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US3002881A - Method of increasing the wet strength of cellulosic material and article formed thereby - Google Patents

Method of increasing the wet strength of cellulosic material and article formed thereby Download PDF

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US3002881A
US3002881A US621208A US62120856A US3002881A US 3002881 A US3002881 A US 3002881A US 621208 A US621208 A US 621208A US 62120856 A US62120856 A US 62120856A US 3002881 A US3002881 A US 3002881A
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resin
guanidine
hydrocolloid
pulp
cellulosic material
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US621208A
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Mcdonnell Basil
Jackson Harry Edward
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Teck Metals Ltd
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Teck Metals Ltd
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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/22—Proteins
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/47—Condensation polymers of aldehydes or ketones
    • D21H17/49—Condensation polymers of aldehydes or ketones with compounds containing hydrogen bound to nitrogen

Definitions

  • paper used herein is intended to include substances which are made in thin sheets or leaves from rags, straw, wood, or other fibrous, cellulosic material.
  • Wet strength paper is paper which has been treated during its manufacture so that it retains a considerable portion of its dry strength when saturated with water. Papers which have Wet strengths greater than about of their dry strengths are considered to be wet strength papers.
  • addition agents such as amino resins, and particularly urea and melamine resins
  • the urea and melamine resins suffer the disadvantage that they must normally be employed under acid conditions either in the pulp beating stage or after the paper formation stage. Such acid conditions are undesirable in that they tend to cause corrosion of metal parts of the papermaking machinery, and they affect adversely the permanency of the paper products and the parts of the apparatus with which the paper comes in contact after manufacture, such as converting and printing equipment.
  • Another group of amino resins, the guanidine resins are not considered to be wet-strength agents for paper and therefore have not heretofore been used for this purpose. Guanidine resins have been proposed for use in paper manufacture but only in minor amounts as a modifier of other amino resins and as a coagulant for dispersions of hydrophobic polymers such as natural and synthetic latexes.
  • water-soluble guanidine resins are in fact effective Wet strength agents when used in conjunction with a hydrophilic material which we refer to herein as a hydrocolloid.
  • a hydrophilic material which we refer to herein as a hydrocolloid.
  • the combination of resin and hydrocolloid can be employed with important advantages in the manufacture of wet strength papers.
  • the combinations of the present invention can be used under neutral, acid or alkaline conditions, and they impart to the treated paper a wet strength at least equivalent to that obtained by the use of known addition agents and usually substantially greater than 15% of the dry strength of the untreated paper.
  • the synthetic compounds are exemplified by sodium polymethylsilicon-- ate, sold under the trade name G.E. SC*50, and water soluble vinyl polymers.
  • guanidine resin alone nor the hydro colloid alone has an appreciable efiect on the Wet strength of pure cellulosic material compared with the result obtained with the combination of guanidine resin and hydrocolloid.
  • the water-soluble guanidine resins are prepared from guanidine salts and formaldehyde.
  • a ketone such as acetone or methyl ethyl ketone, can be used in conjunction with the formaldehyde in the preparation of the resin mixture to give the improved Wet strengths characteristic of the products of the present invention.
  • Guanidine-formaldehyde resins suitable for use in the present invention are those in which the mol ratio of formaldehyde to guanidine is at least 2: 1. This mol ratio may be substantially higher, for example, as high as 10: 1, and is preferably within the range of from about 4:1 to about 5:1. With mol ratios below 2:1, the guanidine resins do not produce satisfactory results.
  • the efiectiveness of the resin-hydrocolloid combination depends on chemical reaction of the resin with the hydrocolloid and the cellulose material to be treated. The reaction may depend on the presence in the resin of free methylol or methylene groups which cause bonding of the resin to the cellulose. With ratios of formaldehyde to guanidine of less than 2:1, the proportion of free methylol or methylene groups is low, and the combination of resin and hydrocolloid is not effective as a wet strength agent.
  • a ketone can be used with the formaldehyde to prepare the guanidine resin.
  • the mol ratio of formaldehyde to ketone should be at least 2:1
  • the mol ratio of formaldehyde to guanidine should be at least 1:1
  • the mol ratio of formaldehyde plus ketone to guanidine should be at least 1.5: 1.
  • the ratio of formaldehyde to guanidine in such mixtures is preferably higher than 1:1, usually about 4:1 to 5:1, although ratios of 10:1 or more can be used.
  • Guanidine carbonate is a suitable salt for the preparation of guanidine resins which are useful for the purpose of the present invention.
  • Other salts of guanidine such as the sulphate, the nitrate, the chloride and the acetate, can be used and derivatives such a methyl guanidine sulphate also produce good results.
  • Other guanidine salts such as the sulphamate and the thiocyanate are less satisfactory and certain other guanidine compounds, such as diphenyl guanidine, are not suitable.
  • the water-soluble guanidine resin can be prepared by heating, at about its boiling temperature, an aqueous solution of a guanidine salt with formaldehyde to form a syrup. Boiling is discontinued while the resin is still in the form of a syrup and before it converts to a gel.
  • This syrup is water soluble and can be used as such or it can be diluted for convenience in handling or metering; or it can be evaporated, for example, under vacuum,
  • the resin can be added as an aqueous solution to the cellulose stock to be treated.
  • Themanner in whichtheguanidine salt-formaldehyde heating step is conducted is important. terminated before the. resulting syrup commences to form .a gel. Prolonged heating results in the formation ofa gel and finally -a solid.
  • the formation of a gel or solid in the heating step is an indication that resin condensation has progressed .toofar; theresultant condensation product is not water soluble and is unsuitable as an additive for cellulose treatment to increase the wet strength of the desired product.
  • the water-soluble guanidine resins can be used without the addition of a hydrocolloid for treating pulps such as unbleached kraft and. ground wood pulp, probably due to the presence in such pulp of hydrocolloid material such as lignin or tannin. However, we have found that substantially improved. results are obtained even with these pulps by the combination of a water-soluble guanidine resin and additional. hydrocolloid.
  • Fillers, sizes and other addition agents usually are employed in the manufacture .of fibrous cellulosic materials to improve. desired properties. in the resulting product. Fillers such ascalcium carbonate and zinc oxide cannot readily bev used under the acid conditions normally required by ureaand melamine resins in the manufacture. of wet strength papers, although some fillers, such as titanium dioxide .and clay, are compatible with such acid conditions.
  • An important advantage of the use of the guanidine resin-hydrocolloid combination of this invention is that the combination is not restricted to use under any specific condition of hydrogen ion concentration but can.
  • guanidine resin-hydrocolloid combination of the present invention for example, guanidine resin and Separan, increases the percentage'retentionv of the fillers in the final cellulose products.
  • the guanidine resin-hydrocolloid combination can be incorporated into the cellulosic stock at any convenient stage of manufacture of the desired product, that is, at the beater, or the stock chest or .the head tank. It can be used as a stream, as'a tub size, or as a spray. For economy of equipment and convenience of operation, it is preferred to make the addition to the pulp at the beating stage.
  • the conditions under which the method of the present invention can be operated can be'varied relatively wide- 1y.
  • cellulosic pulp in which the water-soluble guanidine resin'is employed can be from about pH 3 to about pH ll, but is usually from about pH 6 to pH 8, and is preferably from about pH 7 to about pH 8 in order to ob' tain the advantages for both'the product and equipment of neutral or slightlyalkaline conditions.
  • alum treatment commonly used with other wet strengthadditives, such as melamine and urea resins.
  • the amount of Water-soluble guanidine resin employed can vary from about 0.1% to 10% by weight based on the dry weight of the cellulosic material to be treated, and is. usually larger than the amount of hydrocolloid required.
  • Theamount of hydrocolloid present in the pulp suspension can be from. about 0.02% to about 10% or more of the dry weight of the cellulosic material, depending on the particular hydrocolloidused, andwhether substances having -hydrocolloidal. properties are present in the pulp. For example, in the manufacture of: paper and hardboard from unbleached kraft-pulp, it-is not so essential to add a hydrocolloid with the guanidine resin,
  • the water-soluble guanidine resin by weight, ofthe water-soluble guanidine resin and from about 1% to about 5%, by weight, of the hydrocolloid.
  • the ratio of resin to hydrocolloid is usually about 2:1. This particularratio can be varied widely, of course, depending on the hydrocolloid employed.
  • the resin should be aged to obtain the highest wet strengths in the resulting fibrous cellulose products.
  • the aging process merely involves storing the resin as solution, i.e. syrup, or as a solid under normal atmospheric temperature and pressure conditions for a period of from about one to seven days during which condensation of the resin proceeds to the stage at which the resin produces the best results-in improving. the wet strength of the fibrous cellulosic material. It is merely necessary, in order to determinethe aging. period for a specific resin, to conduct smallscale tests with samples of cellulose stock and observe the results obtained. After aging, the resin retains its activity-for several months.
  • EXAMPLE 1 5.8 grams of acetone, 33.3 grams of formaldehyde (40% solution) and 0.5 ml. of 20% sodium hydroxide solution were mixed and heated at about 40 C. for period of time sufiicient. for the reaction between the constituents to take place. The mixture was then boiledfor about 10 minutesunder a refiux condenser. 13.5 grams of guanidine carbonate in 50 ml. of water were added to the mixture and the resulting mixture was boiled for 15 minutes and. then diluted with Water to 200 ml. The resulting resin syrup was aged for 7 days.
  • EXAMPLE 3 mixture was boiled .forten minutes andthen diluted with water to 200 ml.
  • EXAMPLE 6 5.8 gramsof acetone; 45.0 grams of formaldehyde (40% solution), and l.ml.- of 20% sodium hydroxide solution were mixed and boiled for 10 minutes. 21.6 grams: of guanidine sulphate and 12.4 grams of sodium carbonate (Na CO .H' O) dissolved in 50 ml; of water were added to .the mixture :andthe 1 resulting mixture was boiledwfor 10" minutes and then diluted with water to- EXAMPLE 7 The same procedure was followed as in Example 3, but using 7.5 grams of sodium carbonate (N'a CO H O).
  • EXAMPLE 8 The same procedure was followed as in Example 3, but using 9.3 grams of sodium carbonate (Na CO .H O).
  • the sodium compounds used in Examples "1, 3, 4, 5, 6, 7 and 8 above were added to adjust the pH value of the resin mixture to ensure a value of not less than pH 7.
  • the pH of the guanidine resin mixture should be 7 or higher, preferably 10 to 10.5, for satisfactory results. It may be that with pH values less than 7, condensation of the resin proceeds too far. Althrough the pH of the guanidine resin should not be less than 7, the pH of the pulp solution to which the resin is added may vary from about p l-1'3 to about pH 11, as noted previously.
  • the resin solution is added to a water suspension of cellulose pulp in amount corresponding to about 5%, for example,
  • a hydrocolloid based on the dry weight of the pulp.
  • the hydrocolloid is less essential, as noted previously, but is beneficial.
  • the resultant fibrous cellulosic product should be cured after drying, or the curing may be incorporated in the drying stage. Curingis efiected by heating the product for a time which varies with the temperature. A time period of one hour at about 90 C. is satisfactory. Longer times, up to several days, may be required at lower temperatures, such as 70 C., and shorter times at higher temperatures.
  • the hydrocolloid can be added to the pulp suspension before, with or after the resin, or the resin and hydrocolloid solutions can be mixed and the mixture added to the suspension. It may be convenient to use such mixtures, which can be stored for periods up to 24 hours without impairing their effectiveness, but usually the resin and hydrocolloid are added to the pulp suspension separately at the same stage of operation, preferably at the beater.
  • the following table illustrates the results obtained in wet strength tests using different combinations of watersoluble guanidine resins and hydrocolloids with different cellulosic pulps.
  • the percentage figures for resin and hydrocolloid are based on the dry weight of the pulp.
  • the resin solutions numbers in the table correspond to the preceding examples, solution No. 1 being prepared according to Example 1, solution N0. 2, according to Example 2, etc.
  • the letter K applied to the furnish stands for unbleached kraft pulp, R for highly refined pullp, such as almost pure cellulose pulp, and S for bleached sulphite pulp.
  • the testing procedure consisted of beating a furnish containing about 1.5 grams of pulp, 400 ml. of water and the stated amounts of resin and hydrocolloid for two minutes, then draining the water through a screen. The resulting sheet was sucked free of water, pressed with a load of 250 pounds per square inch for twenty seconds and dried and cured at 100 C. for two hours. The dried and cured sheet was soaked in water for five minutes. Excess water was removed by placing the sheet on blotting paper for 10 minutes. Wet strength measurements were then made using a Mullen bursting tester. These measurements gave the figures in the Wet strength column of the table.
  • the Mullen measurements were 13, 25 and 20 for paper prepared from unbleached kraft pulp, highly refined pulp and bleached sulphite pulp, respectively.
  • hydrocolloids that we have found to be suitable for the purpose of the present invention includes the following:
  • Carbohydrates starch, dextrin, karaya gum, 'guar gum, locust bean gum, gum arabic, gum tragacanth, hydroxyethyl starch, hydroxyethyl cellulose, methyl cellulose, sodium carboxymethyl cellulose, sodium alginate, Chinese vegetable gelatin;
  • Proteins gelatin, glue, zein, egg albumin, blood albumin, soy bean flour, soy bean protein (alpha protein), casein;
  • Wood hydrocolloids lignin, Goulae (calcium lignin sulphonate) tannin;
  • Synthetic hydrocolloids polyvinyl alcohol, p'olyacrylamide, partially degraded polyacrylamide (by Hofmann reaction), poly-acrylamide hydrolyte (Separan 2610), polyvinyl pyrrolidone, polyvinyl methyl ether/maleic anhydride copolymer, styrene/maleic anhydride copolymer (Stymer S), sodium polymethylsiliconate.
  • the present invention possesses a number of important advantages.
  • the Water-soluble guanidine resin can be prepared easily and inexpensively under moderate operating conditions.
  • the use of a water-soluble guanidine resin in conjunction with a hydrocolloid in accordance with the present invention results in a substantial improvement in both the wet strength and dry strength of treated fibrous cellulosic material.
  • the combination of resin and hydrocolloid possesses the added important advantage that it can be used with fibrous cellulosic pulp mixtures over a wide range of hydrogen ion concentrations of from about pH 3 to about pH 1d thus permitting its use with acid, neutral or alkaline pulp mixtures.
  • the improvement which comprises thestep O r-treating saidw fibrous cellulosic material with a combination composed of water soluble guanidine-formalde'hyde resin and a hydrocolloid, the formaldehyde being present in said resin in the ratio of at least abouti2 mols per mol of guanidine, said resin being provided in amount of at least about 0.1% by weight based on the dry-weight of the fibrous cellulosic material, and said hydrocolloid being, provided in amount 6.
  • a process for producing paper which comprises forming an aqueous pulp of fibrous cellulosic material, removing-water from said pulp and forming said pulp into asheet, their'n'provementizwhich comprises providing in at least about 1.5 mols-per mol of guanidine, said resin being provided in amount of at least about 0.1% by Weight based on the dryweight of the fibrous cellulosic material,- and said hydrocolloid being provided in amount of-at leastabout-0.02% by weight based on the dry of at least about 0.02% by weight based onthe dry:weight 15 r Weight 05/1116 fibrous -Ce1l1110SiC at al.
  • hydrocolloid is a'member selected from the group, consistingrof proteins, carbohydrates, wood hydrocolloids' and synthetic hydrocolloids.
  • the'hydro colloid is a member selected from-th egroup consisting; of gelatin, starch, lignin, polyacryl-amide-hydrolyte and sodium polymethylsiliconate.
  • a process for producing paper which comprises"- forming an aqueous pulp of fibrouscellulosic material; removing water from said pulp and forming said pulp into a sheet, the improvement which comprises providing in said pulp a combination oompose'd'of water solubleguanidine-formaldehyde resin and a hydrocolloid, theformaldehyde being present in said resin in the ratio ofatleast about 2 mols per mol of guanidine,- said resin being provided in amount of at least about 0.1% by weight based on the dryweight of the fibrous cellulosic material, and said hydrocolloid being provided in amount of at least about 0.02% by weight based on the dry weight ofthe fibrous cellulosic material.
  • a fibrous cellulosic material treated with a combination of guanidine-formaldehyde resin and a hydrocolloid the formaldehyde being present in said resin in the ratio of at least about 2 mols of formaldehyde per mol of 2m guanidine, said-resin being present in amount of at least about 0.1%by weight based on the dry weight of the fibrous cellulosic material, and said hydrocolloid being present in amount of at-least about 0.02% by weight based on the dry weight of the fibrous cellulosic material.

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Description

United States Patent Ofiice 3,002,88i Patented Oct. 3, 19 61 This invention relates to an improved method of increasing the wet strength properties of cellulosic products and to the cellulosic products produced thereby.
It is well known to treat cellulosic materials, such as paper, prior to or following the sheet formation stage, with certain addition agents to improve the wet strength properties of the resulting products.
The term paper used herein is intended to include substances which are made in thin sheets or leaves from rags, straw, wood, or other fibrous, cellulosic material. Wet strength paper is paper which has been treated during its manufacture so that it retains a considerable portion of its dry strength when saturated with water. Papers which have Wet strengths greater than about of their dry strengths are considered to be wet strength papers.
It is known that the use of addition agents, such as amino resins, and particularly urea and melamine resins, are effective for improving or increasing the wet strength properties of fibrous cellulosic materials. However, the urea and melamine resins suffer the disadvantage that they must normally be employed under acid conditions either in the pulp beating stage or after the paper formation stage. Such acid conditions are undesirable in that they tend to cause corrosion of metal parts of the papermaking machinery, and they affect adversely the permanency of the paper products and the parts of the apparatus with which the paper comes in contact after manufacture, such as converting and printing equipment. Another group of amino resins, the guanidine resins, are not considered to be wet-strength agents for paper and therefore have not heretofore been used for this purpose. Guanidine resins have been proposed for use in paper manufacture but only in minor amounts as a modifier of other amino resins and as a coagulant for dispersions of hydrophobic polymers such as natural and synthetic latexes.
We have found that water-soluble guanidine resins are in fact effective Wet strength agents when used in conjunction With a hydrophilic material which we refer to herein as a hydrocolloid. The combination of resin and hydrocolloid can be employed with important advantages in the manufacture of wet strength papers.
The combinations of the present invention can be used under neutral, acid or alkaline conditions, and they impart to the treated paper a wet strength at least equivalent to that obtained by the use of known addition agents and usually substantially greater than 15% of the dry strength of the untreated paper.
As used herein, the term hydrocolloid is intended to mean hydrophilic substances of the gelatin sol type as defined in Thorpes Dictionary of Applied Chemistry, 4th Edition, volume 3, page 279, and synthetic hydrophilic substances having properties similar to those of the naturally occurring gelatin so=l type of substances. These natural and synthetic substances form colloidal or nearcolloidal solutions in Water. Included in these hydrocolloids are substances which may not be hydrophilic under neutral conditions but which absorb water under alkaline conditions, for example, casein. The synthetic compounds are exemplified by sodium polymethylsilicon-- ate, sold under the trade name G.E. SC*50, and water soluble vinyl polymers. The hydrocolloids which we have found suitable for use with guanidine resins for the purpose of imparting wet strength to fibrous cellulosic material include proteins, for example, gelatin, glue, albumin, casein; carbohydrates, for example, starch, dextn'n, methyl cellulose; Wood products, for example, tannin and lignin; and synthetic hydrooolloids, such as sodium polymethylsiliconate, polyvinyl alcohol, polyvinyl acetate, and the polyacrylarnide hydrolyte sold under the trade name Separan 2610.
Neither the guanidine resin alone nor the hydro colloid alone has an appreciable efiect on the Wet strength of pure cellulosic material compared with the result obtained with the combination of guanidine resin and hydrocolloid.
The water-soluble guanidine resins are prepared from guanidine salts and formaldehyde. A ketone, such as acetone or methyl ethyl ketone, can be used in conjunction with the formaldehyde in the preparation of the resin mixture to give the improved Wet strengths characteristic of the products of the present invention.
Guanidine-formaldehyde resins suitable for use in the present invention are those in which the mol ratio of formaldehyde to guanidine is at least 2: 1. This mol ratio may be substantially higher, for example, as high as 10: 1, and is preferably within the range of from about 4:1 to about 5:1. With mol ratios below 2:1, the guanidine resins do not produce satisfactory results. We believe that the efiectiveness of the resin-hydrocolloid combination depends on chemical reaction of the resin with the hydrocolloid and the cellulose material to be treated. The reaction may depend on the presence in the resin of free methylol or methylene groups which cause bonding of the resin to the cellulose. With ratios of formaldehyde to guanidine of less than 2:1, the proportion of free methylol or methylene groups is low, and the combination of resin and hydrocolloid is not effective as a wet strength agent.
A ketone can be used with the formaldehyde to prepare the guanidine resin. In such mixtures the mol ratio of formaldehyde to ketone should be at least 2:1, the mol ratio of formaldehyde to guanidine should be at least 1:1 and the mol ratio of formaldehyde plus ketone to guanidine should be at least 1.5: 1. The ratio of formaldehyde to guanidine in such mixtures is preferably higher than 1:1, usually about 4:1 to 5:1, although ratios of 10:1 or more can be used.
Guanidine carbonate is a suitable salt for the preparation of guanidine resins which are useful for the purpose of the present invention. Other salts of guanidine such as the sulphate, the nitrate, the chloride and the acetate, can be used and derivatives such a methyl guanidine sulphate also produce good results. Other guanidine salts such as the sulphamate and the thiocyanate are less satisfactory and certain other guanidine compounds, such as diphenyl guanidine, are not suitable.
The presence of the sulphate ion is not objectionable in carrying out the process of the present invention whereas its presence is not compatible with the use of melamine resins employed in known processes for the production of wet strength paper.
The water-soluble guanidine resin can be prepared by heating, at about its boiling temperature, an aqueous solution of a guanidine salt with formaldehyde to form a syrup. Boiling is discontinued while the resin is still in the form of a syrup and before it converts to a gel. This syrup is water soluble and can be used as such or it can be diluted for convenience in handling or metering; or it can be evaporated, for example, under vacuum,
to form a water-soluble solid for convenience in shipping or storage. The resin can be added as an aqueous solution to the cellulose stock to be treated.
Themanner in whichtheguanidine salt-formaldehyde heating step is conducted is important. terminated before the. resulting syrup commences to form .a gel. Prolonged heating results in the formation ofa gel and finally -a solid. The formation of a gel or solid in the heating step is an indication that resin condensation has progressed .toofar; theresultant condensation product is not water soluble and is unsuitable as an additive for cellulose treatment to increase the wet strength of the desired product.
The water-soluble guanidine resins can be used without the addition of a hydrocolloid for treating pulps such as unbleached kraft and. ground wood pulp, probably due to the presence in such pulp of hydrocolloid material such as lignin or tannin. However, we have found that substantially improved. results are obtained even with these pulps by the combination of a water-soluble guanidine resin and additional. hydrocolloid.
Fillers, sizes and other addition agents usually are employed in the manufacture .of fibrous cellulosic materials to improve. desired properties. in the resulting product. Fillers such ascalcium carbonate and zinc oxide cannot readily bev used under the acid conditions normally required by ureaand melamine resins in the manufacture. of wet strength papers, although some fillers, such as titanium dioxide .and clay, are compatible with such acid conditions. An important advantage of the use of the guanidine resin-hydrocolloid combination of this invention is that the combination is not restricted to use under any specific condition of hydrogen ion concentration but can. be employed over a wide range of hydrogen ion concentrations, for example, from about pH 3 to pH 11, and is compatible with the fillers, sizes and other addition agents conventionally employed inthemanufacture of fibrous, cellulosic products. In this regard, we have found that in some cases the use of the guanidine resin-hydrocolloid combination of the present invention, for example, guanidine resin and Separan, increases the percentage'retentionv of the fillers in the final cellulose products.
The guanidine resin-hydrocolloid combination can be incorporated into the cellulosic stock at any convenient stage of manufacture of the desired product, that is, at the beater, or the stock chest or .the head tank. It can be used as a stream, as'a tub size, or as a spray. For economy of equipment and convenience of operation, it is preferred to make the addition to the pulp at the beating stage.
The conditions under which the method of the present invention can be operated can be'varied relatively wide- 1y. The pH range of the aqueous suspension of fibrous,
cellulosic pulp in which the water-soluble guanidine resin'is employed can be from about pH 3 to about pH ll, but is usually from about pH 6 to pH 8, and is preferably from about pH 7 to about pH 8 in order to ob' tain the advantages for both'the product and equipment of neutral or slightlyalkaline conditions. There is no need in our process for the alum treatment commonly used with other wet strengthadditives, such as melamine and urea resins.
The amount of Water-soluble guanidine resin employed can vary from about 0.1% to 10% by weight based on the dry weight of the cellulosic material to be treated, and is. usually larger than the amount of hydrocolloid required. Theamount of hydrocolloid present in the pulp suspension can be from. about 0.02% to about 10% or more of the dry weight of the cellulosic material, depending on the particular hydrocolloidused, andwhether substances having -hydrocolloidal. properties are present in the pulp. For example, in the manufacture of: paper and hardboard from unbleached kraft-pulp, it-is not so essential to add a hydrocolloid with the guanidine resin,
It should be results are obtained with from about 1% to about 10%,
by weight, ofthe water-soluble guanidine resin and from about 1% to about 5%, by weight, of the hydrocolloid. The ratio of resin to hydrocolloid is usually about 2:1. This particularratio can be varied widely, of course, depending on the hydrocolloid employed.
The resin should be aged to obtain the highest wet strengths in the resulting fibrous cellulose products. The aging process merely involves storing the resin as solution, i.e. syrup, or as a solid under normal atmospheric temperature and pressure conditions for a period of from about one to seven days during which condensation of the resin proceeds to the stage at which the resin produces the best results-in improving. the wet strength of the fibrous cellulosic material. It is merely necessary, in order to determinethe aging. period for a specific resin, to conduct smallscale tests with samples of cellulose stock and observe the results obtained. After aging, the resin retains its activity-for several months.
The following examples illustrate methods of preparing water-soluble guanidine resins suitable for use in this invention:
EXAMPLE 1 5.8 grams of acetone, 33.3 grams of formaldehyde (40% solution) and 0.5 ml. of 20% sodium hydroxide solution were mixed and heated at about 40 C. for period of time sufiicient. for the reaction between the constituents to take place. The mixture was then boiledfor about 10 minutesunder a refiux condenser. 13.5 grams of guanidine carbonate in 50 ml. of water were added to the mixture and the resulting mixture was boiled for 15 minutes and. then diluted with Water to 200 ml. The resulting resin syrup was aged for 7 days.
EXAMPLE 2 45 grams of formaldehyde (40% solution), 18 grams of guanidine carbonate and 25 ml. of water were mixed and boiled for 1 hour under a reflux condenser and the resulting resin syrup was diluted with water to 200 ml. The aging period of this resin syrup was 7 days.
EXAMPLE 3 mixture was boiled .forten minutes andthen diluted with water to 200 ml.
EXAMPLE 4 The same procedure was followed as in Example 3 but using only 3.8 grams of sodium carbonate (Na CO .H O).
EXAMPLE 5 The same procedure was followed as in Example 3 but the guanidine resin. syrup, after boiling, was cooled and evaporated to dryness under a vacuum.
EXAMPLE 6 5.8 gramsof acetone; 45.0 grams of formaldehyde (40% solution), and l.ml.- of 20% sodium hydroxide solution were mixed and boiled for 10 minutes. 21.6 grams: of guanidine sulphate and 12.4 grams of sodium carbonate (Na CO .H' O) dissolved in 50 ml; of water were added to .the mixture :andthe 1 resulting mixture was boiledwfor 10" minutes and then diluted with water to- EXAMPLE 7 The same procedure was followed as in Example 3, but using 7.5 grams of sodium carbonate (N'a CO H O).
EXAMPLE 8 The same procedure was followed as in Example 3, but using 9.3 grams of sodium carbonate (Na CO .H O).
The sodium compounds used in Examples "1, 3, 4, 5, 6, 7 and 8 above were added to adjust the pH value of the resin mixture to ensure a value of not less than pH 7. We have found that the pH of the guanidine resin mixture should be 7 or higher, preferably 10 to 10.5, for satisfactory results. It may be that with pH values less than 7, condensation of the resin proceeds too far. Althrough the pH of the guanidine resin should not be less than 7, the pH of the pulp solution to which the resin is added may vary from about p l-1'3 to about pH 11, as noted previously.
In the use of the guanidine resin addition agents, the resin solution is added to a water suspension of cellulose pulp in amount corresponding to about 5%, for example,
based on the dry weight of the pulp. A hydrocolloid,
such as gelatin, in amount corresponding to 2.5%, for example, of the dry weight of the pulp, is added to the pulp suspension as a solution in water at the same time as the resin, and the pulp suspension is then thoroughly mixed. The usual sheet-forming and drying steps follow. With relatively crude pulps the hydrocolloid is less essential, as noted previously, but is beneficial.
For best results, the resultant fibrous cellulosic product should be cured after drying, or the curing may be incorporated in the drying stage. Curingis efiected by heating the product for a time which varies with the temperature. A time period of one hour at about 90 C. is satisfactory. Longer times, up to several days, may be required at lower temperatures, such as 70 C., and shorter times at higher temperatures.
The hydrocolloid can be added to the pulp suspension before, with or after the resin, or the resin and hydrocolloid solutions can be mixed and the mixture added to the suspension. It may be convenient to use such mixtures, which can be stored for periods up to 24 hours without impairing their effectiveness, but usually the resin and hydrocolloid are added to the pulp suspension separately at the same stage of operation, preferably at the beater.
The following table illustrates the results obtained in wet strength tests using different combinations of watersoluble guanidine resins and hydrocolloids with different cellulosic pulps. The percentage figures for resin and hydrocolloid are based on the dry weight of the pulp. The resin solutions numbers in the table correspond to the preceding examples, solution No. 1 being prepared according to Example 1, solution N0. 2, according to Example 2, etc. The letter K applied to the furnish stands for unbleached kraft pulp, R for highly refined pullp, such as almost pure cellulose pulp, and S for bleached sulphite pulp.
The testing procedure consisted of beating a furnish containing about 1.5 grams of pulp, 400 ml. of water and the stated amounts of resin and hydrocolloid for two minutes, then draining the water through a screen. The resulting sheet was sucked free of water, pressed with a load of 250 pounds per square inch for twenty seconds and dried and cured at 100 C. for two hours. The dried and cured sheet was soaked in water for five minutes. Excess water was removed by placing the sheet on blotting paper for 10 minutes. Wet strength measurements were then made using a Mullen bursting tester. These measurements gave the figures in the Wet strength column of the table. For dried sheets prepared in the same manner but not treated with resin or hydrocolloid, and not subjected to the soaking step, the Mullen measurements were 13, 25 and 20 for paper prepared from unbleached kraft pulp, highly refined pulp and bleached sulphite pulp, respectively.
, Table I Guanldlne Resin Hydrocolloid Furnish Wet Wt. Wt. Strength No. per- Material per- Type pH cent cent R 0 S 0 K 0 R 7.0 40 2.5 K 7.8 0 2.5 K 7.8 36 2.5 K 8.0 51 K 8.0 15 2.5 S 7.2 45 1.0 S 7.0 35 2.5 S 7.2 49 5.0 R 6.8 18.5 10 R 7.5 0 2.5 R 7.6 22 2.5 R 8.0 23 R 7.0 0 2.5 R 8.0 15.5 2.5 R 8.0 0 2.5 S 7.6 75 0.02 R 8.0 9 0.5 R 6.8 23 2.5 R 7.2 30 2.5 R 7.6 0 2.5 S 7.6 40 2.5 S 7.4 1 2.5 R 4.0 3 2.5 R 6.0 11.5 2.5 R 7.6 14 2.5 R 9.0 3.5 2.5 K 5.0 5 2.5 K 6.0 26 2.5 K 10.0 13 2.5 S 4.0 6.5 2.5 S 6.0 21 2.5 S 10.5 5 g 2.5 S 7.2 28 Alpha protein 2.5 R 8.5 4.5 Casein 2.5 R 8.0 9 Karaya gum 2.5 R 7.0 11
a 3 ml. 5% N fiZCOil-HZO solution added when beating the pulp.
b 3.5 ml. 5% Na2C0s.H2O solution added when beating the pulp; furnish beaten for 3.5 min.
a 3.5 ml. 5% N 212003320 solution added when beating the pulp.
A list of the hydrocolloids that we have found to be suitable for the purpose of the present invention includes the following:
Carbohydrates: starch, dextrin, karaya gum, 'guar gum, locust bean gum, gum arabic, gum tragacanth, hydroxyethyl starch, hydroxyethyl cellulose, methyl cellulose, sodium carboxymethyl cellulose, sodium alginate, Chinese vegetable gelatin;
Proteins: gelatin, glue, zein, egg albumin, blood albumin, soy bean flour, soy bean protein (alpha protein), casein;
Wood hydrocolloids: lignin, Goulae (calcium lignin sulphonate) tannin;
Synthetic hydrocolloids: polyvinyl alcohol, p'olyacrylamide, partially degraded polyacrylamide (by Hofmann reaction), poly-acrylamide hydrolyte (Separan 2610), polyvinyl pyrrolidone, polyvinyl methyl ether/maleic anhydride copolymer, styrene/maleic anhydride copolymer (Stymer S), sodium polymethylsiliconate.
The present invention possesses a number of important advantages. The Water-soluble guanidine resin can be prepared easily and inexpensively under moderate operating conditions. The use of a water-soluble guanidine resin in conjunction with a hydrocolloid in accordance with the present invention results in a substantial improvement in both the wet strength and dry strength of treated fibrous cellulosic material. The combination of resin and hydrocolloid possesses the added important advantage that it can be used with fibrous cellulosic pulp mixtures over a wide range of hydrogen ion concentrations of from about pH 3 to about pH 1d thus permitting its use with acid, neutral or alkaline pulp mixtures.
It will be understood, of course, that modifications can be made in the embodiments of the invention described herein 'rwithout departingfrom the scop'e ofthe invention as defined by the appended-claimsr- What we claim as new and desire to protect by Letters Patent of the United States of- America is:
1. Ina procession increasingthe-wet strength .properties of fibrous cellulosic material, the improvement which comprises thestep O r-treating saidw fibrous cellulosic material with a combination composed of water soluble guanidine-formalde'hyde resin and a hydrocolloid, the formaldehyde being present in said resin in the ratio of at least abouti2 mols per mol of guanidine, said resin being provided in amount of at least about 0.1% by weight based on the dry-weight of the fibrous cellulosic material, and said hydrocolloid being, provided in amount 6. In a process for producing paper which comprises forming an aqueous pulp of fibrous cellulosic material, removing-water from said pulp and forming said pulp into asheet, their'n'provementizwhich comprises providing in at least about 1.5 mols-per mol of guanidine, said resin being provided in amount of at least about 0.1% by Weight based on the dryweight of the fibrous cellulosic material,- and said hydrocolloid being provided in amount of-at leastabout-0.02% by weight based on the dry of at least about 0.02% by weight based onthe dry:weight 15 r Weight 05/1116 fibrous -Ce1l1110SiC at al.
of the fibrous cellulosic material.
2. The :process according to claim -1 in which the hydrocolloid is a'member selected from the group, consistingrof proteins, carbohydrates, wood hydrocolloids' and synthetic hydrocolloids.
3. The process according to claim -1 in which: the'hydro colloid is a member selected from-th egroup consisting; of gelatin, starch, lignin, polyacryl-amide-hydrolyte and sodium polymethylsiliconate.
4. The process according to 'clairn l in which the guanidine-forrnaldehyde resin is provided in amount with in the range of .from about 0.1% to'about 10% by;weight based on thedry weight of the fibrous cellulosic material.-
5. In a process for producing paperwhich comprises"- forming an aqueous pulp of fibrouscellulosic material; removing water from said pulp and forming said pulp into a sheet, the improvement which comprises providing in said pulp a combination oompose'd'of water solubleguanidine-formaldehyde resin and a hydrocolloid, theformaldehyde being present in said resin in the ratio ofatleast about 2 mols per mol of guanidine,- said resin being provided in amount of at least about 0.1% by weight based on the dryweight of the fibrous cellulosic material, and said hydrocolloid being provided in amount of at least about 0.02% by weight based on the dry weight ofthe fibrous cellulosic material.
7. A fibrous cellulosic material treated with a combination of guanidine-formaldehyde resin and a hydrocolloid, the formaldehyde being present in said resin in the ratio of at least about 2 mols of formaldehyde per mol of 2m guanidine, said-resin being present in amount of at least about 0.1%by weight based on the dry weight of the fibrous cellulosic material, and said hydrocolloid being present in amount of at-least about 0.02% by weight based on the dry weight of the fibrous cellulosic material.

Claims (1)

1. IN A PROCESS FOR INCREASING THE WET STRENGTH PROPERTIES OF FIBROUS CELLULOSIC MATERIAL, THE IMPROVEMENT WHICH COMPRISES THE STEP OF TREATING SAID FIBROUS CELLULOSIC MATERIAL WITH A COMBINATION COMPOSED OF WATER SOLUBLE GUANIDINE-FORMALDEHYDE RESIN AND A HYDROCOLLOID, THE FORMALDEHYDE BEING PRESENT IN SAID RESIN IN THE RATIO OF AT LEAST ABOUT 2 MOLS PER MOL OF GUANIDINE, SAID RESIN BEING PROVIDED IN AMOUNT OF AT LEAST ABOUT 0.1% BY WEIGHT BASED ON THE DRY WEIGHT OF THE FIBROUS CELLULOSIC MATERIAL, AND SAID HYDROCOLLOID BEING PROVIDED IN AMOUNT OF AT LEAST ABOUT 0.02% BY WEIGHT BASED ON THE DRY WEIGHT OF THE FIBROUS CELLULOSIC MATERIAL.
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Cited By (8)

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US3298853A (en) * 1963-06-03 1967-01-17 Miles Lab Water-insolubilizing starch-clay paper coatings with a reaction product of dialdehyde starch and a dicyandiamide formaldehyde condensation product
US3384622A (en) * 1965-05-11 1968-05-21 American Cyanamid Co Rapidly water-soluble guanidine-formaldehyde resin and process for the manufacture thereof
US3424650A (en) * 1965-11-05 1969-01-28 Nalco Chemical Co Method of improving dry strength of paper
US3428607A (en) * 1965-02-12 1969-02-18 Ciba Ltd Process for the preparation of finely divided,insoluble and infusible melamine-formaldehyde condensation products
FR2314297A1 (en) * 1975-06-12 1977-01-07 Borden Products Ltd HIGH DRY RESISTANCE PAPER DUE TO ADDITIVES EXERCISING A SYNERGIC ACTION AND ITS MANUFACTURING PROCESS
US4076581A (en) * 1976-01-16 1978-02-28 Scott Paper Company Method for increasing wet strength cure rate of paper
US4461858A (en) * 1980-05-16 1984-07-24 E. I. Du Pont De Nemours And Company Polyvinylalcohol/melamine-formaldehyde interaction products
US5108546A (en) * 1990-09-10 1992-04-28 The Dexter Corporation Bonded fibrous sheet material

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US2668808A (en) * 1951-12-13 1954-02-09 Arnold Hoffman & Co Inc Process of preparing guanidineformaldehyde condensation products
US2736749A (en) * 1952-06-10 1956-02-28 Arnold Hoffman & Co Inc Dye-fixing agents
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US2492702A (en) * 1938-07-08 1949-12-27 Gen Aniline & Film Corp Process of sizing paper and product
US2338602A (en) * 1939-12-04 1944-01-04 Reconstruction Finance Corp Fabrication of wet-strengthened papers
GB613622A (en) * 1945-09-15 1948-12-01 Resinous Prod & Chemical Co Method for production of wet-strength paper
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US2601671A (en) * 1946-10-23 1952-06-24 American Cyanamid Co Resin-impregnated leather board
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3298853A (en) * 1963-06-03 1967-01-17 Miles Lab Water-insolubilizing starch-clay paper coatings with a reaction product of dialdehyde starch and a dicyandiamide formaldehyde condensation product
US3428607A (en) * 1965-02-12 1969-02-18 Ciba Ltd Process for the preparation of finely divided,insoluble and infusible melamine-formaldehyde condensation products
US3384622A (en) * 1965-05-11 1968-05-21 American Cyanamid Co Rapidly water-soluble guanidine-formaldehyde resin and process for the manufacture thereof
US3424650A (en) * 1965-11-05 1969-01-28 Nalco Chemical Co Method of improving dry strength of paper
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US4076581A (en) * 1976-01-16 1978-02-28 Scott Paper Company Method for increasing wet strength cure rate of paper
US4461858A (en) * 1980-05-16 1984-07-24 E. I. Du Pont De Nemours And Company Polyvinylalcohol/melamine-formaldehyde interaction products
US5108546A (en) * 1990-09-10 1992-04-28 The Dexter Corporation Bonded fibrous sheet material

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