Porous polymer microspheres with optical anisotropy, method of manufacturing the same and application of the same
20200306715 ยท 2020-10-01
Assignee
Inventors
Cpc classification
B01J20/3057
PERFORMING OPERATIONS; TRANSPORTING
C09K19/12
CHEMISTRY; METALLURGY
B01D15/08
PERFORMING OPERATIONS; TRANSPORTING
B01J20/3085
PERFORMING OPERATIONS; TRANSPORTING
C09K19/20
CHEMISTRY; METALLURGY
B01J20/261
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J13/04
PERFORMING OPERATIONS; TRANSPORTING
B01J20/26
PERFORMING OPERATIONS; TRANSPORTING
B01J20/30
PERFORMING OPERATIONS; TRANSPORTING
C09K19/12
CHEMISTRY; METALLURGY
Abstract
Porous polymer microsphere having radial optical anisotropy and diverse swelling states when dispersed in different solvents, which have ability to well swell the porous microspheres. A method for preparing the porous polymer microspheres, including: forming a homogeneous liquid crystal mixture; dispersing the liquid crystal mixture into a continuous phase to form a emulsion of liquid crystal droplets; polymerizing the at least one reactive liquid crystal to form intermediate microspheres; removing the at least one non-reactive liquid crystal compound to form the porous polymer microspheres; separating, washing and dispersing or drying the porous polymer microspheres. The polymer microspheres can be used as the stationary phase in chromatograph separation, improving separation efficiency and column packing efficiency.
Claims
1. Porous polymer microspheres, having radial optical anisotropy, wherein the porous polymer microspheres have diverse swelling states when dispersed in different solvents, and wherein the solvents have ability to well swell the porous polymer microspheres.
2. The porous polymer microspheres of claim 1, wherein the average particle size of the porous polymer microspheres in ethanol is 1 m-150 m.
3. The porous polymer microspheres of claim 1, wherein the swelling degree of the porous polymer microspheres in tetrahydrofuran is 1.0-7.0.
4. A method for preparing the porous polymer micro spheres, comprising: (I) forming a homogeneous liquid crystal mixture, wherein the liquid crystal mixture comprises at least one reactive liquid crystal compound, at least one non-reactive liquid crystal compound and at least one polymerization initiator; (II) dispersing the liquid crystal mixture into a continuous phase containing liquid-crystal-configuration-adjusting agent through a membrane emulsification device, to form a emulsion of liquid crystal droplets, wherein the liquid-crystal-configuration-adjusting agent align liquid crystal molecules inside the liquid crystal droplets along the radial direction; (III) polymerizing the at least one reactive liquid crystal compound to form intermediate microspheres; (IV) removing the at least one non-reactive liquid crystal compound from the intermediate microspheres to form the porous polymer microspheres; and (V) separating, washing and dispersing or drying the porous polymer microspheres.
5. The method of claim 4, wherein the step of polymerizing includes photo polymerization, thermal polymerization, radiation polymerization, and combinations thereof.
6. The method of claim 4, wherein the at least one reactive liquid crystal compound is 5%-50% by weight of the liquid crystal mixture.
7. The method of claim 4, wherein the at least one non-reactive liquid crystal compound is nematic liquid crystal.
8. The method of claim 4, wherein the liquid-crystal-configuration-adjusting agent is sodium dodecyl sulfate.
9. The method of claim 8, wherein the concentration of sodium dodecyl sulfate in the continuous phase is 1 mM to 200 mM.
10. An application of the porous polymer microspheres comprising: utilizing the porous polymer microspheres of claim 1 as a stationary phase in chromatograph separation.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0018] These and other features and advantages of the present invention will be better understood by reference to the following detailed description of an illustrative embodiment of the present disclosure when read in conjunction with the accompanying drawings, wherein:
[0019]
[0020]
[0021]
[0022]
[0023]
[0024]
[0025]
[0026]
[0027]
[0028]
[0029]
[0030]
[0031]
[0032]
[0033]
[0034]
DETAILED DESCRIPTION OF THE INVENTION
[0035] The following description of the disclosed embodiments is provided in detail to enable any person skilled in the art to fully understand the present invention. However, it will be apparent to those skilled in the art to readily make or use the present invention without these specific details. In other examples, well-known structures and devices are shown in the block diagram. In this regard, the description of the different illustrative exemplary embodiments presented herein are for the purpose of illustration and description and are not intended to be exhaustive or limited to the inventive concept. Accordingly, the scope of the invention is not to be limited by the specific embodiments described above, and is subject only to the scope of the appended claims.
[0036] Abbreviations used in the present invention are listed below:
##STR00001##
[0037] SPG membrane: Shirasu Porous Glass membrane
[0038] SDS: sodium dodecyl sulfate
[0039] THF: tetrahydrofuran.
[0040] Referring first to
[0041] Porous polymer microspheres with a radial optical anisotropy can be prepared by a liquid-crystal-assisted template polymerization method, including the following steps: First, at least one reactive liquid crystal, at least one non-reactive liquid crystal, and at least one polymerization initiator are mixed in a certain ratio to form a uniform liquid crystal mixture. The reactive liquid crystal compounds contain polymerizable groups and can be further polymerized in the presence of polymerization initiators, such as acrylate type liquid crystals (RM257), methacrylate type liquid crystals (HCM062), allyl type liquid crystals (HCM126) and so on. The non-reactive liquid crystal compounds do not have polymerizable groups to further polymerize. The non-reactive liquid crystal may be a nematic liquid crystal, a cholesteric liquid crystal, a smectic liquid crystal, and other liquid crystals without polymerizable groups. The mass ratio of the reactive liquid crystal compound over the liquid crystal mixture varies from 0.05 to 0.50.
[0042] After that, the liquid crystal mixture is passed through a membrane emulsification device into a continuous phase to form monodisperse liquid crystal droplets. The continuous phase can be water. The principle of the membrane emulsifier device is shown in
[0043] Next, the reactive liquid crystals 11 in the liquid crystal droplets are polymerized to form intermediate microspheres containing the unreacted non-reactive liquid crystals 12. As shown in
[0044] Then porous polymer microparticles are further formed by removing the unreacted non-reactive liquid crystals. As shown in
[0045] Finally, the polymer microspheres are separated, washed and dispersed/dried. Because the polymer microspheres have different swelling states in different solvents, the polymer microspheres at dry and in solvents have different particle sizes and morphologies. In the following examples, the polymer microspheres in ethanol have a particle size from 1 m to 150 m.
[0046] The dried polymer microparticles can be applied in biochemical separation as the stationary phase of chromatography. Chromatography is usually carried out by a column operation, where the polymer microparticles are packed in the column and a mobile phase containing different components is passed through the column. Due to the porous structure, the solvent-dependent swelling degree and the special and regular interior structure, the polymer microparticles, as the stationary phase, have different interaction with various substances as well as different combination levels, achieving the purpose of substance separation.
[0047] In the present invention, the ratios all refer to mass ratios, unless otherwise indicated.
Example 1: Preparation of Liquid Crystal Droplets with Radial Optical Anisotropy
[0048] First, 7.9 g of 5CB (non-reactive liquid crystal) compound 5CB, 2 g of RM257 (reactive liquid crystal), and 0.1 g of DMPAP (photo polymerization initiator) were mixed and heated above the clearing point of the liquid crystals to form a homogeneous solution. After that, the solution was sufficiently shaken to be uniformly blended and then slowly cooled to room temperature, forming a liquid crystal mixture. Since DMPAP is sensitive to light, the solution must be placed in dark during the cooling process. 100 mg of the above uniform liquid crystal mixture was slowly and smoothly passed through a membrane emulsifier device with a membrane pore diameter of 2.8 m under a pressure of 0.030 MPa, and dispersed into 275 ml of mM SDS aqueous solution (water is the continuous phase, SDS is the liquid-crystal-configuration-adjusting agent). The prepared liquid crystal droplets are uniform in size which is averagely 10 m (as shown in
Example 2
[0049] A liquid crystal mixture (40% RM257, 1% DMPAP) was prepared as example 1. Then 10 g of the liquid crystal mixture was slowly and smoothly passed through a membrane emulsifier device with a membrane pore size of 10 m under a pressure of 0.030 MPa, and dispersed in 275 mL of 2 mM SDS aqueous solution (water is the continuous phase, SDS is the liquid-crystal-configuration-adjusting agent) to form an emulsion containing liquid crystal droplets with a uniform size and a radial configuration. After that, the emulsion was placed under a UV light source to process polymerization. The radiation intensity was 2.5 mW/cm.sup.2, and the time was 30 minutes. The system needs to be constantly stirred during the polymerization. After the polymerization, the reaction solution was washed with ethanol and then centrifuged (8000 rpm, 10 minutes) to remove the supernatant. After repeating the washing and centrifugation three times, the ethanol was removed to obtain polymer microspheres without 5CB, and then the polymer microspheres were dispersed in different solvents. The polymer microspheres may also be dried for further applications. As shown in
Example 3
[0050] A liquid crystal mixture (20% RM257, 1% DMPAP) was prepared as example 1. Then 10 g of the liquid crystal mixture was slowly and smoothly passed through a membrane emulsifier device with a membrane pore size of 10 m under a pressure of 0.030 MPa, and dispersed in 275 mL of 78 mM SDS aqueous solution (water is the continuous phase, SDS is the liquid-crystal-configuration-adjusting agent) to form an emulsion containing liquid crystal droplets with a uniform size and a radial configuration. After that, the emulsion was placed under a UV light source to process polymerization. The radiation intensity was 2.5 mW/cm.sup.2, and the time was 30 minutes. The system needs to be constantly stirred during the polymerization. After the polymerization, the reaction solution was washed with ethanol and then centrifuged (8000 rpm, 10 minutes) to remove the supernatant. After repeating the washing and centrifugation three times, the ethanol was removed to obtain polymer microspheres without 5CB, and then the polymer microspheres were dispersed in different solvents. The polymer microspheres may also be dried for further applications. As shown in
Example 4
[0051] A liquid crystal mixture (20% RM257, 1% DMPAP) was prepared as example 1. Then 10 g of the liquid crystal mixture was slowly and smoothly passed through a membrane emulsifier device with a membrane pore size of 20 m under a pressure of 0.030 MPa, and dispersed in 275 mL of 2 mM SDS aqueous solution (water is the continuous phase, SDS is the liquid-crystal-configuration-adjusting agent) to form an emulsion containing liquid crystal droplets with a uniform size and a radial configuration. After that, the emulsion was placed under a UV light source to process polymerization. The radiation intensity was 2.5 mW/cm.sup.2, and the time was 30 minutes. The system needs to be constantly stirred during the polymerization. After the polymerization, the reaction solution was washed with ethanol and then centrifuged (8000 rpm, 10 minutes) to remove the supernatant. After repeating the washing and centrifugation three times, the ethanol was removed to obtain polymer microspheres without 5CB, and then the polymer microspheres were dispersed in different solvents. The polymer microspheres may also be dried for further applications. As shown in
Example 5
[0052] A liquid crystal mixture (20% RM257, 1% DMPAP) was prepared as example 1. Then 10 g of the liquid crystal mixture was slowly and smoothly passed through a membrane emulsifier device with a membrane pore size of 2.8 m under a pressure of 0.030 MPa, and dispersed in 275 mL of 160 mM SDS aqueous solution (water is the continuous phase, SDS is the liquid-crystal-configuration-adjusting agent) to form an emulsion containing liquid crystal droplets with a uniform size and a radial configuration. After that, the emulsion was placed under a UV light source to process polymerization. The radiation intensity was 2.5 mW/cm.sup.2, and the time was 30 minutes. The system needs to be constantly stirred during the polymerization. After the polymerization, the reaction solution was washed with ethanol and then centrifuged (8000 rpm, 10 minutes) to remove the supernatant. After repeating the washing and centrifugation three times, the ethanol was removed to obtain polymer microspheres without 5CB, and then the polymer microspheres were dispersed in different solvents. The polymer microspheres may also be dried for further applications. As shown in
Example 6
[0053] A liquid crystal mixture (10% RM257, 1% DMPAP) was prepared as example 1. Then 10 g of the liquid crystal mixture was slowly and smoothly passed through a membrane emulsifier device with a membrane pore size of 10 m under a pressure of 0.030 MPa, and dispersed in 275 mL of 2 mM SDS aqueous solution (water is the continuous phase, SDS is the liquid-crystal-configuration-adjusting agent) to form an emulsion containing liquid crystal droplets with a uniform size and a radial configuration. After that, the emulsion was placed under a UV light source to process polymerization. The radiation intensity was 2.5 mW/cm.sup.2, and the time was 30 minutes. The system needs to be constantly stirred during the polymerization. After the polymerization, the reaction solution was washed with ethanol and then centrifuged (8000 rpm, 10 minutes) to remove the supernatant. After repeating the washing and centrifugation three times, the ethanol was removed to obtain polymer microspheres without 5CB, and then the polymer microspheres were dispersed in different solvents. The polymer microspheres may also be dried for further applications. As shown in
Example 7
[0054] A liquid crystal mixture (20% RM257, 1% DMPAP) was prepared as example 1. Then 10 g of the liquid crystal mixture was slowly and smoothly passed through a membrane emulsifier device with a membrane pore size of 50 m under a pressure of 0.030 MPa, and dispersed in 275 mL of 2 mM SDS aqueous solution (water is the continuous phase, SDS is the liquid-crystal-configuration-adjusting agent) to form an emulsion containing liquid crystal droplets with a uniform size and a radial configuration. After that, the emulsion was placed under a UV light source to process polymerization. The radiation intensity was 2.5 mW/cm.sup.2, and the time was 30 minutes. The system needs to be constantly stirred during the polymerization. After the polymerization, the reaction solution was washed with ethanol and then centrifuged (8000 rpm, 10 minutes) to remove the supernatant. After repeating the washing and centrifugation three times, the ethanol was removed to obtain polymer microspheres without 5CB, and then the polymer microspheres were dispersed in different solvents. The polymer microspheres may also be dried for further applications. As shown in
[0055] In addition, for the purpose of concise illustration, the drawings herein are described in terms of a substantially planar form. However, it should be understood by those skilled in the art that the rearview mirror (and all of its functional layers) of the present invention may also include concave and convex curved surfaces, such as cylinders, spheres, ellipsoids, parabolas, or their combination. In addition, it will be appreciated by those skilled in the art that the rearview mirror of the present invention may also be applied to a combined rearview mirror system which has two or more different mirrors with different reflection directions or curvature characteristics.
[0056] While several particular exemplary embodiments have been described above in detail, the disclosed embodiments are considered illustrative rather than limiting. Those skilled in the art will readily realize that alternatives, modifications, variations, improvements, and substantial equivalents are possible without substantially departing from the novelty spirits or scope of the present disclosure. Thus, all such alternatives, modifications, variations, improvements, and substantial equivalents are intended to be embraced within the scope of the present disclosure as defined by the appended claims.
INDUSTRIAL APPLICABILITY
[0057] The method of the present invention can be applied to the field of polymer.