US20130082447A1 - Spiral wound gasket - Google Patents

Spiral wound gasket Download PDF

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Publication number
US20130082447A1
US20130082447A1 US13/645,320 US201213645320A US2013082447A1 US 20130082447 A1 US20130082447 A1 US 20130082447A1 US 201213645320 A US201213645320 A US 201213645320A US 2013082447 A1 US2013082447 A1 US 2013082447A1
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US
United States
Prior art keywords
talc
gasket
slurry
fill material
weight
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
US13/645,320
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English (en)
Inventor
Wayne Evans
Chad Yoder
Sherwin Damdar
Paul Jude Nichols
Richard Lynn Dibble
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Garlock Sealing Technologies LLC
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Garlock Sealing 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
Priority claimed from US13/252,718 external-priority patent/US9234589B2/en
Priority to US13/645,320 priority Critical patent/US20130082447A1/en
Application filed by Garlock Sealing Technologies LLC filed Critical Garlock Sealing Technologies LLC
Assigned to GARLOCK SEALING TECHNOLOGIES, LLC reassignment GARLOCK SEALING TECHNOLOGIES, LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: DIBBLE, RICHARD LYNN, YODER, CHAD, DAMDAR, SHERWIN, NICHOLS, PAUL JUDE, EVANS, WAYNE
Publication of US20130082447A1 publication Critical patent/US20130082447A1/en
Priority to SG11201501841SA priority patent/SG11201501841SA/en
Priority to PCT/US2013/060729 priority patent/WO2014081501A1/en
Priority to EP13857509.7A priority patent/EP2898249A4/en
Priority to BR112015006008A priority patent/BR112015006008A2/pt
Priority to MX2015003502A priority patent/MX2015003502A/es
Priority to CN201380060248.0A priority patent/CN104797872A/zh
Priority to KR1020157008971A priority patent/KR102224000B1/ko
Priority to CA2885031A priority patent/CA2885031A1/en
Priority to JP2015532182A priority patent/JP2015535911A/ja
Assigned to BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT reassignment BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT NOTICE OF GRANT OF SECURITY INTEREST IN PATENTS Assignors: GARLOCK SEALING TECHNOLOGIES LLC
Priority to US15/991,789 priority patent/US10955055B2/en
Abandoned legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16J—PISTONS; CYLINDERS; SEALINGS
    • F16J15/00—Sealings
    • F16J15/16—Sealings between relatively-moving surfaces
    • F16J15/18—Sealings between relatively-moving surfaces with stuffing-boxes for elastic or plastic packings
    • F16J15/20—Packing materials therefor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16L—PIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
    • F16L17/00—Joints with packing adapted to sealing by fluid pressure
    • F16L17/06—Joints with packing adapted to sealing by fluid pressure with sealing rings arranged between the end surfaces of the pipes or flanges or arranged in recesses in the pipe ends or flanges
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/14—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor incorporating preformed parts or layers, e.g. injection moulding around inserts or for coating articles
    • B29C45/14778—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor incorporating preformed parts or layers, e.g. injection moulding around inserts or for coating articles the article consisting of a material with particular properties, e.g. porous, brittle
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16J—PISTONS; CYLINDERS; SEALINGS
    • F16J15/00—Sealings
    • F16J15/02—Sealings between relatively-stationary surfaces
    • F16J15/06—Sealings between relatively-stationary surfaces with solid packing compressed between sealing surfaces
    • F16J15/10—Sealings between relatively-stationary surfaces with solid packing compressed between sealing surfaces with non-metallic packing
    • F16J15/12—Sealings between relatively-stationary surfaces with solid packing compressed between sealing surfaces with non-metallic packing with metal reinforcement or covering
    • F16J15/121—Sealings between relatively-stationary surfaces with solid packing compressed between sealing surfaces with non-metallic packing with metal reinforcement or covering with metal reinforcement
    • F16J15/125—Sealings between relatively-stationary surfaces with solid packing compressed between sealing surfaces with non-metallic packing with metal reinforcement or covering with metal reinforcement generally perpendicular to the surfaces
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
    • B29C43/02—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of definite length, i.e. discrete articles
    • B29C43/027—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor of articles of definite length, i.e. discrete articles having an axis of symmetry
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00—Other particular articles
    • B29L2031/26—Sealing devices, e.g. packaging for pistons or pipe joints
    • B29L2031/265—Packings, Gaskets
    • 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
    • Y10T156/00—Adhesive bonding and miscellaneous chemical manufacture
    • Y10T156/10—Methods of surface bonding and/or assembly therefor
    • Y10T156/1002—Methods of surface bonding and/or assembly therefor with permanent bending or reshaping or surface deformation of self sustaining lamina

Definitions

  • Spiral wound gaskets are commonly used to provide a seal between opposing pipe flanges in assemblies used to transport a variety of liquids and gases at various pressures and temperatures.
  • the spiral wound gaskets include a resilient sealing element, formed from alternating layers of a metal band and a winding fill material.
  • an outer guide ring formed typically from carbon steel, extends radially from the sealing element and is dimensioned to prevent over-compression of the sealing element.
  • an inner guide ring typically formed from carbon steel, extends radially inward from the inner periphery to prevent buckling.
  • a common differentiating factor among spiral wound gaskets is the type of winding fill materials used for different applications.
  • the relatively soft winding fill material is usually the ‘weakest’ link in the gasket, especially as application temperatures rise.
  • high temperature winding fill material include: asbestos; mica; vermiculite; and chemically or thermally exfoliated vermiculite (such as THERMICULITE).
  • these winding fill materials are brittle or dusty due to the fact that they lack organics to impart the elastic properties of lower temperature sealing materials, which tend to be more ‘tacky’ and stick together but can impart greater sealing characteristics and seal integrity.
  • a common lower temperature filler material for spiral wound gaskets is graphite.
  • Graphite performs well in common applications for temperatures up to about 850° F., at which point it tends to oxidize and lose mass continuously.
  • Graphite also cannot be used in media classified as strong oxidizers, such as molten salt. This detrimentally affects sealing ability of the gasket. Accordingly, graphite spiral wounds are not suitable for applications of continuous temperature above 850° F. in oxidizing atmospheres, or extended temperature forays above 900° F.
  • Embodiments of a spiral wound gasket include a resilient sealing element that includes spirally wound, alternating layers of metal banding and winding fill material.
  • the spiral wound gasket is provided as only including the sealing element.
  • embodiments of the spiral wound gasket will include an outer guide ring that extends radially outward from an outer periphery of the sealing element.
  • Some embodiments of the spiral wound gasket will include an inner guide ring that extends radially inward from an inner periphery of the sealing element.
  • Various applications of the spiral wound gasket may require the use of either or both of the outer guide ring and the inner guide ring.
  • the sealing element includes a resilient spiral core, which is made with elongate metal banding that is wound into a spiral of overlying turns.
  • the spiral winding of the metal banding positions adjacent turns of the metal banding in a spaced-apart relationship with one another to define a gap between the side portions of the metal banding.
  • the gap is at least substantially filled with the resilient winding fill material in alternate, overlapping relation with the metal banding.
  • Some embodiments of the winding fill material use talc as the inorganic filler in a range from 60% to 90% by weight.
  • Inorganic fiber content for some such embodiments of the winding fill material is from 1% to 14% by weight.
  • organic binder content for embodiments of the winding fill material is from 1% to 8% by weight.
  • the winding fill material includes submicron-sized talc particles that comprise 75 to 90 wt % of the winding fill material.
  • the inorganic fiber can be from 5 to 20 wt % of the winding fill material 16 and can include silicic acid fiber.
  • the binder can be a latex emulsion and can be present in the filler material in the range of from 1 to 5 wt % of the winding fill material.
  • the winding fill material also can include additives, such as flocculant and defoamer. In some embodiments, the amount of organic material present in the winding fill material is limited to less than 5 wt % of the winding fill material.
  • a method for manufacturing the winding fill material described above generally includes preparing a talc slurry, preparing a sheet slurry using the talc slurry, forming a pre-densified gasket sheet from the sheet slurry, and densifying the gasket sheet to form the winding fill material.
  • Other methods of manufacturing the winding fill material are also disclosed herein.
  • the spiral wound gasket include one or more layers of facing material that may be secured to one or both of the axial faces of the sealing element.
  • the layers of facing material may be secured with the axial faces with organic binders, such as one of various spray adhesives.
  • organic binders such as one of various spray adhesives.
  • other securement methods including mechanical press fit and encapsulating are contemplated.
  • Some embodiments use layers of facing material that are formed from the same material as the aforedescribed filler material.
  • the spiral wound gasket includes a resilient sealing element that includes spirally wound, alternating layers of metal banding to define a resilient spiral core. However, no winding fill material is disposed between the layers of metal banding.
  • embodiments of the spiral wound gasket may use either, both, or neither of the outer guide ring and the inner guide ring.
  • a layer of facing material may be secured to one or both of the axial faces of the sealing element.
  • FIG. 1 depicts a perspective view of one embodiment of the spiral wound gasket of the present technology, wherein facing material is positioned
  • FIG. 2 depicts a cross-sectional view of the spiral wound gasket depicted in FIG. 1 .
  • FIG. 3 depicts a perspective view of another embodiment of the spiral wound gasket of the present technology, wherein no inner or outer rings are positioned at the inner and outer peripheral surfaces of the gasket windings.
  • FIG. 4 depicts a perspective view of still another embodiment of the spiral wound gasket of the present technology, wherein no facing material is positioned at the opposing axial faces of the gasket windings.
  • FIG. 5 depicts a cross-sectional view of another embodiment of the spiral wound gasket of the present technology, wherein no filler material is used between the metal windings of the gasket.
  • FIG. 6 depicts comparative testing data for the sealability of different spiral wound gasket at operational temperatures.
  • FIG. 7 depicts sample data demonstrating tensile strength and sealability, as a function of fiber content, in the formula for one embodiment of the facing material of the present technology.
  • embodiments of a spiral wound gasket 10 are depicted.
  • Various embodiments of the spiral wound gasket 10 will include a resilient sealing element 12 that includes spirally wound, alternating layers of metal banding 14 and winding fill material 16 .
  • embodiments of the spiral wound gasket 10 are provided as only including the sealing element 12 .
  • embodiments of the spiral wound gasket 10 will include an outer guide ring 18 that extends radially outward from an outer periphery of the sealing element sealing element 12 .
  • Some embodiments of the spiral wound gasket 10 will include an inner guide ring 20 that extends radially inward from an inner periphery of the sealing element 12 .
  • spiral wound gasket may require the use of either or both of the outer guide ring 18 and the inner guide ring 20 .
  • the spiral wound gasket of the present technology may be provided in nearly any size and shape desirable for particular applications.
  • sealing element 12 include resilient spiral core 15 , which is made with elongate metal banding 14 that is wound into a spiral of overlying turns.
  • the metal banding 14 is shaped to include a medial crest 22 that defines a ridge in the metal banding 14 between opposing sides portions 20 .
  • the spiral winding of the metal banding 14 positions adjacent turns of the metal banding 14 in a spaced-apart relationship with one another to define a gap 24 between the side portions 26 of the metal banding 14 .
  • the thickness of the metal banding 14 is approximately 0.007 inches; however, the thickness of the metal banding 14 may range from about 0.006 inches to about 0.008 inches thick.
  • the width of the metal banding 14 will vary according to the application. Various embodiments will use metal banding 14 that is formed from 316 stainless steel. However, other metal materials, such as Inconel, or other materials having higher temperature or chemical resistant metallurgies may be used, depending on the desired applications and manufacturing cost limits.
  • the gap 24 is at least substantially filled with the resilient winding fill material 16 in alternate, overlapping relation with the metal banding.
  • the winding fill material 16 may be provided with various ratios of filler, fiber, and binder.
  • embodiments of the winding fill material 16 use talc as the inorganic filler in a range from 60% to 90% by weight.
  • Inorganic fiber content for some such embodiments of the winding fill material 16 is from 1% to 14% by weight.
  • organic binder content for embodiments of the winding fill material 16 is from 1% to 8% by weight.
  • Some embodiments of the winding fill material 16 may be provided to include greater than 60% by weight talc, less than 20% by weight inorganic fiber, and less than 5% by weight organic binder.
  • Other embodiments of the winding fill material 16 include 75% to 90 wt % inorganic filler, 5% to 20 wt % inorganic fiber, and 1% to 5 wt % organic binder.
  • the winding fill material 16 is formed to include approximately 90% by weight talc, 7% by weight inorganic fiber, and 3% by weight organic binder.
  • the winding fill materials can be manipulated in a manner consistent with cost effective manufacturing in order to keep the spiral wound gasket 10 competitively priced.
  • the composition and ratio of raw material may be critically balanced to allow strips required for the spiral winding process to be manufactured.
  • the winding fill material 16 is capable of withstanding temperatures in excess of 850° F.
  • the winding fill material 16 can handle temperatures above 850° F. at least in part because of the use of inorganic fiber and inorganic filler and the minimization of the amount of organic binder used. In so doing, the winding fill material 16 minimizes the leak passages that tend to form in a winding fill material 16 when organic material burns off at extreme temperatures.
  • the winding fill material 16 also has improved sealant properties due to high filler content (typically provided at the expense of the fiber content).
  • the filler material is a better sealant than the fiber material, and accordingly, the winding fill material 16 described herein has improved sealing capabilities.
  • the inorganic filler material is, in various embodiments, present in the winding fill material 16 in the range of from 75 to 90 wt %. As noted above, this high filler content improves the sealing properties of the winding fill material 16 over previously known winding fill materials having lower filler content.
  • the inorganic filler is a hydrophobic filler material.
  • An exemplary hydrophobic filler material suitable for use in the winding fill material 16 described herein includes, but is not limited to, talc. Talc naturally repels water and provides for a better sealant, although the use of talc can also make forming the winding fill material more difficult.
  • Talc is also a useful filler material for the winding fill material 16 described herein because it is a platy filler that orients itself in thin layers during the forming process, which provides good sealant properties.
  • the talc used in embodiments described herein is typically a mined inorganic material and not a synthetic material.
  • the hydrophobic inorganic filler is the only filler present in the winding fill material 16 .
  • one or more hydrophilic fillers are used in conjunction with the hydrophobic filler.
  • the overall filler be substantially hydrophobic filler.
  • Exemplary hydrophilic fillers that can be used with a hydrophobic filler include, but are not limited to, mica, fluorinated mica, vermiculite, and boron nitride.
  • hydrophilic fillers can result in an easier process of making the winding fill material 16
  • hydrophilic nature of these inorganic fillers also means the resulting winding fill material 16 will have an affinity to water and therefore have inferior sealing properties to winding fill material 16 formed with only hydrophobic filler.
  • the filler material is preferably low particle size filler, such as submicron-sized filler particles.
  • the particle size of the inorganic filler material is in the range of 0.2 microns to 1.5 microns.
  • the low particle size fillers can help to produce winding fill material having very few voids.
  • the inorganic filler material has a specific gravity in the range of from 2.7 to 2.8 g/cm 3 .
  • Providing a winding fill material 16 having inorganic filler in the range of from 75 to 90 wt % differentiates the winding fill material 16 disclosed herein from some previously known winding fill materials.
  • Applicants believe that including a high percentage of inorganic filler in a winding fill material is generally counterintuitive to those of ordinary skill in the art.
  • the inclusion of higher amounts of filler in winding fill materials is typically at the expense of the amount of fiber used in the winding fill material.
  • those skilled in the art tend to disfavor reducing the fiber content of winding fill materials due to the associated decrease in winding fill material tensile strength.
  • the filler material is a hydrophobic filler material, such as in the case of talc
  • the process of manufacturing the winding fill material becomes more difficult as higher amounts of filler are used.
  • the hydrophobic talc filler material is difficult to wet and turn into a slurry that can be processed into sheet material. To avoid these processing difficulties, those of ordinary skill in the art have generally avoided using high amounts of hydrophobic filler material.
  • the inorganic fiber material is generally present in the winding fill material 16 in range of from 5 to 20 wt %.
  • the inorganic fiber material is a silicic acid fiber.
  • Examples of commercially available inorganic fibers that are suitable for use in the winding fill material 16 described herein include, but are not limited to, Nyad G, manufactured by Nyco Minerals of Willsboro, N.Y.; 3M Nextel Continuous Ceramic Oxide Fibers, manufactured by 3M of St. Paul, Minn.; and Insulfrax and Isofrax, manufactured by UniFrax of Niagra Falls, New York.
  • the inorganic fiber can also be Wollastonite or Sepiolite.
  • An Example of a commercially available silicic acid fibers that is suitable for use in the winding fill material 16 described herein includes, but is not limited to, Belcotex 225 SC 6 mm, manufactured by belChm of Dortmund, Germany.
  • the inorganic fiber is preferably a fiber having no “shot,” which is an undesirable non-fiber scrap byproduct produced during the manufacturing process of many ceramic fibers.
  • the inorganic fiber material is provided in the form of individual segments having small dimensions.
  • the inorganic fiber material suitable for use in the winding fill material 16 described herein can have a length of from 1 mm to 6 mm, and a diameter of from 3 microns to 12 microns. Fibers segments having a length below this range will have an unsuitably low tensile strength and poor sealing properties. Fiber segments having a length above this range may have improved tensile strength, but the resulting gaskets may have unsatisfactory leak rates. Use of fibers having a diameter below the 3 micron to 12 micron range presents safety issues, such as allowing for inhalation of fibers.
  • RCFs include refractory ceramic fibers (RCF) and alkaline earth silicates.
  • RCFs include kaolin clay-based blends of alumina and silica with metal oxides and high purity blends of silica and alumina.
  • An example of a commercially available RCF suitable for use in the winding fill material 16 described herein is Fiberfrax bulk fiber, manufactured by Unifrax of Niagra Falls, N.Y.
  • Alkaline earth silicates, also known as high-temperature glass wools include amorphous fibers that are produced by melting combinations of CaO—, MgO—, SiO 2 , and ZrO 2 .
  • An example of a commercially available alkaline earth silicate suitable for use in the winding fill material 16 described herein is Superwool bulk fibers, manufactured by Thermal Ceramics of August, Ga.
  • the organic binder is generally present in the winding fill material 16 in the range of from 1 wt % to 5 wt %.
  • the organic binder is latex.
  • Exemplary latex emulsions suitable for use in the winding fill material 16 described herein include acrylics, nitrile elastomers, styrene butadiene rubber, ethylene vinyl acetate copolymers, and polyvinyldiene chloride.
  • nitrile elastomers are preferred. Suitable nitrile elastomers include nitrile butadiene rubber (NBR) or styrene butadiene rubber (SBR).
  • An example of a commercially available nitrile elastomer suitable for use in the winding fill material 16 described herein is Nychem, manufactured by Emerald Performance Materials of Cuyahoga Falls, Ohio.
  • An example of a commercially available NBR suitable for use in the winding fill material 16 described herein is Hycar 1572, manufactured by Lubrizol of Wickliffe, Ohio.
  • An example of a commercially available SBR suitable for use in the winding fill material 16 described herein is GenFlo, manufactured by Omnova of Fairlawn, Ohio.
  • the binder is an organic material
  • the amount of organic material in the winding fill material 16 is limited to limit the burn off of organic material at extreme temperatures and the subsequent formation of leak paths. Accordingly, in some embodiments, the amount of organic material present in the winding fill material 16 is limited to no more than 5 wt %, and in some cases, no more than 3 wt %. While other previously known winding fill materials have limited the amount of organic material in recognition of this same problem, Applicants are unaware of any winding fill material that contains as low a quantity of organic material as in the winding fill material 16 disclosed herein.
  • the winding fill material 16 further includes a flocculant.
  • the flocculant aids in the formation of aggregates from individual particles.
  • Flocculants generally include various molecular weight anionic, nonionic, or cationic polymers.
  • the flocculants carry active groups with a charge that counterbalance the charge of the individual particles. Flocculants adsorb on particles and cause destabilization either by bridging or charge neutralization.
  • the flocculant used in the winding fill material 16 described herein is cationic because the binder and filler are anionic.
  • the flocculant used in the winding fill material 16 described herein can be from the polyacrylamide, polyethylene-imine, polyamides-amine, or polyamine group.
  • the preferred flocculant is a high molecular weight polyamine because the intrinsic flocculating power increases with molecular weight.
  • An example of a commercially available flocculant suitable for use in the winding fill material 16 described herein is Superfloc, manufactured by Cytec of Woodland Park, N.J.
  • defoamer Another additive that can be included in the winding fill material 16 described herein is a defoamer.
  • the defoamer is used to control foam formed after mixing together the binder, filler, and fibers but before the winding fill material sheet is formed. Without a defoamer, an inconsistent sheet can form because the density of the slurry will not be consistent when foam is present.
  • the defoamer is a water-based emulsion defoamer. Examples of defoamers suitable for use in the winding fill material 16 described herein include DF-450 manufactured by Chemco of Ferndale, Wash., and Nalco 600096 ANTIFOAM manufactured by Nalco of Naperville, Ill.
  • the winding fill material 16 described above can be difficult to form due to the components used and the amount of certain components used. Accordingly, in some embodiments, a method for manufacturing the winding fill material 16 described above is provided. The method generally includes preparing a talc slurry, preparing a sheet slurry using the talc slurry, forming a pre-densified gasket sheet from the sheet slurry, and densifying the gasket sheet to form the winding fill material 16 .
  • the initial step of forming a talc slurry is carried out at least in part because the hydrophobic filler (e.g., talc) can be difficult to wet down.
  • the hydrophobic filler e.g., talc
  • the talc may not completely wet down in the sheet slurry and may not be completely mixed into the sheet slurry.
  • the talc will then mix sufficiently with the binder and fiber when preparing the sheet slurry.
  • parameters of the mixing step discussed below can be adjusted to prepare a talc slurry that is suitable for use in the method described herein.
  • certain parameters will require adjusting based on, for example, specific mixing equipment used.
  • parameters that can be adjusted include: the shape and size of the mixing bowl; the number, shape and size of mixing blades; the number, shape, and size of baffles in the mixing bowl; mixing speeds; mixing times; mixer design (e.g., kettle, tumble, batch); and the amount of water used in the mixing step.
  • preparing the talc slurry generally includes adding the talc to water in stages and mixing the talc and water.
  • the total amount of talc required can be divided into two quantities, with the first quantity being added to a quantity of water and mixed for a period of time, followed by adding the second quantity of talc to the mixture formed from the first quantity of talc and water.
  • talc is added to water while mixing, such as through the use of a mixing blade.
  • the first quantity of talc is added to the water while a mixing blade mixes the water
  • the second quantity of talc is added to the mixture formed from the water and first quantity of talc while a mixing blade mixes the mixture.
  • the mixing may be conducted by feeding a continuous amount of talc at a rate sufficient to allow complete mixing.
  • the mixing of the water and talc can be carried out in any suitable mixing device, such as an industrial mixer.
  • a quantity of water is added to the mixing bowl of an industrial mixer, and the mixing blade is turned on.
  • a first quantity of talc is then added into the mixing bowl while the mixing blade operates to mix the water and the talc being added into the mixing bowl.
  • Mixing the first quantity of talc is carried out for a period of time, which may be for as little time as about 1 minute, followed by the addition of a further quantity of talc and further mixing.
  • the mixing is carried out at a reduced speed until all of the talc has been added, at which time the speed of the mixing is increased.
  • the mixing device includes a sprayer that is capable of spraying water at the sides of the mixing bowl and the mixing blade to wash off any dry talc adhered thereto and add the talc to the slurry forming in the mixing bowl. In some embodiments, these spraying steps occur while the mixing continues to take place. Multiple spraying steps can be carried out during the mixing process.
  • a first spraying step can occur after all of the talc has been added to the mixing bowl, followed by mixing for a period of time, such as 30 minutes to 1 hour, and then another spray step can be carried out before mixing the slurry for an additional period of time, such as 45 minutes to 90 minutes.
  • the speed of the mixing blade is reduced after the second spraying step, such that the mixing that occurs after the second spraying step is carried out a slower mixing speed then the mixing speed after the first spraying step. Notice the times provided herein should not be considered limiting, but rather, exemplary.
  • the talc slurry formed in the above step will be from 10 wt % to 40 wt % talc and from 60 wt % to 90 wt % water.
  • the entire mixing process can take place over a period of time ranging from 5 to 150 minutes, for example. The longest periods of mixing take place between spray steps and after the final spray step.
  • the mixing blade is generally started at half speed and increases from half speed to full speed after all of the talc has been added to the mixing bowl. The speed may then be reduced from full speed to half speed after the final spray step has occurred. Once the mixing has occurred and the talc slurry is formed, the mixing blade can be turned off and the talc slurry can be removed from the mixing device.
  • a separate talc slurry is not prepared prior to introducing the fiber and binder into the slurry. Rather, the talc, fiber, and binder all mixed together at once with a quantity of water.
  • the slurry is from 97% to 99.8% water and from 0.2% to 3% solids material, with the solids material component of the slurry being from 85% to 95% talc, from 6% to 9% fiber, and from 2% to 5% binder.
  • Advantages of preparing a single slurry of talc, fiber, and binder include only having to have one set of mixing equipment and less transfer equipment since there is no need to transfer talc slurry from one tank to another, while disadvantages include inconsistent mixing of the slurry (vigorous mixing is required to mix the hydrophobic talc, but also causes the fiber to clump).
  • a sheet slurry is formed using the talc slurry and the other components of the winding fill material 16 .
  • the sheet slurry is formed by adding fiber to water and mixing for a period of time, adding the talc slurry to the mixture of water and fiber, adding the binder to the mixture, and optionally adding any additives, such as flocculant and defoamer.
  • any additives such as flocculant and defoamer.
  • the preparation of the sheet slurry generally begins by mixing fiber and water. This step is performed first because the fiber disperses better in the water when no other solids (such as the binder) are present in the water.
  • the mixing of the fiber and water can be carried out in a similar manner as the mixing of talc and water described above.
  • An industrial mixer can be used, in which case the water is added to the mixing bowl, the mixing blade is started, and the fiber is mixed in with the water as the mixing blade operates.
  • the mixing blade will be operated at full speed (e.g., 40 Hz) when the fiber is added to the mixing bowl to mix with the water.
  • the mixing of the fiber and water can take place for a relatively short period of time, such as for about 30 seconds to 10 minutes.
  • the mixture of fiber and water generally includes from 0.01 wt % to 5 wt % fiber and from 95 wt % to 99.99 wt % water. In some embodiments, the mixture is 0.03 wt % fiber and 99.97 wt % water.
  • the mixing is temporarily stopped after the initial mixing of the fiber and water. This may be due to clumping of the fiber that occurs during the initial mixing step. Accordingly, the mixing can be stopped in order to declump the fiber. Any technique suitable for declumping the fiber can be used, such as use of water spray. After declumping has occurred, the mixing blade can be started again and run for an additional period of time. In some embodiments, the mixing is brought back up to full speed after recommencing mixing and the post-declumping mixing of the fiber and water is carried out for about 1 to 10 minutes. Following the mixing of the fiber and water, the talc slurry is added to the mixture of fiber and water.
  • the talc slurry is added to the mixture while mixing continues at full speed, although less than full mixing speed is possible. Once the talc slurry is added, the mixing may be carried out for about 3 to 20 minutes. In some embodiments, it may be useful to raise the level of the mixing blade after the talc slurry has been added.
  • the binder is added to the mixture.
  • the speed of the mixing blade may be decreased to, for example, about half speed (e.g., 20 Hz). Generally speaking, the mixing blade speed should be reduced to 30 Hz or below. If mixing continues at full speed when the binder is added, or even at greater than about 30 Hz, the binder tends to foam up. Accordingly, slowing the speed of the mixing blade so that the binder is blended in to the mixture rather than mixed into the mixture can prevent foaming.
  • the mixture of water, fiber, talc slurry and binder is mixed for a relatively short period of time before adding the next component of the sheet slurry, such as for about 10 to 90 seconds.
  • additives such as the flocculant and defoamer can be added into the slury.
  • the additives can be added in any order.
  • flocculant is added before defoamer.
  • the additives are added while the mixing blade operates at half speed. A relatively short period of time follows the addition of each additive, such as 0.5 minutes of mixing following the addition of flocculant and 0.5 minutes of mixing following the addition of defoamer.
  • a pre-densified gasket sheet is formed from the sheet slurry.
  • the pre-densified gasket sheet can be prepared using a non-woven sheet former specifically designed for forming sheets from the sheet slurry described above.
  • the non-woven sheet former can generally include three sections: an upper section, a filter media, and a lower section.
  • the upper section and the lower section generally enclose the filter media, and in some embodiments the lower section is stationary while the upper section can be separated from the lower section to, for example, access the filter media.
  • the overall shape and size of the non-woven sheet former is not limited, and can be varied based on the desired size and shape of the sheet to be formed by the non-woven sheet former. In some embodiments, the shape of the non-woven sheet former is generally rectangular to thereby form rectangular sheets.
  • water is introduced into the non-woven sheet former prior to adding the sheet slurry.
  • the water such as, for example, about 3 to 4 inches of water, can serve as a cushion for the slurry being pumped into the non-woven sheet former. Without the water cushion, fiber clumps can form when the slurry contacts the filter media.
  • the level of water in the non-woven sheet former is higher than the filter media. The sheet slurry can rest on top of the water, and as the water is drained out of the non-woven sheet former, the sheet slurry lowers on top of the filter media.
  • the filter media located in the enclosed space between the upper portion and lower portion of the non-woven sheet former can generally include a screen and filter paper positioned on top of the screen.
  • the filter media partitions the enclosed space into an upper portion and a lower portion.
  • the slurry deposited into the non-woven sheet former will rest on top of the filter paper and screen, as the slurry is too thick to pass through.
  • the filter paper remains with the pre-densified sheet formed in the non-woven sheet former to provide additional structural support to the pre-densified sheet when it is removed from the non-woven sheet former.
  • the mesh size of the filter media can be selected to allow water to pass through the filter media but to prevent the passage of the sheet slurry through the filter media.
  • the mesh size of the filter media also can be selected to prevent the passage of both the filler and the fiber in the sheet slurry through the filter media. If the mesh size of the filter media is such that filler can pass through, the fiber content of the pre-densified sheet formed on the filter media will be too high.
  • the lower portion of the non-woven sheet former can be stationary and generally includes a drain and vacuum pump to pull water located in the upper portion of the enclosed space down through the filter media and out of the non-woven sheet former. Removing the water through the drain and via the use of the vacuum pump results in the formation of the pre-densified gasket sheet.
  • the sheet slurry deposited on the filter media Prior to removing water through the drain of the lower portion, the sheet slurry deposited on the filter media is dispersed evenly on the filter media.
  • a disperser paddle can be used to accomplish this, and the result is an evenly distributed layer of sheet slurry on the filter media.
  • the disperser paddle is a plunger.
  • the sheet slurry that is transferred into the non-woven sheet former tends to enter into the non-woven sheet former in a swirling manner. By plunging the plunger into the deposited slurry, the swirling action is stopped and the slurry disperses evenly on top of the filter media.
  • the drain in the lower section is opened to begin the removal of water from inside the non-woven sheet former.
  • Water above the filter media is capable of passing through the filter media, and therefore opening the drain leads to water above the filter media passing through the filter media and out of the drain in the lower section of the non-woven sheet former.
  • the drain is opened for a relatively short period of time to allow water to flow out of the lower section, such as for 0.5 minutes.
  • the vacuum pump can be turned on to further remove water from inside of the non-woven sheet former and form the pre-densified sheet. In some embodiments, the vacuum pump is operated for about 4 minutes.
  • the pre-densified sheet can be removed from the non-woven sheet former.
  • the upper portion can be raised to allow for the pre-densified sheet to be removed.
  • the pre-densified sheet can be removed with the filter paper still attached to the sheet in order to provide support to the pre-densified sheet.
  • pre-densified sheet formation step Various characteristics of the pre-densified sheet formation step described above can be adjusted based on a variety of factors, such as the specific materials being used and prior processing steps. Examples of parts of the pre-densified sheet formation step that can be adjusted include, but are not limited to, the type of filter media used, the method of adding the slurry into the non-woven sheet former, the method of dispersing the slurry within the non-woven sheet former, and the amount of water removed from the non-woven sheet former prior to removing the pre-densified sheet.
  • a final step in the method of making the winding fill material 16 involves densifying the sheet.
  • Densifying generally includes applying heat and pressure to the pre-densified sheet.
  • a hydraulic press is used to densify the sheet.
  • Heat can be applied in a range of from 300 to 400° F.
  • the pressure can be applied in a range of from 700 psi to 800 psi.
  • the application of heat and pressure can be carried out for around 7 to 10 minutes, and the finished densified product can have a density in the range of from 85 to 95 ft/lb 2 .
  • a release film is placed on the top and/or bottom of the sheet prior to densification.
  • the release film can be, for example, PET coated with silicone.
  • Densification can also be carried out via calendaring. Densification can be carried out on a continuous or batch basis.
  • the process of manufacturing the winding fill material 16 is a continuous process, such a continuous wet lay process.
  • the continuous wet lay process is similar to traditional paper making processes that use a Fourdrinier machine.
  • the continuous wet lay process can begin with the preparation of a sheet slurry.
  • the preparation of the gasket sleet slurry can be similar or identical to the sheet slurry preparation steps described above in greater detail.
  • the sheet slurry can be prepared by first preparing a talc slurry, followed by adding the fiber and binder to the talc slurry to produce the sheet slurry.
  • the talc, fiber, and binder and be mixed together at the same time with water to create the sheet slurry.
  • the sheet slurry provided at the beginning of the continuous wet lay process will include from 2% to 5% solid material.
  • an initial step of diluting the sheet slurry is carried out in order to reduce the solid content of the sheet slurry to within the range of from 0.5% to 3%. Diluting the sheet slurry can be performed by adding a further amount of water to the sheet slurry. In some embodiments, this dilution step can take place in the headbox of a Fourdrinier machine. It is preferable to dilute the sheet slurry to within this range of solid material because excessive solid content will result in winding fill material 16 that is too wet and thick. It is also preferred not to dilute the sheet slurry below 0.5% solid material because too high a water content will result in the winding fill material 16 being thin and weak.
  • the diluted sheet slurry is continuously transferred onto a continuously running wire mesh conveyor belt.
  • Any suitable manner of transferring the diluted sheet slurry onto the wire mesh conveyor belt can be used, although it is preferable that the manner of transferring the diluted sheet slurry provide for a generally uniform distribution of diluted sheet slurry on to the wire mesh conveyor belt.
  • a Fourdrinier machine will include the appropriate mechanism for transferring the diluted sheet slurry from the headbox to the wire mesh conveyor belt.
  • the mesh size of the wire mesh conveyor belt is a parameter of the process that can be adjusted to alter the characteristics of the gasketing material produced by the continuous wet lay process.
  • the mesh size of the wire mesh conveyor belt is in the range of from 24 to 32 (number of openings per square inch in both the vertical and horizontal direction).
  • the mesh size is larger, the slurry may be capable of falling through the conveyor belt.
  • the mesh size is smaller, the removal of water from the slurry in later processing steps may be inhibited.
  • the speed at which the conveyor belt travels is another parameter of the process that can be adjusted to alter the characteristics of the gasketing material produced by the continuous wet lay process.
  • the conveyor belt is operated at a speed in the range of from 2 ft/min to 5 ft/min. Speeds outside of this range may remove excessive amounts of water from the slurry (such as when the speed is lower than this range), or may remove insufficient amounts of water from the slurry (such as when the speed is higher than this range).
  • the wire mesh conveyor belt travels over one or more suction boxes, which operate to pull water down and out of the diluted sheet slurry being carried by the conveyor belt.
  • Any suction boxes use a mild vacuum to pull the water down through the wire mesh conveyor belt.
  • Any suitable number of suction boxes can be used, and the suction boxes can be located under the entire length of the conveyor belt.
  • the conveyor belt passes the sheet slurry through a press section, which acts to remove additional water from the slurry while also flattening and smoothing the slurry.
  • the press section can include one or more rollers through which the conveyor belt passes. When a Fourdrinier machine is used, the pressing can be accomplished with the use of a Dandy roll.
  • the slurry is carried by the conveyor belt through a drying zone, which aims to reduce the water content of the slurry down to about 5%.
  • the drying zone may include steam heated rollers.
  • the steam heated rollers are heated to a temperature of between 400 and 500° F.
  • the slurry may be sufficiently dried and altered such that the winding fill material 16 is formed.
  • Various additional processing steps can be carried out to further finalize the formation of the winding fill material 16 .
  • One such processing step is the calendaring of the material on the wire mesh conveyor belt. Calendaring can include passing the conveyor belt having the sheet material disposed thereon through a series of rollers in order to smooth the material and provide the material with a more uniform thickness.
  • the wire mesh conveyor described above is positioned at an incline of from 15° to 35° in order to improve the removal of water from the slurry.
  • the a portion of the water content of the slurry remains in behind while the slurry travels upward to be exposed to the various process steps described above, including drying via suction boxes and heated rollers and pressing the slurry material.
  • the drainage steps can be increased, such as by increasing the vacuum pressures traditionally applied.
  • the wire mesh conveyor provides more support than is provided in traditional non-woven paper making processes due to the lower than normal wet tensile strength of the pre-densified sheets.
  • throughput dryers can be used in place of canister dryers. The throughput dryers can be preferable due to the lower than normal wet tensile strength of the pre-densified sheets.
  • a discreet method uses molds to form sheets of various shapes and sizes.
  • the discreet method can be similar to traditional pulp molding processes used in the paper making industry.
  • the sheet slurry described above can be sucked into fine-mesh screens having various shapes and configurations, followed by removing and drying the slurry shaped by the screens.
  • the sheet slurry is slightly modified when a discreet method is used.
  • the latex binder can be substituted with a solvent-based elastomer.
  • Extrusion processing also can be used to manufacture the winding fill material 16 described herein.
  • traditional extrusion apparatus used in ceramics are used to force the sheet slurry through a die and create shaped winding fill material 16 .
  • the latex binder in the sheet slurry can be replaced with solvent-based elastomer when using an extrusion process to form the winding fill material 16 .
  • the winding fill material 16 is made using a process similar or identical to a silk screen process.
  • the process involves providing the sheet slurry (possibly in a thicker consistency) and spreading the sheet slurry over a hole having a specified shape. The slurry will fill the shaped hole and can then be treated further to form a gasket having the shape of the hole.
  • the winding fill material 16 is made using a process similar to injection molding processes.
  • Discrete winding fill material 16 is made by preparing a paste instead of a slurry.
  • a paste can be prepared by using less water in the slurry preparation steps described above. The paste is pushed into a heated barrel after which it is augured into a heated mold using, for example, a screw-type plunger. Once the cavity of the mold is filled, the holding pressure is maintained to compensate for the evaporation of water.
  • the winding fill material 16 is made from a compression molding process. In such a process, sheet slurry is packed in the negative section of a die, heated in an oven, and then pressed at an elevated temperature and pressure using the positive section of the die. The result is winding fill material 16 having the shape of the die used in the compression molding process.
  • the slurry packed in the negative section of the die can be similar or identical to the sheet slurry described in greater detail above, and can also be prepared according to the slurry preparation steps provided above.
  • the slurry is drained prior to being disposed in the negative section of the die. Draining the slurry can include placing the slurry on a mesh screen to allow water to drain down and out of the slurry for a period of time. Any mesh screen capable of allowing water but not the slurry to fall through the screen can be used.
  • the manner of disposing the slurry material into the negative section of the die is not limited, and can include either pouring the slurry into the die with no compression or packing steps, or pouring the slurry into the die followed by packing down the slurry and optionally adding additional slurry into the negative section of the die.
  • the amount of slurry disposed in the negative section of the die is an amount less than will fill the entire cavity of the negative section of the die.
  • the die can be made from, for example, stainless steel.
  • the shape of the die is not limited, and can be selected based on the equipment with which the resulting gasket will be used. In some embodiments, the die will have an elongate configuration to thereby produce strip shaped-gaskets.
  • a heating step is carried out.
  • the die can be an oven and exposed to elevated temperatures for a period of time.
  • the elevated temperature is in the range of from 200° to 250° F. (preferably 212° F.).
  • the die is in the oven for a period of from 1 to 3 hours (preferably 2 hours).
  • the heating step works to further remove water from the slurry and move towards the creation of a gasket sheet material.
  • the positive section of the die can be inserted into the negative section of the die to apply pressure on the winding fill material 16 inside the negative section of the die.
  • the pressure applied by the positive section can be in the range of from 700 psi to 900 psi (preferably 750 psi). Elevated temperatures can also be applied during this step, including by providing heat through the positive section of the die. In some embodiments, the application of pressure is carried out at temperatures in the range of from 250° to 350° F. (preferably 300° F.).
  • winding fill material 16 in the shape of the die will be formed.
  • the winding fill material 16 will have a density that is about double the density of the pre-molded material.
  • the winding fill material 16 can be removed from the die and subjected to any final processing steps, such as further shaping or smoothing of the winding fill material 16 .
  • the winding fill material 16 is slit (or otherwise formed as described above) into elongated strips.
  • the strips may be dimensioned to accommodate the particular parameters of the desired spiral wound gasket 10 .
  • the winding fill material 16 is formed into 0.12 inch strips that are approximately 8 feet long.
  • the strips of winding fill material 16 are positioned against lengths of the metal banding 14 .
  • the thickness of the metal banding 14 is approximately 0.007 inches; however, the thickness of the metal banding 14 may range from about 0.006 inches to about 0.008 inches thick.
  • the width of the metal banding 14 will vary according to the application.
  • the metal banding 14 and winding fill material 16 are wound around a form or mandrel that is dimensioned to produce the desired diameter spiral in the overlying turns of the resilient spiral core 15 .
  • the first two windings are spot welded around the circumference.
  • Some embodiments will employ a minimum of three spot welds, which are not separated by more than 3 inches.
  • the outside diameter may be spot welded with three welds.
  • the last weld will be the terminal weld.
  • the distance from the terminal weld to the first weld in some embodiments, will be no more than 1.5 inches.
  • spiral wound gasket 10 may be provided with either or both of an outer guide ring 18 and an inner guide ring 20 .
  • embodiments of the spiral wound gasket 10 couple the outer guide ring 18 with the outer periphery of the sealing element 12 .
  • the structures may be coupled with an interference fit.
  • the structures may be coupled to one another using other mechanical connection methods, including slotted joints.
  • An inner guide ring 20 may be provided to extend radially inward from an inner periphery of the sealing element 12 and coupled therewith in a manner similar to the connection between the outer guide ring 18 and the outer periphery of the sealing element sealing element 12 . In the embodiments such as that depicted in FIGS.
  • the thickness of the outer guide ring is typically provided between approximately 0.117 inches and 0.131 inches; however, the thickness of the outer guide ring 18 may be provided according to the parameters of the chosen application.
  • the depicted spiral wound gasket 10 includes an inner guide ring 20 with a thickness of between approximately 0.117 inches and 0.131 inches; however, the thickness may be provided according to the parameters of the chosen application. The thickness of either or both of the outer guide ring 18 and inner guide ring 20 will be dictated by the thickness of the metal banding 14 and the degree of over-compression protection desired.
  • outer guide ring 18 and inner guide ring 20 will be dictated by the desired application of the spiral wound gasket 10 and the dimensions of the opposing surfaces that will sandwich the spiral wound gasket 10 .
  • outer guide rings 18 and inner guide rings 20 formed from 316 stainless steel.
  • other materials such as Inconel or other high temperature metallurgies may be used, depending on the desired applications and manufacturing cost limits.
  • Winding fill materials that are resistant to degradation at elevated temperatures are typically less likely to adhere and bind together.
  • a sealing face may be created by winding fill material 16 being extruded from between the spirally wound metal banding 14 .
  • winding fill material 16 does not possess the inherent ability to adhere to form an opposing sealing face, sealing degrades.
  • the extruded sealing face tends to be of lesser quality when using high temperature winding fill materials due to the material properties of high temperature fillers.
  • More standard industrial filler materials, such as graphite extrude to form an extruded sealing face that is an effective sealing surface.
  • graphite is not suitable for applications of continuous temperature above 850° F. in oxidizing atmospheres, or extended temperature forays above 900° F.
  • various embodiments of the spiral wound gasket include one or more layers of facing material 30 .
  • a layer of facing material 30 may be secured to one or both of the axial faces 32 of the sealing element 12 .
  • the layers of facing material may be secured with the axial faces 32 with binders, such as one of the various commercially available spray adhesives.
  • binders such as one of the various commercially available spray adhesives.
  • other securement methods including mechanical press fit and encapsulating are contemplated.
  • the thickness of the layers of facing material 30 is approximately 0.010 inches; however, the thickness of the layers of facing material 30 may range from about 0.004 inches to about 0.020 inches thick.
  • the width of the layers of facing material 30 will generally be dictated by the gasket width.
  • the layers of facing material 30 may be provided using various ratios of inorganic filler, inorganic fiber, and organic binder.
  • embodiments of the layers of facing material 30 use talc as the inorganic filler in a range from 60% to 90% by weight.
  • Inorganic fiber content for some such embodiments of the layers of facing material 30 is from 1% to 14% by weight.
  • organic binder content for embodiments of the layers of facing material 30 is from 1% to 8% by weight.
  • the layers of facing material 30 may be provided to include greater than 60% by weight talc, less than 20% by weight inorganic fiber, and less than 5% by weight organic binder.
  • Other embodiments of the layers of facing material 30 include 75 to 90 wt % inorganic filler, 5 to 20 wt % inorganic fiber, and 1 to 5 wt % organic binder.
  • the layers of facing material 30 are formed to include approximately 90% by weight talc, 7% by weight inorganic fiber, and 3% by weight organic binder.
  • the layers of facing material 30 are formed as a pair of annular rings that are cut from a compressed sheet in one of various known cutting methods known in the industry. Other methods of forming, including but not limited to those described above, (such as continuous wet lay processes, extrusion molding, injection molding, discreet molding methods, and processes similar to a silk screen processes, may be used to fabricate the final form of the layers of facing material 30 .
  • the layers of sealing material 30 are formed to have substantially uniform thickness and density. While the layers of facing material are depicted as being ring-shaped, the layers may be formed in nearly any shape to accommodate the axial faces 32 of the sealing element 12 .
  • the layers of facing material 30 are adhered to the axial faces 32 of the sealing element 12 using spray adhesive, or other suitable adhesives for the anticipated applications for the spiral wound gasket 10 .
  • the adhesive is applied either to the layers of sealing material 30 or to the axial faces of the sealing element 12 .
  • the layers of facing material 30 may by mechanically coupled with the axial faces of the sealing element 12 by creating a mechanical bond between the facing material and the surface of the sealing element. This can be accomplished by pressing the facing material into the axial surface of the seal to encourage the materials to mesh and weakly bond.
  • the spiral wound gasket 10 includes a resilient sealing element 12 that includes spirally wound, alternating layers of metal banding 14 to define a resilient spiral core 15 . However, no winding fill material 16 is disposed between the layers of metal banding 14 .
  • embodiments of the spiral wound gasket 10 will include an outer guide ring 18 that extends radially outward from an outer periphery of the sealing element sealing element 12 .
  • Some embodiments of the spiral wound gasket 10 will include an inner guide ring 20 that extends radially inward from an inner periphery of the sealing element 12 . It is contemplated that various applications of the spiral wound gasket may require the use of either, both, or neither of the outer guide ring 18 and the inner guide ring 20 .
  • a layer of facing material 30 may be secured to one or both of the axial faces 32 of the sealing element 12 .
  • comparative testing of different spiral wound gaskets was performed to determine sealability at operational temperatures of approximately 600° F. after a 24 hour 1000° F. bake. This test mimics an accepted high temperature leakage test performed by a major petrochemical entity. Specifically, test flanges were each fit with one of five different spiral wound gaskets that included different filler and facing materials. A first gasket (industry standard graphite) included standard graphite filler material.
  • a second gasket used a filler material according to the present technology, which included filler material having a formulation of: talc filler, in a range from 60% to 90% by weight; a fiber, from 1% to 14% by weight; and a binder, from 1% to 8% by weight.
  • a third gasket (filler # 2 ) included a filler material formed from the same material used for filler # 1 but is provided with a thickness of 0.04 inches, whereas the sample in filler # 1 had a thickness of 0.23 inches.
  • a fourth gasket (competitor sample) included a filler material primarily formed from vermiculite.
  • a fifth gasket (filler # 1 without facing material) used a filler material with a composition similar to the second gasket.
  • the facing material was not applied.
  • the samples were charged with Nitrogen and brought to testing temperatures (between 600° F. and 1200° F.) and Nitrogen leakage was monitored and recorded. It can be seen that the second gasket, having a talc filler material and facing, consistently outperformed the other sample gaskets. It should be appreciated, however, that operational temperatures of this gasket may exceed 1000 C and is not bounded.
  • sample data is shown that demonstrates tensile strength and sealability as a function of fiber content in the formula for one embodiment of the facing material.
  • trend lines indicate that formulations of the facing material having 25% fiber and below equate to greater sealing quality.
  • a stated range of 1 to 10 should be considered to include and provide support for claims that recite any and all subranges or individual values that are between and/or inclusive of the minimum value of 1 and the maximum value of 10; that is, all subranges beginning with a minimum value of 1 or more and ending with a maximum value of 10 or less (e.g., 5.5 to 10, 2.34 to 3.56, and so forth) or any values from 1 to 10 (e.g., 3, 5.8, 9.9994, and so forth).

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  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
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US13/645,320 2011-10-04 2012-10-04 Spiral wound gasket Abandoned US20130082447A1 (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
US13/645,320 US20130082447A1 (en) 2011-10-04 2012-10-04 Spiral wound gasket
JP2015532182A JP2015535911A (ja) 2012-09-19 2013-09-19 渦巻形ガスケット
CA2885031A CA2885031A1 (en) 2012-09-19 2013-09-19 Spiral wound gasket
SG11201501841SA SG11201501841SA (en) 2012-09-19 2013-09-19 Spiral wound gasket
KR1020157008971A KR102224000B1 (ko) 2012-09-19 2013-09-19 와권 가스켓
PCT/US2013/060729 WO2014081501A1 (en) 2012-09-19 2013-09-19 Spiral wound gasket
EP13857509.7A EP2898249A4 (en) 2012-09-19 2013-09-19 SPIRAL WOVEN SEAL
BR112015006008A BR112015006008A2 (pt) 2012-09-19 2013-09-19 gaxeta enrolada em espiral
MX2015003502A MX2015003502A (es) 2012-09-19 2013-09-19 Junta en espiral.
CN201380060248.0A CN104797872A (zh) 2012-09-19 2013-09-19 螺旋缠绕式衬垫
US15/991,789 US10955055B2 (en) 2011-10-04 2018-05-29 Spiral wound gasket

Applications Claiming Priority (4)

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US13/252,718 US9234589B2 (en) 2010-10-20 2011-10-04 Extreme temperature gasket and method of making the same
US13/252,788 US9732855B2 (en) 2010-10-20 2011-10-04 Extreme temperature gasket and method of making the same
US201261703121P 2012-09-19 2012-09-19
US13/645,320 US20130082447A1 (en) 2011-10-04 2012-10-04 Spiral wound gasket

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US13/252,718 Continuation-In-Part US9234589B2 (en) 2010-10-20 2011-10-04 Extreme temperature gasket and method of making the same

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US15/991,789 Continuation US10955055B2 (en) 2011-10-04 2018-05-29 Spiral wound gasket

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EP (1) EP2898249A4 (pt)
JP (1) JP2015535911A (pt)
KR (1) KR102224000B1 (pt)
CN (1) CN104797872A (pt)
BR (1) BR112015006008A2 (pt)
CA (1) CA2885031A1 (pt)
MX (1) MX2015003502A (pt)
SG (1) SG11201501841SA (pt)
WO (1) WO2014081501A1 (pt)

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WO2014081501A1 (en) 2014-05-30
US20180274680A1 (en) 2018-09-27
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CA2885031A1 (en) 2014-05-30
JP2015535911A (ja) 2015-12-17
MX2015003502A (es) 2015-07-17
EP2898249A1 (en) 2015-07-29
US10955055B2 (en) 2021-03-23
KR20150056579A (ko) 2015-05-26
KR102224000B1 (ko) 2021-03-08
BR112015006008A2 (pt) 2017-07-04
EP2898249A4 (en) 2016-05-04

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