The present invention generally relates to CO2-adsorbing, graphene-containing nanocomposites, methods of making the same, and methods of using the same.
There is a current focus on sequestering carbon dioxide (CO2), particularly CO2 produced during energy production (e.g., from coal-burning power plants). Before CO2 can be sequestrated, it must be separated and captured from its source. Carbon capture and storage (CCS) technologies are a promising route for mitigating CO2 emissions in the near future, because CCS could provide a mid-term solution allowing humanity to continue using fossil energy until renewable energy technologies mature. No unique solution exists currently to solve the problem of CO2 capture, and this complex challenge will almost certainly require the integration of several technology options.
The selectivity of a separation process is determined by a combination of adsorption and diffusion selectivity, which are coupled in most materials. For example, the introduction of a functional group, that specifically binds one species and improves the adsorption selectivity, will simultaneously decrease the diffusion of these molecules. This inverse relationship between the adsorption and diffusion selectivity has recently been investigated extensively in a broad range of meso- and microporous materials including zeolites, carbon nanotubes, carbon molecular sieves, and metal-organic frameworks. The need therefore exists to design materials in which one can independently tune the diffusion and adsorption selectivity at the molecular level.
Layered double hydroxides (LDHs) have received attention because of their wide range of applications (e.g., catalysts, super capacitors, pharmaceuticals, photochemistry, electrochemistry, and adsorbents). LDHs, also known as hydrotalcite-like compounds, have also been considered as promising materials for CO2 adsorption. The general formula of LDHs is:
[M2+1-xN3+x(HO−)2]x+[Ym−x/m]nH2O
Previous CO2 adsorption studies of an Mg—Al—CO3 LDH reported an adsorption capacity of 0.5 mmol/g at 300° C. and 1 bar. (See Z. Yong, et al., Energy Consery Mgmt. 2002, 43, 1865-1876; and, Z. Yong et al., Ind. Eng. Chem. Res. 2001, Vol. 40, 204-209.) Improvements in performance are still required for practical applications.
One of the recent approaches to increase CO2 adsorption capability of LDHs is to support them on oxidized multi-walled carbon nanotubes (MWNTs) or graphene oxide (GO). The reported synthesis method of the nano-composite material is based on in situ co-precipitation of LDH onto either MWNTs or GO in aqueous dispersion followed by thermal treatment at 60° F. for 12 h under magnetic stirring (300 rpm). (See S. Miyata et al., Clays Clay Miner. 1978, 26(6), 441-447; M. K. Ram Reddy et al., Ind. Eng. Chem. Res. 2006, 45, 7504-7509; and, Q. Wang et al., Applied Clay Science, 2012, 55, 18-26.)
In view of the above, it would be advantageous to discover CO2-adsorbing, graphene-containing nanocomposites, and develop methods of making and using the same.
In an aspect, the present invention provides novel, graphene-containing nanocomposites.
In another aspect, the present invention provides novel, graphene-containing layered double hydroxides.
In another aspect, the present invention provides a novel method of making graphene-containing nanocomposites.
In another aspect, the present invention provides a novel method of making graphene-containing layered double hydroxides.
In another aspect, the present invention provides use of novel, graphene-containing nanocomposites to adsorb CO2.
In another aspect, the present invention provides use of novel, graphene-containing layered double hydroxides to adsorb CO2.
These and other aspects, which will become apparent during the following detailed description, have been achieved by the inventors' discovery of graphene-containing nanocomposites.
In an aspect, the present invention provides a novel graphene containing nanocomposite, comprising:
In another aspect, there are at least two interlayer anions in the LDH.
In another aspect, the molar ratio of divalent cation to trivalent cation is 2:1.
In another aspect, the LDH, comprises:
In another aspect, the molar ratio of divalent cation to trivalent cation is 2:1.
In another aspect, the graphene is selected from: graphene nano platelets (GNP), GNP-oxide (GNP-O), graphene oxide (GO), GNP-nitrogen (GNP-N2), GNP-amine (GNP-NH2), and GNP-silicon (GNP-Si). These types of graphene are commercially available from Cheap Tubes and other graphene vendors.
In another aspect, in the nanocomposite:
In another aspect, the divalent and trivalent cations are Mg2+ and Al3+, respectively.
In another aspect, the divalent and trivalent cations are Ca2+ and Al3+, respectively.
In another aspect, the divalent and trivalent cations are Mg2+ and Fe3+, respectively.
In another aspect, the interlayer anion is selected from: CO32− and NO3−.
In another aspect, there are two interlayer anions, which are CO32− and NO3−.
In another aspect, the nanocomposite is selected from A-X:
wherein the molar ratio of divalent cation to trivalent cation is 2:1.
In another aspect, the molar ratio of divalent cation to trivalent cation is 2:1 and the weight (mg)/mmol ratio of graphene to divalent cation is about 3.5 to 214.
In another aspect, the molar ratio of divalent cation to trivalent cation is 2:1 and the weight (mg)/mmol ratio of graphene to divalent cation is selected from: (a) 3.5 to 179, (b) 7.1 to 143, (c) 8.9 to 107, and (d) 8.9 to 71.4.
In another aspect, the present invention provides a novel process of preparing a graphene containing layered double hydroxide (G-LDH), comprising:
In another aspect, the LDH, comprises: at least two interlayer anions.
In another aspect, in the process:
In another aspect, the divalent and trivalent cations are Mg2+ and Al3+, respectively.
In another aspect, the divalent and trivalent cations are Ca2+ and Al3+, respectively.
In another aspect, the divalent and trivalent cations are Mg2+ and Fe3+, respectively.
In another aspect, the interlayer anion is selected from: CO32− and NO3−.
In another aspect, there are two interlayer anions, which are CO32− and NO3−.
In another aspect, the G-LDH formed is selected from A-X:
In another aspect, the weight (mg)/mmol ratio of graphene to divalent cation is about 3.5 to 214.
In another aspect, the weight (mg)/mmol ratio of graphene to divalent cation is selected from: (a) about 3.5 to 179, (b) about 7.1 to 143, (c) about 8.9 to 107, and (d) about 8.9 to 71.4.
In another aspect, the temperature of the mixture during sonication is from 50-80° C.
In another aspect, the temperature of the mixture during sonication is 60° C.
In another aspect, the sonication parameters are chosen to maintain a temperature of the mixture during sonication of from 50-80° C.
In another aspect, the sonication parameters are chosen to maintain a temperature of the mixture during sonication of 60° C.
In another aspect, water is also adding during the mixing.
In another aspect, the resulting G-LDH is washed with water.
In another aspect, the G-LDH is washed with water until the water has a pH of 7.
In another aspect, the LDH-containing solution is formed by mixing a salt solution with an aqueous solution, wherein:
In another aspect, the present invention provides a novel graphene containing nanocomposite, comprising:
In another aspect, the weight (mg)/mmol ratio of graphene to Ti is about 0.6 to 35.5.
In another aspect, the weight (mg)/mmol ratio of graphene to Ti is selected from: (a) about 0.6 to 29.6, (b) about 1.2 to 23.7, (c) about 1.5 to 17.8, and (d) about 1.5 to 11.8.
In another aspect, the graphene is selected from: graphene nano platelets (GNP), GNP-oxide (GNP-O), graphene oxide (GO), GNP-nitrogen (GNP-N2), GNP-amine (GNP-NH2), and GNP-silicon (GNP-Si).
In another aspect, the present invention provides a novel process of preparing a graphene containing nanocomposite, comprising:
In another aspect, the weight (mg)/mmol ratio of graphene to Ti is about 0.6 to 35.5.
In another aspect, the weight (mg)/mmol ratio of graphene to Ti is selected from: (a) about 0.6 to 29.6, (b) about 1.2 to 23.7, (c) about 1.5 to 17.8, and (d) about 1.5 to 11.8.
In another aspect, the graphene is selected from: graphene nano platelets (GNP), GNP-oxide (GNP-O), graphene oxide (GO), GNP-nitrogen (GNP-N2), GNP-amine (GNP-NH2), and GNP-silicon (GNP-Si).
In another aspect, the sol-gel solution is formed by sonicating a mixture of a Ti(IV) tetra ester, an alcohol, and a base.
In another aspect, the resulting G-TiO2 is heated to at least 350° C. for about an hour.
In another aspect, the resulting G-TiO2 is heated to at least 400° C. for about an hour.
In another aspect, the resulting G-TiO2 is heated to at least 450° C. for about an hour.
In another aspect, the molar ratio of divalent cation to trivalent cation is 2:1.
In another aspect, the weight (mg)/mmol ratio of graphene to divalent cation in the G-LDH is about 3.5 to 214. Additional examples of the weight (mg)/mmol ratio of graphene to divalent cation include about (a) 3.5 to 179, (b) 7.1 to 143, (c) 8.9 to 107, (d) 8.9 to 71.4, and (e) 8.9, 17.9, 26.8, 35.7, 44.6, 53.6, 62.5, and 71.4.
In another aspect, the weight (mg)/mmol ratio of graphene to Ti in the TiO2-GNP is about 0.6 to 35.5. Additional examples of the weight (mg)/mmol ratio of graphene to divalent cation include about (a) 0.6 to 29.6, (b) 1.2 to 23.7, (c) 1.5 to 17.8, (d) 1.5 to 11.8, and (e) 1.5, 3, 4.4, 5.9, 7.4, 8.9, 10.4, and 11.8.
In another aspect, from 10-600 mg of graphene is present in the nanocomposite. Additional examples of the amount graphene present (or used in the present process) include: (a) 10-500, (b) 20-400, (c) 25-300, (d) 25-200, and (e) 25, 50, 75, 100, 125, 150, 175, and 200. Other examples include 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, 100, 105, 110, 115, 120, 125, 130, 135, 140, 145, 150, 155, 160, 165, 170, 175, 180, 185, 190, 195, 200, 205, 210, 215, 220, 225, 230, 235, 240, 245, 250, 255, 260, 265, 270, 275, 280, 285, 290, 295, 300, 305, 310, 315, 320, 325, 330, 335, 340, 345, 350, 355, 360, 365, 370, 375, 380, 385, 390, 395, 400, 405, 410, 415, 420, 425, 430, 435, 440, 445, 450, 455, 460, 465, 470, 475, 480, 485, 490, 495, 500, 505, 510, 515, 520, 525, 530, 535, 540, 545, 550, 555, 560, 565, 570, 575, 580, 585, 590, 595, and 600 mg.
The following examples are meant to illustrate, not limit, the present invention.
An Mg—Al LDH mixture was prepared by mixing an aqueous salt solution of Mg2+ and Al3+ ions (with a molar ratio of 2:1) with an alkaline solution of NaOH and Na2CO3.
Aqueous salt solution: 1.4 mL total volume:
Aqueous solution: 2.06 mL total volume:
To the LDH mixture was added distilled water (25 mL) and graphene nano platelets (GNP) (e.g., 25 mg) (purchased from Cheap Tubes, GNPs Grade 4). The resulting mixture was then sonicated. Pulse sonication was used under the following conditions
Once sonication was completed, the formed precipitates were washed with distilled water by placing the sonicated mixture in a vessel, adding distilled water, shaking, allowing the precipitates to settle, decanting off the water, and repeating until the pH of the added water was 7. After the pH reached 7, the precipitates were filtered off using a 0.4 μm polycarbonate membrane and dried in air at room temperature.
1GNP-N2 (GNPs grade 4 N2 rich), GNP-NH2 (GNPs grade 4 NH2 rich), and GNP-Si (Si decorated GNPs) were each purchased from Cheap Tubes.
The Mg—AL LDH's in Table 1A were made according to the above procedure.
The Ca-AL LDH's in Table 1B were made according to the above procedure with the exception that 2.8 mmol Ca(NO3)2.4 H2O replaced 2.8 mmol Mg(NO3)2.6 H2O in the salt solution.
The Mg-AL LDH's in Table 1C were made according to the above procedure with the exception that GNP was replaced by either GNP Oxide (made as described below) or GO (purchased as described below).
GNP Oxide:
A solution (14 mL) of concentrated H2SO4 and HNO3 (3:1 ratio) was prepared. To the solution was added GNP (400 mg). The resulting mixture was stirred at 300 rpm and heated to reflux (80° C.) for 30 min. After cooling, the resulting oxidized GNP (GNP Oxide) was washed with distilled water and 0.01M NaOH until the wash solution reached pH 7. The GNP Oxide was collected on a 0.4 μm polycarbonate membrane.
GO (Graphene Oxide):
A GO dispersion in water (5 g/L) was purchased from Graphene Supermarket. This dispersion is used in place of the GNP/distilled water in the GNP-LDH process described above to prepare GO-LDH.
Characterization:
The products can be characterized by a number of different techniques, including transmission electron microscopy (TEM) imaging, scanning electron microscopy, energy dispersive X-ray spectrometry, and Raman. Raman analysis was performed by using Raman microscopy model IDR-Micro-532 and the results are shown in
The D/G peak ratios from the Raman analysis are shown in tables 1D-1F.
Ti(O-i-Pr)4 (97%) isopropyl alcohol, HNO3, and distilled water in a volume ratio of 1:10:1:0.2, respectively (5 mL/50 mL/5 mL/1 mL)(16.9 mmol Ti)(total volume=61 mL), were mixed and sonicated (conditions below) to achieve a sol-gel solution. GNP (e.g., 100 mg) was mixed with the resulting sol-gel solution and the resulting mixture sonicated (conditions below). The resulting solution was filtered and dried in an oven at 80° C. followed by thermal treatment in air atmosphere at 450° C. for 1 h to achieve TiO2-GNP with a uniform TiO2 phase.
The Ti-GNP's in Table 2A were made according to the above procedure.
Characterization:
The titanium can be characterized as described above. Raman analysis was performed by using Raman microscopy model IDR-Micro-532 and the results are shown in
The D/G peak ratios from the Raman analysis are shown in table 2D.
Calcination was carried as follows:
4A: Adsorption Measurement:
A horizontal tube furnace was used to determine the adsorption capacity of pre-calcined samples, as follows:
4B: Regeneration and Stability:
The regeneration and stability of the absorbent powders of the present invention was assessed by multi-cycle tests in which the adsorption step was carried out at 300° C. and/or 100° C. for 1 hour by flowing the premixed CO2/N2 gas and the desorption step was performed at 400° C. for 1 h by flowing nitrogen. The flow rates of both gases were kept constant during the experiment.
Additional examples of the present invention, which can be prepared as described above, are shown in Tables 6A-6F. The molar ratio of divalent to trivalent cation is 2:1, with 2.8 mmol of divalent cation being present in each example.
Additional TiO2-GNP examples of the present invention, which can be prepared as described above, are shown below. 16.9 mmol of Ti is present in each example.
Numerous modifications and variations of the present invention are possible in light of the above teachings. It is therefore to be understood that within the scope of the appended claims, the invention may be practiced otherwise that as specifically described herein.
Number | Date | Country | |
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62308782 | Mar 2016 | US |