METHOD OF PREPARING A DEGRADABLE PRODUCT
20230192944 · 2023-06-22
Inventors
Cpc classification
C08G63/12
CHEMISTRY; METALLURGY
A61Q11/00
HUMAN NECESSITIES
A61K8/0241
HUMAN NECESSITIES
A61K2800/412
HUMAN NECESSITIES
A61K2800/654
HUMAN NECESSITIES
A61K2800/28
HUMAN NECESSITIES
International classification
Abstract
Provided is a degradable microparticle with a grain size in a range of 2 micrometers to 1400 micrometers, and the degradable microparticle comprises poly(glycerol sebacate), poly(glycerol maleate), poly(glycerol succinate-co-maleate), poly(glycerol succinate), poly(glycerol malonate), poly(glycerol glutarate), poly(glycerol adipate), poly(glycerol pimelate), poly(glycerol suberate), poly(glycerol azelate), or any combination thereof. A degradable product produced from the degradable microparticles can obtain the desired degradation effect and can be produced by chemical synthesis to reduce the production cost. With these advantages, the applicability of the degradable microparticles is improved.
Claims
1. A method of preparing a degradable product, which comprises preparing the degradable product from a degradable microparticle, wherein, a material of the degradable microparticle comprises poly(glycerol sebacate), poly(glycerol maleate), poly(glycerol succinate-co-maleate), poly(glycerol succinate), poly(glycerol malonate), poly(glycerol glutarate), poly(glycerol adipate), poly(glycerol pimelate), poly(glycerol suberate), poly(glycerol azelate), or any combination thereof; a grain size of the degradable microparticle is in a range of 2 micrometers to 1400 micrometers.
2. The method as claimed in claim 1, wherein a polydispersity index of the grain size of the degradable microparticle is in a range of 0.15 to 1.2.
3. The method as claimed in claim 1, wherein a shape of the degradable microparticle is spherical, water drop shaped, threaded, square, polyhedral, or any combination thereof.
4. The method as claimed in claim 1, wherein a structure of the degradable microparticle is a solid structure, a hollow structure, a porous structure, or any combination thereof.
5. The method as claimed in claim 1, wherein the degradable product is able to be degraded in seawater or non-seawater.
6. The method as claimed in claim 1, wherein the degradable product is able to be degraded in an aqueous solution with a pH value greater than or equal to 4 and less than or equal to 10.
7. The method as claimed in claim 1, wherein the degradable product is able to be degraded in static water or flowing water.
8. The method as claimed in claim 1, wherein the degradable product is able to be degraded in an enzyme solution.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0029] Examples were made to prove the degradation effects of the degradable microparticles of the present invention. Comparative Example of plastic microparticle was made to compare with the Examples. One person skilled in the arts can easily realize the advantages and effects of the degradable microparticles in accordance with the present invention from the comparison of the Examples and the Comparative examples. The descriptions proposed herein are just for the purpose of illustrations only, not intended to limit the scope of the invention. Various modifications and variations could be made in order to practice or apply the present invention without departing from the spirit and scope of the invention.
Examples 1 to 13: Preparation of PGM Microparticles
[0030] Firstly, glycerol and maleic acid (purchased from Sigma-Aldrich) were weighed at a mole ratio of 1:1, put into a two-neck bottle under an atmosphere of nitrogen gas and heated to a temperature of 130° C. for 0.5 hours to make the glycerol and the maleic acid fully dissolved and mixed, and then dehydrated under low pressure and a temperature of 160° C., so as to obtain a prepolymer. Finally, the prepolymer was cooled down to ambient temperature, and then was diluted with acetone with a purity of 99% at a weight ratio of 1:0.5 to 1:10, so as to obtain a prepolymer solution for use.
[0031] The aforesaid prepolymer solution was put into an injection pump, setting a caliber size of the injection pump in a range of 580 μm to 1200 μm, and then injecting the prepolymer solution at an injection rate of 0.1 milliliter per minute (mL/min) to 6.0 mL/min into a beaker containing silicon oil at a stirring speed of 400 revolutions per minute (rpm) to 1000 rpm at a temperature of 130° C. for 3 hours, so as to obtain a mixture. Subsequently, the mixture was filtered with membrane and washed with ethyl acetate to remove the unreacted silicone oil and/or the unreacted prepolymer, and then dried in a 50° C. oven for 24 hours, so as to obtain PGM microparticles of Examples 1 to 13.
[0032] The manufacturing parameters of the injection rate, the stirring speed, the dilution ratio and the caliber size corresponding to the PGM microparticle of each Example were listed in the following Table 1.
TABLE-US-00001 TABLE 1 the manufacturing parameters of the PGM microparticles of Examples 1 to 13 (E1 to E13) and the PGS microparticle of Example 14 (E14). Injection rate Stirring Dilution ratio Caliber size Example No. (mL/min) speed (rpm) (w/w) (μm) E1 0.1 1000 1:0.5 580 E2 0.5 1000 1:0.5 580 E3 1 1000 1:0.5 580 E4 3 1000 1:0.5 580 E5 6 1000 1:0.5 580 E6 1 400 1:0.5 580 E7 1 600 1:0.5 580 E8 1 800 1:0.5 580 E9 1 1000 1:1.sup. 580 E10 1 1000 1:5.sup. 580 E11 1 1000 1:10 580 E12 1 1000 1:5.sup. 925 E13 1 1000 1:5.sup. 1200 E14 1 1000 1:10 580
[0033] The mean of the grain size, the standard deviation (SD) of the grain size, the CV of the grain size and the PDI of the grain size of the PGM microparticle of each Example were listed in the following Table 2. The SD, the CV and the PDI of the grain size all could be directed to the closeness of the grain size of each Example prepared by different manufacturing parameters; the lower the SD, the CV and the PDI represents that the grain size is more uniform.
[0034] The calculation method of the CV of the grain size (%): dividing the SD of the grain size by the mean of the grain size×100%. The calculation method of the PDI of the grain size: dividing the square of the SD of the grain size by the square of the mean of the grain size.
TABLE-US-00002 TABLE 2 the mean, the SD, the CV and the PDI of the grain size of the PGM microparticles of Examples 1 to 13 (E1 to E13) and the PGS microparticle of Example 14 (E14). Mean SD CV Example No. (μm) (μm) (%) PDI E1 29.9 25.4 84.9 0.72 E2 31.2 26.4 84.9 0.72 E3 39.4 23.7 60.3 0.36 E4 79.5 80.5 101 1.03 E5 89.1 89.9 99.2 0.98 E6 112 77.7 64.9 0.48 E7 101 81.3 79.9 0.64 E8 66.8 41.9 62.7 0.39 E9 60.0 26.1 43.4 0.19 E10 30.2 13.0 43.1 0.19 E11 26.3 15.7 59.8 0.36 E12 39.7 20.1 50.6 0.26 E13 32 19.1 59.7 0.36 E14 26.0 13.6 52.3 0.27
Examples 14: Preparation of PGS Microparticle
[0035] Firstly, glycerol and sebacic acid (purchased from Sigma-Aldrich) were weighed at a mole ratio of 1:1, put into a two-neck bottle under an atmosphere of nitrogen gas and heated to a temperature of 130° C. for 1 hour to make the glycerol and the sebacic acid fully dissolved and mixed, and then dehydrated under low pressure and a temperature of 130° C., so as to obtain a prepolymer. Finally, the prepolymer was cooled down to ambient temperature, and then was diluted with acetone with a purity of 99% at a weight ratio of 1:10, so as to obtain a prepolymer solution for use.
[0036] The aforesaid prepolymer solution was put into an injection pump, setting a caliber size of the injection pump of 580 μm, and then injecting the prepolymer solution at an injection rate of 1.0 mL/min into a beaker containing silicon oil at a stirring speed of 1000 rpm at a temperature of 160° C. for 5 hours, so as to obtain a mixture. Subsequently, the mixture was filtered with membrane and washed with ethyl acetate to remove the unreacted silicone oil and/or the unreacted prepolymer, and then dried in a 50° C. oven for 24 hours, so as to obtain the PGS microparticle of Example 14.
[0037] The manufacturing parameters of the PGS microparticle of Example 14 were listed in Table 1 above. The mean, the SD, the CV and the PDI of the grain size of the PGS microparticle of Example 14 were listed in Table 2 above.
[0038] As shown in Table 2 above, the PDI of the grain size of the PGM microparticle of Example 10 was the lowest, which demonstrated that the grain size of the PGM microparticle of Example 10 was the most uniform compared with other examples. In addition, as shown in
Comparative Example 1: PLA Microparticle
[0039] The material of the PLA microparticle of Comparative Example 1 was purchased from Chiao Fu Material Technology Co., Ltd., and then was processed to obtain the PLA microparticle of Comparative Example 1.
Test Example 1: DI Water
[0040] First, 250 milligrams (mg) of each of the PGM microparticle of Example 10, the PGS microparticle of Example 14 and the PLA microparticle of Comparative Example 1 was stored in 15 mL of DI water at a rotation speed of 175 rpm at ambient temperature for a period of time. After that, each degradable microparticle and the PLA microparticle were observed by SEM, so as to obtain the degradation results of them.
[0041] Take the degradation results of the PGM microparticle of Example 10 in the DI water for illustration, and the results are shown in
Test Example 2: DI Water and Buffer Solutions with Different pH
[0042] In this test example, the PGM microparticle of Example 10, the PGS microparticle of Example 14 and the PLA microparticle of Comparative Example 1 were stored in buffer solutions with different pH to test the degradation effect. First, 250 mg of each aforesaid microparticle was stored in 15 mL of buffer solutions with different pH at a rotation speed of 175 rpm at ambient temperature for a period of time. After that, each microparticle during different degradation processes was observed by SEM, and 20 μL of the buffer solutions during different degradation processes were taken to analyze the variation of the TOC of the buffer solutions by a TOC analyzer, so as to obtain the degradation results of the degradable microparticles and the PLA microparticle.
[0043] Take the degradation results of the PGM microparticle of Example 10 in the buffer solutions with different pH for illustration, and the results are shown in
[0044] Take the degradation results of the PGS microparticle of Example 14 in a buffer solution of pH 10 for illustration, and the results are shown in
[0045] Take the degradation results of the PLA microparticle of Comparative Example 1 in the buffer solution of pH 10 for illustration, and the results are shown in
[0046] Take the variation of pH of the DI water and the buffer solutions with different pH when the PGM microparticle of Example 10 had been stored in them for a period of time for illustration, and the results are shown in
[0047] Next, take the TOC curves of the buffer solutions with different pH when the PGM microparticle of Example 10 had been stored in them for a period of time for illustration, and the results are shown in
[0048] As shown in
[0049] As shown in
[0050] As shown in
Test Example 3: DI Water and Synthetic Seawater
[0051] In this test example, the PGM microparticle of Example 10 and the PLA microparticle of Comparative Example 1 were stored in different types of water to test the degradation effect. First, 250 mg of each aforesaid microparticle was stored in 15 mL of the DI water and 15 mL of synthetic seawater at a rotation speed of 175 rpm at ambient temperature for a period of time. After that, 20 μL of the DI water and 20 μL of the synthetic seawater at different times during degradation were taken to analyze the variation of the TOC of the DI water and the synthetic seawater by the TOC analyzer, so as to obtain the degradation results of the degradable microparticle and the PLA microparticle.
[0052] As shown in
[0053] As shown in
Test Example 4: Static and Flowing DI Water and Static and Flowing Synthetic Seawater
[0054] In this test example, the PGM microparticle of Example 10 was stored in water of different fluidities to test the degradation effect. First, 250 mg of each aforesaid microparticle was stored in 15 mL of the DI water and 15 mL of the synthetic seawater at a rotation speed of 175 rpm at ambient temperature for a period of time. Both of the DI water and the synthetic seawater were divided into two groups: one of the groups had the water renewed every two days as flowing water, and the other group had the water unchanged as static water for comparison. After that, 20 μL of the DI water and 20 μL of the synthetic seawater at different times during degradation were taken to analyze the variation of the TOC of the DI water and the synthetic seawater by the TOC analyzer, so as to obtain the degradation results of the degradable microparticle.
[0055] As shown in
Test Example 5: Enzyme Solution
[0056] In this test example, the PGM microparticle of Example 10 and the PLA microparticle of Comparative Example 1 were stored in 20 units/mL of an enzyme solution to test the degradation effect. First, 250 mg of each aforesaid microparticle was stored in 15 mL of a PBS containing 10 units/mL of lipase of pH 7.4 at a rotation speed of 175 rpm at ambient temperature for a period of time. After that, each microparticle was observed by SEM at different times, and 20 μL of the PBS at different times during degradation was taken to analyze the variation of the carboxylic acid of the PBS by an ultraviolet-visible spectrophotometer, so as to obtain the degradation results of the degradable microparticle and the PLA microparticle.
[0057] Take the degradation result of the PGM microparticle of Example 10 in the PBS containing enzyme for illustration, and the result is shown in
[0058] Take the degradation result of the PLA microparticle of Comparative Example 1 in the PBS containing enzyme for illustration, and the result is shown in
[0059] As shown in
[0060] According to the results of Test Examples 1 to 5, the degradable microparticles of the present invention can obtain the desired degradation effect under different conditions such as solutions with different pH values, water types, fluidities, and solutions containing enzyme. In addition, the degradable microparticles of the present invention can be produced by chemical synthesis to reduce the production cost. With aforesaid advantages, the technical means of the present invention further improves the applicability of the degradable microparticles and replaces the use of the plastic microparticles, thereby overcoming the environmental problems caused by the plastic microparticles.
[0061] Even though numerous characteristics and advantages of the instant disclosure have been set forth in the foregoing description, together with details of the structure and features of the disclosure, the disclosure is illustrative only. Changes may be made in the details, especially in matters of material, shape, size, and arrangement of parts within the principles of the disclosure to the full extent indicated by the broad general meaning of the terms in which the appended claims are expressed.