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Publication numberUS2661669 A
Publication typeGrant
Publication dateDec 8, 1953
Filing dateFeb 14, 1951
Priority dateFeb 14, 1951
Publication numberUS 2661669 A, US 2661669A, US-A-2661669, US2661669 A, US2661669A
InventorsJr Valentine Friedrich
Original AssigneeBeckett Paper Company
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Process and apparatus for avoiding curl in machine-made paper
US 2661669 A
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Description  (OCR text may contain errors)

Dec. 8, 1953 v v D H, JR 2,661,669

PROCESS AI ID APPARATUS FOR AVOIDING CURL IN MACHINE MADE PAPER Filed Feb. 14, 1951 FELT suns wwgzawiw ATTORNEYs,

Patented Dec. 8, 1953 NT OFFICE PROCESS AND APPARATUS FOR AVOIDING QURL lNMACHDIE-MADE PAPER Application February 14, 1951, Serial No. 210,948

3 Claims.

This invention relates to the art of paper making and is particularly concerned with a process and apparatus for overcoming the natural tendency to curl displayed by machine made paper.

Paper manufactured on conventional Fourdrinier machines displays a marked tendency to curl, invariably in the direction of the Fourdrinier wire upon which it was supported during processing. Particularly in multi-color printing processes such curl prevents the superposition of one color directly over another in exactly the right registration, for the curled, misshapen paper is always distorted, even though slightly, by the rollers of the first color printing. Such distortion is impossible to duplicate exactly at the second impression and therefore one cannot obtain the effect desired from the complementing of colors one printed on top of the other. Also, paper which curls when free to do so is dimcult to handle by mechanical means.

In the past, there have been attempts, at printing establishments athemselvx-zs, to overcome this objectionable tendency of paper to curl. These have been directed to maintaining the atmosphere of the press room at a fixed relative humidity, for example, 50%, at which paper gem erally has been found to display a lesser curling tendency. This has not been found to be the complete answer to press room problems because of the elaborate expensive equipment necessary to maintain the proper humidity, because of the fallibility of such equipment even when in-- stalled, and because of the fact that commercial papers do not always respond satisfactorily to such controls.

The primary objective of this invention is to attack the problem of curl at its source and to manufacture a paper which is free of the curl now exhibited by commercial papers.

The invention is predicated upon the concept of selectively re-introducing small, controlled amounts of moisture to one side only of a paper web, immediately after the web has been dried to a relatively standard water content.

It has been an object and accomplishment of this invention to utilize the basic processes and apparatus of existing paper machines to produce a paper'which exhibits virtually no tendency to curl. The invention will thus be disclosed in the particular environment of a Fourdrinier paper machine, since such machines are in almost universal use, and since the invention can be practiced there with only small alterations in structure and in process steps, but with pronounced improvements in results.

All Fourdrinier machines have in common four sections, 1) a wet end, (2) a pressing section (3) a drier section and (4) a calender section, although in some instances calendering may be omitted in the processing itself. As introduced at the wet end, the paper stock is a suspension of pulp in water. At the wet end of the machine the stool: is deposited on a moving endless belt of wire .cloth, called the Fourdrinier wire, over which the paper constituents travel toward the pressing section. As it passes over the supporting wire, water is drained from the paper web, first by gravity, and later by suction. During this travel, the fibers of the stock align themselves in characteristic pattern. At the end of the wire the paper webhas become self-sustaining sufiicient to be introduced into the pressing section. This portion of the machine is normally constituted by a succession of pairs of rollers between which the paper web travels, while excess water is squeezed out of it. Beyond the bank of pressing rollers are a succession of single-drum, heated drier rollers about which the paper is made to pass successively in a circuitous path. In this portion of the machine endless belts of papermakers felt help absorb Water and maintain an intimate contact between the paper and the surfaces of the respective drier drums, thus.

facilitating the transfer of heat from the drum to the paper and causing the maximum evaporation of water from the paper web. A final set of rollers are called calenders and impart the final desired surface finish to the dried web.

This invention arises from the recognition that the condition of the paper web as it passes from the bank of driers to the calender rolls is such that it is extremely receptive and reactive to only 7 slight moisture introduction. I have discovered that the tendency of a paper to curl can be overcome, and a paper which will remain flat under widely varying humidity conditions canbe produced, by purposefully introducing a small quantity of water in the felt side of the paper after it has been dried. An introduction of small, almost imperceptible amounts of water, immediately following upon deliberate removal of Water from the web, paradoxically greatly affects the properties of the finished product.

It has been determined that the utility of water reintroduced to the travelling web of paper resides in making it available to the felt side of the paper only, i. e., to the side opposite that at which the pulp was supported on the wire in the first section of the Fourdrinier machine. The over-all moisture content of a paper web. at its emergence from the drying section of a Fourdrinier is customarily between /2 70 and 6V This moisture content is sometimes referred to as the equilibrium moisture content of the paper at a given relative humidity, or merely as the atmospheric equilibrium moisture content. The water addition over and above such amount, as contemplated by this invention, is almost immeasurable. Its effect apparently lies not necessarily in its magnitude, but rather in its being applied to one side of the web only, during travel, and at the almost instantaneous interval between the steps of drying and calendering.

I have, in the course of extensive observation of the behavior of paper under controlled conditions of moisture, developed a theory which explains the significant results of my process. Machine-made papers normally contain unre lieved or frozen stresses as a result of having been dried under tension. This increases the directional effect created as the cellulose fibers, carried on the Fourdrinier wire in a watersuspension, tend to align themselves in the di rection of travel. Due to the dragging effect of the moving wire, most of the longer fibers in the bottom layer, or wire side of the sheet, align themselves in the direction of travel, and this effect is accentuated by the loss of shorter fibers from the bottom layer of the sheet through the drainage of water by gravity and by suction. On the upper layer, or felt side, the shorter fibers remain in the web, and the longer fibers, being less affected by the dragging action of the wire, are distributed more nearly at random than are those in the wire side layer. Thus, the upper, or felt side, layer is less unidirectional in character than the wire side.

When the sheet is dried under tension, drying shrinkage is restricted to the cross direction. Since the loss of moisture causes cellulose fibers to shrink greatly in thickness but only slightly in length, the difference in alignment between the fibers in the wire side layer and those in the felt side layer results in different forces exerting themselves along and across the sheet as the web proceeds through the drying process. The wire side layer tends to shrink strongly in the cross direction but very little along the length of the web, while the felt side tends to shrink. as it dries, more evenly in both directions.

Although a sheet of paper dried as described above may lie flat when out off from the web and maintained at the same moisture it contained when released from tension at the end of the paper machine, the different fiber alignment between the fibers of the wire side layer and the felt side layer causes curl toward the wire side if the sheet is dried out in an atmosphere of low relative humidity. The predominant force in this case is the force of contraction of the fibers of the wire side layer, and this force asserts itself most strongly across the web, pulling the upper layer into a curve, toward the wire side.

If one adds moisture to the felt side of the moving web at the end of the drying process, as I have described, the fibers become temporarily limp and flexible, and rearrange themselves so the unequal stresses are relieved. Within a short time the additional moisture briefly present in the felt side is partly absorbed into the other layers of the sheet and partly evaporated to the atmosphere, causing the fibers that had been moistened to shrink slightly, thus counteracting the force caused by the shrinkage of the fibers in the wire side layer. This equalization of strain prevents the accumulation of curling tendencies which inhere in paper processed customarily, and

this condition maintains throughout a much wider range of moisture content than if the sheet had not been so moistened.

In practice, I find that I can substitute, for the last or second-last of the drying rolls of a conventional Fourdrinier, a special chilling roll which contacts the wire side of the web, drawing heat from it and making the web sufiiciently cooler than a moisture-containing surroundings to result in introduction of water to the felt side of the web.

' When I employ a chilling roller, or independently thereof, I find it expedient to utilize an already present source of water, i. e., one of the travelling moisture-laden belts of felt which is used to absorb water from the web during stages of the process. As the felt arrives in the vicinity of the chilling roller, it is both hot and humid as a result of its functions in the drying zone. Its passage over the chilling roll not only causes transfer of moisture from it to the paper web, but also condensation of water from the moisture-laden air entrained between the parallel travelling paper and felt. Bearing thusprecipitated water, the web travels on to the calender rolls for further processing before the added moisture has a chance to undesirably set.

A further determination of this invention is that the control of temperature of the chilling roll additionally contributes to an exact counterbalancing of the inherent tendency of the paper to curl toward its wire side. For given combinations of paper composition, web speed machine dimensions (notably roller size and area of contact between felt and roll), an optimum temperature range exists. Such range usually spans 10 degrees Fahrenheit or more, within which curl is neutralized so that a paper is produced which will lie flat under normal tions of use. Attempts to cool the roll, and the web passing over it, to lower temperatures than the experimentally determined optimum ranges have resulted in a curl of significant magnitude in the opposite direction, that is, a curl toward the felt side of the paper web.

Thus, by this invention a paper can be produced which has curl characteristics more than normally tolerant or independent of wide variations of conditions of transportation, storage and use.

Other objects and advantages of this invention will be apparent from th following description of the drawings in which one typical arrangement for controlled introduction of moisture is employed.

Figure l is a diagrammatic view of a portion of the drying section of a Fourdrinier paper machine equipped for the practice of the invention.

Figure 2 is a diagrammatic view similar to that of Figure l and discloses a variation in the practice of the invention in a modified type of dryer.

Figure 3 is a diagrammatic sectional view of the chilling roller of Figures 1. or 2, on line 3-8 of either, showing an arrangement by which the drum may be maintained within a definite temperature range.

The conventional mechanism for producing a self-sustaining web from paper pulp and water,

forming no part of the present invention, is not Generally, the drying section of a Fourdrinier machine will contain more than the rolls which are shown, and Figures 1 and 2 represent only the terminal portion. or" the drying section. Ihus, by the time the web reaches the drying station, much of the excess Water in the web will have been already removed, and successive steam heated rolls, W, H and 52, rotating in the direction of web travel, continue the extraction of moisture from the web in cooperation with belts i 3 and Hi ofipapermakers felt.

As indicated, the rolls are disposed at two levels, or tiers, and are staggered with respect to each other. The paper web is made to travel a tertuous path over successive rolls, alternating from. the top to the bottom tier, and progressing from left to right in the figures. The path thus defined results in an appreciable contact, with the steam heated rolls, of first the wire side, th n the felt side, etc., of the paper. For purposes of illustration, it is assumed that wire side !5 of the paper web 9 lies adjacent the warm roller surface of roller ii of the upper tier.

As the web travels through the drying zone, alternating faces of the web areintermittently contacted with an endless belt of papermakers felt. This contact is simultaneous, or nearly so, with the winding about of the paper on drying rolls. One such belt 53 is disposed above the upper tier of rolls and in the drawings it will be seen that as the paper embraces portions of the circumference of roll it of the upper tier, the felt side of the paper, it, opposite the wire side it, is contacted by the felt belt i3. An additional belt i i of papermakers felt is disposed beneath the lower tier of drying rolls, of which rolls it and iii are shown. As to rolls H3 and i2, the felt side it of the web 9 lies next adjacent the drying roll surface and wire side 55 is exposed to a felt sur face.

Belts l3 and Id, of course, travel, in the same direction. as the web of paper and at the same speed. The belts themselves are mounted on rollers it? which are disposed to festoon the respective belts in such a way that the traveling felt engages the web of paper over substantial circumferential portions as the paper web passes over corresponding drying rolls.

Rolls ii ii and 82 are each steam heated, as is conventional in a Fourdrinier machine. After leaving roll l2, in Figure l, the web of paper next passes between roll iii and the moving surface of belt 93. In the conventional machine, a roll in the position of roll i?) would be steam heated but in accordance with the present invention roll it! is water chilled to induce introduction of water from moisture-laden belt i3, onto felt side it, as by condensation. Water is thus deposited from belt !3 onto the felt side E6 of paper web 9, in, as will be seen, controlled amounts.

The web proceeds from the drying station of a Fourdrinier machine to a calendering portion after which it is reeled for shipment or storage. To

maintain proper tension between the last web processing roller, e. g., roll 9, as shown in Figure 1, and the calender, a roll 2! of lesser diameter than rolls iii, ll, 52 and i9 engages the web of paper and helps hold it taut after leaving chilling roll 19.

I have found that it is generally desirable to apply cooling water to the interior of this roll to avoid any abrupt change in temperature.

Some Fourdrinier machines are of such construction. that the felt side of the paper resides in contact with the last roller of the dryer section rather than the wire side in the arrangement shown in Figure 1. In such event the construction shown in Figure 2 may be used.

In Figure 2 the construction is similar to that of Figure 1 except that water-chilled roll is is second from last roll in the drying section proper, in order to nduce water introduction on felt side It of paper web 9. In such event the last roll of the dryer section may be decommissioned, or may be allowed to run at room temperature.

' Figure 3 discloses the details for the temperature control of chilling roll I9, of either Figure l or 2. As shown, roll 59 has trunnions .23 and 2s. Paper web passes over the top of roll It; above it is endless belt I 3 of papermakers felt exposing its moist surface to web Q.

Roll iii is hollow and has a hollow trunnion 2 which is connected to a water outlet 25 ior accumulating overflow from the interior of roll it. In typical practice, the roll 19 will be about half full of water, thelevel rising no higher than the overflow provided by trunnion 24 and its outlet conduit. There is disposed in conduit 25 a temperature responsive member 25 which is connected to water valve 21 in inlet 28,, in. any suitable manner.

Inlet line 28 passes through hollow trunnion 24 into the interior of roll 19. Water normally passes into the roll continuously, or at periodic intervals, so as toresult in corresponding overflow and discharge of water into the vicinity of thermo-controller 2%. The thermo-controller 26 responds to the temperature conditions inside roll I 9 but is mounted externally thereof so as not to interfere with its rotation, and is free of the turbulence of the water produced by such rotation. Water passes through inlet line 28 to a spout 29 disposed at a point adjacent the inside wall of the roll Is and near its lowest point. Valve 2'! however, responds to temperature measurements of thermo-controller 26 to admit greater quantities of cooling water to the interior of roll it as the temperature measurements indicate that the overflow is too hot.

As the drying rollers are usually maintained at a temperature of from 220 to 230 F. by means of steam passed through them, roll it will have a chilling effect at any effective temperature below 220 F. However, in order to remove or neutralize the characteristic curl toward the wire side of the paper, it has been found desirable to maintain the temperature of the chilling roll appreciably below the boiling point of water.

The exact optimum temperature of the chilling roller varies from one paper to another, but preferably is between F. and 200 F. For purposes of illustrating typical practices of the invention the following detailed examples are given.

On a given machine, having a web travelling at 400 ft. per minute, a ream of 25 x 38 inch lithographic paper weighing fifty pounds, exhibited the following characteristics at the indicated conditions:

A ream of the same size sheet weighing sixty pounds, with a speed of travel in the machine of 390 ft. per minute, gave the following results.

accmce Temperature of Chilling Boner Curl Characteristic As indicated previously, the exact temperature at which it is desirable to maintain the chilling roller depends upon the weight and composition of the paper, the speed of travel of the web, and the diameter of the rollers and the amount of felt wrapped around the chilling rollers of each particular machine.

But generally speaking, chilling to the temperature of substantially 150 to 170 F. tends to minimize the tendency to curl of almost any ordinary paper, and the tendency may be eliminated entirely by testing samples of paper produced by the machine and adjusting the exact temperature of the chilling roller in conformity with the principles which have been disclosed and discussed.

Having described my invention, I claim:

1. The method of manufacturing, on a Fourdrinier paper making machine, a web of paper which does not display a tendency to curl, the said method comprising, forming a web of paper on a wire of a Fourdrinier machine, progressively drying the paper in the Fourdrinier machine by contacting alternate sides of the paper with drying rolls heated to a temperature higher than approximately 200 F., while respectively opposite sides of the paper are simultaneously engaged by a moisture absorptive papermakers felt, and continuing the drying operation until the web of paper contains less than about 6 /2% of moisture, then passing that side of the paper web which was initially laid upon the wire of the Fourdrinier machine over a substantially dry surface of a roll which is maintained at a temperature in the range of approximately 150 to 170 F., and simultaneously contacting the opposite side of the portion of the paper engaging the said roll with the said papermakers felt of the Fourdrinier machine while the said papermakers felt is in a hot and humid condition, the specific temperature within the said range being so selected that a paper which is substantially free from the tendency to curl is produced.

2. In the process of manufacturing paper wherein a Fourdrinier wire and a moisture absorptive felt are employed to produce a paper web having a wire underside and a felt topside, the successive steps of forming a paper web upon a Fourdrinier wire, passing the said web over a series of drying rolls heated to a temperature above the boiling point of water and in intermittent contact with a belt of the said papermakers felt under such conditions as to reduce the moisture content of the paper web to not more than about ti and then selectively introducing a small quantity of moisture into the felt side of the said paper web by passing the said web over a substantially dry surface of a chilling roll which is maintained at a temperature within the range of approximately to 200 F., with the wire underside of the paper web in direct contact with the surface of the said chilling roll, and simultaneously engaging the felt side of the paper directly opposite the portion of the paper contacting the said roll with the said belt of papermakers felt while the papermakers felt is hot and humid, the specific temperature within the said range being so related to the moisture conditions of the said papermakers felt that a paper which is substantially free from the tendency to curl is produced.

3. In a Fourdrinier paper making machine, a wire for forming a web of paper, a succession of drying rolls about which a moisture-laden travelling web of paper formed on said wire is festooned, the rolls of the succession being so arranged that some of them engage the underside of the said paper web which was initially in contact with said wire, and the remainder of said rolls engage the topside of said web, means for maintaining the temperature of said drying rolls albove approximately 200 F., a pair of endless papermakers felts having portions travelling with the web for respectively engaging those portions of the web which are in engagement with said. drying rolls, and means at the end of said succession of drying rolls for reducing the tendency to curl which the paper would otherwise display, comprising, a chilling roll positioned to engage the wire side of the paper, means for maintaining the temperature of the said chilling roll substantially below 200 F. but above substantially 80 F., and means constituting a portion of one of said papermakers felts for engaging the web of paper as it passes over the said roll to selectively impart a small quantity of moisture from the felt to the felt side of said web.

VALENTINE FRIEDRICH, J'R.

References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 1,595,473 Minton Aug. 10, 1926 1,900,166 Dix Mar. 7, 1983 1,962,882 Shotwell June 12, 1934 2,091,805 Chuse Aug. 31, 1937 2,214,641 Massey et al Sept. 10, 1940 2,314,797 Morris et a1 Mar. 23, 194.3 2,337,163 Milne Dec. 21, 1943 FOREIGN PATENTS Number Country Date 663,948 France Apr. 16, 1929 OTHER REFERENCES Montgomery, Controlled Conditioning of Pap er Paper Trade Journal, March 13, 1941, pages 2 o 30.

Patent Citations
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US1900166 *May 10, 1930Mar 7, 1933Lawton A DixDrier head
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2890037 *Nov 10, 1954Jun 9, 1959United States Steel CorpMethod and apparatus for continuously cooling metal strips
US2994634 *Jan 2, 1958Aug 1, 1961Kimberly Clark CoManufacture of cellulosic products
US3067586 *Mar 29, 1961Dec 11, 1962Offen & Company BProcess and apparatus for chilling printed webs
US3077673 *Oct 7, 1959Feb 19, 1963Aulson Tanning Machinery CompaProcess for drying and flexing of leather
US3191312 *Apr 16, 1962Jun 29, 1965Svenska Flaektfabriken AbMethod of uniformly moistening paper and like hygroscopic web material
US3626480 *Jul 31, 1970Dec 7, 1971Kuraray CoDevice for heating and cooling plastic sheets
US3982056 *Oct 15, 1974Sep 21, 1976International Paper CompanyMethod for improving the printability characteristics of gloss calendered paper
US4474643 *Sep 12, 1979Oct 2, 1984Albany International Corp.Method for controlling the moisture content of a fiber web and apparatus for accomplishing the method and a paper making machine for accomplishing the method and a paper making machine with an apparatus for accomplishing the method
US5291666 *Apr 23, 1993Mar 8, 1994International Paper CompanyApparatus for drying roll material
US5470436 *Nov 9, 1994Nov 28, 1995International Paper CompanyRewetting of paper products during drying
US5471847 *Jan 11, 1995Dec 5, 1995W. R. Grace & Co - Conn.Web cooling device
Classifications
U.S. Classification162/207, 34/392, 162/290
International ClassificationD21F5/02
Cooperative ClassificationD21F5/02
European ClassificationD21F5/02