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
  • 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
  • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
  • D21H17/24—Polysaccharides
• • 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]
  • Y10T428/31971—Of carbohydrate
  • Y10T428/31975—Of cellulosic next to another carbohydrate
• • 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]
  • Y10T428/31971—Of carbohydrate
  • Y10T428/31993—Of paper

Definitions

• This invention relates to water resistant or water repellent paper having desirable properties in the dry state, and to a method of manufacturing it.
• Paper as it is normally manufactured is readily wetted and tends to lose practically all its strength and to disintegrate on thorough Wetting thereof. Accordingly, it is of great importance to increase the wet strength of paper.
• Wet strength paper is ordinarily regarded as paper which retains 40-50% or more of its strength when it becomes thoroughly Wet. Such high wet strength paper has assumed a place of considerable importance in the manufacture of bags and other wrappings for Wet foods, construction and camouflage paper, map and blue-print paper, toweling, paper fabrics, twine. etc.
• Paper may be parchmentized by treatment with snlphuric acid, zinc chloride or the like, but while these treatments impart a certain wet strength to the paper, they also impart stiffness and harshness thereto, rendering the paper brittle in the dry state.
• Certain resinforming materials may be incorporated with the paper making fibers in the beater, or may be used to impregnate the paper web, the resinous properties being subsequently developed into paper by aid of heat and a suitable catalyst. Such materials are relatively expensive and if the necessary conditions of temperature, time, concentration, etc. are not strictly controlled, curing of the resin is likely to be more or less incomplete, resulting invariations in the characteristics of the finished paper. Furthermore, these resin treatments tend to render the paper brittle and to make it diificult to fold or wrap it around packages without tearing the paper.
• One object of this invention is to provide paper havin a predetermined moisture pickup capacity, excellent wet strength when wet, and desirable characteristics in the dry state such as flexibility, softness, and the ability to be mainpulated Without tearing. Another object is to provide such a paper economically. A further object is to provide paper having uniform high, dry and wet strength and substantially free from variations due to processes which depend upon curing operations.
• a dextran or dextran partial conversion product containing chemically bound radicals derived from higher fatty acids containing 8 to 18, preferably 12 to 18 carbon atoms.
• the dextrans are high molecular weight, polysacatent Percent by weight Sucrose 20.0 Corn steep liquor 2.0 Monobasic potassium phosphates 0.5 Manganous sulfate 0.002 Sodium chloride 0.50 Water Balance
• This medium is adjusted to a pH of between about 6.5 and about 7.5, preferably 7.2, and the sterilized material is cooled to room temperature and inoculated with a culture of the dextran-producing bacteria, for instance, Leuconostos mesenteroides B-5l2 (Northern Regional Research Laboratory classification) and incubated at 20 to 30 C. (optimum 25 C.) until a maximum yield of dextran has been attained; normally a period of between 12 and 48 hours will be satisfactory for this procedure.
• the fermented product contains approximately -85% of water and is a thick turbid liquid.
• acetone or alcohol which may be a water-miscible aliphatic, such as methyl, ethyl or isopropyl, is added in sufficient quantity to precepitate the dextran and this brings down, with the dextran, occluded and adsorbed bacteria, and nitrogenous and inorganic elements.
• the precipitated dextran may be dried in any suitable manner, for example by drum drying; Thereafter, it may be reduced to particulate condition.
• a purer dextran may be obtained by adding an aliphatic alcohol to the fermented culture at a pH between about 2.5 and 4.5.
• the precipitate thus obtained may be further purified by again precipitating it with the alchohol. Several precipitations may be performed.
• the dextran thus produced is a so-called native dextran having a high molecular weight and being, in the particular case, soluble in water at ordinary temperatures.
• the higher fatty acid radicals may be introduced into the molecule of high molecular weight dextrans such as the native product obtained as described above or an equivalent dextran, or dextrans of high molecular weight may be hydrolyzed to products of lower molecular weight prior to introduction of the fatty acid radicals.
• the by drolysis may be effected in any suitable way, as by means of acid or enzymatically.
• the dextran which is esterified may be obtained by hydrolyzing the initially water-soluble dextran obtained as described above, or a similar high molecular weight dextran, to a product having a molecular weight or average molecular weight in the range between 20,000 and 100,000, fractionating the hydrolysis product, if necessary, to obtain a fraction of preselected uniform or more nearly uniform molecular weight, and purifying the same by known methods for the removal ofpyrogens and coloring materials.
• dextran may be a so-called clinica dextran such as may be used as a blood plasma extender.
• the dextran may have a molecular weight between 5,000 and 50 10 ,-as determined .by light scattering measurements.
• the dextran to be esterified may be selected on the basis of whether it is to be applied to the paper as an aftercoating or added to the heater, those of lower molecular weight being generally preferred when the ester is to be incorporated in the paper-making stock.
• the dextran maybe obtained by inoculating the culture medium with microorganisms other than that mentioned above.
• it may be a water-soluble dextran obtained by the use of the microorganisms bearing the following NRRL classifications: Leuconostoc mesenterozdes B-119, B-1146, Bl190, or a water-insoluble or substantially water-insoluble dextran obtained by the use of Leuco'nostoc'mesenteroia'es 13-742, B-1191, B-1 196, 13-1208, B 1 216,.B1l20, 3-1144, 13-523 Streptobacterium d xtmnicumB-IZSland Betabacterium vermiforme 134139.
• the dextran is not limitedto oneprepared under any particular set of conditiongjnciuding the microorganism used. It may beproduced enzymatically, in the substantial absence of bacteria, by cultivating an appropriate microorganism, for example, Leuconostoc n'zescnteroides 13-512 to obtain a dextran producing enzyme, separating the enzyme from the medium in which it is produced, and introducing the enzyme into a medium in which dextran is produced .by the action of the enzyme. Also, the dextranmay be obtained by bacterial conversion of 1, 4 linkages of dcxtrin to 1, 6 linkages of dextran. The dextran may beinsoluble in water under ordinary conditions but soluble in aqueous alkali solution.
• the higher fatty acid radicals may be introduced into the dextran molecule by any appropriate method, to produce the dextran fatty acid esters to be associated with the paper or paper-like product.
• the esters may be prepared by the methods described in our pending application, Serial No. 351,743, filed April 28, 1953.
• the dextran the form of a free-flowing, white powder, may be reacted with an esterifying derivative of the higher fatty acid, and preferably 'a halide such as the chloride thereof, in the presence of an acid acceptor or binding agent such as an organic base, as for instance a hetero cyclic tertiary amine of the type of quinoline, pyridine, N-methyl morpholine, etc.
• reaction may be carricdout at temperatures between 100 C. and 155 C. for time periods varying inversely with the temperature between a half hour and three hours.
• the ester may be recovered from the crude reaction mixture by Washing the latter with water to remove the hydrochloride of the organic base, removing the aqueous layer, adding a solvent for the ester to the residual mass, precipitating the solution into a non-solvent for the ester, such as a lower aliphatic alcohol, and filtering to, obtain the ester.
• a non-solvent for the ester such as a lower aliphatic alcohol
• the introduction of the higher fatty acid radicals into the dextran molecule may be effected by reacting the dextran with the selected acid in the presence of an impeller which may be the anhydride of a monohalogenated monobasic organic acid, e. g., monochloro acetic anhydride, and an esterification catalyst such as magnesium perchlorate at temperatures at which the reaction mixture remains in the liquid state, in general in the range between 50 C. and 100 C.
• an impeller which may be the anhydride of a monohalogenated monobasic organic acid, e. g., monochloro acetic anhydride, and an esterification catalyst such as magnesium perchlorate
• the est r may be isolated from the crude reaction mass by cooling the mass, dissolving it in a solvent therefor, precipitating it into a non-solvent for the ester, and filtering the ester.
• the higher fatty acids which may be used as esterification agent, in the free acid form or in the form of their chlorides, are those containing from 8 to 18 carbon atoms and including caprylic, pelargonic, palmitic, margaric, and stearic acids, and the corresponding chlorides. Two or more of the substantially pure acids, or chlorides thereof, may be used, resulting in the production of mixed dextran esters. Or commercial acids, which comprise mixtures, may be used. For example, commercial or technical grade stearic acid, which comprises a mixture of stearic and palmitic acids, yields dextran stearate-palmitate.
• Higher fatty acid esters of the dextran may be produced in wh'ch the D. S. (degree of substitution or ratio of the fatty acid radicals to anhydroglucopyranosidic units of the dextran) is from less than 1.0 up to 3.0, by using the fatty acid or its chloride'in amounts varying between less than 1.0, say 0.1, and 10 parts thereof by weight per part of dextran.
• the fatty acid esters are resistant to moisture to an extent which depends on the D. S., the higher the proportion of the fatty acid radicals peranhydroglucopyranosidic unit, the greater the water resistance.
• the particular ester or mixed ester associated with the paper maybe selected, therefore, to render the paper water repellent or to control the amount of water which is picked up by the paper.
• the character istics of the paper may he predetermined so that, when moisture absorption without disintegration is required, those properties may be imparted to the paper, and when a water repellent paper which is not readily wetted, such as constructionpaper, is desired, a paper having those properties may be readily produced.
• the esters having a D. S. between about 2.5 and 3.0 are definitely hydrophobic and water repellent and are selected when a strongly water resistant paper is required.
• the partial esters i. e. those containing free hydroxyl groups, and say, an average of between 1.5 and 2.0 fatty acid radicals per anhydroglucopyranosidic unit are both hydrophilic and hydrophobic.
• Such esters may be predominantly hydrophilic or predominantiy hydrophobic, or the hydrophilic-hydrophobic properties may be essentially balanced.
• the 'hydrophilic-hydrophobic.esters may be associated with the paper when a paper of high wet strength having the capacity to absorb a certain amount of moisture is desired. 0
• esters derived from fatty acids having the higher carbon content possess a wax-like consistency and areparticularly advantageous for the'reason that they contribute to the flexibility and workability of the paper while conferring strength thereto coupled with either water repellency or a predetermined moisture absorption capacity.
• the dextran ester and the paper making fibers may be mixed by a method suitable to the production of a particular type of paper.
• the mixture of fibers and the higher fatty acid ester of the dextran may be formed into a web in any suitable way, for example, by the use of machines of various types such as the Fourdrinier, Harper, single cylinder or Yankee multi-vat machine, mold, press pate or the like.
• the dextran ester and the fibers are mixed and the mixture is stirred or beaten only long enough to insure that the ester'is substantially uniformly distributed through'the fiber suspension.
• the ester provides t e fibers with a coating which serves as a binder for them, presenting the possibility of eliminating the prolonged conventional beating usually resorted to for cyrsaxvse the purpose of hydrating and fibrillating the fibers, or of reducing .the heating time, and thus producing paper products in which the fibers are non-hydrated and undergraded and bound together by waterproof or water resistant dextran fatty acid ester.
• the amount of ester mixed with the fibers may be between 1% and 5% by weight, or higher.
• the paper is coated with the fatty acid ester of the dextran or dextran conversion product dispersed or dissolved in a suitable medium.
• the paper after calendering thereof may be coated with a solution of a higher fatty acid ester of a dextran, such as dextran palmitate or dextran stearate in a halogenated hydrocarbon such as chloroform or carbon tetrachloride, or with a solution thereof in an aromatic hydrocarbon such as benzene, toluene or Xylene.
• the coating may be applied by passing the paper through the solution, or by spraying or brushing the solution on the paper.
• the paper coated may be any conventional paper, such as that made by the sulfate, soda or sulfite process, or from rag pulp, cotton linters, or the base may be a web of discontinuous fibers such as the paper-like products which are sometimes described as non-woven fabrics.
• Solutions of ester of from 1% to 5% or more by weight may be used, the higher concentration, as much as up to by weight, being generally preferred if stiffer paper products are desired.
• the paper product or base On evaporation of the solvent, the paper product or base is provided with a more or less completely water resistant film which is firmly adherent to the base and which imparts a smooth surface to it, especially when the ester is derived from a fatty acid of the higher carbon content and exhibits the more pronounced wax-like properties.
• the paper of this invention may be used in water, dried, and reused a number of times without disintegrating. It is useful as toweling, drapery substitute, filtering material, twisting paper, disposable sheet material, impregnating paper, etc.
• the esters may be used for modifying the moisture pick-up capacity and hence the wet strength of all kinds of paper including tissue paper, writing paper, book paper, bank note paper, Wrapping paper; boards including Bristol board, wall board and box board, building felts and the like may be improved.
• the term paper product as used in the claims is intended to include all such papers, layers, tubes and molded articles of all kinds which are capable of being fabricated from paper making fibers and whether the ester is applied to the paper base as a coating or distributed through the base, or both.
• the paper comprising the dextran higher fatty acid ester has satisfactory printing qualities.
• Example I To beaten paper stock there is added, at the wet end of the paper-making machine, an aqueous dispersion of dextran palmitate having a D. S. of about 1.2 palmitoyl radicals per anhydroglucopyranosidic unit of the dextran, and derived from a dextran having a molecular weight of about 20,000, to introduce about 5% by Weight of the ester into the stock.
• the furnish or charge is then sheeted in a known manner on a Fourdrinier paper machine. The paper is processed in the usual manner.
• a finished paper having high dry and wet tearing and Example 11 A sheet of bleached kraft paper is passed through a treating bath comprising a 5% chloroform solution of dextran palmitate containing an average of 2.9 palmitoyl groups per anhydroglucopyranosidic unit of the dextran. The paper is passed between doctor blades arranged to remove excess treating medium from the opposite surfaces of the paper, and then dried. A finished water-repellant paper sheet having a smooth surface, good flexibility, and high dry and wet tearing and bursting strength is obtained.
• esters of dextran conversion products may be used instead of or in addition to the dextran esters.
• dextran conversion products low-substituted dextran having at least some free hydroxyl groups and in which the substituent groups are groups or radicals other than the saturated fatty acid radicals of 8 to 18 carbon atoms.
• the low-substituted dextran or dextran partial conversion products contemplated are those which, prior to the introduction of the radicals derived from the fatty acids of 8 to 18 carbon atoms, contain other chemically bound radicals or groups such as lower acyl radicals, i. e.
• the dextran conversion product may be a dextnan acetate, propionate, butyrate, etc., an ethyl, methyl, or benzyl dextran, etc., or a carboxymethyl dextran.
• the average ratio of lower acyl, alkyl, analkyl or carboxyalkyl groups to anhydroglucopyranosidic units of the dextran may be from less than 1:1 to 15:1, and the average ratio of acyl radicals derived from fatty acids of 8 to 18 carbon atoms to anhydroglucopyranosidic units of the dextnan may be from less than 1:1 to 29:1.
• the ratio of the higher fatty acid radicals to anhydroglucopyranosidic units is from less than 1:1 to about 2.511.
• the dextran esters have a natural affinity for the paper base and'adhere to it tenaciously.
• ester may be desirable, when the ester is added to the beater or at the wet end of the machine, and for more ready dispersion of the ester in the aqueous mass, especially when the ester is derived from a dextran of the higher molecular Weights, to use a higher fatty acid ester of a oarboxymethyl dextran.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of a dextran having, initially, at least some free hydroxyl groups, with a fatty acid containing from 8 to 18 carbon atoms.
• Calendered paper characterized by increased mois ture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of a dextran having, initially, at least some free hydroxyl groups, with a fatty acid containing from 12 to 18 carbon atoms.
• Oalendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of a dextran having, initially, at least some free hydroxyl groups, with palmitic acid.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of a dextran having, initially, at least some free hydroxyl groups, with stearic acid.
• Oalendercd paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of dextran with a fatty acid containing from 8 to 18 carbon atoms, said ester containing an average of 2.5 to 3.0 radicals derived from the fatty acid per anhydroglucose unit of the dextran.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of dextran with a fatty acid Containing from 12 to 18 carbon atoms, said ester containing an average of 2.5 to 3.0 radicals derived from the fatty acid per anhydroglucose unit of the dextran.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of dextran with palmitic acid, said ester containing an average of 2.5 to 3.0 palmitoyl radicals per anhydroglucose unit of the dextran.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of deXtran with stearic'acid, said ester containing an average of 2.5 to 3.0 stearoyl radicals per anhydroglucose unit of the dextran.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of carboxymethyl dextran with palmitic acid.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of carboxymethyl dextran with stearic acid.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of dextran with a fatty acid of 12 to 18 carbon atoms, said ester containing an average of about 2.9 radicals derived from fatty acids per anhydroglucose unit of the dextran.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of dextran with palmitic acid, said ester containing an average of about 2.9 palmitoyl radicals per anhydrolucos uni f he d r n- 13.
• Calendered paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially of an ester of dextran with stearic acid, said ester containing an average of about 2.9 stearoyl redicals per anhydroglucose unit of the dextran.
• the method of increasing the inoistureresistance of calendered paper comprising the steps of app-lyingv to the paper a composition consisting essentially of a so1ution of an ester of dextran having,,initially, at least some free hydroxyl groups with a fatty acid containing from 8 to 13 carbon atoms, in a halogenated hydrocarbon solvent for the ester, and then drying the product to leave thereon an adherent coating of the dextran ester.
• the method of increasing the moisture resistance of calendered paper comprising the steps of applying to the paper products a composition consisting essentially of solution of an ester of dextran with palmitic acid con tnining an average of 2.5 to. 3.0 palmitoyl radicals per anhydrcglucose unit of the dextran in the halogenated hydrocarbon solvent for the ester, and then drying the product to leave thereon an adherent coating of dextran palmitate.
• the method of increasing the moisture resistance of calendered paper which comprises the steps of applying to the paper a composition consisting essentially of a solution of an ester of dextran with stearic acid con.- taining an average of 2.5 to 3.0 stearoyl radicals per anhydroglucose unit of the dextran in the halogenated hydrocarbon solvent for the ester, and then drying the product to leave thereon an adherent coating of dextran stearatc.
• Paper characterized by increased moisture resistance imparted thereto by an adherent coating thereon consisting essentially :of an ester of dextran having, in.- itially, at least some free hydnoxyl groups, with a fatty acid containing from 8 to 18 carbon atoms.

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Cited By (6)

Citations (2)

• 0
  • BE BE556111D patent/BE556111A/xx unknown
• 1953
  • 1953-05-14 US US355162A patent/US2786786A/en not_active Expired - Lifetime

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