US2325302A - High-wet-strength paper - Google Patents
High-wet-strength paper Download PDFInfo
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- US2325302A US2325302A US238693A US23869338A US2325302A US 2325302 A US2325302 A US 2325302A US 238693 A US238693 A US 238693A US 23869338 A US23869338 A US 23869338A US 2325302 A US2325302 A US 2325302A
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- paper
- resin
- urea
- wet
- strength
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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
- D21H17/33—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
- D21H17/50—Acyclic compounds
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S215/00—Bottles and jars
- Y10S215/02—Coatings and laminations for making of bottle caps
Definitions
- This invention relates to the art of paper mak-- ing, and a principal object of the invention is to provide papers having a relatively high degree of wet-strength.
- This application is a continuation-in-part of my application Serial No. 91,963, filed July 22, 1936.
- Another object of the invention is to provide paper Whose wet-strength is materially increased without unduly modifying the normal desirable characteristics of the paper or such properties as water absorbency and softness required in certain classes of paper.
- Another and more specific object of the invention is to provide soft, absorbent papers, such as those employed'for towels and toilet tissues, that possess a relatively high degree of strength and resistance to surface disintegration while in the wet state.
- the present invention provides a means for modifying the cellulose structure constituting the bonding or cementation between the individual fibres so that it shall remain strong when the paper is wetted.
- the dry or partially dry web of paper is impregnated with a water solution containing a substance or substances capable under the proper heat and catalytic conditions of polymerizing to a waterinsoluble condition.
- a water solution containing a substance or substances capable under the proper heat and catalytic conditions of polymerizing to a waterinsoluble condition.
- the wetstrengthening agent may actually penetrate the cellulosic structure of the individual fibres, it is important that it exist initially as a true solution in water. After the penetration into the fibres the agent must be capable of polymerizing rapidly to the insoluble stat under relatively mild conditions of heat, e. g., under the conditions of normal drying of paper on a paper machine or paper treating machine. Materials fulfilling the above requirements are found among the substances capable of forming synthetic resins.
- the materials from which the final resin is formed should enter the cellulose structure in the form of a water solution, and for this condition to be fulfilled, the materials should be in the form of compounds of relatively low molecular weight and soluble in water.
- urea and formaldehyde such as urea and formaldehyde, ureaand hexamethylenetetramine, thiourea and formaldehyde, urea and acetaldehyde, and urea and butyraldehyde, the said aldehydes being saturated aliphatic aldehydes having from 1 to 4 carbon atoms.
- numerous other materials are potentially capable of affording the desired results, such, for example, as urea and furfural, phenol and formaldehyde, phenol and furfural, phenol and butyraldehyde, phenol and acetaldehyde, phenol and hexamethylenetetramine, and phthalic anhydride and glycerol.
- the materials which are potential agents I am aware that the impregnation of cellulosic materials with solutions more or less similar to the above has been the subject of previous inventions.
- urea and formaldehyde has been suggested for rendering regenerated c'ellulose (rayon) fabrics resistant to creasing.
- the polymerization or insolubilizmg reaction take place quickly and easily in order to permit the incorporation of the process as a step in the manufacture of paper.
- the polymerization reaction must be accelerated by the use of a catalyst.
- a catalyst With urea-formaldehyde, phenol-formaldehyde, and th ourea-formaldehyde the most suitable catalyst is an acid or acid salt.
- I may, for example, use a mineral acid such as sulphuric acid, hydrochloric acid, or phosphoric acid, or I may use an organic acid such as acetic acid or formic acid, or I may use an acid salt such as ammonium chloride, sodium bisulphate, aluminum sulphate or zinc chloride; or I may use a neutral salt wluch becomes acid under the heat conditions incidental to drying the impregnated sheet, for example, secondary ammonium phosphate, or ammonium sulphite.
- a mineral acid such as sulphuric acid, hydrochloric acid, or phosphoric acid
- I may use an organic acid such as acetic acid or formic acid
- I may use an acid salt such as ammonium chloride, sodium bisulphate, aluminum sulphate or zinc chloride
- I may use a neutral salt wluch becomes acid under the heat conditions incidental to drying the impregnated sheet, for example, secondary ammonium phosphate, or ammonium sulphite
- urea-formaldehyde for example, it is not difiicult to select a catalyst which will induce a rapid polymerization under the heat conditions incidental to the drying of paper since any material capable of producing a mild acid condition will serve. It is, however, more difflcult to select a catalyst which will give a relatively stable stock solution when mixed with urea-formaldehyde, and which need not be re-' moved from the finished sheet. Secondary ammonium phosphate has been found to fulfill these conditions most satisfactorily.
- urea and formaldehyde are particularly well suited for the practice of the invention in that, in an intermediate or partially reacted stage these materials are productive of a water-soluble solid.
- this watersoluble solid takes the form either of monomethylolurea or dimethylolurea, or a mixture of the two.
- Dimethylolurea has been found best suited to the requirements of the present invention, although it is sometimes desirable to employ a mixture of the two ureas.
- Dimethylolurea is available in the trade, and its use insures an introduction of the materials in exact proportions and materially facilitates the process as a whole. Further advantages in the use of dimethylolurea reside in the rapidity with which polymerization takes place and in the mild temperature and catalytic conditions necessary; in the absence of any tendency of the polymerized resin to decrease the absorbency of the paper; in the stability of the dimethylolurea solution; in cheapness of raw materials; in the fact that no residual color or odor is left in the treated paper; and in the further fact that there is no decomposition of the resin with age.
- paper is impregnated to saturation by any suitable means with a water solution of the following composition:
- the paper is then dried, preferably at a relatively low temperature, say below F., in order to insure against polymerization while the paper is in the wet or moist state, or until the water phase is reduced to that amount which is contained within the fibres.
- a relatively low temperature say below F.
- the paper web is heated to a temperature sufficient to convert the water-soluble compound into a substantially water-insoluble ureaformaldehyde resin, which resin is in a substantially cured condition. The extent of this heating subsequent to drying is not great. It has been found that the amount of heating received by a sheet of paper passing through the drier section of a paper machine in the normal papermaking process is sufficient to cause adequate polymerization.
- the relative proportions of the urea and formaldehyde may be stated, for example, as approximately 1 to 1; and if the materials are added to the paper in amount of about 2% of the weight of the latter, the substantial increase in, wet-strength is obtained without appreciable modification in other respects of the normal paper characteristics. 'It will be apparent that the physical properties of the finished sheet may be varied by using more or less of the resin-forming ingredients.
- dimethylolurea it may be prepared by any of the well known methods, but it has been found that the maximum wet-strength is obtained by using the following procedure; urea is dissolved in 37% formaldehyde solution (commercial formalin) in the proportion of parts by weight of urea to 4 parts by weight of HCHO or approximately two mols of HCHO to one mol of urea. Other proportions will produce wetstrength, but it has been found that a higher proportion of urea decreases the amount of wetstrength obtained and a greater proportion of formaldehyde increases the cost and gives residual formaldehyde which mustbe disposed of.
- formaldehyde solution commercial formalin
- Enough sodium carbonate or other alkali is added to the above solution to give a definitely alkaline reaction.
- About 0.05% NazCOs on the basis of urea-i-formaldehyde is a convenient amount.
- the solution is allowed to stand from 4 to 12 hours and isthen diluted to a suitable concentration with water. After addition of the catalyst, this solution is ready for use in the Wet-strength process.
- the solution so prepared is found superior to a mixture of uncombined urea and formaldehyde and to dimethylolurea prepared by heating.
- the acid catalysts which may be employed are such as those already listed above and the amount of these catalysts required is quite small. For example, using sulphuric acid, 0.05% acid in the impregnating solution gives the maximum wet-strength. More than 0.1% sulphuric acid has a destructive action on the fibre. In using aluminum sulphate approximately 0.1% gives the best results, and closely similar amounts are required for the other salts.
- a solution of this character may consist of a mild alkali such as sodium bicarbonate, di-sodium phosphate, sodium borate, or similar salts, in such strength as to neutralize the catalyst and at the same time leave the paper essentially neutral.
- a solution of 0.3% sodium bicarbonate applied in an amount of 20% of the weight of the dry paper is an effective neutralizer. The paper is again dried after this treatment and the resulting sheet constitutes the finished product.
- salts examples include triammonium phosphate, (NH4)3PO4, secondary ammonium phosphate, (NH4)2I-]PO4, and ammonium sulphite, (NI-10280:.
- the first two salts are converted by heat into the acidic monoammonium phosphate, while the third is converted toiammonium sulphate.
- the use of these catalysts has been found to be very convenient in practice.
- a sheet of dry paper for example paper toweling
- a solution consisting of the following materials:
- the moisture content of the sheet immediately after spraying should be about 25-30%. This would mean the application of about 1.0% ureaformaldehyde resin on the basis of the paper.
- the paper is then dried on steam-heated rotating cylindrical driers as normally used in the paper industry. It has been found that a drier temperature of 275 to 300 F. and a total time of contact between the paper and the driers of about 30 seconds gives very good results. Paper so treated would normally have a wet-strength of 35-50% of the dry-strength or 4-6 times that of the untreated paper. The dry-strength would be increased only slightly, say 10 to 15%.
- partially dried paper may be sprayed on a. papermaking machine.
- the paper at the point of spraying contains 40% water.
- the spraying solution would consist of the following:
- the amount of this solution applied would be 6% of the weight of the dry paper, and the moisture content of the sheet would be increased from 40% to 42%.
- the paper is then'dried in the normal way. With the use of the ammonium phosphate catalyst no neutralization step is required.
- the degree of wet-strength obtained is within certain limits a function of the amount of urea-formaldehyde used in proportion to the fibre treated. For example, with paper toweling the use of ureaformaldehyde in amount of 1% on the basis of fibre increases the wet-strength approximately four to five times. The use of 2% increases the wet-strength approximately six to seven times. In either case, the dry strength and other physical properties of the paper are substantially unchanged. The fact that there is substantially no change in the dry-strength of the paper is to be particularly noted, since this indicates that very little, if any, of the resin is acting as an additlonal interflbre cementing medium.
- the urea-formaldehyde resin when used under the conditions specified and in the proportions contemplated by the invention, is sufiiciently soluble to remain in solution until the liquid phase has been reduced by drying to that amount which is held essentially within the fibres themselves.
- fibres treated as above described are never water-repellent. If the resin is used in such large amounts, say in excess of 5% on basis of fibre weight, that considerable amount of condensation product exists between the fibres, absorbency or penetration of water into the interflbre spaces is impaired, but no apparent water-repellency, as such, exists.
- certain modifying ingredients may be used along with the urea-formaldehyde.
- protein matter e. g., soya bean protein, casein or gelatin inamounts of to 50% of the urea-formaldehyde has the effect of making the pape more resistant to exposure to water over long periods of time and at elevated temperatures.
- soya bean protein, casein or gelatin inamounts of to 50% of the urea-formaldehyde has the effect of making the pape more resistant to exposure to water over long periods of time and at elevated temperatures.
- a resin formed by the reaction of a urea and an aldehyde only is employed to distinguish the urea-aldehyde resin from a product in which a third material is one of the resin-forming ingredients with the urea and the aldehyde in the preparation of the resin.
- This expression in the claims includes the preparation of the resin from a urea and an aldehyde in the presence of a catalyst.
- a high-wet-strength paper containing from approximately .5 of 1% to 5% on the basis of the dry weight of the paper, of a resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition.
- a high-wet-strength paper containing from approximately .5 of 1% to 3% on the basis of the dry weight of the paper, of a resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition, said resincontaining paper having a marked increase in wet-strength and substantially the water-absorbency and softness of the same paper free of resin.
- a high-wet-strength paper containing approximately 2% on the basis of the dry weight of the paper, of a resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition.
- a high-wet-strength paper containing from approximately .5 of 1% to 5%, on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition.
- a high-wet-strength paper containing from approximately .5 of 1% to 3%, on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition, said resin-containing paper having a marked increase in wet-strength and substantially the water-absorbency and softness of the same paper free of resin.
- a high-wet-strength paper containing from approximately .5 of 1% to 5% on the basis of the dry weight of the paper, of a resin formed by reacting urea and formaldehyde only, said resin being in substantially cured condition.
- a high-wet-strength paper containing'from approximately .5 of 1% to 3%, on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting urea and formaldehyde only, said resin being in substantially cured condition, said resin-containing paper having a marked increase in wet-strength and substantially the water-absorbency and softness of the same paper free of resin.
- a high-wet-strength paper containing from approximately .5 of 1% to 5% on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting a urea and formaldehyde only, said resin being in substantially cured condition.
Description
Patented July 27, 1943 UNITED HIGH-WET-STRENGTH PAPER Kenneth W. Britt, Norwood, Pa., assignor to Scott Paper Company, Chester, Pa., a corporation of Pennsylvania No Drawing. Application November 3, 1938, Serial No. 238,693
8 Claims.
This invention relates to the art of paper mak-- ing, and a principal object of the invention is to provide papers having a relatively high degree of wet-strength. This application is a continuation-in-part of my application Serial No. 91,963, filed July 22, 1936.
Another object of the invention is to provide paper Whose wet-strength is materially increased without unduly modifying the normal desirable characteristics of the paper or such properties as water absorbency and softness required in certain classes of paper.
Another and more specific object of the invention is to provide soft, absorbent papers, such as those employed'for towels and toilet tissues, that possess a relatively high degree of strength and resistance to surface disintegration while in the wet state.
In the normal paper making process cellulosic fibres, i. e., fibres derived from various plant materials and consisting essentially but not entirely of cellulose, are deposited from suspension in water to produce an interfelted web. A considerable amount of adhesion or bonding between the individual fibres in contact with each other develops upon drying this web, and it is thi peculiar property of cellulose that accounts for the strength of normal papers.
It is thought that at the point of contact between two fibres in a dry sheet of paper there is a minute portion of the cellulose structure which may 'be considered to be held by the two fibres in common. In the normal paper this cellulose structure is hydrophilic, not in the sense of any of the material actually being soluble in water but in the sense of being capable of associating itself intimately with water and thus having its cohesive strength substantially reduced, so that the bonding, cementation, or adhesion between the cellulose fibres of conventional papers has had the disadvantage of losing its strength when wetted with water. Thus, most papers when wet have only a relatively small per cent., say to 10%, of the strength that they possess when dry;
The present invention provides a means for modifying the cellulose structure constituting the bonding or cementation between the individual fibres so that it shall remain strong when the paper is wetted.
In carrying out the invention, the dry or partially dry web of paper is impregnated with a water solution containing a substance or substances capable under the proper heat and catalytic conditions of polymerizing to a waterinsoluble condition. In order that the wetstrengthening agent may actually penetrate the cellulosic structure of the individual fibres, it is important that it exist initially as a true solution in water. After the penetration into the fibres the agent must be capable of polymerizing rapidly to the insoluble stat under relatively mild conditions of heat, e. g., under the conditions of normal drying of paper on a paper machine or paper treating machine. Materials fulfilling the above requirements are found among the substances capable of forming synthetic resins.
In proceeding in accordance with the invention, therefore, there are introduced into the cellulose structure resin-producing ingredients either in the unreacted, the unpolymerized, or the partially reacted state, and thereafter the reaction or a completion of the reaction between these ingredients is effected to produce the desired result. The materials from which the final resin is formed should enter the cellulose structure in the form of a water solution, and for this condition to be fulfilled, the materials should be in the form of compounds of relatively low molecular weight and soluble in water. These materials having penetrated the cellulose structure are caused to undergoa condensation or polymerization, or both, as a result of the appli-- cation of heat in the presence of a catalyst, and this reaction results in the formation within the cellulose structure of a water insoluble resin, the presence of which, particularly in that part of the cellulose structure where two fibres have been dried in contact with each other, has the result of rendering the cellulose bond substantially unaffected by water. Where the properties of absorbency and softness are required, it is essential that no large proportion of the resin shall exist between the fibres of the paper outside of the cellulose bonding structure, since excess resin has the ffect of increasing the stiffness of the sheet,
Several materials may be used in this process, such, for example, as urea and formaldehyde, ureaand hexamethylenetetramine, thiourea and formaldehyde, urea and acetaldehyde, and urea and butyraldehyde, the said aldehydes being saturated aliphatic aldehydes having from 1 to 4 carbon atoms. In addition, numerous other materials are potentially capable of affording the desired results, such, for example, as urea and furfural, phenol and formaldehyde, phenol and furfural, phenol and butyraldehyde, phenol and acetaldehyde, phenol and hexamethylenetetramine, and phthalic anhydride and glycerol. In general, the materials which are potential agents I am aware that the impregnation of cellulosic materials with solutions more or less similar to the above has been the subject of previous inventions. For example, urea and formaldehyde has been suggested for rendering regenerated c'ellulose (rayon) fabrics resistant to creasing. These processes, however, involve the use of such quantities of urea-formaldehyde that when applied to paper of the sort contemplated by this invention they destroy the essential physica1 properties of the paper. Further, a study of the effect of urea-formaldehyde on rayon fabrics would not suggest the very different function disclosed by this invention. Also, it has been suggested to use urea-formaldehyde to prevent the swelling" of cellulosic materials. Here again the application of the'previous invention in such a manner as to substantially reduce swelling destroys certain physical properties of paper which it is the purpose of thisinvention to preserve. Further, the use of urea-formadehyde as specified in this invention has no appreciable effect on the swelling characteristics of the erial. is an essential feature of this invention that the polymerization or insolubilizmg reaction take place quickly and easily in order to permit the incorporation of the process as a step in the manufacture of paper. In order to realize this the polymerization reaction must be accelerated by the use of a catalyst. With urea-formaldehyde, phenol-formaldehyde, and th ourea-formaldehyde the most suitable catalyst is an acid or acid salt. I may, for example, use a mineral acid such as sulphuric acid, hydrochloric acid, or phosphoric acid, or I may use an organic acid such as acetic acid or formic acid, or I may use an acid salt such as ammonium chloride, sodium bisulphate, aluminum sulphate or zinc chloride; or I may use a neutral salt wluch becomes acid under the heat conditions incidental to drying the impregnated sheet, for example, secondary ammonium phosphate, or ammonium sulphite.
With the use of urea-formaldehyde, for example, it is not difiicult to select a catalyst which will induce a rapid polymerization under the heat conditions incidental to the drying of paper since any material capable of producing a mild acid condition will serve. It is, however, more difflcult to select a catalyst which will givea relatively stable stock solution when mixed with urea-formaldehyde, and which need not be re-' moved from the finished sheet. Secondary ammonium phosphate has been found to fulfill these conditions most satisfactorily.
Of the various combinations of materials mentioned above, urea and formaldehyde are particularly well suited for the practice of the invention in that, in an intermediate or partially reacted stage these materials are productive of a water-soluble solid. Depending upon the proportions of formaldehyde and urea, this watersoluble solid takes the form either of monomethylolurea or dimethylolurea, or a mixture of the two. Dimethylolurea has been found best suited to the requirements of the present invention, although it is sometimes desirable to employ a mixture of the two ureas.
Dimethylolurea is available in the trade, and its use insures an introduction of the materials in exact proportions and materially facilitates the process as a whole. Further advantages in the use of dimethylolurea reside in the rapidity with which polymerization takes place and in the mild temperature and catalytic conditions necessary; in the absence of any tendency of the polymerized resin to decrease the absorbency of the paper; in the stability of the dimethylolurea solution; in cheapness of raw materials; in the fact that no residual color or odor is left in the treated paper; and in the further fact that there is no decomposition of the resin with age.
In a specific procedure by way of example, paper is impregnated to saturation by any suitable means with a water solution of the following composition:
Per cent by weight Dimethylolurea 1.0 Sulphuric acid 0.05
The paper is then dried, preferably at a relatively low temperature, say below F., in order to insure against polymerization while the paper is in the wet or moist state, or until the water phase is reduced to that amount which is contained within the fibres. A considerable degree of wet strength will result regardless of the method of drying, but the maximum of wet strength may only be obtained by initial low temperature evaporation. Subsequent to drying, the paper web is heated to a temperature sufficient to convert the water-soluble compound into a substantially water-insoluble ureaformaldehyde resin, which resin is in a substantially cured condition. The extent of this heating subsequent to drying is not great. It has been found that the amount of heating received by a sheet of paper passing through the drier section of a paper machine in the normal papermaking process is sufficient to cause adequate polymerization.
It is apparent that substantially the same results may be'obtained by employing a mixture of urea and formaldehyde rather than dimethylolurea, and in the case of some of the other resin-producing materials, it is necessary to keep the initial solution merely as a mixture in order to retain water solubility. A suitable catalyst may be incorporated in the mixtures in their unreacted state and substantially the same procedure followed as has been described above as to drying the treated sheet and subsequentlyraising the temperature of the sheet to a point effecting the resin-producing reaction. In such cases, it is desirable to employ the materials in amounts and proportions, readily determinable by those familiar with the art, to afford the desired result without leaving any excess of the materials in the paper sheet, either in the form of the completed resin or in their initial individual forms. The relative proportions of the urea and formaldehyde may be stated, for example, as approximately 1 to 1; and if the materials are added to the paper in amount of about 2% of the weight of the latter, the substantial increase in, wet-strength is obtained without appreciable modification in other respects of the normal paper characteristics. 'It will be apparent that the physical properties of the finished sheet may be varied by using more or less of the resin-forming ingredients.
If dimethylolurea is used it may be prepared by any of the well known methods, but it has been found that the maximum wet-strength is obtained by using the following procedure; urea is dissolved in 37% formaldehyde solution (commercial formalin) in the proportion of parts by weight of urea to 4 parts by weight of HCHO or approximately two mols of HCHO to one mol of urea. Other proportions will produce wetstrength, but it has been found that a higher proportion of urea decreases the amount of wetstrength obtained and a greater proportion of formaldehyde increases the cost and gives residual formaldehyde which mustbe disposed of. Enough sodium carbonate or other alkali is added to the above solution to give a definitely alkaline reaction. About 0.05% NazCOs on the basis of urea-i-formaldehyde is a convenient amount. The solution is allowed to stand from 4 to 12 hours and isthen diluted to a suitable concentration with water. After addition of the catalyst, this solution is ready for use in the Wet-strength process. The solution so prepared is found superior to a mixture of uncombined urea and formaldehyde and to dimethylolurea prepared by heating.
The acid catalysts which may be employed are such as those already listed above and the amount of these catalysts required is quite small. For example, using sulphuric acid, 0.05% acid in the impregnating solution gives the maximum wet-strength. More than 0.1% sulphuric acid has a destructive action on the fibre. In using aluminum sulphate approximately 0.1% gives the best results, and closely similar amounts are required for the other salts.
It is undesirable to leave unneutralized acidic catalyst in the finished paper, and the paper may, therefore, be treated after the application of the wet-strength process with a suitable alkaline solution. A solution of this character may consist of a mild alkali such as sodium bicarbonate, di-sodium phosphate, sodium borate, or similar salts, in such strength as to neutralize the catalyst and at the same time leave the paper essentially neutral. A solution of 0.3% sodium bicarbonate applied in an amount of 20% of the weight of the dry paper is an effective neutralizer. The paper is again dried after this treatment and the resulting sheet constitutes the finished product.
It is to be remembered that the conversion of dimethylolurea to the'insoluble resin takes place slowly in acid solution even at room temperature. For this reason a solution containing any of the above catalysts must be used immediately after the addition of the catalyst, and must be used as a relatively dilute solution. Further, the handling of acidic aqueous solutions presents serious engineering difliculties such as corrosion of machinery and equipment of all sorts. For these and other reasons it has been found more convenient to use as catalysts certain salts which in the initial state are neutral or slightly alkaline but which, upon exposure to the heat incident to drying the impregnated paper, develop a mild acid condition which causes the polymerization to take place. Examples of such salts are triammonium phosphate, (NH4)3PO4, secondary ammonium phosphate, (NH4)2I-]PO4, and ammonium sulphite, (NI-10280:. The first two salts are converted by heat into the acidic monoammonium phosphate, while the third is converted toiammonium sulphate. The use of these catalysts has been found to be very convenient in practice. The claims reciting the presence in the paper of an acid-polymerized resin include resins polymerized under acid conditions derived either by reason of the presence of an acid or acidic substance at the time of polymerization; thus, the claims include the use of catalysts which may be neutral or slightly alkaline but which upon exposure to heat develop a mild acidic condition which causes polymerization.
As a further practical example of the way in which the invention may be carried into-effect employing a catalyst of this type, a sheet of dry paper, for example paper toweling, is sprayed by any convenient means with a solution consisting of the following materials:
Per cent Dimethylolurea 3.0 Secondary ammonium phosphate 0.25
Remainder, water.
The moisture content of the sheet immediately after spraying should be about 25-30%. This would mean the application of about 1.0% ureaformaldehyde resin on the basis of the paper. The paper is then dried on steam-heated rotating cylindrical driers as normally used in the paper industry. It has been found that a drier temperature of 275 to 300 F. and a total time of contact between the paper and the driers of about 30 seconds gives very good results. Paper so treated would normally have a wet-strength of 35-50% of the dry-strength or 4-6 times that of the untreated paper. The dry-strength would be increased only slightly, say 10 to 15%.
As another example partially dried paper may be sprayed on a. papermaking machine. Suppose for example the paper at the point of spraying contains 40% water. Then the spraying solution would consist of the following:
Per cent Dimethylolurea 20 Secondary ammonium phosphate 1.5
The amount of this solution applied would be 6% of the weight of the dry paper, and the moisture content of the sheet would be increased from 40% to 42%. The paper is then'dried in the normal way. With the use of the ammonium phosphate catalyst no neutralization step is required.
The degree of wet-strength obtained, other things being the same, is within certain limits a function of the amount of urea-formaldehyde used in proportion to the fibre treated. For example, with paper toweling the use of ureaformaldehyde in amount of 1% on the basis of fibre increases the wet-strength approximately four to five times. The use of 2% increases the wet-strength approximately six to seven times. In either case, the dry strength and other physical properties of the paper are substantially unchanged. The fact that there is substantially no change in the dry-strength of the paper is to be particularly noted, since this indicates that very little, if any, of the resin is acting as an additlonal interflbre cementing medium. This is accounted for by the fact that the urea-formaldehyde resin, when used under the conditions specified and in the proportions contemplated by the invention, is sufiiciently soluble to remain in solution until the liquid phase has been reduced by drying to that amount which is held essentially within the fibres themselves.
Quantities of urea-formaldehyde less than .5%
compared with the great increase in wetstrength. Beyond approximately of resin, however, the rate of increase of wet-strength falls oil so rapidly that the advantage gained in this respect is not sumcient, where the quality I of softness in the product is required, to offset the disadvantage of the increasing hardness.
It is to be noted that fibres treated as above described are never water-repellent. If the resin is used in such large amounts, say in excess of 5% on basis of fibre weight, that considerable amount of condensation product exists between the fibres, absorbency or penetration of water into the interflbre spaces is impaired, but no apparent water-repellency, as such, exists.
In the application of the present invention certain modifying ingredients may be used along with the urea-formaldehyde. In particular, the use of protein matter, e. g., soya bean protein, casein or gelatin inamounts of to 50% of the urea-formaldehyde has the effect of making the pape more resistant to exposure to water over long periods of time and at elevated temperatures. In the foregoing description, the preparation of a resin formed by reacting a urea and an aldehyde is described, and the use of a catalyst in the preparation of the resin from the urea and the aldehyde is recommended. In the claims, the phrase a resin formed by the reaction of a urea and an aldehyde only is employed to distinguish the urea-aldehyde resin from a product in which a third material is one of the resin-forming ingredients with the urea and the aldehyde in the preparation of the resin. This expression in the claims, of course, includes the preparation of the resin from a urea and an aldehyde in the presence of a catalyst.
In previous proposals paper has been heavily filled with resins to an extent largely modifying the normal paper characteristics, but the distinctions between these prior products and the processes by which they are produced and those according to the present invention will be apparent from the foregoing description.
I claim:
1. A high-wet-strength paper containing from approximately .5 of 1% to 5% on the basis of the dry weight of the paper, of a resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition.
2. A high-wet-strength paper containing from approximately .5 of 1% to 3% on the basis of the dry weight of the paper, of a resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition, said resincontaining paper having a marked increase in wet-strength and substantially the water-absorbency and softness of the same paper free of resin.
3. A high-wet-strength paper containing approximately 2% on the basis of the dry weight of the paper, of a resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition.
4. A high-wet-strength paper containing from approximately .5 of 1% to 5%, on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition.
5. A high-wet-strength paper containing from approximately .5 of 1% to 3%, on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting a urea and an aldehyde only, said aldehyde being a saturated aliphatic aldehyde having from 1 to 4 carbon atoms and said resin being in substantially cured condition, said resin-containing paper having a marked increase in wet-strength and substantially the water-absorbency and softness of the same paper free of resin.
6. A high-wet-strength paper containing from approximately .5 of 1% to 5% on the basis of the dry weight of the paper, of a resin formed by reacting urea and formaldehyde only, said resin being in substantially cured condition.
'7. A high-wet-strength paper containing'from approximately .5 of 1% to 3%, on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting urea and formaldehyde only, said resin being in substantially cured condition, said resin-containing paper having a marked increase in wet-strength and substantially the water-absorbency and softness of the same paper free of resin.
8. A high-wet-strength paper containing from approximately .5 of 1% to 5% on the basis of the dry weight of the paper, of an acid-polymerized resin formed by reacting a urea and formaldehyde only, said resin being in substantially cured condition.
KENNETH W. BRI'I'I.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US238693A US2325302A (en) | 1938-11-03 | 1938-11-03 | High-wet-strength paper |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US238693A US2325302A (en) | 1938-11-03 | 1938-11-03 | High-wet-strength paper |
Publications (1)
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US2325302A true US2325302A (en) | 1943-07-27 |
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US238693A Expired - Lifetime US2325302A (en) | 1938-11-03 | 1938-11-03 | High-wet-strength paper |
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Cited By (60)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2422423A (en) * | 1944-11-18 | 1947-06-17 | Du Pont | Treatment of paper |
US2436329A (en) * | 1942-03-24 | 1948-02-17 | Westinghouse Electric Corp | Phenol formaldehyde resin-glycinin protein emulsion |
US2436328A (en) * | 1942-03-24 | 1948-02-17 | Westinghouse Electric Corp | Phenol formaldehyde resin-glycinin protein emulsion |
US2440802A (en) * | 1943-07-20 | 1948-05-04 | Western Electric Co | Method of making electrical conductors |
US2459364A (en) * | 1944-12-05 | 1949-01-18 | Dennison Mfg Co | Creped paper and method of making |
US2503267A (en) * | 1944-09-16 | 1950-04-11 | Ecusta Paper Corp | Cigarette paper |
US2514689A (en) * | 1946-11-07 | 1950-07-11 | Eastman Kodak Co | Sized paper |
US2540352A (en) * | 1945-10-27 | 1951-02-06 | Munising Paper Company | Method of making wet strength paper |
US2554639A (en) * | 1948-11-01 | 1951-05-29 | Crown Cork & Seal Co | Closures |
US2556898A (en) * | 1945-12-21 | 1951-06-12 | American Cyanamid Co | Urea-formaldehyde-sulphoxylate resin for high wet-strength paper |
US2558634A (en) * | 1949-02-09 | 1951-06-26 | Du Pont | Paper impregnating or saturating composition |
US2559234A (en) * | 1945-02-16 | 1951-07-03 | John T Stearn | Process of treating paper |
US2590846A (en) * | 1944-11-30 | 1952-04-01 | Richard H Cutting | Plaster base |
US2595935A (en) * | 1946-08-03 | 1952-05-06 | American Cyanamid Co | Wet strength paper and process for the production thereof |
US2596014A (en) * | 1947-03-05 | 1952-05-06 | American Cyanamid Co | Preparing wet strength paper using polyarylbiguanide-urea resin |
US2599943A (en) * | 1948-12-06 | 1952-06-10 | Fed Cartridge Corp | Process of making disintegratable top shot wads |
US2601598A (en) * | 1947-12-26 | 1952-06-24 | American Cyanamid Co | Application of dispersed materials to cellulosic fibers |
US2601597A (en) * | 1946-09-06 | 1952-06-24 | American Cyanamid Co | Application of dispersed coating materials to cellulosic fibers |
US2622979A (en) * | 1947-08-14 | 1952-12-23 | Hercules Powder Co Ltd | Modified synthetic resin and paper containing the same |
US2624686A (en) * | 1948-11-04 | 1953-01-06 | Olin Mathieson | High wet-strength paper and process of making |
US2642360A (en) * | 1946-12-27 | 1953-06-16 | Union Carbide & Carbon Corp | Manufacture of wet strength paper |
US2650163A (en) * | 1947-05-21 | 1953-08-25 | Hercules Powder Co Ltd | Butadiene-styrene sized paper and method |
US2653090A (en) * | 1948-05-13 | 1953-09-22 | Mosinee Paper Mills Company | Glass strand reinforced paper |
US2654671A (en) * | 1948-07-17 | 1953-10-06 | Hercules Powder Co Ltd | Paper product and process for its preparation |
US2656296A (en) * | 1951-06-05 | 1953-10-20 | Paper Patents Co | Process of manufacturing fibrous sheet covered plywood |
US2657132A (en) * | 1947-03-05 | 1953-10-27 | American Cyanamid Co | Manufacturing wet strength paper containing cationic urea-formaldehyde resin |
US2658828A (en) * | 1948-09-15 | 1953-11-10 | Chemloch Corp | Process of combining synthetic resins and other materials with cellulose |
US2660215A (en) * | 1950-09-22 | 1953-11-24 | Gen Electric | Electrical insulating material |
US2664964A (en) * | 1947-07-16 | 1954-01-05 | Asplund Arne Johan Arthur | Fibrous filter sheet for gases |
US2676898A (en) * | 1950-07-22 | 1954-04-27 | Owens Corning Fiberglass Corp | Method of treating glass fiber bats with resin and product |
US2680682A (en) * | 1950-01-26 | 1954-06-08 | Allied Chem & Dye Corp | Paper of improved wet strength |
US2680995A (en) * | 1950-12-01 | 1954-06-15 | Stimson Lumber Company | Method of making hardboard |
US2683087A (en) * | 1948-02-10 | 1954-07-06 | American Cyanamid Co | Absorbent cellulosic products |
US2683089A (en) * | 1952-06-10 | 1954-07-06 | American Cyanamid Co | Bibulous sheet |
US2683088A (en) * | 1952-06-10 | 1954-07-06 | American Cyanamid Co | Soft bibulous sheet |
US2683400A (en) * | 1948-06-08 | 1954-07-13 | British Fibrak Separator Compa | Method of making acid resisting, microporous material |
US2685508A (en) * | 1950-12-01 | 1954-08-03 | Eastman Kodak Co | High wet strength paper and its preparation |
US2690100A (en) * | 1950-06-24 | 1954-09-28 | Armstrong Cork Co | Method of producing fire-resistant inorganic fiber insulation |
US2694633A (en) * | 1950-02-23 | 1954-11-16 | Talbott Dev Associates | Affixing organic and inorganic additaments to cellulosic materials |
US2698787A (en) * | 1951-12-17 | 1955-01-04 | American Cyanamid Co | Urea-formaldehyde resins for wet strength paper and their use |
US2711961A (en) * | 1950-04-07 | 1955-06-28 | Du Pont | Making paper using a modified ureaformaldehyde resin |
US2713539A (en) * | 1951-02-14 | 1955-07-19 | Eastman Kodak Co | Manufacture of high wet strength paper |
US2721504A (en) * | 1950-07-14 | 1955-10-25 | Statens Skogsind Ab | Process for impregnating fibre materials |
US2721505A (en) * | 1950-12-08 | 1955-10-25 | Statens Skogsind Ab | Process of spray coating a web and heating the coated surface |
US2723195A (en) * | 1950-07-29 | 1955-11-08 | Monsanto Chemicals | Paper products and processes |
US2757086A (en) * | 1950-08-19 | 1956-07-31 | Brown Co | Method of wet-strengthening paper with high molecular weight ureaformaldehyde resins |
US2764483A (en) * | 1951-11-06 | 1956-09-25 | Du Pont | Process for sizing paper |
US2772969A (en) * | 1951-04-18 | 1956-12-04 | American Cyanamid Co | Sizing of paper with fatty acid polyalkylenepolyamine compositions |
US2794737A (en) * | 1954-06-10 | 1957-06-04 | American Cyanamid Co | Paper sized with a condensation product of a fatty amine and hexahydro-1, 3, 5-triacrylyl-s-triazine |
US2797206A (en) * | 1952-12-02 | 1957-06-25 | American Cyanamid Co | Stable melamine-urea resin syrup |
US2806811A (en) * | 1954-12-31 | 1957-09-17 | United States Gypsum Co | Paper-covered gypsum board |
US2822553A (en) * | 1952-11-26 | 1958-02-11 | Kathryn M Florentine | Mats |
US2905585A (en) * | 1954-09-30 | 1959-09-22 | Du Pont | Self-bonded paper |
US2926117A (en) * | 1953-05-18 | 1960-02-23 | Gen Mills Inc | Paper product containing anionic polyamide resin suspensoid |
US3218119A (en) * | 1962-02-02 | 1965-11-16 | American Cyanamid Co | Method of applying cyclic urea resins to cellulosic textile materials |
US3402068A (en) * | 1964-11-12 | 1968-09-17 | Owens Illinois Inc | Method of improving wet strength properties of paperboard |
US4297311A (en) * | 1978-12-07 | 1981-10-27 | Conwed Corporation | Method of manufacturing improved mineral board |
US20180105987A1 (en) * | 2016-02-29 | 2018-04-19 | Kemira Oyj | Softener composition |
RU2696382C1 (en) * | 2016-02-16 | 2019-08-01 | Кемира Ойй | Paper production method |
US10435843B2 (en) * | 2016-02-16 | 2019-10-08 | Kemira Oyj | Method for producing paper |
-
1938
- 1938-11-03 US US238693A patent/US2325302A/en not_active Expired - Lifetime
Cited By (63)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2436329A (en) * | 1942-03-24 | 1948-02-17 | Westinghouse Electric Corp | Phenol formaldehyde resin-glycinin protein emulsion |
US2436328A (en) * | 1942-03-24 | 1948-02-17 | Westinghouse Electric Corp | Phenol formaldehyde resin-glycinin protein emulsion |
US2440802A (en) * | 1943-07-20 | 1948-05-04 | Western Electric Co | Method of making electrical conductors |
US2503267A (en) * | 1944-09-16 | 1950-04-11 | Ecusta Paper Corp | Cigarette paper |
US2422423A (en) * | 1944-11-18 | 1947-06-17 | Du Pont | Treatment of paper |
US2590846A (en) * | 1944-11-30 | 1952-04-01 | Richard H Cutting | Plaster base |
US2459364A (en) * | 1944-12-05 | 1949-01-18 | Dennison Mfg Co | Creped paper and method of making |
US2559234A (en) * | 1945-02-16 | 1951-07-03 | John T Stearn | Process of treating paper |
US2540352A (en) * | 1945-10-27 | 1951-02-06 | Munising Paper Company | Method of making wet strength paper |
US2556898A (en) * | 1945-12-21 | 1951-06-12 | American Cyanamid Co | Urea-formaldehyde-sulphoxylate resin for high wet-strength paper |
US2595935A (en) * | 1946-08-03 | 1952-05-06 | American Cyanamid Co | Wet strength paper and process for the production thereof |
US2601597A (en) * | 1946-09-06 | 1952-06-24 | American Cyanamid Co | Application of dispersed coating materials to cellulosic fibers |
US2514689A (en) * | 1946-11-07 | 1950-07-11 | Eastman Kodak Co | Sized paper |
US2642360A (en) * | 1946-12-27 | 1953-06-16 | Union Carbide & Carbon Corp | Manufacture of wet strength paper |
US2596014A (en) * | 1947-03-05 | 1952-05-06 | American Cyanamid Co | Preparing wet strength paper using polyarylbiguanide-urea resin |
US2657132A (en) * | 1947-03-05 | 1953-10-27 | American Cyanamid Co | Manufacturing wet strength paper containing cationic urea-formaldehyde resin |
US2650163A (en) * | 1947-05-21 | 1953-08-25 | Hercules Powder Co Ltd | Butadiene-styrene sized paper and method |
US2664964A (en) * | 1947-07-16 | 1954-01-05 | Asplund Arne Johan Arthur | Fibrous filter sheet for gases |
US2622979A (en) * | 1947-08-14 | 1952-12-23 | Hercules Powder Co Ltd | Modified synthetic resin and paper containing the same |
US2601598A (en) * | 1947-12-26 | 1952-06-24 | American Cyanamid Co | Application of dispersed materials to cellulosic fibers |
US2683087A (en) * | 1948-02-10 | 1954-07-06 | American Cyanamid Co | Absorbent cellulosic products |
US2653090A (en) * | 1948-05-13 | 1953-09-22 | Mosinee Paper Mills Company | Glass strand reinforced paper |
US2683400A (en) * | 1948-06-08 | 1954-07-13 | British Fibrak Separator Compa | Method of making acid resisting, microporous material |
US2654671A (en) * | 1948-07-17 | 1953-10-06 | Hercules Powder Co Ltd | Paper product and process for its preparation |
US2658828A (en) * | 1948-09-15 | 1953-11-10 | Chemloch Corp | Process of combining synthetic resins and other materials with cellulose |
US2554639A (en) * | 1948-11-01 | 1951-05-29 | Crown Cork & Seal Co | Closures |
US2624686A (en) * | 1948-11-04 | 1953-01-06 | Olin Mathieson | High wet-strength paper and process of making |
US2599943A (en) * | 1948-12-06 | 1952-06-10 | Fed Cartridge Corp | Process of making disintegratable top shot wads |
US2558634A (en) * | 1949-02-09 | 1951-06-26 | Du Pont | Paper impregnating or saturating composition |
US2680682A (en) * | 1950-01-26 | 1954-06-08 | Allied Chem & Dye Corp | Paper of improved wet strength |
US2694633A (en) * | 1950-02-23 | 1954-11-16 | Talbott Dev Associates | Affixing organic and inorganic additaments to cellulosic materials |
US2711961A (en) * | 1950-04-07 | 1955-06-28 | Du Pont | Making paper using a modified ureaformaldehyde resin |
US2690100A (en) * | 1950-06-24 | 1954-09-28 | Armstrong Cork Co | Method of producing fire-resistant inorganic fiber insulation |
US2721504A (en) * | 1950-07-14 | 1955-10-25 | Statens Skogsind Ab | Process for impregnating fibre materials |
US2676898A (en) * | 1950-07-22 | 1954-04-27 | Owens Corning Fiberglass Corp | Method of treating glass fiber bats with resin and product |
US2723195A (en) * | 1950-07-29 | 1955-11-08 | Monsanto Chemicals | Paper products and processes |
US2757086A (en) * | 1950-08-19 | 1956-07-31 | Brown Co | Method of wet-strengthening paper with high molecular weight ureaformaldehyde resins |
US2660215A (en) * | 1950-09-22 | 1953-11-24 | Gen Electric | Electrical insulating material |
US2680995A (en) * | 1950-12-01 | 1954-06-15 | Stimson Lumber Company | Method of making hardboard |
US2685508A (en) * | 1950-12-01 | 1954-08-03 | Eastman Kodak Co | High wet strength paper and its preparation |
US2721505A (en) * | 1950-12-08 | 1955-10-25 | Statens Skogsind Ab | Process of spray coating a web and heating the coated surface |
US2713539A (en) * | 1951-02-14 | 1955-07-19 | Eastman Kodak Co | Manufacture of high wet strength paper |
US2772969A (en) * | 1951-04-18 | 1956-12-04 | American Cyanamid Co | Sizing of paper with fatty acid polyalkylenepolyamine compositions |
US2656296A (en) * | 1951-06-05 | 1953-10-20 | Paper Patents Co | Process of manufacturing fibrous sheet covered plywood |
US2764483A (en) * | 1951-11-06 | 1956-09-25 | Du Pont | Process for sizing paper |
US2698787A (en) * | 1951-12-17 | 1955-01-04 | American Cyanamid Co | Urea-formaldehyde resins for wet strength paper and their use |
US2683088A (en) * | 1952-06-10 | 1954-07-06 | American Cyanamid Co | Soft bibulous sheet |
US2683089A (en) * | 1952-06-10 | 1954-07-06 | American Cyanamid Co | Bibulous sheet |
US2822553A (en) * | 1952-11-26 | 1958-02-11 | Kathryn M Florentine | Mats |
US2797206A (en) * | 1952-12-02 | 1957-06-25 | American Cyanamid Co | Stable melamine-urea resin syrup |
US2926117A (en) * | 1953-05-18 | 1960-02-23 | Gen Mills Inc | Paper product containing anionic polyamide resin suspensoid |
US2794737A (en) * | 1954-06-10 | 1957-06-04 | American Cyanamid Co | Paper sized with a condensation product of a fatty amine and hexahydro-1, 3, 5-triacrylyl-s-triazine |
US2905585A (en) * | 1954-09-30 | 1959-09-22 | Du Pont | Self-bonded paper |
US2806811A (en) * | 1954-12-31 | 1957-09-17 | United States Gypsum Co | Paper-covered gypsum board |
US3218119A (en) * | 1962-02-02 | 1965-11-16 | American Cyanamid Co | Method of applying cyclic urea resins to cellulosic textile materials |
US3402068A (en) * | 1964-11-12 | 1968-09-17 | Owens Illinois Inc | Method of improving wet strength properties of paperboard |
US4297311A (en) * | 1978-12-07 | 1981-10-27 | Conwed Corporation | Method of manufacturing improved mineral board |
RU2696382C1 (en) * | 2016-02-16 | 2019-08-01 | Кемира Ойй | Paper production method |
US10435843B2 (en) * | 2016-02-16 | 2019-10-08 | Kemira Oyj | Method for producing paper |
US10458068B2 (en) * | 2016-02-16 | 2019-10-29 | Kemira Oyj | Method for producing paper |
US20180105987A1 (en) * | 2016-02-29 | 2018-04-19 | Kemira Oyj | Softener composition |
US10570567B2 (en) * | 2016-02-29 | 2020-02-25 | Kemira Oyj | Softener composition |
US11492760B2 (en) | 2016-02-29 | 2022-11-08 | Kemira Oyj | Softener composition |
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