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US2116544A - Method of enhancing the wetstrength of papers - Google Patents

Method of enhancing the wetstrength of papers Download PDF

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US2116544A
US2116544A US94157A US9415736A US2116544A US 2116544 A US2116544 A US 2116544A US 94157 A US94157 A US 94157A US 9415736 A US9415736 A US 9415736A US 2116544 A US2116544 A US 2116544A
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paper
wet
strength
sheet
binder
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US94157A
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Milton O Schur
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Brown Co
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H25/00After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/04Physical treatment, e.g. heating, irradiating
    • D21H25/06Physical treatment, e.g. heating, irradiating of impregnated or coated paper

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  • This invention relates to a method of enhancing the wet-strength of various kinds of papers, including substantially waterleaf papers and papers impregnated with colloidal binders of the nature of glue, casein, viscose, etc., which are introduced into the paper as aqueous solutions or suspensions and which, upon drying of the paper, are more or less irreversibly set to impart waterresistivity or high wet-strength to the paper.
  • vI may impregnate a waterleaf paper sheet of any suitable basis weight and fiber composition with a glue solution containing about 3% glue, based on solution, and about 2% formalde- 5 hyde, based on glue.
  • the sheet may be squeezed upon emergence from an impregnating bath of such glue solution, as by squeeze rolls, so that it retains about its own weight of the impregnating solution, whereupon it may be air-dried, say, at 70 to 100 F.
  • a sheet of kraft pulp pa- 5 per of 47 pounds basis weight was thus impregnated and dried as usual, it was found to have a bursting strength (Mullen) of 12 pounds per square inch after a thorough soaking through with water effected by its submergence in a water 10 bath for one-half hour.
  • a oneminute heat treatment performed on a sheet traveling at a speed of 200 to 400 feet per minute obviously requires a heating surface 200 to 400 feet long, whereas, on the other hand, a one-- second heat treatment reduces the length of the heating surface to 1/60th, that is, to only 3.3 to 6.7 feet. It is thus understandable why I prefer, especially in the case of high speed paper production, to "conduct the heat treatment at about 475 to 500 R, which represent a temperature to which most papers can be exposed momentarily without being. materially injured, and to correlate such temperature with an area of heating surface and a paper speed corresponding roughly to about a one-second heating period. In some instances, I may go to an elevated temperature as low as 400 F. or to an elevated temperature as high as 650 F., depending upon such factors as composition of paper, surface texture, basis weight, etc.
  • strips one-half inch in width were pulled apart a few seconds after having been streaked transversely with a camel-hair brush wet with water.
  • test strips become wet throughby the time the tensile load is applied thereto.
  • the short, high temperature heattreatment of my invention may be advantageously applied to various binder-impregnated papers whose binder depends upon dehydration to render it relatively strong when rewet.
  • papers impregnated with viscose solutions or suspensions and other aqueous binders, besides albuminous binders, appearing as wetstre'ngthening agents in paper may be made to exert a much greater wet-strengthening effect on the paper by such heat treatment even after the paper containing such binder has already been dried thoroughly, as ordinarily.
  • the surprising enhancement in wet-strength of the paper to be gained by my invention varies with the different binders.
  • my invention may be advantageously appliedno matter at what stage of paper-making the binder is infused into the paper sheet.
  • the glue, etc. may be introduced into the bulk pulp or fiber preparatory to its sheeting on the paper making machine; or such binders may be applied, as by spraying, to the wet or freshly -formed paper web before it reaches the dry end of the papermaking machine, for instance, in advance of the last press rolls.
  • thesubstantially dry, absorbent waterleaf paper sheet as it issues progressively from the dry end of the paper-mat ing machine may be passed progressively through a bath of the binder solution, excess solution removed from the sheet immediately upon its emergence from .the bath, as by squeeze rolls or scraper blades, whereupon the sheet may be redried to completion and finally exposed to a temperature upwards of about 300 for less than temperature of the'drum, the extent to which the drum is wrapped by the paper sheet, and the speed of the sheet may be controlled to yield the best results according to the nature of the hinder, the wet-strength desired in the finished paper product, and other circumstances of manufacture.
  • interfelted fibrous sheet material as covering carded webs felts, and papers, as all such fibrous sheet material is characterized by a more or less interfelted fibrous structure or texture.
  • the resulting papers might be of such high binder content as to be "sized or water-repellent or, in the case of viscose oralbuminous binders, such as glue and casein, be of such controlled binder content as to be water-absorbing and hence adapted for such uses as toweling, handkerchiefs, diaper linings, etc. It is obvious that the paper might be composed of various fibers or fiber mixtures,
  • the paper base might be formed with various degrees of absorbency, depending upon the use to which the final paper product is to be put. Indeed, the paper mightcontain non-cellulosic fibers such as wool and asbestos. Should my invention be applied to papers comprising esssentially only mineral fibers, such as asbestos, it becomes possible to heat the binder-impregnated paper at temperatures higher than 050 F. and for a. time longer g 2,110,544 than mere seconds by reason of the incombustibility of such fiber. In-such latter case, the limit in temperature and time of final heat treatment is essentially that at which the binder is injured or decomposed by heat.
  • I may start with refined wood pulp (Duracel) prepared by exposing kraft pulp to the refining action of comparatively strong alkaline liquor, for instance, so-calied white liquor, at about room or slightly elevated temperature until the pulp has acquired an alpha cellulose content of about 90 to 92%.
  • refined pulp in either unbleached orbleached condition is put into substantiallyuniform aqueous suspension preparatory to the papermaking operation while preserving its fiber length'as much as is compatible with the realization of the desired substantially uniformly tax-- tured waterleaf paper sheet therefrom.
  • the highly absorptive waterleaf paper sheet thus formed from such pulp is impregnated with a glue solution containing about 3% to 4% glue solids and a small amount of formaldehyde, squeezed to a glue content of about 3%, based on the dry weight of paper, air-dried at about room temperature, and finally brought into momentary contact with an intensely heated surface, as hereinbefore described.
  • the resulting paper product is characterized by its unique combination of remarkably high wet-strength and very high dry tear-resistance.
  • such a paper product is not only'similar to vegetable parchment in its high wet-strength and wet scuff-resistance but far surpasses ordinary vegetable parchment in its toughness or dry tearresistance. Because of the comparatively low glue content of such a paper product, it retains to a very large degree the flexibility of its waterleaf paper base as opposed to the comparatively stiff or brittle paper product produced when a similar paper base is impregnated to much higher glue content with a view toward giving it the high wet-strength of the paper product hereof simply by the usual passage over steam-heated drier drums of the papermaking or impregnating machine.
  • the high dry tear-resistance of the paper product hereof is a reflection of the preservation of high average fiber length and fiber flexibility in the pulp entering into its waterleaf paper base; and the glue impregnant brought to the desired high degree of irreversibility by the intense heat treatment hereof is relied upon herein for the purpose of binding together the fibers and developing in the paper the wet-strength ordinarily sought to be gained by parchmentizing the fibers and thus sacrificing verysignificantiy the tear-resistance in the paper product.
  • the invention hereof may be applied advantageously to waterleaf papers, that is, papers whose fabrication is carried out without the addition of binder to the paper-making stock at any stage of papermaking.
  • waterleaf papers that is, papers whose fabrication is carried out without the addition of binder to the paper-making stock at any stage of papermaking.
  • I mean a paper fabricated in the complete absenceof binder or sizingingradient or containing binder or sizing ingredient of such type or in such small amount that when made as heretofore its wet-strength is markedly lower than the percentage ratios just expressed; andI'do not mean to include by such quoted expression papers which have received a special chemical hydrating treatment, such as parchmentization.
  • the hot-shot" treatment may in the case of such substantially waterleaf paper involve subjecting such paper, after it has been dried in the usual way, to a one-second heating on each face by progressively passing the paper sheet as it is coming from the papermaking machine in contact with a surface heated to about 450 to 500 F.
  • the wet-strength (tensilestrength of a strip wide) of a waterleaf sheet of kraft towellng was increased from an initial value of 0.64% to 1.0#; of a waterleaf sheet com posed of 50% kraft and 50% groundwood from an initial value of 0.6# to 1.2#; of a waterleaf sheet composed of refined wood pulp and intended for nitrating purpose from an initial value of 0.3# to 1.0#.
  • Results of a similar order were obtained with various other papers, for instance, papers made from Duracel pulp, sulphite pulp, and cookedmanila pulp. I shall now give in tabular form various characteristics of particular kinds of paper before and after a hot-shot treatment as above described.
  • the paper toweling When dried in the usual way, the paper toweling had a wet-tensile-strength of 0.6#, but when subjected after drying to contact on each of its faces for one second with a surface at about 450 to 500 F., the wet-strength of the paper toweling was increased to 2.5#. The resulting paper toweling was very absorbent and was not embrittled to any serious extent by the momentary heating. A similar improvement in the quality paper both in waterleaf and tub-sized condition before and after the hot-shot treatment above described.
  • the present invention thus makes possible among.
  • the finished waterleaf paper products hereof have, as already indicated, a Mullen wetstrength of more than about 8% of the dry 'Mullen strength and a wet tensile strength of morethan about 12% of the dry tensile strength.
  • the papers sized with rosin and heat-treated as hereinbefore described have a wet Mullen strength or wet tensile strength higher than about 25% of the corresponding dry tests; and such highwet-strength is inherent in the heat-treated paper base itself for the sizing agent in the heattreated paper product having such high wet!
  • the strength may be one for instance, rosin size, that has but little or no wet strength itself on long soaking of the paper in water and that hence imparts very little or no wet-strength to the paper.
  • the function of the sizing agent itself may be simply and essentially cose, casein, etc., and to sized papers whose size content does not contribute significantly to the high wet-strength of the finished paper product hereof, it appears likely that in the case of all of these papers there is an incipient' caramelization or searing of the fibers and/or of the colloidal matter present in the paper under the high temperature heating treatment hereof and that such action is accompanied-by the-formation of wet-strengthening reaction products in the paper base; or it is possible that wet-strengthening reaction products arise in the paper baseas-a result of some oxidation of the fibers and/or of the colloidal matter under the high temperature heating treatment hereof.
  • a method of producing. a. paper product of high wet-strength which comprises exposing a predried' paper sheet containing,.if at all, only a very small amount of binder to temperatures upwards. of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet while markedly increasing its wetstrength.
  • a method of producing a paper product'of' high wet-strength as a dry paper sheet is being fabricated progressively at high speed, "which comprises progressively bringing the dried sheet into only momentary contact with a surface heated to about 400 to 650 F.
  • a method of producing substantially waterleaf paper ofliigh wet-strength which comprises exposing a predried'sheet of the waterleaf paper to temperatures upwards of about 300 F. for such alimited period of time as to avoid sensible burning of or injury to such sheet while markedly increasing its Wet-strength.
  • a method of producing sized paper of high wet- -strength which comprises exposing a predried sheet of sized paper containing only a very small amount of size to temperatures upwards of about 300 F, for such a limited period of time asto avoid sensible burningof or injury to such sheet while markedly increasing its wet-strength. 5.
  • a method involving the impregnation of fibrous sheet material with aqueous binder composition whose binder content tends to set irreversibly-upon the drying of such sheet material that step which comprises exposing the dried impregnated sheet material containing only a very small amount of the binder to temperatures upwards of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet material while markedly increasing its wet-strength.
  • step 6 which comprises exposing the dried impregnated sheet material containing only a very small amount of such binder to temperatures upwards of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet material while markedly increas-- ing its wet-strength.
  • step 7 which comprises exposing the dried impregnated sheet material containing only a very small amount of the binder to temperatures upwards of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet material while markedly increasing its wet-strength.

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y 1938- M. o. SCHUR 2,116,544
METHOD OF ENHANCING THE WET STRENGTH OF PAPERS Filed Aug. 4 1936 Patented May 10, 1938 METHOD OF ENHANCING THE WET STRENGTH OF PAPERS Milton 0. Schur, Berlin, N. H., assignor to Brown Company, Berlin, N. H., a corporation of Maine Application August 4,1936, Serial No. 94,157
30 Claims. (Cl. 91-70) v This invention relates to a method of enhancing the wet-strength of various kinds of papers, including substantially waterleaf papers and papers impregnated with colloidal binders of the nature of glue, casein, viscose, etc., which are introduced into the paper as aqueous solutions or suspensions and which, upon drying of the paper, are more or less irreversibly set to impart waterresistivity or high wet-strength to the paper.
I have discovered that the water-resistivity or wet-strength of substantially waterleaf papers and papers impregnated with binders of the foregoing character may be enhanced to an amazing degree by the application of heat to the dry paper,
- and advantageously by the momentary applicadrier drums at temperatures of about 212 to 265 F. While various temperatures of heating upwards of about 300 F. may be employed according to my process in the heat-treatment of the predried, substantially waterleaf or binder-impregnated paper for the purpose of enhancing gogreatly its water-resistivity or wet-strength, I have found it in many instances preferable to work within a temperature range of about 400 to 650 F., for instance, to expose the dry paper to a temperature of about 475 to 500 F.,'as at such temperature it is possible to develop practically instantly a phenomenal increase in the wetstrength of the paper without injuring it and to do so inexpensively with a comparatively small heating surface while the paper is traveling continuously and at high speed, for instance, from v the dry end of a papermaking or impregnating machine. I
I shall now give instances of the application of my invention to demonstrate the remarkable and '45 advantageous results that can be realized thereby. In one case, my aim was to produce a paper of maximum wet-strength such as is of value in wrapping wet vegetables, such as lettuce and celery, or lining the crates in which such vegetables 50 in iced condition are packed and shipped. To this end, vI may impregnate a waterleaf paper sheet of any suitable basis weight and fiber composition with a glue solution containing about 3% glue, based on solution, and about 2% formalde- 5 hyde, based on glue. The sheet may be squeezed upon emergence from an impregnating bath of such glue solution, as by squeeze rolls, so that it retains about its own weight of the impregnating solution, whereupon it may be air-dried, say, at 70 to 100 F. When a sheet of kraft pulp pa- 5 per of 47 pounds basis weight was thus impregnated and dried as usual, it was found to have a bursting strength (Mullen) of 12 pounds per square inch after a thorough soaking through with water effected by its submergence in a water 10 bath for one-half hour. When an impregnated and dried sheet of similar character was, according to the instant invention, exposed for roughly one second to a temperature of about 475 to 500 F., its wet-strength, that is, bursting strength 15 after similar water-submergence, was 35 pounds per square inch. This remarkable increase in the wet-strength of the paper sheet by momentary intense heating was had with practicallyno burning or other sensible injury thereof. The heating 20 of the paper sheet for two seconds at such temperature increased its wet-strength to 39 pounds per square inch without significant burning of the fiber, but heating for a longer period did not enhance the wet strength of the paper materially 25 and the paper became noticeably embrittled. When the paper was exposed to a temperature of 435 F., it was found possible to increase its wetstrengthmarkedly by extending the time of its onds. An improvement may also be realized by exposing the paper to a temperature of 350 F.
for about 1 to 2 minutes.
As already indicated, it is preferable in many cases to expose the paper to maximum safe ele- 35 vated temperature for a very short time. In this connection, it is to be borne in mind that heating of arapidly moving paper sheet, for instance, a sheet traveling continuously at 200 to 400 feet per minute from the dry end of a paper-making or W impregnating machine, requires extensive heat-. ing surface and that the provision of such heating surface and its maintenance at temperatures upwards of 300 F. is prohibitively costly. A oneminute heat treatment performed on a sheet traveling at a speed of 200 to 400 feet per minute obviously requires a heating surface 200 to 400 feet long, whereas, on the other hand, a one-- second heat treatment reduces the length of the heating surface to 1/60th, that is, to only 3.3 to 6.7 feet. It is thus understandable why I prefer, especially in the case of high speed paper production, to "conduct the heat treatment at about 475 to 500 R, which represent a temperature to which most papers can be exposed momentarily without being. materially injured, and to correlate such temperature with an area of heating surface and a paper speed corresponding roughly to about a one-second heating period. In some instances, I may go to an elevated temperature as low as 400 F. or to an elevated temperature as high as 650 F., depending upon such factors as composition of paper, surface texture, basis weight, etc.
Another example involving the use of my invention was centered about the production of paper toweling possessed of good absorbency as well as high wet-strength. In such case, an absorbent, waterleaf paper sheet of kraft pulp having a basis weight of 37 pounds was impregnated with a 2% aqueous solution of ammoniated casein, squeezed to a content of impregnating solution about equal to the dryweight of paper, and dried on the usual steam-heated drums at 240- F. The wet-tensile-strength of a one-half inch width strip of the resulting paper sheet averaged 1.5 pounds.
In testing for wet-tensile-strength, strips one-half inch in width were pulled apart a few seconds after having been streaked transversely with a camel-hair brush wet with water.
Since the dried impregnated sheet is quite waterabsorbent, the test strips become wet throughby the time the tensile load is applied thereto. A
test similarly performed on the paper sheet before it was impregnated with a casein solution gave a wet-tensile-strength of 0.7 pound. When the dried, impregnated sheet was heated for one second at 475 to 500 F. and for about two to three minutes at 350 F., its wet-tensile-strength was increased to 2.5 pounds. The presence of a small amount of formaldehyde in the impregnating bath may boost the wet-strength values both before and after the shot of intense heat.
As already indicated, the short, high temperature heattreatment of my invention may be advantageously applied to various binder-impregnated papers whose binder depends upon dehydration to render it relatively strong when rewet. Thus, papers impregnated with viscose solutions or suspensions and other aqueous binders, besides albuminous binders, appearing as wetstre'ngthening agents in paper may be made to exert a much greater wet-strengthening effect on the paper by such heat treatment even after the paper containing such binder has already been dried thoroughly, as ordinarily. Of course, the surprising enhancement in wet-strength of the paper to be gained by my invention varies with the different binders. The presence of formalde-' hyde or other tanning agent in solutions of glue, casein, or other albuminous binders, such as I may employ herein, which causes a tanning reaction on the binder during the momentary intense heating of the binder-impregnated paper, may be advantageous in that such reaction may sometimes be brought more nearly to completion and the finished paper product ordinarily has higher wet-strength than isotherwise the case.
It is to be understood that my invention may be advantageously appliedno matter at what stage of paper-making the binder is infused into the paper sheet. Thus, in some instances, the glue, etc., may be introduced into the bulk pulp or fiber preparatory to its sheeting on the paper making machine; or such binders may be applied, as by spraying, to the wet or freshly -formed paper web before it reaches the dry end of the papermaking machine, for instance, in advance of the last press rolls. In the examples hereinbefore given, thesubstantially dry, absorbent waterleaf paper sheet as it issues progressively from the dry end of the paper-mat ing machine may be passed progressively through a bath of the binder solution, excess solution removed from the sheet immediately upon its emergence from .the bath, as by squeeze rolls or scraper blades, whereupon the sheet may be redried to completion and finally exposed to a temperature upwards of about 300 for less than temperature of the'drum, the extent to which the drum is wrapped by the paper sheet, and the speed of the sheet may be controlled to yield the best results according to the nature of the hinder, the wet-strength desired in the finished paper product, and other circumstances of manufacture. The cost of such a heating instrumentality is relatively low, for it is of compact simple construction and easily operated and controlled. In some instances, it may be desirable to cool the paper before it is reeled or accumulated or to moisten it with a small amount of water, say, with about 5% to 7% of its own weight of water, but these expedients, being simply additive to the invention hereof and being readily accomplished in simple ways by those skilled in the art, need not be discussed in detail or illustrated.
I While the invention hereof has been described as being applied to paper, it should be obvious that its utility may extend also to binder-impregnated woven'fabrics and to carded or felted fiber webs, for instance, tocarded cotton fiber webs or to wool felts wherein it may be desired to attain the highest wet-strengths by the use of binder-impregnants of the class hereinbefore described. I shall use in the appended claims the expression interfelted fibrous sheet material" as covering carded webs felts, and papers, as all such fibrous sheet material is characterized by a more or less interfelted fibrous structure or texture. So far as concerns the aspect of producing by my invention papers of the highest wetstrength, it will, of course be appreciated that the resulting papers might be of such high binder content as to be "sized or water-repellent or, in the case of viscose oralbuminous binders, such as glue and casein, be of such controlled binder content as to be water-absorbing and hence adapted for such uses as toweling, handkerchiefs, diaper linings, etc. It is obvious that the paper might be composed of various fibers or fiber mixtures,
for instance, of the usual chemical wood pulps, such as sulphite or kraft, wood pulps refined-to distinctly higher alpha-cellulose contents, say,
' upwards of 93%, rag pulp, etc.; and the paper base might be formed with various degrees of absorbency, depending upon the use to which the final paper product is to be put. Indeed, the paper mightcontain non-cellulosic fibers such as wool and asbestos. Should my invention be applied to papers comprising esssentially only mineral fibers, such as asbestos, it becomes possible to heat the binder-impregnated paper at temperatures higher than 050 F. and for a. time longer g 2,110,544 than mere seconds by reason of the incombustibility of such fiber. In-such latter case, the limit in temperature and time of final heat treatment is essentially that at which the binder is injured or decomposed by heat.
It isv possible by applying the inventive principles hereof to produce impregnated paper products of surprisingly high dry tear or shear resistance coupled with unusually high wetstrength (Mullen andtensile) Thus, I may start with refined wood pulp (Duracel) prepared by exposing kraft pulp to the refining action of comparatively strong alkaline liquor, for instance, so-calied white liquor, at about room or slightly elevated temperature until the pulp has acquired an alpha cellulose content of about 90 to 92%. Such refined pulp in either unbleached orbleached condition is put into substantiallyuniform aqueous suspension preparatory to the papermaking operation while preserving its fiber length'as much as is compatible with the realization of the desired substantially uniformly tax-- tured waterleaf paper sheet therefrom. The highly absorptive waterleaf paper sheet thus formed from such pulp is impregnated with a glue solution containing about 3% to 4% glue solids and a small amount of formaldehyde, squeezed to a glue content of about 3%, based on the dry weight of paper, air-dried at about room temperature, and finally brought into momentary contact with an intensely heated surface, as hereinbefore described. The resulting paper product is characterized by its unique combination of remarkably high wet-strength and very high dry tear-resistance. It might be noted that such a paper product is not only'similar to vegetable parchment in its high wet-strength and wet scuff-resistance but far surpasses ordinary vegetable parchment in its toughness or dry tearresistance. Because of the comparatively low glue content of such a paper product, it retains to a very large degree the flexibility of its waterleaf paper base as opposed to the comparatively stiff or brittle paper product produced when a similar paper base is impregnated to much higher glue content with a view toward giving it the high wet-strength of the paper product hereof simply by the usual passage over steam-heated drier drums of the papermaking or impregnating machine. The high dry tear-resistance of the paper product hereof is a reflection of the preservation of high average fiber length and fiber flexibility in the pulp entering into its waterleaf paper base; and the glue impregnant brought to the desired high degree of irreversibility by the intense heat treatment hereof is relied upon herein for the purpose of binding together the fibers and developing in the paper the wet-strength ordinarily sought to be gained by parchmentizing the fibers and thus sacrificing verysignificantiy the tear-resistance in the paper product.
The invention hereof may be applied advantageously to waterleaf papers, that is, papers whose fabrication is carried out without the addition of binder to the paper-making stock at any stage of papermaking. Thus, by subjecting various substantially waterleaf papers to the hotshot treatment hereof, it is possible to increase and appended claims, I mean a paper fabricated in the complete absenceof binder or sizingingradient or containing binder or sizing ingredient of such type or in such small amount that when made as heretofore its wet-strength is markedly lower than the percentage ratios just expressed; andI'do not mean to include by such quoted expression papers which have received a special chemical hydrating treatment, such as parchmentization. The hot-shot" treatment may in the case of such substantially waterleaf paper involve subjecting such paper, after it has been dried in the usual way, to a one-second heating on each face by progressively passing the paper sheet as it is coming from the papermaking machine in contact with a surface heated to about 450 to 500 F. In this way, the wet-strength (tensilestrength of a strip wide) of a waterleaf sheet of kraft towellng was increased from an initial value of 0.64% to 1.0#; of a waterleaf sheet com posed of 50% kraft and 50% groundwood from an initial value of 0.6# to 1.2#; of a waterleaf sheet composed of refined wood pulp and intended for nitrating purpose from an initial value of 0.3# to 1.0#. Results of a similar order were obtained with various other papers, for instance, papers made from Duracel pulp, sulphite pulp, and cookedmanila pulp. I shall now give in tabular form various characteristics of particular kinds of paper before and after a hot-shot treatment as above described.
Tests before hot-shot Mullen Tensile (p (i /l4) Tm Watrleiii papers Dry Wet Dry Wet Dry Wet 45f Kraft (106% Ostrand"). 48 1. 3 13. 6 1. 1 102 26 4 DuraceP' 52 1. 7 12. 7 1. 0 157 42 40* Alpha N. 13 1. 0 5. l D. 3 73 12 Tests after hot-shot Mullen Tensile (po (i /a") Waterleaf papers Dry Wet Dry Wet Dry Wet 45* Kraft (100% Ostrand 48 5. 0 13. 6 2. 2 98 58 48# Duracel'krfl- 52 5. 4 14. 4 2. 1 128 82 40# "Alpha N" 14 l. 3 4.? 0. 9 67 24 All test specimens of paper were soaked in water for one-half hour before the various wet tests were applied thereto; and the wet Mullen test was determined by bursting through 4 plies of the material under examination and dividing the gage reading by 4.
In other examples involving the application of the invention hereof, small quantities of binder, including casein and rosin size, were added to the papermaking stock after the manner of making the usual so-called engine-sized papers. Thus, A% casein, based on the dry weight of fiber, was precipitated from an ammonia-casein solution by means of alum. in a papermaking stock of 50% kraft and 50% groundwood. The stock was converted on a paper-making. machine into a sheet of creped toweling of 37# basis weight. When dried in the usual way, the paper toweling had a wet-tensile-strength of 0.6#, but when subjected after drying to contact on each of its faces for one second with a surface at about 450 to 500 F., the wet-strength of the paper toweling was increased to 2.5#. The resulting paper toweling was very absorbent and was not embrittled to any serious extent by the momentary heating. A similar improvement in the quality paper both in waterleaf and tub-sized condition before and after the hot-shot treatment above described.
' Tests before hot-shot f I Mullen Tensile (points) #m") 5'. we
. scuff rating Dry Wet Dry Wet Dry Wet 4MRom8l"krafi a1 4.0 10.0 1.3 68 it. 8 Same paper tub-sized with sodium caseinate with deposition of 1% casein (based on weight of paper) 39 5.0 11.5 1.6 76 92 8 Tests after hot-shot Mullen Tensile T ints r Wet (D (/36 m rating Dry Wet Dry Wet Dry Wel- #Romal"krait. 38 14.3 10.4 3.3 62 99 30 Same paper tub-sized with sodium caseinate with deposi-. tionil 1% Caste!!! ase on we 0 1 From the foregoing tables, it is apparent that the present inventionv makes possible in a simple and inexpensive way a marked and important increase in the utility of ordinary papers. Apropos of such increased utility, it might be noted that ordinary wrapping paper, for instance, is enhanced by-the invention hereof tremendously in its'resistance to breakage or scuff when thoroughly soaked with water and is hencefi-endered much more suitable as a wrapping paper which may be'soaked, as by exposure to rain, or for fabrication into bags intended to hold moist or wet vegetables, or for use as aerate-liner, etc.
The present invention thus makes possible among.
other things the production of paper products adapted' to supersede in various fields of use requiring papers of high wet-strength such comparativelyexpensive prior art paper products as parchment papers, wax papers, etc. t So far asI know, I am the first to recognize that waterleaf papers and'ordinary sized papers, for instance, rosin-sized wrapping paper, may beconverted by the high temperatureheating treatment hereof into finished paper products whose resistance to the disintegrating effect of' water is enormously greater than that of the original papers. The finished waterleaf paper products hereof have, as already indicated, a Mullen wetstrength of more than about 8% of the dry 'Mullen strength and a wet tensile strength of morethan about 12% of the dry tensile strength. The papers sized with rosin and heat-treated as hereinbefore described have a wet Mullen strength or wet tensile strength higher than about 25% of the corresponding dry tests; and such highwet-strength is inherent in the heat-treated paper base itself for the sizing agent in the heattreated paper product having such high wet! strength may be one for instance, rosin size, that has but little or no wet strength itself on long soaking of the paper in water and that hence imparts very little or no wet-strength to the paper. In other words, the function of the sizing agent itself may be simply and essentially cose, casein, etc., and to sized papers whose size content does not contribute significantly to the high wet-strength of the finished paper product hereof, it appears likely that in the case of all of these papers there is an incipient' caramelization or searing of the fibers and/or of the colloidal matter present in the paper under the high temperature heating treatment hereof and that such action is accompanied-by the-formation of wet-strengthening reaction products in the paper base; or it is possible that wet-strengthening reaction products arise in the paper baseas-a result of some oxidation of the fibers and/or of the colloidal matter under the high temperature heating treatment hereof. Whether or not the foregoing explanation of the mechanism underlying the wet-strengthening action in paper realized by the invention hereof is'correct, it is a. fact that I am enabled pursuant to the present invention to produce at low expense very valuable paper products heretofore unknown to the industry,
so far as I am aware.
I claim:
1. A method of producing. a. paper product of high wet-strength, which comprises exposing a predried' paper sheet containing,.if at all, only a very small amount of binder to temperatures upwards. of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet while markedly increasing its wetstrength.
' 2. A method of producing a paper product'of' high wet-strength as a dry paper sheet is being fabricated progressively at high speed, "which comprises progressively bringing the dried sheet into only momentary contact with a surface heated to about 400 to 650 F.
v 3. A method of producing substantially waterleaf paper ofliigh wet-strength, which comprises exposing a predried'sheet of the waterleaf paper to temperatures upwards of about 300 F. for such alimited period of time as to avoid sensible burning of or injury to such sheet while markedly increasing its Wet-strength.
4. A method of producing sized paper of high wet- -strength, which comprises exposing a predried sheet of sized paper containing only a very small amount of size to temperatures upwards of about 300 F, for such a limited period of time asto avoid sensible burningof or injury to such sheet while markedly increasing its wet-strength. 5. In a method involving the impregnation of fibrous sheet material with aqueous binder composition whose binder content tends to set irreversibly-upon the drying of such sheet material, that step which comprises exposing the dried impregnated sheet material containing only a very small amount of the binder to temperatures upwards of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet material while markedly increasing its wet-strength.
6. In a method involving the impregnation of fibrous sheet material with aqueous albuminous 5 binder composition and drying such sheet material, that step which comprises exposing the dried impregnated sheet material containing only a very small amount of such binder to temperatures upwards of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet material while markedly increas-- ing its wet-strength.
7. In a method involving the impregnation of an interfelted fibrous sheet material with aqueous binder composition whose binder content tends to set irreversibly upon the drying of such sheet material, that step which comprises exposing the dried impregnated sheet material containing only a very small amount of the binder to temperatures upwards of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet material while markedly increasing its wet-strength.
8. In a method involving the impregnation of an interfelted fibrous sheet material with aqueous albuminous binder composition and drying. such sheet material, that step which comprises exposing the dried impregnated sheet material containing only. a small amount of suchbinder to temperatures upwards of about 300 F. for such a limited period of time as to avoid sensible burning of or injury to such sheet material while markedly increasing its wet-strength;
9. In a method involving the impregnation of a 85 fibrous base with aqueous albuminous binder composition and drying such base, that step which comprises exposing the dried impregnated base containing only a small amount of such binder momentarily to a temperature of about 400 to 650 F. i
10. In a method involving the impregnation of a fibrous base with aqueous albuminous binder composition and drying such base, that step which comprises exposing the dried impregnated base containing only a small amount of such binder momentarily to a temperature ,of about 400 to 650 F. in the presence of an insolubilizing agent for said albuminous binder.
11. In a method involvingthe impregnation a paper sheet with aqueous binder composition whose binder content tends to set irreversibly upon. the drying of the impregnated sheet ,7 and involving further the production of the dried impregnated paper sheet progressively and at high speed, that step which comprises progressively exposing the dried impregnated sheet containing only a small amount of such binder momentarily to intense heat and thereby to enhence the wet-strengththereoi.
12. In a method involving the impregnation of a paper sheet with aqueous colloidal binder composition whole binder content tends to set irreversibly upon the drying of the impregnated sheet and involving further the production oi the dried impregnated paper sheet progressively and 'at high speed. that step which comprises progressively exposing the dried impre nated sheet containing onlya small amount or such binder so to a temperature upwards of about 300 1". for suchslimitedperiod of timesstoavoidsensible burning of or injury to such sheet while markedly increasing its wet-strength.
13. In a method involving the impregnation of a fibrous sheet with aqueous binder composition whose binder content tends to set irreversibly upon the drying of the impregnated sheet and involving further the production of the dried impregnated sheet progressively and at high speed, that step which comprises progressively bringing the dried impregnated sheet containing only a small amount of such binder into only momentary contact with a surface heated to about 400 to 650 F.
14. In a method involving the progressive impregnation of a progressively moving paper sheet with aqueous albuminous binder solution and the progressive drying of the impregnated paper sheet, that step which comprises progressively bringing the dried impregnated sheet containing only a small amount of such binder to a very high temperature for such a limited period of time as to avoid sensible burning of or injury to such sheet while markedly increasing its wetstrength.
15. In a method involving the progressive impregnation of a progressively moving paper sheet with aqueous albuminous binder solution and the progressive drying of the impregnated paper sheet, that step which comprises bringing the dried impregnated sheet containing onlya smallamount of such-binder into momentary contact with a surface heated to about 400 to 650 F. and thereby enhancing the wet-strength imparted thereto by said albuminous binder.
16. In a method involving the progressive impregnation of a progressively moving paper sheet with aqueous albuminous binder solution and the progressive drying of the impregnated paper sheet, that step which comprises exposing the dried impregnated sheet containing only a small amount of such binder .in the presence of an insolubilizing agent for said albuminous binder momentarily to a temperature of about 400 to 650 F. and thereby enhancing the wet-strength imparted thereto by said albuminous binder.
17. A paper product which has been exposed in dried condition to a temperature upwards of about 300 F. for such a short period of time as 19. A sized paper product which contains only a very small amount of size and which has been exposed in dried condition to a temperature upwards oiabout-300 Fdor such a short period or time as to be substantially unscorched while being improved markedly in its wet-strength.
20. A method of producing a paper product.
of high wet-strength, which comprises exposing a. predried paper sheet containing, it stall, only a very small amount of binder to temperatures 0! about 400 to 650 1". for such a limited period of time as to avoid sensible burning of or injury to such sheet while markedly increasing its wetstrength.
. MILTON O. SCHUR.
US94157A 1936-08-04 1936-08-04 Method of enhancing the wetstrength of papers Expired - Lifetime US2116544A (en)

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FR828018D FR828018A (en) 1936-08-04 1937-10-18 Process for improving the wet resistance of papers

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1141876B (en) * 1959-03-20 1962-12-27 Dr Rolf Mohr Process for the production of wet-strength cellulose wadding and papers
US3103462A (en) * 1960-04-18 1963-09-10 Eastman Kodak Co Method of improving the strength characteristics of paper prepared from partially acylated cellulose fibers
EP0216145A3 (en) * 1985-08-23 1987-06-16 International Paper Company Heat treatment of paper products having milk and other additives
US4718982A (en) * 1985-08-23 1988-01-12 International Paper Company Densification and heat treatment of paperboard produced from SCMP and other sulfite pulps
US4718981A (en) * 1985-08-23 1988-01-12 International Paper Company Bleached kraft paperboard by densification and heat treatment
US4818342A (en) * 1985-08-23 1989-04-04 International Paper Company Heat treatment of paper products
US4828650A (en) * 1985-08-23 1989-05-09 International Paper Company Heat treatment of paper products having milk and other additives
US4919758A (en) * 1985-08-23 1990-04-24 International Paper Company Heat treatment of paper products having starch additives
US5582682A (en) * 1988-12-28 1996-12-10 Ferretti; Arthur Process and a composition for making cellulosic composites
US5637195A (en) * 1995-03-23 1997-06-10 Westvaco Corporation Method to reduce off-taste and/or odor from hygienic paper packages
US5834095A (en) * 1996-12-17 1998-11-10 Kimberly-Clark Worldwide, Inc. Treatment process for cellulosic fibers
US20060174904A1 (en) * 2005-02-07 2006-08-10 Schweitzer-Mauduit International, Inc. Smoking articles having reduced analyte levels and process for making same

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2510628B1 (en) * 1981-08-03 1985-07-12 Personal Products Co STABILIZED ABSORBENT SHEET, ESPECIALLY FOR HYGIENIC PADS AND LAYERS

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1141876B (en) * 1959-03-20 1962-12-27 Dr Rolf Mohr Process for the production of wet-strength cellulose wadding and papers
US3103462A (en) * 1960-04-18 1963-09-10 Eastman Kodak Co Method of improving the strength characteristics of paper prepared from partially acylated cellulose fibers
EP0216145A3 (en) * 1985-08-23 1987-06-16 International Paper Company Heat treatment of paper products having milk and other additives
US4718982A (en) * 1985-08-23 1988-01-12 International Paper Company Densification and heat treatment of paperboard produced from SCMP and other sulfite pulps
US4718981A (en) * 1985-08-23 1988-01-12 International Paper Company Bleached kraft paperboard by densification and heat treatment
US4818342A (en) * 1985-08-23 1989-04-04 International Paper Company Heat treatment of paper products
US4828650A (en) * 1985-08-23 1989-05-09 International Paper Company Heat treatment of paper products having milk and other additives
US4919758A (en) * 1985-08-23 1990-04-24 International Paper Company Heat treatment of paper products having starch additives
US5582682A (en) * 1988-12-28 1996-12-10 Ferretti; Arthur Process and a composition for making cellulosic composites
US5637195A (en) * 1995-03-23 1997-06-10 Westvaco Corporation Method to reduce off-taste and/or odor from hygienic paper packages
US5834095A (en) * 1996-12-17 1998-11-10 Kimberly-Clark Worldwide, Inc. Treatment process for cellulosic fibers
US20060174904A1 (en) * 2005-02-07 2006-08-10 Schweitzer-Mauduit International, Inc. Smoking articles having reduced analyte levels and process for making same
US20110000497A1 (en) * 2005-02-07 2011-01-06 Schweitzer-Mauduit International, Inc. Smoking Articles Having Reduced Analyte Levels and Process For Making Same
US8151806B2 (en) 2005-02-07 2012-04-10 Schweitzer-Mauduit International, Inc. Smoking articles having reduced analyte levels and process for making same

Also Published As

Publication number Publication date
GB502425A (en) 1939-03-17
FR828018A (en) 1938-05-09

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