Classifications

• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
  • D21H13/10—Organic non-cellulose fibres
  • D21H13/12—Organic non-cellulose fibres from macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D21H13/14—Polyalkenes, e.g. polystyrene polyethylene
• • D—TEXTILES; PAPER
  • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
  • D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
  • D06N7/00—Flexible sheet materials not otherwise provided for, e.g. textile threads, filaments, yarns or tow, glued on macromolecular material
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
  • D21H13/36—Inorganic fibres or flakes
  • D21H13/38—Inorganic fibres or flakes siliceous
  • D21H13/40—Inorganic fibres or flakes siliceous vitreous, e.g. mineral wool, glass fibres
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
  • D21H17/20—Macromolecular organic compounds
  • D21H17/33—Synthetic macromolecular compounds
  • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D21H17/35—Polyalkenes, e.g. polystyrene
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
  • D21H17/20—Macromolecular organic compounds
  • D21H17/33—Synthetic macromolecular compounds
  • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
  • D21H17/375—Poly(meth)acrylamide
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
  • D21H17/20—Macromolecular organic compounds
  • D21H17/33—Synthetic macromolecular compounds
  • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
  • D21H17/42—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic
  • D21H17/43—Carboxyl groups or derivatives thereof
• • D—TEXTILES; PAPER
  • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
  • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
  • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
  • D21H17/20—Macromolecular organic compounds
  • D21H17/33—Synthetic macromolecular compounds
  • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
  • D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
  • D21H17/55—Polyamides; Polyaminoamides; Polyester-amides

Definitions

• This invention relates to flooring felt compositions and to a process for preparing them. More particularly, the invention relates to flooring felt compositions having the dimensional and thermal stability and the resistance to water and high humidity of asbestos-based compositions, but which additionally have the overall mechanical properties necessary to provide a satisfactory backing for the thermoplastic vinyl resins ordinarily used as floor coverings and to a process for making the same.
• cellulosic fibers have traditionally been a major component of fibrous compositions used as backing materials for vinyl floor coverings and linoleum.
• these floor covering products have not always exhibited satisfactory dimensional stability, and it has additionally been known that this problem of dimensional stability could be overcome through utilization of asbestos, in whole or in part, in place of the cellulosic fibers.
• asbestos-free formulations having the desirable properties of the asbestos-based compositions.
• U.S. Patent 4,274,916 discloses a backing material comprised of polypropylene fibers, wood pulp fibers, glass fibers, filler, polymeric binder and a cationic quaternary modified acrylic polymer.
• a wet strength resin including cationic resins, can be added.
• such a backing material having been found, said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• said material being an asbestos-free flooring felt composition
• All percentages of the above components are by weight based on the dry weight of the flooring felt composition
• compositions will have a.density of from about 0.35 to about 0.80 gm/cc, a dry tensile strength greater than 1000 psi, a hot (177°C.) tensile strength greater than 300 psi, where the composition has a basis weight of from about 160 to about 340 pounds/3000 sq. ft. and a thickness of from about 0.01 to about 0.04 inch (10 to 40 mils).
• these compositions are dimensionally stable, thermally stable, resistant to water, sufficiently flexible to permit easy installation of the floor covering product backed therewith, and resistant to discoloration upon exposure to heat and light.
• the process of preparing the compositions of this invention comprises the steps of forming an anionic aqueous fiber dispersion comprising from about 4 to about 55% and preferably from about 8 to about 35% of water dispersible spurted polyolefin fibers, from about 2 to about 30% of wood pulp fibers, from about 2 to about 20% of water dispersible glass fibers and from about 1 to about 10% of an anionic polyacrylamide resin containing from about 2 to about 15% by weight of acrylic acid units, adding to said anionic aqueous fiber dispersion from 0 to about 50% of an inorganic filler, from about 5 to about 25% of an anionic elastomeric polymeric binder and from about 1 to about 10% of the cationic resin reaction product of epichlorohydrin and a poly(diallylamine) or an aminopolyamide derived from a dicarboxylic acid and a polyalkylene polyamine having two primary amine groups and at least one secondary or tertiary amine group (all percentages of the above components being by weight
• the water dispersible spurted polyolefin fibers which are used in accordance with this invention typically can be prepared by a process wherein the polyolefin is dispersed in a liquid which is not a solvent for the polypropylene at its normal boiling point, heating the resulting dispersion at superatmospheric pressure to dissolve the polymer and then discharging the resulting solution into a zone of reduced temperature and pressure to form the fibrous product.
• the liquid in which the polyolefin is dispersed may be a halogenated hydrocarbon such as methylene chloride, chloroform or carbon tetrachloride, an aromatic hydrocarbon such as benzene, toluene or xylene, an aliphatic hydrocarbon such as pentane or hexane, or an alicyclic hydrocarbon such as cyclohexane.
• a halogenated hydrocarbon such as methylene chloride, chloroform or carbon tetrachloride
• an aromatic hydrocarbon such as benzene, toluene or xylene
• an aliphatic hydrocarbon such as pentane or hexane
• an alicyclic hydrocarbon such as cyclohexane.
• the pressure generated by the solvent vapors may, and normally will, be augmented by a pressurized inert gas such as nitrogen or carbon dioxide.
• the temperature to which the dispersion of the polyolefin in the solvent is heated to form a solution of the polyolefin will depend upon the particular solvent used but should be sufficiently high to effect dissolution of the polypropylene. Temperatures in the range of about 100° to about 225°C. ordinarily will be used, and the concentration of the polyolefin in the resulting solution normally will be from about 5 to about 40% by weight.
• the pressure on the polyolefin solution may be from about 600 to about 1500 p.s.i., preferably from about 900 to about 1200 p.s.i.
• the orifice through which the solution is discharged will have a diameter of from about one-2ialf to about fifteen millimeters and a length to diameter ratio of from about 1.0 to 10:1.
• the polyolefin fibers shown in the examples are spurted polypropylene and combinations of spurted polypropylene and polyethylene fibers.
• the invention is applicable not only to spurted polypropylene but to admixtures of from about 50 to about 100% polypropylene and from about 0 to about 50% polyethylene, based on the dry weight of the entire composition.
• spurted fibers prepared from polyethylene and copolymers of ethylene or propylene and other 1-olefins such as 1-butene, 4-methyl-pentane-l and 1-hexene, and mixtures of any of the aforementioned polymers may also be used in accordance with this invention.
• the wood pulp fibers used in the flooring felt compositions of this invention are anionic and are preferably of the bleached softwood pulp variety, for example, the Rayonier bleached softwood kraft _(RBK.) pulp fibers shown in the examples. These fibers have lengths of from about 0.05 to about 0.2 inch, with length to width ratios of about 100:1 or more. Also useful are hardwood pulp fibers, such as Weyerhaeuser bleached hardwood kraft (WBK) pulp fibers. Ordinarily, these fibers are used in combination with RBK pulp fibers, a 50:50 by weight admixture being highly satisfactory.
• WBK Weyerhaeuser bleached hardwood kraft
• the water dispersible glass fibers of the flooring felt compositions are characterized by very high tensile strengths and densities, excellent dimensional stability, thermal stability and resistance to water and moisture. They preferably average from about 0.1 to about 0.7 inch in length and from about 0.0002 to about 0.0006 inch in diameter.
• the inorganic fillers which may be used in the felt compositions of this invention are essentially water-insoluble and exemplified by the clay filler used in the examples.
• Alternative fillers are materials such as calcium carbonate, talc, magnesium silicate, calcium silicate, mica, aluminum silicate and diatomaceous earth.
• the particle size of the fillers is such that the major amount will be below 50 microns in diameter, with the average diameter generally being above 0.1 micron and preferably from about 0.1 to about 20 microns.
• the anionic elastomeric polymer binder component of the felt compositions is illustrated in the examples by the 50:50 styrene-butadiene copolymer containing carboxylic functionality.
• the ratio of the styrene component to the diene monomer may be varied from about 40:60 to about 90:10.
• ethylene-acrylic acid copolymers are also operable are ethylene-acrylic acid copolymers, the corresponding methacrylic acid copolymers, polychloroprenes containing carboxylic functionality, alkylacrylate-acrylonitrile-acrylic acid copolymers, the corresponding alkylmethacrylate copolymers, butadiene-acrylonitrile-methacrylic acid copolymers, the corresponding acrylic acid copolymers and vinyl acetate- acrylic acid copolymers.
• the elastomeric polymer binder will be in the form of a latex, that is, an aqueous colloidal dispersion, containing from about 35 to about 60% solids, usually about 50%.
• the latex will normally already contain, or have added thereto prior to use in accordance with this invention, a stabilizer to retard thermal discoloration of the polymer.
• the anionic polyacrylamide resin component used in accordance with this invention is a copolymer containing from about 85 to about 98% by weight of acrylamide units and from about 2 to about 15% by weight of acrylic acid units.
• the copolymer is normally obtained by copolymerization of acrylamide and acrylic acid, as illustrated in Example 4.
• Comparable products can be prepared, however, by partial hydrolysis of polyacrylamide or a poly(acrylamide-co-alkyl acrylate), such as a copolymer of acrylamide with ethyl acrylate. Any of these polyacrylamides are prepared by conventional methods for the polymerization of water-soluble monomers and preferably have molecular weights less than about 25,000, for example, in the range of from about 10,000 to about 20,000.
• One of the cationic resins used in this invention is the reaction product of epichlorohydrin and a poly(diallylamine). The preparation of such a product is shown in Example 2.
• Specific hydrohalide salts of the diallylamines which can be polymerized to provide the polymer units of the invention include diallylamine hydrochloride; N-methyldiallylamine hydrochloride; N-methyldiallylamine hydrobromide; 2,2'-dimethyl-N-methyldiallylamine hydrochloride; N-ethyldiallylamine hydrobromide; N-isopropyldiallylamine hydrochloride; N-tert-butyl- diallylamine hydrochloride; and N-octadecyldiallylamine hydrochloride.
• diallylamines and N-alkyldiallylamines are themselves prepared by the reaction of ammonia or a primary amine with an allyl halide.
• N-methyldiallylamine can be prepared by reaction of two moles of an allyl halide, such as allyl chloride, with one mole of methylamine.
• the latter is used in an amount ranging from about 0.5 mole to about 1.5 moles, preferably from about one mole to about 1.5 moles, per mole of secondary plus tertiary amine present in the polymer.
• the reaction is carried out at a t em- perature of from about 30° to about 80°C., preferably from about 40° to about 60°C., until the viscosity measured at 25°C. on a solution containing 20 to 30% solids is in the range of A to E, and preferably C to D, on the Gardner scale.
• the reaction preferably is carried out in aqueous solution to moderate the reaction, and at a pH of from about 7 to about 9 .
• the poly(diallylamine)-epichlorohydrin product can be stabilized against gelation by adjusting the pH of the solution to about 2 with, for example, sulfuric or hydrochloric acid.
• the other cationic resin which may be used in accordance with this invention is the reaction product of epichlorohydrin and an aminopolyamide derived from a dicarboxylic acid and a polyalkylene polyamine having two primary amine groups and at least one secondary or tertiary amine group.
• a representative product of this type is described in Example 3.
• Particularly suitable dicarboxylic acids are the saturated aliphatic dicarboxylic acids containing from 3 through 10 carbon atoms such as malonic acid, succinic acid, glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid, and sebacic acid.
• dicarboxylic acids include terephthalic acid, isophthalic acid, phthalic acid, maleic acid, fumaric acid, itaconic acid, glutaconic acid, citraconic acid, and mesaconic acid.
• a number of polyalkylene polyamines can be employed. Polyalkylene polyamines can be represented as polyamines in which the nitrogen atoms are linked together by groups of the formula --C n H 2n -- where n is a small integer greater than unity and the number of such groups in the molecule ranges from two up to about eight.
• Polyamines such as diethylenetriamine, triethylenetetramine, tetraethylenepentamine, and dipropylenetriamine, which can be obtained in reasonably pure form, are suitable for preparing water-soluble aminopoly- amides.
• Other polyalkylene polyamines that can be used include methyl bis-(3-aminopropyl)amine; methyl bis-(2-aminoethyl)amine; and 4,7-dimethyltriethylenetetramine. Mixtures of polyalkylene polyamines can be used, if desired.
• the temperatures employed for carrying out the reaction between the dicarboxylic acid and the polyalkylenepolyamine may vary from about 110°C. to about 250°C. or higher at atmospheric pressure. For most purposes, however, temperatures between about 160°C. and 210°C. have been found satisfactory and are preferred.
• it is pre- ⁇ ferred to use an amount of dicarboxylic acid sufficient to react substantially completely with the primary amine groups of the polyalkylenepolyamine but insufficient to react with the secondary and/or tertiary amine groups to any substantial extent. This will usually require a mole ratio of polyalkylenepolyamine to dicarboxylic acid of from about 0.9:1 to about 1.2:1. However, mole ratios of from about 0.8:1 to about 1.4:1 may be used with satisfactory results.
• the aminopolyamide In converting the aminopolyamide to a cationic resin, it is reacted with epichlorohydrin at a temperature from about 45°C. to about 100°C. and preferably between about 45°C. and 70°C. until the viscosity of a 20% solids solution at 25°C. has reached about C or higher on the Gardner scale.
• This reaction is preferably carried out in aqueous solution to moderate the reaction. Adjustment of pH is usually not necessary. When the desired viscosity is reached, sufficient water is then added to adjust the solids content of the resin solution to the desired amount, i.e., about 10% more or less, the product cooled to about 25°C. and then stabilized by adding sufficient acid to reduce the pH at least to about 6 and preferably to about 5.
• the spurted polyolefin fibers are needed to provide the required dimensional stability, resistance to water and moisture and tensile strength. Less than the lower limit of 4% by weight based on the dry weight of the composition gives a product inadequate in tensile strength. On the other hand, the upper limit of about 55% merely represents a practical amount, above which no outstanding advantages are obtained.
• the preferred amount of water dispersible spurted polypropylene fibers is from about 8 to about 35% by weight.
• the wood pulp fibers are needed for a number of reasons, one of which is to act as the dispersant for the polypropylene fibers in the aqueous medium in which the components of the flooring felt composition are brought together. In this capacity, about two parts of the wood pulp fibers per 100 parts of the polypropylene fibers is desirable. In addition to acting as the dispersant for polypropylene fibers, the wood pulp fibers provide uniformity and smoothness during sheet formation, with no formation of clumps or floc. Other dispersants are in no way comparable to wood pulp fibers in this respect. Moreover, the presence of wood pulp fibers in the flooring felt composition improves appreciably its tensile strength. At least about two percent of the wood pulp fibers is required to insure proper sheet formation, and increasing amounts up to about 30% by weight provide the desired improvement in tensile strength. The preferred range is from about 5 to about 10%.
• the water dispersible glass fibers are also required to contribute to tensile strength and dimensional stability, and they also provide thermal stability to the flooring felt composition, all of which are important properties.
• the amount of water dispersible glass fibers to provide these properties is in the range of from about 2 to about 20% by weight based on the dry weight of the flooring felt composition. A preferred range is from about 3 to about 10% by weight.
• the inorganic filler is not a necessary component of the flooring felt composition. However, its presence will not only decrease the overall cost of the composition but will also increase the density and decrease the stiffness of the composition when such changes in these properties of the composition are desired.
• the amount of filler will ordinarily be in the range of from about 10 to about 20% by weight but should not exceed about 50%, since at higher levels it detracts from the overall balance of properties desired in the composition.
• the anionic elastomeric polymer binder component is essential to the cohesion of the fibrous components and the filler, if present, and also to the water and moisture resistance of the flooring felt composition.
• a composition containing no binder may absorb as much as twice the amount of water as a composition containing the binder.
• the amount of the binder should be at least about 5% up to about 25% by weight based on the dry weight of the flooring felt composition, preferably from about 10 to about 15% by weight. It is noteworthy that the effectiveness of the binder is dependent upon the presence of both the anionic and cationic resin components of the composition. In the absence of both resin components, the tensile strength of the composition is inadequate, and the same is true when either one of the resin components is not present.
• anionic and cationic resin components each is necessary, as just mentioned, and the amount required is from about 1 to about 10% by weight, preferably from about 2 to about 5%.
• the anionic resin functions to maintain the anionic character of the aqueous fiber dispersion up to and during the addition of the anionic, elastomeric polymer binder, and the cationic resin functions to precipitate the polymer binder on the fiber and filler, if present, components of the composition and to react with the anionic resin to form a crosslinked composition.
• the particular order of addition of the various components is readily determinable by one skilled in the paper making art.
• a major factor is the arrangement of the available paper making equipment.
• a second factor is whether the water dispersible spurted polyolefin fibers and the wood pulp fibers are to be refined. Where refining is desired, these fibers may be refined either separately or together.
• the inorganic filler, the anionic polyacrylamide resin and anionic elastomeric polymeric binder may be added in any order, before or after, refining of the fibers.
• the water dispersible glass fibers and the cationic resins are preferably not added until after any refining has been completed. Otherwise the water dispersible glass fibers may be added at any time. Regardless of whether refining has occurred, it has been found preferable to add at least some of the cationic resin after all of the anionic elastomeric polymer binder has been incorporated into the composition.
• components may be present in minor amounts in the flooring felt compositions of this invention, being present in the aggregate in an amount no more than about 10% and usually no more than about 3 to about 5%. They are minor also in the sense that they do not directly contribute functionally to the physical properties of the compositions.
• exemplary of such components are stabilizers for the polypropylene fibers and the polymer binder, antioxidants, pigments, dyes and preservatives such as mildewicides.
• Also present may be small amounts of defoamers, retention aids and drainage aids, all to improve the efficiency of the operation of the papermaking machine used in forming the felt compositions.
• one or more layers of resinous polymeric compositions are applied to the flooring felt backing material.
• resinous polymeric compositions are generally based on vinyl chloride homopolymers or copolymers, but also may be based on polyurethanes and other suitable thermoplastic polymers. Methods of preparing such layers of the resinous polymeric compositions are disclosed, for example, in U.S. 3,293,094 and U.S. 3,293,108, both to Nairn et al.
• the compositions of this invention may also be. used to form other useful products, such as gaskets, filters and acoustical board, wherein the physical properties of the compositions are desired.
• This example illustrates the preparation of a typical spurted polypropylene fiber used in accordance with this invention.
• One hundred eighty parts of isotactic polypropylene having an intrinsic viscosity of 2.7 dl/g in decahydronaphthalene at 135°C. and 1020 parts of pentane were charged to a closed autoclave.
• the contents of the autoclave were stirred and heated to 160°C., at which point the vapor pressure in the autoclave was raised to 850 p.s.i. by the introduction of nitrogen.
• this product was composed of very fine filaments, of a thickness of the order of a micron, connected to one another to form a three-dimensional network.
• the general shape of the fibers, which have a flocculent appearance, is oblong. Their length varies from about one-half millimeter to about five centimeters and their diameter varies from about one-hundreth of a millimeter to about five millimeters.
• the specific surface area of these products is greater than one square meter per gram and in some cases may be greater than ten square meters per gram.
• This example shows the preparation of an epichlorohydrin- poly(diallylamine) reaction product usable as the cationic resin component in accordance with this invention.
• methyldiallylamine was slowly added 290-295 parts of concentrated hydrochloric acid to provide a solution having a pH of 3 to 4. The solution then was sparged with nitrogen for 20 minutes and the temperature was adjusted to 50° to 60°C.
• the resin product from the above process, prior to use ih accordance with this invention, is preferably base activated. This is accomplished by adding 18 parts of water and 12 parts' of one molar sodium hydroxide solution to each 10 parts of the 20% solids solution of the resin. The resulting five percent solids solution, after aging for 15 minutes, should have a pH of 10 or higher. Additional sodium hydroxide should be added, if necessary, to obtain this level of pH.
• the present example illustrates the preparation of a typical epichlorohydrin-aminopolyamide reaction product also utilizable as the cationic resin in accordance with this invention.
• Diethylenetriamine in the amount of 0.97 mole was added to a reaction vessel equipped with a mechanical stirrer, a thermometer and a reflux condenser. There then was gradually added to the reaction vessel one mole of adipic acid with stirring. After the acid had dissolved in the amine, the reaction mixture was heated to 170°-175°C. and held at that temperature for one and one-half hours, at which time the reaction mixture had become very viscous. The reaction mixture then was cooled to 140°C., and sufficient water was added to provide the resulting polyamide solution with a solids content of about 50%.
• a sample of the polyamide isolated from this solution was found to have a reduced specific viscosity of 0.155 dl/g when measured at a concentration of two percent in a one molar aqueous solution of ammonium chloride.
• the polyamide solution was diluted to 13.5% solids and heated to 4 ⁇ °C., and epichlorohydrin was slowly added in an amount corresponding to 1.32 moles per mole of secondary amine in the polyamide.
• the reaction mixture then was heated at a temperature between 70° and 75°C. until it attained a Gardner viscosity of E-F.
• Sufficient water next was added to provide a solids content of about 12.5%, and the solution was cooled to 25°C.
• the pH of the solution then was adjusted to 4.7 with concentrated sulfuric acid.
• the final product contained 12.5% solids and had a Gardner viscosity of B-C.
• This example describes the preparation of a representative polyacrylamide which is used as the anionic resin in accordance with this invention.
• a reaction vessel equipped with a mechanical stirrer, a thermometer, a reflux condenser and a nitrogen adapter was added 890 parts of water.
• a reaction vessel equipped with a mechanical stirrer, a thermometer, a reflux condenser and a nitrogen adapter was added 890 parts of water.
• acrylamide two parts of acrylic acid and one and one-half parts of aqueous 10% cupric sulfate.
• the resulting solution was sparged with nitrogen and heated to 76°C., at which point two parts of ammonium persulfate dissolved in six and one-half parts of water was added.
• the temperature of the reaction mixture increased 21.5°C. over a period of three minutes following addition of the persulfate.
• the temperature returned to 76°C., it was maintained there for two hours, after which the reaction mixture was cooled to room temperature.
• the resulting solution had a Brookfield viscosity of 54 centipoises at 21°C. and contained less than 0.2% acrylamide based on the polymer content.
• This example describes the preparation of one of the flooring felt compositions of this invention.
• a one-quart Waring blender was charged with 500 milliliters of water. To the water was added with stirring an admixture of 3.46 grams of water dispersible spurted polypropylene fibers, 0.43 gram of Rayonier bleached softwood kraft (RBK) fibers, 0.97 gram of water dispersible spurted polyethylene fibers and then an additional 1.30 grams of RBK fibers. The dispersion was transferred to a two-liter container equipped with a highspeed stirrer.
• RBK Rayonier bleached softwood kraft
• Water was added to provide a total volume of one liter of the dispersion, after which the following were added with stirring: 10.15 grams of clay presuspended in approximately 80 milliliters of water; 2.83 grams of a manufacturer-stabilized carboxylated styrene-butadiene copolymer latex, commercially available as Dow XD 30608 (added as a 50% solids latex additionally diluted with about 20 milliliters of water); 0.03 gram of a cationic polyacrylamide retention aid (commercially available as Betz 1260), previously dissolved in 6 milliliters of water; 0.97 gram of water dispersible glass fibers having a length of about 3 milliliters and a diameter of about 6 microns; 8.15 grams of the anionic polyacrylamide resin solution (containing 0.81 gram of polymer) prepared according to Example 4; and 13.0 grams of the base-activated cationic resin solution (containing 0.65 gram of resin) prepared according to Example 2.
• the fibrous dispersion resulting from the above process was formed into a sheet on a 100-mesh screen.
• the formed sheet was wet pressed and then dried by six passes over a 24 ⁇ -25 ⁇ °F drum dryer, the side of the sheet in contact with the drum being alternated on each pass.
• the individual components thereof were present in the following amounts: spurted polyethylene fibers, 4.5%; spurted polypropylene fibers, 16.0%: wood pulp fibers, 8.0%; glass fibers, 4.5%; clay, 47.0%; stabilized butadienestyrene copolymer, 13.1%; anionic resin, 3.75%; cationic resin, 3.0%; and cationic retention aid, 0.14%.
• the felt composition was found to have a basis weight of 302 pounds/3000 square feet, a caliper of 30 mils, a density of 0.710 gram/cubic centimeter, a dry tensile strength of 1353 p.s.i. and a hot (177°C) tensile strength of 522 p.s.i.
• a handsheet was prepared according to the procedure of Example 5 except that the base-activated cationic resin solution of Example 2 was omitted. Upon analysis the felt composition was found to have a basis weight of 285 pounds/ 3000 square feet, an average caliper of 32.4 mils, a density of 0.563 gram/cubic centimeter, a dry tensile strength of only 315 p.s.i., and a hot (177°C) tensile strength of only 68 p.s.i.
• a handsheet was prepared according to the procedure of Example 5 except the anionic polyacrylamide resin solution of Example 4 was omitted.
• the felt composition was found to have a basis weight of 283 pounds/3000 square feet, an average caliper of 30.9 mils, a density of 0.586 grams/cubic centimeter, a dry tensile strength of only 709 pounds/ square inch, and a hot (177°C) tensile strength of only 152 p.s.i.
• a handsheet was prepared according to the procedure of Example 5 except that the 0.03 grams of cationic polyacrylamide retention aid was replaced by 0.17 gram of alum (aluminum sulfate octadecahydrate).
• the felt composition was found to have a basis weight of 302 pounds/ 3000 square feet, a caliper of 27.2 mils, a density of 0.719 gram/cubic centimeter, a dry tensile strength of 1513 pounds/ square inch, and a hot (177°C) tensile strength of 595 p.s.i.
• Example 5 Following the procedure of Example 5, additional flooring felt compositions were prepared and evaluated.
• the com- postions are described in Table 1, and their physical properties are set forth in Table 2.
• Example 5 The procedure of Example 5 was duplicated except to replace the cationic resin component of that example with an equal amount of the cationic resin prepared in accordance with Example 3.
• the flooring felt product had a basis weight of 322 pounds/3000 square feet, a caliper of 27.4 mils, a specific gravity of 0.751 gram/cubic centimeter, a dry tensile strength of 1773 p.s.i. and a hot (177°C) tensile strength of 478 p.s.i.
• the dilute pulp slurry existing at this point in the process was pumped to a conventional Fourdrinier paper machine and formed into a sheet, the rate of addition of the slurry to the wire, the wet pressing, the drying and the calendering being balanced so as to produce a sheet having a thickness in the range of 20 to 30 mils and a specific gravity in the range of 0.600 to 0.700.
• the felt composition product was found to have a basis weight of 220 pounds/3000 square feet, a caliper of 21 mils, a specific gravity of 0.670, a dry tensile strength of 1620 p.s.i. and a hot (177°C) tensile strength of 470 p.s.i.

Landscapes

• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Inorganic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Textile Engineering (AREA)
• Paper (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Epoxy Resins (AREA)

Applications Claiming Priority (2)

Publications (1)

Family

ID=23557344

Family Applications (1)

Country Status (2)

Cited By (7)

Citations (7)

• 1983
  • 1983-06-29 JP JP11622883A patent/JPS5966600A/ja active Pending
  • 1983-06-30 EP EP83106392A patent/EP0097974A1/fr not_active Withdrawn

Patent Citations (7)

Also Published As

Similar Documents

Legal Events