Patent Application
20240375316
The present disclosure relates to the field of material preparation, in particular to a single-component silica gel medium suitable for direct ink writing 3D printing, a preparation method and application thereof.
3D printing, as a new precision processing and manufacturing technology, is featured in an additive manufacturing process developed from nothing in the manufacturing process, which is different from a subtractive manufacturing process as the traditional process, in which redundant materials tend to be subtracted gradually until no materials are available. Compared with the traditional manufacturing process, the 3D printing technology featuring additive manufacturing has higher flexibility and practicability. At present, common 3D printing technologies include fused deposition modeling (FDM), stereo lithography appearance (DLP (digital light processing), CLIP (continuous liquid interface production), or PolyJet), selective laser sintering (SLA and SLS), three-dimensional printing (3DP), and the like, however, none of these 3D printing technologies is made available to the printing of precision structures with silica gel media.
Direct ink writing (DIW) printing, as an emerging 3D printing technology, has been widely applied in electronic devices, structural materials, histological engineering, soft robotics, and other fields by extruding semisolid ink materials with shear thinning properties out of a printer head and stacking them layer upon layer to constitute a preliminarily designed three-dimensional structure. At present, this technology may fit very happily with silica gel medium materials in the precision processing of products.
Technologies for researching silica gel printing media are also provided in the prior art, for example, CN105643939B and CN107674429A have disclosed 3D printing silica gel and a printing method thereof, respectively. However, single-component silica gel materials therefor have a short storage cycle and may pose the risk of being susceptible to the blockage of the printer head resulting from thickening, gelling or coarse particles during printing. CN106313505A and C′N107638231A have disclosed a two-component mixed silica gel 3D printer and a printing method thereof, in which no specific technical details of two-component mixed silica gel were disclosed, and the temperature of annular heating sheets is as high as 100° C. to 400° C. during printing, which results in the blockage of the printer head due to gelling of the silica gel therein at high temperature.
In summary, at present, no silica gel materials which may be well adapted to direct ink writing 3D printing are available in the market, which, in turn, poses a limit to the market promotion and application of 3D printing technologies.
In the prior art, 3D printing silica gel has a short storage cycle and may pose the risk of being susceptible to the blockage of the printer nozzle resulting from thickening, gel (high temperature) or coarse particles during printing.
The present disclosure aims to provide a single-component silica gel medium suitable for direct ink writing 3D printing, a preparation method and application thereof. The single-component silica gel medium is suitable for the high-precision printing of micron-sized lines, with the combination of high viscosity and stability.
In order to fulfill the above objective, in the first embodiment, the present disclosure provides a single-component silica gel medium suitable for a direct ink writing 3D printing process. A viscosity of the single-component silica gel medium is 200 to 1000 Pa·s, and a viscosity change value is smaller than or equal to 10% after the single-component silica gel medium is stored at room temperature for more than 30 days.
In some embodiments, a cone penetration of the single-component silica gel medium is 120 to 280*0.1 mm at 25° C.
The single-component silica gel medium suitable for the direct ink writing 3D printing process is prepared by a preparation method, including the following steps of S1, mixing polysiloxane containing carbon-carbon double bonds, a tackifier, and a platinum catalyst to obtain a first mixture; S2, heating the first mixture and holding for first time, adding a polymerization inhibitor and holding for second time to obtain a second mixture; S3, cooling the second mixture, and mixing the second mixture with hydrogen-containing polysiloxane to obtain a third mixture; S4, mixing the third mixture with an inorganic nano-filler to obtain a fourth mixture; and S5, performing vacuum defoamation and filtration under pressure on the fourth mixture sequentially to obtain the single-component silica gel medium.
In the second embodiment, the present disclosure provides a preparation method of a single-component silica gel medium suitable for a direct ink writing 3D printing process, including the following steps:
In step S1, the polysiloxane containing carbon-carbon double bonds and the tackifier are mixed and cross-linked at an appropriate temperature under an action of the platinum catalyst to form a reticular cross-linked polymer, and thus, the first mixture obtained in step S1 is the reticular cross-linked polymer, which is advantageous in that the obtained first mixture can maintain a good shape retention during printing under an intrinsic reticular frame. This can prevent printed lines from collapsing due to leveling, thereby obtaining a pattern with a height-width ratio larger than 0.5.
In this cross-linking reaction, the polysiloxane containing carbon-carbon double bonds is mixed as a primary component. The polysiloxane, the tackifier, and the platinum catalyst are mixed at the following ratio: the amount of the polysiloxane is 200 to 2000 times as large as that of the catalyst, and is 2 to 10 times as large as that of the tackifier. In some embodiments, the ratio of the polysiloxane to the tackifier to the catalyst is 100:10-50:0.05-0.5. Preferably, the ratio of the polysiloxane to the tackifier to the catalyst is 100:30:0.1; and the ratio of the polysiloxane to the tackifier to the catalyst is 100:20:0.3.
The polysiloxane containing carbon-carbon double bonds is selected from at least one of vinyl polysiloxane, methylvinyl polysiloxane, and methylphenylvinyl polysiloxane. In the case that the polysiloxane containing carbon-carbon double bonds is the vinyl polysiloxane, vinyl of the vinyl polysiloxane sits at an alpha, omega or middle position of a polysiloxane molecular chain, a viscosity of the vinyl polysiloxane is 50 to 500 Pa·s, a vinyl content is 0.05 to 10 mol %, every molecule in the vinyl polysiloxane contains more than two vinyl functional groups linked with silicon atoms, and a molecular weight is (40-100)*104.
The platinum catalyst is prepared from chloroplatinic acid or at least one of complexes formed by the chloroplatinie acid and alkene, cycloalkane, alcohol, ester, ketone and ether, and preferably, is a Speier platinum catalyst or a Karstedt platinum catalyst with the platinum metal content of 0.1-5%, and a mass fraction of the catalyst added to the medium material is 0.1-0.5%.
The tackifier is selected from one or more of HO—Si(CH3)2O[Si(CH3)2O]nSi(CH3)2—OH (n=3 to 8), hexamethylcyclotrisiloxane (D3), octamethyl cyclotetrasiloxane (D4), decamethylcyclopentasiloxane (D5), and a dimethylsiloxane cyclic mixture (DMC).
In step S2, the first mixture is heated to 50° C. to 80° C. The first mixture is stabilized at any temperature of 50° C. to 80° C. for first time, which facilitates a cross-linking reaction between the tackifier and the polysiloxane containing carbon-carbon double bonds to improve a degree of cross-linking of the material, thereby boosting the integrated viscosity and shape, retention of the final material, wherein the first time ranges from 30 to 180 minutes, which may be 40/50/60/70/80/90:100/110 minutes; and the first mixture may also be stabilized at 60° C./70° C.
The polymerization inhibitor added in step S2 may effectively inhibit the activity of the platinum catalyst to further stop the cross-linking reaction of the first mixture. The material that keeps stabilized at room temperature is obtained, which further improves the stability of the final single-component silica gel medium. The silica gel medium is not polymerized at room temperature in the presence of the polymerization inhibitor. The silica gel medium may be further polymerized only after the polymerization inhibitor is volatilized at a higher temperature and after the catalytic activity of the platinum catalyst is recovered, thereby finally achieving thermocuring. This is, the second mixture is added with the polymerization inhibitor compared with the first mixture to ensure that the silica gel medium may still maintain the high stability at room temperature on the premise of the high shape retention.
The polymerization inhibitor is alkynol having less than 15 carbon atoms, and preferably, is selected from one or more of 1-ethynyl-1-cyclohexanol, 2-methyl-3-butyn-2-ol, propargyl alcohol, 3-butyn-1-ol and 3,5-dimethyl-1-hexyne-3-ol, and the mass fraction of the inhibitor added to the medium material is 0.1 to 2%.
In step S3, the addition of the hydrogen-containing polysiloxane may achieve the effect of improving the degree of polymerization to which the material is cured and the final hardness of the cured material. In addition, the addition of the hydrogen-containing polysiloxane in step S3 may also ensure that the catalytic effect of the platinum catalyst on the hydrogen-containing polysiloxane is higher.
In the embodiments of the present disclosure, the amount of the hydrogen-containing polysiloxane is 1 to 10 times as much as that of the polysiloxane containing carbon-carbon double bonds. That is, a ratio of the polysiloxane containing carbon-carbon double bonds to the hydrogen-containing polysiloxane is 100:10-100. In some preferred embodiments, a ratio of the polysiloxane containing carbon-carbon double bonds to the hydrogen-containing polysiloxane is 1:2.
The hydrogen-containing polysiloxane is selected from at least one of hydrogen-containing methylpolysiloxane, hydrogen-containing methylphenylpolysiloxane, hydrogen-containing methyl silicone resin, and hydrogen-containing phenyl silicone resin, wherein a viscosity of the hydrogen-containing polysiloxane is 50 to 500 Pa·s, a hydrogen content is 0.1 to 1 mol %; and every molecule in the hydrogen-containing polysiloxane contains more than two hydrogen atoms linked with the silicon atoms, and a molecular weight is (40-100)*104.
In step S3, the second mixture is cooled to 20° C. to 40° C., which may be 25° C./30° C./35° C.
In step S4, the inorganic nano-filler is added to the third mixture for the purpose of improving the shearing stress of the material to boost the stability of extrusion during printing.
The inorganic nano-filler is selected from one or more of silicon dioxide, calcium silicate, calcium carbonate, titanium dioxide, carbon black, graphene and zinc oxide, with a size ranging from 1 to 500 nm.
A mixed means provided by the present disclosure may be one or more of ball milling, grinding, or mechanical stirring, which is sufficient to ensure the uniform mixing of the mixed materials.
In the third embodiment, the present disclosure provides application of the single-component silica gel medium prepared according to the preparation method in direct ink writing 3D printing, in which a printed line width is 1 to 200 μm. As a result, the single-component silica gel medium is applicable to the printing of a line with a height-width ratio larger than 0.5.
Compared with the prior art, the technical solution has the following characteristics and beneficial effects:
The technical solutions in the embodiments of the present disclosure will be clearly and completely described below with reference to the drawings in the embodiments of the present disclosure, and apparently, the described embodiments are merely part, rather than all of the embodiments of the present disclosure. All other embodiments derived by those ordinarily skilled in the art based on the embodiments given herein are intended to be within the scope of protection of the present disclosure.
It is understood that the terms “a” and “an” should be interpreted as “at least one” or “one or more”, meaning that a number of one element may be one in one embodiment, while a number of the element may be plural in other embodiments, and the terms “a” and “an” should not be interpreted as limiting the number.
The implementations of the present disclosure will be explained by specific embodiments. Other advantages and effects of the present disclosure will be readily apparent to those skilled in the art from the disclosure herein. It is to be understood that the scope of the present disclosure is not limited to the specific embodiments described below. It is also to be understood that the terms used in the embodiments are for the purpose of describing particular embodiments only, and is not intended to limit the scope of the present disclosure. The test methods in the following embodiments, in which specific conditions are not indicated, are generally carried out based on the conventional methods or the conditions as suggested by respective manufacturers.
The viscosity of the single-component silica gel medium is tested via a viscometer, which is 200 Pa·s. Cone penetrations for 30 days are tested using a cone penetrometer (25° C., and 0.1 mm), which are 276 (initial) and 278 (after 30 days) respectively. The material shows the excellent storage stability.
Application test: as shown in
The viscosity of the single-component silica gel medium is tested via a viscometer, which is 500 Pa·s. Cone penetrations for 30 days are tested using a cone penetrometer (25° C., and 0.1 mm), which are 178 (initial) and 180 (after 30 days) respectively. The material shows the excellent storage stability.
Application test: as shown in
The viscosity of the single-component silica gel medium is tested via a viscometer, which is 1000 Pa·s. Cone penetrations for 30 days are tested using a cone penetrometer (25° C. and 0.1 mm), which are 120 (initial) and 119 (after 30 days) respectively. The material shows the excellent storage stability.
Application test: as shown in
the usage amount is the same as that in Embodiment 1, and the method process is different therefrom in that:
Without heating, all raw materials are mixed evenly and transferred into the three-roller mill for grinding.
Material viscosity: 150 Pa·s. Cone penetrations for 30 days are tested using a cone penetrometer (25° C., and 0.1 mm), which are 308 (initial) and 158 (after 30 days) respectively. The material shows the increasing hardness and the poor storage stability after being stored for a long time. As shown in
The comparison between Comparative Example 1 and Embodiment 1 shows that according to the present disclosure, the single-component silica gel medium obtained by cross-linking the polysiloxane containing carbon-carbon double bonds with the tackifier under the induction of the catalyst, and then, adding the polymerization inhibitor has higher viscosity and higher stability at room temperature, and yields the better line width ratio when applied to 3D printing.
The operation steps are the same as those in Embodiment 1, with the slight difference in that the tackifier of the hexamethylcyclotrisiloxane (D3) in step (1) is removed.
Material viscosity: 80 Pa·s. Cone penetrations for 30 days are tested using a cone penetrometer (25° C., and 0.1 mm), which are 356 (initial) and 268 (after 30 days) respectively. The material shows the increasing hardness and the poor storage stability after being stored for a long time. As shown in
The comparison between Comparative Example 2 and Embodiment 1 shows that according to the present disclosure, the polysiloxane containing carbon-carbon double bonds may be cross-linked to form the reticular cross-linked polymer under the assistance of the tackifier to further improve the stability of the single-component silica gel medium while boosting the viscosity thereof. In addition, the addition of the tackifier is also of great significance for the printed line width.
The operation steps are the same as those in Embodiment 1, with the slight difference in that the polymerization inhibitor of the 1-ethynyl-1-cyclohexanol in step (2) is removed. Final material performance:
Material viscosity: 270 Pa·s. A cone penetration for 30 days is tested using a cone penetrometer (25° C. and 0.1 mm), which is 246 (initial) and 140 (after 30 minutes), indicating the poor storage stability. The hardness of the cured material is tested by a Shore A durometer, which is 46.
The operation steps are the same as those in Embodiment 1, with the slight difference in that the Karstedt platinum catalyst in step (1) is removed.
Material viscosity: 80 Pa·s. Cone penetrations are tested using a cone penetrometer (25° C., and 0.1 mm), which are 428 (initial) and 430 (after 30 days). The material is stable after being stored for a long time. Due to no platinum catalyst, the material cannot be cured.
The component A and the component B of the single-component silica gel are mixed at a ratio of 1:1. Cone penetrations are tested using a cone penetrometer (25° C., and 0.1 mm), which are 296 (initial) and 168 (after 12 hours), indicating the material has poor storage stability. As shown in
The performance tests of the single-component silica gel media in the above embodiments and Comparative Examples are summarized as follows:
aTest the material after storing it for 30 minutes.
bTest the material after storing it for 12 h.
The above table clearly shows that the dual-component silica gel medium materials of Embodiments 1 to 3 provided by the present disclosure have the excellent performance. The preparation method provided by the present disclosure is particularly advantageous.
The present disclosure is not limited to the above preferred implementation, and any other various products can be obtained by anyone under the inspiration of the present disclosure, but any changes in shapes or structures thereof, which are similar or identical to the technical solution of the present application, fall within the protection scope of the present disclosure.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202210069440.7 | Jan 2022 | CN | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2022/139958 | 12/19/2022 | WO |
