US20080251443A1 - Systems having nanostructured adsorption material and methods for purification of fluid - Google Patents
Systems having nanostructured adsorption material and methods for purification of fluid Download PDFInfo
- Publication number
- US20080251443A1 US20080251443A1 US11/938,049 US93804907A US2008251443A1 US 20080251443 A1 US20080251443 A1 US 20080251443A1 US 93804907 A US93804907 A US 93804907A US 2008251443 A1 US2008251443 A1 US 2008251443A1
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- Prior art keywords
- fluid
- chamber
- porous matrix
- contaminants
- water
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- Abandoned
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- 238000000746 purification Methods 0.000 title claims description 19
- 239000000463 material Substances 0.000 title abstract description 57
- 238000001179 sorption measurement Methods 0.000 title abstract description 31
- 238000000034 method Methods 0.000 title abstract description 16
- 239000011159 matrix material Substances 0.000 claims abstract description 83
- 239000000356 contaminant Substances 0.000 claims abstract description 70
- 239000011148 porous material Substances 0.000 claims abstract description 35
- 229910052709 silver Inorganic materials 0.000 claims description 9
- 239000004332 silver Substances 0.000 claims description 9
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- 239000002086 nanomaterial Substances 0.000 description 9
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Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
- C02F1/002—Processes for the treatment of water whereby the filtration technique is of importance using small portable filters for producing potable water, e.g. personal travel or emergency equipment, survival kits, combat gear
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
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- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
- B01J20/28007—Sorbent size or size distribution, e.g. particle size with size in the range 1-100 nanometers, e.g. nanosized particles, nanofibers, nanotubes, nanowires or the like
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28026—Particles within, immobilised, dispersed, entrapped in or on a matrix, e.g. a resin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/2805—Sorbents inside a permeable or porous casing, e.g. inside a container, bag or membrane
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28052—Several layers of identical or different sorbents stacked in a housing, e.g. in a column
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28078—Pore diameter
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28095—Shape or type of pores, voids, channels, ducts
- B01J20/28097—Shape or type of pores, voids, channels, ducts being coated, filled or plugged with specific compounds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
- C02F1/505—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/08—Nanoparticles or nanotubes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2307/00—Location of water treatment or water treatment device
- C02F2307/02—Location of water treatment or water treatment device as part of a bottle
Definitions
- the present invention relates to removal of particulates and/or contaminants, including impure compounds and elements, from fluid, and more specifically, to containers having a nanostructured adsorption material for removing such particulates and/or contaminants.
- fluid such as water
- fit for consumption may not be available.
- the fluid available such as that in a pond
- the fluid available may contain levels of particulates and/or contaminants exceeding the prescribed limits that is intended for human consumption.
- U.S. Pat. No. 703,654 discloses a canteen having two separate chambers enclosed within the canteen for filtered and unfiltered water. A filtering media is placed between the two chambers and an air-pump is connected to the chamber for unfiltered water. The air-pump is used to force unfiltered water through the filtering media into the chamber for filtered water.
- U.S. Pat. No. 2,781,312 discloses a receptacle for receiving a supply of water having an access opening.
- a loose mass of treating material is provided within the receptacle so that it can be freely dispersed within the water to treat water having chemical content, along with a filter for filtering the treated water of undesirable constituents. Water is forced through the filter for filtration purposes.
- a dye is provided on the treating material to impart color to the water to indicate the state of exhaustion of the treating material is partially or wholly exhausted and thereby signal the operator when the quality of the treated water is below a specified standard.
- U.S. Pat. No. 4,714,550 discloses a water purifying system that includes an elongate chambered purifying assembly that is sized to be detachable mounted in a conventional canteen.
- the assembly is provided with an internal chamber filled with a particulate water purifying material.
- Concentric tubes within the chamber allow water flowing into the chamber through a filtered inlet at the bottom of the assembly to follow an extended chambered flow path through the purifying material to an outlet at the top of the assembly.
- the U.S. Pat. No. 4,800,018 discloses a simplified portable water purification system that provides an unfiltered water receiving compartment, a disposable filter cartridge, and a filtered water reservoir all in a single container.
- the disposable filter cartridge is horizontally positioned centrally and divides the container into the two compartments. Contaminated and unfiltered water is poured into the top receiving compartment of the container and is allowed to pass through filtering materials in the disposable filter cartridge into the reservoir below.
- the U.S. Pat. No. 5,122,272 discloses a container assembly having a removable filter device extending into the container through an opening at the top.
- the filter device comprising an elongated cylindrical member, is constructed so as to provide an upper chamber and a lower chamber.
- the upper chamber serves as a passageway for air entering the container while the lower chamber includes a water filter for water exiting the container.
- water disposed in the container is extracted through the filter by suction and is replaced by air entering the container through the upper chamber.
- the U.S. Pat. No. 5,149,437 discloses a device that includes a filter housing having an inlet at one end for water to be purified and an outlet for purified water at an opposing end.
- the filter device including in sequence first, second and third layers of purification material.
- the first layer of purification material includes metallic particles for establishing a suitable redox potential in the first layer.
- the second layer of purification material includes activated carbon.
- the third layer of purification material includes a weak acid ion exchange resin.
- the U.S. Pat. No. 5,186,830 discloses an apparatus filtering drinking water which includes a lower non-porous container to receive the filtrate.
- An upper vessel closed at its lower end by a high density ceramic filter is stacked in nested relationship to the lower container.
- water containing contaminants and pollutants is poured into the filter vessel, it drips through the ceramic filter under gravitational forces and is stored in the lower receptacle.
- the U.S. Pat. No. 5,431,813 discloses a bottle that includes a water filtering apparatus incorporated within the neck of the bottle. During normal consumption of the water from the water filtering bottle, water is filtered by the filtering apparatus to remove unwanted substances such as pesticides, chlorine, particulate matter, algae, bacteria, heavy metals, and improves odor and flavor of the consumable water.
- the U.S. Pat. No. 5,562,824 discloses a gravity percolation water purifier assembly.
- the assembly includes a covered storage container having a dispensing spigot.
- a flanged filtration chamber is supported beneath the cover to receive untreated water.
- a porous filter cartridge is sealed to an outlet port.
- a purifier cartridge is threaded to the outlet port and supports multiple fibrous spacers and treatment chambers containing beds of treatment media, including a multi-valent iodine media, granular activated carbon, and a halogen scavenger media.
- water passes from multiple inlet ports at an inlet bore through adjoining centric chambers and to the storage container via outlet ports at the periphery of the purifier cartridge.
- the U.S. Pat. No. 5,609,759 discloses a filter assembly for use with a plastic bottle having an open neck.
- the assembly includes a tube of filtering material connected to one surface of a cap with a valve extending from an opposite surface of the cap.
- the tube includes a filtering material, such as activated carbon with plastic binder, having a substantially continuous liquid-porous sidewall, a hollow interior, a first closed end, and a second open end.
- the tube is operatively connected to the cap second surface at the tube second open end.
- a biocidal medium may be disposed within the hollow interior of the filter tube, and the tube may be wrapped with a filter material.
- the filtering material is capable of reducing the level of chlorine and water passing through it by at least 50% at a flow rate of about 5 ml/second.
- the U.S. Pat. No. 5,733,448 discloses a container having two chambers separated by a filter.
- One of the chambers is capable of being compressed so as to pressurize a volume of water to be filtered in the chamber.
- the water is forced through the filter into the second chamber where it is stored for use in a clean and drinkable form.
- the filter includes a series of discs arranged to effectively remove particulate, chemical and other undesired contents of the water.
- the filtered water may be filtered to the molecular level providing an essentially sterile drinking water.
- the U.S. Pat. No. 5,830,360 discloses a gravity-fed, pour-through water filtration device that includes a chamber for housing a spiral filter.
- the devices also includes a biocidal material and an annular holding chamber.
- porous separator disks, a volume of filtration media, and a cyst membrane can be positioned beneath the spiral filter and holding chamber.
- the device is designed to reduce the number of bacteria, viruses and cysts present in the filtrated water.
- the U.S. Pat. No. 6,117,332 discloses a feeder insert for a tubular water filtration cartridge utilized in household point of use water filtration systems.
- the feeder insert allows a chemical to be fed into a incoming water supply at a controlled rate by employing a bypass system that allows a predetermined amount of incoming water to flow past the feed chemical without contacting the chemical.
- the amount of water in the bypass flow can also be manually adjusted through the use of two adjustment mechanisms, an adjustable ring and a rotatable end cap, located on the feeder insert.
- the U.S. Pat. No. 6,344,146 discloses an integrated water purification device which includes a receptacle modified to accommodate a filtration assembly for purifying water, and to store water following purification.
- the receptacle provides separate openings for water intake, and water outflow.
- the filtration assembly includes a pump and a multistage filter cartridge. Pump action draws water into the water purification device and forces the water though the multistage filter and into the receptacle. Purified water may be stored in the receptacle until consumption.
- the U.S. Pat. No. 6,733,669 discloses a water purification system having a watertight polymeric container having an upper unfiltered water receiving chamber and a lower filtered water chamber. A disposable filter cartridge is provided between the chambers. This allows for gravity induced filtering through cartridge as opposed to pressure induced filtering.
- the above referenced systems are designed to filter water by way of a flow-through process utilizing either gravity or pressure.
- a mechanism is not readily available to determine the level of particulates removed by the filter, as well as whether the filter can still remove particulates. Accordingly, it is desirable provide a system for removing particulate from water that not only can display the level of contaminants removed, but whether contaminants can still be removed by a particulate removal mechanism.
- the system includes a receptacle having a chamber into which a volume of fluid may be placed.
- the system may also include a porous matrix placed within the chamber for entrapment of the particulates and/or contaminants upon surface contact between the fluid and the porous matrix.
- the porous matrix includes a nanostructured adsorption material and may be embedded on the interior surface of the receptacle.
- the porous matrix may be placed onto the interior surface of the receptacle as a thin film, coating, layer or as a sheet of material.
- the porous matrix may be a loose mass of macro particles that can freely move within the fluid in the receptacle.
- the nanostructured adsorption material in one embodiment, may be contain different chemical materials, including silver or silver compounds.
- the system may further include a sensor in communication with the porous matrix, so as to detect levels of particulates and/or contaminants adsorbed on the matrix or quantity of particulates and/or contaminants removed from the fluid to be treated.
- the present invention also provides a method for purification of fluid by removing unwanted particulates and/or contaminants from a fluid.
- a receptacle having a chamber for accommodating a fluid to be treated may be provided.
- a porous matrix having nanoscaled pores may thereafter be placed within the chamber.
- the fluid to be treated may next be introduced into the chamber.
- movement of the fluid within the receptacle may be initiated.
- the particulates and/or contaminants may be directed within the porous matrix and trapped therein. If there is no movement of drinking water within the portable containers or bottles, the contaminants may still removed by slow molecular displacement or diffusion into the porous matrix.
- levels of contaminants removed from the fluid may be indicated, as well as whether the ability of the porous matrix to remove additional contaminants has been exhausted.
- FIG. 1 illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with one embodiment of the present invention.
- FIGS. 2A-B illustrate a cross section view of various porous matrices for use in connection with the present invention.
- FIG. 3A illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with another embodiment of the present invention.
- FIG. 3B illustrates a sectional view of a porous matrix for use in connection with the system in FIG. 3A .
- FIG. 4A illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with still another embodiment of the present invention.
- FIG. 4B illustrates a cross sectional view of the receptacle shown in FIG. 4A .
- FIG. 5 illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with a further embodiment of the present invention.
- FIG. 6 illustrates a longitudinal section view of another system for removing contaminants from fluid in accordance with one embodiment of the present invention.
- FIG. 7 illustrates schematically the process for removing contaminants from fluid in accordance with one embodiment of the present invention.
- the present invention provides, in one embodiment, a system purification of fluid for consumption by removing particulates, such as impure and undesirable constituents, contaminants, such as microorganisms, biological contaminants, organic and inorganic compounds and elements, and/or matters or substances ranging from about 1 nanometer (nm) to about 100 nm or larger from the fluid, for instance water, so that the resulting treated or purified fluid will be safe to consume, i.e., the fluid has levels of contaminants not exceed the prescribed limits intended for human consumption.
- particulates such as impure and undesirable constituents, contaminants, such as microorganisms, biological contaminants, organic and inorganic compounds and elements, and/or matters or substances ranging from about 1 nanometer (nm) to about 100 nm or larger from the fluid, for instance water, so that the resulting treated or purified fluid will be safe to consume, i.e., the fluid has levels of contaminants not exceed the prescribed limits intended for human consumption.
- FIG. 1 there is shown a system 10 having a receptacle 11 , for example, a bottle, a container, or the like, into which a volume of fluid to be treated or purified may be placed.
- the receptacle 11 may include a chamber 12 for accommodating a volume of fluid, and an opening 13 through which a volume of fluid may be introduced into the chamber 12 .
- a cover 14 may be provided across the opening 13 to prevent spillage of fluid from within the chamber 12 .
- the cover 14 in one embodiment, may be a snap-on cover, a threaded cover, or any other cover known in the art, so long as it can operate to prevent fluid from spilling from within the chamber 12 .
- the receptacle 11 may be larger in scale and can be of any size, depending on the application of interest.
- the receptacle 11 may be made from a transparent material to permit viewing of the fluid content therein.
- the system 10 may also include a porous matrix, such as that illustrated in FIGS. 2A and 2B , positioned within the chamber 12 for the removal of particulates and/or contaminants from the fluid within chamber 12 .
- porous matrix 20 may include a nanostructured adsorption material 21 having a large volume of pores 23 .
- the porous matrix 20 may be provided with a fluid contact surface 24 against or across which fluid within the chamber 12 may flow, and a substantially fluid impermeable surface 25 across which fluid within the porous matrix 20 and chamber 12 cannot pass.
- Pores 23 in one embodiment, may be nanoscale in size, ranging from about 1 nanometer (nm) to about 100 nm.
- the pores 23 may include a total volume ranging from about 0.5 cm 3 /g to about 1.0 cm 3 /g. In a preferred embodiment, the total volume of pores 23 may range from about 0.8 cm 3 /g to about 0.95 cm 3 /g, with a total specific surface area ranging from at least approximately 1000 m 2 /g to approximately 3000 m 2 /g, and higher.
- the nanostructured adsorption material 21 may include, in one embodiment, a plurality of layers 22 , each having pores 23 within a predetermined size range.
- layers 22 may be arranged so that the pores 23 in each successive layer 22 get successively smaller in size, moving from the layer immediately adjacent the contact surface 24 to the layer immediately adjacent the substantially impermeable surface 25 . In this manner, smaller particulates and/or contaminants may be permitted to move through the larger pores adjacent the contact surface 24 and into the smaller pores adjacent the substantially impermeable surface 25 where they can be trapped and retained.
- the nanostructured adsorption material 21 may be designed without distinctive layers 22 , such that pores 23 of various nanoscale size ranges may be interspersed throughout the entire nanostructured adsorption material 21 .
- the nanostructured adsorption material 21 may be provided with a plurality of layers as shown in FIG. 2A , while each layer may include pores 23 of various nanoscale size ranges interspersed therein, similar to those in FIG. 2B .
- the porous matrix 20 used in connection with the system 10 of the present invention may, in one embodiment, be formed from, for instance, porous char generated from various starting materials, for example, discarded or used automobile tires or other materials that can generate a relatively high fixed carbon content within the porous char.
- the starting materials may be heated in a reactor, within which the environment may be controlled, initially from room temperature to about 250° C. to 300° C. During this initial heating period, a mixture of condensable and non-condensable gases may be given off from the starting material within the reactor.
- This mixture of gases which can be captured for reintroduction at a later stage, can typically include approximately 25%-35% carbon dioxide, approximately 10%-15% carbon monoxide, approximately 5%-10% methane, approximately 1%-5% volatile acids, with the remaining portion containing a mixture of hydrogen, oxygen, hydrocarbons, i.e., organic materials.
- an exothermic reaction can occur within the reactor pushing the temperature of the reactor and thus the resulting porous char to temperatures ranging from about 500° C. to about 600° C.
- the previously captured condensable and non-condensable gases may be reintroduced into the reactor for exposure to the porous char.
- the resulting porous char may contain, at this stage, mostly macro-pores and may only be moderately dense in nature. To subsequently obtain a nanostructured adsorption material, this moderately dense porous char must be transformed to a relatively high-density material with a relatively high fixed carbon content.
- impurities present in the starting materials, and in the transformed material, i.e., porous char may be removed, using known procedures, at various stages during the conversion process to produce a fixed carbon content in the porous char of greater than about 90% to about 95%. It should be noted that, on average, approximately 20 pounds of starting material, e.g., used tires, will yield about 4 pounds of porous char with a fixed carbon content of between 90% to 95%.
- the temperature within the reactor may be increased so that the porous char may be heated at a relatively high temperature range of from about 1000° C.
- a controlled mixture of steam and air may be introduced into the reactor.
- a controlled mixture of steam and air may be introduced into the reactor.
- from about 1.0 pound to about 1.5 pounds of steam and air mixture may be injected into the reactor.
- the amount of steam and air may vary depending upon how much the pores within the porous char are to be enlarged, and could vary from about 0.5 pounds to over 2.0 pounds per pound of porous char.
- the introduction of steam and air into the reactor in one embodiment, can generate a producer gas in the presence of the hot porous char.
- the content of the producer gas may vary, but can contain about 15%-20% hydrogen, 20%-25% carbon monoxide, with the remainder a mixture of nitrogen, hydrocarbons and other organic materials.
- the porous char By exposing the porous char to such a temperature range and a mixture of steam and air, the porous char may be transformed into a relatively high density nanostructured material having the desired porosity. Typically, approximately 1 pound of the high density nanostructured material can be generated from the 4 pounds of the porous char.
- the exposure of the porous char to such high temperature in addition to enlarging and generating pores of various nanoscale sizes, can provide the resulting nanostructured adsorption material with internal surface areas ranging from at least approximately 1000 m 2 /g to approximately 3000 m 2 /g, and higher.
- the resulting nanostructured material may be used in connection with the porous matrix 20 of the present invention.
- the process of enlarging the pores structure to specific nanoscale ranges, along with the removal of impurities within the porous char can impart special properties to the nanostructured material.
- such a process can impart the nanostructured material with adsorption properties necessary for removal of particulates and contaminants.
- the ability of nanostructured material to adsorb particulates and contaminant molecules can also be dependent upon the structure of the nanoscale pores, the total surface area, the carbon particle size, and the void space between carbon particles.
- the nanostructured adsorption material such as item 21 in FIGS. 2A and 2B , essentially comprises nanocarbon particles 26
- the spaces 27 between these nanocarbon particles must be sufficiently small, i.e., nanoscale in size and smaller than the molecules of the fluid, so as to facilitate the fluid going through the pores 23 within the nanoadsorption material 21 and not through spaces around the pores 23 .
- the carbon particles may block, partially block, and/or create interference with the flow of the fluid into the pores 23 , thus allowing fluid to flow away from the pores 23 .
- particulates and/or contaminants within the fluid flow may escape entrapment within the pores 23 .
- the porous matrix 20 may further, in accordance with an embodiment of the present invention, be impregnated with, for instance, silver or silver compound(s) so as to minimize microbial growth within the porous matrix 20 .
- the nanostructured adsorption material 21 may be treated with a silver compound in the presence of acid or alkaline materials, depending on the silver compound used, so that the silver compound can be substantially evenly distributed against internal surfaces of pores 23 . Since this process can generate undesirable materials during the chemical reactions, such materials can be removed, in one embodiment, by leaching.
- the process employed herein can enhance the properties of the porous matrix 20 .
- the presence of the silver compound as noted, can minimize microbial growth within the porous matrix 20 .
- the silver content provided within the porous matrix 20 using the process described herein may be at a level far below the permissible limits of silver in drinking water. In an embodiment, the silver content may be approximately 1 percent by weight. Additionally, the process employed herein can minimize the leaching of the silver content from within the porous matrix 20 . In this manner, the presence of the silver compound within the porous matrix 20 does not act to elevate the level of silver above permissible limits.
- the system 30 may include a receptacle 31 , similar to that of system 10 shown in FIG. 1 .
- the receptacle 31 may include a chamber 32 for accommodating a volume of fluid, and an opening 33 through which a volume of fluid may be introduced into the chamber 32 .
- a cover 34 may be provided across the opening 33 to prevent spillage of fluid from within the chamber 32 .
- the system 30 may also include a porous matrix 35 positioned within the chamber 32 for the removal of contaminants from the fluid.
- the porous matrix 35 in accordance with one embodiment of the present invention, may be substantially similar to the porous matrix 20 of FIGS. 2A-B , and may be used to retain or trap particulates and/or contaminants in the fluid.
- the porous matrix 35 as shown in FIG. 3B , and used in connection with system 30 , may be embedded within chamber walls 36 , so that contact surface 37 may be exposed to the fluid within the chamber 32 , while substantially impermeable surface 38 may be positioned against chamber walls 36 .
- the porous matrix 35 may be embedded substantially circumferentially about chamber walls 36 .
- porous matrix 35 may be permitted to extend substantially along the length of walls 36 .
- means known in the art may be employed, for instance, co-extrusion of the porous matrix 35 along with the material comprising receptacle 31 .
- porous matrix 35 may be provided with a thickness ranging from about 0.20 mm to about 0.30 mm.
- the porous matrix 35 instead of being embedded within the walls 36 of the chamber 32 , the porous matrix 35 , made from a nanostructured adsorption material, may be applied directly onto the walls 36 .
- the porous matrix may be coated onto walls 36 as a thin film or layer.
- the porous matrix 35 may be designed as a sheet of material that can be adhered to the walls 36 of chamber 32 . Regardless of the adherence material used, such material should be one that is non degradable in the presence of fluid.
- the thin film or sheet of porous matrix 35 may be designed so that it is sufficiently flexible and pliable for removal or insertion across opening 33 .
- the system 40 may include a receptacle 41 having a chamber 42 for accommodating a volume of fluid, and an opening 43 through which a volume of fluid may be introduced into the chamber 42 .
- a cover 44 may be provided across the opening 43 to prevent spillage of fluid from within the chamber 42 .
- the system 40 may also include a porous matrix 45 positioned within the chamber 42 for the removal of contaminants from the fluid.
- the porous matrix 45 being substantially similarly to the previous porous matrices, acts to retain or trap therein contaminants from the fluid.
- the porous matrix 45 made from a nanostructured adsorption material, may be designed as a substantially cylindrical tube 47 having a contact surface 471 , and an opposing impermeable surface 472 .
- the porous matrix 45 as shown in FIG. 4A , may be positioned away from walls 46 of chamber 42 . In one embodiment, as illustrated from the perspective of FIG.
- porous matrix 45 may be positioned substantially concentrically to the walls 46 , and may be designed to have a diameter that permits its removal from or placement within the chamber 42 through opening 43 .
- a base (not shown) may be provided within which porous matrix 45 may be positioned.
- porous matrix 45 may be permitted to float freely within the chamber 42 .
- FIG. 5 there is illustrated another system 50 for purification of a fluid by removing contaminants, such as microorganisms, organic, inorganic and particulate matter from the fluid, in accordance with one embodiment of the present invention.
- the system 50 may include a receptacle 51 having a chamber 52 for accommodating a volume of fluid, and an opening 53 through which a volume of fluid may be introduced into the chamber 52 .
- a cover 54 may be provided across the opening 53 to prevent spillage of fluid from within the chamber 52 .
- the system 50 may also include a porous matrix 55 positioned within the chamber 52 for retaining, trapping, and thus removal of contaminants from the fluid.
- the porous matrix 55 made from a nanostructured adsorption material, and in accordance with this particular embodiment of the present invention, may be provided as a loose mass of macro particles 56 that can freely move within the fluid in chamber 52 .
- Each of the particles 56 may include a contact surface 561 and an impermeable core (not shown), so that fluid may be prevented from flowing through the particles 56 .
- the particles 56 in one embodiment, may be uniform in size and shape, or as illustrated, vary in size and shape. It should be appreciated that the particles 56 may be of a size and shape that would facilitate their removal from or placement within the chamber 52 through opening 53 for replacement purposes.
- a system 60 for purification of fluid by removing contaminants, such as microorganisms, organic, inorganic and particulate matter from the fluid.
- the system 60 may include a receptacle 61 having a chamber 62 for accommodating a volume of fluid, and an opening 63 through which a volume of fluid may be introduced into the chamber 62 .
- a cover 64 may be provided across the opening 63 to prevent spillage of fluid from within the chamber 62 .
- the system 60 may also include a porous matrix 65 , made from a nanostructured adsorption material, that is positioned within the chamber 52 for retaining, trapping, and thus removal of contaminants from the fluid.
- the porous matrix 65 in accordance with one embodiment of the present invention, may be placed circumferentially about walls 66 at an end 67 of the chamber 62 opposite the opening 63 .
- porous matrix 65 may be designed to be sufficiently flexible and pliable to permit its removal from and placement within the chamber 62 through opening 63 .
- receptacle 61 may be provided with a removable end 67 about which porous matrix 65 may be circumferentially situated. In this manner, should the porous matrix 65 needs to be exchanged, the end 67 may be removed from receptacle 61 and disposed along with matrix 65 , and a new end 67 with new porous matrix 65 may be reattached to receptacle 61 .
- the end 67 and the receptacle 61 may be provided with threaded engagement.
- other engagement mechanisms known in the art, for example, snap-fit etc. may be used, so long as such engagement can prevent leakage of fluid from within the chamber 62 , while permitting easy removal of end 67 from the receptacle 61 .
- the system of the present invention may be used to purify fluid by removing particulates and/or contaminants from the fluid, such as water, when the levels of particulates and/or contaminants exceed the prescribed limits for fluid that is intended for human consumption.
- the limits of contaminants in the drinking fluids may be prescribed by the regulators.
- fluid 71 that may include particulates and/or contaminants may be initially be introduced into the chamber of receptacle 72 .
- the fluid along with the molecules of contaminants therein when come into contact with the porous matrix having the nanostructured adsorption material (e.g., flowing against or across the contact surface of the porous matrix), may be directed into the pores of the nanostructured adsorption material, wherein the molecules of contaminants may be trapped.
- the movement of fluid within the receptacle caused by or due to, for instance, shaking or moving of the receptacle should be sufficient to direct the flow of contaminants into the pores. If the situation is such that there is no movement of fluid within the receptacle, the contaminants may still be removed by slow molecular displacement or diffusion of molecules into the porous matrix within the receptacle.
- the particulates and/or contaminants typically cannot be released from the pores within which they are trapped without enormous pressure or the application of heat at elevated levels.
- the weight of nanostructured adsorption material can increase to a measurable difference. Such an increase can be detected and displayed, for example, by a sensor, to indicate, for instance, the levels of contaminants removed from the fluid.
- a sensor 73 may be coupled to the receptacle 72 , such that the sensor 73 may be in communication with a porous matrix within the receptacle in order to display the levels of contaminants removed from the fluid.
- Sensor 73 can be any sensor which can detect a pressure, weight or heat differential between a porous matrix at time t o and the same porous matrix at time t n , subsequent to exposure of the porous matrix to the fluid.
- the sensor 73 may include pressure detector sufficiently thin (e.g., thin layer wired mesh or sheet), so as to be capable of being embedded within the nanostructured adsorption material of the porous matrix, and a display in communication with the detector. The pressure detector can act to transform the pressure differential between t o and t n into electrical signals that can subsequently be process and shown on the display as the amount of particulates or contaminants in the porous matrix or the amount of contaminant removed.
- the sensor 73 may alternatively employ a weight sensor. It is noted that if at t o the weight of the porous matrix is x milligram, then at t n , for instance, 15 seconds, when the nanostructured material of the porous matrix has had a chance to adsorb the particulates and/or contaminants, the weight of nanostructured adsorption material will be x+y, with y being the weight of contaminants that has been removed from the fluid. The weight increase due to the adsorption of the contaminants can be transformed to electrical signals, which can subsequently be displayed as information on a scale in terms of percentage of contaminants removed from the fluid.
- the sensor 73 may also employ a heat sensor. If, for instance, at t o the temperature of the porous matrix is x degrees, then at t n , for instance, 15 seconds, when the nanostructured material of the porous matrix has had a chance to adsorb the particulates and/or contaminants, the heat generated in the nanostructured adsorption material will be x+y, with y being the temperature increase due to the adsorption of contaminants in the nanostructured material. This temperature increase can be transformed to electrical signals, which can subsequently be displayed as information on a scale in terms of percentage of contaminants removed from the fluid.
- the senor 73 in one embodiment, can be designed to warn the user, for instance, by audio, visual, or other applicable indicators, that the porous matrix needs replacing or that the receptacle can no longer be used, if the receptacle is designed to be a disposable system.
- the system of the present invention accordingly, may be refilled over and over again with fluid to be treated.
- the system may be used successively to generate purified fluid meeting standards or limits prescribed for human consumption, until the nanostructured adsorption material of the porous matrix approaches its exhaustive capacity for trapping and retaining particles therein, i.e., having entrapped and retained therein particulates and/or contaminants at about 90% of its capacity.
Abstract
A system for removing particulates and/or contaminants, including impure compounds and elements from fluid to be treated is provided. The systems can include a receptacle having chamber in which a volume of fluid may be accommodated, a cover for placement across an opening into the chamber, so as to prevent fluid from within the chamber from spilling, and a porous matrix, positioned within the chamber and having a nanostructured adsorption material for trapping and retaining, within its pores, particles and contaminants in the fluid. A method for removing particulates and contaminants is also provided.
Description
- The present invention relates to removal of particulates and/or contaminants, including impure compounds and elements, from fluid, and more specifically, to containers having a nanostructured adsorption material for removing such particulates and/or contaminants.
- In many instances, fluid, such as water, fit for consumption may not be available. For example, during an extended trip away from a concentrated community, the fluid available, such as that in a pond, may contain levels of particulates and/or contaminants exceeding the prescribed limits that is intended for human consumption. Currently, there are various known processes and methods for removal of particulates, including impure compounds and elements, and/or contaminants from fluid.
- U.S. Pat. No. 703,654 discloses a canteen having two separate chambers enclosed within the canteen for filtered and unfiltered water. A filtering media is placed between the two chambers and an air-pump is connected to the chamber for unfiltered water. The air-pump is used to force unfiltered water through the filtering media into the chamber for filtered water.
- U.S. Pat. No. 2,781,312 discloses a receptacle for receiving a supply of water having an access opening. A loose mass of treating material is provided within the receptacle so that it can be freely dispersed within the water to treat water having chemical content, along with a filter for filtering the treated water of undesirable constituents. Water is forced through the filter for filtration purposes. A dye is provided on the treating material to impart color to the water to indicate the state of exhaustion of the treating material is partially or wholly exhausted and thereby signal the operator when the quality of the treated water is below a specified standard.
- U.S. Pat. No. 4,714,550 discloses a water purifying system that includes an elongate chambered purifying assembly that is sized to be detachable mounted in a conventional canteen. The assembly is provided with an internal chamber filled with a particulate water purifying material. Concentric tubes within the chamber allow water flowing into the chamber through a filtered inlet at the bottom of the assembly to follow an extended chambered flow path through the purifying material to an outlet at the top of the assembly.
- The U.S. Pat. No. 4,800,018 discloses a simplified portable water purification system that provides an unfiltered water receiving compartment, a disposable filter cartridge, and a filtered water reservoir all in a single container. The disposable filter cartridge is horizontally positioned centrally and divides the container into the two compartments. Contaminated and unfiltered water is poured into the top receiving compartment of the container and is allowed to pass through filtering materials in the disposable filter cartridge into the reservoir below.
- The U.S. Pat. No. 5,122,272 discloses a container assembly having a removable filter device extending into the container through an opening at the top. The filter device, comprising an elongated cylindrical member, is constructed so as to provide an upper chamber and a lower chamber. The upper chamber serves as a passageway for air entering the container while the lower chamber includes a water filter for water exiting the container. In using the container, water disposed in the container is extracted through the filter by suction and is replaced by air entering the container through the upper chamber.
- The U.S. Pat. No. 5,149,437 discloses a device that includes a filter housing having an inlet at one end for water to be purified and an outlet for purified water at an opposing end. The filter device including in sequence first, second and third layers of purification material. The first layer of purification material includes metallic particles for establishing a suitable redox potential in the first layer. The second layer of purification material includes activated carbon. The third layer of purification material includes a weak acid ion exchange resin.
- The U.S. Pat. No. 5,186,830 discloses an apparatus filtering drinking water which includes a lower non-porous container to receive the filtrate. An upper vessel closed at its lower end by a high density ceramic filter is stacked in nested relationship to the lower container. When water containing contaminants and pollutants is poured into the filter vessel, it drips through the ceramic filter under gravitational forces and is stored in the lower receptacle.
- The U.S. Pat. No. 5,431,813 discloses a bottle that includes a water filtering apparatus incorporated within the neck of the bottle. During normal consumption of the water from the water filtering bottle, water is filtered by the filtering apparatus to remove unwanted substances such as pesticides, chlorine, particulate matter, algae, bacteria, heavy metals, and improves odor and flavor of the consumable water.
- The U.S. Pat. No. 5,562,824 discloses a gravity percolation water purifier assembly. The assembly includes a covered storage container having a dispensing spigot. A flanged filtration chamber is supported beneath the cover to receive untreated water. A porous filter cartridge is sealed to an outlet port. A purifier cartridge is threaded to the outlet port and supports multiple fibrous spacers and treatment chambers containing beds of treatment media, including a multi-valent iodine media, granular activated carbon, and a halogen scavenger media. In one purification cartridge, water passes from multiple inlet ports at an inlet bore through adjoining centric chambers and to the storage container via outlet ports at the periphery of the purifier cartridge.
- The U.S. Pat. No. 5,609,759 discloses a filter assembly for use with a plastic bottle having an open neck. The assembly includes a tube of filtering material connected to one surface of a cap with a valve extending from an opposite surface of the cap. The tube includes a filtering material, such as activated carbon with plastic binder, having a substantially continuous liquid-porous sidewall, a hollow interior, a first closed end, and a second open end. The tube is operatively connected to the cap second surface at the tube second open end. A biocidal medium may be disposed within the hollow interior of the filter tube, and the tube may be wrapped with a filter material. The filtering material is capable of reducing the level of chlorine and water passing through it by at least 50% at a flow rate of about 5 ml/second.
- The U.S. Pat. No. 5,733,448 discloses a container having two chambers separated by a filter. One of the chambers is capable of being compressed so as to pressurize a volume of water to be filtered in the chamber. Upon applying pressure, the water is forced through the filter into the second chamber where it is stored for use in a clean and drinkable form. The filter includes a series of discs arranged to effectively remove particulate, chemical and other undesired contents of the water. The filtered water may be filtered to the molecular level providing an essentially sterile drinking water.
- The U.S. Pat. No. 5,830,360 discloses a gravity-fed, pour-through water filtration device that includes a chamber for housing a spiral filter. The devices also includes a biocidal material and an annular holding chamber. Several porous separator disks, a volume of filtration media, and a cyst membrane can be positioned beneath the spiral filter and holding chamber. The device is designed to reduce the number of bacteria, viruses and cysts present in the filtrated water.
- The U.S. Pat. No. 6,117,332 discloses a feeder insert for a tubular water filtration cartridge utilized in household point of use water filtration systems. The feeder insert allows a chemical to be fed into a incoming water supply at a controlled rate by employing a bypass system that allows a predetermined amount of incoming water to flow past the feed chemical without contacting the chemical. The amount of water in the bypass flow can also be manually adjusted through the use of two adjustment mechanisms, an adjustable ring and a rotatable end cap, located on the feeder insert.
- The U.S. Pat. No. 6,344,146 discloses an integrated water purification device which includes a receptacle modified to accommodate a filtration assembly for purifying water, and to store water following purification. The receptacle provides separate openings for water intake, and water outflow. The filtration assembly includes a pump and a multistage filter cartridge. Pump action draws water into the water purification device and forces the water though the multistage filter and into the receptacle. Purified water may be stored in the receptacle until consumption.
- The U.S. Pat. No. 6,733,669 discloses a water purification system having a watertight polymeric container having an upper unfiltered water receiving chamber and a lower filtered water chamber. A disposable filter cartridge is provided between the chambers. This allows for gravity induced filtering through cartridge as opposed to pressure induced filtering.
- The above referenced systems are designed to filter water by way of a flow-through process utilizing either gravity or pressure. In addition, with these systems, a mechanism is not readily available to determine the level of particulates removed by the filter, as well as whether the filter can still remove particulates. Accordingly, it is desirable provide a system for removing particulate from water that not only can display the level of contaminants removed, but whether contaminants can still be removed by a particulate removal mechanism.
- The invention described herein relates to a system designed for purification of fluid for consumption by removing contaminants, such as microorganisms, organic, inorganic, and particulate matters from the fluid. In one embodiment of the present invention, the system includes a receptacle having a chamber into which a volume of fluid may be placed. The system may also include a porous matrix placed within the chamber for entrapment of the particulates and/or contaminants upon surface contact between the fluid and the porous matrix. In one embodiment, the porous matrix includes a nanostructured adsorption material and may be embedded on the interior surface of the receptacle. Alternatively, the porous matrix may be placed onto the interior surface of the receptacle as a thin film, coating, layer or as a sheet of material. In another embodiment, the porous matrix may be a loose mass of macro particles that can freely move within the fluid in the receptacle. The nanostructured adsorption material, in one embodiment, may be contain different chemical materials, including silver or silver compounds. The system may further include a sensor in communication with the porous matrix, so as to detect levels of particulates and/or contaminants adsorbed on the matrix or quantity of particulates and/or contaminants removed from the fluid to be treated.
- The present invention also provides a method for purification of fluid by removing unwanted particulates and/or contaminants from a fluid. In one embodiment, a receptacle having a chamber for accommodating a fluid to be treated may be provided. A porous matrix having nanoscaled pores may thereafter be placed within the chamber. The fluid to be treated may next be introduced into the chamber. Next, movement of the fluid within the receptacle may be initiated. Upon surface contact between the fluid and the porous matrix, the particulates and/or contaminants may be directed within the porous matrix and trapped therein. If there is no movement of drinking water within the portable containers or bottles, the contaminants may still removed by slow molecular displacement or diffusion into the porous matrix. In an embodiment, levels of contaminants removed from the fluid may be indicated, as well as whether the ability of the porous matrix to remove additional contaminants has been exhausted.
- The invention is explained in greater detail below with reference to an exemplary embodiment that is illustrated in the accompanying figures.
-
FIG. 1 illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with one embodiment of the present invention. -
FIGS. 2A-B illustrate a cross section view of various porous matrices for use in connection with the present invention. -
FIG. 3A illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with another embodiment of the present invention. -
FIG. 3B illustrates a sectional view of a porous matrix for use in connection with the system inFIG. 3A . -
FIG. 4A illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with still another embodiment of the present invention. -
FIG. 4B illustrates a cross sectional view of the receptacle shown inFIG. 4A . -
FIG. 5 illustrates a longitudinal section view of a system for removing contaminants from fluid in accordance with a further embodiment of the present invention. -
FIG. 6 illustrates a longitudinal section view of another system for removing contaminants from fluid in accordance with one embodiment of the present invention. -
FIG. 7 illustrates schematically the process for removing contaminants from fluid in accordance with one embodiment of the present invention. - The present invention provides, in one embodiment, a system purification of fluid for consumption by removing particulates, such as impure and undesirable constituents, contaminants, such as microorganisms, biological contaminants, organic and inorganic compounds and elements, and/or matters or substances ranging from about 1 nanometer (nm) to about 100 nm or larger from the fluid, for instance water, so that the resulting treated or purified fluid will be safe to consume, i.e., the fluid has levels of contaminants not exceed the prescribed limits intended for human consumption.
- In
FIG. 1 , there is shown asystem 10 having areceptacle 11, for example, a bottle, a container, or the like, into which a volume of fluid to be treated or purified may be placed. Thereceptacle 11, in one embodiment, may include achamber 12 for accommodating a volume of fluid, and anopening 13 through which a volume of fluid may be introduced into thechamber 12. Acover 14 may be provided across theopening 13 to prevent spillage of fluid from within thechamber 12. Thecover 14, in one embodiment, may be a snap-on cover, a threaded cover, or any other cover known in the art, so long as it can operate to prevent fluid from spilling from within thechamber 12. Although illustrated as a portable container, thereceptacle 11 may be larger in scale and can be of any size, depending on the application of interest. In addition, thereceptacle 11 may be made from a transparent material to permit viewing of the fluid content therein. - The
system 10 may also include a porous matrix, such as that illustrated inFIGS. 2A and 2B , positioned within thechamber 12 for the removal of particulates and/or contaminants from the fluid withinchamber 12. In accordance with one embodiment of the present invention,porous matrix 20 may include ananostructured adsorption material 21 having a large volume ofpores 23. In addition, theporous matrix 20 may be provided with afluid contact surface 24 against or across which fluid within thechamber 12 may flow, and a substantially fluidimpermeable surface 25 across which fluid within theporous matrix 20 andchamber 12 cannot pass.Pores 23, in one embodiment, may be nanoscale in size, ranging from about 1 nanometer (nm) to about 100 nm. In this manner, particles and/or contaminants ranging from about 1 nm to about 10 nm or larger can be removed from the fluid. Thepores 23 may include a total volume ranging from about 0.5 cm3/g to about 1.0 cm3/g. In a preferred embodiment, the total volume ofpores 23 may range from about 0.8 cm3/g to about 0.95 cm3/g, with a total specific surface area ranging from at least approximately 1000 m2/g to approximately 3000 m2/g, and higher. - As illustrated in
FIG. 2A , thenanostructured adsorption material 21 may include, in one embodiment, a plurality oflayers 22, each having pores 23 within a predetermined size range. In such an embodiment, layers 22 may be arranged so that thepores 23 in eachsuccessive layer 22 get successively smaller in size, moving from the layer immediately adjacent thecontact surface 24 to the layer immediately adjacent the substantiallyimpermeable surface 25. In this manner, smaller particulates and/or contaminants may be permitted to move through the larger pores adjacent thecontact surface 24 and into the smaller pores adjacent the substantiallyimpermeable surface 25 where they can be trapped and retained. - Alternatively, as illustrated in
FIG. 2B , thenanostructured adsorption material 21 may be designed withoutdistinctive layers 22, such that pores 23 of various nanoscale size ranges may be interspersed throughout the entirenanostructured adsorption material 21. Although not illustrated, it should be appreciated that thenanostructured adsorption material 21 may be provided with a plurality of layers as shown inFIG. 2A , while each layer may includepores 23 of various nanoscale size ranges interspersed therein, similar to those inFIG. 2B . - The
porous matrix 20 used in connection with thesystem 10 of the present invention may, in one embodiment, be formed from, for instance, porous char generated from various starting materials, for example, discarded or used automobile tires or other materials that can generate a relatively high fixed carbon content within the porous char. Of course, new automobile tires or similar starting materials may also be used to generated the porous char. In one embodiment, the starting materials may be heated in a reactor, within which the environment may be controlled, initially from room temperature to about 250° C. to 300° C. During this initial heating period, a mixture of condensable and non-condensable gases may be given off from the starting material within the reactor. This mixture of gases, which can be captured for reintroduction at a later stage, can typically include approximately 25%-35% carbon dioxide, approximately 10%-15% carbon monoxide, approximately 5%-10% methane, approximately 1%-5% volatile acids, with the remaining portion containing a mixture of hydrogen, oxygen, hydrocarbons, i.e., organic materials. - Upon the reaching between 250° C. to 300° C., an exothermic reaction can occur within the reactor pushing the temperature of the reactor and thus the resulting porous char to temperatures ranging from about 500° C. to about 600° C. During this period, the previously captured condensable and non-condensable gases may be reintroduced into the reactor for exposure to the porous char. The resulting porous char may contain, at this stage, mostly macro-pores and may only be moderately dense in nature. To subsequently obtain a nanostructured adsorption material, this moderately dense porous char must be transformed to a relatively high-density material with a relatively high fixed carbon content.
- To generate a relatively high fixed carbon content in the porous char, impurities present in the starting materials, and in the transformed material, i.e., porous char, may be removed, using known procedures, at various stages during the conversion process to produce a fixed carbon content in the porous char of greater than about 90% to about 95%. It should be noted that, on average, approximately 20 pounds of starting material, e.g., used tires, will yield about 4 pounds of porous char with a fixed carbon content of between 90% to 95%. Once the condensable and non-condensable gases have been reintroduced into the reactor, the temperature within the reactor may be increased so that the porous char may be heated at a relatively high temperature range of from about 1000° C. to about 1100° C. to enlarge the pores within the porous char. During this stage, a controlled mixture of steam and air may be introduced into the reactor. In one embodiment, for approximately 1 pound of porous char, from about 1.0 pound to about 1.5 pounds of steam and air mixture may be injected into the reactor. The amount of steam and air may vary depending upon how much the pores within the porous char are to be enlarged, and could vary from about 0.5 pounds to over 2.0 pounds per pound of porous char. The introduction of steam and air into the reactor, in one embodiment, can generate a producer gas in the presence of the hot porous char. The content of the producer gas may vary, but can contain about 15%-20% hydrogen, 20%-25% carbon monoxide, with the remainder a mixture of nitrogen, hydrocarbons and other organic materials.
- By exposing the porous char to such a temperature range and a mixture of steam and air, the porous char may be transformed into a relatively high density nanostructured material having the desired porosity. Typically, approximately 1 pound of the high density nanostructured material can be generated from the 4 pounds of the porous char. The exposure of the porous char to such high temperature, in addition to enlarging and generating pores of various nanoscale sizes, can provide the resulting nanostructured adsorption material with internal surface areas ranging from at least approximately 1000 m2/g to approximately 3000 m2/g, and higher.
- The resulting nanostructured material, similar to
nanostructured adsorption material 21 shown inFIGS. 2A-B , may be used in connection with theporous matrix 20 of the present invention. It should be noted that the process of enlarging the pores structure to specific nanoscale ranges, along with the removal of impurities within the porous char can impart special properties to the nanostructured material. In particular, such a process can impart the nanostructured material with adsorption properties necessary for removal of particulates and contaminants. - In addition to the size of the nanoscale pores, the ability of nanostructured material to adsorb particulates and contaminant molecules can also be dependent upon the structure of the nanoscale pores, the total surface area, the carbon particle size, and the void space between carbon particles. Specifically, as the nanostructured adsorption material, such as
item 21 inFIGS. 2A and 2B , essentially comprisesnanocarbon particles 26, thespaces 27 between these nanocarbon particles must be sufficiently small, i.e., nanoscale in size and smaller than the molecules of the fluid, so as to facilitate the fluid going through thepores 23 within thenanoadsorption material 21 and not through spaces around thepores 23. Likewise, should the carbon particles be larger than nanoscale size, such large carbon particles may block, partially block, and/or create interference with the flow of the fluid into thepores 23, thus allowing fluid to flow away from thepores 23. As a result, particulates and/or contaminants within the fluid flow may escape entrapment within thepores 23. - It should be appreciated that since one
surface 25 of theporous matrix 20 is substantially impermeable to fluid, theporous matrix 20 of the present invention does not have flow-through properties similar to commercially available filters. Rather, fluid flowing against or across thecontact surface 24 will enter and exit along thecontact surface 24. Specifically, fluid flowing against or across thecontact surface 24 into thenanostructured adsorption material 21 cannot thereafter exit throughsurface 25. In the presence of theimpermeable surface 25, the fluid directed into one opening of apore 23 adjacent theimpermeable surface 25 may subsequently be allowed to flow out another opening ofpore 23 not blocked by theimpermeable surface 25, as illustrated by the arrows inFIGS. 2A and 2B , and eventually make its way out through thecontact surface 24.Impermeable surface 25, in one embodiment of the present invention, may be generated by applying a layer of a substantially fluid impermeable material to one surface of theporous matrix 20. - The
porous matrix 20 may further, in accordance with an embodiment of the present invention, be impregnated with, for instance, silver or silver compound(s) so as to minimize microbial growth within theporous matrix 20. In particular, thenanostructured adsorption material 21 may be treated with a silver compound in the presence of acid or alkaline materials, depending on the silver compound used, so that the silver compound can be substantially evenly distributed against internal surfaces ofpores 23. Since this process can generate undesirable materials during the chemical reactions, such materials can be removed, in one embodiment, by leaching. The process employed herein can enhance the properties of theporous matrix 20. In addition to removal of particulates and contaminants, the presence of the silver compound, as noted, can minimize microbial growth within theporous matrix 20. Furthermore, it should be noted that the silver content provided within theporous matrix 20 using the process described herein may be at a level far below the permissible limits of silver in drinking water. In an embodiment, the silver content may be approximately 1 percent by weight. Additionally, the process employed herein can minimize the leaching of the silver content from within theporous matrix 20. In this manner, the presence of the silver compound within theporous matrix 20 does not act to elevate the level of silver above permissible limits. - With reference now to
FIGS. 3A-B , there is illustrated asystem 30 for purification of fluid by removing contaminants, such as microorganisms, organic, inorganic and particulate matter from the fluid. Thesystem 30, in one embodiment, may include areceptacle 31, similar to that ofsystem 10 shown inFIG. 1 . Thereceptacle 31 may include achamber 32 for accommodating a volume of fluid, and anopening 33 through which a volume of fluid may be introduced into thechamber 32. Acover 34 may be provided across theopening 33 to prevent spillage of fluid from within thechamber 32. - The
system 30 may also include aporous matrix 35 positioned within thechamber 32 for the removal of contaminants from the fluid. Theporous matrix 35, in accordance with one embodiment of the present invention, may be substantially similar to theporous matrix 20 ofFIGS. 2A-B , and may be used to retain or trap particulates and/or contaminants in the fluid. Theporous matrix 35, as shown inFIG. 3B , and used in connection withsystem 30, may be embedded withinchamber walls 36, so thatcontact surface 37 may be exposed to the fluid within thechamber 32, while substantiallyimpermeable surface 38 may be positioned againstchamber walls 36. In one embodiment, theporous matrix 35 may be embedded substantially circumferentially aboutchamber walls 36. Although illustrated as extending partially upwalls 36, should it be desired,porous matrix 35 may be permitted to extend substantially along the length ofwalls 36. To embed theporous matrix 35 within thewalls 36, means known in the art may be employed, for instance, co-extrusion of theporous matrix 35 along with thematerial comprising receptacle 31. In one embodiment of the present invention,porous matrix 35 may be provided with a thickness ranging from about 0.20 mm to about 0.30 mm. - In an alternate embodiment, instead of being embedded within the
walls 36 of thechamber 32, theporous matrix 35, made from a nanostructured adsorption material, may be applied directly onto thewalls 36. In one embodiment, the porous matrix may be coated ontowalls 36 as a thin film or layer. Alternatively, theporous matrix 35 may be designed as a sheet of material that can be adhered to thewalls 36 ofchamber 32. Regardless of the adherence material used, such material should be one that is non degradable in the presence of fluid. In either embodiment, the thin film or sheet ofporous matrix 35 may be designed so that it is sufficiently flexible and pliable for removal or insertion acrossopening 33. - Looking now to
FIGS. 4A and 4B , there is illustrated asystem 40 for purification of fluid by removing contaminants, such as microorganisms, organic, inorganic and particulate matter from the fluid, similar to the systems disclosed above. Thesystem 40, in one embodiment, may include areceptacle 41 having achamber 42 for accommodating a volume of fluid, and anopening 43 through which a volume of fluid may be introduced into thechamber 42. Acover 44 may be provided across theopening 43 to prevent spillage of fluid from within thechamber 42. - The
system 40 may also include aporous matrix 45 positioned within thechamber 42 for the removal of contaminants from the fluid. Theporous matrix 45, being substantially similarly to the previous porous matrices, acts to retain or trap therein contaminants from the fluid. As illustrated inFIGS. 4A and 4B , theporous matrix 45, made from a nanostructured adsorption material, may be designed as a substantiallycylindrical tube 47 having acontact surface 471, and an opposingimpermeable surface 472. Theporous matrix 45, as shown inFIG. 4A , may be positioned away from walls 46 ofchamber 42. In one embodiment, as illustrated from the perspective ofFIG. 4B ,porous matrix 45 may be positioned substantially concentrically to the walls 46, and may be designed to have a diameter that permits its removal from or placement within thechamber 42 throughopening 43. In order to maintainporous matrix 45 substantially concentric to the walls 46, a base (not shown) may be provided within whichporous matrix 45 may be positioned. Alternatively,porous matrix 45 may be permitted to float freely within thechamber 42. - In
FIG. 5 , there is illustrated anothersystem 50 for purification of a fluid by removing contaminants, such as microorganisms, organic, inorganic and particulate matter from the fluid, in accordance with one embodiment of the present invention. Thesystem 50, similar to the previously disclosed systems, may include areceptacle 51 having achamber 52 for accommodating a volume of fluid, and an opening 53 through which a volume of fluid may be introduced into thechamber 52. Acover 54 may be provided across the opening 53 to prevent spillage of fluid from within thechamber 52. - The
system 50 may also include aporous matrix 55 positioned within thechamber 52 for retaining, trapping, and thus removal of contaminants from the fluid. Theporous matrix 55, made from a nanostructured adsorption material, and in accordance with this particular embodiment of the present invention, may be provided as a loose mass of macro particles 56 that can freely move within the fluid inchamber 52. Each of the particles 56 may include a contact surface 561 and an impermeable core (not shown), so that fluid may be prevented from flowing through the particles 56. The particles 56, in one embodiment, may be uniform in size and shape, or as illustrated, vary in size and shape. It should be appreciated that the particles 56 may be of a size and shape that would facilitate their removal from or placement within thechamber 52 through opening 53 for replacement purposes. - In another embodiment, referring now to
FIG. 6 , asystem 60 is provided for purification of fluid by removing contaminants, such as microorganisms, organic, inorganic and particulate matter from the fluid. Thesystem 60, as with the previously disclosed systems, may include a receptacle 61 having achamber 62 for accommodating a volume of fluid, and anopening 63 through which a volume of fluid may be introduced into thechamber 62. Acover 64 may be provided across theopening 63 to prevent spillage of fluid from within thechamber 62. - The
system 60 may also include aporous matrix 65, made from a nanostructured adsorption material, that is positioned within thechamber 52 for retaining, trapping, and thus removal of contaminants from the fluid. Theporous matrix 65, in accordance with one embodiment of the present invention, may be placed circumferentially aboutwalls 66 at anend 67 of thechamber 62 opposite theopening 63. In addition,porous matrix 65 may be designed to be sufficiently flexible and pliable to permit its removal from and placement within thechamber 62 throughopening 63. - In an alternate embodiment, receptacle 61 may be provided with a
removable end 67 about whichporous matrix 65 may be circumferentially situated. In this manner, should theporous matrix 65 needs to be exchanged, theend 67 may be removed from receptacle 61 and disposed along withmatrix 65, and anew end 67 with newporous matrix 65 may be reattached to receptacle 61. To permit removal from the receptacle 61, theend 67 and the receptacle 61 may be provided with threaded engagement. Alternatively, other engagement mechanisms known in the art, for example, snap-fit etc., may be used, so long as such engagement can prevent leakage of fluid from within thechamber 62, while permitting easy removal ofend 67 from the receptacle 61. - Referring now to
FIG. 7 , the system of the present invention may be used to purify fluid by removing particulates and/or contaminants from the fluid, such as water, when the levels of particulates and/or contaminants exceed the prescribed limits for fluid that is intended for human consumption. The limits of contaminants in the drinking fluids may be prescribed by the regulators. In operation, fluid 71 that may include particulates and/or contaminants may be initially be introduced into the chamber ofreceptacle 72. Once introduced within thereceptacle 72, the fluid along with the molecules of contaminants therein, when come into contact with the porous matrix having the nanostructured adsorption material (e.g., flowing against or across the contact surface of the porous matrix), may be directed into the pores of the nanostructured adsorption material, wherein the molecules of contaminants may be trapped. It should be noted that the movement of fluid within the receptacle caused by or due to, for instance, shaking or moving of the receptacle should be sufficient to direct the flow of contaminants into the pores. If the situation is such that there is no movement of fluid within the receptacle, the contaminants may still be removed by slow molecular displacement or diffusion of molecules into the porous matrix within the receptacle. - Since the phenomenon occurs at a molecular level, the particulates and/or contaminants typically cannot be released from the pores within which they are trapped without enormous pressure or the application of heat at elevated levels. As the particulates and/or contaminants enter and become trapped within the pores, the weight of nanostructured adsorption material can increase to a measurable difference. Such an increase can be detected and displayed, for example, by a sensor, to indicate, for instance, the levels of contaminants removed from the fluid.
- Accordingly, still referring to
FIG. 7 , asensor 73 may be coupled to thereceptacle 72, such that thesensor 73 may be in communication with a porous matrix within the receptacle in order to display the levels of contaminants removed from the fluid.Sensor 73 can be any sensor which can detect a pressure, weight or heat differential between a porous matrix at time to and the same porous matrix at time tn, subsequent to exposure of the porous matrix to the fluid. In one embodiment, thesensor 73 may include pressure detector sufficiently thin (e.g., thin layer wired mesh or sheet), so as to be capable of being embedded within the nanostructured adsorption material of the porous matrix, and a display in communication with the detector. The pressure detector can act to transform the pressure differential between to and tn into electrical signals that can subsequently be process and shown on the display as the amount of particulates or contaminants in the porous matrix or the amount of contaminant removed. - The
sensor 73 may alternatively employ a weight sensor. It is noted that if at to the weight of the porous matrix is x milligram, then at tn, for instance, 15 seconds, when the nanostructured material of the porous matrix has had a chance to adsorb the particulates and/or contaminants, the weight of nanostructured adsorption material will be x+y, with y being the weight of contaminants that has been removed from the fluid. The weight increase due to the adsorption of the contaminants can be transformed to electrical signals, which can subsequently be displayed as information on a scale in terms of percentage of contaminants removed from the fluid. - The
sensor 73 may also employ a heat sensor. If, for instance, at to the temperature of the porous matrix is x degrees, then at tn, for instance, 15 seconds, when the nanostructured material of the porous matrix has had a chance to adsorb the particulates and/or contaminants, the heat generated in the nanostructured adsorption material will be x+y, with y being the temperature increase due to the adsorption of contaminants in the nanostructured material. This temperature increase can be transformed to electrical signals, which can subsequently be displayed as information on a scale in terms of percentage of contaminants removed from the fluid. - Whether using the pressure, weight and/or heat detector, when the nanostructured adsorption material approaches about 90% its capacity level for trapping particulates and/or contaminants, the
sensor 73, in one embodiment, can be designed to warn the user, for instance, by audio, visual, or other applicable indicators, that the porous matrix needs replacing or that the receptacle can no longer be used, if the receptacle is designed to be a disposable system. - The system of the present invention, accordingly, may be refilled over and over again with fluid to be treated. The system may be used successively to generate purified fluid meeting standards or limits prescribed for human consumption, until the nanostructured adsorption material of the porous matrix approaches its exhaustive capacity for trapping and retaining particles therein, i.e., having entrapped and retained therein particulates and/or contaminants at about 90% of its capacity.
- While the invention has been described in connection with the specific embodiments thereof, it will be understood that it is capable of further modification. Furthermore, this application is intended to cover any variations, uses, or adaptations of the invention, including such departures from the present disclosure as come within known or customary practice in the art to which the invention pertains, and as fall within the scope of the appended claims.
Claims (10)
1. A system for purification of fluid, the system comprising:
a receptacle;
a chamber situated within the receptacle and into which a volume of fluid to be treated may be placed; and
a porous matrix, positioned within the chamber, having a plurality of nanoscaled pores dispersed therein, such that fluid having particulates and/or contaminants flowing across one surface of the matrix flows back out along the same surface of the matrix substantially without the particulates and contaminants.
2. (canceled)
3. A system as set forth in claim 1 , wherein the plurality of nanoscaled pores within the porous matrix have sizes ranging from about 1 nm to about 100 nm.
4. A system as set forth in claim 1 , wherein the plurality of nanoscaled pores are arranged in distinct layers according to range of size.
5. A system as set forth in claim 1 , wherein the porous matrix is impregnated with silver or a silver compound to minimize microbial growth within the porous matrix.
6. A system as set forth in claim 5 , wherein the silver or silver compound is distributed against internal surfaces of the pores.
7-11. (canceled)
12. A system as set forth in claim 1 , wherein porous matrix is circumferentially positioned about the bottom end of the chamber.
13. A system as set forth in claim 1 , wherein the bottom end of the chamber is removable from the receptacle to permit replacement of the bottom end with a new porous matrix.
14-26. (canceled)
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US11/938,049 US20080251443A1 (en) | 2004-09-23 | 2007-11-09 | Systems having nanostructured adsorption material and methods for purification of fluid |
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US11/938,049 US20080251443A1 (en) | 2004-09-23 | 2007-11-09 | Systems having nanostructured adsorption material and methods for purification of fluid |
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US8926840B2 (en) | 2008-03-18 | 2015-01-06 | Rubbermaid Incorporated | Drinking container and filter assembly |
US9656191B2 (en) | 2008-03-18 | 2017-05-23 | Rubbermaid Incorporated | Drinking container and filter assembly |
US11825974B1 (en) * | 2020-03-01 | 2023-11-28 | Michael O. Murphy | Expandable strainer insert for bottles |
Also Published As
Publication number | Publication date |
---|---|
CA2581407A1 (en) | 2006-04-06 |
WO2006036191A2 (en) | 2006-04-06 |
US20060060530A1 (en) | 2006-03-23 |
CN101060900A (en) | 2007-10-24 |
WO2006036191A3 (en) | 2006-10-05 |
US7297281B2 (en) | 2007-11-20 |
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