Patent Application
20220356102
The present invention pertains to the field of water filtration and in particular to filter systems for remediation of contaminated water sources to provide water suitable for human consumption.
The increasing demand for clean drinking water, rising scarcity of water resources, and rapid industrialization represent real-world factors that necessitate the need for scalable water treatment solutions.
Conventional filtering materials (e.g., activated carbon, zeolites, flocculants, etc.) have limitations such as pH sensitivity, poor efficiency and recoverability that limit their usefulness with respect to the treatment of the wide variety of contaminants that may be found in wastewater and contaminated water sources.
Although there are several products available on the market that target point-of-use generation of drinking water from contaminated water sources, these are typically designed for personal use or for small volumes of water. These types of filters typically focus on using simple ultrafiltration without a carbon-based filter for adsorption of chemical contaminants.
There are also larger systems available for remediation of contaminated water sources, such as the Liquinex Compact Water Purification Systems, AMPAC systems, and Icon LifeSaver systems, however, none of these prior art systems are able to efficiently remove dissolved chemical contaminants, which are often present in groundwater or natural flowing water sources, while also being adaptable to a region's specific microbiological concerns.
Therefore there is a need for a lightweight, portable, modular device adaptable to the needs of the user that can be used to generate clean drinking water from any salt-free water source, regardless of the potential range of pathogens and dissolved chemicals that may exist in the water before filtration.
This background information is provided to reveal information believed by the applicant to be of possible relevance to the present invention. No admission is necessarily intended, nor should be construed, that any of the preceding information constitutes prior art against the present invention.
An object of the present invention is to provide a graphene based filters and systems comprising same. In accordance with an aspect of the present invention, there is provided a multi-stage filter system for remediation of water from a contaminated water source to provide a purified water product, the system comprising: a first filter stage configured to remove coarse solid contaminants, the first filter stage comprising an intake port for placement into the contaminated water source, at least one strainer element, and a pump configured to draw water from the contaminated water source into the intake port and through the at least one strainer element to provide a first filtrate; a second filter stage configured to remove contaminants larger than about 20 nm to about 40 nm to provide a second filtrate, the second filter stage comprising a filter element having a maximum average pore opening diameter of about 20 nm to about 40 nm; a third filter stage configured to remove dissolved chemical contaminants from the second filtrate to provide a third filtrate, the third filter stage comprising at least one graphene-based filter containing at least one graphene-based material; a fourth filter stage configured to remove residual nanoparticle contaminants from the third filtrate to provide the purified water product; and an outflow structure configured to convey the purified water product from the fourth filter stage for output from the system.
In accordance with another aspect of the present invention, there is provided a graphene-based filter cartridge comprising a filtering material in a filter cartridge housing, wherein the filtering material comprises at least one graphene-based material.
The term “graphene-based material” is used to describe a material including graphene, graphene oxide and graphene derivatives. Examples of graphene-based materials suitable for use in the present invention include single layer graphene, few-layer graphene, graphene nano-platelets, fully oxidized single layer graphene oxide, partially oxidized few-layer graphene oxide, surface modified cationic graphene oxide, nitrogen doped graphene oxide, porous graphene oxide and other functionalized graphenes.
The term “graphene-based filter” is used to describe a filter containing at least one graphene-based material.
As used herein, the term “about” refers to a +/−10% variation from the nominal value. It is to be understood that such a variation is always included in a given value provided herein, whether or not it is specifically referred to.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs.
The present invention provides a multi-stage filter/water purification system for remediation of water from a contaminated water source to provide a purified water product, wherein each stage is configured to remove a particular size or type of contaminant from the water passing through.
The system of the present invention is particularly useful for remediating water obtained from contaminated water sources including, but not limited to, contaminated groundwater, industrial wastewater, mine tailings, natural flowing fresh water, lake water, pond water, rain water runoff, any source of fresh water with unknown potential dissolved or dispersed contaminants, and municipal drinking water sources containing contaminants derived from underground piping systems or chlorinated hydrocarbons such as trihalomethane.
In a preferred embodiment, the system comprises at least four filter stages, wherein each stage is configured to remove a specific type or size of contaminant.
Due to the modular nature of the present system, the filters of the different stages can be independently removed, regenerated and replaced as required to ensure optimum performance of the filter system.
The modular nature also allows for the customization of filter combinations according to the remediation requirements of the contaminated water source.
The first filter stage is preferably configured to remove coarse solid contaminants larger than about 0.1 mm. In one embodiment, the first filter stage comprises one or more strainer elements, each strainer in sequence provided to remove successively smaller particles. In one embodiment, the first filter stage comprises a strainer element having an average opening diameter of from about 0.1 mm to about 1 mm. The first filter stage also comprises an intake port for placement into the contaminated water source, and a pump configured to draw water from the contaminated water source into the intake port and through the strainer element to provide a first filtrate which has had the coarse solid contaminants removed.
The second filter stage is preferably configured to remove contaminants larger than about 40 nm to provide a second filtrate. In one embodiment, the second filter stage comprises a filter element having an average pore opening diameter of from about 10 nm to 40 nm. In another embodiment, the second filter stage is configured to remove contaminants larger than 20 nm, and comprises a filter element having an average pore opening diameter of from about 10 nm to 20 nm. The second filter stage is provided to mechanically remove microorganisms such as bacteria, fungi, parasites, cysts, viruses, as well as colloidal microparticles.
The third filter stage is preferably configured to remove dissolved chemical contaminants from the second filtrate to provide a third filtrate. In one embodiment, the third filter stage comprises at least one graphene-based filter material. In one embodiment, the graphene-based filter material comprises graphene and/or graphene oxide. In a preferred embodiment, the graphene is few layer graphene, and the graphene oxide is few layer graphene oxide. In one embodiment, the third filter stage comprises two or more filter cartridges, wherein the cartridges may be different or the same.
The fourth filter stage is preferably configured to remove any nanoparticle contaminants from the third filtrate to provide the final purified water product. In one embodiment, the fourth filter stage comprises a filter membrane having an average pore opening diameter of from about 8 nm to about 20 nm. The fourth filter stage is provided to mechanically remove any particles that are too small to be captured by the previous filter stages, including for example, small viruses or greater than 20 nanometer-scale sized particles.
The purification system also comprises an outflow structure configured to convey the purified water product from the fourth filter stage for output from the system and use. In a preferred embodiment, the outflow structure is a hose.
In one embodiment, all components of the system are provided in a single portable housing to facilitate transportation of the filter system to a suitable location near the contaminated water source. The compact size of the system within its housing makes it particularly suitable for use in remote or difficult to access locations. In one embodiment, the filter system is provided as a compact filtration suitcase.
In one embodiment, the system further comprises a power source. In one embodiment, the power source is located within the system housing. In one embodiment, the power source is located external to the system housing. In one embodiment, the power source can be packaged into a separate box that connects to the filtration system. In one embodiment, the power source is provided as one or more rechargeable or single use batteries. Where rechargeable batteries are used, the batteries can be recharged via a built-in renewable power source such as a solar panel, or via connection to a power grid, generator, portable wind turbine, or manually-driven power mechanism.
In one embodiment, the power source is an external solar panel. In one embodiment, the power source is provided by a plug-in connection to an external power source such as a generator or a power grid.
In accordance with the present invention, each of the first filter stage, the second filter stage, the third filter stage and the fourth filter stage are independently replaceable.
In accordance with one embodiment, the filter system employs an operating system configured to monitor one or more of power consumption, flow rate, and location using a GPS based locator. In one embodiment, the operating system is configured to trigger an automatic backwash cleaning process of the second and/or fourth filter stages based on system usage levels.
In one embodiment, the filter system is configured to process contaminated water at a rate of 100-1000 litres per hour, or 2400-24000 litres per day (LPD) at 24-hour operation.
An exemplary embodiment of a filter system of the present invention is schematically depicted in
The individual filter stages are described in more detail as follows.
The first filter stage is employed to remove coarse solid contaminants larger than about 0.1 mm. In one embodiment, the first filter stage employs one or more strainer elements associated with an intake port that is placed into the contaminated water source. In one embodiment, the strainer element has an average opening diameter of from about 0.1 mm to about 1 mm. The first filter stage also comprises a pump configured to draw from the contaminated water source into the intake port and through the strainer element to provide a first filtrate which has had the coarse solid contaminants removed. The first filter stage is provided to decrease the filtration burden on downstream filter stages, thus increasing their filtration lifetime.
In one embodiment that may be particularly suitable for use with contaminated water sources containing a large amount of bulk solids, the one or more strainer elements include a perforated mesh at the intake end of the intake port having an average opening size of about 0.2 cm to about 1 cm to prevent the larger solid materials from entering the downstream filter stages.
In one embodiment that may be particularly suitable for use with contaminated water sources such as rivers or lakes, the system further comprises a flotation device attached to the intake port to prevent it from sinking below the surface of the water source to avoid contact with the muddy, sandy, or silty bottom of the water source to prevent a large influx of particulate materials that would rapidly overwhelm the subsequent stages of the filtration system.
The strainer or mesh elements may be manufactured from any suitable material, such as metal alloys (including but not limited to stainless steel and brass), metals (including but not limited to aluminum), and polymeric materials (including but not limited to PVC, PTFE, Nylon, or the like).
The second filter stage is employed to remove contaminants larger than about 40 nm, but may also preferably be configured to remove particulate contaminants as small as about 20 nm, which includes microorganisms such as bacteria, fungi, parasites and some larger viruses, as well as colloidal particles. In one embodiment, the second filter stage comprises a filter element having an average pore opening diameter of about 10 nm to about 40 nm. In one embodiment, the second filter stage comprises a filter element having an average pore opening diameter of about 10 nm to about 20 nm.
In one embodiment, the second filter stage comprises a hollow-fiber filtration membrane. In one embodiment, the second filter stage comprises a ceramic filter membrane. In one embodiment of a ceramic filter, the ceramic is a silicon carbide.
In one embodiment, the second filter stage further comprises a booster pump to pull the first filtrate through the ceramic filter.
In one embodiment, once the second stage filter has reached its filtration capacity, it can be regenerated using a reverse flow (or backwash) process by forcing clean water through the filter in the opposite flow direction to remove the filtered contaminants from the filter membrane. In one embodiment, once the second stage filter has reached its filtration capacity, it can be regenerated using a crossflow filtration process by forcing water across the filter to dislodge the filtered contaminants from the filter membrane. In one embodiment, the regeneration mechanism will be triggered automatically once built-in sensors have detected that the filter has reached filtration capacity. In one embodiment, the direction of flow is controlled by solenoid valves.
The third filter stage is employed to remove dissolved chemical contaminants from the second filtrate. In one embodiment, the third filter stage comprises at least one graphene-based filter cartridge containing at least one graphene-based material, for example, graphene and/or graphene oxide, which are particularly suitable for adsorbing and/or absorbing dissolved chemicals, including but not limited to organic compounds such as phenolic compounds, organic dyes, oil contaminants, volatile organic compounds, petrochemical compounds, and pharmaceutical drug molecules that can lead to undesirable colour and/or odour, as well as inorganic compounds such as ammonia, nitrite and dissolved metals including heavy metals.
In one embodiment, the graphene-based filter cartridge contains graphene. In one embodiment, the graphene is few layer graphene. In a further preferred embodiment, the few layer graphene is made using the process described in WO2013/089642, incorporated herein by reference, which provides a few layer graphene material having fewer defects (oxygen groups, or other impurities embedded in the carbon lattice) than other common sources of graphene, bilayer graphene, trilayer graphene, and few layer graphene (as described above) while also retaining the relatively large surface area of the flakes of from about 1 to about 1000 microns in lateral size.
In one embodiment, the few layer graphene is formed using a process comprising immersing at least a portion of graphite ore into a slurry comprising metal salt and organic solvent. The rock is electrochemically charged by incorporating the rock into at least one electrode and performing electrolysis through the slurry using the electrode and thereby introducing the organic solvent and ions from the metal salt from the slurry into the interlayer spacing of the graphite rock to form 1st-stage charged graphite mineral that exfoliates from the graphite rock. The process further includes expanding the 1st-stage charged graphite by applying an expanding force to increase the interlayer spacing between the atomic layers. As a result, few layered graphene sheets are obtained by a one step process from graphite ore.
In a preferred embodiment, the graphene material is Mesograf™, which is a graphene comprising bilayer, trilayer, and few layer (up to 5 graphene layers) graphene nanoparticles having a flake size of 1-1000 microns, distributed within an overall powder-like state.
In one embodiment, the graphene-based filter cartridge contains graphene oxide. In one embodiment, the graphene oxide is few layer graphene oxide. In a preferred embodiment, the graphene oxide is formed by oxidizing few layer graphene made using the process described in WO2013/089642, incorporated herein by reference.
In one embodiment, the few layer graphene is mixed with sulfuric acid and then combined with a preformed mixture of Mn2O7 and rapidly heated to 50° C. The resulting oxidized material is few layer graphene oxide.
In one embodiment, the few layer graphene oxide is then refluxed in 5 M NaOH, filtered and washed with deionized water until pH is 8, and thereafter refluxed again in H2SO4. This creates a nanoporous graphene oxide which is then filtered, washed with deionized water until pH is 5-6 and then vacuum dried.
In one embodiment, the graphene-based material is provided within the cartridge housing as a loose powder, as a granular material or in pelletized form. In one embodiment, the graphene-based material is incorporated into or associated with a polymeric matrix or membrane. In one embodiment, a combination of two or more different types of graphene-based materials is provided with a single cartridge.
In one embodiment, the graphene-based filter cartridge may also contain additional non-graphene components, including activated carbon (powdered or granular), inert fillers, or polymeric materials to ensure adequate flowthrough rates.
In accordance with the present invention, the third filter stage of the filter system may include any combination of graphene-based filter cartridge types to provide the appropriate performance for removal of chemical contaminants known to be present in the contaminated water source.
The following is a description of exemplary graphene-based filter cartridges suitable for use in the filter system in accordance with embodiments of the present invention. These examples are not intended to limit the scope of the present invention.
In one embodiment, the third filter stage comprises at least one graphene-based filter comprising a combination of graphene powder and pellets of a composite material comprising a mixture of polyether sulfone, graphene oxide, and dimethylformamide contained within the cartridge shell. This cartridge is referred to as a Type A cartridge. In one embodiment, the graphene is few layer graphene. In a further preferred embodiment, the few layer graphene is Mesograf™.
In one embodiment, the pellets are about 0.1 cm to about 1.0 cm in diameter. In one embodiment, the pellets comprise 50-80% by weight of the cartridge contents, and Mesograf comprises the remainder.
A Type A cartridge is particularly suitable for removing phenolic compounds, organic dyes, and other organic compounds. In a preferred embodiment, a Type A cartridge is capable of achieving at least 99% efficiency in removal of organic dyes and 99% efficiency in removal of phenolic compounds from the source water. A Type A cartridge may also be used to reduce the chemical oxygen demand (COD) of the source water. COD provides a measure of the amount of organics in water, by measuring the amount of oxidizable pollutants found in a contaminated water source. Thus, COD can be correlated to the amount of oxidizable pollutants in the water. COD is reduced by directly removing the chemicals contributing to the COD via adsorption and absorption of these chemical contaminants by the graphene-based filter materials.
In one embodiment, the third filter stage comprises at least one graphene-based filter comprising graphene powder contained within the cartridge shell. This cartridge is referred to as a Type B cartridge. In one embodiment, the graphene is few layer graphene. In a further preferred embodiment, the few layer graphene is Mesograf™.
A Type B cartridge is particularly suitable for removing oil contaminants, phenolic compounds, organic dyes, organic compounds that can lead to undesirable colour and/or odour, inorganic compounds such as ammonia and nitrite, as well as reducing COD of the source water.
In one embodiment, the third filter stage comprises at least one graphene-based filter comprising a composite material comprising a combination of chitosan and graphene oxide. This cartridge is referred to as a Type C cartridge. In one embodiment, the graphene oxide is few layer graphene oxide.
In one embodiment, the composite material comprises chitosan, about 1% to about 10% graphene oxide, sodium sulfate, and ferric chloride hexahydrate, prepared in a solvent mixture of water and acetic acid.
A Type B cartridge is particularly suitable for achieving up to 95% removal of inorganic compounds such as heavy metal ions from source water. The specific metal ions being removed may include lead, arsenic, chromium, copper, iron, aluminum, nickel, boron, or cadmium.
In one embodiment, the third filter stage comprises at least one graphene-based filter comprising a combination of graphene powder, a composite material comprising chitosan and graphene oxide, and granular activated carbon. This cartridge is referred to as a Type M1 cartridge. In one embodiment, the graphene oxide is few layer graphene oxide. In one embodiment, the graphene is few layer graphene. In a further preferred embodiment, the few layer graphene is Mesograf™.
In one embodiment, the composite material comprises chitosan, about 0.5% to about 10% graphene oxide, sodium sulfate, and ferric chloride hexahydrate, prepared in a solvent mixture of water and acetic acid.
In accordance with the present invention, multiple cartridges of a single type may be used in a parallel arrangement to increase flow through capacity of this stage.
In accordance with the present invention, multiple cartridges may be used in a serial arrangement. In one embodiment, the multiple cartridges may all be of the same type, for example, to increase the filtration effectiveness for a specific contaminant. In one embodiment, the multiple cartridges may be of different types, for example, to increase the filtration effectiveness for multiple contaminants.
The type of cartridge chosen for use in the system depends on the type of chemical contaminant that is present in the source water. For example, if there was a high amount of dye in the water, without concern for reduction of COD or removal of heavy metals, the system could be outfitted with multiple Type A cartridges. If removal of heavy metals and dye were a concern, Type A, C and/or M1 cartridges could be combined in series to target both. The large matrix of possible cartridge combinations allows the system of the present invention to be customizable to the source water specifics.
In one embodiment, the filter system can employ any combination of up to 5 cartridges of Type M1, A, B, and/or C.
The effectiveness of the chemical contaminant removal can be measured using both quantitative and qualitative methods, selected according to the nature of the contaminant being removed. These include methods of chemical detection as are known in the art, including but not limited to, absorbence assays, assays that employ direct and indirect colorimetric analysis of analytes, gas chromatography coupled with suitable analyte detectors to measure the presence of analytes, for example, mass spectrometers, electron capture detectors or flame ionization detectors. For example, removal of a dye contaminant can be qualitatively measured by detection of a decrease in the colour of the filtrate as compared to the input solution.
Each of the types of graphene-based filter cartridges may be regenerated for reuse once the cartridge has reached its filtration/adsorption capacity. In one embodiment, the regeneration process comprising passing a dilute aqueous solution of an acid (for example, sulfuric acid or hydrochloric acid) or a base (for example, sodium hydroxide), through the cartridge. This regeneration protocol allows the cartridges to be reused, which provides a sustainability benefit that cannot be achieved using prior art activated carbon-based filters, which must be disposed of after reaching their filtration capacity is reached.
The graphene oxide-chitosan composite employed in the M1 filter cartridge was found to be an efficient adsorbent of heavy metals while also being readily regenerated for repeated use.
For the adsorption of heavy metals and subsequent regeneration of the chitosan-based adsorbent, an effective, fast, and easy way to regenerate the adsorbents saturated by heavy metals is through adjustment of the pH to the point where desorption can occur. The adsorption can be physisorption or chemisorption. In terms of adsorbent regeneration, physical adsorption is the desirable type due to its reversibility. In contrast, the chemical adsorption is usually an irreversible reaction which makes it impossible or very hard to desorb the adsorbates from the adsorbents surface. Fortunately, the dominant part of heavy metals adsorption on the chitosan surface is physical and reversible. According to zeta potential results reported for chitosan materials in different studies, the surface of chitosan material is expected to be positively charged at pH <7 and it turns to negative at pH >7 (Mukherjee et al., “Sustainable and Affordable Composites Built Using Microstructures Performing Better than Nanostructures for Arsenic Removal,” ACS Sustain. Chem. Eng., vol. 7, no. 3, pp. 3222-3233). Furthermore, the behavior of heavy metals in aqueous media at different pH levels depends on their surface charges. Therefore, the most efficient regeneration can occur in a certain range of pH where desorption is maximum.
For Cr, As, and Fe cations which have surface charges of 3+ or more, some complex compounds are generated at different pH (Mukherjee et al., ACS Sustain. Chem. Eng.; Hadi Najafabadi et al., “Removal of Cu2+, Pb2+ and Cr6+ from aqueous solutions using a chitosan/graphene oxide composite nanofibrous adsorbent,” RSC Adv., vol. 5, no. 21, pp. 16532-16539, 2015). At pH of lower than 2, the complex compounds have no charges on their surface results in lower adsorption rate. By increasing the pH, the components with more negative charges appear in the aquatic media. Therefore, at basic pH repulsion between the charges on the surface of complex heavy metal compounds and the surface of adsorbent will be stronger which results in desorption or precipitation of heavy metals. While, the maximum adsorbent can occur between pH range of 2-7 in which the chitosan surface is positive and the heavy metals component surface is negative.
In case of the cations with 2+ surface charges like Pb, Ni, Cu, or Cd, there is a different scenario. High desorption rate at pH <2 can be explained by the protonation of amide groups on the surface of chitosan material. The electrostatic repulsion between —NH3 and heavy metal cations reduces the adsorption rate. With the increase in pH, the amide protonation decreases results in increasing the adsorption. Then, at basic pH, due to formation of hydroxylated heavy metal complexes, the desorption or precipitation might happen (Hadi Najafabadi et al., RSC Adv.; Sheshmani et al. “Preparation of graphene oxide/chitosan/FeOOH nanocomposite for the removal of Pb(II) from aqueous solution,” Int. J. Biol. Macromol., vol. 80, pp. 475-480, 2015). As a conclusion, the best pH ranges for heavy metal regeneration of chitosan based materials are pH <2 or pH >11.
The fourth filter stage is employed to mechanically remove any particles remaining in the third filtrate that were either too small to be captured by the previous filter stages, including for example, small viruses or nanometer-scale sized particles, or particles released by the third stage, thus providing the final purified water product.
In one embodiment, the fourth filter stage comprises a filter membrane having an average pore opening diameter of from about 8 nm to about 20 nm.
In one embodiment, the fourth filter stage comprises a hollow fiber membrane filter. In one embodiment, a hollow fiber membrane having an average pore diameter of about 8 nm to about 20 nm is chosen to allow passage of the water through at a flow rate of at least 100 litres per hour, while preventing particles larger than 20 nanometers from exiting this stage in the water outflow.
The fourth filter stage can reduce the nanoparticle concentrations to 1-10 ppb, therefore improving the safety of the graphene-based filtration device of the present invention for continuous use in creating a supply of drinking water. The fourth filter stage also provides for the removal of any nanoscale graphene or graphene oxide particles that may leach into the outflow water from the third filter stage. Heretofore, graphene or graphene oxide nanoparticles have not been recognized as a human health concern, but are detectable at 50-250 ppb in the outflow of the third filter stage. Although this concentration is well below the current estimates of a toxicity threshold of 1 ppm, the fourth filter stage therefore provides an additional degree of safety for human consumption of the output drinking water.
In one embodiment, once the fourth stage filter has reached its filtration capacity, it can be regenerated using a crossflow filtration process by forcing water across the filter to dislodge the filtered contaminants from the filter membrane.
The invention will now be described with reference to specific examples. It will be understood that the following examples are intended to describe embodiments of the invention and are not intended to limit the invention in any way.
The performance characteristics for removing phenol and methylene blue of one exemplary embodiment of a Type A cartridge comprising 56 g of pellets comprising polyether sulfone and graphene oxide and 18 grams of Mesograf™ powder in a 10 inch cartridge operating at an operating pressure of 10-60 psi are summarized in Table 2. The water sample was obtained from the Singapore River. Dye concentration in the filtrate is determined using an absorbance assay at 668 nm (the absorbance peak for methylene blue dye).
The Type A cartridge was restored to >90% of its original performance capacity upon regeneration with an aqueous 0.1 M hydrochloric acid solution.
The performance characteristics for removing phenol and ammonia and reducing COD of one exemplary embodiment of a Type B cartridge comprising 60 grams of Mesograf™ powder in a 10 inch cartridge operating at an operating pressure of 10-60 psi are summarized in Table 3. The water sample was obtained from the Singapore River. Ammonia, phenol and COD levels in the samples were determined using colorimetric analytical methods as are known in the art.
The Type A cartridge was restored to >90% of its original performance capacity upon regeneration with an aqueous 0.1 M hydrochloric acid solution.
One exemplary embodiment of a Type C cartridge comprising a graphene oxide and chitosan polymer composite comprising 2% by weight of graphene oxide in a 10-inch cartridge was shown to remove greater than 98% of lead ion (Pb2+) contamination from a wastewater sample comprising an initial concentration of Pb2+ of 190 ppm. The concentration of Pb2+ is determined by ICP-OES elemental analysis.
A Type C cartridge was restored to >90% of its original performance capacity upon regeneration with an aqueous 0.1 M hydrochloric acid solution.
A mixture of 6 L of water and 500 mL of a paste of graphene oxide in water (6 mg/mL) is combined in a 10 L mixing vessel, and stirred overnight. 120 mL of glacial acetic acid was added to the mixing vessel, and stirring continued for 1 hour, followed by addition of 72 g of chitosan powder. Stirring continued for 48 hours to disperse all solids. Once solids were dispersed, a solution of 420 g of Na2SO4 in 200 mL H2O was added to the mixing vessel, and stirring continued for about 12 hours, or until dissolution was complete. 1 L of 1M FeCl3.6H2O was added, and stirred for approximately 3-5 hours. Approximately 450 mL of NaOH solution (500 g/L) was added to adjust the pH to 10. Stirring continued for 3 days. The pH level was checked every 24 hours to ensure the pH remained at pH 10, with adjustment through addition of 1M NaOH or 98% acetic acid to maintain the desired pH level. Solids were filtered by centrifugation and the resulting solid product was dried in an oven at 85° C. for 12 hours. The dried product was washed with water at 300 RPM, the solids were again collected by centrifugation. The washing step was repeated until the total dissolved solids level of the waste water is <50 or the conductivity of the waste water is <100 micron S/cm. The washed product was heated in an oven at 65° C. for 48-72 hours for complete removal of water.
The filtration performance of an exemplary Type M1 cartridge was assessed in comparison to a prior art granulated activated carbon (GAC) filter cartridge. The resulting comparative data is presented in
The general protocol used to generate the comparative data reported in
a Mesograf ™, obtained from Grafoid Inc., Kingston Ontario
b prepared according to the methods of Example 4
c GC 12x40s, General Carbon Corp., from coconut shell
Table 5 provides a summary of average pressure ratings and corresponding clean water output flow rate at three key locations within the Compact Filtration Suitcase (CFS) System flow diagram during automatic CFS operating conditions for filtration of water obtained from Lake Ontario in Kingston, ON.
Experimental Setup: Briefly, clean distilled water (dH2O) was used to stress test CFS filtration stage 3 (S3) over a three-hour experiment in which the dH2O was continuously cycled directly through an M1 filter cartridge as described in Example 5 in a closed loop system. Under all experimental conditions, a separate water sample (volume=2000 mL) was taken for timepoint A (10 minutes of CFS operation) and timepoint B (180 minutes of CFS operation). Under experiment Condition 1, the water passing through S3 filters was sampled directly into 2000 mL beakers and labelled to note the timepoint and sample ID. Under experiment Condition 2, the water passing through S3 filters was subsequently passed through S4 filters, then S4 filtered water was sampled directly into 2000 mL beakers and labelled to note the timepoint and Sample ID. The collected 2000 mL water samples were subsequently handled by personnel employed at the Department of Chemical Engineering at Queen's University. Briefly, the 2000 mL water samples were centrifuged at 19950 RCF for 15 minutes to create a ‘pellet’ of solids which would contain graphene-based nanoparticles picked up in the distilled water from S3.
Prior to analysis by UV-Vis Spectroscopy to detect suspended graphene and graphene oxide particles, the pellet of solids was resuspended in a 10 mL volume of dH2O, which represented a 200× concentration when compared to the original sample volume of 2000 mL. UV-Vis Spectroscopy was utilized to generate a standard curve to describe the relationship between graphene oxide concentration standards ranging from 10 parts per billion (ppb) to 100 parts per million (ppm) and UV-Vis absorbance at 230 nanometer (nm) wavelength setting. UV-Vis Spectroscopy was utilized to generate a standard curve to describe the relationship between graphene concentration standards ranging from 10 parts per billion (ppb) to 100 parts per million (ppm) and UV-Vis absorbance at 265 nm wavelength setting. For these experimental control sample standard curves, an equation of the curve was generated using Microsoft Excel software. R2 values of 0.93 and 0.99 were recorded, respectively. The equation of the curve was used for subsequent analysis of the unknown, 200× concentrated, samples for experiment Condition 1 and experiment Condition 2, which were subjected to UV-Vis Spectroscopy at both 230 nm and 265 nm wavelength settings to detect graphene oxide and/or graphene nanoparticles, respectively. For the unknown, 200× concentrated samples, the absorbance values obtained at 230 nm and 265 nm were used to calculate the expected concentration of graphene oxide and graphene nanoparticles, respectively, from the equation of the curves generated for graphene oxide and graphene experimental controls. The determined concentration for the unknown sample was then divided by 200× to represent the actual concentration within the 2000 mL sample, rather than the centrifuged and concentrated 10 mL sample used for nanoparticle detection purposes only.
It is obvious that the foregoing embodiments of the invention are examples and can be varied in many ways. Such present or future variations are not to be regarded as a departure from the spirit and scope of the invention, and all such modifications as would be obvious to one skilled in the art are intended to be included within the scope of the following claims.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CA2020/050906 | 6/29/2020 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 62868217 | Jun 2019 | US |
