REDUCED GRAPHENE OXIDE BARRIER MATERIALS
20200215496 ยท 2020-07-09
Inventors
Cpc classification
B82Y40/00
PERFORMING OPERATIONS; TRANSPORTING
G01N15/082
PHYSICS
B32B37/14
PERFORMING OPERATIONS; TRANSPORTING
B82Y30/00
PERFORMING OPERATIONS; TRANSPORTING
B32B37/12
PERFORMING OPERATIONS; TRANSPORTING
Y10S977/847
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y10S977/734
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
B01D67/00
PERFORMING OPERATIONS; TRANSPORTING
B32B37/12
PERFORMING OPERATIONS; TRANSPORTING
B32B37/14
PERFORMING OPERATIONS; TRANSPORTING
Abstract
This invention relates to barrier materials comprising reduced graphene oxide, methods of making said materials and their uses. The reduced graphene oxide is preferably formed from the reduction of graphene oxide by HI, HBr or ascorbic acid.
Claims
1. A method of making a barrier material, the method comprising reducing a graphene oxide laminate membrane to form a reduced graphene oxide laminate membrane with a reducing agent, wherein the reducing agent does not generate CO.sub.2 or CO as a major component when it reduces graphene oxide.
2. The method of claim 1, wherein the reducing agent is selected from the group consisting of HI, HBr and ascorbic acid (vitamin C).
3. The method of claim 1, wherein the method further comprises: (A) supporting the graphene oxide laminate membrane on a substrate; and (B) reducing the graphene oxide laminate membrane to form the reduced graphene oxide laminate membrane supported on the substrate.
4. The method of claim 3, wherein step (A) further comprises depositing a graphene oxide suspension onto the substrate to form the graphene oxide laminate membrane supported on the substrate.
5. The method of claim 3, wherein the method further comprises, before the graphene oxide laminate membrane is supported on the substrate (step (A)), modifying the substrate to increase the strength of the association between the substrate and the graphene oxide and/or reduced graphene oxide laminate membrane.
6. The method of claim 5, wherein modifying the substrate comprises coating the surface of the substrate with an adhesion promoter.
7. The method of claim 5, wherein the substrate is a polymer substrate and the step of modifying the substrate comprises oxidising the surface of the substrate by exposing it to ozone and/or oxygen plasma to form an oxidised polymer substrate.
8. The method of claim 7, wherein the polymer substrate is poly(ethylene terephthalate) (PET).
9. The method of claim 3, wherein the substrate is a porous structure or material and the method is a method of reducing the porosity of a porous structure or material.
10. The method of claim 2, wherein the reducing agent is ascorbic acid (vitamin C).
11. The method of claim 6, wherein the adhesion promoter is a polymer.
12. The method of claim 5, wherein the adhesion promoter is selected from the group consisting of phytic acid, PMMA, poly(vinyl alcohol) (PVA), polystyrene, poly(4-styrenesulfonate), Nafion, carboxymethyl cellulose, chitosan, polyvinyl pyrrolidone and polyaniline.
13. The method of claim 5, wherein the substrate is a metal substrate and the adhesion promoter is selected from the group consisting of phytic acid, poly(methyl methacrylate) (PMMA) and polystyrene.
14. The method of claim 6, wherein the substrate is a glass or silicon-based substrate and the adhesion promoter is sodium metasilicate.
15. The method of claim 3, wherein the method further comprises: C) transferring the reduced graphene oxide laminate membrane from the first substrate to a second substrate.
16. The method of claim 1, wherein the method further comprises the step of rinsing the reduced graphene oxide laminate membrane with a rinsing agent.
17. The method of claim 1, wherein the method further comprises the step of drying the reduced graphene oxide laminate membrane after the reduction step.
18. The method of claim 1, wherein the step of reducing the graphene oxide laminate membrane takes place at a temperature from about 5 C. to about 150 C.
19. The method of claim 1, wherein the step of reducing the graphene oxide laminate membrane takes from about 0.5 minutes to about 120 hours.
20. A barrier material prepared according to the method of claim 1.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0097] Embodiments of the invention are further described hereinafter with reference to the accompanying drawings, in which:
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DETAILED DESCRIPTION OF THE INVENTION
[0105] A barrier material is a material which is substantially impermeable to gases and water vapour. The exact permeability at which a material becomes a barrier material depends on the specific application. Organic light emitting diodes and other electronic applications often require a material which is more impermeable than might be required in certain food packaging applications. As a rule of thumb, throughout this specification a barrier material is one having a water permeability below 10.sup.6 g/m.sup.2/day at 100% RH and room temperature. However, for certain less critical applications, a water permeability below 10.sup.5 g/m.sup.2 day at 100% RH and room temperature, or even a water permeability below 10.sup.4 g/m.sup.2/day at 100% RFI and room temperature, may be acceptable. These materials exhibit a relatively larger degree of transmission of gases and water vapour. In the particular applications concerned, this might be perfectly acceptable. The skilled person will be able to determine the appropriate level of impermeability for any particular application. The degree of permeability is permissible thus depends exactly the purpose that the barrier of the present invention is being used for. For example, in the case of barrier materials that might be used for nuclear applications a very low level of permeability, for example, a water permeability below 10.sup.5 g/m2/day at 100% RH and room temperature may be more appropriate whereas in food packaging applications for less sensitive foodstuffs a much lower level of impermeability. i.e., a higher permeability such as a water permeability below 10.sup.4 g/m.sub.2/day at 100% RH and room temperature
[0106] Atomic percentage is defined as the number of atoms in element in 100 atoms representative of the substance. Mathematically, the atomic percent is
atomic percent (1)=.sub.N.sub.
where N.sub.i are the number of atoms of interest and N.sub.tot are the total number of atoms. The atomic % therefore can be represented as 100 * number of atoms of one component/total number of all atoms in sample, which is the same as 100 * number of moles of one component/number of moles of all components.
[0107] Reduced graphene oxide is graphene oxide which has been reduced. It is not pristine graphene as it retains some oxygen content. It is substantially less oxygenated than graphene oxide.
[0108] The present invention involves the use of reduced graphene oxide membranes which may be formed from graphene oxide membranes. The reduced graphene oxide membranes and graphene oxide membranes are laminate membranes. They comprise stacks of individual graphene oxide flakes, in which the flakes are predominantly monolayer reduced graphene oxide or graphene oxide respectively. Although the flakes are predominantly monolayer reduced graphene oxide or graphene oxide respectively, it is within the scope of this invention that some of the reduced graphene oxide or graphene oxide is present as two- or few-layer reduced graphene oxide or graphene oxide. Thus, it may be that at least 75% by weight of the reduced. graphene oxide or graphene oxide is in the form of monolayer reduced graphene oxide or graphene oxide flakes, or it may be that at least 85% by weight of the reduced graphene oxide or graphene oxide is in the form of monolayer reduced graphene oxide or graphene oxide flakes (e.g., at least 95%, for example, at least 99% by weight of the reduced graphene oxide or graphene oxide is in the form of monolayer reduced graphene oxide or graphene oxide flakes) with the remainder made up of two- or few- layer reduced graphene oxide or graphene oxide.
[0109] The graphene oxide for use in this application can be made by any means known in the art. In a preferred method, graphite oxide can be prepared from graphite flakes e.g., natural graphite flakes) by treating them with potassium permanganate and sodium nitrate in concentrated sulphuric acid. This method is called Hummers method. Another method is the Brodie method, which involves adding potassium chlorate (KClO.sub.3) to a slurry of graphite in fuming nitric acid. For a review see Dreyer et al. The chemistry of graphene oxide, Chem. Soc. Rev., 2010, 39, 228-240.
[0110] Individual graphene oxide (GO) sheets can then be exfoliated by dissolving graphite oxide in water or other polar solvents with the help of ultrasound, and bulk residues can then be removed by centrifugation and optionally a dialysis step to remove additional salts. Thus, exfoliation of graphite oxide in water into individual graphene oxide can be achieved by the sonication technique followed by centrifugation at 10000 rpm to remove few layers and thick flakes. Graphene oxide membranes can be formed by restacking of these single layer graphene oxides by a number of different techniques such as spin coating, spray coating, rod coating and vacuum filtration.
[0111] Graphene oxide was prepared by Hummers method and that was dispersed in water by sonication to make stable dispersions of graphene oxide in water. Mainly two types of samples were used for the experiments: free standing membranes and GO or rGO coated substrates, such as 12 m PET, 25-100 m metal foils and 290 nm oxidised silicon wafers. For fabricating free standing membranes, GO dispersions were vacuum filtered to obtain free standing (X) membranes with thickness ranging from 500 nm to 5 m. GO coating on different substrates were fabricated by rod-coating technique. GO membranes and GO coatings were reduced mainly by thermal and chemical routes. Thermal reduction was carried out at 300 C. for four hours in 10% hydrogen/argon gas mixture and chemical reductions were carried out using previously reported HI acid and ascorbic acid reduction methods Pei., S., Zhao, J., Du, J., Ren, W. & Cheng, H.-M. Direct reduction of graphene oxide films into highly conductive and flexible graphene films by hydrohalic acids. Carbon 48, 4466-4474, 2010; Zhang, J. et al. Reduction of graphene oxide via L-ascorbic acid. Chem. Common. (Comb.) 46, 1112-1114, 2010; Moon, I. K., Lee, J., Ruoff, R. S. & Lee. H. Reduced graphene oxide by chemical graphitization. Nature Communications 1, 73, 2010; and Fernandez-Merino, M. J. et al, Vitamin C is an ideal substitute for hydrazine in the reduction of graphene oxide suspensions. The Journal of Physical Chemistry C 114, 6426-6432, 2010).
[0112] HI reductions were carried out by exposing GO membranes or GO coatings to HI acid vapours at 90 C. for several minutes. The reduction time were varied from 0.5-30 minutes depending on the thickness of the membranes or coatings; this is to achieve the complete reduction of GO. After the reduction, the samples were rinsed with ethanol for several times to remove the residual HI acid and finally the samples were dried in air. For ascorbic acid reduction, the GO membranes or GO coatings were immersed into the ascorbic acid solution with a concentration of 30 mg/mL for 1 hour at 90 C. The samples were further rinsed with water and finally dried in air. Permeation properties of GO and rGO samples were measured. In brief, for vapour permeation, free standing membranes and rGO coated. PET were glued to a Cu foil with an opening of 1 cm in diameter and placed between two O-rings of a specially designed metal container. Vapour permeability was measured by monitoring the weight loss of the container filled with solvents or water with time by using a computer-controlled precision balance (Denver Instruments). For gas permeation measurements, standard vacuum components incorporated with the vacuum flanges to allow pumping, pressure gauges and controlled supply of gases were used. rGO coated PET were placed between two rubber gaskets and pressurised. (up to 1 Bar) from one side and monitored the gas leak on the other side by using mass spectrometry. Helium-leak detector INFICON UL200 was used which allowed detection of helium and hydrogen.
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[0114] To evaluate the permeation properties of ultra-thin chemically reduced GO coatings and to assess its application for barrier coating, the gas and vapour permeation properties of thin layers of rGO on PET was further investigated.
[0115] Superior water and gas barrier behaviours of rGO membranes and coatings lead to further investigation of the salt permeation properties, which could be used in the anti-corrosion and chemical resistant coating or lining applications. The salt permeation properties of rGO membranes were measured as follows. Briefly, 1 M salt solution (NaCl) and water were filled in a U-shaped two-compartment container separated with a rGO membrane. Salt diffusion through the membranes was monitored by measuring the salt permeated to the pure water side by ion chromatography and gravimetric technique.
[0116] Without wishing to be bound by theory, the observed barrier properties of high-quality reduced GO can be explained using the known mechanisms of reduction process and the structure of reduced GO. Molecular and ionic permeation in GO membranes mainly occurs through the interlayer capillary between GO sheets and the capillary width for pristine graphene oxide varies from 0.7 nm to 1.3 nm depending on the humidity or water content. After the chemical or thermal reduction this interlayer capillary collapses and the inter-layer distance reduces to 0.36001 nm (see
[0117] In conclusion, high quality HI acid reduced GO membranes show perfect barrier properties towards different gases, salts and water vapours. These properties of high quality rGO can be useful in different practical applications such as O.sub.2 and moisture barrier coating for electronics, food and pharmaceutical packaging and chemical and corrosion protection applications. The scalability and solution processability of this technique is highly advantages for various applications. Even though HI acid-reduced GO shows the perfect barrier property, it might not be suitable for all applications. However, the ascorbic acid-reduced GO also shows nearly the same barrier properties as that of HI acid-reduced GO and may be suitable for applications in which the HI-reduced GO would not be suitable.
EXAMPLE 1
Optical and AFM Characterisation of HI-rGO on PET
[0118] To characterize rGO films on PET scanning electron microscopy (SEM), atomic force microscopy (AFM) and optical absorption spectroscopy were used.
EXAMPLE 2
rGO Coating on Rough and Porous Surfaces
[0119] To understand the effect of surface roughness and porosity on the barrier properties of our rGO films, GO was deposited onto various surfaces. Those included polymer materials, such as porous polycarbonate, polyvinylidene fluoride, polysulthne, etc., and extremely rough substrates, such as brick and concrete surfaces. GO laminates on all these substrates were reduced by treating them with an ascorbic acid solution at 80 C. for 2 hours or 50 C. for 24 hours. It was found that, although the barrier quality can be sensitive to roughness and porosity, GO laminates provide a high permeation barrier for all tested surfaces. As an example,
EXAMPLE 3
Polyvinyl Alcohol Modified GO for Improved Adhesion
[0120] Adhesion between treated surfaces and rGO is critical for the perspective use of such films as chemical and anticorrosion coatings. Adhesion of rGO to plastic and glass surfaces has been found strong. Qualitatively, the graphitic films were as robust as the standard barrier films (40 nm Al on PET) but the wear properties require further studies and quantification. In contrast, adhesion of rGO to metal surfaces was weak, which resulted in easy scratching and partial peeling of the protective coating. To overcome the drawbacks of weak adhesion to metal surfaces, GO laminates were provided with interlayer cross-linking with PVA. For the purpose of this report, permeation properties of PVA-GO composite films were tested, both before and after their chemical reduction.
[0121] PVA-GO samples were prepared by blending water solutions of GO and PVA by using a magnetic stirrer. The concentrations were chosen such that 60-80 weight percentage of GO was achieved in the final laminates, after water evaporated. All the tested PVA-GO films exhibited similar properties, irrespective of their PVA fraction. Vacuum filtration, drop casting and rod coating techniques were used to produce free standing PVA-GO membranes and PVA-GO coated substrates.
[0122] Salt permeation properties of such cross-linked GO membranes was also studied and it was found that permeation rates are beyond the detection limit, too. Not only HI- but also ascorbic acid- reduced PVA-GO were tested and no major differences were observed. The inset of
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[0124] Membranes were also prepared using polyvinylpyrrolidinone and imidazole as cross linkers, respectively. The methods carried out were substantially the same as for the PVA crosslinked membranes. In the case of imidazole, GO was stirred with imidazole at 80 C. to get better cross-linking.
EXAMPLE 4
The Effect of Reduction Conditions on Ascorbic Acid Reduced GO
[0125] To study barrier properties of ascorbic acid reduced GO with different reduction conditions, water permeation experiments with GO reduced with ascorbic acid at different temperatures and also for different reduction time were performed. The results are shown in
EXAMPLE 5
Methods of Increasing the Adhesion between GO and/or rGO Laminate Membranes and Various Substrates
[0126] Activating PET substratePET substrates were cleaned by sonication in ethanol and isopropanol followed by drying with dry nitrogen gas blow. After the cleaning process, the PET substrates were placed under the UV light/ozone for 0.5-2 hours for surface activation. Alternatively, PET substrates can be treated by oxygen plasma for 5-30 minutes with a power of 30-300 W instead of UV/ozone exposure. During this process, the surfaces of the PET get activated with oxygen containing functional groups, which is beneficial for improving the adhesion (due to the improved bonding between GO and PET) and uniformity of the GO/rGO coating on the PET.
[0127] Metal surface pre-coatingPre-coating metal substrates with polymers or molecules is an option to improve the adhesion of GO to metal surfaces. For example, one could spin-coat 20-100 nm-thick PMMA on metal surface to improve the adhesion of GO/rGO to the metal.
[0128] Use of phytic acid as a pre-coating molecule was also tested: metal substrates (steel) were dipped inside phytic acid for 10-60 minutes and then a GO coating applied on top of it. It is believed that phytic acid forms complexes with the atoms on the surface of the metal and Pi-Pi interaction with GO plane, which could improve the adhesion of GO to the metal substrates.
[0129] Glass or other silicon-based substratesSodium metasilicate-GO composite (cross-linked) exhibited good adhesion to glass substrates. Thus, a laminate membrane comprising 60 wt % GO with the remainder sodium metasilicate shows better adhesion to glass substrates than a pure GO laminate.
EXAMPLE 6
Effect of Mechanical Deformation and Wear on Barrier Properties
[0130] Mechanical robustness of barrier films is important for their practical applications. For qualitative assessment of mechanical stability of the rGO films, He tests were performed for HI-rGO on PET before and after multiple (>10) folding to a radius of less than 1 mm in different directions. An example of the results is shown and compared with those for the industry-standard films (Al on PET), which experienced the same deformations, The AL film exhibited a 2-3-fold increase in He permeation rates whereas HI-rGO of a similar thickness showed no discernible change. Only films with HI-rGO thickness of200 nm exhibited increased He leaks. In this case, the resulting permeation rate was >100 times above the detection limit but still remained significantly lower than the gas permeation through the standard aluminized PET, even before its deformation.
[0131] The increased gas permeation after multiple folding for the thicker rGO films can be attributed to their weaker adhesion to PET compared to that of thin coatings. To support this idea, simple scratch tests were performed on both thin and thick rGO on PET and it was found that thin (<50 nm) rGO coatings on PET were stable with respect to scratching by a PTFE or wooden sticks, whereas thicker films exhibited scratching marks. It is possible that, similar to the standard Al films used as gas barriers, the scratchability, adhesion and mechanical robustness could be significantly improved by encapsulating rGO with another thin PET or polymer film.
[0132] For further evaluation of the effect of mechanical strain on permeation properties of the barrier films, an isotropic strain was applied by introducing a differential pressure across PET membranes. The maximum pressure that could be applied to the PET films before rupturing them was approximately 4 bar and, therefore, the pressure applied to the barrier films was limited to 2 bar. Membranes were kept under this pressure for 30 minutes and permeation experiments were performed after releasing it. The effect of the strain on bare PET and PET coated with Al and HI-rGO is shown. Bare PET exhibits high He permeation but it changes little before and after applying the strain. The industry-standard aluminized PET became ten times more transparent to He after straining, nearly as transparent as bare PET. This shows that the strain test effectively destroyed the Al film as a gas barrier. Although a tenfold increase in He permeation for strained HI-rGO on PET was observed, the permeability remained much lower than for aluminized PET sheets before their straining.
[0133] Throughout the description and claims of this specification, the words comprise and contain and variations of them mean including but not limited to, and they are not intended to (and do not) exclude other moieties, additives, components, integers or steps. Throughout the description and claims of this specification, the singular encompasses the plural unless the context otherwise requires. In particular, where the indefinite article is used, the specification is to be understood as contemplating plurality as well as singularity, unless the context requires otherwise.
[0134] Features, integers, characteristics, compounds, chemical moieties or groups described in conjunction with a particular aspect, embodiment or example of the invention are to be understood to be applicable to any other aspect, embodiment or example described herein unless incompatible therewith. All of the features disclosed in this specification (including any accompanying claims, abstract and drawings), and/or all of the steps of any method or process so disclosed, may be combined in any combination, except combinations where at least some of such features and/or steps are mutually exclusive. The invention is not restricted to the details of any foregoing embodiments. The invention extends to any novel one, or any novel combination, of the features disclosed in this specification (including any accompanying claims, abstract and drawings), or to any novel one, or any novel combination, of the steps of any method or process so disclosed.
[0135] The reader's attention is directed to all papers and documents which are filed concurrently with or previous to this specification in connection with this application and which are open to public inspection with this specification, and the contents of all such papers and documents are incorporated herein by reference.