US2664376A - Mineral fiber mat and process of making same - Google Patents
Mineral fiber mat and process of making same Download PDFInfo
- Publication number
- US2664376A US2664376A US237618A US23761851A US2664376A US 2664376 A US2664376 A US 2664376A US 237618 A US237618 A US 237618A US 23761851 A US23761851 A US 23761851A US 2664376 A US2664376 A US 2664376A
- Authority
- US
- United States
- Prior art keywords
- fibers
- mat
- binder
- gelatin
- resin
- 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.)
- Expired - Lifetime
Links
- 239000002557 mineral fiber Substances 0.000 title description 8
- 238000000034 method Methods 0.000 title description 7
- 239000000835 fiber Substances 0.000 claims description 43
- 229920000159 gelatin Polymers 0.000 claims description 30
- 239000008273 gelatin Substances 0.000 claims description 30
- 108010010803 Gelatin Proteins 0.000 claims description 28
- 235000019322 gelatine Nutrition 0.000 claims description 28
- 235000011852 gelatine desserts Nutrition 0.000 claims description 28
- 229920000178 Acrylic resin Polymers 0.000 claims description 24
- 239000004925 Acrylic resin Substances 0.000 claims description 24
- 238000004519 manufacturing process Methods 0.000 claims description 14
- 238000000465 moulding Methods 0.000 claims description 12
- 239000000843 powder Substances 0.000 claims description 8
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 5
- 239000011707 mineral Substances 0.000 claims description 5
- 229920001169 thermoplastic Polymers 0.000 claims description 3
- 239000004416 thermosoftening plastic Substances 0.000 claims description 3
- 239000011230 binding agent Substances 0.000 description 32
- 239000011347 resin Substances 0.000 description 30
- 229920005989 resin Polymers 0.000 description 30
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 12
- 239000002245 particle Substances 0.000 description 12
- 239000000839 emulsion Substances 0.000 description 10
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 10
- 239000000203 mixture Substances 0.000 description 10
- 238000010438 heat treatment Methods 0.000 description 9
- 239000004793 Polystyrene Substances 0.000 description 8
- 239000007787 solid Substances 0.000 description 7
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 6
- 239000003365 glass fiber Substances 0.000 description 6
- 229920002223 polystyrene Polymers 0.000 description 6
- 238000003860 storage Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 5
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 5
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000004014 plasticizer Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 4
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 4
- 230000004927 fusion Effects 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 4
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 3
- 239000002313 adhesive film Substances 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000007598 dipping method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 3
- 229920005990 polystyrene resin Polymers 0.000 description 3
- NIQCNGHVCWTJSM-UHFFFAOYSA-N Dimethyl phthalate Chemical compound COC(=O)C1=CC=CC=C1C(=O)OC NIQCNGHVCWTJSM-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- FLKPEMZONWLCSK-UHFFFAOYSA-N diethyl phthalate Chemical compound CCOC(=O)C1=CC=CC=C1C(=O)OCC FLKPEMZONWLCSK-UHFFFAOYSA-N 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229920000058 polyacrylate Polymers 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000003039 volatile agent Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical class ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000002238 attenuated effect Effects 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- FBSAITBEAPNWJG-UHFFFAOYSA-N dimethyl phthalate Natural products CC(=O)OC1=CC=CC=C1OC(C)=O FBSAITBEAPNWJG-UHFFFAOYSA-N 0.000 description 1
- 229960001826 dimethylphthalate Drugs 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011490 mineral wool Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000006060 molten glass Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 125000005498 phthalate group Chemical class 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- -1 that is Polymers 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C25/00—Surface treatment of fibres or filaments made from glass, minerals or slags
- C03C25/10—Coating
- C03C25/24—Coatings containing organic materials
- C03C25/26—Macromolecular compounds or prepolymers
- C03C25/28—Macromolecular compounds or prepolymers obtained by reactions involving only carbon-to-carbon unsaturated bonds
- C03C25/285—Acrylic resins
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/44—Fibrous material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/431—Inorganic material
- H01M50/434—Ceramics
- H01M50/437—Glass
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- 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
- Y10T428/2938—Coating on discrete and individual rods, strands or filaments
-
- 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
-
- 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
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31551—Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]
- Y10T428/31623—Next to polyamide or polyimide
-
- 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
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31551—Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]
- Y10T428/31645—Next to addition polymer from unsaturated monomers
- Y10T428/31649—Ester, halide or nitrile of addition polymer
Definitions
- This invention relates to the treatment of mineral fibers and more particularly glass fibers to produce a mat adapted particularly for use as a separator or retainer mat in storage batteries.
- the fibers are deposited on a slowly moving conveyor to form a web or mat having a thickness varying from about a few thousandths of an inch to one quarter of an inch.
- Binding material is usually applied to the fibers, either before or after they are deposited on the conveyor, as by spraying or dipping, and, subsequently, this binding material is heated to be cured, fused, or otherwise set to a form in which the fibers are firmly bound in the desired relation.
- the mat is used as a retainer mat or separator in electric storage batteries, it is desired to have the binder resistant to the battery acids and unaffected by the battery reactions.
- albumen and compounds which may, under some conditions, lose their nitrogen as through decomposition, cannot be used.
- An object of the invention is to produce an improved bonded mineral wool adapted particularly for battery use which not only has increased resistance to battery acids, but does not militate against the performance of the battery.
- a binder composed principally of polystyrene or acrylic resin such as me'thacrylate is employed.
- Poly-- styrene is particularly resistant to attack by 8111- phuri c-acid and also has excellent electrical properties and is resistantto moisture. It is found that the molding powder grade, that is, medium 'nw wu er w g t r n. is most desirable.
- R is a radical selected from the class consisting of hydrogen and methyl
- R is an alkyl radical selected from the class consisting of methyl, ethyl, propyl, isopropyl, butyl and isobutyl.
- methyl acrylate and methyl methacrylate are preferable. It is often desirable to plasticize these resins in order to use lower baking temperatures or provide a more flexible product.
- many of the conventional plasticizers may be used as will be apparent to those skilled in the art.
- the phthalates such as dibutyl phthalate, diethyl phthalate, and dimethyl phthalate are recommended especially when the mineral fiber mat is to be used in storage batteries.
- plasticizer are taken to include other acrylic resins of the described monomeric structure which also may be applicable for that purpose.
- butyl acrylate or butyl methacrylate which are softer acrylic resins, are well suited for the plasticizing of methyl acrylate or methyl methacrylate.
- the amount of plasticizer employed is not critical and largely dependent on the results desired, Ordinarily, the amount of plasitcizer may range from 15 per cent to 50 per cent by weight of the resin to be plasticized.
- the molecular weight of the acrylic resins used may vary widely since it is contemplated and required only that the resins fuse upon exposure to elevated temperatures as compared to room temperatures, fiow along fibers to form a coating as more fully described hereafter, and then congeal as upon cooling.
- themolecular weights preferred are those of the molding pow-' resins of these molecular weights do not fuse too readily nor too slowly. For example, resins of such molecular weights flow well at about 250 F. to 475 F. e
- a resin is contemplated having a polymeric growth of such degree as to provide a specific gravity of about 1.16 to 1.20 in the resin, a molding temperature of about 285 F. to 340 F., or an injection temperature of about 325 F. to 475 F.,
- the lower molecular weight resins of these types have insuflicient strength for the purpose of the invention. Accordingly, polystyrene having a molecular weight below 65,000 and acrylic resins which are substantially deformable at room temperatures are not preferred.
- solutions of these higher molecular weight resins that is, polystyrene resins having a molecular weight over about 85,000 and acrylic resins which fuse substantially above 475 F., are not readily usable because of the dangers and high costs incident to the use of solvents. For this reason the resin binder is applied in the form of an aqueous emulsion or dispersion.
- the integrity of the mat is initially maintained by one binder until subsequently another binder which is normally nonadhesive but is rendered adhesive by changed temperature conditions, replaces the preliminary binder, the final binder preferably having certain properties rendering it particularly useful for use in storage batteries.
- the resin constituent of the binder preferably polystyrene of the specified molecular weight, or methacrylate or any of the other disclosed acrylic resins having similar physical characteristics
- gelatin in a ratio of about 15 parts gelatin to 85 parts polystyrene or methacrylate although other proportions ranging from about partsgelatin up to 25 parts gelatin with '75 to 90 parts of polystyrene or methacrylate may be used.
- the polystyrene or other resin is preferably polymerized in an aqueous emulsion .or dispersion so that in order to produce the binder all that is necessary is to add the gelatin tothe emulsion or dispersion.
- the gelatin may be added to theoriginal mixture to operate as the dispersing agent. In. any event, the gelatin adds to the stability of the suspension.
- binder formulations follow:
- Example I 12.5 pounds-Methyl methacrylate emulsion of 40% solids content and molecular weight of the molding powder grade.
- agitation should be sufficient only to mix thoroughly .theingredients.
- Example II 17.0 pounds-Methyl acrylate emulsion of 25% .resin solids and molecular weight of the molding powder grade.
- the method of applying the emulsion or mixture to the mineral fibers may be similar to any of those presently in use.
- the mixture may be sprayed onto the fibers as they build up into mat formation, or the mat may be saturated by dipping or other suitable means.
- the mat is heated to cause the binding agent to be converted to its final set, in the present case, to be fused.
- a somewhat higher temperature, about 475 F., may be used in the case of the acrylic resins.
- the gelatin retains the fibers in place until the fusion of the polystyrene or acrylic resin takes place and also during the time the diluent is reduced to such an extent that it no longer causes the fibers to cling to each other.
- the styrene or acrylic polymer preferably usedhas a lower fusion temperature as a result of its plasticization by the dibutyl phthalate or other plasticizers, but unplasticized resins may, of course, be used by resorting to higherbakmg temperatures.
- the binder of this invention makes use of the adhesiveness of gelatin in solution during the timethe vehicle for the resin is being removed.
- the temperature of the bake is in the softening range of the styrene or acrylic polymer, and at this point the resin fuses to afford a binder for retaining the fibers together.
- the gelatin is apparently sufficiently incorporated in or mixed with the styrene or acrylic resins, or its binding effect is not permanently required, because its leaching or attack by the battery acids has no noticeable effect on the mat.
- Figure 2 is a view on a greatly enlarged scale of the fluidbinder applied to the fibers.
- Figure 3 is a similar view illustrating the final binder stage.
- the apparatus comprises a glass melting unit 5 of suitable construction adapted to discharge the molten glass in a plurality of fine streams.
- the flowing molten streams are engaged by a blast of steam or air from a blower 8 disposed adjacent the source of the streams and by which the streams are attenuated to fine fibers.
- the fibers are blown downwardly through the hood 8 onto a collecting surface which is in the form of an endless foraminous belt 9.
- a suction chamber I is provided beneath the belt 9 to aid in collecting the fibers in the form of a mat II in which the fibers are haphazardly arranged.
- the thickness of the mat is primarily controlled by regulating the speed of the belt 9. Thus, increasing the conveyor speed produces a thinner mat, and conversely, slowing the conveyor speed provides a greater thickness.
- the mat As the mat is carried from beneath the hood 8 on the conveyor 9, it is drafted into a sheet I2 by mechanism including a draft bar or idler roller I 4 and drafting rolls I5 and I6.
- the sheet I2 passes downwardly from the roll I4 and around the roll I 5 which is driven by any suitable mechanism.
- the roll I6 cooperates With the roll I5 as a pinch roll to assure uniform contact of the sheet with the roll I5.
- the rolls I5 and I6 serve a two-fold purpose since the roll I5 is mounted within a container I1 and is adapted for rotation partially submerged in a binder solution I8.
- the sheet I2 is saturated with binder as it is drawn from the conveyor 9 and excess binder is squeezed out as the sheet passes between the rolls I5 and I6.
- the binder impregnated sheet as it leaves the dipping tank passes through a drying and/or curing oven 20 in which a suitable baking temperature is maintained preferably by circulating heated air.
- the sheet is supported in the oven 20 on a traveling conveyor belt 2
- have similar surface speeds which are slightly in excess of the drafting speed of the roll I 5. This difference in speed may be only sufiicient to prevent the sheet from wrinkling as the binder is cured.
- the cured sheet upon leaving the oven 20 may be rolled as at 24 or cut into sheets for storage or subsequent handling and fabrication.
- Figure 2 illustrates on a gigantic scale several fibers F which represent the primary binder phase, that is, the mat after passing through the binder solution but before sufilcient heat has been applied to cause the resin to flow.
- Passage of the mat through the binder I8 in the tank I! produces a film on the fibers as indicated at 28.
- This film or residuary emulsion completely wets and covers the fibers with a uniform coating embodying the solubilized gelatin.
- Solid particles of resin 29 dispersed in the gelatin emulsion are adhered to the fiber surface by the fluid phase of the binder as the volatiles evaporate.
- the preliminary heating of the binder causes the liquid to evaporate thereby leaving a relatively solid bond of gelatin holding the fibers together.
- fluffiness in the mat and separation of fibers is prevented until the permanent resin bond is accomplished by additionally heating the mat.
- a mineral fibrous mat carrying a susbtantially uniform continuous film on the surface of the individual fibers, said film comprising a fused thermoplastic acrylic resin having a molecular weight of the molding powder grade and a substantial amount of gelatin incorporated therein, said acrylic resin having the following monomeric structure:
- R is a radical selected from the class consisting of hydrogen and methyl
- R is an alkyl radical selected from the class consisting of methyl, ethyl, propyl, isopropyl, butyl, and isobutyl.
- a mineral fibrous mat carrying a substantially uniform continuous film on the surface of the individual fibers,.said film comprising a fused thermoplastic resin having incorporated therein a substantial amount of gelatin, said resin of a molding powder grade being a plasticized acrylic resin selected from the class consisting of methyl acrylate and methyl methacrylate.
- plasticizer is an acrylic resin selected from the class consisting of butyl acrylate and butyl methacrylate.
- a mineral fibrous mat carrying a substantially uniform continuous film on the surface of the individual fibers, said film including a binder composition consisting essentially of a fused methyl methacrylate resin having incorporated therein a substantial amount of gelatin, said resin having a polymeric growth of such degree as to provide a specific gravity of about 1.16 to 1.20 in the resin, a molding temperature of about 285 F. to 340 F., and an injection molding temperature of about 325 F. to 475 F.
- a binder composition consisting essentially of a fused methyl methacrylate resin having incorporated therein a substantial amount of gelatin, said resin having a polymeric growth of such degree as to provide a specific gravity of about 1.16 to 1.20 in the resin, a molding temperature of about 285 F. to 340 F., and an injection molding temperature of about 325 F. to 475 F.
- a mineral fibrous mat carrying a substantially uniform continuous film on the surface of the individual fibers, said film including a binder composition consisting essentially of methyl acrylate plasticized with butyl acrylate and having incorporated therein a substantial amount of gelatin, said methyl acrylate being of molding powder grade and fusible at from 250 to 475 F.
- R is a radical selected from the class consisting of hydrogen and methyl
- R is an alkyl radical selected from the class consisting of methyl,- ethyl, propyl, isopropyl, butyl, and iso--i butyl.
- a composition comprising; particles of methyl aqueous solution of to deposit the particles on the fiber surfaces while the gelatin functions throughout as porary binder to hold the fibers in predetermined form, and then heating to fuse the discrete particles into an adhesive film, said methyl methacrylate having a polymeric growth of such. de-, greevas to provide a specific gravity of about 1.16 to 1.20 in the resin, a molding temperature of about 285 F. to 340 F., and an injection mold,- ing temperature of about 325 F. to 475 9.
- the steps of coating the fibers with, a composition comprising discrete particles of a thermoplastic acrylic resin having a molecular weight of the molding powder grade dispersed in an aqueous solution of gelatin, the
- R is a radical selected from the class consisting of hydrogen and methyl
- R. is an alkyl radical selected from the class consisting of methyl, ethyl, propyl, isopropyl, butyl, and isobutyl.
- the steps of treating the fibers with a composition comprising discrete particles of an acrylic resin selected from the class consisting of methyl acrylate and methyl methacrylate plasticized with an acrylic resin selected from the class consisting of butyl acrylate and butyl methacrylate, said particles being dispersed in an aqueous solution of gelatin; volatilizing the water to deposit the fibers on the fiber surfaces while th gelatin functions throughout as a temporary binder to hold the fibers in predetermined form; and then heating to fuse the discrete particles into an adhesive film.
- a composition comprising discrete particles of an acrylic resin selected from the class consisting of methyl acrylate and methyl methacrylate plasticized with an acrylic resin selected from the class consisting of butyl acrylate and butyl methacrylate, said particles being dispersed in an aqueous solution of gelatin; volatilizing the water to deposit the fibers on the fiber surfaces while th gelatin functions throughout as a temporary binder to hold the fibers in predetermined form; and then
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Electrochemistry (AREA)
- Inorganic Chemistry (AREA)
- Ceramic Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Nonwoven Fabrics (AREA)
- Laminated Bodies (AREA)
Description
Dec'. 29, 1953 'r. E. PHlLIPPS MINERAL FIBER MATS AND PROCESS OF MAKING SAME Filed July 19, 195] 5 INVENTOR. @zgj 1mm, E. PkiZi a Patented Dec. 29, 1953 MINERAL FIBER MAT AND PROCESS OF MAKING SAME Thomas E. Philipps, Newark, Ohio, assignor to Owens-Corning Fiber poration of Delaware glas Corporation, a cor- Application July 19, 1951, Serial No. 237,618
This invention relates to the treatment of mineral fibers and more particularly glass fibers to produce a mat adapted particularly for use as a separator or retainer mat in storage batteries.
Ordinarily, in the making of mineral fiber mats of the present type, the fibers are deposited on a slowly moving conveyor to form a web or mat having a thickness varying from about a few thousandths of an inch to one quarter of an inch. Binding material is usually applied to the fibers, either before or after they are deposited on the conveyor, as by spraying or dipping, and, subsequently, this binding material is heated to be cured, fused, or otherwise set to a form in which the fibers are firmly bound in the desired relation. When the mat is used as a retainer mat or separator in electric storage batteries, it is desired to have the binder resistant to the battery acids and unaffected by the battery reactions.
Heretofore, a number of materials have been employed to bond the fibers, but these materials have not completely satisfied the requirements where the mats are for storage battery use. The components of the binder must be resistant to acid. No component can contain chlorine since the resulting formation of hydrochloric acid attacks the battery plates. This precludes the use of vinyl chlorides, chlorinated rubber, and the like. Also, animal glues are usually leached with hydrochloric acid during their processing so that they often contain chlorides and for the same reason are objectionable. Nor should acetates or any organic acid derivative, acid anhydride, or other acid forming compound be present in any of the ingredients. 7 r M In addition, practice has indicated that the presence of free nitrogen is detrimental to the performance of a battery. Consequently, casein,
albumen, and compounds which may, under some conditions, lose their nitrogen as through decomposition, cannot be used. a
An object of the invention is to produce an improved bonded mineral wool adapted particularly for battery use which not only has increased resistance to battery acids, but does not militate against the performance of the battery.
In accordance with this invention, a binder composed principally of polystyrene or acrylic resin such as me'thacrylate is employed. Poly-- styreneis particularly resistant to attack by 8111- phuri c-acid and also has excellent electrical properties and is resistantto moisture. It is found that the molding powder grade, that is, medium 'nw wu er w g t r n. is most desirable.
12 Claims. (Cl. 154-101) 2 the polymer range being between 65,000 and 85,000 molecular weight.
With respect to the acrylic resins, those particularly contemplated have this monomeric structure:
1 n coon wherein R is a radical selected from the class consisting of hydrogen and methyl, and R is an alkyl radical selected from the class consisting of methyl, ethyl, propyl, isopropyl, butyl and isobutyl.
Of these acrylic resins, methyl acrylate and methyl methacrylate (sometimes referred to for convenience simply as methacrylate) are preferable. It is often desirable to plasticize these resins in order to use lower baking temperatures or provide a more flexible product. For this purpose many of the conventional plasticizers may be used as will be apparent to those skilled in the art. However, the phthalates such as dibutyl phthalate, diethyl phthalate, and dimethyl phthalate are recommended especially when the mineral fiber mat is to be used in storage batteries.
In the present specification and claims, forms of the term plasticizer are taken to include other acrylic resins of the described monomeric structure which also may be applicable for that purpose. As an instance, butyl acrylate or butyl methacrylate, which are softer acrylic resins, are well suited for the plasticizing of methyl acrylate or methyl methacrylate.
The amount of plasticizer employed is not critical and largely dependent on the results desired, Ordinarily, the amount of plasitcizer may range from 15 per cent to 50 per cent by weight of the resin to be plasticized.
The molecular weight of the acrylic resins used may vary widely since it is contemplated and required only that the resins fuse upon exposure to elevated temperatures as compared to room temperatures, fiow along fibers to form a coating as more fully described hereafter, and then congeal as upon cooling. In practice, themolecular weights preferred are those of the molding pow-' resins of these molecular weights do not fuse too readily nor too slowly. For example, resins of such molecular weights flow well at about 250 F. to 475 F. e
Particularly in the case of methyl methacry- 3 late, a resin is contemplated having a polymeric growth of such degree as to provide a specific gravity of about 1.16 to 1.20 in the resin, a molding temperature of about 285 F. to 340 F., or an injection temperature of about 325 F. to 475 F.,
as these steps are today practiced in the art.
The lower molecular weight resins of these types have insuflicient strength for the purpose of the invention. Accordingly, polystyrene having a molecular weight below 65,000 and acrylic resins which are substantially deformable at room temperatures are not preferred. On the other hand, solutions of these higher molecular weight resins, that is, polystyrene resins having a molecular weight over about 85,000 and acrylic resins which fuse substantially above 475 F., are not readily usable because of the dangers and high costs incident to the use of solvents. For this reason the resin binder is applied in the form of an aqueous emulsion or dispersion. The use of dispersions are attended with great difiiculty, however, in that as the vehicle is evaporated during the heat treatment of the binder, the resin is deposited on the fibers as separate particles of hardened resin which are devoid of any adhesiveness. As a result, the fibers of the mat fluif up and otherwise move from desired compact relation where the vehicle evaporates, and subsequent fusion of the binder particles by the heat treatment is incapable of binding the fibers into the required relation in the mat. The mats are, as a consequence, poorly bonded, fuzzy, and have poor strength.
It is another object of the invention to provide a process utilizing resin dispersions for binding glass fibers in a mat by which a compact, well bonded, product may be obtained.
In accordance with a second aspect of the invention, the integrity of the mat is initially maintained by one binder until subsequently another binder which is normally nonadhesive but is rendered adhesive by changed temperature conditions, replaces the preliminary binder, the final binder preferably having certain properties rendering it particularly useful for use in storage batteries.
The resin constituent of the binder, preferably polystyrene of the specified molecular weight, or methacrylate or any of the other disclosed acrylic resins having similar physical characteristics, is mixed with gelatin in a ratio of about 15 parts gelatin to 85 parts polystyrene or methacrylate although other proportions ranging from about partsgelatin up to 25 parts gelatin with '75 to 90 parts of polystyrene or methacrylate may be used. The polystyrene or other resin is preferably polymerized in an aqueous emulsion .or dispersion so that in order to produce the binder all that is necessary is to add the gelatin tothe emulsion or dispersion. In some processes, the gelatin may be added to theoriginal mixture to operate as the dispersing agent. In. any event, the gelatin adds to the stability of the suspension.
Specific examples of binder formulations follow:
Example I 12.5 pounds-Methyl methacrylate emulsion of 40% solids content and molecular weight of the molding powder grade.
6 pounds-Dibutyl phthalate. emulsion (28%- solids content).
0.2 pound-Gelatin of commercial. grade h10:
rine-free).
47.8 gallons-Distilled water.-
lons by adding the remainder of the water. The
agitation should be sufficient only to mix thoroughly .theingredients.
Example II 17.0 pounds-Methyl acrylate emulsion of 25% .resin solids and molecular weight of the molding powder grade.
12.0 pounds-Butyl acrylate emulsion of 20% resin solids.
0.2 pound-Gelatin of commercial grade (chlorine-free).
46.5 gallons-Water The preparation of this formulation is similar to steps set forth for Example 1 beginning with the addition of the gelatin in about one-half of the amount of water.
The method of applying the emulsion or mixture to the mineral fibers may be similar to any of those presently in use. The mixture may be sprayed onto the fibers as they build up into mat formation, or the mat may be saturated by dipping or other suitable means. After the fibers are properly coated, the mat is heated to cause the binding agent to be converted to its final set, in the present case, to be fused. A baking tel perature of 250 to 450 F. for three to twenty minutes, suffices to drive off the volatiles and effect the desired fusion. A somewhat higher temperature, about 475 F., may be used in the case of the acrylic resins. The gelatin retains the fibers in place until the fusion of the polystyrene or acrylic resin takes place and also during the time the diluent is reduced to such an extent that it no longer causes the fibers to cling to each other. The styrene or acrylic polymer preferably usedhas a lower fusion temperature as a result of its plasticization by the dibutyl phthalate or other plasticizers, but unplasticized resins may, of course, be used by resorting to higherbakmg temperatures. The binder of this invention makes use of the adhesiveness of gelatin in solution during the timethe vehicle for the resin is being removed. The temperature of the bake is in the softening range of the styrene or acrylic polymer, and at this point the resin fuses to afford a binder for retaining the fibers together. The gelatin is apparently sufficiently incorporated in or mixed with the styrene or acrylic resins, or its binding effect is not permanently required, because its leaching or attack by the battery acids has no noticeable effect on the mat.
One form of apparatus by which the present invention may be accomplished is disclosed in detail in Patent No. 2,306,347 to Games Slayter, dated December 22, 1942, but for purposes of illustrationreference may be hadto the accompanying drawing, inwhich-z Figural is a schematic view of apparatus which may be used in thevpresen t, process;
Figure 2 is a view on a greatly enlarged scale of the fluidbinder applied to the fibers; and
Figure 3 is a similar view illustrating the final binder stage.
Referring now to the drawings and Figure 1 in particular, the apparatus comprises a glass melting unit 5 of suitable construction adapted to discharge the molten glass in a plurality of fine streams. The flowing molten streams are engaged by a blast of steam or air from a blower 8 disposed adjacent the source of the streams and by which the streams are attenuated to fine fibers. The fibers are blown downwardly through the hood 8 onto a collecting surface which is in the form of an endless foraminous belt 9. A suction chamber I is provided beneath the belt 9 to aid in collecting the fibers in the form of a mat II in which the fibers are haphazardly arranged. The thickness of the mat is primarily controlled by regulating the speed of the belt 9. Thus, increasing the conveyor speed produces a thinner mat, and conversely, slowing the conveyor speed provides a greater thickness.
As the mat is carried from beneath the hood 8 on the conveyor 9, it is drafted into a sheet I2 by mechanism including a draft bar or idler roller I 4 and drafting rolls I5 and I6. The sheet I2 passes downwardly from the roll I4 and around the roll I 5 which is driven by any suitable mechanism. The roll I6 cooperates With the roll I5 as a pinch roll to assure uniform contact of the sheet with the roll I5. The rolls I5 and I6 serve a two-fold purpose since the roll I5 is mounted within a container I1 and is adapted for rotation partially submerged in a binder solution I8. Thus the sheet I2 is saturated with binder as it is drawn from the conveyor 9 and excess binder is squeezed out as the sheet passes between the rolls I5 and I6.
The binder impregnated sheet as it leaves the dipping tank passes through a drying and/or curing oven 20 in which a suitable baking temperature is maintained preferably by circulating heated air. The sheet is supported in the oven 20 on a traveling conveyor belt 2| and has a tensioning roll 22 cooperating therewith. The roll 22 and conveyor 2| have similar surface speeds which are slightly in excess of the drafting speed of the roll I 5. This difference in speed may be only sufiicient to prevent the sheet from wrinkling as the binder is cured. The cured sheet upon leaving the oven 20 may be rolled as at 24 or cut into sheets for storage or subsequent handling and fabrication.
Figure 2 illustrates on a gigantic scale several fibers F which represent the primary binder phase, that is, the mat after passing through the binder solution but before sufilcient heat has been applied to cause the resin to flow. Passage of the mat through the binder I8 in the tank I! produces a film on the fibers as indicated at 28. This film or residuary emulsion completely wets and covers the fibers with a uniform coating embodying the solubilized gelatin. Solid particles of resin 29 dispersed in the gelatin emulsion are adhered to the fiber surface by the fluid phase of the binder as the volatiles evaporate. The preliminary heating of the binder causes the liquid to evaporate thereby leaving a relatively solid bond of gelatin holding the fibers together. Thus fluffiness in the mat and separation of fibers is prevented until the permanent resin bond is accomplished by additionally heating the mat.
The solids content in the above stated amount have been found sufficient when melted to form a susbtantially uniform film on the fiber as indicated at 30 in Figure 3. subjecting the mat whereby the heat plasticized resin flows about the fibers and their points of contact and forms a permanent bond.
The present invention is a continuation-inpart of my application filed October 12, 1943, Serial Number 54,116, now U. S. Patent No.
. 2,566,960 wherein the combination of polystyrene and gelatin as and for the purpose here described is disclosed and claimed.
It is to be understood that modifications and variations may be effected within the spirit of the present invention as defined by the appended claims.
I claim:
1. As an article of manufacture, a mineral fibrous mat carrying a susbtantially uniform continuous film on the surface of the individual fibers, said film comprising a fused thermoplastic acrylic resin having a molecular weight of the molding powder grade and a substantial amount of gelatin incorporated therein, said acrylic resin having the following monomeric structure:
If R
1 I I coon wherein R is a radical selected from the class consisting of hydrogen and methyl, and R is an alkyl radical selected from the class consisting of methyl, ethyl, propyl, isopropyl, butyl, and isobutyl. 2. An article of manufacture as claimed in claim 1 wherein said acrylic resin has a polymeric growth conducive to ready fusing and flowing of the resin in a temperature range of about 250 F. to 475 F.
3. As an article of manufacture, a mineral fibrous mat carrying a substantially uniform continuous film on the surface of the individual fibers,.said film comprising a fused thermoplastic resin having incorporated therein a substantial amount of gelatin, said resin of a molding powder grade being a plasticized acrylic resin selected from the class consisting of methyl acrylate and methyl methacrylate.
4. An article of manufacture as claimed in claim 8 wherein the plasticizer is an acrylic resin selected from the class consisting of butyl acrylate and butyl methacrylate.
5. As an article of manufacture, a mineral fibrous mat carrying a substantially uniform continuous film on the surface of the individual fibers, said film including a binder composition consisting essentially of a fused methyl methacrylate resin having incorporated therein a substantial amount of gelatin, said resin having a polymeric growth of such degree as to provide a specific gravity of about 1.16 to 1.20 in the resin, a molding temperature of about 285 F. to 340 F., and an injection molding temperature of about 325 F. to 475 F.
6. As an article of manufacture, a mineral fibrous mat carrying a substantially uniform continuous film on the surface of the individual fibers, said film including a binder composition consisting essentially of methyl acrylate plasticized with butyl acrylate and having incorporated therein a substantial amount of gelatin, said methyl acrylate being of molding powder grade and fusible at from 250 to 475 F.
'7. In the method of manufacturing a bonded mat of mineral fibers, the step of treating the fibers witlgr a, ccmpesitic ing. powdergrade, dispersed in an aqueous solution of gelatin, volatilizingthe water to deposit the particles on the fiber surfaces while the gelatin functions throughout as a temporary binder to hold the fibers in predetermined form, and then heating to fuse the discrete particles into an adhesive film, said acrylic resinhaving the following. monomeric structure:
l l rr n coon v wherein R is a radical selected from the class consisting of hydrogen and methyl, and R is an alkyl radical selected from the class consisting of methyl,- ethyl, propyl, isopropyl, butyl, and iso--i butyl.
8. In the method of manufacturing abonded matof glass fibers, the steps of treating the fibers with a composition comprising; particles of methyl aqueous solution of to deposit the particles on the fiber surfaces while the gelatin functions throughout as porary binder to hold the fibers in predetermined form, and then heating to fuse the discrete particles into an adhesive film, said methyl methacrylate having a polymeric growth of such. de-, greevas to provide a specific gravity of about 1.16 to 1.20 in the resin, a molding temperature of about 285 F. to 340 F., and an injection mold,- ing temperature of about 325 F. to 475 9. In the method of manufacturing battery mats of bonded glass fibers, the steps of coating the fibers with, a composition comprising discrete particles of a thermoplastic acrylic resin having a molecular weight of the molding powder grade dispersed in an aqueous solution of gelatin, the
materials being present in the ratio of '75 to 90 parts by weight of acrylic resin to 10 to 25 parts by weight of gelatin, volatilizing thewater to deposit the discrete particlesof acrylic resin on the glass fiber surfaces while the gelatinfunctions as,
v .coninnsinadi c e e. partieleswofl atherm p astic.aory i -r m i Q n discrete methacrylate dispersed in an gelatin, volatilizing the water a tern following monomeric, structure:
H C O O R wherein R is a radical selected from the class consisting of hydrogen and methyl, and R. is an alkyl radical selected from the class consisting of methyl, ethyl, propyl, isopropyl, butyl, and isobutyl.
10. In the method of manufacturing a bonded; mat of fibers, the steps as claimed in claim '7 wherein concomitantly with the heating step the fibrous mass is maintained under tension whereby wrinkling is avoided.
11. In the method of manufacturing a bonded mat of glass fibers, the steps of treating the fibers with a composition comprising discrete particles of an acrylic resin selected from the class consisting of methyl acrylate and methyl methacrylate plasticized with an acrylic resin selected from the class consisting of butyl acrylate and butyl methacrylate, said particles being dispersed in an aqueous solution of gelatin; volatilizing the water to deposit the fibers on the fiber surfaces while th gelatin functions throughout as a temporary binder to hold the fibers in predetermined form; and then heating to fuse the discrete particles into an adhesive film.
12, The article of manufacture of claim 1 wherein said film comprises from to parts by weight resin and from 10 to 25 parts by weight gelatin.
THOMAS E. PHILIPPS.
References Cited in the file of this patent UNITED STATES PATENTS Number and then heating the mass from about.
Claims (1)
1. AS AN ARTICLE OF MANUFACTURE, A MINERAL FIBROUS MAT CARRYING A SUBSTANTIALLY UNIFORM CONTINUOUSLY FILM ON THE SURFACE OF THE INDIVIDUAL FIBERS, SAID FILM COMPRISING A FUSED THERMOPLASTIC ACRYLIC RESIN HAVING A MOLECULAR WEIGHT OF THE MOLDING POWDER GRADE AND A SUBSTANTIAL AMOUNT OF GELATIN INCORPORATED THEREIN, SAID ACRYLIC RESIN HAVING THE FOLLOWING MONOMERIC STRUCTURE:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US237618A US2664376A (en) | 1951-07-19 | 1951-07-19 | Mineral fiber mat and process of making same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US237618A US2664376A (en) | 1951-07-19 | 1951-07-19 | Mineral fiber mat and process of making same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2664376A true US2664376A (en) | 1953-12-29 |
Family
ID=22894475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US237618A Expired - Lifetime US2664376A (en) | 1951-07-19 | 1951-07-19 | Mineral fiber mat and process of making same |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2664376A (en) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1058589B (en) * | 1957-03-16 | 1959-06-04 | Continental Gummi Werke Ag | Process for the production of separators from glass fibers for accumulators |
| US2913365A (en) * | 1954-12-01 | 1959-11-17 | C H Dexter & Sons Inc | Fibrous webs and method and apparatus for making same |
| US2948634A (en) * | 1956-02-10 | 1960-08-09 | Bofors Ab | Rigid dressings |
| US2961364A (en) * | 1954-12-09 | 1960-11-22 | Rohm & Haas | Method of making bonded fibrous products |
| US3092509A (en) * | 1957-08-22 | 1963-06-04 | Oldham & Son Ltd | Glass fiber reinforced battery separators |
| US3184368A (en) * | 1959-12-29 | 1965-05-18 | Union Carbide Corp | Metal fiber containing structures and method therefor |
| US3287155A (en) * | 1962-11-08 | 1966-11-22 | Du Pont | Process for impregnating glass fiber mat with methyl methacrylate polymer |
| US3940536A (en) * | 1972-07-03 | 1976-02-24 | Compagnie Europeenne D'accumulateurs | Mechanically reinforced high porosity partially fused glass fiber galvanic separator |
| US5242765A (en) * | 1992-06-23 | 1993-09-07 | Luz Electric Fuel Israel Limited | Gas diffusion electrodes |
| WO2006023137A3 (en) * | 2004-07-23 | 2006-08-24 | Johns Manville | Control of pre-cured product moisture for formaldehyde-free fiberglass products |
| US20060257639A1 (en) * | 2004-12-22 | 2006-11-16 | Bianchi Marcus V A | Insulation having a thermal enhancement material and method of making same |
| US20060283135A1 (en) * | 2003-12-23 | 2006-12-21 | Fellinger Thomas J | Method of making a nodular inorganic fibrous insulation |
| US20070012809A1 (en) * | 2004-03-18 | 2007-01-18 | Fellinger Thomas J | Particles with a hose having a reduced internal diameter variation |
| US20070014641A1 (en) * | 2004-03-18 | 2007-01-18 | Fellinger Thomas J | System and method for forming an insulation particle/air suspension |
| US20080003431A1 (en) * | 2006-06-20 | 2008-01-03 | Thomas John Fellinger | Coated fibrous nodules and insulation product |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2484787A (en) * | 1945-03-14 | 1949-10-11 | Owens Corning Fiberglass Corp | Battery separator |
| US2566960A (en) * | 1948-10-12 | 1951-09-04 | Owens Corning Fiberglass Corp | Mineral fiber mat and process of making same |
-
1951
- 1951-07-19 US US237618A patent/US2664376A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2484787A (en) * | 1945-03-14 | 1949-10-11 | Owens Corning Fiberglass Corp | Battery separator |
| US2566960A (en) * | 1948-10-12 | 1951-09-04 | Owens Corning Fiberglass Corp | Mineral fiber mat and process of making same |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2913365A (en) * | 1954-12-01 | 1959-11-17 | C H Dexter & Sons Inc | Fibrous webs and method and apparatus for making same |
| US2961364A (en) * | 1954-12-09 | 1960-11-22 | Rohm & Haas | Method of making bonded fibrous products |
| US2948634A (en) * | 1956-02-10 | 1960-08-09 | Bofors Ab | Rigid dressings |
| DE1058589B (en) * | 1957-03-16 | 1959-06-04 | Continental Gummi Werke Ag | Process for the production of separators from glass fibers for accumulators |
| US2999123A (en) * | 1957-03-16 | 1961-09-05 | Continental Gummi Werke Ag | Separating plates |
| US3092509A (en) * | 1957-08-22 | 1963-06-04 | Oldham & Son Ltd | Glass fiber reinforced battery separators |
| US3184368A (en) * | 1959-12-29 | 1965-05-18 | Union Carbide Corp | Metal fiber containing structures and method therefor |
| US3287155A (en) * | 1962-11-08 | 1966-11-22 | Du Pont | Process for impregnating glass fiber mat with methyl methacrylate polymer |
| US3940536A (en) * | 1972-07-03 | 1976-02-24 | Compagnie Europeenne D'accumulateurs | Mechanically reinforced high porosity partially fused glass fiber galvanic separator |
| US5242765A (en) * | 1992-06-23 | 1993-09-07 | Luz Electric Fuel Israel Limited | Gas diffusion electrodes |
| US20060283135A1 (en) * | 2003-12-23 | 2006-12-21 | Fellinger Thomas J | Method of making a nodular inorganic fibrous insulation |
| US7608159B2 (en) | 2003-12-23 | 2009-10-27 | Johns Manville | Method of making a nodular inorganic fibrous insulation |
| US20070012809A1 (en) * | 2004-03-18 | 2007-01-18 | Fellinger Thomas J | Particles with a hose having a reduced internal diameter variation |
| US20070014641A1 (en) * | 2004-03-18 | 2007-01-18 | Fellinger Thomas J | System and method for forming an insulation particle/air suspension |
| US7789596B2 (en) | 2004-03-18 | 2010-09-07 | Johns Manville | System and method for forming an insulation particle/air suspension |
| WO2006023137A3 (en) * | 2004-07-23 | 2006-08-24 | Johns Manville | Control of pre-cured product moisture for formaldehyde-free fiberglass products |
| US20060257639A1 (en) * | 2004-12-22 | 2006-11-16 | Bianchi Marcus V A | Insulation having a thermal enhancement material and method of making same |
| US20080003431A1 (en) * | 2006-06-20 | 2008-01-03 | Thomas John Fellinger | Coated fibrous nodules and insulation product |
| US20080003432A1 (en) * | 2006-06-20 | 2008-01-03 | Thomas John Fellinger | Insulation having a fibrous material and method of making same |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2566960A (en) | Mineral fiber mat and process of making same | |
| US2664376A (en) | Mineral fiber mat and process of making same | |
| USRE23644E (en) | Battery separator | |
| DE69826862T2 (en) | NON-AQUEOUS SUBSTITUTES FOR GLASS FIBERS AND INJECTION MOLDABLE POLYMERS | |
| EP0705226B2 (en) | Method for manufacturing a mineral fiber product | |
| US3684645A (en) | Glass fiber reinforced thermoplastic article | |
| US5736475A (en) | Mineral fiber product containing polymeric material | |
| US4869855A (en) | Method of manufacturing molded articles | |
| DE2053167B2 (en) | Device for heat-pressure fusing of toner images | |
| EP0535223B1 (en) | Process for producing tubes or pipes formed from a thermoplastic powder impregnated fiberglass roving | |
| DE2322440A1 (en) | BIODEGRADABLE MATERIAL MADE OF PLASTIC | |
| US4358501A (en) | Storage stable polyolefin compatible size for fiber glass strands | |
| JPS6354735B2 (en) | ||
| US3673027A (en) | Method of forming coated fibers | |
| GB697627A (en) | A process and apparatus for moulding thermoplastic materials | |
| DE2125905A1 (en) | Process for expanding and drying expandable microspheres | |
| US3014085A (en) | Composite glass fiber battery separator | |
| US2550650A (en) | Process of producing a plastic composition from waste nylon fibers | |
| US3671378A (en) | Glass fiber reinforced composite and method of making same | |
| CN1042171A (en) | A kind of high-molecular coating glue and application thereof | |
| US2092903A (en) | Methods of coating abrasive grain | |
| US2981980A (en) | Production of light polarizing elements | |
| US3681157A (en) | Method for forming an integrated mass | |
| US2710426A (en) | Process for preparing thin films | |
| GB2154899A (en) | Stiffening materials, a process for their production and the use thereof |