Transparent and Insulating Materials Having Evacuated Capsules

Abstract

Transparent and insulating materials having evacuated capsules are provided. According to an aspect of the invention, a method includes forming evacuated capsules within a solution, and dispersing and suspending the evacuated capsules within the solution such that a packing density of the evacuated capsules within the solution is greater than 30%, and a visible light transmission of the solution including the evacuated capsules is greater than 75%. According to another aspect of the invention, a layer includes a plurality of evacuated capsules distributed within a dried sol-gel. A thermal conductivity of the layer is between 0.02 W/m-K and 0.001 W/m-K, and the layer has a visible light transmission of greater than 30%.

Description

BACKGROUND OF THE INVENTION

Presently, buildings account for approximately 40% of the energy usage and CO₂ emissions in the United States, and windows account for approximately 30% to 50% of the energy losses in buildings. This is because the vast majority of the trillions of square feet of installed windows have very poor energy efficiencies. Considering that the life expectancy of installed windows is greater than 30 years, it could take decades and tens of trillions of dollars before they are replaced with higher efficiency windows, and these new windows may still be less energy efficient than the walls and roofs of buildings.

To address the overall energy being consumed by buildings, improvements are needed in both space conditioning and building envelope technologies. However, while there are relatively inexpensive methods to treat the energy loss through roofs and walls of older buildings by applying low cost insulation, the only way to substantially improve the insulation value of windows is through replacement with relatively expensive new windows that typically require substantial construction and add substantial weight. While the walls and roofs of older buildings can be retrofitted to have R-values in the 15 to 50 range, new replacement windows typically have R values less than 3 and older windows have R values much less than 1. In addition, replacement of windows can be a very costly ($200 to $1000 just for the window) and arduous task. Thus, there is a need to improve the energy efficiency of installed windows in older buildings at a lower cost.

Presently, vacuum insulated glass (VIG), in which a vacuum is pulled between two panes of glass, provides an energy-efficiency solution for windows with thermal conductivities around 0.007 Watts per meter-degree Kelvin (W/m-K) (i.e., insulation value R12) with low-e coatings. However, VIG is expensive, with costs projected to be approximately $6/ft² (approximately 25% more than present conventional windows). Furthermore, VIG has substantial differential thermal expansion problems that require tempered glass, which also increases costs and reduces durability. Finally, due to the fact that VIG needs to be sealed at the edges, it is only available in preset assembled sizes, making use with retrofitting more expensive and difficult. Thus, it would be advantageous to retrofit installed windows and to develop new windows to improve energy efficiency by using transparent insulating materials that overcome the drawbacks of VIG, such as high cost, low durability, edge seal leaking, and weight problems.

Recently, hollow glass microspheres (HGMs), also known as glass bubbles, have been incorporated into insulation systems, hydrogen storage, and other applications. Typically, these HGMs are on the order of 10 micrometers to 1000 micrometers in diameter, and scatter visible light. HGMs may be filled with a fluid or gas, evacuated, and/or coated with materials such as dielectrics and metals. Commercially available HGMs that have not been evacuated are used to improve the insulating value of many products including paint, vacuum insulating panels, and insulation for cryogenic applications. However, the size, thickness, and/or density of the HGMs needed to achieve a high insulation value prevents their use as a transparent layer.

When used in very thin layers, such as a monolayer or two of HGMs, HGMs can be used for antireflection coatings for windows, for visibly transparent applications, and to improve the optical quality of glass. For example, when used as an antireflection coating, HGMs improved the transmission of visible light from approximately 90% to 96%, while reducing the reflection from 8% to 2%. However, these layers are too thin to provide a substantial increase of the insulation value. Further, CN102618016 discloses a method of incorporating evacuated HGMs within a resin matrix to produce a transmissive and insulating film. However, because the HGMs are limited to 1% of the mass of the resin, the reduction in the thermal conductivity of the film is minimal. Specifically, the thermal conductivity of the film is reported to be approximately 0.05 W/m-K. Accordingly, it would be advantageous to provide a method of producing a film in which the thermal conductivity is substantially reduced while the visible light transmission is maintained.

SUMMARY OF THE INVENTION

Exemplary embodiments of the invention use evacuated capsules to provide transparent and insulating materials. According to an aspect of the invention, a method includes forming evacuated capsules within a solution, and dispersing and suspending the evacuated capsules within the solution such that a packing density of the evacuated capsules within the solution is greater than 30%, and a visible light transmission of the solution including the evacuated capsules is greater than 75%.

The dispersing and suspending of the evacuated capsules may include adjusting a pH of the solution to a value between 9 and 14, and adding a polycation or a polyanion to the solution. The packing density of the evacuated capsules within the solution may be greater than 70%.

The method may also include processing the solution with a sol-gel method, and drying the processed solution to form a layer. The method may also include adding a strengthening agent to the solution before processing the solution. The strengthening agent may include poly(vinyl alcohol) and/or boric acid.

Forming the evacuated capsules may include forming templates using dodecanethiol and cetyl-trimethylammonium bromide, coating the templates with a silica-gel, and heating the templates to a temperature of at least 250° C. in vacuum. Forming the evacuated capsules may also include performing atomic layer deposition, physical vapor deposition, chemical vapor deposition, or solution phase deposition to deposit a low-emissivity coating on shells formed by heating the templates.

Each of the evacuated capsules may have a lateral dimension between 50 nm and 300 nm. The lateral dimension may be between 80 nm and 100 nm.

According to another aspect of the invention, a layer includes a plurality of evacuated capsules distributed within a dried sol-gel. A thermal conductivity of the layer is between 0.02 W/m-K and 0.001 W/m-K, and the layer has a visible light transmission of greater than 30%.

Each of the evacuated capsules may have a lateral dimension between 50 nm and 300 nm. The lateral dimension may be between 80 nm and 100 nm. A packing density of the evacuated capsules within the dried silica-gel is greater than 30%. The packing density may be greater than 70%.

Each of the evacuated capsules may include a silica shell. Each of the evacuated capsules may also include a low-e coating formed on the silica shell. The low-e coating may include at least one of tin oxide or zinc oxide.

The visible light transmission may be greater than 75%. At least one of the evacuated capsules may include a plurality of primary shells surrounded by a secondary shell.

Other objects, advantages, and novel features of the present invention will become apparent from the following detailed description of the invention when considered in conjunction with the accompanying drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows a flowchart of a method of forming a transparent and insulating film according to exemplary embodiments of the invention;

FIG. 2 shows a flowchart of a solution phase method for forming capsules according to exemplary embodiments of the invention;

FIGS. 3(a) and 3(b) show a scanning electron microscopy (SEM) image and a transmission electron microscopy (TEM) image, respectively, of capsules that were constructed to have a diameter between 80 nm and 100 nm;

FIG. 4 shows an example of the temperature-programmed desorption spectra of evacuated capsules;

FIG. 5(a) shows an example of evacuated capsules as formed in a solution, and 5(b) shows an example in which the evacuated capsules are dispersed and suspended within the solution in order to increase the transparency;

FIG. 6 shows a flowchart of a method of integrating evacuated capsules to form a layer according to exemplary embodiments of the invention;

FIG. 7 shows an example of a layer that was produced by exemplary embodiments of the invention; and

FIG. 8 shows the measured transmission of a film that was produced by exemplary embodiments of the invention.

DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS

FIG. 1 shows a flowchart of a method of forming a transparent and insulating film according to exemplary embodiments of the invention. Evacuated capsules are incorporated into a layer of material to achieve the high R values needed for window applications, such as R-5 to R-20, with a layer thickness between 0.125 inches and 0.25 inches. As discussed in further detail below, the size and arrangement of the evacuated capsules are designed to minimize the effect of the layer on the transparency of a window to which the layer will be applied.

As shown in FIG. 1, the method begins by forming capsules at step 100. In general, related art commercial manufacturing of HGMs involves blowing air or gases through molten glass. Because of viscosity limitations, this method cannot make glass bubbles smaller than about 10 micrometers in diameter. In contrast, exemplary embodiments of the invention may use solution phase processes to form capsules having a lateral dimension between 50 nm and 300 nm. For example, solution phase processes involving approximately 0.1 liter of solution may be used to create 5 to 10 mL of silica capsules with different sizes (e.g., a diameter between 70 nm and 120 nm) and shapes (e.g., spherical, spheroid, pseudo-cylindrical, pseudo-cubic, and capsules with concave sides). For example, an efficient spray process using liquid sources may be used to form hollow silica structures from a templating route using either aerosol spray pyrolysis or plasma spray processes.

FIG. 2 shows a flowchart of a solution phase method for forming the capsules according to exemplary embodiments of the invention. During the solution phase method, templates are formed using dodecanethiol (C₁₂—SH), cetyl-trimethylammonium bromide (CTAB), and trimethylbenzene (TMB) at step 200. The C₁₂—SH, CTAB, and TMB form nano-emulsion droplets that serve as the templates. As an alternative, poly(methyl methacrylate) (PMMA) may be used to form the nano-emulsion droplets instead of the C₁₂—SH, CTAB, and TMB. In one example, the C₁₂—SH, CTAB, and TMB are mixed in water at a temperature of 80° C. and a mixing speed of 2500 RPM. The molar ratio of TMB to CTAB may be 2, and may be adjusted to between 3 and 4. The molar ratio of TMB to CTAB, the amount of C₁₂—SH, and the initial amount of TEOS may be adjusted to create templates with different shapes. The C₁₂—SH to CTAB ratio and stirring speed may also be changed to adjust the morphology and structure of the templates. For example, by adjusting the molar ratio of TMB to CTAB to between 3 and 4, decreasing the initial amount of TEOS from 1.5 ml to 0.75 ml/100 ml solvent, and then adding the remaining TEOS after 2 hours, concave shells can be made that increase the stacking density of the capsules. Also, by adjusting the stirring speed from approximately 2500 revolutions per minute to 2000 revolutions per minute, and adding 1 ml TEOS per 100 ml of solvent, to start, more cubical or oblate spheroids can be synthesized.

The templates may then be coated with a silica-gel such as tetraethoxysilane (TEOS) in step 210. The silica-gel may coat individual templates and/or groups of templates. The templates are then removed by evaporation and the silica-gel is dried at high temperatures of approximately 50° C. at step 220, thereby creating hollow silica shells. In general, any material may be used for the templates, provided that it has the desired size and shape to form the shells, and can be removed after the shells are formed.

Primary shells may be formed by coating individual templates with silica-gel in step 210, while secondary shells may be formed by coating multiple templates that are in contact with each other with silica-gel in step 210. The thicknesses of the primary and secondary shells may be varied from a few nanometers to 20 nm based on the amount of silica-gel that is added during step 210. Further, the silica-gel may be injected into the solution at different times after introducing the initial silica-gel. This causes the primary shells to have different thicknesses and forms the secondary shells around multiple primary shells, such that the secondary shells have longer shapes that are similar to cylinders.

FIGS. 3(a) and 3(b) show a scanning electron microscopy (SEM) image and a transmission electron microscopy (TEM) image, respectively, of capsules that were constructed to have a diameter between 80 nm and 100 nm. As shown in FIGS. 3(a) and 3(b), the geometry of the capsules may be adjusted to have a cubic shape with a high stacking density and/or non-spherical shapes by the methods discussed above.

A low-emissivity (low-e) coating may also be deposited on the silica shells at step 230. The low-e coating is transparent in the visible range of the spectrum (from 390 to 700 nm) and reflects more than 50% in the far infrared range of the spectrum (from 8 to 13 μm). An oxide layer may be used as the low-e coating. For example, tin oxide and/or zinc oxide may be deposited on the silica shells by using atomic layer deposition (ALD). In this case, the silica shells are placed in a vacuum chamber, and vapor phase tin oxide and/or zinc oxide is deposited monolayer-by-monolayer to achieve the desired thicknesses and low-e properties. Alternatively, the low-e coating may be applied by physical vapor deposition, chemical vapor deposition, or solution phase deposition. The low-e coating may have a thickness between 0.5 nm and 10 nm. As another alternative, the low-e coating may be incorporated into the silica-gel that is used to form the shells.

Once the capsules have been formed at step 100, the capsules are then evacuated at step 110. FIG. 4 shows the temperature-programmed desorption spectra of evacuated capsules. In this example, the air is first evacuated from the secondary shells at a temperature of approximately 250° C., and is then evacuated from the primary shells at a temperature of approximately 400° C. As the temperature increases, the gas diffusion through the silica shells increases. For this specific sample, at approximately 400° C., gasses (such as the water shown in FIG. 4) start to come out from inside the silica shells, as measured by a mass spectrometer in the vacuum chamber. Over time, all of the water and the other gasses come out of the shells, leaving behind a vacuum inside of the shells.

The temperature applied at step 110 may be adjusted based on the thickness, composition, and structure of the capsules. For example, thicker and denser shells require higher temperatures to be evacuated. Further, the chemical composition of the capsules can affect the molecular transport rate through the shells, thus affecting the temperature needed for transport. A final pressure inside the capsules of less than 1 microtorr may be achieved to minimize the thermal conductivity. However, the internal pressure of the capsules may vary depending on the desired thermal conductivity, with a lower pressure required for higher thermal conductivities.

As shown in FIG. 1, the evacuated capsules are then dispersed and suspended in the solution at step 120. This step may be performed at ambient temperature and pressure. FIG. 5(a) shows an example of evacuated capsules as formed in a solution by the methods discussed above. As shown in FIG. 5(a), the evacuated capsules initially agglomerate together to form clusters that are large enough to scatter light, and thus create a whitish-colored and opaque solution. In contrast, FIG. 5(b) shows an example in which the evacuated capsules are subsequently dispersed and suspended within the solution in order to increase the transparency. This may be achieved by adjusting the pH of the solution to a value between 9 and 14, and/or adding a dispersant to the solution. In this example, the evacuated capsules are dispersed and suspended such that the visible light transmission is greater than 85%. However, the visible light transmission may have any value greater than 75%. The pH of the solution may be adjusted by adding a material such as sodium hydroxide. The dispersant may be a polycation such as poly(diallyldimethylammonium chloride) (PDDA) or a polyanion such as sodium poly(4-styrenesulfonate (PSS). The evacuated capsules remain dispersed in the solution indefinitely such that the visible light transmission of the solution is maintained. The packing density of the evacuated capsules within the solution may be greater than 30%. A higher packing density greater than 70% may maintain the visible light transmission, while minimizing the number and size of air pockets to keep the insulation value as high as possible. The evacuated capsules are dispersed to prevent clusters that are larger than the wavelength of visible light from forming and acting as light scattering centers.

As shown in FIG. 1, the evacuated capsules are then integrated by additional sol-gel processes to form a solid layer at step 130. The details of this process are shown in FIG. 6, which may include adding 1 mL of boric acid, poly(vinyl alcohol) (PVA), and glycerol (diluted 100 to 1 in water) to the solution in which the evacuated capsules were dispersed and suspended in step 120. As shown in FIG. 6, the PVA and the boric acid act as strengthening agents at step 300. The process continues at step 310, in which the solution is processed with a sol-gel method. For example, the solution may be added to 4 mL of TEOS in 4 mL of methanol with a drop of concentrated HCl that has been stirring at 300 revolutions per minute and room temperature for 2 hours. This mixture is stirred for about 30 seconds, poured into pans, and let sit overnight to form sol-gels.

The sol-gels are then dried by any suitable method at step 320. For example, the sol-gels may be covered in methanol and heated at 50° C. for 4 hours. All of the liquids are then removed and the sol-gels are covered with methanol again. This process is repeated for a total of 4 times. The sol-gels are then covered loosely in a petri dish and allowed to dry at ambient conditions for a few days to a few weeks. A drying agent such as trimethylchlorosilane may be used after the second rinse to make the surfaces more hydrophobic and accelerate the removal of water.

In another example, the sol-gels may be placed in a super-critical CO₂ drying chamber after the second rinse with methanol. CO₂ is then added at a pressure above approximately 6 bar at ambient temperature, to cover the sol-gels in liquid CO₂. The sol-gels are soaked for 2 hours, and this process is repeated 3 more times. The sol-gels are then removed from the drying chamber and allowed to sit in a loosely covered petri dish for a few hours to completely dry out.

In yet another example, the sol-gels may be covered in equal parts methanol and toluene in a sealed chamber. The sol-gels are heated to a temperature between 150° C. and 250° C., and the pressure is released quickly by opening a vent valve. The ratio of methanol and toluene may be adjusted to affect the critical point temperature based on the standard rule of mixtures and vapor point knowledge in the literature, and to optimize the rapid removal of solvent from the sol-gel pores without collapsing the pores due to surface tension from the solvent.

Although the secondary shells are optional, they provide more volume that can be evacuated, such that there is less volume with air once the transparent film is formed. Preferably, the evacuated capsules have a cubic or cylindrical shape, and are packed closely together to form a stack with very little air between the evacuated capsules. The packing density of the evacuated capsules within the dried sol-gel material may be greater than 30%. Advantageously, the packing density may be greater than 70%, in order to maximize the insulation value of the film.

An example of a layer produced by the methods discussed above is shown in FIG. 7. The layer includes the evacuated capsules that are distributed within the dried sol-gel material. In this example, the layer is a film having a visible light transmission greater than 85%, a haze between 0% and 10%, a thickness of approximately 5 mm, and a diameter of approximately 75 mm. The measured transmission of the film is shown in FIG. 8. For most window applications, the film may be formed to have a visible light transmission greater than 75%. However, for applications in which tinting is required, the film may be formed to have a lower visible light transmission, such as greater than 30%. Tinting may be achieved by forming nanometer thick films of electrically conducting materials, such as metals, graphitic carbon, tin oxide, and zinc oxide, on the evacuated capsules, where the oxide deposition process is adjusted to give the films more metallic properties. Advantageously, the thermal conductivity of the film may be less than 0.02 W/m-K without a low-e coating, and between 0.01 and 0.001 W/m-K with a low-e coating. The thermal conductivity of the film depends on the thermal conductivity of the evacuated capsules, as well as the structure and configuration of the film. The film may be integrated between plastic films or glass sheets in order to provide a thermally insulating material that has a minimal effect on the visible transparency of the window on which it is ultimately affixed.

The foregoing disclosure has been set forth merely to illustrate the invention and is not intended to be limiting. Since modifications of the disclosed embodiments incorporating the spirit and substance of the invention may occur to persons skilled in the art, the invention should be construed to include everything within the scope of the appended claims and equivalents thereof.

Claims

1. A method comprising: forming evacuated capsules within a solution; anddispersing and suspending the evacuated capsules within the solution such that a packing density of the evacuated capsules within the solution is greater than 30%, and a visible light transmission of the solution including the evacuated capsules is greater than 75%.

2. The method according to claim 1, wherein the dispersing and suspending of the evacuated capsules comprises: adjusting a pH of the solution to a value between 9 and 14, andadding a polycation or a polyanion to the solution.

3. The method according to claim 1, wherein the packing density is greater than 70%.

4. The method according to claim 1, further comprising: processing the solution with a sol-gel method; anddrying the processed solution to form a layer.

5. The method according to claim 4, further comprising adding a strengthening agent to the solution before processing the solution.

6. The method according to claim 5, wherein the strengthening agent comprises at least one of poly(vinyl alcohol) or boric acid.

7. The method according to claim 1, wherein forming the evacuated capsules comprises: forming templates using dodecanethiol and cetyl-trimethylammonium bromide;coating the templates with a silica-gel; andheating the templates to a temperature of at least 250° C. in vacuum.

8. The method according to claim 7, wherein forming the evacuated capsules further comprises performing atomic layer deposition, physical vapor deposition, chemical vapor deposition, or solution phase deposition to deposit a low-emissivity coating on shells formed by heating the templates.

9. The method according to claim 1, wherein each of the evacuated capsules has a lateral dimension between 50 nm and 300 nm.

10. The method according to claim 9, wherein the lateral dimension is between 80 nm and 100 nm.

11. A layer comprising: a plurality of evacuated capsules distributed within a dried sol-gel; wherein:a thermal conductivity of the layer is between 0.02 W/m-K and 0.001 W/m-K, andthe layer has a visible light transmission of greater than 30%.

12. The layer according to claim 11, wherein each of the evacuated capsules has a lateral dimension between 50 nm and 300 nm.

13. The layer according to claim 12, wherein the lateral dimension is between 80 nm and 100 nm.

14. The layer according to claim 11, wherein a packing density of the evacuated capsules within the dried silica-gel is greater than 30%.

15. The layer according to claim 14, wherein the packing density is greater than 70%.

16. The layer according to claim 11, wherein each of the evacuated capsules comprises a silica shell.

17. The layer according to claim 16, wherein each of the evacuated capsules further comprises a low-e coating formed on the silica shell.

18. The layer according to claim 17, wherein the low-e coating comprises at least one of tin oxide or zinc oxide.

19. The layer according to claim 11, wherein the visible light transmission is greater than 75%.

20. The layer according to claim 11, wherein at least one of the evacuated capsules comprises a plurality of primary shells surrounded by a secondary shell.