[go: up one dir, main page]

WO2003051407A1 - Appareil et procedes pour distribuer un gaz - Google Patents

Appareil et procedes pour distribuer un gaz Download PDF

Info

Publication number
WO2003051407A1
WO2003051407A1 PCT/US2002/040302 US0240302W WO03051407A1 WO 2003051407 A1 WO2003051407 A1 WO 2003051407A1 US 0240302 W US0240302 W US 0240302W WO 03051407 A1 WO03051407 A1 WO 03051407A1
Authority
WO
WIPO (PCT)
Prior art keywords
vessel
gas
sachet
reactant
kit
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US2002/040302
Other languages
English (en)
Inventor
Richard A. Hamilton
John J. Warner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Selective Micro Technologies LLC
Original Assignee
Selective Micro Technologies LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Selective Micro Technologies LLC filed Critical Selective Micro Technologies LLC
Priority to AU2002357279A priority Critical patent/AU2002357279A1/en
Publication of WO2003051407A1 publication Critical patent/WO2003051407A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
    • A61L2/20—Gaseous substances, e.g. vapours
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00—Disinfection, sterilisation or deodorisation of air
    • A61L9/015—Disinfection, sterilisation or deodorisation of air using gaseous or vaporous substances, e.g. ozone
    • 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
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
    • C02F1/763—Devices for the addition of such compounds in gaseous form

Definitions

  • the present invention relates generally to apparatus and methods for delivery of gas, and more specifically, to apparatus and methods for initiating gas generation and controlling the amount, rate and duration of gas delivery.
  • gas for retarding controlling, killing and preventing microbiological contamination e.g., bacterial, fungi, viruses, mold spores, algae, and protozoa
  • microbiological contamination e.g., bacterial, fungi, viruses, mold spores, algae, and protozoa
  • gases include, but are not limited to, chlorine dioxide, sulfur dioxide, nitrogen dioxide, nitric oxide, carbon dioxide, hydrogen sulfide, hydrocyanic acid, and dichlorine monoxide.
  • chlorine dioxide has been found to be useful as a disinfectant antiseptic and sanitizer. It is used, e.g., to disinfect drinking water and various water supplies.
  • chlorine dioxide finds use as a bleaching agent for flour, fats, and textiles.
  • Chlorine dioxide also has shown great utility as an antiseptic for treating metal and plastic surfaces, as well as other substrates such as countertops, meat processing and packaging equipment, and dental and medical instruments and devices.
  • One disadvantage of the prior art methods for generating chlorine dioxide generally is that unsatisfactory levels of by-products or reactants remain as a residue. For example, in the case of chlorine dioxide gas, the byproduct chlorite leaves residues on food handling equipment and medical and dental surfaces.
  • the present invention includes a unique delivery system that controls the rate and efficiency of gas-producing reactions. Moreover, by using discreet amounts of reactant contained with a defined reaction volume, the skilled practitioner can fabricate a gas delivery apparatus that is compact, cost-effective, and safe. Furthermore, the present invention can be used for a variety of applications, including delivery of gas to air or water, for a variety of purposes including disinfection, deodorization, bleaching and sanitization.
  • the present invention features an apparatus for delivery of a gas that generally includes a vessel defining a reaction volume, and a reactant disposed within the vessel that generates a gas in the presence of an initiating agent.
  • the vessel includes a sachet layer disposed about an aperture defined by the vessel, and a puncturable surface.
  • the reactant includes an aqueous soluble acid and an aqueous soluble chlorite.
  • the sachet layer comprises a hydrophobic material.
  • the sachet layer comprises a water vapor selective film.
  • Apparatus of the invention can further include an envelope layer disposed about the aperture and disposed adjacent to the sachet layer.
  • the sachet layer is constructed from a hydrophilic material and the envelope layer is constructed from a hydrophobic material.
  • the apparatus can include a sachet disposed within the vessel, wherein the reactant is disposed within the sachet.
  • Such apparatus can further include a second reactant disposed outside of the sachet and within the vessel.
  • the puncturable surface can be constructed from a retractable material or a frangible material.
  • the apparatus further includes a second vessel formed to engage the vessel and to provide a compound.
  • the compound can include a second reactant and/or an initiating agent.
  • the second vessel can be a needle.
  • the second vessel can be formed to couple with the vessel and further define the reaction volume.
  • the second vessel can include a male member that is formed to slidably engage the vessel upon actuation of the male member.
  • the second vessel and the vessel can define complementary surfaces for a snap fit upon actuation of the male member.
  • the second vessel and the vessel define complementary threads for threaded engagement.
  • the invention features a kit for delivery of a gas.
  • the kit generally includes a first vessel defining a reaction volume, the first vessel including a sachet layer disposed about an aperture defined by the vessel, and a puncturable surface.
  • the kit also includes a reactant disposed within the first vessel that generates a gas in the presence of an initiating agent and a second vessel selectively engageable with the first vessel and formed to provide a compound.
  • the reactant includes an aqueous soluble acid and an aqueous soluble chlorite.
  • the sachet layer comprises a hydrophobic material.
  • the sachet layer comprises a water vapor selective film.
  • the vessel can further include an envelope layer disposed about the aperture and disposed adjacent to the sachet layer.
  • the sachet layer in constructed from a hydrophilic material and the envelope layer is constructed from a hydrophobic material.
  • the apparatus can include a sachet disposed within the vessel, wherein the reactant is disposed within the sachet.
  • Such apparatus can further include a second reactant disposed outside of the sachet and within the vessel.
  • the puncturable surface can be constructed from a retractable material or a frangible material.
  • the kit further includes a second vessel formed to engage the vessel and to provide a compound.
  • the compound can include a second reactant and/or an initiating agent.
  • the second vessel can be a needle.
  • the second vessel can be formed to couple with the vessel and further define the reaction volume.
  • the second vessel can include a male member that is formed to slidably engage the vessel upon actuation of the male member.
  • the second vessel and the vessel can define complementary surfaces for a snap fit upon actuation of the male member.
  • the second vessel and the vessel define complementary threads for threaded engagement.
  • the present invention features a method of delivering a gas.
  • the method includes the step of providing an apparatus for delivery of a gas including a vessel defining a reaction volume.
  • the vessel generally includes a sachet layer disposed about an aperture defined by the vessel, and a puncturable surface.
  • Reactant is disposed within the vessel that generates a gas in the presence of an initiating agent.
  • This embodiment further includes the step of delivering an initiating agent to the vessel to initiate delivery of the gas.
  • the method features the further steps providing a second vessel formed to engage the vessel and deliver a compound (e.g. , initiating agent and/or reactant), and engaging the vessel and the second vessel to deliver the compound.
  • a compound e.g. , initiating agent and/or reactant
  • the present invention features a method of delivering a gas.
  • the method generally includes providing a vessel including an aperture defined by the vessel and a puncturable surface, disposing a reactant within the vessel that generates a gas in the presence of an initiating agent, and sealing a sachet layer about the aperture defined by the vessel to define a reaction volume.
  • Figure 1 illustrates an exemplary embodiment of an apparatus for delivery of a gas in accordance with the present invention.
  • Figures 2A and 2B illustrate further exemplary embodiments of apparatus for delivery of a gas that include second vessels that are formed for pressure fit and threaded engagement, respectively.
  • Figures 3 A and 3B further illustrate the embodiments depicted in Figures 2A and 2B, respectively, where the second vessel is engaged with the first vessel.
  • gas can be generated efficiently and safely.
  • the user may initiate gas generation by delivering reactant and/or initiating agent via the puncturable surface.
  • the reaction can be controlled by controlling the release of gas through the sachet layer.
  • the reactant Upon initiation, the reactant generates the gas that exits the apparatus through the sachet layer.
  • the gas delivery apparatus is compact, cost-effective and safe.
  • the present invention can be used for a variety of applications, including delivery of gas to air or water, and for a variety of purposes including disinfection, deodorization, decontamination, bleaching and sanitization.
  • One advantage to this approach is that at user demand, the user can initiate the reaction that generates the gas. Another advantage is that the reactants, which can be dangerous to handle directly, are isolated from contact with the user because the reactant is enclosed within the vessel until the reaction is initiated. Yet, another advantage is that the reactants and any by-products remain enclosed in the apparatus before, during and after the reaction is initiated.
  • Another advantage is that the apparatus of the present invention do not allow for the dilution of the reactant. Because the reactant remains concentrated within the reaction volume, less reactant is necessary to drive the reaction to completion, and the reaction is more efficient than it would be if the reactants were diluted. Furthermore, because the reaction is driven to completion, unreacted reactant is minimized or eliminated. The reactant concentration also minimizes unwanted by-products.
  • the apparatus is small and stable, and thus can be easily and economically shipped, stored, and administered. Still a further advantage is that the apparatus can be manipulated to allow for either rapid or slow delivery of gas, e.g. , by selection of sachet layer material, and optional envelope layer material. Another advantage is that the apparatus can be designed to deliver gas to either a gaseous environment, e.g., ambient air, or a liquid environment, e.g., water. Other advantages will be evident to the practitioner having ordinary skill in the art. In order to more clearly and concisely describe the subject matter of the claims, the following definitions are intended to provide guidance as to the meaning of specific terms used in the following written description, examples and appended claims.
  • the term "vessel” refers to a hollow receptacle defining a reaction volume.
  • the vessel defines an aperture, e.g., an opening positioned on the vessel.
  • the vessel generally includes a puncturable surface for the introduction of a compound (e.g. , initiating agent or reactant), and a sachet layer disposed about an aperture defined by the vessel.
  • Reactant refers to a reactant or a mixture of reactants that generate gas in the presence of an initiating agent. Such reactants include, but are not limited to metal chlorites (e.g., sodium chlorite), and acids (e.g., citric acid). The reactant or reactants can further include additives, such as activated hydrotalcite.
  • initiating agent refers to any agent that initiates the generation of gas from the reactant.
  • initiating agent includes, but is not limited to, gaseous or liquid water.
  • the initiating agent can enter the apparatus through the sachet layer and/or the initiating agent can be included within the apparatus, e.g., contained in a second vessel that is coupled with the first vessel.
  • “Puncturable surface” refers a surface that may be pierced or punctured when a force is applied to the surface. A puncturable surface may comprise material that retains a puncture hole where it was punctured.
  • a puncturable surface may comprise material that retracts or contracts to an unpierced (e.g., a closed) configuration after being punctured (e.g., by a needle).
  • a puncturable surface is a frangible surface that ruptures upon application of pressure, e.g. , by actuation of a second vessel against the puncturable surface, thereby allowing the second vessel to engage the first vessel.
  • Sachet layers refers to layers that allow exit of the gas from the apparatus through the sachet layer.
  • Sachet layers typically are constructed from a planar material, such as, but not limited to, a polymeric sheet or film.
  • Sachet layers include any of the layers described herein and in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002, and incorporated herein by reference.
  • sachet refers a closed receptacle for reactant.
  • the sachet is "closed” in the sense that the reactants are substantially retained within the sachet and the sachet volume is substantially sealed around its perimeter.
  • the sachets of the present invention also can include further materials, e.g. a sachet can comprise a barrier layer and a sachet layer sealed about the perimeters of the layers to define a closed receptacle for reactant.
  • a sachet is a rigid frame defining one or more openings and one or more layers, including at least one sachet layer, disposed about one or more openings to define a closed receptacle for reactant.
  • envelope layers are layers that allow exit of the gas from the apparatus through the envelope layer, and are disposed adjacent to at least one sachet layer such that the sachet layer is on the reaction volume side of envelope layer.
  • Envelope layers typically comprise a planar material such as a sheet or film, including, but not limited to, perforated films, non- perforated films and membranes. Further materials that can be used to construct envelope layers are described in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002. Relying upon the teaching disclosed herein and in pending United States Patent Application Serial No.
  • envelope means a closed receptacle wherein the envelope volume is sealed substantially about its perimeter, and contains at least one sachet and allows release of the gas from the envelope.
  • Impermeable layer refers to a layer that substantially prevents or hinders passage of initiating agent. As contemplated herein, the impermeable layer does not participate in the generation of gas in that it does not facilitate contact between initiating agent and reactant. Impermeable layers can be constructed from various materials, including polymeric material, glass, metal, metallized polymeric material and/or coated papers. As used herein, barrier layers are impermeable layers. Preferred materials for impermeable layers and barrier layers may be any of the materials described in greater detail throughout this application and in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002.
  • dry application for the purposes of this application means at least an application where the apparatus of the present invention is not immersed in water or any other liquid.
  • dry application for the purposes of the present invention means at least an application where the apparatus of the present invention is immersed in water, or other liquid, which can optionally include water.
  • a gas e.g., by acid activation
  • chlorine dioxide ClO 2
  • an acid such as citric acid
  • chlorine dioxide can be produced by the reduction of a chlorate, e.g. , sodium chlorate or potassium chlorate, in the presence of an acid, e.g. , oxalic acid.
  • a sulfite e.g., sodium bisulfite or potassium bisulfite
  • an acid e.g., fumaric acid and/or potassium bitartrate
  • a carbonate e.g., calcium carbonate with an acid, e.g., citric acid
  • an acid e.g., citric acid
  • nitrogen dioxide by the acid activation of a nitrite, e.g., sodium nitrite or potassium nitrite.
  • Alternative routes for generation of a gas e.g. , reduction of chlorates by sulfur dioxide (Mathieson Process) are well known in the art and can be utilized in accordance with the present invention.
  • the present invention relates to apparatus and methods for delivering biocidal- effective amounts of a gas such as chlorine dioxide and sulfur dioxide.
  • Chlorine dioxide gas may be released into a volume of water or other fluid to make a solution ofthe gas.
  • the apparatus and methods ofthe present invention achieve delivery of a desired amount of gas, at a desired rate of generation, at a desired release rate, over a desired time period. This is accomplished by disposing suitable reactants in a defined and confined reaction volume such that upon initiation, by the user, the reactants, initiating agent, products, and by-products are held within a desired concentration range.
  • the amount, rate and duration of delivery can be manipulated by, e.g., choice of sachet layers, envelope layers, reactant amount, reactant ratio, aperture size, aperture shape, aperture location, reaction volume, and sachets and envelopes disposed within the vessel. Such manipulations can be exercised by the artisan using only routine experimentation in view ofthe teachings disclosed herein, described in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002, together with knowledge in the art.
  • FIG. 1 illustrates a perspective view of an exemplary embodiment of an apparatus 10 for delivery of a gas constructed in accordance with the present invention.
  • apparatus 10 includes a vessel 20 that includes a sachet layer 50 disposed about aperture 30, and has a puncturable surface 40.
  • the sachet layer 50 is substantially sealed about the periphery ofthe aperture 30 such that aclosed reaction volume is defined within the vessel.
  • a reactant 60 is disposed inside the vessel 20 that generates a gas in the presence of an initiating agent.
  • the sachet layer 50 allows exit ofthe gas through the sachet layer.
  • the apparatus 10 may optionally contain a sachet 90 which contains a second reactant 92.
  • Apparatus 10 is particularly useful for user-initiated reaction, generation and delivery of a gas.
  • puncturable surface 40 can be utilized to provide initiating agent 80 to initiate reaction generation with reactant 60 with a syringe 75. After the initiating agent is introduced into the vessel, the apparatus generates gas in a controlled manner. In one embodiment, the apparatus provides a predetermined concentration of gas, which is released through the sachet layer from the reaction volume in a controlled and/or sustained concentration and/or rate.
  • Vessels ofthe invention may be fabricated from various materials and the materials may be, for example, impermeable layer materials or barrier layer materials. Suitable materials for impermeable layers and barrier layers may be any ofthe materials described in greater detail in this patent application and in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002.
  • the barrier layer materials may have a rigid or semirigid structure. Suitable materials that may be used to fabricate vessels include, e.g., metals, polymeric materials, metallized polymeric materials, and glass. The vessel can be shaped and sized to suit a particular gas delivery application.
  • the vessel may be shaped so that it can be inserted into another device, e.g., a cartridge, a humidifier, a vaporizer, a pipe or other machine.
  • the vessel also can be formed into a shape such that the apparatus is easily inserted into or removed from various environments.
  • the user may initiate gas generation in a cylindrical vessel adapted to fit snugly with the inner diameter of a pipe, cartridge, or pipe system for transporting fluid.
  • a cylindrical vessel size may be adapted to move through the inner diameter of a pipe system along with the fluid traveling through the pipe.
  • Suitable vessel geometries include cylindrical, oval, spherical, rectangular, and pyramid. Vessels can be formed into various geometries by various manufacturing methods, including, e.g., the manufacturing methods describing forming barrier layer material into various geometries as described in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002.
  • the vessel 20 may be a cylinder having a first end 21 A and a second end 2 IB.
  • Vessel wall 22 preferably has a thickness suited to the materials of construction, the reactant and/or the space into which vessel 20 will be inserted.
  • the vessel height 24 and the vessel diameter 26 also may be dimensioned to suit a particular application.
  • the aperture ofthe vessels ofthe present invention may be sized and/or shaped to deliver a quantity of gas suited to the intended application. Suitable aperture geometries include spheres, circles, ovals, triangles, rectangles, squares, and slits.
  • the vessel can define one or multiple apertures having similar or dissimilar shapes for the introduction of one or more compounds.
  • the size, shape, and/or location on vessel where the one or more apertures are disposed may be selected to control, e.g., limit or maximize, the quantity of gas released from the vessel.
  • Apertures can be excised from or otherwise defined in the vessel after the vessel is formed or, alternatively, apertures may be molded or formed into the vessel during its manufacture.
  • the vessel aperture is formed to include an edge about its perimeter for forming a seal with sachet layer and/or an envelope layer or other additional layers.
  • the sachet layers ofthe present invention can be chosen to control the diffusion ofthe reactants out ofthe sachet, control the rate of gas release from the reaction volume and control the initiation ofthe reactants.
  • a hydrophilic sachet layer can increase the rate at which water and/or water vapor diffuses into the sachet; and the pore size and thickness ofthe sachet layer can effect the passage of water, reactants and gas through the sachet layer.
  • the sachet layers include materials that are durable and stable during construction, storage and reaction, and are capable of fusing upon the application of heat or ultrasonic energy for construction purposes, e.g., so that a sachet layer can be fused about its perimeter to an aperture to construct a vessel, or another sachet layer to construct a sachet.
  • the sachet layers ofthe present invention can be constructed of various materials, including polymeric material or coated papers, selective transmission films, woven material, non-woven membrane, membranes including extruded membranes, or perforated films.
  • composite layers including, but not limited to, starch/polymer composite layers.
  • the sachet layer ofthe present invention can be constructed from material that is hydrophobic and/or hydrophilic.
  • the sachet layer can be constructed from a material having one or more hydrophilic zones and one or more hydrophobic zones. These zones can be created, e.g., by printing a functional chemical group or polymer onto a surface ofthe sachet that is hydrophilic, hydrophobic, or charged to create one or more hydrophilic, hydrophobic, or charged zones.
  • Yet another alternative embodiment uses a material to construct the sachet layer that has a first surface that is hydrophilic and a second surface that is hydrophobic, formed, e.g., by coextrusion or coating.
  • the sachet includes a material that is water vapor selective.
  • water vapor selective refers to a material that selectively allows permeation of water vapor and substantially impedes permeation of liquid water. More preferably, the material excludes permeation of liquid water.
  • the water vapor selective material is hydrophobic.
  • the skilled practitioner typically refers to water vapor selective material as water impermeable, although water vapor can permeate the layer, and refers to materials that allow permeation of liquid water as water permeable.
  • Suitable water vapor selective materials can be made from a variety of materials including, but not limited to, polytetrafluoroethylene (PTFE), polypropylene (PP), polyethylene (PE), and fluorinated ethylene propylene (FEP).
  • PTFE polytetrafluoroethylene
  • PP polypropylene
  • PE polyethylene
  • FEP fluorinated ethylene propylene
  • Water vapor selective material is particularly advantageous because it substantially impedes or excludes the diffusion of water soluble species, such as water soluble reactants, additives, and reaction by-products, out ofthe apparatus.
  • Membranes that allow liquid water permeation allow soluble species such as soluble reactants to permeate the apparatus and enter the environment.
  • Prior attempts have been made to ameliorate or avoid escape of soluble species by using insoluble reactants or by binding or otherwise disposing the soluble species on insoluble materials such as clays and molecular sieves. This is not advantageous because it introduces additional steps and/or expense to the preparation ofthe apparatus.
  • the water vapor selective materials ofthe present invention are advantageous because they impede or preclude the permeation ofthe soluble reactants, additives, and by-products, thus removing the need to include or generate insoluble reactants, by-products and/or additives.
  • water vapor selective materials are advantageous because their use eliminates the need to use any further layers, e.g., further sachet and/or envelope layers, to retain soluble species in the apparatus, which introduces additional steps and expense in the construction ofthe apparatus.
  • the water vapor selective material has a thickness between about 5 microns and about 400 microns thick, a pore size between about 0.05 microns and about 10 microns, and a water intrusion pressure between about 30 millibars and about 4,000 millibars.
  • the water vapor selective material is adhered to or otherwise supported by a support layer that allows liquid water to permeate the support layer, and the overall thickness of both the water vapor selective layer and the support layer is between about 1 mil and 20 mils.
  • water vapor selective materials having a thickness between about 15 microns and about 200 microns thick, a pore size between about 0.25 microns and about 5 microns, and a water intrusion pressure between about 100 millibars and about 1,500 millibars.
  • this layer has a water permeable support layer such that the total thickness of both layers is between about 2 mils and about 10 mils.
  • water vapor selective materials having a thickness between about 20 microns and about 100 microns thick, a pore size between about 1 micron and about 3 microns, and a water intrusion pressure between about 200 millibars and about 750 millibars.
  • this layer has a water permeable support layer such that the total thickness of both layers is between about 3 mils and about 8 mils.
  • a thinner layer is preferred because the thinner the layer, the more rapidly water vapor can diffuse into the apparatus and initiate the reaction, and the more rapidly gas can diffuse out ofthe apparatus.
  • a thicker material is preferred, such as between about 5 mils and about 20 mils.
  • pore size ofthe water vapor selective layer can be selected to produce the desired release at specific depths of water in which the apparatus will be used. A smaller pore size will correspond to deeper operation by increasing the amount of hydraulic water pressure that the membrane will experience while remaining impermeable to liquid water.
  • Water vapor selective layers suitable for use in constructing the apparatus ofthe present invention preferably have water vapor permeability of between about 2,000 g/m 2 /24hrs and about 150,000 g/m 2 /24hrs, as determined by JIS L 1099-1985 (Method B), "Testing Methods for Water Vapour Permeability of Clothes," from the Japanese Standards Association.
  • Water vapor selective layers preferably have a resistance to liquid water permeation of at least about 30 millibars as determined by ISO 811-1981 "Textile fabrics - Determination of resistance to water penetration - Hydrostatic pressure test" published by the International Organization for Standardization.
  • the water vapor selective layer or layers ofthe present invention can include a support layer to increase the strength ofthe layer, and/or to increase its ability to bond to the other materials used to construct the apparatus.
  • the support layer preferably allows diffusion or passage of initiating agent to the surface ofthe water vapor selective layer.
  • the support layer can be spun, perforated or have large pores that allow passage of liquid water and vapor to the surface ofthe water vapor selective layer.
  • the support layer can be affixed to the water vapor selective layer by any means, for example, lamination, casting, co-extrusion, and/or adhesive layers.
  • the apparatus is constructed so that the water vapor selective layer faces the interior ofthe vessel.
  • the support layer itself can be hydrophilic and/or hydrophobic.
  • Suitable support layers include, but are not limited to, polyethylene, polypropylene, nylon, acrylic, fiberglass, and polyester in the form of woven, non- woven, and mesh layers. Preferably, the support layer thickness is between about 1 mil and 20 mils.
  • Suitable water vapor selective materials include the 0.60 pore size, hydrophobic, polypropylene (PP) membrane having a thickness between about 250 microns and about 300 microns sold under the designation 060P1 by Cuno Incorporated (Meriden, CT).
  • hydrophobic polyethylene material sold under the trade designation DOHP by Millipore (Bedford, MA).
  • DOHP 0.65 micron pore size, hydrophobic polyethylene material sold under the trade designation DOHP by Millipore (Bedford, MA).
  • Another water vapor selective material suitable for use in a rapid release apparatus includes a 1.75 mil thick, hydrophobic polytetrafluoroethylene (PTFE) layer thermally bonded to a 5 mil thick, hydrophobic polyethylene (PE) support layer sold under the trade designation BHA-TEX® by BHA Technologies (Kansas City, MO). Its resistance to liquid water permeation is at least about 500 millibar.
  • PTFE polytetrafluoroethylene
  • PE polyethylene
  • a protective seal made from impermeable materials can be placed over the sachet layer to prevent initiation until the user removes the protective seal.
  • the user may remove the protective seal by, e.g., peeling the protective seal off of the sachet layer prior to or after initiating the reaction.
  • the reactant contained within the vessel, and optionally, a second vessel as described below can be in solid or solubilized form, e.g., aqueous soluble reactant can be solubilized in water.
  • Reactant can be maintained loose within the vessel and/or in one more sachets disposed in the vessel. For example, citric acid can be maintained in a sachet disposed in a vessel and sodium chlorite can be maintained loose in the vessel exterior to the sachet.
  • Additives can be included in the reactant as well.
  • the puncturable surface ofthe present invention is utilized to deliver a compound to the vessel, typically, a reactant and/or initiating agent that will commence reaction.
  • the puncturable surface is constructed to suit the means of delivery ofthe compound.
  • the puncturable surface can be retractable such that the compound can be injected and the integrity ofthe vessel maintained after removal ofthe injection device.
  • the puncturable surface is frangible such that it is ruptured upon application of pressure. This embodiment can be used when engaging or coupling a second vessel to the first vessel, so that the barrier to delivery ofthe compound in the second vessel is removed by application of pressure.
  • the puncturable surface can be a removable layer which can be removed or peeled aside allowing the administration of a second compound or engagement of a second vessel.
  • the puncturable surface can be removed and replaced after delivery of a compound, e.g., by threaded engagement, pressure fit, or snap fit with the vessel.
  • the puncturable surface portion of vessel is constructed from impermeable or barrier layer material to prevent premature initiation.
  • the puncturable surface can be manufactured from, e.g., a polymer or a rubber material. Suitable puncturable surface materials include, for example, polyethylene, polypropylene, polystyrene, polyvinyledene chloride, polyvinyl chloride, latex rubber and/or other polymers.
  • a protective seal can be placed over the puncturable surface. The protective seal may protect the puncturable surface from inadvertently being pierced. The user removes the protective seal, for example, by peeling it from the vessel, prior to initiating the reaction by, e.g., pushing the second vessel into the puncturable surface.
  • the user employs a needle 70 (e.g., a hypodermic needle), to pierce the puncturable surface 40, then plunges the syringe 75 to release a compound 80 (e.g., initiating agent and/or additional reactants), into vessel 20.
  • a compound 80 e.g., initiating agent and/or additional reactants
  • the user can initiate a gas generating reaction within the apparatus. Gas is then delivered to the atmosphere surrounding apparatus through the sachet layer in a controlled, safe, and efficient manner.
  • Figure 2A is a cross-sectional side view of another embodiment of an apparatus 110 for delivery of a gas constructed in accordance with the present invention.
  • apparatus 110 includes a vessel 120, which defines an aperture 130, and a puncturable surface 140.
  • a sachet layer 150 is disposed and substantially sealed about the aperture 130, and an optional envelope layer 190 is also disposed and substantially sealed about the aperture 130 adjacent the sachet layer 150.
  • a reactant 160 is disposed inside vessel 120.
  • the apparatus 110 also includes a second vessel 220 formed to couple or engage with vessel 120.
  • the second vessel 220 may include a second reactant 265 and the second vessel 220 may be adapted to deliver the second reactant 265 to vessel 120.
  • the first vessel 120 and the second vessel 220 are configured to engage in a pressure fit configuration as shown in Figure 3 A, by applying pressure to the vessels such that the second vessel punctures the first vessel at the puncturable surface.
  • the puncturable surface is a frangible layer that is ruptured by the first end 221 A ofthe second vessel 220.
  • the first vessel 120 and second vessel 220 define the reaction volume and the reactants 160, 265 are contacted. The reaction can then be initiated by initiating agent entering through the sachet layer and/or the initiating agent can be disposed in one ofthe vessels.
  • the puncturable surface is constructed from a frangible multi-layer plastic material, e.g., a weak layer of polyolefin positioned near the sealing surface that will fail under pressure.
  • frangible materials may also include brittle plastic or glass. Suitable frangible materials may be any ofthe frangible materials described herein or in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002.
  • An envelope layer can be included in apparatus ofthe invention to control or prevent the influx of water vapor into the vessel, while limiting the diffusion ofthe reactants to the surrounding fluid, be it gaseous or liquid.
  • the envelope layer also allows the gas to diffuse through it to the surrounding fluid from the apparatus.
  • initiating agent e.g., water vapor
  • the reactant remains concentrated and the pH ofthe reactive system is localized within the apparatus to optimize the conversion of reactant to gas.
  • intermediates and/or by-products ofthe reaction e.g., water, also can contribute to the efficiency and/or duration ofthe reaction by its affect on the equilibrium ofthe reactions.
  • the envelope layer preferably is constructed of a material that is durable and stable. Preferably, it also is capable of fusing to a like material upon the application of heat for construction purposes, e.g. , so that two pieces of such material can be fused about its perimeter to an aperture or form an envelope.
  • the envelope layer can be constructed of various materials, including polymeric material, such as perforated films, liquid water permeable films, membranes, and selective transmission films. Suitable envelope layer materials may be any ofthe envelope materials or envelope layer materials described in pending United States Patent Application Serial No. 10/225,769, filed August 22, 2002, incorporated by reference herein.
  • At least a portion ofthe second vessel can be dimensioned to fit within the first vessel, which itself can be formed to receive the second vessel.
  • the vessels can be formed to engage in a pressure fit (e.g. , as shown in Figures 2A and 3 A), a threaded fit (e.g., as shown in Figures 2B and 3B), a snap fit (not shown), or any known fitting configuration.
  • the vessels can be configured to have a tongue and groove fit or complementary threads that are fit by twisting or pushing the vessels together to force the tongue into the groove or force complementary threads into alignment. After the vessels are coupled, the vessels define the reaction volume, and the reactants and byproducts are substantially retained within the apparatus.
  • the second vessel may be made from a material having impermeable layers, and contains a compound, e.g., a reactant and/or initiating agent.
  • a sachet enclosing a second reactant and/or imtiating agent may be disposed within the second vessel.
  • the second vessel, or at least a portion ofthe second vessel is dimensioned to fit within the puncturable surface ofthe vessel.
  • the second vessel may be shaped to suit any particular application, and can have various geometries including cylindrical, oval, spherical, rectangular, and pyramid.
  • the second vessel also preferably has a wall thickness suited to the materials of construction, the reactant and/or the space where the vessel will be placed.
  • the second vessel wall 222 can be adapted to pierce the puncturable surface 140 of vessel 120 by virtue ofthe difference in wall heights 224A and 224B.
  • the wall can form a sharp end and have, e.g., a straight edge or a serrated edge.
  • the first end features a blunt edge.
  • the height ofthe second vessel wall is uniform.
  • Figure 3 A illustrates a method for delivering a gas 210 employing the apparatus 110, described above with reference to Figure 2A.
  • the user aligns the first end 221 A ofthe second vessel 220 with the puncturable surface 140 of vessel 120.
  • the second vessel 220 creates a hole inor ruptures the puncturable surface 140.
  • the second vessel 220 slides into vessel 120 and couples or engages with vessel 120.
  • the second vessel 220 slides axially into vessel 120.
  • the second vessel 220 is engaged with the first vessel 120 by a pressure fit.
  • the second vessel 220 may be adapted to deliver reactant 265 to vessel 120.
  • the second reactant 265 contained in the second vessel 220 contacts the reactant 160 contained in vessel 120, initiating the reaction to generate the gas 200.
  • the generated gas 200 exits apparatus 110 through sachet layer 150 and optional envelope layer, and gas 210 is delivered to the environment surrounding apparatus 110.
  • FIG. 2B is a cross-sectional side view of another embodiment of an apparatus 110 for delivery of a gas constructed in accordance with the present invention.
  • apparatus 110 includes the vessel 120, which defines an aperture 130, and a puncturable surface 140.
  • a sachet layer 150 is disposed about and substantially sealed to the aperture 130.
  • a reactant 160 is disposed insidethe vessel 120.
  • the apparatus 110 also includes a second vessel 220 formed to couple withthe vessel 120.
  • the second vessel may include a second reactant 265 and the second vessel 220 may be adapted to deliver the second reactant 265 to vessel 120.
  • the first vessel 120 is connected with the second vessel 220 in a threaded fit configuration, prior to the rupture ofthe puncturable surface. Optionally, however, they can be provided separately.
  • the first vessel is formed with the female threads 300 to fit with male threads 310 formed on the second vessel to couple the two vessels by a threaded fit.
  • the second vessel 220 engages the first vessel 120 by actuating the vessels to thread the second vessel into the first, such that puncturable surface 140 is ruptured delivering the reactant 265 contained in the second vessel, as shown in Figure 3B.
  • the second vessel first end 221 A is adapted to pierce the puncturable surface 140 of vessel 120.
  • the elements ofthe apparatus including the vessels, reactant, sachet layers, aperture, puncturable surface, etc., are as described herein.
  • the puncturable surface is constructed from a frangible multi-layer plastic material, e.g., a weak layer of polyolefin positioned near the sealing surface that will fail under applied pressure.
  • the apparatus can further include additional elements as discussed herein, such as an envelope layer adjacent the sachet layer and sealed about the aperture, a sachet, etc.
  • Figure 3B illustrates a method for delivering a gas 210 employing the apparatus 110, described above with reference to Figure 2B.
  • the user aligns the female threads of first vessel 120 and the male threads of second vessel 220 at the first end 221 A ofthe second vessel with the puncturable surface 140 of vessel 120.
  • the second vessel 220 creates a hole in the puncturable surface 140.
  • the second vessel 220 inserts into vessel 120 and couples with vessel 120.
  • the second vessel 220 twists axially into vessel 120.
  • the second vessel is engaged with the first vessel by a threaded fit.
  • the second vessel 220 may be adapted to deliver reactant 265 to vessel 120.
  • the second reactant 265 contained in the second vessel 220 contacts the reactant 160 contained in vessel 120, initiating the reaction to generate the gas 200.
  • the generated gas 200 exits apparatus 110 through sachet layer 150, and gas 210 is delivered to the environment surrounding apparatus 110.
  • the invention features a kit for delivery of a gas.
  • the kit generally includes a first vessel defining a reaction volume, the first vessel including a sachet layer disposed about an aperture defined by the vessel, and a puncturable surface.
  • the kit also includes a reactant disposed within the first vessel that generates a gas in the presence of an initiating agent, and a second vessel selectively engageable with the first vessel and formed to provide a compound.
  • the kit can comprise any ofthe apparatus as described above.
  • the kit optionally can contain initiating agent and/or reactant separately packaged for take up by a second vessel (e.g., a syringe), and delivery to the first vessel.
  • a second vessel e.g., a syringe
  • the kit can contain multiple first and second vessels, and the vessels and reactants contained therein can be of different sizes and quantities, so that a user can select appropriate vessels to deliver a desired amount of gas over a desired time period.
  • the present invention features a method of delivering a gas by providing an apparatus for delivery of a gas as described herein, and delivering an initiating agent to the vessel to initiate delivery of a gas.
  • the method can feature any ofthe steps discussed herein, for example, the method can include the further steps of providing a second vessel formed to engage a vessel ofthe invention and deliver a compound, and engaging the vessels to the deliver the compound.
  • chlorine dioxide can be used for: the disinfection of water, e.g., municipal water treatment; as a disinfectant for equipment used in the preparation of foods, beverages, fruits and vegetables; for sanitizing fruits and vegetables prior to packaging; for the cleaning and disinfection of medical, dental and food equipment; and for cleaning and disinfecting fluid tanks, fluid lines, and fluid dispensing equipment.
  • Chlorine dioxide has been shown to be an effective disinfectant at concentrations as low as 0.2 mg/L. Chlorine dioxide is a desirable replacement for chlorine, the traditional water treatment chemical, because it has been found to inactivate microbes at lower levels and over a wider pH range.
  • chlorine dioxide can be used to reduce or eliminate biofilms because it penetrates the cell wall of naturally occurring, colony-building microorganisms and disrupts the proteins necessary for reproduction. Moreover, chlorine dioxide does not produce chlorinate by-products, e.g., trihalomethanes. Furthermore, it has been found to be active against pathogens that are resistant to chlorine. It can be used as a slimicide for paper or pulp machines, for wastewater treatment, and for industrial water treatment, e.g., cooling or recycle streams. It can be used for odor control or as an aerial biocide and virucide. It can be used for the treatment of sulfides in the oil industry, for industrial cleaning, e.g., circuit board cleansing, and for paper or tallow bleaching.
  • Sulfur dioxide also has a variety of uses, such as a mold and fungus inhibitor for use in shipping and storing fruits and vegetables. Based on the teachings disclosed herein a practitioner of ordinary skill will appreciate the numerous other applications for which the present invention can be used and provides a heretofore-unmet need.
  • a predetermined concentration of gas may be supplied to, for example, a confined space.
  • the apparatus supplies the gas for a specific period of time.
  • a controlled initiation and release of gas into water to make an aqueous solution may be employed as a biocide fluid flowing through, for example, tanks or fluid lines, for example, in fluid dispensing equipment.
  • chlorine dioxide gas is dispensed at a predetermined concentration over a specific period of time, such that the user can disinfect a fluid line with chlorine dioxide. After a set time has passed, the user may clear or flush the fluid line of chlorine dioxide thereby taking advantage ofthe ability of chlorine dioxide gas to quickly "wash out" of fluid lines.
  • the present invention features a method of manufacturing an apparatus for delivery of a gas.
  • This method comprises the steps of: providing a vessel comprising an aperture defined by the vessel and a puncturable surface; disposing a reactant within the vessel that generates a gas in the presence of an initiating agent; and sealing a sachet layer about the aperture defined by the vessel to define a reaction volume.
  • This method can further include the provision and construction of any ofthe elements described herein. Further embodiments featuring methods of manufacturing apparatus have been described herein.

Landscapes

  • Health & Medical Sciences (AREA)
  • Epidemiology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

La présente invention concerne un appareil pour distribuer un gaz (10), tel que du dioxyde de carbone et/ou du dioxyde de chlore, ainsi que des procédés pour utiliser et produire cet appareil. Ledit appareil comprend une cuve (20) qui définit un volume réactionnel et qui comprend une couche sachet (50), placée autour d'une ouverture (30) définie par la cuve, ainsi qu'une surface (40) pouvant être perforée. La cuve contient un ou plusieurs réactifs (60) qui produisent un gaz en présence d'un agent d'amorçage, tel que de l'eau. L'appareil selon cette invention peut comprendre une seconde cuve (220) conçue pour venir en prise avec la surface pouvant être perforée afin de distribuer un agent d'amorçage et/ou un second réactif dans la cuve (20).
PCT/US2002/040302 2001-12-17 2002-12-17 Appareil et procedes pour distribuer un gaz Ceased WO2003051407A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2002357279A AU2002357279A1 (en) 2001-12-17 2002-12-17 Apparatus and methods for delivery of a gas

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US34142901P 2001-12-17 2001-12-17
US60/341,429 2001-12-17
US40520202P 2002-08-22 2002-08-22
US60/405,202 2002-08-22

Publications (1)

Publication Number Publication Date
WO2003051407A1 true WO2003051407A1 (fr) 2003-06-26

Family

ID=26992502

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2002/040302 Ceased WO2003051407A1 (fr) 2001-12-17 2002-12-17 Appareil et procedes pour distribuer un gaz

Country Status (2)

Country Link
AU (1) AU2002357279A1 (fr)
WO (1) WO2003051407A1 (fr)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7347994B2 (en) 2002-09-13 2008-03-25 Ica Trinova, Llc Method and composition for attracting arthropods by volatilizing an acid
EP1701747A4 (fr) * 2004-01-07 2009-05-27 Noxilizer Inc Systeme et dispositif de sterilisation
US8017074B2 (en) 2004-01-07 2011-09-13 Noxilizer, Inc. Sterilization system and device
US8425837B2 (en) 2009-02-23 2013-04-23 Noxilizer, Inc. Device and method for gas sterilization
US9382116B2 (en) 2013-01-10 2016-07-05 Ica Trinova, Llc Mixtures for producing chlorine dioxide gas in enclosures and methods of making the same
WO2017106685A1 (fr) * 2015-12-18 2017-06-22 Sabre Intellectual Property Holdings Llc Procédés d'extraction d'huiles et de graisses à partir d'une matière solide à l'aide de dioxyde de chlore
US10850981B2 (en) 2017-04-25 2020-12-01 Ica Trinova, Llc Methods of producing a gas at a variable rate
US20220126254A1 (en) * 2020-10-27 2022-04-28 Selective Micro Technologies, Llc Gas micro reactor utilizing membrane packaging
US11912568B2 (en) 2018-03-14 2024-02-27 Ica Trinova, Llc Methods of producing a gas at a controlled rate

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4411918A (en) * 1980-03-26 1983-10-25 Kontek - Tecnologie Della Conservazione - S.R.L. Apparatus for preserving food by generating preservative gas
US5705092A (en) * 1995-06-05 1998-01-06 Southwest Research Institute Multilayered biocidal film compositions

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4411918A (en) * 1980-03-26 1983-10-25 Kontek - Tecnologie Della Conservazione - S.R.L. Apparatus for preserving food by generating preservative gas
US5705092A (en) * 1995-06-05 1998-01-06 Southwest Research Institute Multilayered biocidal film compositions

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7922992B2 (en) 2002-09-13 2011-04-12 Ica Trinova, Llc Composition and method for producing carbon dioxide
US8709396B2 (en) 2002-09-13 2014-04-29 Premark Feg L.L.C. Method and composition for attracting arthropods by volatizing an acid
US7347994B2 (en) 2002-09-13 2008-03-25 Ica Trinova, Llc Method and composition for attracting arthropods by volatilizing an acid
US8808622B2 (en) 2004-01-07 2014-08-19 Noxilizer, Inc. Sterilization system and device
EP1701747A4 (fr) * 2004-01-07 2009-05-27 Noxilizer Inc Systeme et dispositif de sterilisation
AU2005204360B2 (en) * 2004-01-07 2011-03-31 Noxilizer, Inc. Sterilization system and device
US8017074B2 (en) 2004-01-07 2011-09-13 Noxilizer, Inc. Sterilization system and device
US9180217B2 (en) 2004-01-07 2015-11-10 Noxilizer, Inc. Sterilization system and device
US8703066B2 (en) 2004-01-07 2014-04-22 Noxilizer, Inc. Sterilization system and method
US8721984B2 (en) 2009-02-23 2014-05-13 Noxilizer, Inc. Device and method for gas sterilization
US8425837B2 (en) 2009-02-23 2013-04-23 Noxilizer, Inc. Device and method for gas sterilization
US9382116B2 (en) 2013-01-10 2016-07-05 Ica Trinova, Llc Mixtures for producing chlorine dioxide gas in enclosures and methods of making the same
WO2017106685A1 (fr) * 2015-12-18 2017-06-22 Sabre Intellectual Property Holdings Llc Procédés d'extraction d'huiles et de graisses à partir d'une matière solide à l'aide de dioxyde de chlore
US10850981B2 (en) 2017-04-25 2020-12-01 Ica Trinova, Llc Methods of producing a gas at a variable rate
US11518676B2 (en) 2017-04-25 2022-12-06 Ica Trinova Llc Methods of producing a gas at a variable rate
US11912568B2 (en) 2018-03-14 2024-02-27 Ica Trinova, Llc Methods of producing a gas at a controlled rate
US12221341B2 (en) 2018-03-14 2025-02-11 Ica Trinova, Llc Methods of producing a gas at a controlled rate
US20220126254A1 (en) * 2020-10-27 2022-04-28 Selective Micro Technologies, Llc Gas micro reactor utilizing membrane packaging
US12036525B2 (en) * 2020-10-27 2024-07-16 Selective Micro Technologies, Llc Gas micro reactor utilizing membrane packaging

Also Published As

Publication number Publication date
AU2002357279A1 (en) 2003-06-30

Similar Documents

Publication Publication Date Title
EP1255572B1 (fr) Appareil et procede de distribution regulee d'un gaz
US7922984B2 (en) Apparatus and method for controlled delivery of a gas
US6607696B1 (en) Apparatus and method for controlled delivery of a gas
US4370305A (en) Device for the sterilization of fluid substances
CA2966165C (fr) Emballages auto-sterilisant et procedes pour les fabriquer et les utiliser
US6764661B1 (en) Device for producing an aqueous chlorine dioxide solution
US20060120945A1 (en) Reusable apparatus for gas generation
US20060039841A1 (en) Systems and methods for producing aqueous solutions and gases having disinfecting properties and substantially eliminating impurities
WO2003051407A1 (fr) Appareil et procedes pour distribuer un gaz
US20240335813A1 (en) Gas micro reactor utilizing membrane packaging
CA3204435A1 (fr) Insert de bouteille de pulverisation comprenant un micro-reacteur de production de dioxyde de chlore utilisant un emballage a membrane
WO2004073755A1 (fr) Dispositif de distribution de gaz et procedes d'utilisation correspondants
US20240066487A1 (en) Improved device for facilitating a chemical reaction
AU2006200542A1 (en) Apparatus and method for controlled delivery of a gas
US20070243103A1 (en) Disinfectant system
ZA200205889B (en) Apparatus and method for controlled delivery of a gas.

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ OM PH PL PT RO RU SC SD SE SG SK SL TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR IE IT LU MC NL PT SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
122 Ep: pct application non-entry in european phase
NENP Non-entry into the national phase

Ref country code: JP

WWW Wipo information: withdrawn in national office

Country of ref document: JP