US20160166960A1 - Filter media with improved conductivity - Google Patents

Filter media with improved conductivity Download PDF

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Publication number
US20160166960A1
US20160166960A1 US14/938,202 US201514938202A US2016166960A1 US 20160166960 A1 US20160166960 A1 US 20160166960A1 US 201514938202 A US201514938202 A US 201514938202A US 2016166960 A1 US2016166960 A1 US 2016166960A1
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US
United States
Prior art keywords
filter media
fibers
filtration substrate
filtration
conductive coating
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.)
Abandoned
Application number
US14/938,202
Inventor
Wai Ming Choi
Karin N. Soper
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.)
Hollingsworth and Vose Co
Original Assignee
Hollingsworth and Vose Co
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Filing date
Publication date
Application filed by Hollingsworth and Vose Co filed Critical Hollingsworth and Vose Co
Priority to US14/938,202 priority Critical patent/US20160166960A1/en
Assigned to HOLLINGSWORTH & VOSE COMPANY reassignment HOLLINGSWORTH & VOSE COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CHOI, WAI MING, SOPER, KARIN NOELLE
Publication of US20160166960A1 publication Critical patent/US20160166960A1/en
Abandoned legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/1692—Other shaped material, e.g. perforated or porous sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
    • B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
    • B01D29/016—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements with corrugated, folded or wound filtering elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D37/00—Processes of filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
    • B01D39/1615—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of natural origin
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2003—Glass or glassy material
    • B01D39/2017—Glass or glassy material the material being filamentary or fibrous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2027—Metallic material
    • B01D39/2041—Metallic material the material being filamentary or fibrous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2055—Carbonaceous material
    • B01D39/2058—Carbonaceous material the material being particulate
    • B01D39/2062—Bonded, e.g. activated carbon blocks
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2055—Carbonaceous material
    • B01D39/2065—Carbonaceous material the material being fibrous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2068—Other inorganic materials, e.g. ceramics
    • B01D39/2082—Other inorganic materials, e.g. ceramics the material being filamentary or fibrous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/52—Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material
    • B01D46/521—Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material using folded, pleated material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/04—Plant or installations having external electricity supply dry type
    • B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
    • B03C3/155—Filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/02—Types of fibres, filaments or particles, self-supporting or supported materials
    • B01D2239/0241—Types of fibres, filaments or particles, self-supporting or supported materials comprising electrically conductive fibres or particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/04—Additives and treatments of the filtering material
    • B01D2239/0471—Surface coating material
    • B01D2239/0478—Surface coating material on a layer of the filter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/0604—Arrangement of the fibres in the filtering material
    • B01D2239/0618—Non-woven
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/0604—Arrangement of the fibres in the filtering material
    • B01D2239/0622—Melt-blown
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/0604—Arrangement of the fibres in the filtering material
    • B01D2239/0627—Spun-bonded
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/065—More than one layer present in the filtering material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/065—More than one layer present in the filtering material
    • B01D2239/0668—The layers being joined by heat or melt-bonding
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/065—More than one layer present in the filtering material
    • B01D2239/0672—The layers being joined by welding
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/065—More than one layer present in the filtering material
    • B01D2239/0681—The layers being joined by gluing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/08—Special characteristics of binders
    • B01D2239/083—Binders between layers of the filter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/08—Special characteristics of binders
    • B01D2239/086—Binders between particles or fibres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01D2239/10—Filtering material manufacturing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1208—Porosity
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1225—Fibre length
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1233—Fibre diameter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1241—Particle diameter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/125—Size distribution
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1258—Permeability
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1275—Stiffness
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12—Special parameters characterising the filtering material
    • B01D2239/1291—Other parameters
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T29/00—Metal working
    • Y10T29/49—Method of mechanical manufacture
    • Y10T29/49002—Electrical device making

Definitions

  • the present invention relates to filter media having an improved conductivity and to methods for making the same.
  • precipitator type air filter which is an electronic air filter having ionizing wires of about 0.005 inches diameter, charged at about 7 Kilovolts, placed between grounded plates to generate a corona and charge the dust particles passing therethrough. Further down the airflow path, alternating charged and grounded plates collect the charged particles of dust.
  • precipitator type filters are difficult to maintain, requiring regular cleaning of the collector plates, which get loaded with fine dust. Cleaning often requires using very strong detergents.
  • Another disadvantage of the precipitator type filter is that they produce a significant amount of ozone. This occurs because the charging wires are placed near grounded surfaces.
  • the present invention generally provides filter media having an improved conductivity to enhance filtration efficiency and/or static electricity dissipation, and to methods for making the same.
  • a filter media is provided having a filtration substrate, and at least one conductive coating disposed on at least a portion of the at least one filtration substrate.
  • the filtration substrate can be formed from a variety of materials, and it can include any number of filtration layers that together form a substrate.
  • the filtration substrate can be formed from natural fibers, organic fibers, inorganic fibers, or combinations thereof. Suitable fibers include, for example, glass fibers, ceramic fibers, polymer fibers, cotton fibers, hemp fibers, carbon fibers, and combinations thereof.
  • the conductive coating can also be formed from a variety of materials, and it can be disposed on all or only a portion of the filtration substrate.
  • the conductive coating can be formed from carbon fibers, carbon particles, metal fibers, conductive polymers such as poly(3,4ethylenedioxythiophene)poly(styrenesulfonate), polyaniline, nickel coated carbon fibers, or other conductive materials.
  • the conductive coating is formed from a metal fiber that includes a metal such as, for example, aluminum, silver, copper, nickel, gold, lead, tin, zinc, steel, and combinations thereof.
  • the conductive coating can be formed from a metal, such as aluminum, silver, copper, nickel, gold, lead, tin, zinc, and combinations thereof.
  • the conductive coating can also be disposed on the filtration substrate using a variety of techniques.
  • the filtration substrate can be saturated with the conductive coating.
  • the conductive coating can be painted or extruded onto the filtration substrate.
  • the filter media can include a bonding agent that bonds the conductive coating to the filtration substrate.
  • the bonding agent can be formed from, for example, a polymer such as polyvinylidene chloride, acrylic latex, polyurethane dispersion, polyvinyl acetate, polyvinyl alcohol, and combinations thereof.
  • the bonding agent can also optionally be conductive.
  • the filter media can be configured for a variety of purposes, including EMI shielding, optical shielding, or other uses that require electrically enhanced filtration and/or static dissipation.
  • the filter media can also be pleated or have any other configuration that can vary depending on the intended use.
  • the filter media can also include a coupling mechanism for connecting a high voltage power source to the conductive coating. When energy is delivered to the conductive coating, the coating will emit ions to increase the efficiency of the filter media.
  • the present invention also provides exemplary methods for forming a filter media.
  • the method can include forming a filtration substrate having at least one filtration layer, and disposing at least one conductive coating on at least one surface of the filtration substrate to form a conductive filter media.
  • the conductive coating can be, for example, a conductive polymer, and the conductive coating can be disposed on at least one surface of the filtration substrate by saturating the filtration substrate with the conductive polymer.
  • the conductive coating can be bonded to at least one surface of the filtration substrate.
  • a polymer coating for example, can be used to bond the conductive coating to the filtration substrate.
  • the method can also include placing the conductive filter media in an air stream, and coupling a high voltage power supply to the conductive filter media to create an electric field such that the conductive coating will emit ions that charge dust particles in the air stream to increase the trapping efficiency of the conductive filter media.
  • the method can include placing the conductive filter media in an fluid stream, and coupling a high voltage power supply to the conductive filter media to create an electric field such that the conductive coating will dissipate static charge generated from the flow of fluid through the conductive filter media.
  • a polymer can be deposited via an extrusion process.
  • the filter media can include a filtration substrate, and at least one conductive coating disposed on at least a portion of the filtration substrate.
  • the conductive coating is coupled to an energy source and effectively emits ions when energy is delivered thereto. This increases the efficiency of the filtration substrate, and in particular increases the trapping efficiency of the filter media.
  • the conductive coating can also eliminate or dissipate static charge, particularly static charge generated during fluid filtration.
  • the filter media can be adapted for use in a variety of applications including, by way of non-limiting example, EMI shielding, optical shielding, or other uses that require electrically enhanced filtration, such as in ASHRAE filters, vacuum bag filters, vacuum exhaust filters, room air cleaner filters, engine/cabin air filters, HEPA (High Efficiency Particulate Air) filters, ULPA (Ultra Efficiency Particulate Air) filters, fuel filters, and hydraulic fluid filters.
  • the filter media can also be formed into a variety of filter constructs including, for example, a pleated filter media.
  • the conductive media can also have application in the area of static charge elimination or dissipation.
  • the filter media is formed from a filtration substrate and a conductive coating disposed on at least a portion of the filtration substrate.
  • the filtration substrate can have virtually any configuration known in the art, and the particular configuration can vary depending on the intended use.
  • the filtration substrate can be formed from one or more filtration layers, such as a non-woven web, that are combined to form the filtration substrate.
  • the filtration layer(s) can be formed from a variety of materials, including natural fibers, organic fibers, inorganic fibers, and combinations thereof. Suitable exemplary fibers include glass fibers, ceramic fibers, polymer fibers, cotton fibers, hemp fibers, carbon fibers, and combinations thereof.
  • the filtration layers can also be formed using a variety of techniques known in the art, including web forming, e.g., wet laid, dry laid, and direct laid, carding, spun bonding, melt blowing, film fibrillation, etc.
  • web forming e.g., wet laid, dry laid, and direct laid, carding, spun bonding, melt blowing, film fibrillation, etc.
  • multiple layers can be combined using various techniques known in the art, including, by way of non-limiting example, ultrasonic welding, ultrasonic bonding, adhesives or other methods known to those having ordinary skill in the art. Ultrasonic bonding can be accomplished by edge welding, full width bonding, partial width bonding, or combinations thereof.
  • the layers can be pressed together by a calendaring process which causes each layer to physically adhere to the other layer.
  • the filter media can also include a conductive coating that is applied to at least a portion of the filtration substrate.
  • the coating is preferably configured to emit ions that charge dust particles in the air stream to increase the trapping efficiency of the conductive filter media.
  • the conductive coating can also be used to eliminate or dissipate any static charge that may be generated, particularly during fluid filtration.
  • the conductive coating produces a filter media having a surface resistivity in the range of about 1 ⁇ 10 2 to 1 ⁇ 10 12 ohms per square, however the surface resistivity can vary depending on the intended use as well as the particular materials and processes used to form the filter media. For example, where the filter media is to be used to dissipate static charge, the surface resistivity is preferably less than about 1 ⁇ 10 7 ohms per square.
  • the conductive coating can be formed from a variety of materials, but as indicated above it is preferably formed from a material that is configured to emit ions when energy is delivered thereto.
  • the conductive coating can be from a conductive metal or metal fibers that include one or more metals, such as aluminum, silver, copper, nickel, gold, lead, tin, zinc, and combinations thereof.
  • the conductive coating can be formed from conductive carbon fibers, such as a nickel coated carbon fiber.
  • One exemplary nickel coated carbon fiber is manufactured by Toho Tenax America, Inc. of Rockwood, Tenn.
  • the conductive coating can also be formed from a conductive polymer, such as poly(3,4ethylenedioxythiophene)poly(styrenesulfonate) or polyaniline.
  • the conductive coating can be formed either prior to or during application of the coating on the filtration substrate, and various processes known in the art can be used to form the coating and/or apply it to the substrate.
  • the conductive coating can also be applied to all or only portions of one or both opposed surfaces of the filtration substrate, or to all or only portions of one or both of the opposed surfaces of the filtration layers that are combined to form the filtration substrate.
  • the conductive materials can be dispersed in a solution, such as water or a polymer, and the filtration substrate can be saturated with the solution such that the coating surrounds the fibers that form the filtration substrate.
  • the substrate can be placed into a mold, and a slurry containing water or a polymer solution and the conductive fibers or metal can be drained through the substrate to saturate the substrate and thereby deposit the conductive fibers or metal onto the substrate.
  • the conductive coating can be painted onto the surface(s), e.g., using a paint brush, applied using a vacuum metalizing process, an electrode plating process, a chemical plating process (without electrodes), sputtered onto the filtration substrate or filtration layers that form the substrate, or extruded onto the substrate.
  • a conductive polymer or a polymer and a conductive material such as a conductive powder or particles
  • the hot melt can be extruded directly onto the substrate whereby it surrounds and bonds with the fibers that form the substrate.
  • the conductive coating can be formed using various techniques and from various combinations of materials. Moreover, a variety of techniques can be used to apply the coating to all or discrete portions of the filtration substrate.
  • a bonding agent such as a polymer, can also optionally be used to bond the conductive coating to the filtration substrate.
  • the bonding agent can be added during various stages of the process. For example, where the conductive material is dispersed in water, the bonding agent can be added to the water and saturated onto the substrate with the conductive material.
  • the bonding agent can also or alternatively be applied to the coating, particularly in the case of a fiber or particle. While a variety of bonding agents can be used, suitable exemplary bonding agents include polymers, such as polyvinylidene chloride, acrylic latex, polyurethane dispersion, polyvinyl acetate, and polyvinyl alcohol.
  • the bonding agent can also optionally be conductive, and can be formed from various conductive materials, such as those previously disclosed herein.
  • energy is delivered to the filter media, and in particular to the conductive coating, from a high voltage power source to impart conductivity to the filter media.
  • the high voltage power supply can be connected to the filter media using a coupling mechanism, such as electrodes.
  • a coupling mechanism such as electrodes.
  • an electric field will be created and the conductive coating will emit ions that charge dust particles in the air stream, thereby increasing the trapping efficiency of the conductive filter media.
  • the conductive coating also offers a path for redirecting any static charge that is generated during filtration, thereby reducing or eliminating the static charge.
  • a glass fiber filter media is formed from glass wool fibers having a diameter in the range of about 0.3 to 4.0 microns, and chopped glass fibers having a length of about 0.25 inches and a diameter of about 7 microns.
  • the glass fiber filter media is then placed in a vacuum chamber which is pumped down to a pressure of about 10E-04 to 10E-05 torr.
  • a vacuum metalizing process is used to deposit a conductive coating onto the glass fiber filter media.
  • an aluminum wire is heated electrically within the chamber, whereby it vaporizes under vacuum and re-condenses onto a surface of the filter media to form a layer of conductive aluminum coating of approximately 300 Angstrom.
  • the coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured less than 50 ohm, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 10E13 ohm.
  • a glass fiber filter media is formed from 0.25 inch chopped strand glass fiber having a diameter of about 6 to 7 microns, 0.8 micron microglass fiber, 4.5 to 5.0 micron microglass fiber, and polyvinyl alcohol fiber.
  • Nickel coated carbon fibers purchased from Toho Tenax America, Inc. are dispersed in water, along with a polyvinyl alcohol fiber to facilitate adhesion of the fiber to the glass fiber filter media.
  • the glass fiber filter media is saturated with the dispersion to deposit approximately 21 g/m 2 of nickel coated carbon fiber onto the glass fiber filter media.
  • the coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured about 25.3 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1 ⁇ 10 13 ohms per square.
  • a glass fiber filter media is prepared as set forth in Example 2.
  • the filter media is coated with carbon fibers using the process set forth in Example 2.
  • the coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991.
  • the electrical resistance of the coated glass fiber filter media measured to be 13.5 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1 ⁇ 10 13 ohms per square.
  • a glass fiber filter media is prepared as set forth in Example 2.
  • the filter media is coated with stainless steel fibers using the process set forth in Example 2.
  • the coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991.
  • the electrical resistance of the coated glass fiber filter media measured to be 27.6 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1 ⁇ 10 13 ohms per square.
  • a glass fiber filter media is formed from 0.4 micron microglass fiber, 0.6 micron glass fiber, 1 micron glass fiber, 2.6 micron glass fiber, and 1.0 denier polyvinyl alcohol fiber.
  • the fiber composition is such that it will attain a required filter efficiency.
  • a painting process is used to deposit carbon containing ink onto the glass fiber filter media.
  • the coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured in the range about 300 to 55,000 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1 ⁇ 10 13 ohms per square.

Abstract

Filter media are provided having improved conductivity to enhance filtration efficiency and/or dissipate static charge, and methods for making the same. In one exemplary embodiment, the filter media can include a filtration substrate, and at least one conductive coating disposed on at least a portion of the filtration substrate. In use, the conductive coating is coupled to an energy source and it is effective to emit ions when energy is delivered thereto to increase the efficiency of the filtration substrate and/or to dissipate or eliminate static charge generated during filtration.

Description

    CROSS REFERENCE TO RELATED APPLICATIONS
  • This application is a continuation of U.S. application Ser. No. 14/154,307, filed Jan. 14, 2014, which is a continuation of U.S. application Ser. No. 13/103,170 (now U.S. Pat. No. 8,663,358), filed May 9, 2011, which is a continuation of U.S. application Ser. No. 11/461,804 (now U.S. Pat. No. 7,694,012), filed Aug. 2, 2006, which claims priority to U.S. Provisional Application No. 60/705,135 filed Aug. 3, 2005, all of which are hereby incorporated by reference in their entireties.
    • FIELD OF THE INVENTION
  • The present invention relates to filter media having an improved conductivity and to methods for making the same.
    • BACKGROUND OF THE INVENTION
  • It is well known that charged particles are more readily captured by a filter media than are neutral particles. One of the most common ionizing air filters is a precipitator type air filter, which is an electronic air filter having ionizing wires of about 0.005 inches diameter, charged at about 7 Kilovolts, placed between grounded plates to generate a corona and charge the dust particles passing therethrough. Further down the airflow path, alternating charged and grounded plates collect the charged particles of dust. The disadvantage of precipitator type filters is that they are difficult to maintain, requiring regular cleaning of the collector plates, which get loaded with fine dust. Cleaning often requires using very strong detergents. Another disadvantage of the precipitator type filter is that they produce a significant amount of ozone. This occurs because the charging wires are placed near grounded surfaces. This arrangement generates corona all along the length of the wires, which can be seen glowing in the dark. Moreover, in some liquid filtration applications, such as filtrating of hydraulic fluid, a static charge can build up on the surface of the filter, potentially causing an explosion or fire hazard.
  • Accordingly, there remains a need for filter media having improved conductivity to enhance filtration efficiency and/or static electricity dissipation, and to methods for making the same.
    • SUMMARY OF THE INVENTION
  • The present invention generally provides filter media having an improved conductivity to enhance filtration efficiency and/or static electricity dissipation, and to methods for making the same. In one exemplary embodiment, a filter media is provided having a filtration substrate, and at least one conductive coating disposed on at least a portion of the at least one filtration substrate. The filtration substrate can be formed from a variety of materials, and it can include any number of filtration layers that together form a substrate. By way of non-limiting example, the filtration substrate can be formed from natural fibers, organic fibers, inorganic fibers, or combinations thereof. Suitable fibers include, for example, glass fibers, ceramic fibers, polymer fibers, cotton fibers, hemp fibers, carbon fibers, and combinations thereof. The conductive coating can also be formed from a variety of materials, and it can be disposed on all or only a portion of the filtration substrate. By way of non-limiting example, the conductive coating can be formed from carbon fibers, carbon particles, metal fibers, conductive polymers such as poly(3,4ethylenedioxythiophene)poly(styrenesulfonate), polyaniline, nickel coated carbon fibers, or other conductive materials. In one exemplary embodiment, the conductive coating is formed from a metal fiber that includes a metal such as, for example, aluminum, silver, copper, nickel, gold, lead, tin, zinc, steel, and combinations thereof. In another exemplary embodiment, the conductive coating can be formed from a metal, such as aluminum, silver, copper, nickel, gold, lead, tin, zinc, and combinations thereof.
  • The conductive coating can also be disposed on the filtration substrate using a variety of techniques. For example, in one embodiment the filtration substrate can be saturated with the conductive coating. In another embodiment, the conductive coating can be painted or extruded onto the filtration substrate. In another embodiment, the filter media can include a bonding agent that bonds the conductive coating to the filtration substrate. The bonding agent can be formed from, for example, a polymer such as polyvinylidene chloride, acrylic latex, polyurethane dispersion, polyvinyl acetate, polyvinyl alcohol, and combinations thereof. The bonding agent can also optionally be conductive.
  • In use, the filter media can be configured for a variety of purposes, including EMI shielding, optical shielding, or other uses that require electrically enhanced filtration and/or static dissipation. The filter media can also be pleated or have any other configuration that can vary depending on the intended use. In order to electrically charge the conductive coating, the filter media can also include a coupling mechanism for connecting a high voltage power source to the conductive coating. When energy is delivered to the conductive coating, the coating will emit ions to increase the efficiency of the filter media.
  • The present invention also provides exemplary methods for forming a filter media. In one embodiment, the method can include forming a filtration substrate having at least one filtration layer, and disposing at least one conductive coating on at least one surface of the filtration substrate to form a conductive filter media. In one embodiment, the conductive coating can be, for example, a conductive polymer, and the conductive coating can be disposed on at least one surface of the filtration substrate by saturating the filtration substrate with the conductive polymer. In another embodiment, the conductive coating can be bonded to at least one surface of the filtration substrate. A polymer coating, for example, can be used to bond the conductive coating to the filtration substrate. The method can also include placing the conductive filter media in an air stream, and coupling a high voltage power supply to the conductive filter media to create an electric field such that the conductive coating will emit ions that charge dust particles in the air stream to increase the trapping efficiency of the conductive filter media. In another embodiment, the method can include placing the conductive filter media in an fluid stream, and coupling a high voltage power supply to the conductive filter media to create an electric field such that the conductive coating will dissipate static charge generated from the flow of fluid through the conductive filter media. In other embodiments, a polymer can be deposited via an extrusion process.
    • DETAILED DESCRIPTION OF THE INVENTION
  • The present invention provides filter media having improved conductivity to enhance filtration efficiency, and methods for making the same. In one exemplary embodiment, the filter media can include a filtration substrate, and at least one conductive coating disposed on at least a portion of the filtration substrate. In use, the conductive coating is coupled to an energy source and effectively emits ions when energy is delivered thereto. This increases the efficiency of the filtration substrate, and in particular increases the trapping efficiency of the filter media. The conductive coating can also eliminate or dissipate static charge, particularly static charge generated during fluid filtration.
  • The filter media can be adapted for use in a variety of applications including, by way of non-limiting example, EMI shielding, optical shielding, or other uses that require electrically enhanced filtration, such as in ASHRAE filters, vacuum bag filters, vacuum exhaust filters, room air cleaner filters, engine/cabin air filters, HEPA (High Efficiency Particulate Air) filters, ULPA (Ultra Efficiency Particulate Air) filters, fuel filters, and hydraulic fluid filters. The filter media can also be formed into a variety of filter constructs including, for example, a pleated filter media. The conductive media can also have application in the area of static charge elimination or dissipation.
  • As indicated above, in an exemplary embodiment the filter media is formed from a filtration substrate and a conductive coating disposed on at least a portion of the filtration substrate. The filtration substrate can have virtually any configuration known in the art, and the particular configuration can vary depending on the intended use. In one embodiment, the filtration substrate can be formed from one or more filtration layers, such as a non-woven web, that are combined to form the filtration substrate. The filtration layer(s) can be formed from a variety of materials, including natural fibers, organic fibers, inorganic fibers, and combinations thereof. Suitable exemplary fibers include glass fibers, ceramic fibers, polymer fibers, cotton fibers, hemp fibers, carbon fibers, and combinations thereof. The filtration layers can also be formed using a variety of techniques known in the art, including web forming, e.g., wet laid, dry laid, and direct laid, carding, spun bonding, melt blowing, film fibrillation, etc. Once the layers are formed, if desired multiple layers can be combined using various techniques known in the art, including, by way of non-limiting example, ultrasonic welding, ultrasonic bonding, adhesives or other methods known to those having ordinary skill in the art. Ultrasonic bonding can be accomplished by edge welding, full width bonding, partial width bonding, or combinations thereof. Alternatively, the layers can be pressed together by a calendaring process which causes each layer to physically adhere to the other layer.
  • As previously indicated, the filter media can also include a conductive coating that is applied to at least a portion of the filtration substrate. When energy is delivered to the conductive coating, the coating is preferably configured to emit ions that charge dust particles in the air stream to increase the trapping efficiency of the conductive filter media. The conductive coating can also be used to eliminate or dissipate any static charge that may be generated, particularly during fluid filtration. In an exemplary embodiment, the conductive coating produces a filter media having a surface resistivity in the range of about 1×102 to 1×1012 ohms per square, however the surface resistivity can vary depending on the intended use as well as the particular materials and processes used to form the filter media. For example, where the filter media is to be used to dissipate static charge, the surface resistivity is preferably less than about 1×107 ohms per square.
  • The conductive coating can be formed from a variety of materials, but as indicated above it is preferably formed from a material that is configured to emit ions when energy is delivered thereto. In one exemplary embodiment, the conductive coating can be from a conductive metal or metal fibers that include one or more metals, such as aluminum, silver, copper, nickel, gold, lead, tin, zinc, and combinations thereof. In one exemplary embodiment, the conductive coating can be formed from conductive carbon fibers, such as a nickel coated carbon fiber. One exemplary nickel coated carbon fiber is manufactured by Toho Tenax America, Inc. of Rockwood, Tenn. The conductive coating can also be formed from a conductive polymer, such as poly(3,4ethylenedioxythiophene)poly(styrenesulfonate) or polyaniline.
  • The conductive coating can be formed either prior to or during application of the coating on the filtration substrate, and various processes known in the art can be used to form the coating and/or apply it to the substrate. The conductive coating can also be applied to all or only portions of one or both opposed surfaces of the filtration substrate, or to all or only portions of one or both of the opposed surfaces of the filtration layers that are combined to form the filtration substrate. In one embodiment, the conductive materials can be dispersed in a solution, such as water or a polymer, and the filtration substrate can be saturated with the solution such that the coating surrounds the fibers that form the filtration substrate. For example, the substrate can be placed into a mold, and a slurry containing water or a polymer solution and the conductive fibers or metal can be drained through the substrate to saturate the substrate and thereby deposit the conductive fibers or metal onto the substrate. In other embodiments, the conductive coating can be painted onto the surface(s), e.g., using a paint brush, applied using a vacuum metalizing process, an electrode plating process, a chemical plating process (without electrodes), sputtered onto the filtration substrate or filtration layers that form the substrate, or extruded onto the substrate. For example, where an extrusion process is used, a conductive polymer, or a polymer and a conductive material such as a conductive powder or particles, can be placed into an extruder to form a hot melt. The hot melt can be extruded directly onto the substrate whereby it surrounds and bonds with the fibers that form the substrate. A person skilled in the art will appreciate that the conductive coating can be formed using various techniques and from various combinations of materials. Moreover, a variety of techniques can be used to apply the coating to all or discrete portions of the filtration substrate.
  • A bonding agent, such as a polymer, can also optionally be used to bond the conductive coating to the filtration substrate. The bonding agent can be added during various stages of the process. For example, where the conductive material is dispersed in water, the bonding agent can be added to the water and saturated onto the substrate with the conductive material. The bonding agent can also or alternatively be applied to the coating, particularly in the case of a fiber or particle. While a variety of bonding agents can be used, suitable exemplary bonding agents include polymers, such as polyvinylidene chloride, acrylic latex, polyurethane dispersion, polyvinyl acetate, and polyvinyl alcohol. The bonding agent can also optionally be conductive, and can be formed from various conductive materials, such as those previously disclosed herein.
  • In use, energy is delivered to the filter media, and in particular to the conductive coating, from a high voltage power source to impart conductivity to the filter media. The high voltage power supply can be connected to the filter media using a coupling mechanism, such as electrodes. As a result, an electric field will be created and the conductive coating will emit ions that charge dust particles in the air stream, thereby increasing the trapping efficiency of the conductive filter media. The conductive coating also offers a path for redirecting any static charge that is generated during filtration, thereby reducing or eliminating the static charge.
  • The following non-limiting examples serve to further illustrate various exemplary embodiments of the invention:
    • Example 1
  • A glass fiber filter media is formed from glass wool fibers having a diameter in the range of about 0.3 to 4.0 microns, and chopped glass fibers having a length of about 0.25 inches and a diameter of about 7 microns. The glass fiber filter media is then placed in a vacuum chamber which is pumped down to a pressure of about 10E-04 to 10E-05 torr. A vacuum metalizing process is used to deposit a conductive coating onto the glass fiber filter media. In particular, an aluminum wire is heated electrically within the chamber, whereby it vaporizes under vacuum and re-condenses onto a surface of the filter media to form a layer of conductive aluminum coating of approximately 300 Angstrom.
  • The coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured less than 50 ohm, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 10E13 ohm.
    • Example 2
  • A glass fiber filter media is formed from 0.25 inch chopped strand glass fiber having a diameter of about 6 to 7 microns, 0.8 micron microglass fiber, 4.5 to 5.0 micron microglass fiber, and polyvinyl alcohol fiber. Nickel coated carbon fibers, purchased from Toho Tenax America, Inc. are dispersed in water, along with a polyvinyl alcohol fiber to facilitate adhesion of the fiber to the glass fiber filter media. The glass fiber filter media is saturated with the dispersion to deposit approximately 21 g/m2 of nickel coated carbon fiber onto the glass fiber filter media.
  • The coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured about 25.3 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1×1013 ohms per square.
    • Example 3
  • A glass fiber filter media is prepared as set forth in Example 2. The filter media is coated with carbon fibers using the process set forth in Example 2. The coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured to be 13.5 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1×1013 ohms per square.
    • Example 4
  • A glass fiber filter media is prepared as set forth in Example 2. The filter media is coated with stainless steel fibers using the process set forth in Example 2. The coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured to be 27.6 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1×1013 ohms per square.
    • Example 5
  • A glass fiber filter media is formed from 0.4 micron microglass fiber, 0.6 micron glass fiber, 1 micron glass fiber, 2.6 micron glass fiber, and 1.0 denier polyvinyl alcohol fiber. The fiber composition is such that it will attain a required filter efficiency. A painting process is used to deposit carbon containing ink onto the glass fiber filter media.
  • The coated glass fiber filter media is measured for surface electrical resistance using a Vermason H1003 square probe for testing surface resistivity. The measurement equipment is confirmed to EN100015 Part 1:1991. The electrical resistance of the coated glass fiber filter media measured in the range about 300 to 55,000 ohms per square, compared to an uncoated glass fiber filter media which has an electrical resistance in excess of 1×1013 ohms per square.
  • One skilled in the art will appreciate further features and advantages of the invention based on the above-described embodiments. Accordingly, the invention is not to be limited by what has been particularly shown and described, except as indicated by the appended claims. All publications and references cited herein are expressly incorporated herein by reference in their entirety.

Claims (19)

1. A filter media, comprising:
a filtration substrate comprising fibers; and
at least one conductive coating disposed on at least a portion of the filtration substrate.
2. A method, comprising:
passing a fluid stream through a filter media comprising:
a filtration substrate comprising fibers; and
at least one conductive coating disposed on at least a portion of the filtration substrate.
3. The method of claim 2, wherein the fluid stream comprises a liquid.
4. The method of claim 2, wherein the fluid stream comprises air.
5. The method of claim 2, comprising emitting ions from the filter media and charging particles in the fluid stream.
6. The method of claim 2, comprising generating an electric field from the filter media.
7. The method of claim 2, wherein the filter media has a surface resistivity in the range of about 1×1012 ohms per square.
8. The method of claim 2, wherein the filter media has surface resistivity of less than about 1×107 ohms per square.
9. The method of claim 2, wherein the filtration substrate is formed from multiple filtration layers.
10. The method of claim 2, wherein the filtration substrate comprises natural fibers, organic fibers, and/or inorganic fibers.
11. The method of claim 2, wherein the filtration substrate comprises glass fibers, ceramic fibers, polymer fibers, cotton fibers, hemp fibers, metal fibers and/or carbon fibers.
12. The method of claim 2, wherein the filtration substrate comprises metal fibers, and wherein the metal fibers are formed from a metal selected from the group consisting of aluminum, silver, copper, nickel, gold, lead, tin, zinc, steel, and combinations thereof.
13. The method of claim 2, wherein the filtration substrate comprises a wet-laid fiber web, a meltblown fiber web, and/or a dry laid fiber web.
14. The method of claim 2, wherein the filtration substrate comprises a bonding agent bonding the conductive coating to the filtration substrate.
15. The method of claim 2, wherein the filtration substrate comprises a conductive metal.
16. The method of claim 2, wherein the filtration substrate is formed from glass fibers.
17. The method of claim 2, wherein the filter media is pleated.
18. The method of claim 2, comprising dissipating static charge during the step of passing the fluid stream through the filter media.
19. The method of claim 2, wherein the conductive coating comprises conductive particles.
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US20140190353A1 (en) 2014-07-10
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US20110265312A1 (en) 2011-11-03
US8663358B2 (en) 2014-03-04
US20070028767A1 (en) 2007-02-08
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US9192942B2 (en) 2015-11-24
WO2007019294A2 (en) 2007-02-15

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