US2797167A - Hydrophobic blends comprising fortified rosin and wax - Google Patents

Hydrophobic blends comprising fortified rosin and wax Download PDF

Info

Publication number
US2797167A
US2797167A US488997A US48899755A US2797167A US 2797167 A US2797167 A US 2797167A US 488997 A US488997 A US 488997A US 48899755 A US48899755 A US 48899755A US 2797167 A US2797167 A US 2797167A
Authority
US
United States
Prior art keywords
rosin
wax
fortified
fortified rosin
mol
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
US488997A
Inventor
Edwin R Kolodny
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.)
Wyeth Holdings LLC
Original Assignee
American Cyanamid Co
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
Application filed by American Cyanamid Co filed Critical American Cyanamid Co
Priority to US488997A priority Critical patent/US2797167A/en
Application granted granted Critical
Publication of US2797167A publication Critical patent/US2797167A/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
    • D21H17/62Rosin; Derivatives thereof
    • 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
    • D21H17/60Waxes

Definitions

  • the present invention relates to homogeneous blends of fortified rosin and wax suitable for conversion into paper sizing dispersions. More particularly, the invention relates to homogeneous fortified rosin-hydrophobic wax blends containing a higher alcohol as coupling agent, that is, as agent rendering the fortified rosin and wax mutually compatible.
  • the invention includes aqueous dispersions of the blends and paper sized therewith, as well as the several methods involved.
  • the rosin is present in unsaponified form, that is, in the form of a free organic acid.
  • Molten rosin has excellent compatibility. for wax and will form a homogeneous solution therewith in any ratio.
  • liquid rosin size that is, rosin predominantly in the form of sodium rosinate
  • saponifying with aqueous caustic Such size is now sold on a largecommercial. scale.
  • the reaction occurring is well-known Diels-Alder condensation, and is efiected by heating the rosin withthe acidic organic compound at 17S200. C. for a few hours.
  • the acidic organic compound is generally employed within the range of to 4 mol per mol of rosin, and best fortification is usually obtained within the range of about A to. /s mol of the-compound per mol of rosin.
  • the melting point of the fortified rosins. thus obtained is usually between about 140 and'200 F., depending principally on the amount and type of acid compound taken.
  • maleic anhydride other compounds may be used such as itaconic acid, citraconic acid, and the mixture. of acids or anhydrides obtained by heating.
  • rosin may be reacted with a large amount of the organic acidic material, say 0.7-0.9 mol, and then diluted with ordinary rosin to bring the amount of combined organic acid within the range mentioned above.
  • fortified rosin size When used in normal amounts, fortified rosin size usually causes increases of from 20 to 50% or more in the lactic acid values obtained over the values obtained in similar manner by the use of ordinary, rosin size.
  • the fortified rosin and wax are taken in the amounts at which ordinary rosin and wax have heretofore been employed for the manuf acture of paper sizes, that is, in weight ratio between about 40:60 and 60:40, so as to obtain maximum benefit from each component.
  • thewax andjfortified rosin are first melted together and the alcoholi s. then added in solid or liquid form.
  • the amount of alcohol added need be .no more than that sufficient'to cause the wax and fortified rosin to form a unitary, homogeneous mixture.
  • the precise amount of fatty alcohol needed is not the same in each instance as itidepends upon such variables as the number of anhydride groups in the.
  • any of the normally solid monohydric allganols may be. employed as well as mixtures thereof, that is alkanols which melt at temperatures above about 70 F.
  • alkanols include dodecanol, myristyl alcohol, octadecanolalready mentioned, and the mixtures of higher alcohols produced from oxidized petroleum.
  • the alcohols Preferably have melting points below 190 P. so as not to increase emulsification temperatures.
  • the primary alcohols having 16 to 20 carbon atoms give excellent coupling effect, are readily available, and melt below about F. Such alcohols are therefore pre ferred.
  • compositions of thepresent invention consist essentially of homogeneous blends offortified rosin and a wax in weight ratio between 40:60 and 60:40 together with a small but effective' amount of a normally solid monohydric primary fatty alcohol as coupling agent therefor.
  • the invention includes the blends both in solid and also in molten form.
  • the method of the present invention principally comprises the stirring together of fortified rosin and wax of the above-stated types in the above-stated proportions in molten form with a suitable higher fatty alcohol as coupling agent.
  • the hot melts may contain other materials customarily present in rosin-wax sizes including wax-soluble dyes, and organophilic fillers and pigments including organic polysiloxane-coated titanium dioxide pigment.
  • U. S. Patent No. 2,717,246 discloses pigment of this description.
  • the fortified rosins may be prepared from any of the rosins heretofore used in the manufacture of paper sizes.
  • Such rosins include gum rosin, wood rosin, and tall oil rosin.
  • Such rosins may and often do contain small amounts of special additives such as phenothiazine, diphenylamine, or N-phenyl-Z-naphthylamine as antioxidants; phenolic compounds such as saligenins as crystallization inhibitors; and sulfur or sulfur acid salts as residual catalysts.
  • the waxes in the compositions of the present invention are preferably hydrocarbon waxes having a melting point between about 115 and 190 F. these being the waxes customarily employed as sizing agents for paper.
  • Specific waxes frequently used are slack wax (a petroleum wax containing residual oil and having a melting point of about 120 F.), crude scale wax having a melting point of about 130 F., microcrystalline Waxes melting at about 130 to 150 F., and the highly refined petroleum waxes from which oil has largely been removed and which melt sharply at about 150 to 160 F. Although they have not been tried it is believed that any waterinsoluble hydrophobic wax melting below about 200 F. is benefited by the present invention including carnauba wax, candililla wax, bees wax, montan Wax and ozocerite,
  • Waxes are therefore included within the scope of the present invention.
  • waxes melting between about 115 and 160 F. since they permit comparatively low emulsification temperatures while affording sizes which confer excellent waterresistance to paper.
  • Aqueous dispersions of the foregoing blends may be prepared by any of the methods heretofore employed for the preparation of paper sizes from rosin-wax blends.
  • we have found the following general method to be particularly advantageous in that the dispersions obtained are quite stable to alum acidity and therefore on sheeting are more uniformly distributed through the web. The procedure involves two principal steps.
  • the first step consists in forming an aqueous phase by dissolving a hydrophilic colloidal gum and one or more alum-stable anionic dispersing agents of the sulfonate or sulfate type in water.
  • the weight of the water is sufficient so that the final dispersion contains 30 to 60% solids by weight.
  • the combined weight of the gum and dispersing agent should be determined as described below but is generally between about A% and 10% of the hot melt to be added.
  • the temperature of the water should be above the flow point of the hot melt so as to insure formation of an emulsion of the liquid-in-liquid type.
  • the hot melt is slowly poured into the aqueous phase with vigorous agitation.
  • An emulsion rapidly forms which is homogenized hot and then rapidly cooled to preserve the colloidal size of the particles.
  • the dispersing agents referred to are characterized in that 0.5% by weight aqueous solution thereof do not precipitate or flocculate at 20 C; in the presence of 500 p. p. m. of alum as aluminum sulfate tetradecylhydrate.
  • Representative members of the group include sodium propyl naphthalene sulfonate condensed with formaldehyde; sodium isopropylnaphthalene sulfonate; sodium tetrahydronaphthalene sulfonate; sodium octylsulfobenzoate condensed with formaldehyde; sodium lignin sulfonate; sodium octyl sulfate; the sodium salt of N-oleyl-N-methyltaurine, and the commercial agents known as Triton 720, Tanak KL, and Nacconal NR.
  • Triton 720 is the sodium sulfonate of octylphenol-ethylene oxide reaction product;
  • Tanak KL is the di-sodium salt of methylene-bis-naphthalene sulfonic acid; and Nacconal NR is sodium keryl benzene sulfonate.
  • any of the commercially available hydrophilic (i. e., water-soluble) materials may be used which have heretofore been employed as protective colloids for oil-in-water dispersions including gum arable, methylcellulose, sodium carboxymethyl cellulose, gum ghatti, and sodium 'alginate.
  • the anionic dispersing agent or agents should be employed to insure rapid and complete emulsification of the hot melt.
  • the amount will vary with the precise agent selected, the amount of combined organic acid in the fortified rosin, the temperature, and solids content of the batch, and can be most easily determined by trial.
  • Sufficient of the gum should be used to prevent flocculation when one volume of the resulting dispersion at 50% solids is cooled to 20 C. and diluted with 20 volumes of water. The several gums vary in their effectiveness and the optimum amount is likewise most conveniently determined by trial. So far, the total weight of gum and dispersing agent required has in no instance amounted to more than 10% of the weight of the hot melt.
  • the preferred dispersions of the present invention are uncommon in that they are not directly substantive towards cellulosic fibers and cannot be precipitated on the fibers by addition of alum, at least in conventional vamounts. They are most conveniently deposited by the action of subsequently-added liquid rosin and alum, the flocculated rosin size appearing to carry the fortified rosin-wax particles to the fibers.
  • Example 1 The following illustrates the preparation of a homogeneous hot melt and an alumand acid-stable paper sizing dispersion therefrom.
  • the hot melt was prepared as follows: gm. of fortified gum rosin (prepared by heating gum rosin with 0.25 mol of maleic anhydride at 200 C. for four hours) was melted on a steam bath. To this 170 gm. of molten refined petroleum paraflin wax (M. P. 155' F.) was slowly added with stirring. Two layers formed when stirring was momentarily stopped, showing that the two materials were incompatible, the wax floating as a very light tan layer on the rosin. Molten stearic alcohol was then slowly added with continued stirning. When 10 gm. of stearic alcohol had been added, the solution became homogeneous and did not separate on standing. The sizing dispersion was prepared by heating 600 gm.
  • the size gave satisfactorily high lactic acid resistance values when added to paper pulp in the heater and precipitated byaddition of rosin size and alum.
  • Example 2 Two comparative sizing dispersions were prepared to illustrate the jump in lactic acid resistance which occurs when ordinary rosin is replaced with fortified rosin according to the present invention.
  • the hot melts were prepared by the method of Example 2, except that the fortified rosin was prepared by the reaction of gum rosin with only 4% of its weight (M; mol) of maleic anhydride, and slack wax (M. P. 120 F.) was used in place of the refined parafiin wax.
  • the hot melts were emulsified by the method of Example 1, both emulsions being emulsified hot and rapidly cooled in the same manner.
  • the amount of stearyl alcohol used in size 3-B was about the needed to render the fortified rosin compatible with the wax.
  • the materials used were as follows:
  • Hot melt Percent Percent Gum rosin 24. 01 Nil Fortified gum rosin Nil 24. 01 Slack wax 24. 01 24. 01 Stearic alcohol Nil 0. 50 Aqueous phase:
  • the resulting dispersions were diluted to solids with water and applied to paper as follows.
  • a suspension of beaten 60% sulfite-40% soda fibers was diluted to a consistency of 2% with water and 2 aliquots withdrawn.
  • To each aliquot was added first 0.5% of one of the above described sizing dispersions, then 1.5% of liquid gum rosin size, and finally 2% of alum (solids in each instance based on the dry weight of the fibers) the pulps were sheeted on a British handsheet machine, dried at 190 F. for 2 minutes, conditioned for 24 hours at 73 F. and 50% relative humidity, and tested. Results are as follows:
  • Example 4 The stability of the sizing dispersion of Example 1 was demonstrated by stirring 10 gm. of the emulsion obtained into 200 cc. of water and adjusting the pH first to 5.0 by addition of hydrochloric acid and then to 8.5 by addition of sodium hydroxide. The dispersion remained stable throughout. A second test showing its alum stability was made by stirring 5 gm. of the emulsion into 100 cc. of water and adding sufiicient alum solution to decrease the pH to 4.5. The dispersion also remained stable for a period.
  • a homogeneous blend consisting essentially of fortified rosin and a hydrocarbon wax in weight ratio between 40:60 and 60:40 together with a small but effective amount of a C16C20 monohydric fatty alcohol as coupling agent therefor, said rosin corresponding to that formed by reacting 1 mol of rosin with between A and /5 mol of maleic anhydride, said wax having a melting point between about F. and F.
  • a blend according to claim 2 wherein the alcohol is stearic alcohol.
  • a colloidal aqueous dispersion of a blend according to claim 1 containing from 30% to 60% solids by weight.

Description

medium;
HYDROBHOBIC BLENDS coMPRIsmo ronrirrnnnosm AND, WAX
Edwin R. Kolodny, Stamford, Conn, assignor to American Cyanamid Company, NewYork, N. Y., a corporation of Maine N a in Appl cation eb uao 9 Serial'No. 488,997
Claims, ((11.16.61230) The present invention relates to homogeneous blends of fortified rosin and wax suitable for conversion into paper sizing dispersions. More particularly, the invention relates to homogeneous fortified rosin-hydrophobic wax blends containing a higher alcohol as coupling agent, that is, as agent rendering the fortified rosin and wax mutually compatible. The invention includes aqueous dispersions of the blends and paper sized therewith, as well as the several methods involved.
In the past, heavily sized paper for use as ice cream, cottage cheese, margarine, and butter containers and as oyster pails has been made by a process which comprises forming an aqueous slurry of papermaking cellulosic fibers, adding thereto an aqueous rosin-wax sizing dispersion (such as is formed by emulsifying a homogeneous rosin-wax hot melt in water), sheeting the fibers, and drying the Web thus formed at a convenient temperature within the range of about 190 260. F. The rosin-wax particles melt and flow during the heating step, thus conferring sizing to each fiber as a whole. In papers for the uses described, lactic acid; resistance is particularly important.
In such sizes the rosin is present in unsaponified form, that is, in the form of a free organic acid. Molten rosin has excellent compatibility. for wax and will form a homogeneous solution therewith in any ratio.
More recently it has been found that the lactic acid resistance of liquid rosin size (that is, rosin predominantly in the form of sodium rosinate) can be increased by first condensing rosin with a small amount of a compound of acidic character containing a -CO.C=C-linkage usually maleic anhydride (cf. U. 8. Patents Nos. 2,383,- 933, 2,628,918 and 2,684,300) thereby forming fortified rosin, and then saponifying with aqueous caustic. Such size is now sold on a largecommercial. scale.
The reaction occurring is well-known Diels-Alder condensation, and is efiected by heating the rosin withthe acidic organic compound at 17S200. C. for a few hours. The acidic organic compound is generally employed within the range of to 4 mol per mol of rosin, and best fortification is usually obtained within the range of about A to. /s mol of the-compound per mol of rosin. The melting point of the fortified rosins. thus obtained is usually between about 140 and'200 F., depending principally on the amount and type of acid compound taken. For example, in place of maleic anhydride other compounds may be used such as itaconic acid, citraconic acid, and the mixture. of acids or anhydrides obtained by heating. citric acid at 200 C. A number of other means are known for preparing fortified rosin, and thus rosin may be reacted with a large amount of the organic acidic material, say 0.7-0.9 mol, and then diluted with ordinary rosin to bring the amount of combined organic acid within the range mentioned above.
When used in normal amounts, fortified rosin size usually causes increases of from 20 to 50% or more in the lactic acid values obtained over the values obtained in similar manner by the use of ordinary, rosin size.
Patented June 25, 1957 Despite this foreseeable advantage, up to the present it has not been considered possible to employ fortified rosin in the manufacture of aqueous rosin-wax dispersions. The principal reason for this is that fortified rosin and waxv are incompatible when melted together, the materials behaving as mutual non-solvents even when stirred together for extended periods of times. This is due to the more organophobic character which fortified rosin possesses resulting from the presence of the organic acidic material therein. As a result, when molten fortified rosin-and wax are mixed, two layers form, the wax floating on-.the rosin layer and nosignificant solubilization occurs .even after thorough stirring.
' I have now discovered that the higher monohydric fatty alcohols such as stearic alcohol are coupling agents for molten fortified rosin-wax and that the presence of only a small amount'of such alcohols permits formation of fortified rosin-wax hot melts which are completely homogeneous and free fromany tendency to form two layers. I have further foundthat such homogeneous hot melts may be readily emulsified to form valuable sizing agents for paper.
It is of particular advantage that the alcohols referred to do not more than negligibly decrease the benefits expected from the presence of the fortified rosin.
In the preparation ofthe hot melts the fortified rosin and wax are taken in the amounts at which ordinary rosin and wax have heretofore been employed for the manuf acture of paper sizes, that is, in weight ratio between about 40:60 and 60:40, so as to obtain maximum benefit from each component. According to. one embodiment, thewax andjfortified rosin are first melted together and the alcoholi s. then added in solid or liquid form. The amount of alcohol added need be .no more than that sufficient'to cause the wax and fortified rosin to form a unitary, homogeneous mixture. The precise amount of fatty alcohol needed is not the same in each instance as itidepends upon such variables as the number of anhydride groups in the. fortified rosin, the fortified rosin:wax weight ratio, the chain lengthof the fatty alcohol selected, and the temperature of the melt. The amount is most easily found by trial, and so far less than 5% based on the weight of the melt has generally proved sufficient. Since normal melt temperatures do not exceed 200 F. and half an hour of mixingis ample to form the melt, no substantial esterification of they alcohol takes place.
As coupling agents any of the normally solid monohydric allganols may be. employed as well as mixtures thereof, that is alkanols which melt at temperatures above about 70 F. Such alcohols include dodecanol, myristyl alcohol, octadecanolalready mentioned, and the mixtures of higher alcohols produced from oxidized petroleum. Preferably the alcohols have melting points below 190 P. so as not to increase emulsification temperatures. The primary alcohols having 16 to 20 carbon atoms give excellent coupling effect, are readily available, and melt below about F. Such alcohols are therefore pre ferred.
From the foregoing it is apparent that the compositions of thepresent invention consist essentially of homogeneous blends offortified rosin and a wax in weight ratio between 40:60 and 60:40 together with a small but effective' amount of a normally solid monohydric primary fatty alcohol as coupling agent therefor. The fortified rosin is most conveniently described as corresponding to the mixture formed by reacting one mol of rosin with between about A and ,4 mol of a compound of acidic character containing a -C O-C=C-linkage. The invention includes the blends both in solid and also in molten form.
The method of the present invention principally comprises the stirring together of fortified rosin and wax of the above-stated types in the above-stated proportions in molten form with a suitable higher fatty alcohol as coupling agent.
The hot melts may contain other materials customarily present in rosin-wax sizes including wax-soluble dyes, and organophilic fillers and pigments including organic polysiloxane-coated titanium dioxide pigment. U. S. Patent No. 2,717,246 discloses pigment of this description.
The fortified rosins may be prepared from any of the rosins heretofore used in the manufacture of paper sizes. Such rosins include gum rosin, wood rosin, and tall oil rosin. Such rosins may and often do contain small amounts of special additives such as phenothiazine, diphenylamine, or N-phenyl-Z-naphthylamine as antioxidants; phenolic compounds such as saligenins as crystallization inhibitors; and sulfur or sulfur acid salts as residual catalysts.
The waxes in the compositions of the present invention are preferably hydrocarbon waxes having a melting point between about 115 and 190 F. these being the waxes customarily employed as sizing agents for paper. Specific waxes frequently used are slack wax (a petroleum wax containing residual oil and having a melting point of about 120 F.), crude scale wax having a melting point of about 130 F., microcrystalline Waxes melting at about 130 to 150 F., and the highly refined petroleum waxes from which oil has largely been removed and which melt sharply at about 150 to 160 F. Although they have not been tried it is believed that any waterinsoluble hydrophobic wax melting below about 200 F. is benefited by the present invention including carnauba wax, candililla wax, bees wax, montan Wax and ozocerite,
and such Waxes are therefore included within the scope of the present invention. In practice we prefer to use waxes melting between about 115 and 160 F. since they permit comparatively low emulsification temperatures while affording sizes which confer excellent waterresistance to paper. Aqueous dispersions of the foregoing blends may be prepared by any of the methods heretofore employed for the preparation of paper sizes from rosin-wax blends. However, we have found the following general method to be particularly advantageous in that the dispersions obtained are quite stable to alum acidity and therefore on sheeting are more uniformly distributed through the web. The procedure involves two principal steps.
The first step consists in forming an aqueous phase by dissolving a hydrophilic colloidal gum and one or more alum-stable anionic dispersing agents of the sulfonate or sulfate type in water. The weight of the water is sufficient so that the final dispersion contains 30 to 60% solids by weight. The combined weight of the gum and dispersing agent should be determined as described below but is generally between about A% and 10% of the hot melt to be added. The temperature of the water should be above the flow point of the hot melt so as to insure formation of an emulsion of the liquid-in-liquid type.
In the second step the hot melt is slowly poured into the aqueous phase with vigorous agitation. An emulsion rapidly forms which is homogenized hot and then rapidly cooled to preserve the colloidal size of the particles.
The dispersing agents referred to are characterized in that 0.5% by weight aqueous solution thereof do not precipitate or flocculate at 20 C; in the presence of 500 p. p. m. of alum as aluminum sulfate tetradecylhydrate. Representative members of the group include sodium propyl naphthalene sulfonate condensed with formaldehyde; sodium isopropylnaphthalene sulfonate; sodium tetrahydronaphthalene sulfonate; sodium octylsulfobenzoate condensed with formaldehyde; sodium lignin sulfonate; sodium octyl sulfate; the sodium salt of N-oleyl-N-methyltaurine, and the commercial agents known as Triton 720, Tanak KL, and Nacconal NR. Triton 720 is the sodium sulfonate of octylphenol-ethylene oxide reaction product;
I hot melt with vigorous agitation.
Tanak KL is the di-sodium salt of methylene-bis-naphthalene sulfonic acid; and Nacconal NR is sodium keryl benzene sulfonate.
As gums, any of the commercially available hydrophilic (i. e., water-soluble) materials may be used which have heretofore been employed as protective colloids for oil-in-water dispersions including gum arable, methylcellulose, sodium carboxymethyl cellulose, gum ghatti, and sodium 'alginate.
Sufficient of the anionic dispersing agent or agents should be employed to insure rapid and complete emulsification of the hot melt. The amount will vary with the precise agent selected, the amount of combined organic acid in the fortified rosin, the temperature, and solids content of the batch, and can be most easily determined by trial. Sufficient of the gum should be used to prevent flocculation when one volume of the resulting dispersion at 50% solids is cooled to 20 C. and diluted with 20 volumes of water. The several gums vary in their effectiveness and the optimum amount is likewise most conveniently determined by trial. So far, the total weight of gum and dispersing agent required has in no instance amounted to more than 10% of the weight of the hot melt.
The preferred dispersions of the present invention are uncommon in that they are not directly substantive towards cellulosic fibers and cannot be precipitated on the fibers by addition of alum, at least in conventional vamounts. They are most conveniently deposited by the action of subsequently-added liquid rosin and alum, the flocculated rosin size appearing to carry the fortified rosin-wax particles to the fibers.
The invention will be more particularly described by the examples which follow. These examples represent embodiments of the invention and are not to be construed as limitations thereon.
Example 1 The following illustrates the preparation of a homogeneous hot melt and an alumand acid-stable paper sizing dispersion therefrom.
The hot melt was prepared as follows: gm. of fortified gum rosin (prepared by heating gum rosin with 0.25 mol of maleic anhydride at 200 C. for four hours) was melted on a steam bath. To this 170 gm. of molten refined petroleum paraflin wax (M. P. 155' F.) was slowly added with stirring. Two layers formed when stirring was momentarily stopped, showing that the two materials were incompatible, the wax floating as a very light tan layer on the rosin. Molten stearic alcohol was then slowly added with continued stirning. When 10 gm. of stearic alcohol had been added, the solution became homogeneous and did not separate on standing. The sizing dispersion was prepared by heating 600 gm. of water to F., adding 40 gm. of gum arabic and 10 gm. of sodium lignin sulfonate, and slowly flowing in the A creamy emulsion resulted which was homogenized at once and rapidly cooled to about room temperature by flowing through a laboratory heat exchanger.
The size gave satisfactorily high lactic acid resistance values when added to paper pulp in the heater and precipitated byaddition of rosin size and alum.
Example 2 Example 3 Two comparative sizing dispersions were prepared to illustrate the jump in lactic acid resistance which occurs when ordinary rosin is replaced with fortified rosin according to the present invention. The hot melts were prepared by the method of Example 2, except that the fortified rosin was prepared by the reaction of gum rosin with only 4% of its weight (M; mol) of maleic anhydride, and slack wax (M. P. 120 F.) was used in place of the refined parafiin wax. The hot melts were emulsified by the method of Example 1, both emulsions being emulsified hot and rapidly cooled in the same manner. The amount of stearyl alcohol used in size 3-B was about the needed to render the fortified rosin compatible with the wax. The materials used were as follows:
Size
Hot melt: Percent Percent Gum rosin 24. 01 Nil Fortified gum rosin Nil 24. 01 Slack wax 24. 01 24. 01 Stearic alcohol Nil 0. 50 Aqueous phase:
Gum arabic 0.50 0. 50 Sodium llgm'n sulfonate 1. 20 1. 20 Dowieide 7 0. 12 0. 12 owieide G 0. 16 0. 16 50. 49. 50 Total 100. 00 100. 00
The resulting dispersions were diluted to solids with water and applied to paper as follows. A suspension of beaten 60% sulfite-40% soda fibers was diluted to a consistency of 2% with water and 2 aliquots withdrawn. To each aliquot was added first 0.5% of one of the above described sizing dispersions, then 1.5% of liquid gum rosin size, and finally 2% of alum (solids in each instance based on the dry weight of the fibers) the pulps were sheeted on a British handsheet machine, dried at 190 F. for 2 minutes, conditioned for 24 hours at 73 F. and 50% relative humidity, and tested. Results are as follows:
Thin Sheets Thick Sheets Sizing Dispersion Resistance to Lactic Sheet Sheet Acid Basis Basis Resist 4 Wt. Water 2 Ink 3 Wt. 1 (Sec (Sea) (See) Ex. B-A 46.4 55 310 194. 0 190 Ex. 3-B 45.9 59 375 193. 5 300 1 Lb. per 25 x 40 500 ream.
9 By Currier test (slack scale).
a By BKY method.
4 By penescope. The results show that the paper containing fortified gum rosin exhibited a jump in lactic acid resistance of 58%. This increase is wholly ascribable to the fortified rosin content of the size. The data also show very pronounced increases in the water and ink resistance values. The results further show that the stearyl alcohol present had at most only a negligible effect upon the sizingresults.
Example 4 The stability of the sizing dispersion of Example 1 was demonstrated by stirring 10 gm. of the emulsion obtained into 200 cc. of water and adjusting the pH first to 5.0 by addition of hydrochloric acid and then to 8.5 by addition of sodium hydroxide. The dispersion remained stable throughout. A second test showing its alum stability was made by stirring 5 gm. of the emulsion into 100 cc. of water and adding sufiicient alum solution to decrease the pH to 4.5. The dispersion also remained stable for a period.
I claim:
1. A homogeneous blend consisting essentially of fortified rosin and Wax in weight ratio between about 40:60 and :40 and a small but effective amount of a normaily solid mono-hydric fatty alcohol having a melting point below 190 F. as coupling agent therefor, said fortified rosin corresponding to that formed by reacting rosin with from about $4 to A of a mol of an organic compound of acidic character containing a COC=C- linkage, and said wax having a melting point between and 180 F.
2. A homogeneous blend consisting essentially of fortified rosin and a hydrocarbon wax in weight ratio between 40:60 and 60:40 together with a small but effective amount of a C16C20 monohydric fatty alcohol as coupling agent therefor, said rosin corresponding to that formed by reacting 1 mol of rosin with between A and /5 mol of maleic anhydride, said wax having a melting point between about F. and F.
3. A blend according to claim 2 wherein the alcohol is stearic alcohol.
4. A method of forming a homogeneous blend from fortified rosin and wax in weight ratio between about 40:60 and 60:40 which consists essentially of stirring said rosin and said Wax in molten form with a small but effective amount of a normally solid monohydric fatty alcohol having a melting point below 190 F. as coupling agent therefor, said fortified rosin corresponding to that formed by reacting rosin with from about A to A of a mol of an organic compound of acidic character containing a COC=C-linkage, and said wax having a melting point between 100 and F.
5. A colloidal aqueous dispersion of a blend according to claim 1 containing from 30% to 60% solids by weight.
References Cited in the file of this patent UNITED STATES PATENTS 1,394,610 De CeW Oct. 25, 1921 2,003,789 Falls June 4, 1935 2,198,289 Neitzke Apr. 23, 1940 2,317,372 Gessler et al. Apr. 27, 1943 2,324,671 Bernstein July 20, 1943 2,383,933 Bump Sept. 4, 1945 2,684,300 Wilson July 20, 1954

Claims (1)

1. A HOMOGENEOUS BLEND CONSISTING ESSENTIALLY OF FORTIFIED ROSIN AND WAX IN WEIGHT RATIO BETWEEN ABOUT 40:60 AND 40:60 AND A SMALL BUT EFFECTIVE AMOUNT OF A NORMALLY SOLID MONO-HYDRIC FATTY ALCOHOL HAVING A MELTING POINT BELOW 190*F. AS COUPLING AGENTHEREFOR, SAID FORTIFIED ROSIN CORRESPONDING TO THAT FORMED BY REACTING ROSIN WITH FROM ABOUT 1/12 TO 1/4 OF A MOL OF AN ORGANIC COMPOUND OF ACIDIC CHARACTER CONTAINING A -CO-C=CLINKAGE, AND SAID WAX HAVING A MELTING POINT BETWEEN 100* AND 180*F.
US488997A 1955-02-17 1955-02-17 Hydrophobic blends comprising fortified rosin and wax Expired - Lifetime US2797167A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US488997A US2797167A (en) 1955-02-17 1955-02-17 Hydrophobic blends comprising fortified rosin and wax

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US488997A US2797167A (en) 1955-02-17 1955-02-17 Hydrophobic blends comprising fortified rosin and wax

Publications (1)

Publication Number Publication Date
US2797167A true US2797167A (en) 1957-06-25

Family

ID=23941982

Family Applications (1)

Application Number Title Priority Date Filing Date
US488997A Expired - Lifetime US2797167A (en) 1955-02-17 1955-02-17 Hydrophobic blends comprising fortified rosin and wax

Country Status (1)

Country Link
US (1) US2797167A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3044890A (en) * 1958-03-31 1962-07-17 Becker & Co Ltd Paper sizing agents
JPS5043202A (en) * 1973-08-06 1975-04-18
JPS50156564A (en) * 1974-06-07 1975-12-17
US20170009400A1 (en) * 2015-07-10 2017-01-12 Minxuan TAN Method for manufacturing transfer paper

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1394610A (en) * 1921-10-25 Neebs
US2003789A (en) * 1932-08-27 1935-06-04 J F Kelley Composition and method of preparing same
US2198289A (en) * 1936-02-24 1940-04-23 Bennett Inc Sizing composition and process of preparation
US2317372A (en) * 1940-12-26 1943-04-27 Interchem Corp Method of printing and composition useful therein
US2324671A (en) * 1941-11-29 1943-07-20 H D Roosen Company Printing ink
US2383933A (en) * 1942-12-10 1945-09-04 Monsanto Chemicals Preparation of resinous dispersions
US2684300A (en) * 1948-05-13 1954-07-20 Monsanto Chemicals Sizing paper and product

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1394610A (en) * 1921-10-25 Neebs
US2003789A (en) * 1932-08-27 1935-06-04 J F Kelley Composition and method of preparing same
US2198289A (en) * 1936-02-24 1940-04-23 Bennett Inc Sizing composition and process of preparation
US2317372A (en) * 1940-12-26 1943-04-27 Interchem Corp Method of printing and composition useful therein
US2324671A (en) * 1941-11-29 1943-07-20 H D Roosen Company Printing ink
US2383933A (en) * 1942-12-10 1945-09-04 Monsanto Chemicals Preparation of resinous dispersions
US2684300A (en) * 1948-05-13 1954-07-20 Monsanto Chemicals Sizing paper and product

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3044890A (en) * 1958-03-31 1962-07-17 Becker & Co Ltd Paper sizing agents
JPS5043202A (en) * 1973-08-06 1975-04-18
JPS534866B2 (en) * 1973-08-06 1978-02-21
US4157982A (en) * 1973-08-06 1979-06-12 Monsanto Company Dispersed rosin
JPS50156564A (en) * 1974-06-07 1975-12-17
JPS5332380B2 (en) * 1974-06-07 1978-09-07
US20170009400A1 (en) * 2015-07-10 2017-01-12 Minxuan TAN Method for manufacturing transfer paper

Similar Documents

Publication Publication Date Title
AU726025B2 (en) Sizing composition
US4816073A (en) Aqueous dispersions, a process for their preparation and the use of the dispersions as sizing agents
US6048439A (en) Modified rosin emulsion
US4157982A (en) Dispersed rosin
US4743303A (en) Aqueous dispersions, a process for their preparation and the use of the dispersions as sizing agents
US2797167A (en) Hydrophobic blends comprising fortified rosin and wax
CA2085845C (en) Emulsified alkenylsuccinic acid sizing agent
US3050437A (en) Manufacture of sized paper
US4203776A (en) Aqueous fortified rosin dispersions
CA1107910A (en) Aqueous fortified rosin dispersions
US2117256A (en) Paper manufacture
US2340846A (en) Wax emulsion
US3279975A (en) Method of surface sizing paper with a reaction product of an unsaturated acid and a petroleum resin
US2665206A (en) Sizing of fibrous materials and compositions useful for sizing and for other purposes
US2056209A (en) Paper manufacture
JP3477932B2 (en) Rosin-based emulsion sizing agent for papermaking and paper sizing method
CA1134556A (en) Paper sizing agent and process for the preparation thereof
JPS5887395A (en) Papermaking size composition
US4404034A (en) Process for preparing aqueous dispersion of rosin-base materials
CA1057467A (en) Method of preparing aqueous dispersions of fortified rosin
US2058085A (en) Sizing paper
US2059465A (en) Sizing paper
US1842112A (en) Process of sizing paper
US2099880A (en) Composition of matter adapted for increasing the water-resistance of fibrous substances specifically paper products and process of making same
US1607519A (en) Paper product and process of making same