BORON CARBIDE BILAYER FOAM SOLAR EVAPORATOR AND METHOD FOR PREPARING THEREOF

Abstract

The present invention provides a solar absorber incorporated bilayer foam solar evaporator for seawater and wastewater purification including a plurality of solar absorbers partially incorporated into a porous polymer framework and partially forming a thermal insulation layer proximal to solar irradiation. In particular, low-cost commercially available B.sub.4C powders are embedded into a porous polymer foam in a one-pot method to form a scaffold of boron carbide bilayer foam (BCBF) with good hydrophilic wettability, heat-shielding, and solar-thermal conversion. The boron carbide bilayer foam (BCBF) of the present invention enables a high cost-performance seawater desalination and wastewater purification at a high evaporation rate of 2.8 kg/m.sup.2/h with 93% solar evaporation efficiency under 1 sun illumination (or 1 kW/m.sup.2). The present invention thereby provides an excellent and cost-effective solar evaporator tool for industrial-level water purification. Following the present method to prepare the BCBF solar evaporator, the fabrication cost can be as low as 3.6 $/m.sup.2.

Claims

1. A solar absorber incorporated bilayer foam solar evaporator for seawater and wastewater treatment comprising a porous polymer framework; and a plurality of hydrophilic solar absorbers partially incorporated into the porous polymer framework and partially forming a thermal insulation layer while the porous polymer framework incorporated with the hydrophilic solar absorbers providing a highly wettable structure to facilitate water transportation under solar irradiation of at least 1 kW/m.sup.2 in ambient air.

2. The solar absorber incorporated bilayer foam solar evaporator of claim 1, wherein the porous polymer framework comprises one or more polymers of polyvinyl alcohol (PVA), polydimethylsiloxane (PDMS), polyurethane (PU) and melamine.

3. The solar absorber incorporated bilayer foam solar evaporator of claim 1, wherein the plurality of solar absorbers is selected from boron carbide.

4. The solar absorber incorporated bilayer foam solar evaporator of claim 1, wherein the thermal insulation layer is disposed proximal to the solar irradiation and distal to a contact surface of the solar evaporator with the seawater or wastewater.

5. The solar absorber incorporated bilayer foam solar evaporator of claim 4, wherein the porous polymer framework is disposed proximal to the contact surface of the solar evaporator with the seawater or wastewater and distal to the solar irradiation.

6. The solar absorber incorporated bilayer foam solar evaporator of claim 2, wherein the solar absorbers have a water contact angle of about 44°.

7. The solar absorber incorporated bilayer foam solar evaporator of claim 2, wherein the plurality of solar absorbers is in a weight ratio of 1:2-19 to the one or more polymers of the porous polymer framework, and wherein the one or more polymers is polyvinyl alcohol.

8. The solar absorber incorporated bilayer foam solar evaporator of claim 3, wherein the amount of boron carbide is from more than 0 to 50 wt % to one or more polymers of the porous polymer framework.

9. The solar absorber incorporated bilayer foam solar evaporator of claim 1, wherein the solar evaporator has an evaporation rate of about 2.8 kg/m.sup.2/h of seawater or wastewater under 1 kW/m.sup.2 solar irradiation, an overall heavy metal removal efficiency of about 99.9%, and a bacterial removal efficiency of 99.99% under 1 1 kW/m.sup.2 solar irradiation for 1 hour.

10. The solar absorber incorporated bilayer foam solar evaporator of claim 9, wherein the heavy metal removed by the solar evaporator comprises Hg.sup.+, Cd.sup.2+, Pb.sup.2+, Fe.sup.3+, Co.sup.2+, Ni.sup.2+, Ag.sup.+, Zn.sup.2+, Na.sup.+, Mg.sup.2+, K.sup.+, and Ca.sup.2+.

11. The solar absorber incorporated bilayer foam solar evaporator of claim 1, wherein the solar evaporator has a working pH range of 1 to 14.

12. A method for preparing a scaffold of a solar absorber incorporated bilayer foam for seawater desalination and wastewater purification, the method comprising: dissolving a plurality of solar absorbers into a solvent thoroughly; mixing the plurality of solar absorbers dissolved in solvent with one or more polymers vigorously to form a gelation formation mixture; adding the gelation formation mixture into a solution of hydrochloric acid and glutaraldehyde dropwisely to have an in-situ gelation to form a hydrogel; settling the hydrogel at a low temperature; freeze-drying the hydrogel until an aerogel is obtained which is the scaffold of the solar absorber incorporated bilayer foam.

13. The method of claim 12, wherein said mixing the plurality of solar absorbers dissolved in solvent with the one or more polymers vigorously is by sonication for about 1 to 60 minutes until the gelation formation mixture is formed.

14. The method of claim 12, wherein said adding the gelation formation mixture into the solution of hydrochloric acid and glutaraldehyde dropwisely comprises mild stirring during said adding for about 0.5 to 6 hours until the hydrogel is formed.

15. The method of claim 12, wherein said settling the hydrogel is carried out by immersing the hydrogel in water for overnight at about 5 to −30 degrees Celsius.

16. The method of claim 12, wherein the plurality of solar absorbers is selected from boron carbide.

17. The method of claim 12, wherein the one or more polymers comprise polyvinyl alcohol (PVA), polydimethylsiloxane (PDMS), polyurethane (PU) and melamine.

18. The method of claim 16, wherein boron carbide dissolved into the solvent is mixed with the one or more polymers in a weight ratio of 1:2-19, and wherein the one or more polymers is selected from polyvinyl alcohol.

19. The method of claim 18, wherein boron carbide at more than 0 to about 50% w/w with respect to polyvinyl alcohol is dissolved in the solvent.

20. The method of claim 19, wherein the solvent is an organic solvent selected from ethanol, methanol, acetone, or tetrahydrofuran.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0037] Embodiments of the invention are described in more details hereinafter with reference to the drawings, in which:

[0038] FIG. 1 schematically depicts how a boron carbide bilayer foam (BCBF) based solar evaporator is prepared according to an embodiment of the present invention;

[0039] FIG. 2A shows X-ray diffraction (XRD) of B.sub.4C used in the present invention;

[0040] FIG. 2B shows Raman spectrum of B.sub.4C used in the present invention;

[0041] FIG. 2C shows absorption spectrum of B.sub.4C used in the present invention;

[0042] FIG. 2D shows digital photograph of B.sub.4C layer formed in the present invention;

[0043] FIG. 3A shows photos of a blank foam (top panel) and BCBF (bottom panel);

[0044] FIG. 3B shows SEM image of a blank foam (top panel) and BCBF (bottom panel) in lower magnification;

[0045] FIG. 3C shows SEM image of a blank foam (top panel) and BCBF (bottom panel) in higher magnification;

[0046] FIG. 3D shows wettability of the present BCBF according to an embodiment of the present invention;

[0047] FIG. 3E shows water droplet impregnation process on the surface of the present BCBF (top panel) and blank PVA foam (bottom panel);

[0048] FIG. 3F shows a thermal insulation performance

[0049] FIG. 4A shows solar absorption (dark line) and absorption spectra as a function of light wavelength by BCBF according to an embodiment of the present invention;

[0050] FIG. 4B show temperature change in the present BCBF within 10 minutes of irradiation of 1 solar light in air compared with a blank PVA foam;

[0051] FIG. 5A shows mass change in BCBF as a function of different irradiations against exposure time;

[0052] FIG. 5B shows evaporation rates and solar conversion efficiencies of different BCBFs prepared according to various embodiments of the present invention;

[0053] FIG. 5C shows change in evaporation rate of BCBF under different intensities of solar illumination for 6 cycles according to a preferred embodiment of the present invention;

[0054] FIG. 6A shows UV-Vis-NIR absorption spectra of methylene blue (MB) containing wastewater (a), and

[0055] FIG. 6B shows UV-Vis-NIR absorption spectra of rhodamine B (RhB) containing wastewater;

[0056] FIG. 6C shows change in absorbance of E. coli

[0057] FIG. 6D shows change in some heavy metals in water before and after treated with the BCBF according to an embodiment of the present invention;

[0058] FIG. 6E shows change in other heavy metals in water before and after treated with the BCBF according to an embodiment of the present invention;

[0059] FIG. 6F shows photographs of wastewater before and after treated with the BCBF according to an embodiment of the present invention.

[0060] FIG. 7A schematically depicts deacidification, dealkalization and desalination tests of the present BCBF to mimic exposure to extreme conditions;

[0061] FIG. 7B shows stability test result of the present BCBF under pH 1 and pH 14 for 24 hours;

[0062] FIG. 7C shows dealkalization and desalination performances of the present BCBF evaporator.

DETAILED DESCRIPTION OF THE INVENTION

[0063] In the following description, systems, devices, methods of, and the likes are set forth as preferred examples. It will be apparent to those skilled in the art that modifications, including additions and/or substitutions may be made without departing from the scope and spirit of the invention. Specific details may be omitted so as not to obscure the invention; however, the disclosure is written to enable one skilled in the art to practice the teachings herein without undue experimentation.

[0064] It should be apparent to practitioner skilled in the art that the foregoing and subsequent examples of the system and method are only for the purposes of illustration of working principle of the present invention. It is not intended to be exhaustive or to limit the invention to the precise forms disclosed.

[0065] In the preferred embodiment, B.sub.4C powders are selected as solar absorber because they not only have good optical absorption over the solar spectrum, but also have very good stability in different extreme environments (e.g. high temperature, strong acid, base, oxidation resistance, etc). These materials are very suitable for being applied in seawater desalination and wastewater purification system which are usually exposed to a very extreme environment.

[0066] These merits also suggest that the resulting solar absorber shall also have good stability and solar-thermal conversion performance. After embedding into a polymer framework such as polyvinyl alcohol (PVA) foam (Scheme 1), the boron carbide bilayer foam (BCBF) achieved a high evaporation rate of 2.8 kg/m.sup.2/h with a solar evaporation efficiency of 93% under 1 sun illumination. Combining this good solar steam generation performance with the very low cost, the BCBF delivers a record high cost-effectiveness of 778 g/h/$. It is also demonstrated that the present can be achieved low-cost high rate freshwater production from water contaminated with various kinds of common contaminants including heavy metals, dyes, and microorganisms. The composite foam can also work in extreme conditions, including concentrated acid, strong alkali, and high salinity.

[0067] Turning to FIG. 1, boron carbide (B.sub.4C) powders are added into an organic solvent system, followed by mixing with polyvinyl alcohol (PVA) (101) to form a gelation formation mixture, then the gelation formation mixture is added dropwisely into a solution of diluted HCl and glutaraldehyde (102) to form an in-situ gelation. In one embodiment, weight ratio between B.sub.4C powders and PVA is 1:2. In other embodiments, amount of B.sub.4C powders added can vary to obtain different mass loads of B.sub.4C in the boron carbide bilayer foam (BCBF). The B.sub.4C powders after dissolved into the organic solvent is mixed with the PVA by sonication for 1 to 60 mins to obtain the gelation formation mixture. The gelation formation mixture is added dropwisely into the solution of HCl and glutaraldehyde under mild stirring for about 0.5 to 6 hours to have an in-situ gelation. During the in-situ gelation, cross-linking occurs among polymers to form a polymer framework incorporating boron carbide. A hydrogel is obtained after the in-situ gelation, and is then settled in water at a low temperature for overnight (103). B.sub.4C tends to sediment to the bottom of the reaction system to form a bilayer structure. Preferably, the hydrogel is settled by immersing in water and then storing at 5 to −30 degrees Celsius for overnight. After freeze-drying the hydrogel (104), an aerogel is obtained (105), which is a scaffold of boron carbide bilayer foam in a porous polymer framework.

[0068] Turning to FIG. 2A, it shows the chemical structure of the B.sub.4C used in the present invention, where the XRD pattern at two theta confirms the rhombohedral crystal form thereof (there are some minor peaks representing boron oxide and carbon, but the intensity is relatively smaller). The Raman spectrum of B.sub.4C in FIG. 2B shows peaks at 270, 318, 480, 536, 715, 799, 826, 1,001 and 1,088 cm.sup.1 which correspond to the vibrations of the principal structural elements: icosahedra and three-atom linear chains in the crystalline B.sub.4C (FIG. 2B). UV-Vis-NIR absorption spectrum of B.sub.4C is also shown in FIG. 2C. The B.sub.4C layer exhibits full-solar absorption and a distinguishable black color (FIG. 2D). The B.sub.4C as solar absorber of the present invention has solar absorption efficiency of about 99.4%, which is better than many known solar absorbers.

[0069] Turning to FIGS. 3A-3C, the appearance of a blank (top panel) and the present BCBF (bottom panel) and their micro-structure under scanning electronic microscopy in lower and higher magnifications are shown. As it can be seen, a darker aerogel foam is obtained from BCBF, especially at the top layer of the bilayer structure containing B.sub.4C when the aerogel foam is turned upside down out of the reaction container, as compared to the blank polymer (PVA) foam (FIG. 3A); a cross-section of the blank PVA foam (without B.sub.4C) shows abundant capillary channels with some sub-10 μm micropores in the internal wall structure thereof (FIG. 3B) for facilitating water transportation by capillary force; from a higher magnification SEM image, the cross-section of the present BCBF, PVA foam is shown to be loaded with B.sub.4C particles with an average size from approximately 10 to 70 μm (FIG. 3C). Loading of B.sub.4C particles in the BCBF does not significantly affect the pore size of the PVA foam.

[0070] Turning to FIG. 3D, the present BCBF (about 2 cm diameter) is turned into blue color within 18 sec when it is placed on the bottom of a Petri dish filled with blue ink aqueous solution.

[0071] To further demonstrate the wettability of the present BCBF, a series of digital photos showing process of water droplet impregnation on the surface of the present BCBF confirms that loading of the B.sub.4C particles facilitates water transportation in the PVA framework (˜0.2 sec) as compared to that on the PVA blank foam (˜0.4 sec) (FIG. 3E). The present BCBF is shown to have a water contact angle of 44°, compared to 77° in the blank PVA foam.

[0072] To demonstrate solar steam generation performance, the present BCBF is put onto a heating plate with a surface temperature of 170° C. and the temperature profile in the present BCBF is continuously monitored by an infrared camera (FIG. 3F). It can be seen from the thermal profile that the top surface, which is about 1 cm from the bottom of the BCBF, is only about 36° C., confirming that the present BCBF is a good thermal insulator, in addition to its water transportation efficiency and hydrophilicity.

[0073] As compared with a graphene-based aerogel, the present BCBF is more hydrophilic mainly due to more abundant porous structures in the present BCBF which would offer a more efficient water transportation within the foam network. The present BCBF also has lower mass density and higher flexibility, which facilitates floating at water-air interface and transportation of water from water side to the air side of the BCBF for evaporation.

[0074] Turning to FIG. 4A, the present BCBF is shown to have good light absorption capacity over the whole solar spectrum. Optical reflectance measurements also confirmed that the present BCBF has substantially negligible reflectance from 400 to 2000 nm (not shown in FIG. 4A), whereas blank PVA foam exhibits strong reflection.

[0075] Turning to FIG. 4B, solar-thermal conversion capability of the present BCBF is further characterized by measuring the temperature change using an irradiation source (e.g., a Xenon lamp) under 1 kW/m.sup.2 in air which is considered to be equivalent to 1 solar light in air. Upon continuous illumination, the present BCBF has a rapid temperature increase within a 10 min-irradiation with a maximum temperature of 77° C. The present BCBF is measured to have effectively held equilibrium temperature, whereas the temperature of the blank PVA foam substantially remains unchanged under the same illumination conditions.

[0076] Turning to FIG. 5A, the present BCBF is shown to have an evaporation rate of 2.8, 4.8 and 7.1 kg/m.sup.2/h under 1, 3, and 5 kW/m.sup.3 irradiation, respectively. The present BCBF is further compared with a boron carbide monolayer foam (BCMF) under 1 kW/m.sup.3 irradiation. The evaporation rate of the present BCBF (2.8 kg/m.sup.2/h) is higher than that of the BCMF (1.63 kg/m.sup.2/h), suggesting that bilayer structure of boron carbide based composite foam has a better solar water evaporation rate under 1 solar light in air than that of the monolayer structure.

[0077] Turning to FIG. 5B, the evaporation rate of BCBF is increased as the mass loadings of PVA increases, where the weight ratio of B.sub.4C: PVA in BCBF1, BCBF2, and BCBF3 are 1:2, 1:9 and 1:19, respectively.

[0078] Turning to FIG. 5C, the present BCBF is subjected to different irradiation intensity (1, 3, and 5 kW/m.sup.2) in air for 6 cycles, where each cycle last for 1 hour. From the result, it shows that the evaporation rate remains substantially steady over 6 cycles of irradiation at different intensities up to 5 solar light in air (5 sun).

[0079] Turning to FIG. 6A, a characteristic peak of methylene blue (MB) at 660 nm is observed in the present BCBF after the present BCBF is subjected to solar evaporation under 1 kW/m.sup.2, and clean (colorless and transparent) water is collected after purification. Similarly, a characteristic peak of rhodamine B (RhB) at about 550 nm is observed in the present BCBF after it is subjected to the solar evaporation (FIG. 6B).

[0080] Turning to FIG. 6C, bacteria (E. coli) in a microbial contaminated water are substantially removed by the present BCBF after being subjected to the solar evaporation, evident by disappearance on both torridness pattern and optical absorption at 600 nm.

[0081] Turning to FIGS. 6D and 6E, different heavy metals (Hg.sup.+, Cd.sup.2+, Pb.sup.2+, Fe.sup.3+, Co.sup.2+, Ni.sup.2+, Ag.sup.+, Zn.sup.2+, Na.sup.+, Mg.sup.2+, K.sup.+, Ca.sup.2+) are shown to be purified by the present BCBF over 99.9%. FIG. 6F shows before and after solar purification by the present BCBF, the contaminated water by the heavy metals is clear.

[0082] To be qualified as an ideal solar evaporator, it should withstand extreme conditions such as concentrated acid, strong alkali, high salinity, etc. To demonstrate that the present BCBF is qualified to be an ideal solar evaporator under extreme conditions, the present BCBF is soaked for 24 hours in pH 1 or pH 14 condition (FIG. 7A). After that, no obvious changes in the appearance and microstructure have been observed (FIG. 7B). The present BCBF is also subjected to high-salt solution, which is also not observed with any obvious changes in appearance and microstructure. FIG. 7C shows that the present BCBF absorbs strong acid and strong alkali from the solution to turn the highly acidic or highly alkaline solution into a neutral solution under 1 solar light. From these results, the present invention is shown to be an ideal solar evaporator under extreme conditions.

[0083] In summary, the present invention is not just a high cost-performance evaporator, but also easy-to-fabricate, able to withstand extreme conditions and eliminate bacteria, heavy metals, and strong acid/alkali from any seawater and wastewater.

[0084] The foregoing description of the present invention has been provided for the purposes of illustration and description. It is not intended to be exhaustive or to limit the invention to the precise forms disclosed. Many modifications and variations will be apparent to the practitioner skilled in the art.

[0085] The embodiments were chosen and described in order to best explain the principles of the invention and its practical application, thereby enabling others skilled in the art to understand the invention for various embodiments and with various modifications that are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the following claims and their equivalence.

INDUSTRIAL APPLICABILITY

[0086] The boron carbide bilayer foam (BCBF) of the present invention enables a high cost-performance seawater desalination and wastewater purification. Low-cost commercially available B.sub.4C powders are embedded into a porous polymer foam in a one-pot method to form the boron carbide bilayer foam (BCBF) with good hydrophilic wettability, heat-shielding, and solar-thermal conversion, in low cost which is as low as 3.6 $/m.sup.2. Notably, under 1 sunlight illumination, the BCBF offers a high evaporation rate of 2.8 kg/m.sup.2/h with 93% solar evaporation efficiency. The present BCBF based solar evaporator is demonstrated to possess an ultra-high cost-effectiveness of 778 g/h/$, superior to recently reported solar evaporation systems. The present invention thereby provides an excellent and cost-effective solar evaporator tool for industrial-level water purification.