US2505045A - Filamentary product and method of its production - Google Patents
Filamentary product and method of its production Download PDFInfo
- Publication number
- US2505045A US2505045A US40816A US4081648A US2505045A US 2505045 A US2505045 A US 2505045A US 40816 A US40816 A US 40816A US 4081648 A US4081648 A US 4081648A US 2505045 A US2505045 A US 2505045A
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- US
- United States
- Prior art keywords
- mat
- filaments
- adjacent
- layers
- binder
- Prior art date
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- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 15
- 238000004519 manufacturing process Methods 0.000 title description 4
- 239000011230 binding agent Substances 0.000 description 36
- 239000011521 glass Substances 0.000 description 12
- 230000001154 acute effect Effects 0.000 description 11
- 239000000428 dust Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000003292 diminished effect Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000004925 Acrylic resin Substances 0.000 description 3
- 229920000178 Acrylic resin Polymers 0.000 description 3
- 229920001807 Urea-formaldehyde Polymers 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 230000000979 retarding effect Effects 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- GZCGUPFRVQAUEE-SLPGGIOYSA-N aldehydo-D-glucose Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O GZCGUPFRVQAUEE-SLPGGIOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 229920001187 thermosetting polymer Polymers 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000012840 feeding operation Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 235000019422 polyvinyl alcohol Nutrition 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B26/00—Compositions of mortars, concrete or artificial stone, containing only organic binders, e.g. polymer or resin concrete
- C04B26/02—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
- C04B2111/00612—Uses not provided for elsewhere in C04B2111/00 as one or more layers of a layered structure
-
- 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
- Y10T156/1007—Running or continuous length work
- Y10T156/1016—Transverse corrugating
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24058—Structurally defined web or sheet [e.g., overall dimension, etc.] including grain, strips, or filamentary elements in respective layers or components in angular relation
- Y10T428/24074—Strand or strand-portions
- Y10T428/24083—Nonlinear strands or strand-portions
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24058—Structurally defined web or sheet [e.g., overall dimension, etc.] including grain, strips, or filamentary elements in respective layers or components in angular relation
- Y10T428/24074—Strand or strand-portions
- Y10T428/24091—Strand or strand-portions with additional layer[s]
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24479—Structurally defined web or sheet [e.g., overall dimension, etc.] including variation in thickness
- Y10T428/2457—Parallel ribs and/or grooves
-
- 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
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2913—Rod, strand, filament or fiber
- Y10T428/2933—Coated or with bond, impregnation or core
- Y10T428/2964—Artificial fiber or filament
Definitions
- the product suitably contains a minor proportion of a binder which re-. tains the filaments thereof in their positions and bonds the whole into a unitary body.
- the product is of particular utility as an air filter medium.
- Thesurface of less density and more open texture is employed as the air entry side of the filter and, as the'dust-laden air enters the body, the coarse dust, lint and the like are removed.
- the finer dust is progressively deposited, the relatively dense structure adjacent the opposite surface forming a final clean-up section to remove any remainder of the dust.
- the single unit is thus comparable to a series of filters of varying dustremoval characteristics. By removing the coarse dust and lint in the more open section, it is possible to obtain a greatly increased dust retention capacity before resistance to air flow becomes excessive. It will be appreciated, however, that the product may find other fields of usefulness than.
- Another object of the invention is the provision of a multi-layer, glass filament mat pulled or expanded in the direction of its thickness comprising a plurality of layers having substantially parallel corrugations or undulations, the undutween the two extremes.
- Fig. 1 is a perspective view of a segment of an expanded product in accordance with the instant invention
- Fig. 2 is a view similar to Fig. 1 illustrating a modified embodiment
- Fig. 3 is a diagrammatic, end elevational view of an apparatus employed in preparing the initial mat from which the instant structure is derived;
- Fig. 4 is a diagrammatic, front elevational view of the apparatus of Fig. 3;
- Fig. 5 is a plan view of the mat as made on the apparatus of Figs. 3 and 4;
- Fig. 6' is a diagrammatic, elevational View of the apparatus embodying the instant invenion;
- Fig. 7 is a top plan view of the apparatus of
- Fig. 8 illustrates a modified construction of a portion of the apparatus.
- a product of the instant invention consists of a body in composed of a plurality of layers l2, each formed of continuous, or substantially continuous glass filaments It.
- the filaments of each layer lie in approximate parallelism and the filaments of adjacent layers cross each other.
- the product is pulled or expanded in the direction of its thick- Suitabiy the product ness to produce a lightweight, low density material.
- the filamentary layers particularly those adjacent one surface of the product, the upper surface of Fig. l, are corrugated and the corrugations are brought into relatively adjacent, lateral relationship. At the same time the corrugated layers are somewhat separated, although tied together by a.
- the corrugations or undulations of the layers inwardly of the surface are gradually of lesser depth as the opposite surface is approached, the layers adjacent the opposite surface being only slightly corrugated or at least having corrugations of relatively shallow depth as compared with the layers adjacent the other surface.
- the separation between the layers also progressively decreases as the opposite surface is approached and the density of the product proportionately increases.
- Fig. 1 is diagrammatic and that in actual practice the binder particles illustrated by reference character l6 will be visually insignificant.
- the product shown in Fig. 2 is of the same character as that shown in Fig. 1 except in thb case the body has been compressed from the thickness shown in Fig. 1 and maintained in compressed state by the set binder. In this embodiment similar gradation of structure of the body is present but the body is proportionately denser throughout.
- the products described above are adapted for many uses but are particularly valuable as air filtering media as previously explained.
- the products are very lightweight and a great multiplicity of fine, intercrossing filaments form a reticulated structure well adapted to remove particulate matter from air or other gases.
- the gradual increase of density and decrease of the size of the interstices permits a graduated removal of the dust particles, the larger particles being caught or held adjacent the more open side of the filter body.
- the greatest mass of the particles E removed from the airstream by the intermediate layers and the residue of fine particles which penetrate substantially through the body are collected by the final relatively dense layers.
- the body may be used in its compressed form, particularly where finer dust particies are present. and exceptional high efilciency is required. In both forms a large filtering capacity is obtained due to the distribution of the deposited dust throughout the body.
- the products are made from the initial mat l8 (see Fig. 5), known as the condensed mat, fabricated in a substantially conventional manner by drawing a plurality of continuous glass filaments directly from the spinning orifices of the melting furnace 22 and accumulating the filaments on a drum 24.
- the drawing drum is rotated in the direction indicated by the arrow in Fig. 3 by any suitable driving means (not shown) and at a relatively high speed to continuously draw fine filaments, say, of 6 to 30 micron diameter, and wind the filaments on the drum.
- Either the furnace or the drum is reciprocated to lay the filaments on the drum in a plurality of layers of spirals with the filaments of each layer crossing the filaments of adjacent layers.
- the furnace 22 is reciprocated, as indicated by the doubleended arrow in Fig. 4.
- the rate of reciprocation relatively to the drawing speed, that is the peripheral speed of the drum, is such that the filaments of adjacent layers cross each other at acute angles.
- a binder may be applied during the filament drawing operation.
- This application may be made in any suitable way, for example by a manually operated spray device 26 (see Fig. 3), which is moved back and forth across the mat on the drum at intervals to uniformly spray the binder material onto the mat.
- the amount of binder used is carefully controlled. As will later be explained in greater detail, only a portion of the total binder content, say up to 70%, is preferably applied at this stage, the remainder of the binder being applied to the mat during later stages in the formation of the product.
- the total binder used is such that th solids binder content of the finished product is, say, 1 to 5% by weight of the product.
- the binder is preferably employed in the form of an emulsion, a water dispersion being suitable. However, a solution of the binder in a solvent may also be employed.
- the binder may be either thermosetting or thermoplastic, but thermosetting adhesives are referred. Examples of suitable matezials are acrylic resins, urea-formaldehyde resins, polyvinyl alcohols, latices, and the like. In commercial operations it has been found preferable to apply a water dispersion of an acrylic resin during the filament drawing operation and a dispersion of a urea-formaldehyde resin at the later stage.
- the binder Due to the relatively high speed movement of the mat on th drum and the temperatures prevalent during the filament drawing operation, the binder rapidl dries by evaporation of the water or solvent, as the case may be, so that, upon completion of the drawing operation, the mat contains a substantially dry but unset binder.
- the condensed mat When the condensed mat is completed, it is severed along a line of generation of the drum and is removed therefrom.
- the mat is then placed on a conveyor 28 of a feed device including a conveyor 30 mounted in a suitable manner to overlie the forward end of conveyor 28 and to yieldably engage the latter.
- a binder softener In the case of a binder such as the preferred acrylic resin, the softener is water, which in eifect again places the finely divided binder in suspension. If binders are employed of the type which cannot be practically softened with water, an appropriate solvent is used.
- the softener may be applied to the mat in the form of a spray, or a hand brush, illustrated at 32, may b employed for the purpose.
- a port-ion of the total binder content was applied to the condensed mat during the winding operation. Where this practice was followed the remainder of the binder is applied at this time.
- the added binder may be the same as that already used but suitably is a material such as a urea-formaldehyde resin. This material, in the form of a suspension, is spread on the mat on the conveyor, simila:ly as the softener.
- This apparatus in addition to feed conveyors 28 and 30, previously mentioned, includes in its preferred embodiment, a substantially level table or plate 34 having a forwardly and downwardly angling side flange 36, a
- Rolls 38 and 48 are supported to be driven at regulated speeds by suitable-means (not shown).
- An oven 42 is provided forwardly of the rolls, the oven including a conveyor 44 supported at th rear end by pulleys 48 and 48 for movement in the direction indicated by the arrow by any suitable drivin means (not shown).
- the forward end of the oven conveyor will be similarly supported.
- the conveyor is of open, gas pervious construction and suitably may be made of wire mesh material. Means are provided to heat the material carried by the conveyor. For this purpose any suitable heating system may be employed. For example,
- hot air may be circulated from a furnace (not shown) through a duct ill, the heated air being forced through the mat on the conveyor and out of the oven through duct 52.
- the condensed mat is fed forwardly, initially at an accelerated speed, between conveyors 28 and 301 until its forward edge protrudes beyond the conveyors.
- the mat [8, when placed on the feed conveyors, is positioned so that the filaments lie generally transversely of the conveyors, the feeding operation moving the mat in the direction indicated by the arrows in Fig. 6.
- the protruding forward edge of the mat is grasped, suitably by hand, and drawn or expanded into an elongated web which is passed over table 34 and roll 38 and under roll 48, and carried onto conveyor 44 where the end of the web is temporarily secured in any suitable manner, for example, by weighting it.
- Feed conveyors 38 and 28 are then driven to constantly feed the mat forwardly, and conveyor 44 is driven at a much higher speed to continuously draw or expand the mat as it is supplied by the feed conveyors.
- Table 34 is positioned so that a portion of the flat plate presses against the under surface of the web.
- Roll 38 is similarly positioned so that the web is in contact with its upper peripheral portion and roll 48 is positioned so that the web is in contact with its lower peripheral portion.
- conveyor 44 is driven at a much higher speed than feed conveyors 28 and 30, the speed differential being such as to stretch the mat to. say, between 60 and 70 times its original length.
- the filaments of the several layers shift or slide from directions substantially transverse of the mat or web, to positions, say, at a 45 angle or greater to the transverse dimension of the web to lie in what is here termed a direction "generally longitudinal of the web.
- the shifting of the fibers is accompanied by a narrowing of the web as illustrated in Fig. 7.
- Roll 38 is positively driven in the direction indicated by the arrow at a speed preferably slightly greater than the speed of the oven conveyor, and roll 48 is driven at a speed greater than the speed of the oven conveyor and of roll 38.
- the surfaces of rolls 38 and 48 may rotate at a speed of, say. 6.3 and 6.6 per minute, respectively.
- the lower surface of the web is not tensioned to the same extent, or the tension is temporarily relieved and, although some eorrugating and separation of the layers may take place, depending upon the particular operating conditions, the layers adjacent this surface will be relatively smooth
- the intermediate layer of the web will vary between the condition of the upper layers and the condition of the lower layers to form a portion of intermediate density and openness of structure.
- the extent to which the original mat must be expanded or stretched to produce the desired effeet will vary, depending upon the weight, filament diameter and character of the original mat.
- the operations are identical except that the oven (see particularly Fig. 8) is provided with a pressure conveyor 54 overlying the upper reach of conveyor 44.
- Pressure conveyor 54 is made adjustable relatively to conveyor 44 by any suitable means (not shown) and is driven at the same speed as the latter.
- Conveyor 54 is similarly of open, wire mesh construction to permit the passage of the heated air therethrough. As the puffed mat passes between the two conveyors it is compressed to the desired thickness and density and-is maintained in its compressed state during the binder setting operation, whereby it will retain its compressed condition after leaving the oven.
- the products made by the instant invention are very resilient and compressible and, due to the gradation of structure from one surface to the other, perform admirably as filtering media.
- the process is relatively simple and does not require involved equipment.
- a product comprising a multilayer body of intercrossed filaments, the layers adjacent one face having a continuous succession of adjacent substantially parallel undulations extendingat angles to the length of the filaments, and forming an openwork structure, and succeeding layers having similar undulations of diminished depth.
- a product comprising a unitary multilayer body of intercrossed filaments, the layers adjacent one face having a continuous succession of adjacent substantially parallel undulations extending at angles to the length of the filaments, and forming an openwork structure, and succeeding layers having similar undulations of diminished depth, and a set binder bonding the filaments into the unitary body.
- a product comprising a multilayer body of intercrossed, glass filaments, said body being expended in the direction of its thickness to provide a relatively lightweight, open, porous structure and to provide the layers adjacent one face with a continuous succession of adjacent substantially parallel undulations extending at angles to the lengths of the filaments and to provide succeeding layers with similar undulations of diminished depth,
- a product comprising a multilayer body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and the layers adjacent one face thereof having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments whereby a relatively lightweight, open, porous structure is provided, and succeeding layers having similar undulations of diminished depth whereby said body i of greater density adjacent the face opposite to said one face.
- a product comprising a, multilayer, unitary body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and said layers having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments, said undulations being of less depth adjacent one surface of the body than the other, and said body being of greater density adjacent said one surface.
- a product comprising a multilayer, unitary body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and said layers having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments, said undulations being of less depth adjacent one surface of the body than the other, said body being of greater density adjacent said one surface, and a hardened binder bonding the filaments into the unitary body.
- a product comprising a compressed, unitary, multilayer body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and said layers having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments, said undulations being of less depth adjacent one surface of the body than the other, said body being of greater density adjacent said one surface, and a hardened binder bonding the filaments into the unitary body.
- the method comprising drawing a multilayer mat, in which the filaments of adjacent layers cross each other at acute angles, in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, and retarding the drawing movement of the layers adjacent one face of the mat to cause the mat to have a greater density adjacent said one face than the other.
- the method comprising drawin a multilayer mat, in which the filaments of adjacent layers cross each other at acute angles, in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, and retarding the movement of the layers adjacent one face of the mat to cause relatively minor undulation of the layers adjacent said one face of said mat and relatively major undulation adjacent the opposite face.
- the method comprising drawing a multilayer mat, in which the filaments of adjacent layers cross each other at acute angles and which contains an unset binder, in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, retarding the drawing movement of the layers adjacent one face of the mat while accelerating the drawing movement of the layers adjacent the other face to cause relatively minor undulation of the layers adjacent said one face oi the mat and relatively major undulation adjacent the opposite face, and setting the binder.
- the method comprising drawing a multilayer glass mat in which the filaments of adjacent layers cross each other at acute angles in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said drawing and expanding operation contacting one face of the mat with a relatively slower moving surface and the other face thereof with a relatively rapidly moving surface to cause greater expansion of said mat adjacent one face than the other.
- the method comprising drawing a multilayer glass mat in which the filaments of adjacent layers cross each other at acute angles in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said drawing and expanding operation contacting one face of the mat with a relatively slower moving surface and subsequently contacting the other face of the mat with a relatively rapidly moving surface and then conveying the expanded mat away from the expanding operation.
- the method comprising feeding a multilayer mat in which the filaments of adjacent layers cross each other at acute angles, drawing the mat in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, by contacting the mat at a point remote from the feed by means moving at a, relatively high speed, contacting one face of the mat intermediate said feed and means witha relatively slow moving surface and contacting the other face of the mat intermediate said feed and means with a relatively rapidly moving surface to cause greater expansion of said mat adjacent one face than the other.
- the method comprising drawing a multilayer glass mat containing an unset binder, and in which the filaments of adjacent layers cross each other at acute angles, until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, and during said drawing and expanding operation contacting one face of the mat with a relatively slower moving surface and the other face thereof with a relatively rapidly moving surface to cause greater expansior of said mat adjacent one face than the other, and setting the binder.
- the method comprising drawing a multilayer glass mat containing an unset binder, and in which the filaments of adjacent layers cross each other at acute angles, until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said drawing and expanding operation contacting one face of the mat with a relatively greater expansion of said mat adjacent one face than the other, compressing the mat and setting the binder.
- the method comprising feeding a multilayer mat in which the filaments of adjacent layers cross each other at acute angles, expanding the mat in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said expanding operation drawing one face of the mat over a stationary plate, contacting said face of the mat with a relatively slowly moving surface, and contacting the other face of the mat with a relatively rapidly moving surface, to cause greater expansion of said mat adjacent one face than the other.
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Description
H. E. HOLCOMB 7 April 25, 1950 FILAMENTARY PRODUCT AND METHOD OF ITS PRODUCTION 2 Sheets-Sheet 1 Filed July 27, 1948 lNVENT OR flaw/Pr 5156460415. 4/{7Li0 TTORNEY April 25, 1950 H. E. HOLCOMB FILAMENTARY PRODUCT AND METHOD OF ITS PRODUCTION 2 Sheets-Sheet 2 Filed July 27, 1948 Patented Apr. 25, 1950 umrsu STATES PATENT orncs FILAMENTARY PRODUCT AND METHOD OF ITS PRODUCTION Harry E. Holcomb, Stratford, Com,
Johns-Manville Corporation, New York, N.
assignor to Yo,
a corporation of New York Application July 27, 1948, Serial No. 40,816 16 Claims. (Cl. 154-124) 2 with the filaments of each layer substantially parallel and the filaments of adjacent layers crossing at acute angles, is drawn or expanded by pulling the mat in a. direction substantially provision of an improved product of this type of lesser density and more open texture adjacent one surface than the other, the texture and density preferably gradually changing through at right angles to the general lay of the filaments. the operation being continued until layers of the mat corrugate and the mat as a whole pufls up or expands in the direction of its thickness. In accordance with the instant invention, expansion of the mat is retarded adjacent one surface and is accelerated adjacent .the other, whereby the mat puffs to a lesser extent and, hence, is denser adjacent one surface than the other, the
' intermediate structure of the body varying bethe thickness of the product from the one condition to the other. The product suitably contains a minor proportion of a binder which re-. tains the filaments thereof in their positions and bonds the whole into a unitary body. The product is of particular utility as an air filter medium. Thesurface of less density and more open texture is employed as the air entry side of the filter and, as the'dust-laden air enters the body, the coarse dust, lint and the like are removed. As the air passes on through the body the finer dust is progressively deposited, the relatively dense structure adjacent the opposite surface forming a final clean-up section to remove any remainder of the dust. The single unit is thus comparable to a series of filters of varying dustremoval characteristics. By removing the coarse dust and lint in the more open section, it is possible to obtain a greatly increased dust retention capacity before resistance to air flow becomes excessive. It will be appreciated, however, that the product may find other fields of usefulness than.
air filters.
Another object of the invention is the provision of a multi-layer, glass filament mat pulled or expanded in the direction of its thickness comprising a plurality of layers having substantially parallel corrugations or undulations, the undutween the two extremes. contains a binder which is applied in an unset state to the original mat to insure distribution throughout the mat and is set after the expansion operation. Where a product of higher density is desired, the puffed body is compressed and held in that condition during the binder setting operation.
My invention will be more fully understood and further objects and advantages thereof will become apparent when reference is made to the more deta led description of the preferred embodiment of the invention which is to follow, and to the accompanying drawings in which:
Fig. 1 is a perspective view of a segment of an expanded product in accordance with the instant invention;
Fig. 2 is a view similar to Fig. 1 illustrating a modified embodiment;
Fig. 3 is a diagrammatic, end elevational view of an apparatus employed in preparing the initial mat from which the instant structure is derived;
Fig. 4 is a diagrammatic, front elevational view of the apparatus of Fig. 3;
Fig. 5 is a plan view of the mat as made on the apparatus of Figs. 3 and 4;
Fig. 6' is a diagrammatic, elevational View of the apparatus embodying the instant invenion;
Fig. 7 is a top plan view of the apparatus of,
i Fig. 6; and,
Fig. 8 illustrates a modified construction of a portion of the apparatus.
Referring now to the drawings, a product of the instant invention consists of a body in composed of a plurality of layers l2, each formed of continuous, or substantially continuous glass filaments It. The filaments of each layer lie in approximate parallelism and the filaments of adjacent layers cross each other. The product is pulled or expanded in the direction of its thick- Suitabiy the product ness to produce a lightweight, low density material. In the expanding and pulling operation in accordance with the instant invention, the filamentary layers, particularly those adjacent one surface of the product, the upper surface of Fig. l, are corrugated and the corrugations are brought into relatively adjacent, lateral relationship. At the same time the corrugated layers are somewhat separated, although tied together by a. multiplicity of interconnecting filaments, to form a very low density, open work structure. The corrugations or undulations of the layers inwardly of the surface are gradually of lesser depth as the opposite surface is approached, the layers adjacent the opposite surface being only slightly corrugated or at least having corrugations of relatively shallow depth as compared with the layers adjacent the other surface. The separation between the layers also progressively decreases as the opposite surface is approached and the density of the product proportionately increases.
Intermingled with the filaments of the several layers, and bonding the mass of fibers into a unitary body, is a minor proportion of a binder, say between and by weight of the product. It will be understood that Fig. 1 is diagrammatic and that in actual practice the binder particles illustrated by reference character l6 will be visually insignificant.
The product shown in Fig. 2 is of the same character as that shown in Fig. 1 except in thb case the body has been compressed from the thickness shown in Fig. 1 and maintained in compressed state by the set binder. In this embodiment similar gradation of structure of the body is present but the body is proportionately denser throughout.
The products described above are adapted for many uses but are particularly valuable as air filtering media as previously explained. The products are very lightweight and a great multiplicity of fine, intercrossing filaments form a reticulated structure well adapted to remove particulate matter from air or other gases. The gradual increase of density and decrease of the size of the interstices permits a graduated removal of the dust particles, the larger particles being caught or held adjacent the more open side of the filter body. The greatest mass of the particles E removed from the airstream by the intermediate layers and the residue of fine particles which penetrate substantially through the body are collected by the final relatively dense layers. The body may be used in its compressed form, particularly where finer dust particies are present. and exceptional high efilciency is required. In both forms a large filtering capacity is obtained due to the distribution of the deposited dust throughout the body.
Referring now particularly to Figs. 38 inclusive, the method and apparatus employed to produce the products described above will be explained in detail. The products are made from the initial mat l8 (see Fig. 5), known as the condensed mat, fabricated in a substantially conventional manner by drawing a plurality of continuous glass filaments directly from the spinning orifices of the melting furnace 22 and accumulating the filaments on a drum 24. The drawing drum is rotated in the direction indicated by the arrow in Fig. 3 by any suitable driving means (not shown) and at a relatively high speed to continuously draw fine filaments, say, of 6 to 30 micron diameter, and wind the filaments on the drum. Either the furnace or the drum is reciprocated to lay the filaments on the drum in a plurality of layers of spirals with the filaments of each layer crossing the filaments of adjacent layers. In the apparatus illustrated, the furnace 22 is reciprocated, as indicated by the doubleended arrow in Fig. 4. The rate of reciprocation relatively to the drawing speed, that is the peripheral speed of the drum, is such that the filaments of adjacent layers cross each other at acute angles.
A binder may be applied during the filament drawing operation. This application may be made in any suitable way, for example by a manually operated spray device 26 (see Fig. 3), which is moved back and forth across the mat on the drum at intervals to uniformly spray the binder material onto the mat. The amount of binder used is carefully controlled. As will later be explained in greater detail, only a portion of the total binder content, say up to 70%, is preferably applied at this stage, the remainder of the binder being applied to the mat during later stages in the formation of the product. The total binder used is such that th solids binder content of the finished product is, say, 1 to 5% by weight of the product.
The binder is preferably employed in the form of an emulsion, a water dispersion being suitable. However, a solution of the binder in a solvent may also be employed. The binder may be either thermosetting or thermoplastic, but thermosetting adhesives are referred. Examples of suitable matezials are acrylic resins, urea-formaldehyde resins, polyvinyl alcohols, latices, and the like. In commercial operations it has been found preferable to apply a water dispersion of an acrylic resin during the filament drawing operation and a dispersion of a urea-formaldehyde resin at the later stage. Due to the relatively high speed movement of the mat on th drum and the temperatures prevalent during the filament drawing operation, the binder rapidl dries by evaporation of the water or solvent, as the case may be, so that, upon completion of the drawing operation, the mat contains a substantially dry but unset binder.
When the condensed mat is completed, it is severed along a line of generation of the drum and is removed therefrom. The mat is then placed on a conveyor 28 of a feed device including a conveyor 30 mounted in a suitable manner to overlie the forward end of conveyor 28 and to yieldably engage the latter. While the condensed mat is on conveyor 28 and before it is fed beneath the overlying conveyor, it is treated with a binder softener. In the case of a binder such as the preferred acrylic resin, the softener is water, which in eifect again places the finely divided binder in suspension. If binders are employed of the type which cannot be practically softened with water, an appropriate solvent is used. The softener may be applied to the mat in the form of a spray, or a hand brush, illustrated at 32, may b employed for the purpose. As pointed out above, preferably although not necessarily, only a port-ion of the total binder content was applied to the condensed mat during the winding operation. Where this practice was followed the remainder of the binder is applied at this time. The added binder may be the same as that already used but suitably is a material such as a urea-formaldehyde resin. This material, in the form of a suspension, is spread on the mat on the conveyor, simila:ly as the softener. When the mat has been treated as described above, it is allowed to stand for an appreciable length of time to-permit thorough soaking of the mat.
Referring now specifically to Figs. 6 and 7, the apparatus for expanding the mat, prepared as explained above, will be described. This apparatus, in addition to feed conveyors 28 and 30, previously mentioned, includes in its preferred embodiment, a substantially level table or plate 34 having a forwardly and downwardly angling side flange 36, a
hot air may be circulated from a furnace (not shown) through a duct ill, the heated air being forced through the mat on the conveyor and out of the oven through duct 52.
Inthe operation of the above-described apparatus, the condensed mat, treated as previously mentioned, is fed forwardly, initially at an accelerated speed, between conveyors 28 and 301 until its forward edge protrudes beyond the conveyors. The mat [8, when placed on the feed conveyors, is positioned so that the filaments lie generally transversely of the conveyors, the feeding operation moving the mat in the direction indicated by the arrows in Fig. 6. The protruding forward edge of the mat is grasped, suitably by hand, and drawn or expanded into an elongated web which is passed over table 34 and roll 38 and under roll 48, and carried onto conveyor 44 where the end of the web is temporarily secured in any suitable manner, for example, by weighting it. Feed conveyors 38 and 28 are then driven to constantly feed the mat forwardly, and conveyor 44 is driven at a much higher speed to continuously draw or expand the mat as it is supplied by the feed conveyors. Table 34 is positioned so that a portion of the flat plate presses against the under surface of the web. Roll 38 is similarly positioned so that the web is in contact with its upper peripheral portion and roll 48 is positioned so that the web is in contact with its lower peripheral portion.
As mentioned above, conveyor 44 is driven at a much higher speed than feed conveyors 28 and 30, the speed differential being such as to stretch the mat to. say, between 60 and 70 times its original length. During the stretching operation the filaments of the several layers shift or slide from directions substantially transverse of the mat or web, to positions, say, at a 45 angle or greater to the transverse dimension of the web to lie in what is here termed a direction "generally longitudinal of the web. The shifting of the fibers is accompanied by a narrowing of the web as illustrated in Fig. 7. Roll 38 is positively driven in the direction indicated by the arrow at a speed preferably slightly greater than the speed of the oven conveyor, and roll 48 is driven at a speed greater than the speed of the oven conveyor and of roll 38. For example, if the oven conveyor is traveling at a speed of, say, 6' per minute, the surfaces of rolls 38 and 48 may rotate at a speed of, say. 6.3 and 6.6 per minute, respectively. The continued pull on the web, together with the acand close together.
tion of fast driven roll 40, tensions the web to such an extent that, as it reaches the relatively slower moving oven conveyor, the upper and adjacent layers separate, although tied together by numerous intercrossing or interlocking filaments,-
and form into a series of longitudinally extending, substantially parallel corrugations which move into close, laterally adjacent relationship. Due to the drag of plate 34 and the slower speed of roll 38, the lower surface of the web is not tensioned to the same extent, or the tension is temporarily relieved and, although some eorrugating and separation of the layers may take place, depending upon the particular operating conditions, the layers adjacent this surface will be relatively smooth The intermediate layer of the web will vary between the condition of the upper layers and the condition of the lower layers to form a portion of intermediate density and openness of structure. As the expanded or pulled web is carried through oven 42, the temperature is maintained in the oven by the circulation of heated air or otherwise, to the degree required to set and harden the binder to bond the filaments together into a unitary product.
The extent to which the original mat must be expanded or stretched to produce the desired effeet will vary, depending upon the weight, filament diameter and character of the original mat.
Where a mat as disclosed in Fig. 2 is desired, the operations are identical except that the oven (see particularly Fig. 8) is provided with a pressure conveyor 54 overlying the upper reach of conveyor 44. Pressure conveyor 54 is made adjustable relatively to conveyor 44 by any suitable means (not shown) and is driven at the same speed as the latter. Conveyor 54 is similarly of open, wire mesh construction to permit the passage of the heated air therethrough. As the puffed mat passes between the two conveyors it is compressed to the desired thickness and density and-is maintained in its compressed state during the binder setting operation, whereby it will retain its compressed condition after leaving the oven.
The products made by the instant invention are very resilient and compressible and, due to the gradation of structure from one surface to the other, perform admirably as filtering media. The process is relatively simple and does not require involved equipment.
Having thus described my invention in rather full detail, it will be understood that these details need not be strictly adhered to and that various changes and modifications may suggest themselves to one skilled in the art, all falling within the scope of the invention as defined by the sub- Joined claims.
What I claim is:
I 1. A product comprising a multilayer body of intercrossed filaments, the layers adjacent one face having a continuous succession of adjacent substantially parallel undulations extendingat angles to the length of the filaments, and forming an openwork structure, and succeeding layers having similar undulations of diminished depth.
2. A product comprising a unitary multilayer body of intercrossed filaments, the layers adjacent one face having a continuous succession of adjacent substantially parallel undulations extending at angles to the length of the filaments, and forming an openwork structure, and succeeding layers having similar undulations of diminished depth, and a set binder bonding the filaments into the unitary body.
3. A product comprising a multilayer body of intercrossed, glass filaments, said body being expended in the direction of its thickness to provide a relatively lightweight, open, porous structure and to provide the layers adjacent one face with a continuous succession of adjacent substantially parallel undulations extending at angles to the lengths of the filaments and to provide succeeding layers with similar undulations of diminished depth,
4. A product comprising a multilayer body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and the layers adjacent one face thereof having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments whereby a relatively lightweight, open, porous structure is provided, and succeeding layers having similar undulations of diminished depth whereby said body i of greater density adjacent the face opposite to said one face.
5. A product comprising a, multilayer, unitary body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and said layers having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments, said undulations being of less depth adjacent one surface of the body than the other, and said body being of greater density adjacent said one surface.
6. A product comprising a multilayer, unitary body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and said layers having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments, said undulations being of less depth adjacent one surface of the body than the other, said body being of greater density adjacent said one surface, and a hardened binder bonding the filaments into the unitary body.
7. A product comprising a compressed, unitary, multilayer body of intercrossed, glass filaments, said body being expanded in the direction of its thickness and said layers having a continuous succession of adjacent substantially parallel, continuous undulations extending at angles to the lengths of the filaments, said undulations being of less depth adjacent one surface of the body than the other, said body being of greater density adjacent said one surface, and a hardened binder bonding the filaments into the unitary body.
8. The method comprising drawing a multilayer mat, in which the filaments of adjacent layers cross each other at acute angles, in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, and retarding the drawing movement of the layers adjacent one face of the mat to cause the mat to have a greater density adjacent said one face than the other.
9. The method comprising drawin a multilayer mat, in which the filaments of adjacent layers cross each other at acute angles, in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, and retarding the movement of the layers adjacent one face of the mat to cause relatively minor undulation of the layers adjacent said one face of said mat and relatively major undulation adjacent the opposite face.
10. The method comprising drawing a multilayer mat, in which the filaments of adjacent layers cross each other at acute angles and which contains an unset binder, in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, retarding the drawing movement of the layers adjacent one face of the mat while accelerating the drawing movement of the layers adjacent the other face to cause relatively minor undulation of the layers adjacent said one face oi the mat and relatively major undulation adjacent the opposite face, and setting the binder.
11. The method comprising drawing a multilayer glass mat in which the filaments of adjacent layers cross each other at acute angles in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said drawing and expanding operation contacting one face of the mat with a relatively slower moving surface and the other face thereof with a relatively rapidly moving surface to cause greater expansion of said mat adjacent one face than the other.
12. The method comprising drawing a multilayer glass mat in which the filaments of adjacent layers cross each other at acute angles in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said drawing and expanding operation contacting one face of the mat with a relatively slower moving surface and subsequently contacting the other face of the mat with a relatively rapidly moving surface and then conveying the expanded mat away from the expanding operation.
13. The method comprising feeding a multilayer mat in which the filaments of adjacent layers cross each other at acute angles, drawing the mat in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, by contacting the mat at a point remote from the feed by means moving at a, relatively high speed, contacting one face of the mat intermediate said feed and means witha relatively slow moving surface and contacting the other face of the mat intermediate said feed and means with a relatively rapidly moving surface to cause greater expansion of said mat adjacent one face than the other.
14. The method comprising drawing a multilayer glass mat containing an unset binder, and in which the filaments of adjacent layers cross each other at acute angles, until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness, and during said drawing and expanding operation contacting one face of the mat with a relatively slower moving surface and the other face thereof with a relatively rapidly moving surface to cause greater expansior of said mat adjacent one face than the other, and setting the binder.
15. The method comprising drawing a multilayer glass mat containing an unset binder, and in which the filaments of adjacent layers cross each other at acute angles, until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said drawing and expanding operation contacting one face of the mat with a relatively greater expansion of said mat adjacent one face than the other, compressing the mat and setting the binder.
16. The method comprising feeding a multilayer mat in which the filaments of adjacent layers cross each other at acute angles, expanding the mat in a direction at right angles to the general lay of the filaments until layers of the mat assume an undulatory form and the mat expands in the direction of its thickness and during said expanding operation drawing one face of the mat over a stationary plate, contacting said face of the mat with a relatively slowly moving surface, and contacting the other face of the mat with a relatively rapidly moving surface, to cause greater expansion of said mat adjacent one face than the other.
HARRY E. HOLCOMB.
10 REFERENCES CITED Themfoilowing references are of record in the file of this patent:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US40816A US2505045A (en) | 1948-07-27 | 1948-07-27 | Filamentary product and method of its production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US40816A US2505045A (en) | 1948-07-27 | 1948-07-27 | Filamentary product and method of its production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2505045A true US2505045A (en) | 1950-04-25 |
Family
ID=21913119
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US40816A Expired - Lifetime US2505045A (en) | 1948-07-27 | 1948-07-27 | Filamentary product and method of its production |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2505045A (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2644780A (en) * | 1949-01-11 | 1953-07-07 | Johns Manville | Method of forming fluffed filamentary masses and article produced thereby |
| DE939678C (en) * | 1952-12-17 | 1956-03-01 | Torfoleum Werke Eduard Dyckerh | Process for the production of insulation boards or mats from fibers |
| DE1052647B (en) * | 1954-10-26 | 1959-03-12 | Owens Corning Fiberglass Corp | Process for the treatment of fibers made of glass or other inorganic, glass-like substances as well as device for carrying out the process |
| US2906314A (en) * | 1954-03-02 | 1959-09-29 | Dunlop Tire & Rubber Corp | Pneumatic tires |
| US2913037A (en) * | 1953-12-29 | 1959-11-17 | Johns Manville | Method and apparatus for forming condensed glass fiber mats |
| US3342658A (en) * | 1963-12-11 | 1967-09-19 | American Air Filter Co | Method of making filamentous mats |
| US3476635A (en) * | 1966-07-11 | 1969-11-04 | American Air Filter Co | Graduated density filamentous mat |
| US3479239A (en) * | 1965-11-24 | 1969-11-18 | Owens Corning Fiberglass Corp | Method and apparatus for producing tubular fibrous bodies |
| US3526557A (en) * | 1966-11-18 | 1970-09-01 | American Air Filter Co | Method for making filamentous mats |
| US3622413A (en) * | 1967-12-11 | 1971-11-23 | Silvio Tasca | Method of making preformed mats |
| US6183579B1 (en) * | 1998-12-14 | 2001-02-06 | Pps Packaging Company | Method of manufacturing evaporative cooler pads |
| US9694510B2 (en) | 2015-03-27 | 2017-07-04 | Charles Douglas Spitler | Skin stiffness characteristics and loft control production system and method with variable moisture content in input fiberglass media |
| US9695084B2 (en) * | 2015-05-11 | 2017-07-04 | Charles Douglas Spitler | Preparation for fiberglass air filtration media |
| US9968876B1 (en) * | 2014-02-14 | 2018-05-15 | Superior Fibers, Llc | Method of manufacturing fiberglass filtration media |
| US10106452B2 (en) | 2014-02-14 | 2018-10-23 | Superior Fibers, Llc | System and method of continuous glass filament manufacture |
| US10487427B2 (en) | 2014-02-14 | 2019-11-26 | Superior Fibers, Llc | System and method for continuous strand fiberglass media processing |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2644780A (en) * | 1949-01-11 | 1953-07-07 | Johns Manville | Method of forming fluffed filamentary masses and article produced thereby |
| DE939678C (en) * | 1952-12-17 | 1956-03-01 | Torfoleum Werke Eduard Dyckerh | Process for the production of insulation boards or mats from fibers |
| US2913037A (en) * | 1953-12-29 | 1959-11-17 | Johns Manville | Method and apparatus for forming condensed glass fiber mats |
| US2906314A (en) * | 1954-03-02 | 1959-09-29 | Dunlop Tire & Rubber Corp | Pneumatic tires |
| DE1052647B (en) * | 1954-10-26 | 1959-03-12 | Owens Corning Fiberglass Corp | Process for the treatment of fibers made of glass or other inorganic, glass-like substances as well as device for carrying out the process |
| US3342658A (en) * | 1963-12-11 | 1967-09-19 | American Air Filter Co | Method of making filamentous mats |
| US3479239A (en) * | 1965-11-24 | 1969-11-18 | Owens Corning Fiberglass Corp | Method and apparatus for producing tubular fibrous bodies |
| US3476635A (en) * | 1966-07-11 | 1969-11-04 | American Air Filter Co | Graduated density filamentous mat |
| US3526557A (en) * | 1966-11-18 | 1970-09-01 | American Air Filter Co | Method for making filamentous mats |
| US3622413A (en) * | 1967-12-11 | 1971-11-23 | Silvio Tasca | Method of making preformed mats |
| US6183579B1 (en) * | 1998-12-14 | 2001-02-06 | Pps Packaging Company | Method of manufacturing evaporative cooler pads |
| US9968876B1 (en) * | 2014-02-14 | 2018-05-15 | Superior Fibers, Llc | Method of manufacturing fiberglass filtration media |
| US10106452B2 (en) | 2014-02-14 | 2018-10-23 | Superior Fibers, Llc | System and method of continuous glass filament manufacture |
| US10351462B1 (en) | 2014-02-14 | 2019-07-16 | Superior Fibers, Llc | Method of manufacturing fiberglass filtration media |
| US10487427B2 (en) | 2014-02-14 | 2019-11-26 | Superior Fibers, Llc | System and method for continuous strand fiberglass media processing |
| US9694510B2 (en) | 2015-03-27 | 2017-07-04 | Charles Douglas Spitler | Skin stiffness characteristics and loft control production system and method with variable moisture content in input fiberglass media |
| US10046477B2 (en) | 2015-03-27 | 2018-08-14 | Superior Fibers, Llc | Skin stiffness characteristics and loft control production system and method with variable moisture content in input fiberglass media |
| US9695084B2 (en) * | 2015-05-11 | 2017-07-04 | Charles Douglas Spitler | Preparation for fiberglass air filtration media |
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