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Publication numberUS2772604 A
Publication typeGrant
Publication dateDec 4, 1956
Filing dateJun 3, 1953
Priority dateJun 3, 1953
Publication numberUS 2772604 A, US 2772604A, US-A-2772604, US2772604 A, US2772604A
InventorsMuggleton Gerald D
Original AssigneeCombined Locks Paper Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of coating paper with high solids content coating material
US 2772604 A
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Description  (OCR text may contain errors)

m NR O m T AB EM LG: e Gum Um M CJ d .T D Nu E QM Dec. 4, 1956 METHOD OF COATING PAPER WITH HIGH SOLIDS x hw if INVENTOR. GERALD D. MUGGLETON ATTORNEY United States Patent O METHOD OF COATING PAPER WITH HIGH SOLIDS CONTENT COATING MATERIAL Gerald D. Muggleton, Appleton, Wis., assignor to Combined Locks Paper Co., Combined Locks, W1s., a corporation of Delaware Application June 3, 1953, Serial No. 359,392

1 Claim. (Cl. 9240) This invention relates to improvements in the art of paper making and particularly to improved methods of applying paper treating material such as coatings, loading materials, pigments, sizing, and the like.

In applying paper treating material to the web of paper on the customary paper machine, several problems arise. The rapidly moving web (speeds as high as 1000 feet per minute) is carried on various wires, felts, and rollers the speeds of which are controlled and correlated with the speed of the web and with the elongation thereof to prevent undue slack or tension. Any addition of paper treating material to the traveling web must there fore be done by transfer from a rolling surface to the web. However, if a pattern is formed on such rolling surface such pattern will be transferred to the web. Likewise, if paper treating material remains on such rolling surface as such surface parts from the web, a pattern will result from the splitting action of the material remaining on the web and material remaining on such rolling surface. The various methods heretofore used to prevent the finished web from having a commercially undesirable pattern have all had some economic disadvantages. If the treating material is added by the dandy roll while the web is still on the wire (Muggleton Patent No. 2,426,043), there is a low limit on the solids content of such treating material, the use of large quantities of water, and the need to recover treating material which passes through the web at the suction boxes and couch rolls. If pattern dispersing devices are used, such as reversing rolls, doctors, and metering rolls (Muggleton Patents Nos. 2,398,843 and 2.398,844), the additional friction requires more operating power, speedsare lowered, and maintenance costs are increased.

It is the object of this invention therefore to provide an economical method for applying paper treating material to a web of paper without formation of commercially non-acceptable pattern thereon and without use evenness due to a pattern imparted by the coating roll.

If the web has a water content of 80% to 86% and the coating material has a solids contents in excess of the solids content of the web, the web seems to be able to take the paper treating material and any pattern transferred from the coating roll or caused by the splitting of the material as the web breaks away from the coating roll levels out and disperses.

The novel features, which are considered characteristic of the invention, are set forth with particularity in the appended claim. The invention, together with additional objects and advantages thereof, will best be understood from the following description of a specific embodiment when read in connection with the accompanying drawings, in which:

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Fig. 1 is a diagrammatic view in side elevation of the wet end of a Fourdrinier paper making machine showing the press rolls by which the method embodying this invention is carried out;

Fig. 2 is an enlarged fragmentary diagrammatic view in side elevation of the first press of said machine; and

Fig. 3 is an enlarged fragmentary diagrammatic view in side elevation of the third press of said machine.

The web 10 is formed in the usual manner on the wire 12 of the paper making machine. Upon leaving the couch roll 14 the web is picked up by the felt 16 of the first press 18. After passing through the press 18, the web is picked up by the felt 20 of the second press 22. At this press the web 10 being stronger may be carried over the tops of applicator rolls and again deposited on the felt 20. Thereafter the web is transferred to the felt 24 of the third or reversing press 26. As the web leaves the couch roll 14 and is received by the first press rolls 18, it has a water content of from to 86% and a solids content of 14% to 20%, such solids content may be free of clay or other ash forming content.

At such consistency the web is able to take from the upper roll of the first press 18 a film or coating of paper treating material which has a solids content in excess of the solids content of the web and in the range of 35% to 50%. When the web is taking up such coating, any pattern which is imparted from the upper roll or caused by splitting of the material will disperse and become uniform to a sufficient extent so that there will remain in the web no commercially unacceptable pattern. To apply the film of material to a coating roll or the upper roll of the first press 18 there is reanired only a single smooth roll 28 in rolling engagement with said upper roll to form a nip in which a supply pool 30 of the material may be maintained. As both of these rolls operate without appreciable relative sliding motion therebetween, there is no frictional resistance to retard sp ed or require additional driving power such as results with the use of pattern removing devices. Such single smooth roll 28 may be added to the press without material or costly structural alterations.

Various kinds of paper treating material may be added to the web by this method. Pigments such as titanium dioxide, sizings such as starch and casein, and loading materials such as clay, may be used singly or in varying mixtures. It is only essential that the percentage of solids content of the material be substantially greater than the percentage of solids in the web and within the range specified. If the percentage of solids content in the material is too low, the web cannot take up the water in the paper treating material because at such stage the web has few, if any, voids. When the solids content of the paper treating material becomes too excessive the material will not be completely removed from the surface of the press roll 18. When this occurs the pattern tends to become so pronounced that it will not satisfactorily disperse. Therefore, the upper limit of such solids content is attained when the capa itv of the web to take all the coating material is reached.

During the application of the paper treating material the web may be run within a large range of speeds without making any appreciable difference in the creation of pattern. The important aspect is that the web may be run more easily and with less power and at higher speeds. In fact, the speed of the web may be slightly increased over the customary speed when not adding material because of the presence of the paper treating material on the upper press roll. This helps eliminate pick-up and consequent breakage, thus letting the speed be increased. Speeds as high as 1000 feet per minute are permissible, the lowest practical speed being in the neighborhood of 350 feet per minute.

The web at the recommended range of 30% to 86% water content should be supported on a felt. It does not have proper tensile strength to withstand breakage and damage when passing through the nips of the first press 18 unless supported by the felt 16. In all paper making machines the web is supported by a felt at the first press and hence no felt need be added. In some paper making machines the lower roll of the first press has a suction box. This may be disconnected when the press is being used to apply paper treating material and thus keep the material from penetrating the web and let it remain on the surface of the web. The use or non-use of the suction at the lower roll of the first press, however, does not affect the operation of this method.

There does not seem to be a critical range of press roll pressures. The normal press roll pressures can be used. Nip pressures in linear inch of face of 72.8 pounds for 22 /2 pound classified paper, 207 pounds for 54 pound Loxco grade, and 41 pounds for 28 pound Rotolox have been considered normal and found satisfactory for use in this method.

The nature of the solids in the web is not a factor in the operation of this method. So long as the range of solids content is maintained, the solids may comprise fiber, coloring matter, filler, hinder, or other materials introduced in the beater. additives may be omitted entirely in the beater and the clay or filler required for the ash content added at the first press.

The advantages of applying the paper treating material to the web by the method herein described are: (a) a more smooth surface paper results because of permissible orientation of the fibers in the solids content during the application process; (b) an increase in tensile strength of the paper by the addition of clay and binder at a point subsequent to the heater; the ability to make a high ash paper without adding clay in the beater, thus eliminating wire wear and recovery costs and the limitations placed on ash content by the present method of adding clay in the beater; (d) elimination of costly doctors, reversing rolls, metering rolls, and the like; (e) elimination of additional power re quired for operating accessory pattern eliminating devices; and (f) increase in traveling speeds of the web and therefore increase in production.

It is within the contemplation of this invention that the paper treating material may be added at the second press 22 by using a smooth roll 32 which functions in the same manner as the roll 28 on the first press.

However, at the second press 22 the tensile strength of the web is higher than at the first press and it is possible for the web to be separated from the felt by guiding rolls 34- and 36 to provide operating space for a smooth coating roll 38 and an applicator roll 40. The coating roll 38 can be used to apply paper treating material to the wire side of the web 10 in much the same limits as applied by the roll 32.

When at the third (reversing) press 36 the solids content of the web 10 is so high that the paper treating material can be applied only if the percentage of solids However, with this method content thereof is very low. Even when so limited, it is difficult to apply the material without making objectionable pattern, and unless conditions are perfectly balanced it will be necessary to also use pattern re moval devices. The means for applying a coating at the third press 26 to the wire side of the web 10 consists of a smooth roll 42, which engages the top roll of the press 26 to form a nip in which a supply pool 44 of paper treating material may be maintained. The top roll of such press is coated with a film of such material and such film is transferred to the web 10 as previously described. if it is desired to apply coating to the top side of the web 10 at the third press 26, a smooth roll 46 runs in engagement with the web 10 and a smooth roll 48 engages the roll 46 to form a nip therebetween in which a. pool 50 of such material may be maintained. The application, however, of paper treating material to the web at the third press is in both instances limited to very narrow tolerances of solids content and great care must be taken to prevent the formation of noncommercially acceptable patterns.

Although only one embodiment of the invention is shown and described herein, it will be understood that this application is intended to cover such changes or modifications as come within the spirit of the invention or scope of the following claim.

I claim:

The method of treating paper consisting of passing a web of paper while between percent to 86 percent water content and supported on a felt, between two rolls, the roll in direct contact with the paper having a smooth web contacting surface, applying by a smooth surfaced applicator roll in contact with the roll directly engaging said web a film of paper-coating material having a solids content of between 35 percent to 50 percent to said last-mentioned roll and transferring said film as deposited on said roll to said web.

References Cited in the file of this patent UNITED STATES PATENTS OTHER REFERENCES Hunter: Tech. Assn. Papers, series 19, pp. 313-319 (1936). (Copy in Div. 67.) Egan: Paper Trade 1., (Copy in Sci. Lib.)

Pulp and Paper, by Casey, vol. I, pp. 460 and 577, pub. by Interscience Publishers, New York (1952). (Copy in Sci. Lib.)

October 25, pp. 49-43.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1598302 *Nov 26, 1924Aug 31, 1926Whitfield Paper WorksMatrix-flong machine
US1921369 *Nov 4, 1931Aug 8, 1933Peter J MasseyMethod of coating paper
US2176418 *May 9, 1938Oct 17, 1939Chas E Francis CoCoating machine
US2208236 *Dec 16, 1936Jul 16, 1940Johns ManvilleMethod of making sheet products
US2243604 *May 5, 1939May 27, 1941Parkinson LeonardDevice for applying films of coating material to paper webs
US2398843 *Jul 11, 1942Apr 23, 1946Combined Locks Paper CoApparatus for coating paper
US2422345 *Aug 2, 1940Jun 17, 1947Carey Philip Mfg CoManufacture of hydraulic cement products
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GB189716315A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3096229 *Oct 29, 1959Jul 2, 1963Riegel Paper CorpCarbon impregnated paper and method of making same
US3115438 *Aug 11, 1960Dec 24, 1963Champion Papers IncMethod of coating paper
US3146159 *Aug 1, 1960Aug 25, 1964Combined Locks Paper CoMethod of coating paper with high solids high viscosity coating in the wet end of the paper making machine
US3231418 *May 5, 1964Jan 25, 1966Combined Locks Paper CoCoating a moving paper web with a coating roller having lower peripheral speed than web
US3293067 *Mar 27, 1963Dec 20, 1966Cons Papers IncProduction of coated paper
US3370590 *Aug 17, 1966Feb 27, 1968Riegel Textile CorpProcess of preventing undesirable loosening or matting in paper for use in sanitary products and the products thereof
US3911174 *May 16, 1974Oct 7, 1975Anglo American Clays CorpMethod of coating flexible sheet material
US4793899 *Jul 23, 1987Dec 27, 1988Beloit CorporationPapermaking machine
US5028457 *Aug 9, 1990Jul 2, 1991Dainippon Screen Mfg. Co., Ltd.Roll coating apparatus and method capable of providing coatings without pin holes
US5152872 *Oct 15, 1990Oct 6, 1992Stone-Consolidated Inc.Couch rolls with suction box for depositing, conveying, applying substance on webs and dewatering; efficiency
US5242545 *May 26, 1992Sep 7, 1993Union Camp CorporationStarch treated high crush linerboard and medium
US7045036 *Jun 28, 2002May 16, 2006Metso Paper, Inc.forming webs in multilayer paper apparatus from raw materials comprising water and fibers, then pressing to drain water and drying heating
DE1227773B *Mar 13, 1961Oct 27, 1966Combined Locks Paper CoVerfahren zum Maschinenstreichen von Papier
Classifications
U.S. Classification162/184, 118/224, 118/227
International ClassificationD21H23/00, D21H23/26
Cooperative ClassificationD21H23/26, D21H23/00
European ClassificationD21H23/26, D21H23/00