US2229620A - Method of applying coating materials to paper - Google Patents

Method of applying coating materials to paper Download PDF

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US2229620A
US2229620A US174876A US17487637A US2229620A US 2229620 A US2229620 A US 2229620A US 174876 A US174876 A US 174876A US 17487637 A US17487637 A US 17487637A US 2229620 A US2229620 A US 2229620A
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web
paper
coating material
coating
wet
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Donald B Bradner
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Champion Paper and Fibre Co
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Champion Paper and Fibre 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
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/22Addition to the formed paper
    • D21H23/32Addition to the formed paper by contacting paper with an excess of material, e.g. from a reservoir or in a manner necessitating removal of applied excess material from the paper
    • 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
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/22Addition to the formed paper
    • D21H23/24Addition to the formed paper during paper manufacture
    • D21H23/26Addition to the formed paper during paper manufacture by selecting point of addition or moisture content of the paper
    • D21H23/28Addition before the dryer section, e.g. at the wet end or press section
    • 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
    • D21H25/08Rearranging applied substances, e.g. metering, smoothing; Removing excess material
    • D21H25/12Rearranging applied substances, e.g. metering, smoothing; Removing excess material with an essentially cylindrical body, e.g. roll or rod

Definitions

  • This invention relates to methods of applying coating materials to paper; and it comprises a method wherein a web is formed from an aqueous pulp suspension in one of the usual ways, the wet 5 web is subjected to at least the first of the usual pressing operations, then before the web is subjecteo to any substantial drying operation which may cause appreciable shrinkage of the web, liquid coating material is applied in excess to the web, excess coating material is removed and the web is dried; further pressing operations sometimes being applied to the web'prior to drying; all as more fully hereinafter set forth and as claimed.
  • a partially shrunken web are overcome by applying thecoating to the web before there has been any shrinkage, that is at a location after the web has passed through at least the first of the usual wet presses and before the web has reached the stage of dryness described.
  • the paper is dried, and shrinkage takes place in the normal manner causing no more difii'culty' than with a web to which no coating material has been applied.
  • the surfacing material may be applied in any conyenient way, as by means of a roll engaging the under side of the web and wiping against it to eliminate any bubbles and to insure complete covering of the web with coating.
  • This roll dips into a trough kept supplied with the coating material.
  • a roll driven in the reverse direction to the paper serves the purpose very well though the desired wiping action can also be secured if the roll is driven in the paper direction at a speed sumciently greater or less than that of the paper.
  • a large excess of coating composition is thus applied all across the web.
  • the greater part of the coating composition, specifically that part which lies above the level of the surface fibers is then removed from the web and returned to the source of supply.
  • This removal may be accomplished by a wiping action, as described in my hereinbefore cited patent, as distinguished from the pressing-in action of press or squeeze rolls, and as further distinguished from removal by suction devices of any kind.
  • One device suitable for removing the excess coating may take the form of a rod mounted on a rigid support and adapted to bear on the pap r, in a manner similar to that illustrated in Patent No. 1,944,835 to C. F. Boyers.
  • Another device'for the same purpose is a reversely turning roll, advantageously of relatively small radius, wiping against the wet coattion.
  • suction elements means suction boxes, or suction rolls, such as the suction couch or press rolls commonly used on the wet end of a paper making-machine.
  • the object of my invention is thus the elimination of the difilculties heretofore encountered in making a filled-surface paper on the paper machine, and the provision of means whereby a paper web can be surface filled on one or both sides in or adjacent to the wet press section of the machine, and whereby this can be accom plished at usual paper machine speeds.
  • Fig. 1 is a diagrammatic view in elevation of the wet press section of a paper making machine showing devices for applying coating ma terial to paper in accordance with my inven- Fig. 2 is a fragmentary view showing these Fig. 3 is a fragmentary view showing the same devices arranged to applyv coating material to the upper (felt) side of the web instead of the lower (wire) side. 7
  • Fig. 4 is an enlarged view of a portion 0 Fig. 1 showing the devices for applying coating material and removing the excess, in greater detail.
  • Fig. 5 isan enlarged view similar to Fig. 4, but showing a modified arrangement for removing the excess coating material.
  • the web is taken off the first felt under a guide roll 22.
  • Coating material is supplied to the trough through an inlet pipe i2 and is maintained at a constant level by an overflow pipe l3.
  • Excess coating is now removed from the surface of the web by passing the surface over a rod l4 mounted on a beam 2
  • the web which is now surface filled passes over a guide roll 24 and is taken up on a felt H.
  • the felt and web pass between second press rolls l5 and IS.
  • the web, still damp. may now be passed between third press rolls if desired (not shown) and thence to driers.
  • Fig. 2 shows an advantageous modification wherein the coating applying and removing devices are arranged to take the web after it has passed through the so-called felt presses shown in Fig. l, and a so-called offset press 3l-42, and before it passes to first drier drums 34 and 35, in the drier section of the machine
  • the coating applying and removing device in this location functions exactly as has been described.
  • the location is particularly advantageous because the freshly filled surface is not subjected to a pressing operation which tends to drive the coating material into the web instead of leaving it in the surface depressions to the desired extent.
  • Fig. 3 is shown an arrangement which uses the same devices, to apply the coating material to the upper or felt side of the web. This can be used independently if desired, or combined with a device for applying coating material to the wire side of the web as shown in Fig. 1 or Fig. 2, so that a web can be treated on either one or both sides as may be desired.
  • the arrangement of Fig. 3 is shown as including additional guide rolls 31, 38. Three of the drums 34, 35 and 38 of the dryer section of the machine are shown in this figure. l
  • Fig. 5 is illustrated an alternative method by which the surplus coating material may be removed from the web.
  • an excess of the coating or filling material is applied to the web by the roll H as already described.
  • the coating material is held in a wider trough 41 instead of the trough III as before, In this trough also rotates another, preferably smaller, reversely turning roll 42 which wipes from the web the excess coating material.
  • this roll 42 shall not simply wipe this removed material back onto the web it is arranged to dip into the material in trough 4
  • Roll 42 thus constantly presents a clean surface to the leaving web, which may be thus wiped clean and smooth down to the level of the surface fibers.
  • excess as applied to the coating material removed I mean the amount of coating material lying above the-level of the surface cium carbonate, titanium oxide and other mineral pigments may be used in aqueous suspension in combination with' adhesives, such as casein, starch, and the like. Either side or both sides of the web may be thus treated.
  • the resulting filled surface paper has improved printed properties and improvedmolor and appearance and the method of manufacture described is simple and economical.
  • aqueous coating composition was applied to the under (wire) side by means of a reversely turning roll dipping into a trough.
  • This particular coating composition on a dry basis consisted of 90 parts clay, 10 parts finely divided calcium carbonate and 11 parts casein. The total solids in the suspension were 23.5 per cent.
  • the web was then drawn against a small rod mounted on a heavy beam and having a radius of curvature of about 5 inch. The wrap of the paper on the rod was about 20 degrees. The rod removed the excess coating composition, i.
  • the coating composition lying above the upper level of the surface fibers leaving the surface well filled with mineral pigment and adhesive in amount of about 4 pounds per ream (500 sheets) of 25 x 38 inches paper.
  • the paper web, which was still wet, was then passed to the second press, oifset press, driers and calenders, in the usual manner.
  • the completed surfacefilled paper had improved printing characteristics, color, and appearance.
  • a coating composition which on the dry basis consisted of 80 parts of clay, 20 parts of finely divided calcium carbonate, and 23 parts of starch, in aqueous suspension comprising 17 per cent total solids, was applied to a paper web between the last wet press and the driers in the manner described.
  • the draw on the web was regulated so that in the dried web the surface was filled with about 2 pounds of pigment and adhesive per ream, which were concentrated in the surface depressions of the web.
  • Method of making surface-filled paper which comprises forming a web of paper, subjecting the web while wet to at least one pressing operation, thereafter, in operations separate from any pressing operation, after the last application of suction to the undried web and before any drying, applying aqueous liquid coating. material comprising adhesive and pigment in suspension to one surface only of the web, then wiping oil that part of the coating material which lies above the level of the surface fibres, thereby leaving on the paper only a small amount of coating material localized in and substantially filling the surface depressions of the web, and thereafter drying the web.
  • Method of making surface-filled paper which comprises forming a web of paper, subjecting the web while wet to at least one pressing operation, thereafter, in operations separate from any pressing operation,,after the last application of suction to the undried web and before any drying, applying aqueous liquid coating material comprising adhesive and pigment in suspension to one surface only of the web, then wiping off by means of a small-radius edge that part of the coating material which lies above the level of the surface fibres, thereby leaving on the paper only a small amount of coating material localized in and substantially filling the surface depressions of the web, and thereafter drying the web.
  • Method of making surface-filled paper which comprises forming a web of paper. subjecting the web while wet to at least one pressing operation, thereafter, in operations separate from any pressing operation, after the last application of. suction to the undried web and before any drying, applying aqueous liquid coating material comprising adhesive and pigment in suspension to one surface only of the web, then, where the web is not supported on its other side, wiping it over a small-radius edge to remove the coating material which lies above the level of the surface fibres, thereby leaving on the paper only a small amount of coating material localized in and substantially filling the surface depressions of the web, and thereafter drying the web.

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Description

EEG 21, D. B. BRADNER 2,239,620
METHOD OF APPLYING COATING MATERIALS TO PAPER Filed Nov. 16, 1957 Dona/0L 23. Bromine);
Patente Jan. 21, 194i METHOD OFAPPLYING COATING MATERIALS T0 PAPER Donald B. B radner, Hamilton, Ohio, assignor to The Champion Paper and Fibre Company, Hamilton, Ohio, a corporation of Ohio Application November 16, 1937, Serial No. 174,876
4 Claims.
This invention relates to methods of applying coating materials to paper; and it comprises a method wherein a web is formed from an aqueous pulp suspension in one of the usual ways, the wet 5 web is subjected to at least the first of the usual pressing operations, then before the web is subjecteo to any substantial drying operation which may cause appreciable shrinkage of the web, liquid coating material is applied in excess to the web, excess coating material is removed and the web is dried; further pressing operations sometimes being applied to the web'prior to drying; all as more fully hereinafter set forth and as claimed.
In my United States Patent No. 1,913,329 there is described a process of making paper having a filled surface wherein a layer of mineral coating material is applied as an aqueous suspension to a web of paper which has been subjected to at least a partial drying operation and the excess coating is removed down to the upper level of the surface fibers by scraping or blowing. The printing sur face of the resulting product contains both fiber and mineral matter; thelatter filling inter-fiber depressions, but not covering the face of the paper. The method of filling is simple, and with ordinary care and regulation, is certain in results.
It has been found, however, when the application of the coating material is carried out, as described in my prior patent, at the usual stage of operations, 1. e., after the web has been sub: jected to at least a partial drying operation, that dimculties are sometimes encountered due to the shrinkage of the web which has accompanied the drying. Application of the liquid coating material at this stage can cause a swelling of the web, tending to cause a wrinkling or puckering which can only be prevented by extremely close attention and regulation. Furthermore, the drying and consequent shrinkage commonly take place more or les's'unevenly across the width of the web.-
unevenness serves to accentuate the tendency of the web to. pucker, which at times operating dimculty. v
Now, I have discovered that, as water is removed from a freshly formedpaper web, no appreciable changev in'dini'ensions takes-place until the retained waterin the web is reduced to a certain definite amount which varies'somewhat with the particular grade of paper, but is ordinarily found when the weight of retained water is from 1.5 to 2 times the dry weight of the paper. The particular point in the paper machine at which may become so serious asto'constitute a major I .have discovered that the puckering and 10\ wrinkling of the web incident to the application l of coating material to. a partially shrunken web are overcome by applying thecoating to the web before there has been any shrinkage, that is at a location after the web has passed through at least the first of the usual wet presses and before the web has reached the stage of dryness described. After the coating operation, the paper is dried, and shrinkage takes place in the normal manner causing no more difii'culty' than with a web to which no coating material has been applied. By this means I find it possible to practically eliminate various troubles and wastes formerly incident to the surface filling operation.
The surfacing material may be applied in any conyenient way, as by means of a roll engaging the under side of the web and wiping against it to eliminate any bubbles and to insure complete covering of the web with coating. This roll dips into a trough kept supplied with the coating material. A roll driven in the reverse direction to the paper serves the purpose very well though the desired wiping action can also be secured if the roll is driven in the paper direction at a speed sumciently greater or less than that of the paper. A large excess of coating composition is thus applied all across the web. The greater part of the coating composition, specifically that part which lies above the level of the surface fibers is then removed from the web and returned to the source of supply. This removal may be accomplished by a wiping action, as described in my hereinbefore cited patent, as distinguished from the pressing-in action of press or squeeze rolls, and as further distinguished from removal by suction devices of any kind. One device suitable for removing the excess coating may take the form of a rod mounted on a rigid support and adapted to bear on the pap r, in a manner similar to that illustrated in Patent No. 1,944,835 to C. F. Boyers. Another device'for the same purpose is a reversely turning roll, advantageously of relatively small radius, wiping against the wet coattion.
' devices in a different location.
ing on the web and in turn itself wiped clean before again contacting the paper web. v
I have further discovered the surprising fact that in spite of the extremely tender and weak condition of the web in the wet press section of the paper machine, when the web still contains more water than fibers by weight, the application of coating and the drastic treatment incident to removal of the excess, for example, the pulling ofthe web over a small radius scraper or wiper blade, can be successfully carried out on the web in this state without damage to the web and often even without reducing the speed of the machine.- It is a remarkable and totally unexpected fact that this operation can be conducted on even a well filled light weight book paper-an exceptionally tender material at this stage of manufacturewithout difficulty and at usual machine speeds.
It is arranged so that the application and the removal of surplus coating material be carried out at a point of contact with press rolls, advantageously after the last press, while the web still contains more water than fiber by weight, and that after the coating has beenapplied to one side of the web, this side be not subjected to suction, which might tend to remove some of the coating material or suck it out of the surface pores or depressions of the web. Advantageously no suction is applied to either side of the web after the coating has once been applied as this tends to interfere with the desired distribution of the coating material. For these reasons the application of coating and the removal of the surplus are advantageously carried out at a location in the paper machine after the web has passed at least one wet press, after the last suction element, and before any substantial drying of the web has taken place. By suction elements I means suction boxes, or suction rolls, such as the suction couch or press rolls commonly used on the wet end of a paper making-machine.
The object of my invention is thus the elimination of the difilculties heretofore encountered in making a filled-surface paper on the paper machine, and the provision of means whereby a paper web can be surface filled on one or both sides in or adjacent to the wet press section of the machine, and whereby this can be accom plished at usual paper machine speeds.
The method of my invention can be carried out by using apparatus such as that illustrated more or less diagrammatically in the accompanying drawing, in which:
Fig. 1 is a diagrammatic view in elevation of the wet press section of a paper making machine showing devices for applying coating ma terial to paper in accordance with my inven- Fig. 2 is a fragmentary view showing these Fig. 3 is a fragmentary view showing the same devices arranged to applyv coating material to the upper (felt) side of the web instead of the lower (wire) side. 7
Fig. 4 is an enlarged view of a portion 0 Fig. 1 showing the devices for applying coating material and removing the excess, in greater detail.
Fig. 5 isan enlarged view similar to Fig. 4, but showing a modified arrangement for removing the excess coating material.
Referring to Fig. 1, a wet paper web 43 formed in any of the usual ways, is taken oh the end of the paper making machine (not shown) at a roll 8 under a guide roll I, and on to a first felt iwhich carries it through'the first press, which may advantageously be a suction press of known type, comprising rolls and I. The web is taken off the first felt under a guide roll 22. At this stage it is still very wet and tender, only part of the water having been rell picks up coating material from the trough and distributes it evenly over the web as it 15 passes over the roll. Coating material is supplied to the trough through an inlet pipe i2 and is maintained at a constant level by an overflow pipe l3. Excess coating is now removed from the surface of the web by passing the surface over a rod l4 mounted on a beam 2| as shown. The excess removed flows back into the rough. The web which is now surface filled passes over a guide roll 24 and is taken up on a felt H. The felt and web pass between second press rolls l5 and IS. The web, still damp. may now be passed between third press rolls if desired (not shown) and thence to driers.
Fig. 2 shows an advantageous modification wherein the coating applying and removing devices are arranged to take the web after it has passed through the so-called felt presses shown in Fig. l, and a so-called offset press 3l-42, and before it passes to first drier drums 34 and 35, in the drier section of the machine The coating applying and removing device in this location functions exactly as has been described.
The location, however, is particularly advantageous because the freshly filled surface is not subjected to a pressing operation which tends to drive the coating material into the web instead of leaving it in the surface depressions to the desired extent.
In Fig. 3 is shown an arrangement which uses the same devices, to apply the coating material to the upper or felt side of the web. This can be used independently if desired, or combined with a device for applying coating material to the wire side of the web as shown in Fig. 1 or Fig. 2, so that a web can be treated on either one or both sides as may be desired. The arrangement of Fig. 3 is shown as including additional guide rolls 31, 38. Three of the drums 34, 35 and 38 of the dryer section of the machine are shown in this figure. l
In Fig. 5 is illustrated an alternative method by which the surplus coating material may be removed from the web. In this arrangement an excess of the coating or filling material is applied to the web by the roll H as already described. The coating material is held in a wider trough 41 instead of the trough III as before, In this trough also rotates another, preferably smaller, reversely turning roll 42 which wipes from the web the excess coating material. In order that this roll 42 shall not simply wipe this removed material back onto the web it is arranged to dip into the material in trough 4| which thoroughly wets the surface of roll 42 which is then wiped clean by a rubber, or other suitable doctor blade 43. Roll 42 thus constantly presents a clean surface to the leaving web, which may be thus wiped clean and smooth down to the level of the surface fibers.
By the term excess" as applied to the coating material removed I mean the amount of coating material lying above the-level of the surface cium carbonate, titanium oxide and other mineral pigments may be used in aqueous suspension in combination with' adhesives, such as casein, starch, and the like. Either side or both sides of the web may be thus treated. The resulting filled surface paper has improved printed properties and improvedmolor and appearance and the method of manufacture described is simple and economical.
It will be seen from the following example that in my process no addition of rag or other special highstrength pulp is necessary to give the web added wet strength at this point, even though considerable proportions of filler be used.
The following example will illustrate the process: A certain book stock paper of such a thickness that 500 sheets of by 38 inches weigh 50 pounds and consisting of soda and sulfite pulp with a fair amount of clay filling, was formed on a Fourdrinier wire at 300 feet per minute. The
web was passed through a suction press to remove some water and then, while the web was still wet and before the web was subjected to any drying operation, a large excess of aqueous coating composition was applied to the under (wire) side by means of a reversely turning roll dipping into a trough. This particular coating composition on a dry basis consisted of 90 parts clay, 10 parts finely divided calcium carbonate and 11 parts casein. The total solids in the suspension were 23.5 per cent. The web was then drawn against a small rod mounted on a heavy beam and having a radius of curvature of about 5 inch. The wrap of the paper on the rod was about 20 degrees. The rod removed the excess coating composition, i. e., the coating composition lying above the upper level of the surface fibers, leaving the surface well filled with mineral pigment and adhesive in amount of about 4 pounds per ream (500 sheets) of 25 x 38 inches paper. The paper web, which was still wet, was then passed to the second press, oifset press, driers and calenders, in the usual manner. The completed surfacefilled paper had improved printing characteristics, color, and appearance.
In another case a coating composition which on the dry basis consisted of 80 parts of clay, 20 parts of finely divided calcium carbonate, and 23 parts of starch, in aqueous suspension comprising 17 per cent total solids, was applied to a paper web between the last wet press and the driers in the manner described. The draw on the web was regulated so that in the dried web the surface was filled with about 2 pounds of pigment and adhesive per ream, which were concentrated in the surface depressions of the web.
This application is a continuation-in-part of.
my prior application Ser. No. 729,341, filed June 6, 1934.
What I claim is:
1. Method of making surface-filled paper which comprises forming a web of paper, subjecting the web while wet to at least one pressing operation, thereafter, in operations separate from any pressing operation, after the last application of suction to the undried web and before any drying, applying aqueous liquid coating. material comprising adhesive and pigment in suspension to one surface only of the web, then wiping oil that part of the coating material which lies above the level of the surface fibres, thereby leaving on the paper only a small amount of coating material localized in and substantially filling the surface depressions of the web, and thereafter drying the web.
2. Method of making surface-filled paper which comprises forming a web of paper, subjecting the web while wet to at least one pressing operation, thereafter, in operations separate from any pressing operation,,after the last application of suction to the undried web and before any drying, applying aqueous liquid coating material comprising adhesive and pigment in suspension to one surface only of the web, then wiping off by means of a small-radius edge that part of the coating material which lies above the level of the surface fibres, thereby leaving on the paper only a small amount of coating material localized in and substantially filling the surface depressions of the web, and thereafter drying the web.
3. Method of making surface-filled paper which comprises forming a web of paper. subjecting the web while wet to at least one pressing operation, thereafter, in operations separate from any pressing operation, after the last application of. suction to the undried web and before any drying, applying aqueous liquid coating material comprising adhesive and pigment in suspension to one surface only of the web, then, where the web is not supported on its other side, wiping it over a small-radius edge to remove the coating material which lies above the level of the surface fibres, thereby leaving on the paper only a small amount of coating material localized in and substantially filling the surface depressions of the web, and thereafter drying the web.
4. The method of claim 1 in which the wiping off of the coating material from above the level of the surface fibres is accomplished where the web is not supported on the other side, by a reversely turning roll whose surface is wiped clean before it contacts the coated surface of the paper web.
DONALD B. BRADNER.
cERTI'ficATE OF CORRECTION. Patent No. 2,229, 620. January 21, mil.
DONALD B. BRADNER.
It is hereby certified that error appears in the printed specification of the above numbered patent requiring correctionas follows; Page 2, first column, line, 21, after the word "point" insert --out-; line 59, for "means" read mean-; same page, second column, line 60, after "web" insert the reference numeral --b.--; and that the sid Letters Patent should be read with this correction thereinthat the same may conform to the record of the case in the Patent Office Signed .and sealed this tum day of March, A. D 19in;
Henry Van Arsdale, (Seal) Acting Commissioner of Patents.
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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2518359A (en) * 1947-07-21 1950-08-08 United States Gypsum Co Coating for insulation boards
US2581058A (en) * 1947-07-21 1952-01-01 United States Gypsum Co Coatings for insulation board
US2649386A (en) * 1948-02-21 1953-08-18 North American Paper Process C Coated paper and method for making same
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
US2798414A (en) * 1952-11-26 1957-07-09 Combined Locks Paper Company Press roll couple and felt arrangement
US3063407A (en) * 1959-10-20 1962-11-13 Bergstein Packaging Trust Self-cleaning adhesive doctoring device
US3080847A (en) * 1959-10-21 1963-03-12 Beloit Iron Works Web coating and doctoring apparatus
US4238533A (en) * 1976-04-16 1980-12-09 La Cellophane Coating process and apparatus
WO1997047810A1 (en) * 1996-06-07 1997-12-18 Cartons St-Laurent Inc./St.Laurent Paperboard Inc. Method of making coated or impregnated paper or paperboard
US5865953A (en) * 1996-08-30 1999-02-02 Merrimac Paper Company, Inc. Paper for corrugating medium
US6299728B1 (en) * 1997-01-31 2001-10-09 Voith Sulzer Papiermaschinen Gmbh Multi-ply paper
US20020090457A1 (en) * 2001-01-10 2002-07-11 3M Innovative Properties Company Coating device and method using pick-and-place devices having equal or substantially equal periods
US20020192360A1 (en) * 2001-04-24 2002-12-19 3M Innovative Properties Company Electrostatic spray coating apparatus and method
US20030003238A1 (en) * 2001-01-10 2003-01-02 Leonard William K. Sheet coater
US6579574B2 (en) 2001-04-24 2003-06-17 3M Innovative Properties Company Variable electrostatic spray coating apparatus and method
US20070264431A1 (en) * 2006-05-11 2007-11-15 Chung Yuan Christian University Apparatus for film formation

Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2518359A (en) * 1947-07-21 1950-08-08 United States Gypsum Co Coating for insulation boards
US2581058A (en) * 1947-07-21 1952-01-01 United States Gypsum Co Coatings for insulation board
US2649386A (en) * 1948-02-21 1953-08-18 North American Paper Process C Coated paper and method for making same
US2721504A (en) * 1950-07-14 1955-10-25 Statens Skogsind Ab Process for impregnating fibre materials
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