EP0074544B2 - Aqueous sizing compositions - Google Patents

Aqueous sizing compositions Download PDF

Info

Publication number
EP0074544B2
EP0074544B2 EP82107893A EP82107893A EP0074544B2 EP 0074544 B2 EP0074544 B2 EP 0074544B2 EP 82107893 A EP82107893 A EP 82107893A EP 82107893 A EP82107893 A EP 82107893A EP 0074544 B2 EP0074544 B2 EP 0074544B2
Authority
EP
European Patent Office
Prior art keywords
sizing
rosin
cationic
dispersion
cellulose
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP82107893A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0074544B1 (en
EP0074544A1 (en
Inventor
David Howard Dumas
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hercules LLC
Original Assignee
Hercules LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=23165867&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0074544(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Hercules LLC filed Critical Hercules LLC
Priority to AT82107893T priority Critical patent/ATE23379T1/de
Publication of EP0074544A1 publication Critical patent/EP0074544A1/en
Publication of EP0074544B1 publication Critical patent/EP0074544B1/en
Application granted granted Critical
Publication of EP0074544B2 publication Critical patent/EP0074544B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/14Carboxylic acids; Derivatives thereof
    • D21H17/15Polycarboxylic acids, e.g. maleic acid
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/07Nitrogen-containing compounds
    • D21H17/08Isocyanates
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/17Ketenes, e.g. ketene dimers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/62Rosin; Derivatives thereof

Definitions

  • This invention relates to paper sizing compositions and more particularly to aqueous compositions containing hydrophobic cellulose-reactive sizes and fortified rosin.
  • Aqueous dispersions containing finely divided particles of fortified rosin, a water-soluble cationic resin dispersing agent and water are described by Aldrich in USP 3,966,654.
  • the aqueous fortified rosin dispersions are useful as internal or surface sizing agents for paper. Sizing performance, however, is dependent on both pH and concentration and it is necessary to use greater than about 0.1 % fortified rosin based on the dry weight of the pulp (the critical level) and to carry out sizing in acidic systems to achieve good sizing efficiency.
  • Sizing compositions which are aqueous emulsions or dispersions of a hydrophobic cellulose-reactive sizing agent such as a ketene dimer and a nonionic, anionic or cationic dispersion agent are also known.
  • a hydrophobic cellulose-reactive sizing agent such as a ketene dimer and a nonionic, anionic or cationic dispersion agent.
  • the cellulose-reactive sizing agents and particularly the ketene dimer sizing agents have been commercially important since sizing can be effected under alkaline conditions which do not adversely effect the paper strength and higher sizing can be achieved at a lower critical level than is realizable with rosin sizes. They suffer one serious drawback, however, in that drying is required for initial sizing to develop and the ultimate sizing which can be expected does not develop for a significant period of time depending upon the conditions of use.
  • compositions of this type are described, for example, in British patent 1,533,434 and USP 4,240,935. Although these compositions provide substantial improvement in the rate of size development, complete drying is required to achieve ultimate sizing. With ground wood pulp and other difficult-to size pulp, however, aging is required to achieve ultimate sizing.
  • aqueous dispersions which contain both fortified rosin and cellulose-reactive sizes and which, surprisingly, overcome the disadvantages inherent to the use of either of the components individually.
  • the dispersions of this invention also provide the advantages of the individual components and additionally provide higher and more rapid sizing than would be expected from either component alone.
  • the aqueous dispersions of this invention have as the continuous phase an aqueous solution containing at least one of any of the known water-soluble nitrogen-containing cationic dispersing agents for rosin size and as the dispersed phase (a) finely divided particles of a hydrophobic cellulose-reactive sizing agent selected from the group consisting of ketene dimers, organic acid anhydrides, organic isocyanates and mixtures thereof, characterized in that it also contains (b) finely divided particles of fortified rosin the weight ratio of (b):(a) in the dispersed phase being within the range of 0.1: to 10:1 and the amount of dispersing agent being within the range of about 5 to about 140% based on the weight of the dispersed phase.
  • a hydrophobic cellulose-reactive sizing agent selected from the group consisting of ketene dimers, organic acid anhydrides, organic isocyanates and mixtures thereof, characterized in that it also contains (b) finely divided particles of fortified
  • the fortified rosin component of the dispersed phase is the adduct reaction product of rosin and an acidic compound containing the group and is derived by reacting rosin and the acidic compound at elevated temperatures of from about 150°C to about 210°C.
  • the amount of acidic compound employed will be that amount which will provide fortified rosin containing from about 1 % to about 12 % by weight of adducted acidic compound based on the weight of the fortified rosin.
  • Methods of preparing fortified rosin are disclosed and described in U.S. Patent Nos. 2,628,918 and 2,684,300, reference to which is hereby made.
  • Examples of acidic compounds containing the group that can be used to prepare the fortified rosin include the alpha-beta-unsaturated organic acids and their available anhydrides, specific examples of which include fumaric acid, maleic acid, acrylic acid, maleic anhydride, itaconic acid, itaconic anhydride, citraconic acid, and citraconic anhydride. Mixtures of acids can be used to prepare the fortified rosin if desired. Also mixtures of different fortified rosins can be used if desired. Thus, for example, a mixture of the acrylic acid adduct of rosin and the fumaric acid adduct can be used to prepare the novel dispersions of this invention. Also fortified rosin that has been substantially completely hydrogenated after adduct formation can be used.
  • the fortified rosin can be extended if desired by known extenders therefor such as waxes (particularly paraffin wax and microcrystalline was); hydrocarbon resins including those derived from petroleum hydrocarbons and terpenes; and the like. This is accomplished by blending with the fortified rosin from about 10% to about 100% by weight based on the weight of fortified rosin of the fortified rosin extender.
  • blends of fortified rosin and rosin, and blends of fortified rosin, rosin and rosin extender can be used.
  • Fortified rosin-rosin blends will comprise about 25% to 95%, fortified rosin and about 75% to 5% rosin.
  • Blends of fortified rosin, rosin, and rosin extender will comprise about 25% to 45% fortified rosin, about 5% to 50% rosin, and about 5% to 50% rosin extender.
  • rosin that is, unfortified rosin
  • fortified rosin it can be any of the commercially available types of rosin, such as wood rosin, gum rosin, tall oil rosin, and mixtures of any two or more, in their crude or refined state.
  • Partially orsubstantially completely hydrogenated rosins and polymerized rosins, as well as rosins that have been treated to inhibit crystallization such as by heat treatment or reaction with formaldehyde, can be employed.
  • Aqueous dispersions containing finely divided particles of fortified rosin are commercially available.
  • One method of preparing such dispersions is described by Aldrich in U.S. Patent 3,966,654 and involves first dissolving the fortified rosin in a water-immiscible organic solvent therefor such as, for example, benzene, xylene, chloroform, methylene chloride and 1,2-dichloropropane. Mixtures of two or more solvents can be used if desired.
  • the selected solvent will also be nonreactive to the components of the aqueous dispersion to be subsequently prepared.
  • the organic solvent-fortified rosin solution is then mixed with an aqueous solution of a cationic dispersing agent to provide an emulsion which is essentially unstable and in which the organic solvent-fortified rosin solution forms the dispersed phase.
  • the essentially unstable aqueous emulsion is then subjected to extreme shear to provide an essentially stable aqueous emulsion. Extreme shear is conveniently accomplished by means of an homogenizer.
  • an homogenizer thus passing, at least once, the unstable aqueous emulsion through an homogenizer under a pressure of the order of from about 7000 kPa to about 55260 kPa, will provide an essentially stable emulsion.
  • the organic solvent component of the emulsion is removed from the emulsion and there is provided an essentially stable aqueous dispersion of fortified rosin particles.
  • the organic solvent-fortified rosin solution can be mixed with an aqueous solution of a cationic dispersing agent in an amount to provide a stable water-in-oil emulsion which is subsequently inverted to a stable oil-in-water emulsion by the rapid addition of water vigorous stirring.
  • the organic solvent is subsequently removed, as by distillation under reduced pressure.
  • the dispersing agent can be any of the known dispersing agents for rosin size and is cationic in nature. Particularly preferred are the cationic thermosetting water-soluble polyaminopolyamide-epichlorohydrin resins, alkylenepolyamine-epichlorohydrin resins and the poly(diallylamine)-epichlorohydrins resins. These resins are described in U.S. Patents 2,926,116, 2,926,154 and 3,700,623 as well as 3,966,654.
  • hydrophobic cellulose-reactive sizing agents which have been found to be particularly useful as the second component of the dispersed phase are ketene dimers, acid anhydrides and organic isocyanates.
  • Examples of ketene dimers include octyl, decyl, dodecyl, tetradecyl, hexadecyl, octadecyl, eicosyl, docosyl, tetracosyl, phenyl, benzyl, beta-napthyl and cyclohexyl ketene dimers, as well as the ketene dimers prepared by known methods from montanic acid, naphthenic acid, ⁇ 9 .
  • 10- decylenic acid A 9,10- dodecylenic acid, palmitoleic acid, oleic acid, ricinoleic acid, linoleic acid, and eleostearic acid, as well as ketene dimers prepared from naturally occurring mixtures of fatty acids, such as those mixtures found in coconut oil, babassu oil, palm kernel oil, palm oil, olive oil, peanut oil, rape oil, beef tallow, lard (leaf) and whale blubber. Mixtures of any of the above-named fatty acids with each other may also be used.
  • Acid anhydrides useful as cellulose-reactive sizing agents for paper are well-known in the art and include (A) rosin anhydride, see United States Patent 3,582,464; (B) anhydrides having the structure where R 1 is a saturated or unsaturated hydrocarbon radical, the hydrocarbon radical being a straight or branched chain alkyl radical, an aromatic substituted alkyl radical, or an alkyl substituted aromatic radical so long as the hydrocarbon radical contains a total from about 14 to 36 carbon atoms; and (C) cyclic dicarboxylic acid anhydrides having the structure: where R' represents a dimethylene or trimethylene radical and where R" is a hydrocarbon radical containing more than 7 carbon atoms and is preferably alkyl, alkenyl, aralkyl or aralkenyl.
  • Substituted cyclic dicarboxylic acid anhydrides falling within the above formula (II) are substituted succinic and glutaric anhydrides.
  • each R 1 can be the same hydrocarbon radical or each R 1 can be a different hydrocarbon radical.
  • anhydrides of formula (I) are myristoyl anhydride; palmitoyl anhydride; oleoyl anhydride; and stearoyl anhydride.
  • anhydrides of formula (II) are isooctadecenyl succinic acid anhydride; n-hexadecenyl succinic acid anhydride; dodecyl succinic acid anhydride; decenyl succinic acid anhydride; octenyl succinic acid anhydride; and heptyl glutaric acid anhydride.
  • Hydrophobic organic isocyanates used as sizing agents for paper are well-known in the art. Best results are obtained when the hydrocarbon chain of the isocyanates contain at least 12 carbon atoms, preferably from 14 to 36 carbon atoms.
  • Such isocyanates include rosin isocyanate; dodecyl isocyanate; octadecyl isocyanate; tetradecyl isocyanate; hexadecyl isocyanate; eicosyl isocyanate; docosyl isocyanate; 6-ethyldecyl isocyanate; 6-phenyldecyl isocyanate; and polyisocyanates such as 1,18-octadecyl diisocyanate and 1,12-dodecyl diisocyanate, wherein one long chain alkyl group serves two isocyanate radicals and imparts hydrophobic properties to the molecule as a whole.
  • Aqueous dispersions or emulsions containing finely divided particles of hydrophobic cellulose-reactive sizing agents are known commercially. Such dispersions are conventionally prepared by stirring the cellulose-reactive sizing agent into an aqueous solution of an emulsifier and passing the premix through a homogenizer. Emulsifiers conventionally employed in the production of emulsions of cellulose-reactive sizing agents are suitable. Such emulsifiers include cationic starches that are water-soluble starches containing sufficient amino groups, quaternary ammonium or other cationic groups to render the starch, as a whole, cellulose substantive. Examples of such cationic starches are the cationic amine-modified starches described in U.S.
  • Patent 3,130,118 and the known cationic starch graft copolymers are the water-soluble cationic thermosetting resins obtained by reacting epichlorohydrin with a water-soluble aminopolyamide formed from a 3 to 10 carbon dibasic carboxylic acid and a polyalkylene polyamine containing from 2 to 8 alkylene groups (see U.S. Patent Nos. 2,926,116 & 2,926,154), with a water-soluble poly(diallylamine) (see U.S. Patent No. 3,966,654), with condensates of dicyandiamide or cyanamide and a polyalkylenepolyamine (see U.S. Patent No. 3,403,113), with bis-aminopropylpiperazine or condensates thereof with dicyandiamide or cyanamide (see U.S. Patent No. 4,243,481 ) and the like.
  • the dispersed phase of the cationic aqueous dispersions of this invention contains both finely divided particles of a hydrophobic cellulose-reactive size and finely divided particles of fortified rosin and it has been found that the dispersed phase should comprise at least 10 weight % of each if the advantages of this invention are to be realized.
  • the weight ratio of the fortified rosin size to the cellulose-reactive size will range from 0.1:1 to 10:1. The most practical range, however, is from 0.2:1 to 5:1 and this is the preferred range.
  • the aqueous dispersions of this invention also contain, as stated, a water-soluble nitrogen-containing cationic dispersing agent.
  • a water-soluble nitrogen-containing cationic dispersing agent Any cationic nitrogen-containing dispersing agent which is water-soluble and confers a positive surface charge to the particles of the disperse phase of the dispersion is suitable.
  • Nitrogen-containing dispersing agents of this type are well-known to the art and are available commercially.
  • the dispersing agents are quaternary ammonium compounds; homopolymers or copolymers of ethylenically unsaturated amines; the resinous reaction products of epihalohydrins and polyaminopolyamides, alkylenepolyamines, poly(diallylamines), bis-aminopropylpiperazine, dicyandiamide (or cyanamide) -polyalkylene polyamine condensates, dicyandiamide (or cyanamide) -formaldehyde condensates, and dicyandiamide (or cyanamide) -bis-aminopropylpiperazine condensates; and cationic starches and particularly starch ethers containing amino or quaternary ammonium groups.
  • cationic starch and the resinous reaction products of epichlorohydrin with an aminopolyamide, an alkylenepolyamine, a poly(diallylamine) ora dicyandiamide-polyalkylenepolyamine condensate.
  • the dispersing agents can be used singly, in combination with each other or in combination with anionic or nonionic dispersing agents.
  • the minimum amount of cationic dispersing agent used must, of course, be sufficient to render the dispersion cationic.
  • the amount used will vary, of course, depending upon the water solubility, the initial anionic or cationic strength of the dispersions used, and the cationic strength of the particular agent employed. Usually, the amount will range from about 5 to about 140, preferably 20 to 120 and more preferably from 40 to 100 weight % based on the dispersed phase. Amounts less than about 5% generally are not sufficient to render the dispersion cationic and amounts greater than about 140% have not been found to provide additional advantages and hence are not necessary.
  • the cationic dispersions of this invention can be prepared at any convenient concentration. Particularly useful are dispersions in which the dispersed phase is about 5 to 70%, preferably 10 to 55%, the dispersing agent is 1 to 15%, preferably 2 to 10% and the balance is water to 100%.
  • the dispersions of this invention can also contain other sizing or non-sizing ingredients provided their presence does not destroy the advantages of the invention. Particularly useful in this respect is alum which is conventionally used to set rosin size.
  • alum cannot be added to fortified rosin prior to its use as a sizing agent for paper and must be added separately to an aqueous suspension of papermaking fibers at various stages prior to sheet formation for internal sizing or applied to the formed sheet prior to, simultaneously with orfollowing application of the rosin in external sizing.
  • alum in any amount can be present in the aqueous cationic dispersions of this invention without destroying size efficiency and that the presence of alum provides an outstanding advantage in convenience which was not realizable heretofore.
  • the amount will range from about 25 to about 200% based on the weight of fortified rosin particles. The most practical range, however, is 75 to 150% and this is the preferred range.
  • Other additives such as preservatives can also be present in small amounts.
  • novel dispersions of this invention can be prepared by blending a preformed dispersion of the fortified rosin particles with a preformed cationic dispersion of the hydrobic cellulose-reactive sizing agent. They can also be prepared by mixing a melt or organic solution of fortified rosin and the cellulose-reactive size in aqueous medium containing the cationic dispersing agent and subjecting the mixture to conditions of extreme shear, as set forth above. Modifications of the above procedures are also suitable and are within the skill of the art to which the invention pertains.
  • the dispersions of this invention are particularly useful for internal or surface sizing of paper and maximize the advantages of the individual sizing components while minimizing the disadvantages.
  • the dispersions provide improved sizing under conditions which are not practical for cellulose-reactive size dispersions alone or for fortified rosin dispersions alone, and also provide the fast rate of cure typical of fortified rosin size and the high degree of sizing typical of the cellulose-reactive sizes.
  • this invention it is possible to control readily the rate and degree of sizing under normal paper mill conditions wherein alum is usually present and to use pH levels which provide paper having excellent permanence and durability.
  • the aqueous dispersions can be added to the pulp suspension at any point after refining is complete and prior to sheet formation or can be applied to the sheet on the paper machine, as for example, at the size press.
  • the aqueous dispersions of this invention can be formed in situ at the size press by simultaneous or separate additions of the individual cationic components in dispersion form and blending.
  • the amount of dispersion added to the aqueous pulp suspension (internal sizing) or to the formed paper sheet (external sizing) should be such as to provide a retained amount of from about 0.01 to about 1% and preferably from about 0.01 to 0.5% by weight of the combination of cellulose-reactive size and fortified rosin, based on the dry weight of fiber.
  • a ketene dimer dispersion having a total solids of 15% and containing 5,4% ketene dimer solids, 1,4% cationic starch and 8.2% of a cationic reisn prepared by condensing 1 mole of dicyandiamide with 1 mole of diethylenetriamine, and reacting the condensate with 1.2 mole of epichlorohydrin was prepared as follows.
  • An emulsion of a ketene dimer prepared from a mixture of palmitic and stearic acids was prepared by admixing 880 parts of water, 50 parts of cationic corn starch and 10 parts of sodium lignin sulfonate. The mixture was adjusted to a pH of about 3.5 with 98% sulfuric acid and heated at 90-95°C for about 1 hour. Water was then added to the mixture in an amount sufficient to provide a mixture of 1760 parts (total weight). Then 240 parts of the ketene dimer were stirred into the mixture and the mixture (at 65°C) was homogenized in one pass through an homogenizer at 27600 kPa.
  • the homogenized product (at 15% total solids and 12% ketene dimer solids, 136.4 parts) was then mixed with 136.4 parts of an 18% aqueous solutions of the cationic resin and 27.2 parts of water and the pH was adjusted to 4.0 to 4.5.
  • a cationic dispersion of fortified rosin having a total solids content of 34.1% and containing 28.4% of rosin solids and 5.7% of a cationic resinous reaction product of 1.25 moles of epichlorohydrin with an aminopolyamide derived from 1 mole of adipic acid and 0.97 mole of diethylenetriamine was prepared as follows.
  • a solution was prepared by dissolving 300 parts of fortified rosin in 200 parts of methylene chloride over a 20-minute period.
  • the fortified rosin contained 7.5% fumaric acid, substantially all of which was in the combined or adducted form.
  • the fortified rosing was prepared by adducting 22.5 parts of fumaric acid with 277.5 parts of formaldehyde treated tall oil resin at a temperature of about 205°C until substantially all of the fumaric acid had reacted and then cooling the fortified rosin to room temperature.
  • the fortified rosin solution was thoroughly mixed with a preblend of 480 parts of amino-polyamidelepichlorohydrin resin at 12.5% solids and 260 parts water and the mixture was homogenized twice at 20700 kPa.
  • the methylene chloride was subsequently removed by distillation under reduced pressure at 60°C.
  • the product was cooled and filtered through a 149 Il m screen, giving 750 parts of a dispersion having a viscosity of 0.051 Pas.
  • compositions were prepared by mixing in a vessel equipped with a magnetic stirrer 50 parts of the cationic dispersion of Example A and from about 9 to about 59 parts of the cationic dispersion of Example B. Details of these examples and the resulting cationic dispersions are set forth in Table I, below.
  • the sizing efficiency of each of the aqueous cation ic dispersions of Examples 1 to 5 was tested by preparing handsheets using varying amounts of size solids. To prepare the handsheets, a 50:50 blend of Rayonier bleached softwood and Weyerhaeuser bleached hardwood kraft pulp was suspended in standard hard water and beaten to 500 Canadian standard freeness in a Noble and Wood cycle beater. The pulp slurry was diluted to a consistency of 0.25% in the proportioner.
  • a 2-liter portion of the slurry was treated with sufficient of the cationic dispersion to give various percentages of size, and with sufficient papermakers alum to give 0.5% alum, based on the weight of the pulp and diluted to 0.025% consistency in order to form a 65 g/m 2 sheet at a pH of 6.5 using a Noble and Wood sheet making apparatus.
  • the formed sheets were wet-pressed to 33% solids content and then dried at 105°C for 45 seconds on a steam drum drier to 3-4% moisture.
  • the sheets were tested for size properties using the Hercules Size Test with test solution No. 2 to 80% reflectance.
  • the off-machine data were obtained within two minutes of drying and the natural aged data after 7 days of storage at room temperature and 50% relative humidity. Size results for these trials and for 7 controls prepared in the same manner except that the dispersion of Example A or Example B was added to the portion of slurry are set forth in Table II, below.
  • the aqueous dispersions of Examples 6 to 8 were used to prepare internally sized paper on a pilot paper machine.
  • the paper was made from a 50:50 blend of hardwood and softwood kraft pulp beaten to a Canadian standard freeness of 500 and formed into sheets having a basis weight of 65 g/m 2 at a pH of 6.4 to 6.6.
  • Each dispersion was added to the thick stock just prior to dilution at the fan pump. Papermakers alum, if used, was added simultaneously with the dispersion.
  • the sized sheets were dried to 3% moisture before the size press and to 4% moisture at the reel.
  • the size press contained a 6% solution of oxidized corn starch. The sizing was measured by the Hercules Size Test with test solution No.
  • compositions of this invention clearly demonstrate that marked improvement in sizing is obtained with the compositions of this invention under conditions which are not practical for ketene dimer dispersions alone (control trial 7) or for fortified rosin dispersions alone (control trials 8 and 9).
  • the data further show that the compositions of this invention provide the fast rate of cure typical of rosin size and the high degree of sizing typical of ketene dimer size, and that the rate and degree of sizing can be controlled readily under normal mill conditions wherein alum is usually present and at pH levels which provide paper with excellent permanence and durability.
  • a dispersion having a total solids of 51 % and containing by weight 21.2% of fortified rosin, 4.3% of the cationic resinous reaction product of Example B and 25.5% of alum was prepared by blending 50 parts of the dispersion of Example B with 17.1 parts of alum (A1 2 (SO 4 ) 3 .18H 2 0).
  • compositions were prepared by mixing in a vessel equipped with a magnetic stirrer 50 parts of the cationic dispersion of Example A and 30 parts (Example 11 ) or 60 parts (Example 12) of the dispersion of Example C.
  • the cationic dispersion of Example 11 contained, by weight of the total composition, 7.95% of fortified rosin, 3.41 % of ketene dimer, 7.58% of the mixed cationic dispersing agent and 9.56% of alum and had a total solids content of 28.5%.
  • the cationic dispersion of Example 12 contained, by weight of the total composition, 11.56% of fortified rosin, 2.48% of ketene dimer, 6.68% of the mixed dispersing agent and 13.90% of alum and had a total solids content of 34.6%.
  • the efficiency of the aqueous dispersions of these examples to surface size paper was evaluated using unsized bleached kraft paper (65 g/m 2 ) made at a pH of 6.5.
  • the sheets were treated using a small horizontal laboratory size press by adding samples of the aqueous dispersions to the nip of the size press and passing sheets of paper through the dispersion before being squeezed by the rolls of the size press. Under these conditions the sheets picked up about 70% of their weight of size press dispersion.
  • the sized sheets were dried for about 20 seconds at 93°C to a moisture content of about 5%. Sizing was determined by the Hercules Size Test using test solution No.
EP82107893A 1981-09-15 1982-08-27 Aqueous sizing compositions Expired - Lifetime EP0074544B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT82107893T ATE23379T1 (de) 1981-09-15 1982-08-27 Waessrige leimungszusammensetzung.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US30201081A 1981-09-15 1981-09-15
US302010 1981-09-15

Publications (3)

Publication Number Publication Date
EP0074544A1 EP0074544A1 (en) 1983-03-23
EP0074544B1 EP0074544B1 (en) 1986-11-05
EP0074544B2 true EP0074544B2 (en) 1991-12-27

Family

ID=23165867

Family Applications (1)

Application Number Title Priority Date Filing Date
EP82107893A Expired - Lifetime EP0074544B2 (en) 1981-09-15 1982-08-27 Aqueous sizing compositions

Country Status (15)

Country Link
EP (1) EP0074544B2 (pt)
JP (1) JPS5860093A (pt)
AT (1) ATE23379T1 (pt)
AU (1) AU551897B2 (pt)
BR (1) BR8205384A (pt)
CA (1) CA1187658A (pt)
DE (1) DE3274133D1 (pt)
DK (1) DK159210B (pt)
ES (1) ES515701A0 (pt)
FI (1) FI69160C (pt)
MX (1) MX166782B (pt)
NO (1) NO162300C (pt)
NZ (1) NZ201798A (pt)
PH (1) PH18888A (pt)
ZA (1) ZA826772B (pt)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0678462B2 (ja) * 1984-06-04 1994-10-05 日本ピー・エム・シー株式会社 ケテンダイマー系水性分散液
JPH0678463B2 (ja) * 1984-06-04 1994-10-05 日本ピー・エム・シー株式会社 ケテンダイマー系水性分散液
SE455102B (sv) * 1985-07-10 1988-06-20 Nobel Ind Paper Chemicals Ab Vattenhaltiga dispersioner av kolofoniummaterial och ett syntetiskt hydrofoberingsmedel, forfarande for framstellning derav samt anvendning av dessa som hydrofoberingsmedel
SE465833B (sv) * 1987-01-09 1991-11-04 Eka Nobel Ab Vattenhaltig dispersion innehaallande en blandning av hydrofoberande kolofoniummaterial och syntetiskt hydrofoberingsmedel, saett foer framstaellning av dispersionen samt anvaendning av dispersionen vid framstaellning av papper och liknande produkter
GB8712349D0 (en) * 1987-05-26 1987-07-01 Hercules Inc Sizing pulp
US4859244A (en) * 1988-07-06 1989-08-22 International Paper Company Paper sizing
SE506467C2 (sv) * 1991-06-28 1997-12-22 Eka Chemicals Ab Förfarande för framställning av stabiliserad kolofonium och dess användning som klibbgivarharts i bindemedel
DE59305310D1 (de) * 1992-08-07 1997-03-13 Bayer Ag Chlorfreie multifunktionelle Harze für die Papierveredlung
GB9300188D0 (en) * 1993-01-06 1993-03-03 Dexter Speciality Materials Fibrous bonded sheet material
ES2124873T3 (es) * 1993-02-15 1999-02-16 Eka Chemicals Ab Un metodo para reducir el contenido de disolvente organico en agentes hidrofobos reactivos con celulosa.
US5510003A (en) 1994-07-20 1996-04-23 Eka Nobel Ab Method of sizing and aqueous sizing dispersion
DE4446334A1 (de) * 1994-12-23 1996-06-27 Bayer Ag Wiederaufschließbare cellulosehaltige Materialien
DE19522832A1 (de) * 1995-06-23 1997-01-02 Chem Fab Bruehl Oppermann Gmbh Mittel zum Leimen von Papier, Pappe und Karton und ihre Verwendung
DE19610995C2 (de) * 1996-03-21 2002-12-19 Betzdearborn Inc Papierleimungsmittel und -verfahren
AT406492B (de) 1998-01-26 2000-05-25 Krems Chemie Ag Wässrige papierleimungsmitteldispersionen und verfahren zu ihrer herstellung
SE513080C2 (sv) 1998-04-14 2000-07-03 Kemira Kemi Ab Limningskomposition och förfarande för limning
SE0000449L (sv) * 2000-02-14 2001-08-15 Kemira Kemi Ab Limningskomposition
FI111745B (fi) 2001-12-19 2003-09-15 Kemira Chemicals Oy Parannettu kartonginvalmistusmenetelmä
JP4595283B2 (ja) * 2003-01-24 2010-12-08 日油株式会社 サイズ剤組成物
JP6012206B2 (ja) * 2012-03-08 2016-10-25 地方独立行政法人京都市産業技術研究所 変性セルロースナノファイバー及び変性セルロースナノファイバーを含む樹脂組成物

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL129371C (pt) * 1961-09-08
US3139373A (en) * 1962-06-08 1964-06-30 Allied Chem Process for the internal sizing of paper with a salt of a substituted succinic acid
US3966654A (en) * 1973-08-06 1976-06-29 Hercules Incorporated Stable rosin dispersions
GB2050453B (en) * 1979-05-23 1983-02-09 Tenneco Chem Chemical compositions useful in the manufacture of paper sizing agents

Also Published As

Publication number Publication date
JPH0250240B2 (pt) 1990-11-01
ES8403998A1 (es) 1984-04-01
DK159210B (da) 1990-09-17
EP0074544B1 (en) 1986-11-05
AU551897B2 (en) 1986-05-15
EP0074544A1 (en) 1983-03-23
MX166782B (es) 1993-02-04
PH18888A (en) 1985-10-25
ES515701A0 (es) 1984-04-01
FI69160C (fi) 1985-12-10
FI823045L (fi) 1983-03-16
NO162300B (no) 1989-08-28
NO162300C (no) 1989-12-06
DK412282A (da) 1983-03-16
BR8205384A (pt) 1983-08-23
CA1187658A (en) 1985-05-28
FI823045A0 (fi) 1982-09-03
FI69160B (fi) 1985-08-30
NO823117L (no) 1983-03-16
ZA826772B (en) 1983-07-27
NZ201798A (en) 1985-09-13
JPS5860093A (ja) 1983-04-09
AU8838282A (en) 1983-03-24
ATE23379T1 (de) 1986-11-15
DE3274133D1 (en) 1986-12-11

Similar Documents

Publication Publication Date Title
US4522686A (en) Aqueous sizing compositions
EP0074544B2 (en) Aqueous sizing compositions
US4919724A (en) Stable aqueous emulsions of ketene dimer/nonreactive hydrophobe
US5972100A (en) Pretreatment of filler with cationic ketene dimer
EP2691572B1 (en) Sizing compositions
US4323425A (en) Paper sizing
US6228219B1 (en) Rosin sizing at neutral to alkaline pH
FI88405C (fi) Vattenhaltiga dispersioner, foerfarande foer framstaellning samt anvaendning av dessa som hydrofoberingsmedel
US3957574A (en) Sizing method and composition for use therein
US6273997B1 (en) Rosin/hydrocarbon resin size for paper
US5488139A (en) Paper opacifying composition
CA1044859A (en) Method of sizing paper
US4786330A (en) Diurethane latex and processes
CA1069410A (en) Emulsified lipophilic paper sizing
US20060049377A1 (en) Alkenylsuccinic anhydride composition and method of using the same
US2954313A (en) Sizing fibrous cellulosic materials
WO1994013883A1 (en) Process for the preparation of a hydrophobic sizing agent dispersion
US3821075A (en) C21-dicarboxylic acid anhydride and size agents and sizing process
NZ614875B2 (en) Sizing compositions
EP0218110A1 (en) Storage stable paper size composition containing ethoxylated lanolin

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT LI NL SE

17P Request for examination filed

Effective date: 19830919

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE FR GB IT LI NL SE

REF Corresponds to:

Ref document number: 23379

Country of ref document: AT

Date of ref document: 19861115

Kind code of ref document: T

ITF It: translation for a ep patent filed

Owner name: ING. C. GREGORJ S.P.A.

REF Corresponds to:

Ref document number: 3274133

Country of ref document: DE

Date of ref document: 19861211

ET Fr: translation filed
PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

26 Opposition filed

Opponent name: ALBRIGHT& WILSON LIMITED

Effective date: 19870804

NLR1 Nl: opposition has been filed with the epo

Opponent name: ALBRIGHT & WILSON LIMITED

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

R26 Opposition filed (corrected)

Opponent name: ALBRIGHT& WILSON LIMITED

Effective date: 19870804

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

R26 Opposition filed (corrected)

Opponent name: ALBRIGHT& WILSON LIMITED

Effective date: 19870804

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

R26 Opposition filed (corrected)

Opponent name: EKA NOBEL AB

Effective date: 19870804

NLXE Nl: other communications concerning ep-patents (part 3 heading xe)

Free format text: IN PAT.BUL.19/87,CORR.:EKA NOBEL AB.

ITTA It: last paid annual fee
PUAH Patent maintained in amended form

Free format text: ORIGINAL CODE: 0009272

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: PATENT MAINTAINED AS AMENDED

27A Patent maintained in amended form

Effective date: 19911227

AK Designated contracting states

Kind code of ref document: B2

Designated state(s): AT BE CH DE FR GB IT LI NL SE

ITF It: translation for a ep patent filed

Owner name: ING. C. GREGORJ S.P.A.

REG Reference to a national code

Ref country code: CH

Ref legal event code: AEN

ET3 Fr: translation filed ** decision concerning opposition
NLR2 Nl: decision of opposition
NLR3 Nl: receipt of modified translations in the netherlands language after an opposition procedure
EAL Se: european patent in force in sweden

Ref document number: 82107893.8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19950828

Year of fee payment: 14

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Effective date: 19960831

Ref country code: CH

Effective date: 19960831

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20000620

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20000703

Year of fee payment: 19

Ref country code: AT

Payment date: 20000703

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20000802

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20000803

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20000830

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20000915

Year of fee payment: 19

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010827

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010827

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010828

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20010831

BERE Be: lapsed

Owner name: HERCULES INC.

Effective date: 20010831

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020301

EUG Se: european patent has lapsed

Ref document number: 82107893.8

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20010827

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020430

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 20020301

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020501

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO