solution and glyceryl octanoate are mutually dissolved in the presence of ethyl acetate as the dispersed phase, and fluorocarbon oil is used as the dispersed phase. The continuous phase forms droplets of uniform size. After standing, the volatilization of ethyl acetate will cause the silica precursor solution and glyceryl octanoate to be immiscible. At the same time, the surfactant in the fluorocarbon oil will not dissolve with the silica precursor solution. The reaction solidifies the droplets, thus forming silica microspheres with a core-shell structure. On this basis, the contents of the silica precursor solution and glyceryl octanoate in the dispersed phase were changed, and silica microspheres with different core-shell thicknesses were obtained.
本发明还提供上述方法制备的核壳二氧化硅微球的应用:所述核壳二氧化硅微球具有吸附功能,用于吸附碘离子。The present invention also provides the application of the core-shell silica microspheres prepared by the above method: the core-shell silica microspheres have an adsorption function and are used to adsorb iodide ions.
进一步的,在碘水溶液中加入制备的核壳二氧化硅微球,静置一晚后,与未加微球的碘水溶液进行对比,测定两种溶液的紫外吸光光度值,以验证微球的应用。Further, the prepared core-shell silica microspheres were added to the iodine aqueous solution, and after letting it stand for one night, they were compared with the iodine aqueous solution without adding microspheres, and the ultraviolet absorbance photometric values of the two solutions were measured to verify the performance of the microspheres. application.
本发明的优点是采用液滴微流控技术能够生成高度单分散性的液滴,固化后得到尺寸均一的二氧化硅微球,二氧化硅微球具有核壳结构,通过改变分散相体积比可得到不同核壳厚度的二氧化硅微球,并且制备的微球具有吸附功能。The advantage of the present invention is that droplet microfluidic technology can be used to generate highly monodispersed droplets. After solidification, uniform-sized silica microspheres are obtained. The silica microspheres have a core-shell structure. By changing the volume ratio of the dispersed phase Silica microspheres with different core-shell thicknesses can be obtained, and the prepared microspheres have adsorption functions.
总之本发明的制备方法独特,通过微流控液滴技术中的梯度乳化法制备核壳二氧化硅微球,既能得到单分散微球又提高了液滴生成速率;形成核壳结构的试剂独特,由于二氧化硅前体溶液与辛癸酸甘油酯在乙酸乙酯存在下能够互溶,生成液滴后乙酸乙酯的挥发,导致二氧化硅前体溶液与辛癸酸甘油酯逐渐不互溶,从而得到核壳机构。通过液滴-微球一步到位制备核壳二氧化硅微球,制备快速,方法简单。In short, the preparation method of the present invention is unique. The core-shell silica microspheres are prepared through the gradient emulsification method in microfluidic droplet technology, which can not only obtain monodispersed microspheres but also increase the droplet generation rate; the reagents that form the core-shell structure Uniquely, because the silica precursor solution and glyceryl octanoate are mutually soluble in the presence of ethyl acetate, the volatilization of ethyl acetate after the droplets are generated makes the silica precursor solution and glyceryl octanoate gradually insoluble in each other. , thus obtaining the core-shell mechanism. Core-shell silica microspheres are prepared in one step through droplets and microspheres. The preparation is fast and the method is simple.
附图说明Description of the drawings
图1为本发明方法的原理示意图和实物图。Figure 1 is a schematic diagram and a physical diagram of the method of the present invention.
图2为本发明中梯度乳化装置的示意图。Figure 2 is a schematic diagram of the gradient emulsification device in the present invention.
图3为本发明中不同分散相体积比下液滴刚形成以及凝固后的实物图。Figure 3 is a physical diagram of droplets just formed and after solidification under different dispersed phase volume ratios in the present invention.
图4为本发明中不同分散相体积比下液滴刚形成以及凝固后的尺寸统计图。Figure 4 is a statistical diagram of the size of droplets just formed and after solidification under different dispersed phase volume ratios in the present invention.
图5为本发明中不同分散相体积比下二氧化硅微球的电镜图。Figure 5 is an electron microscope image of silica microspheres under different dispersed phase volume ratios in the present invention.
图6为本发明中未加与加入二氧化硅微球静置一晚后的碘水溶液示意图。Figure 6 is a schematic diagram of the iodine aqueous solution in the present invention without and after adding silica microspheres and left to stand for one night.
图7为本发明中未加与加入二氧化硅微球静置一晚后的碘水溶液紫外吸收光光度曲线图。Figure 7 is a graph showing the ultraviolet absorption light photometric curve of the iodine aqueous solution after leaving it alone overnight without adding silica microspheres in the present invention.
具体实施方式Detailed ways
下面结合附图对本发明的技术方案做进一步的详细说明:本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护权限不限于下述的实施例。The technical solution of the present invention will be further described in detail below with reference to the accompanying drawings: This embodiment is implemented on the premise of the technical solution of the present invention, and detailed implementation modes and specific operating procedures are given. However, the protection rights of the present invention are not limited to Limited to the following examples.
实施例1 梯度乳化装置中核壳二氧化硅微球的制备Example 1 Preparation of core-shell silica microspheres in gradient emulsification device
采用标准光刻流程加工具有特定图案的光刻胶阳模,即可得到梯度乳化装置模板,该模板具有与梯度乳化装置上的主副通道及储液池相对应的阳性图案。聚二甲基硅氧烷(PDMS)的预聚物分别浇筑在阳模板上,直至预聚物高度与阳模齐平,同时将聚二甲基硅氧烷(PDMS)的预聚物浇筑在无图案的空模板上,分别进行真空脱气后,加热固化、定型。冷却后,剥离带有通道图案的聚二甲基硅氧烷块,打孔,等离子体清洗,将带有通道图案的聚二甲基硅氧烷块与空白的聚二甲基硅氧烷块进行封接,再与玻璃基板进行封接,形成微流控梯度乳化芯片,微流控梯度乳化芯片由一个分散相主通道、七个平行化副通道和一个装载连续相的储液池构成,其中主通道的一端与注射泵的注射针头可插拔连接,另一端与副通道的入口相连,副通道的出口与储液池相连(见图2)。储液池内装有连续相,连续相为氟碳油。Using a standard photolithography process to process a photoresist positive mold with a specific pattern, a gradient emulsification device template can be obtained. The template has positive patterns corresponding to the main and secondary channels and liquid reservoirs on the gradient emulsification device. The prepolymers of polydimethylsiloxane (PDMS) are poured on the positive mold respectively until the height of the prepolymer is flush with the positive mold. At the same time, the prepolymer of polydimethylsiloxane (PDMS) is poured on the positive mold. On the empty template without pattern, vacuum degassing is performed respectively, and then heated, cured and finalized. After cooling, the polydimethylsiloxane block with the channel pattern is peeled off, punched, plasma cleaned, and the polydimethylsiloxane block with the channel pattern is combined with the blank polydimethylsiloxane block. Sealing, and then sealing with the glass substrate to form a microfluidic gradient emulsification chip. The microfluidic gradient emulsification chip consists of a dispersed phase main channel, seven parallel secondary channels and a liquid storage tank loaded with the continuous phase. One end of the main channel is pluggably connected to the injection needle of the syringe pump, the other end is connected to the inlet of the secondary channel, and the outlet of the secondary channel is connected to the liquid reservoir (see Figure 2). The liquid reservoir is filled with a continuous phase, which is fluorocarbon oil.
将修饰液注入梯度乳化装置的通道内,修饰30min后,去除修饰液,重复操作两次。修饰液为含氟三氯硅烷与电子氟化液(FC 40)组成的混合溶液,其中混合溶液含有3体积%的含氟三氯硅烷及97体积%的电子氟化液。Inject the modification fluid into the channel of the gradient emulsification device. After modification for 30 minutes, remove the modification fluid and repeat the operation twice. The modification liquid is a mixed solution composed of fluorine-containing trichlorosilane and electronic fluorination liquid (FC 40). The mixed solution contains 3 volume % of fluorine-containing trichlorosilane and 97 volume % of electronic fluorination liquid.
修饰完成后,通过注射泵将分散相以一定的流速注入芯片中,由于副通道末端连接储液池区域的分散相尖端的拉普拉斯压力差不断增大,分散相破裂成液滴,进入盛满连续相的储液池中,静置一段30~40 min后,二氧化硅前体溶液随着乙酸乙酯的挥发固化成微球(见图1、图3和图4,图3中二氧化硅前体溶液与辛癸酸甘油酯的体积比分别为A、D :20:1;B、E: 30:1;C、F : 50:1)。其中,将二氧化硅前体溶液与辛癸酸甘油酯按照体积比20:1、30:1、50:1的比例分别溶于乙酸乙酯(加入乙酸乙酯的量为使两者互溶即可)中,混合均匀构成分散相。二氧化硅前体溶液的制备方法如下:以正硅酸四乙酯为硅源,将2.7 g 0.01M 盐酸溶液、3 g 乙醇溶液和5.2 g 正硅酸四乙酯混合,搅拌30 min。将微球放置在马弗炉中于800℃下煅烧2小时去除微球中的辛癸酸甘油酯,得到具有核壳结构的微球。After the modification is completed, the dispersed phase is injected into the chip at a certain flow rate through a syringe pump. As the Laplace pressure difference at the tip of the dispersed phase connected to the reservoir area at the end of the secondary channel continues to increase, the dispersed phase breaks into droplets and enters. In a storage tank filled with the continuous phase, after standing for 30 to 40 minutes, the silica precursor solution solidifies into microspheres as the ethyl acetate evaporates (see Figures 1, 3 and 4, in Figure 3 The volume ratios of the silica precursor solution and glyceryl octanoate are A and D: 20:1; B and E: 30:1; C and F: 50:1). Among them, the silica precursor solution and glyceryl octanoate were dissolved in ethyl acetate in a volume ratio of 20:1, 30:1, and 50:1 respectively (the amount of ethyl acetate added was such that the two are mutually soluble. Yes), mix evenly to form a dispersed phase. The preparation method of the silica precursor solution is as follows: using tetraethyl orthosilicate as the silicon source, mix 2.7 g 0.01M hydrochloric acid solution, 3 g ethanol solution and 5.2 g tetraethyl orthosilicate, and stir for 30 min. The microspheres were placed in a muffle furnace and calcined at 800°C for 2 hours to remove the octanoic acid glyceryl ester in the microspheres to obtain microspheres with a core-shell structure.
另外,改变分散相中二氧化硅前体溶液与辛癸酸甘油酯的体积比为10:1、30:1、50:1,分别制备不同核壳厚度的二氧化硅微球(见图5,二氧化硅前体溶液与辛癸酸甘油酯的体积比分别为A、B、C10:1;D、E、F : 20:1;G、H、I: 30:1;J、K、L : 50:1)。In addition, the volume ratio of the silica precursor solution and octanoic acid glyceryl ester in the dispersed phase was changed to 10:1, 30:1, and 50:1 to prepare silica microspheres with different core-shell thicknesses (see Figure 5 , the volume ratios of silica precursor solution and glyceryl octanoate are A, B, C 10:1; D, E, F: 20:1; G, H, I: 30:1; J, K, L : 50:1).
实施例2 核壳二氧化硅微球的应用验证Example 2 Application verification of core-shell silica microspheres
在碘水溶液中加入制备的核壳二氧化硅微球,静置一晚后,与未加微球的碘水溶液进行对比,观察溶液颜色变化,如图6所示,A表示未加微球的碘水溶液;B 表示加入微球的碘水溶液,同时测定两种溶液的紫外吸光光度值,结果见图7。Add the prepared core-shell silica microspheres to the iodine aqueous solution. After leaving it for one night, compare it with the iodine aqueous solution without microspheres to observe the color change of the solution, as shown in Figure 6. A represents the iodine aqueous solution without microspheres. Iodine aqueous solution; B represents the iodine aqueous solution with microspheres added, and the UV absorbance photometric values of the two solutions were measured at the same time. The results are shown in Figure 7.
以上所述,仅为本发明中的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉该技术的人在本发明所揭露的技术范围内,可理解想到的变换或替换,都应涵盖在本发明的包含范围之内,因此,本发明的保护范围应该以权利要求书的保护范围为准。The above are only specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto. Anyone familiar with this technology can understand the conceivable transformations or substitutions within the technical scope disclosed in the present invention. All should be included within the scope of the present invention. Therefore, the protection scope of the present invention should be subject to the protection scope of the claims.
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