US3065041A - Method of graft-polymerizing acrylate monomers onto paper in presence of ethylene dimethacrylate, and resulting product - Google Patents

Method of graft-polymerizing acrylate monomers onto paper in presence of ethylene dimethacrylate, and resulting product Download PDF

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US3065041A
US3065041A US730248A US73024858A US3065041A US 3065041 A US3065041 A US 3065041A US 730248 A US730248 A US 730248A US 73024858 A US73024858 A US 73024858A US 3065041 A US3065041 A US 3065041A
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weight
paper
acrylate
ceric
substrate
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US730248A
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Suen Tzeng Jiueq
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Wyeth Holdings LLC
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American Cyanamid Co
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Priority to FR792212A priority patent/FR1221546A/en
Priority to BE577900A priority patent/BE577900A/en
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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
    • D21H17/03—Non-macromolecular organic compounds
    • D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/18—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with itself, or other added substances, e.g. by grafting on the fibres
    • D21H17/19—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with itself, or other added substances, e.g. by grafting on the fibres by reactions only involving carbon-to-carbon unsaturated bonds
    • 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
    • D21H13/02—Synthetic cellulose fibres
    • D21H13/08—Synthetic cellulose fibres from regenerated cellulose
    • 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
    • D21H13/18—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylonitriles
    • 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
    • D21H13/20—Organic non-cellulose fibres from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H13/26—Polyamides; Polyimides
    • 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
    • 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
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S8/00—Bleaching and dyeing; fluid treatment and chemical modification of textiles and fibers
    • Y10S8/18—Grafting textile fibers

Definitions

  • This invention relates to a novel process for polymerizing certain lower alkyl acrylates with a cellulosic paper in the presence of a polymerizable cross-linking agent and to the products thus produced. Still further, this invention relates to a method for treating cellulosic paper webs by reacting the same with a monomeric lower alkyl acrylate while polymerizing said acrylate and cross-linking the polymerized reaction product with small quantities of a polyfunctional cross-linking agent.
  • One of the objects of the present invention is to produce an improved cellulosic product by reacting a cellulose containing paper with a monomeric lower alkyl acrylate in the presence of a cross-linking agent.
  • a further object of the present invention is to improve the properties of cellulosic paper Webs by practicing the process of the present invention.
  • a cellulosic paper is graft polymerized with a lower alkyl acrylate in an aqueous system using a ceric salt as the polymerization initiator and in the presence of small quantities of certain cross-linking agents.
  • the aqueous system may be either a solution of the particular monomer employed in Water or a system wherein the monomer is in the aqueous medium in a dispersed and/or emulsified state. These latter systems are preferred.
  • the cellulosic paper substrates suitable and operable in the process of the present invention can be any one of the well known cellulosic types. This designation is broadly intended to include paper fabricated from natural cellulose fibers and/ or regenerated cellulose fibers. One may additionally use paper substrates which contain comparatively small amounts of noncellulosic fibers such as glass, rayon, superpolyamides (polyhexamethyleneadipamide), polyacrylonitrile and similar synthetic type fibers. It is preferred that the amount of the noncellulosic fibers of these types does not constitute more than about 20% of the total weight of the paper substrate.
  • the cellulosic paper substrates to be employed in the practice of the process of the present invention be reasonably free of systems other than the fibrous material composing the paper.
  • systems it is meant the various inorganic fillers and water insolubles that may be present in paper.
  • the paper substrate be free of these materials, but desirably so, from an efiiciency standpoint in that the inert materials such as inorganic materials do not contribute significantly to the products of this invention and, of course, if these impurites are water soluble, they are leached out by the aqueous medium and in such instance would serve no useful purpose within the reaction system.
  • the cellulosic paper substrates employed in the practice of the present invention be of any particular porosity. Nevertheless, the porosity of the paper is important from the standpoint of an efficient processing technique. It has been observed that in the practice of the process of the present invention porous paper allows the monomers and ceric ions to penetrate readily the interstices of the substrate thereby facilitating the grafting mechanism so that a considerable area of the substrate becomes readily available as potential grafting points. Obviously, there are almost unlimited numbers of fabricated papers varying in thickness and degree of porosity which may be used in the practice of this invention. This invention, therefore, contemplates the use of all of these grades of paper to prepare the prodnets of this invention.
  • the cellulosic substrate is suspended in the aqueous medium containing the ceric ion and the monomeric acrylate with the pH of the system adjusted to 3.5 or below and in the presence of between about 0.01% and 1.0% by weight based on the total weight of monofunctional acrylate of a divinylidene monomeric compound having at least two ethylenic linkages which are in conjugation with other unsaturated linkages which latter are themselves nonethylenic.
  • the cellulosic substrate in the system serves as a backbone onto which the monomeric arcylate is grafted. Upon the addition of the ceric salts, and under the pH conditions required, the graft polymerization reaction begins.
  • each hydroxyl group of the cellulose substrate serves as a potential grafting point.
  • the number of these reactive groups which provide actual graft points is a function of the ceric ion concentration, among other factors, including the particular acidity of the system, the temperature at which the graft polymerization is carried out and the concentration of monomer in the system.
  • the polymeric links to which the monomer extends is a function of monomer concentration, ceric ion concenrtation, temperature and time of reaction.
  • the amount of pickup i.e., the amount of polymeric material chemically attached to the substrate may be varied over a fairly wide range. This range can be conveniently expressed in the terms of the original dry weight of the cellulosic paper substrate. Using such a basis, the pickup amounts contemplated herein range from about to about 900% and preferably from about 200% to about 500%.
  • the temperature may be controlled between about 5 C. and 100 C. but preferably at temperatures between about 10 C. and 60 C. Temperatures significantly above 70 C. are to be avoided because the hydroxyl groups of the cellulosic paper and the ceric salts used herein constitute a redox system which is prone to decompose too rapidly at these elevated temperatures, thus diminishing the effectiveness of the system.
  • the process of the present invention may be carried out under superatmospheric pressure or even under partial vacuum but it is preferred for practical purposes to utilize atmospheric pressure inasmuch as the reaction runs very favorably at this pressure.
  • the graft polymerization reaction of the present invention is carried out in an acidic aqueous medium.
  • the pH of said medium may be any value up to and including 3.5. For optimum results, it is preferred that the pH value he maintained between 1 and 2. Suitable acids for obtaining the desired pH are adequately shown in the specific examples set forth hereinbelow.
  • ceric ion is preferably introduced into the reaction mixture according to the present invention in the form of a ceric salt.
  • the salts adapted for use in the present invention are ceric nitrate, ceric sulfate, ceric ammonium nitrate, ceric ammonium sulfate, ceric ammonium pyrophosphate, ceric iodate and the like. These compounds may be employed singly or in combination with one another.
  • Ceric compounds which are capable of forming ceric salts in situ under the acid conditions of the polymerization reaction such as ceric oxide, ceric hydroxide and the like may be used.
  • the monomers useful in preparing the novel products of this invention are certain alkyl esters of acrylic acid. Specifically, these monomers are ethyl acrylate, propyl acrylate, and butyl acrylate.
  • the various isomeric forms of propyl acrylate and butyl acrylate, namely, isopropyl acrylate, sec-butyl acrylate, tert-butyl acrylate are contemplated herein. Obviously, these monomers may be used singly or in combination. All of the monomeric substances mentioned hereinabove give types of plastic products having the singular properties attributed to the products of this invention.
  • These vinylidene monomeric compounds must have at least two ethylenic linkages which are in conjugation with other unsaturated linkages which latter unsaturated linkages are themselves nonethylenic.
  • the cross-linking agents of this class which may be used in the practice of the process of the present invention are such monomers that result from the full esterification of a glycol with an alpha, beta-ethylenically unsaturated monocarboxylic acid.
  • these cross-linking agents result from the complete esterification of ethylene glycol, propanediol-1,3, butanediol-1,4 and the like, with acrylic acid, methacrylic acid and the like.
  • acrylic acid methacrylic acid and the like
  • cross-linking agents as divinyl benzene, divinyl naphthalene and the like.
  • the alkylene bis acrylamides may also be utilized effectively such as those disclosed in the US. Patent No. 2,475,846. Obviously, these cross-linking agents may be used either singly or in combination with one another.
  • Example 1 An emulsion is prepared by mixing, in a Waring Blendor for 3 minutes, 2250 parts of distilled water, 125 parts of a mixture of monomeric n-butyl acrylate and ethylene dimethacrylate (99.9%-0.1% respectively, each inhibitor free) and 1.425 parts of octadecyl trimethyl ammonium chloride, 50% solids in Water.
  • the emulsion thus prepared is introduced into a suitable reaction vessel equipped with a purging tube. 12.5 parts of a cellulosic filter paper is immersed in the emulsion.
  • the system is purged for 30 minutes with prepurified nitrogen at 500 parts per minute whereupon 125 parts of a 0.1 molar solution of ceric ammonium nitrate in 1 molar nitric acid is added and the purging continued during the entire run. After reacting at 25 C., the treated paper is removed and washed thoroughly with water. The paper is dried to a constant weight at 220 F. and the paper shows a polymer pickup of parts per hundred parts of paper weight.
  • Example 2 Example 1 is repeated in all details except that the reaction time is increased to give a polymer pickup of 250 parts per hundred parts of paper weight.
  • Example 3 Example 1 is repeated in every detail except that the weight ratio of the monomeric n-butyl acrylate to the ethylene dimethacrylate is 99%1%, respectively.
  • Example 4 Example 2 is repeated in every detail except that the weight ratio of the monomeric n-butyl acrylate to the ethylene dimethacrylate i 99%1%, respectively.
  • Example 5 Example 1 is repeated in every detail except that no cross-linking agent is used with the n-butyl acrylate.
  • Example 6 Example 2 is repeated in every detail except that no cross-linking agent is used with the n-butyl acrylate.
  • Example 7 Example 1 is repeated in all details except that the monomer to cross-linking agent was 99.5%0.5%, respectively.
  • Example 8 Example 2 is repeated in all retails except that the monomer to cross-linking agent was 99.5%0.5%, re-
  • a process comprising graft polymerizing a monomeric compound selected from the group consisting of ethyl acrylate, propyl acrylate and butyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the total weight of said acrylates, of ethylene dimethacrylate onto a paper substrate composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of a ceric salt which is soluble in at least one component of the reaction medium until the weight of said monoacrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
  • a process comprising graft polymerizing butyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacryate onto a cellulosic paper web composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of 'a ceric salt which is soluble in at least one component of the reaction medium until the Weight of said butyl acrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
  • a process comprising graft polymerizing ethyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacrylate onto a cellulosic paper web composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of a ceric salt which is soluble in at least one component of the reaction medium until the Weight of said ethyl acrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
  • a process comprising graft polymerizing propyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacrylate onto a cellulosic paper Web composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of a ceric salt which is soluble in at least one component of the reaction medium until the weight of said propyl acrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
  • a cellulosic paper Web reacted With butyl acrylate and from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacryate, wherein said butyl acrylate on said paper is in a graftpolymerized state and is present in an amount varying between about 100% and 900% by weight based on the Weight of said paper Web.
  • a cellulosic paper web reacted with ethyl acrylate and from about 0.01% to about 1%,by Weight, based on the weight of said acrylate of ethylene dimethacrylate, wherein said ethyl acrylate on said paper is in a graftpolymerized state and is present in an amount varying between about 100% and 900% by weight based on the weight of said paper web.

Description

United States Patent Ofiice 3,0650% Patented Nov. 20, 1962 METHOD OF GRAFTTOLYMERIZING ACRYLATE MQNOMERS ONTO PAPER IN PREENCE F ETHYLENE DlMETI-LACRYLATE, AND RESULT- ING PRGDUCT Tzeng .liueq Siren, New Canaan, Conn, assignor to American Cyanamid Company, New York, N.Y., a corporation of Maine No Drawing. Filed Apr. 23, 1958, Ser. No. 730,248
7 Claims. (Cl. 8-416) This invention relates to a novel process for polymerizing certain lower alkyl acrylates with a cellulosic paper in the presence of a polymerizable cross-linking agent and to the products thus produced. Still further, this invention relates to a method for treating cellulosic paper webs by reacting the same with a monomeric lower alkyl acrylate while polymerizing said acrylate and cross-linking the polymerized reaction product with small quantities of a polyfunctional cross-linking agent.
One of the objects of the present invention is to produce an improved cellulosic product by reacting a cellulose containing paper with a monomeric lower alkyl acrylate in the presence of a cross-linking agent. A further object of the present invention is to improve the properties of cellulosic paper Webs by practicing the process of the present invention. These and other objects of the present invention will be discussed in greater detail hereinbelow.
In the practice of the process of the present invention, a cellulosic paper is graft polymerized with a lower alkyl acrylate in an aqueous system using a ceric salt as the polymerization initiator and in the presence of small quantities of certain cross-linking agents. The aqueous system may be either a solution of the particular monomer employed in Water or a system wherein the monomer is in the aqueous medium in a dispersed and/or emulsified state. These latter systems are preferred.
The cellulosic paper substrates suitable and operable in the process of the present invention can be any one of the well known cellulosic types. This designation is broadly intended to include paper fabricated from natural cellulose fibers and/ or regenerated cellulose fibers. One may additionally use paper substrates which contain comparatively small amounts of noncellulosic fibers such as glass, rayon, superpolyamides (polyhexamethyleneadipamide), polyacrylonitrile and similar synthetic type fibers. It is preferred that the amount of the noncellulosic fibers of these types does not constitute more than about 20% of the total weight of the paper substrate. It is additionally preferred that the cellulosic paper substrates to be employed in the practice of the process of the present invention be reasonably free of systems other than the fibrous material composing the paper. By other systems, it is meant the various inorganic fillers and water insolubles that may be present in paper. It is not imperative that the paper substrate be free of these materials, but desirably so, from an efiiciency standpoint in that the inert materials such as inorganic materials do not contribute significantly to the products of this invention and, of course, if these impurites are water soluble, they are leached out by the aqueous medium and in such instance would serve no useful purpose within the reaction system. Furthermore, it is not imperative that the cellulosic paper substrates employed in the practice of the present invention be of any particular porosity. Nevertheless, the porosity of the paper is important from the standpoint of an efficient processing technique. It has been observed that in the practice of the process of the present invention porous paper allows the monomers and ceric ions to penetrate readily the interstices of the substrate thereby facilitating the grafting mechanism so that a considerable area of the substrate becomes readily available as potential grafting points. Obviously, there are almost unlimited numbers of fabricated papers varying in thickness and degree of porosity which may be used in the practice of this invention. This invention, therefore, contemplates the use of all of these grades of paper to prepare the prodnets of this invention. In carrying out the process of the present invention, the cellulosic substrate is suspended in the aqueous medium containing the ceric ion and the monomeric acrylate with the pH of the system adjusted to 3.5 or below and in the presence of between about 0.01% and 1.0% by weight based on the total weight of monofunctional acrylate of a divinylidene monomeric compound having at least two ethylenic linkages which are in conjugation with other unsaturated linkages which latter are themselves nonethylenic. The cellulosic substrate in the system serves as a backbone onto which the monomeric arcylate is grafted. Upon the addition of the ceric salts, and under the pH conditions required, the graft polymerization reaction begins. Theoretically, at least, each hydroxyl group of the cellulose substrate serves as a potential grafting point. The number of these reactive groups which provide actual graft points is a function of the ceric ion concentration, among other factors, including the particular acidity of the system, the temperature at which the graft polymerization is carried out and the concentration of monomer in the system. Once these grafts are accomplished, the polymeric links to which the monomer extends is a function of monomer concentration, ceric ion concenrtation, temperature and time of reaction. The amount of pickup, i.e., the amount of polymeric material chemically attached to the substrate may be varied over a fairly wide range. This range can be conveniently expressed in the terms of the original dry weight of the cellulosic paper substrate. Using such a basis, the pickup amounts contemplated herein range from about to about 900% and preferably from about 200% to about 500%.
In carrying out the precess of the present invention, the temperature may be controlled between about 5 C. and 100 C. but preferably at temperatures between about 10 C. and 60 C. Temperatures significantly above 70 C. are to be avoided because the hydroxyl groups of the cellulosic paper and the ceric salts used herein constitute a redox system which is prone to decompose too rapidly at these elevated temperatures, thus diminishing the effectiveness of the system.
The process of the present invention may be carried out under superatmospheric pressure or even under partial vacuum but it is preferred for practical purposes to utilize atmospheric pressure inasmuch as the reaction runs very favorably at this pressure.
The graft polymerization reaction of the present invention is carried out in an acidic aqueous medium. The pH of said medium may be any value up to and including 3.5. For optimum results, it is preferred that the pH value he maintained between 1 and 2. Suitable acids for obtaining the desired pH are adequately shown in the specific examples set forth hereinbelow.
The amount of ceric compound which is utilized in the practice of the process of the present invention may be varied over fairly wide limits. 'For example, one may utilize from about 10 to 10* mol of ceric ion per mol of polymerizable monomer. Preferably, one would use between 10" to 10" mol of ceric ion per mol of polymeriza ble monomer. Ceric ion is preferably introduced into the reaction mixture according to the present invention in the form of a ceric salt. Among the salts adapted for use in the present invention are ceric nitrate, ceric sulfate, ceric ammonium nitrate, ceric ammonium sulfate, ceric ammonium pyrophosphate, ceric iodate and the like. These compounds may be employed singly or in combination with one another. Ceric compounds which are capable of forming ceric salts in situ under the acid conditions of the polymerization reaction such as ceric oxide, ceric hydroxide and the like may be used.
The monomers useful in preparing the novel products of this invention are certain alkyl esters of acrylic acid. Specifically, these monomers are ethyl acrylate, propyl acrylate, and butyl acrylate. The various isomeric forms of propyl acrylate and butyl acrylate, namely, isopropyl acrylate, sec-butyl acrylate, tert-butyl acrylate are contemplated herein. Obviously, these monomers may be used singly or in combination. All of the monomeric substances mentioned hereinabove give types of plastic products having the singular properties attributed to the products of this invention.
The cross-linking agents used in the practice of the process of the present invention should be present in amounts varying between about 0.01% and 1% by weight of a polymerizable compound containing at least two polymerizable CH =C groups. These vinylidene monomeric compounds must have at least two ethylenic linkages which are in conjugation with other unsaturated linkages which latter unsaturated linkages are themselves nonethylenic. Among the cross-linking agents of this class which may be used in the practice of the process of the present invention are such monomers that result from the full esterification of a glycol with an alpha, beta-ethylenically unsaturated monocarboxylic acid. More particularly, these cross-linking agents result from the complete esterification of ethylene glycol, propanediol-1,3, butanediol-1,4 and the like, with acrylic acid, methacrylic acid and the like, As specific compounds, one may use ethylene diacrylate, propylene diacrylate, butylene diacrylate, ethylene dimethacrylate, propylene dimethacrylate, butylene dimethacrylate and the like. In addition, one may use such cross-linking agents as divinyl benzene, divinyl naphthalene and the like. The alkylene bis acrylamides may also be utilized effectively such as those disclosed in the US. Patent No. 2,475,846. Obviously, these cross-linking agents may be used either singly or in combination with one another.
It has been indicated hereinabove that the process of the present invention can be carried out in aqueous solution but preferably in a dispersion or an emulsion medium. In the latter instance, advantageous use of an emulsifying agent can be made of which agents a substantial plurality are well known in the art and the technique for using the same has been so widely published that further description herein is deemed to be unnecessary.
In order that the concept of the present invention may be more fully understood, the following examples are set forth in which all parts are parts by weight unless otherwise indicated. These examples are set forth primarily for the purpose of illustration and any specific enumeration of detail contained therein should not be interpreted as a limitation on the case except as is indicated in the appended claims.
Example 1 An emulsion is prepared by mixing, in a Waring Blendor for 3 minutes, 2250 parts of distilled water, 125 parts of a mixture of monomeric n-butyl acrylate and ethylene dimethacrylate (99.9%-0.1% respectively, each inhibitor free) and 1.425 parts of octadecyl trimethyl ammonium chloride, 50% solids in Water. The emulsion thus prepared is introduced into a suitable reaction vessel equipped with a purging tube. 12.5 parts of a cellulosic filter paper is immersed in the emulsion. The system is purged for 30 minutes with prepurified nitrogen at 500 parts per minute whereupon 125 parts of a 0.1 molar solution of ceric ammonium nitrate in 1 molar nitric acid is added and the purging continued during the entire run. After reacting at 25 C., the treated paper is removed and washed thoroughly with water. The paper is dried to a constant weight at 220 F. and the paper shows a polymer pickup of parts per hundred parts of paper weight.
Example 2 Example 1 is repeated in all details except that the reaction time is increased to give a polymer pickup of 250 parts per hundred parts of paper weight.
Example 3 Example 1 is repeated in every detail except that the weight ratio of the monomeric n-butyl acrylate to the ethylene dimethacrylate is 99%1%, respectively.
Example 4 Example 2 is repeated in every detail except that the weight ratio of the monomeric n-butyl acrylate to the ethylene dimethacrylate i 99%1%, respectively.
Example 5 Example 1 is repeated in every detail except that no cross-linking agent is used with the n-butyl acrylate.
Example 6 Example 2 is repeated in every detail except that no cross-linking agent is used with the n-butyl acrylate.
Example 7 Example 1 is repeated in all details except that the monomer to cross-linking agent was 99.5%0.5%, respectively.
Example 8 Example 2 is repeated in all retails except that the monomer to cross-linking agent was 99.5%0.5%, re-
1. A process comprising graft polymerizing a monomeric compound selected from the group consisting of ethyl acrylate, propyl acrylate and butyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the total weight of said acrylates, of ethylene dimethacrylate onto a paper substrate composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of a ceric salt which is soluble in at least one component of the reaction medium until the weight of said monoacrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
2. A process comprising graft polymerizing butyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacryate onto a cellulosic paper web composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of 'a ceric salt which is soluble in at least one component of the reaction medium until the Weight of said butyl acrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
3. A process comprising graft polymerizing ethyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacrylate onto a cellulosic paper web composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of a ceric salt which is soluble in at least one component of the reaction medium until the Weight of said ethyl acrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
4. A process comprising graft polymerizing propyl acrylate in the presence of from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacrylate onto a cellulosic paper Web composed predominately of cellulosic fibers in an aqueous medium at a pH not greater than 3.5 in the presence of a ceric salt which is soluble in at least one component of the reaction medium until the weight of said propyl acrylate grafted onto said substrate is between 100% and 900% based on the weight of the substrate.
5. A cellulosic paper Web reacted With butyl acrylate and from about 0.01% to about 1% by weight, based on the weight of said acrylate of ethylene dimethacryate, wherein said butyl acrylate on said paper is in a graftpolymerized state and is present in an amount varying between about 100% and 900% by weight based on the Weight of said paper Web.
6. A cellulosic paper web reacted with propyl acrylate 6 and from about 0.01% to about 1% by Weight, based on the weight of said acrylate of ethylene dimethacrylate, wherein said propyl acrylate on said paper is in a graftpolymerized state and is present in an amount varying between about 100% and 900% by weight based on the weight of said paper web.
7. A cellulosic paper web reacted with ethyl acrylate and from about 0.01% to about 1%,by Weight, based on the weight of said acrylate of ethylene dimethacrylate, wherein said ethyl acrylate on said paper is in a graftpolymerized state and is present in an amount varying between about 100% and 900% by weight based on the weight of said paper web.
References Cited in the file of this patent UNITED STATES PATENTS 2,434,106 Flood et al. Jan. 6, 1948 2,719,132 Schweitzer Sept. 27, 1955 2,789,030 'Fetscher Apr. 16, 1957 2,813,838 Lyman et al. Nov. 19, 1957 2,922,768 Mino et a1. Jan. 26, 1960 2,955,015 Segro et a1. Oct. 4, 1960

Claims (1)

1. A PROCESS COMPRISING GRAFT POLYMERIZING A MONOMERIC COMPOUND SELECTED FROM THE GROUP CONSISTING OF ETHYL ACRYLATE. PROPYL ACRYLATE AND BUTYL ACRYLATE IN THE PRESENCE OF FROM ABOUT 0.01% TO ABOUT 1% BY WEIGHT BASED ON THE TOTAL WEIGHT OF SAID ACRYLATES, OF ETHYLENE DIMETHACRYLATE ONTO A PAPER SUBSTRATE COMPOSED PREDOMINATELY OF CELLULOSIC FIBERS IN AN AQUEOUS MEDIUM AT A PH NOT GREATER THAN 3.5 IN THE PRESENCE OF A CERIC SALT WHICH IS SOLUBLE IN AT LEAST ONE COMPONENT OF THE REACTION MEDIUM UNTIL THE WEIGHT OF SAID MONOACRYLATE GRAFTED ONTO SAID SUBSTRATE IS BETWEEN 100% AND 900% BASED ON THE WEIGHT OF THE SUBSTRATE.
US730248A 1958-04-23 1958-04-23 Method of graft-polymerizing acrylate monomers onto paper in presence of ethylene dimethacrylate, and resulting product Expired - Lifetime US3065041A (en)

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US730248A US3065041A (en) 1958-04-23 1958-04-23 Method of graft-polymerizing acrylate monomers onto paper in presence of ethylene dimethacrylate, and resulting product
GB12168/59A GB884805A (en) 1958-04-23 1959-04-10 Process for producing cellulosic products
FR792212A FR1221546A (en) 1958-04-23 1959-04-16 Process for the polymerization of certain lower alkyl acrylates with cellulosic paper
BE577900A BE577900A (en) 1958-04-23 1959-04-20 Process for the polymerization of certain lower alkyl acrylates with cellulosic paper.

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Cited By (8)

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Publication number Priority date Publication date Assignee Title
US3232823A (en) * 1962-05-02 1966-02-01 Rayonier Inc Process of converting hydrophilic cellulose graft copolymers to hydrophobic copolymers
US3455643A (en) * 1961-09-29 1969-07-15 Emma K Light Continuous vinyl grafting of cellulose
US3485777A (en) * 1966-03-28 1969-12-23 Us Plywood Champ Papers Inc Compatibilization of polymers by adding graft copolymers
US3488210A (en) * 1966-11-03 1970-01-06 Fmc Corp Cellulosic graft polymerization process with suppression of homopolymer formation
US4028290A (en) * 1975-10-23 1977-06-07 Hercules Incorporated Highly absorbent modified polysaccharides
US4174417A (en) * 1975-10-14 1979-11-13 Kimberly-Clark Corporation Method of forming highly absorbent fibrous webs and resulting products
EP0218382A1 (en) * 1985-09-12 1987-04-15 The British Library Treatment of archival material
US4672005A (en) * 1984-03-01 1987-06-09 Intera Corporation Process for improving polymer substrate properties, and modified polymers produced thereby

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Publication number Priority date Publication date Assignee Title
US2434106A (en) * 1945-01-13 1948-01-06 Catalin Corp Of America Impregnation of cellulosic material
US2719132A (en) * 1954-05-25 1955-09-27 Du Pont Polymerization catalyst and methacrylic acid diester compositions polymerized therewith
US2789030A (en) * 1950-03-30 1957-04-16 Cluett Peabody & Co Inc Process of topochemical modification of clllulose fabrics by reacting with a copolymerizable monomer and copolymerizing the reaction product and product produced thereby
US2813838A (en) * 1955-02-07 1957-11-19 Rohm & Haas Boron-adsorbing resin and process for removing boron compounds from fluids
US2922768A (en) * 1956-04-12 1960-01-26 Mino Guido Process for polymerization of a vinylidene monomer in the presence of a ceric salt and an organic reducing agent
US2955015A (en) * 1957-06-05 1960-10-04 American Cyanamid Co Graft polymerization of certain esters of acrylic acid with cellulose substrate

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434106A (en) * 1945-01-13 1948-01-06 Catalin Corp Of America Impregnation of cellulosic material
US2789030A (en) * 1950-03-30 1957-04-16 Cluett Peabody & Co Inc Process of topochemical modification of clllulose fabrics by reacting with a copolymerizable monomer and copolymerizing the reaction product and product produced thereby
US2719132A (en) * 1954-05-25 1955-09-27 Du Pont Polymerization catalyst and methacrylic acid diester compositions polymerized therewith
US2813838A (en) * 1955-02-07 1957-11-19 Rohm & Haas Boron-adsorbing resin and process for removing boron compounds from fluids
US2922768A (en) * 1956-04-12 1960-01-26 Mino Guido Process for polymerization of a vinylidene monomer in the presence of a ceric salt and an organic reducing agent
US2955015A (en) * 1957-06-05 1960-10-04 American Cyanamid Co Graft polymerization of certain esters of acrylic acid with cellulose substrate

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3455643A (en) * 1961-09-29 1969-07-15 Emma K Light Continuous vinyl grafting of cellulose
US3232823A (en) * 1962-05-02 1966-02-01 Rayonier Inc Process of converting hydrophilic cellulose graft copolymers to hydrophobic copolymers
US3485777A (en) * 1966-03-28 1969-12-23 Us Plywood Champ Papers Inc Compatibilization of polymers by adding graft copolymers
US3488210A (en) * 1966-11-03 1970-01-06 Fmc Corp Cellulosic graft polymerization process with suppression of homopolymer formation
US4174417A (en) * 1975-10-14 1979-11-13 Kimberly-Clark Corporation Method of forming highly absorbent fibrous webs and resulting products
US4028290A (en) * 1975-10-23 1977-06-07 Hercules Incorporated Highly absorbent modified polysaccharides
US4672005A (en) * 1984-03-01 1987-06-09 Intera Corporation Process for improving polymer substrate properties, and modified polymers produced thereby
EP0218382A1 (en) * 1985-09-12 1987-04-15 The British Library Treatment of archival material
US4808433A (en) * 1985-09-12 1989-02-28 The British Library Treatment of archival material

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GB884805A (en) 1961-12-20

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