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Publication numberUS3257734 A
Publication typeGrant
Publication dateJun 28, 1966
Filing dateSep 29, 1965
Priority dateSep 29, 1965
Publication numberUS 3257734 A, US 3257734A, US-A-3257734, US3257734 A, US3257734A
InventorsJames L Barlow, John D Boadway
Original AssigneeCons Paper Bahamas Ltd
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method for controlling tension in supported sheet material
US 3257734 A
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Description  (OCR text may contain errors)

June 1966 J. D. BOADWAY ETAL 3,257,734

METHOD FOR CONTROLLING TENSION IN SUPPORTED SHEET MATERIAL Filed Sept. 29, 1965 5 Sheets-Sheet l PATENT AGENT 3 Sheets-Sheet 2 Awimbd 2051i...

J. D. BOADWAY ETAL METHOD FOR CONTROLLING TENSION IN SUPPORTED SHEET MATERIAL C. H m N m6 Nmm n w y fimqo mu #6 G a W H I a Q. a \1 H fi N o a 26 m Z w m w w w G RS m o. m no a .I.\ 0N 8 June 28, 1966 Filed Sept. 29, 1965 J1me 1966 J. D. BOADWAY ETAL 3,

METHOD FOR CONTROLLING TENSION IN SUPPORTED SHEET MATERIAL Filed Sept. 29, 1965 5 Sheets-Sheet 5 ATTORNEY United States Patent 3,257,734 METHOD FOR CONTROLLING TENSION IN SUPPORTED SHEET MATERIAL John D. Boadway and James L. Barlow, GrandMere, Quebec, Canada, assignors to Consolidated Paper (Bahamas) Limited, Nassau, Bahamas Filed Sept. 29, 1965, Ser. No. 491,360 4 Claims. (CI. 34-18) This invention relates to a method for controlling shrinkage in a paper web during the drying stage in paper manufacture. This application is a continuationin-part of application, Serial No. 227,010, filed September 28, 1962.

It is known that if paper is allowed to shrink freely while drying certain desirable properties are imparted to the paper.

A paper web, after wet pressing and as it enters the dry end of the paper machine, has a moisture content of approximately 65%. If the web is unrestrained as it dries to a moisture content of 45%, it will shrink very little. However, on drying from 45 to 9% moisture, the web may shrink as much as 12%.

A sheet, which is allowed to shrink while drying will, after drying, exhibit stretchability or elongation before rupture of as much as 15%. On the other hand, the stretchability of a similar sheet dried under restriction and tension, may be as low as 2%.

It is well recognized that a paper of substantial stretchability or extensibility possesses advantages. For example, stretchability allows the paper to withstand impact forces to a higher degree. It also permits papers, such as wrapping papers, to conform to the shape of the object which it carries, thus distributing the load and minrnizing breakage. Therefore, there is an advantage in allowing the paper to shrink during at least a part of the drying procedure thereby to impart a high degree of stretchability to the paper.

The conventional drying procedures are not readily adaptable to accomplishment of this shrinking during drying. This is mainly due to the manner in which the drying cylinders are driven and the manner in which the paper is transported through the drying section of the paper machine. These conventional procedures are such that the paper web does not have the opportunity to shrink but rather is continually subjected to a tension or draw which tends to adversely affect the stress-strain characteristics of the paper.

The amount of shrinkage involved, however, is generally small by the time this is spread over a large number of drying cylinders, so that the percentage speed change between consecutive cylinders becomes exceedingly small. To affect and control this shrinkage, the drying mechanism for these dryers would, therefore, need to control an extremely small differential between the dryers. Furthermore, web tension must always be maintained close to zero so as to permit a uniform shrinkage to take place; this means, that little or no variation in this differential can be tolerated.

A mechanical system of gears would be too crude to handle such a requirement. In the case of using electric drives on the individual dryers and controlling electronically the required differential speed between the dryers, an error generally has to exist before the electronic circuitry will make a correcting adjustment. This creates a temporary fluctuation which is in itself corrected for by an over-compensating adjustment so as to maintain the correct average condition. All this then gives rise to fluctuations of a cyclic nature. Since a tensionless web can lead to web wrinkling and wandering, the minimum allowable tension should be close to zero tension;

3,257,734 Patented June 28, 1966 ice however, because of these cycles, a mean tension is maintained which is considerably above zero. As mentioned above, this is undesirable from a paper quality Y point of view.

It is an object of this invention to provide a method for drying a paper web whereby shrinkage thereof may be substantially and accurately controlled and desirable characteristics thereby imparted to the final paper product.

One manner of controlling tension in a travelling paper web would be to store one or more lengths thereof at very low tensions between a pair of the drier rolls, whereby short term dilferential speed variations could be absorbed without creating large changes in tension. It will be apparent that this storage may be effected by some form of web takeup. One possibility would be the deflection or diversion of the web from the straight path between the pair of rolls by means of a take-up roll which would be lightly loaded in order to maintain a light tension. A major drawback of such a means, however, would be that such a take-up roll would, because of its inertia, resist sudden changes in position which it would need to do so as to follow the short term variations in differential speed.

The present invention contemplates deflecting a paper web from its normal straight line path between two supporting drying cylinders or rolls and maintaining such web in a state of tension, by means of a fluid jet. In accordance with the invention, such a fluid jet provides a force sufficient to create a deflection in the web, which deflection creates a slight tension in the web. The greater the distance of deflection of the web, the greater is the length of web stored between the two transport points. Thus, with fluctuations in the differential speed between the two points, the-re will be a fluctuation in web deflection, but only minor fluctuations in the web tension.

The invention will be described with reference to the accompanying drawings, in which FIGURE 1 is a side elevation, partly in diagrammatic form, of an apparatus in accordance with the invention,

FIGURE 2 is a partial plan view of a jet forming device,

FIGURE 3 is a graph indicating the type of relationship existing between the deflection and the web tension for various fluid pressures,

FIGURE 4 is a graph showing the relationship between shrinkage in a paper web for a given loss in moisture and paper tension,

FIGURES 5 and 6 are diagrammatic side elevations of modified forms of apparatus, and

FIGURES 7 and 8 are plan views of alternative forms of jet producing devices.

Referring to FIGURES 1 and 2, 10 is a wet paper web travelling over a pair of drier rolls or cylinders .11. The web has been formed in conventional manner on a Fourdrinier wire 1 supported on breast roll 2, and couch roll 3, and fed with stock from head box 4. Standard presses 5 may be provided. The normal straight line path of the web between the cylinders 11 is indicated at 12.

In accordance with the invention, the portion 13 of the web between the cylinders is deflected as shown by means of a fluid jet 14 produced by a jet forming device 15 which may comprise a pipe 16 supplied with fluid, such as air, under pressure, and having a row of openings 17 therein.

The jet force may be roughly estimated at PA per unit width where P is the fluid pressure and A is the area of the jet opening or openings per unit width. The variation of the jet force with respect to distance from the point of issuance is complex. Up to a distance of 12 inches, this force has been found to be approximately constant.

The force from the jet acts against the sheet which gives rise to a tension (t) in the web. It will be apparent that this tension (t) has a component which acts directly against the jet force (PA) and this component is equal to t sin 0. Since there are two such components ea'ch acting on an opposite side of the jet, then (1) PA=2 (t sin For small angles of 0 we can let d 2d sin z and 2d PA= 2t (2) Therefore:

t PAL where P=air pressure per unit area L=length of span between transport points A jet opening area per unit width d =deflection of web t=web tension per unit width Practical experiments have indicated that the relationship is:

(3) t: PAL

4:43 d 0.845 the units employed being pounds and inches.

By way of example, in a typical design for a paper machine 12 feet wide, 500 cubic feet per minute of air would be supplied at a pressure of 10 inches of water to a 4 inch diameter pipe 16 running across the machine and having a single row of A; inch diameter holes 17 therein /2 inch apart.

Thus, for a straight line span of 40 inches, air issuing from such a row of holes under the above conditions would deflect a web of paper approximately 4 inches and the tension in the web would be in the order of 0.3 pound per foot of width. This deflection is equivalent to a storage of approximately 0.8 inch of paper. FIG- URE 2 illustrates the experimental relationship between t and d for other air pressures (P).

In the case of a paper machine operating at 1000 feet per minute, its drive is capable of causing a speed variation of 0.1%, the maximum duration of which would be in the order of 2 seconds. Under these conditions, the sheet deflection would alter from 4 inches to 2% inches in the case of an increase in tension and 4 to inches in the case of a decrease in tension (i.e., increase in slackness); the tension changes corresponding to these deflections would be from 0.3 to 0.44 and 0.3 to 0.25 lb. per linear foot respectively. On the other hand, if the web with straight transfer is to be kept under sufiicient tension so that a of a percent change in draw would not produce slack paper it would have to be kept at a tension of, say, at least 5 lbs. per foot of width with a tension varying up to 20 lbs. per foot of width. Such tensions would prevent or hinder any shrinkage of the web as it dried.

The present invention is thus capable of providing storage of relatively short lengths of paper web which can be made smoothly available as required to compensate for short term fluctuations in the difference in speed between successive dryers. This storage, including the range that it might fluctuate in an effort to compensate for these speed variations, is under conditions of low web tension (very much lower than those presently used) and this tension is in a range which will allow the paper to shrink quite freely (see FIGURE 4, top part of curves) and thus improve the final properties of the paper. The invention makes it possible to maintain a tension which is as low as possible while avoiding the region of zero tension where wrinkling of the web may take place. Present practice not only prevents shrinkage of the paper but rather stretches it, with resultant loss in certain strength properties (see FIGURE 4, lower part of curves).

A further advantage of the invention will become apparent by examination of FIGURE 4. Since it is possible to operate at a very low tension, a greater elongation potential is now available as an additional last resort compensation for speed variations. This provides an increase in the safety factor in terms of paper rupture. The deflection feature (plus the remaining shrinkage potential) is capable of compensating for increased web slackness. Also to be noted is the self-adjusting feature of the inter-action between the shrinkage and the decreasing tension with increasing deflection. That is, as the deflection (d) increases in an effort to take up slack, the tension (t) decreases (since it is a function of the angle 0, or d-Equat-ions 1 and 2 above), and this allows more shrinkage to take place and itself take up some of the slack.

While this invention is very useful in absorbing short term drive fluctuations, it is somewhat limited in its ability to absorb long term variations or a slight drive maladjustment. This would be particularly true for webs where very small dimensional changes in the width are accompanied by large tension changes, for in this case, the paper stored by this deflection technique would be rapidly consumed. However, the invention has another feature which allows it to be used as an indicating or control device which can be used to control more effectively the guiding mechanisms which originated the long term variation. Equation 3 indicates an empirical relationship existing between the deflection (d) and the web tension (t). As mentioned above, this has been plotted in FIGURE 3 for various air pressures P. Since the position of the web is dependent on web tension, and since its position can be detected by various known means (e.g., light beams, mechanical devices) the signals from the positioners can then be used to regulate the differential speed of controls of the web transport means. Thus, these troublesome long term variations can be ironed out leaving the remaining deflection of the web to smooth out the short term variations for which it is well suited. Where it is not necessary to employ this control device, the web position detector might still serve as a simple indicator of web tension.

It will be apparent that the fluid jet employed to deflect the web could at the same time be used for any desirable processing of the web such as, for instance, in the drying, heating or chemical treatment of it. To ensure uniform processing, it may be desirable to allow the jet to impinge alternately on opposite sides of the web. In its application to the drying of paper, this may readily be effected, as shown in FIGURE 5, wherein the portion 18 of the web between a pair of dryers 19 and 20 is subjected on one side to the action of jet 21 and the succeeding web portion 22 between the pair of dryers 20 and 23 is subjected on the other side of the action of a jet 24.

It should be observed that a jet of, for instance, air, would result in other effects in addition to drying. Thus, the drying phenomena could be accompanied by a cooling effect resulting from the evaporation of water in the web, and this in turn would induce further shrinkage of the web which would further enhance the properties of the final paper.

FIGURE 6 illustrates another modification of the invention wherein the web 25 between two drier rolls 26 and 27 is subjected to a jet 28 and a succeeding jet 29 on the opposite side of the web whereby zigzag deflections 30 and '31 are produced. This results in additional storage of the web.

It will be obvious that the jet forming device may take a wide variety of forms. Instead of a row of holes in a pipe, as shown in FIGURE 2, a single continuous slot 32 may be provided in a pipe or like header 36, as shown in FIGURE 7. Another alternative means is shown in FIGURE 8, wherein a row of separate nozzles 34 are provided. It will be understood, however, that the word jet as employed in this specification and appended claims, is intended to include a jet formed by means of a continuous jet opening extending from side to side of the web or one formed by means of a series of jet openings arranged in a row.

The type of fluid employed to create the jet will vary in accordance with surrounding circumstances. Generally speaking, the fluid will be gaseous. Air is a logical choice and would fulfill many conditions of use, particularly since compressed air is readily available and relatively inexpensive to supply. Steam may be employed. Other gases, depending upon the need for chemical treatment of the web, may be employed. In other instances, a liquid jet of, say, water, may be employed. A liquid jet containing a coating composition or other chemical composition may be employed.

We claim:

1. A method of manufacturing paper which comprises forming a wet paper web on a fourdrinier wire from pulp stock, directing said wet web onto a pair of driven dryer cylinders, drying said web by engagement with said cylinders while applying continuous travelling movement to said web by driving said cylinders, each said cylinder having fluctuations in the speed thereof diflering from those of the other said cylinder, said web normally assuming a substantially straight line path between said cylinders, and reducing the fluctuations in tension of said web as a result of said diflerential cylinder speed fluctuations by applying a gaseous jet from an elongated jet opening Z0116 to one surface of said web between said cylinders and extending transversely from edge to edge of said web to deflect from said straight line path a length of said web between said cylinders, and controlling the extent of deflection of said deflected length to compensate for said differential cylinder speed fluctuations.

2. A method of manufacturing paper as defined in claim '1, wherein the extent of said deflection of said web is controlled in accordance with the formula PAL where t is web tension per unit length, P is gas pressure per unit area, L is the length of the web between said cylinders, A is the area of said jet opening zone per unit width, and d is the extent of deflection of said Web.

3. A method of manufacturing paper which comprises forming a wet paper web on a fourdinier wire from a pulp stock, directing said web onto a plurality of driven dryer cylinders, drying said web by engagement with said cylinders while applying continuous travelling movement to said web by driving said cylinders, each said cylinder having fluctuations in the speed thereof diflering from those of the other of said cylinders, said web normally assuming a substantially straight line pat-h between each pair of successive cylinders, and reducing the fluctuations in tension of said web as a result of said differential cylinder speed fluctuations by applying a gaseous jet from an elongated jet opening zone to at least one surface of said web between each pair of successive cylinders and extending transversely from edge to edge of said Web to deflect from said straight line path a length of said web between each said pair of cylinders and controlling the extent of deflection of said deflected length to compensate for said differential cylinder speed fluctuations.

4. A method of manufacturing paper as defined in claim 3, including the step of applying a gaseous jet to each surface of said web, said jets being applied to spaced portions of said web whereby said web is deflected in opposite directions from said straight line path.

References Cited by the Examiner UNITED STATES PATENTS 1,154,560 7/1915 Bryant 34156 2,393,243 1/1946 Franz 34156 X 2,678,173 5/1954 Phelps 242-147 3,199,214 8/1965 Osban et al. 34156 X ALDEN D. STEWART, Primary Examiner.

D. A. TAMBURRO, Assistant Examiner.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1154560 *Jan 23, 1915Sep 21, 1915Asa T BryantDrying-machine.
US2393243 *Oct 6, 1943Jan 22, 1946Western Electric CoStrand handling apparatus and a method of handling strands
US2678173 *Dec 29, 1950May 11, 1954IbmTape feed mechanism
US3199214 *Oct 13, 1961Aug 10, 1965American Cyanamid CoMethod of treating wet moving tow bands of filamentary material
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3370359 *May 10, 1965Feb 27, 1968Beloit CorpWeb drying method and apparatus
US3496648 *Mar 18, 1968Feb 24, 1970Offen & Co Inc BWeb damping nozzle system
US3786574 *May 26, 1972Jan 22, 1974Eastman Kodak CoMethod for removing water from tow
US3910320 *Dec 13, 1973Oct 7, 1975Eastman Kodak CoTow dewatering jet device
US4596632 *May 25, 1982Jun 24, 1986Appleton Papers Inc.Apparatus and process for a decurling system
US5072527 *Jun 6, 1990Dec 17, 1991Loomie Leo SLength of textile fabric
US6024836 *Dec 20, 1996Feb 15, 2000Voith Sulzer Papiermaschinen GmbhProducing a pulp web, e.g., a paper web, in a paper production machine
US7067039 *Jan 8, 2003Jun 27, 2006Metso Automation OyAdjusting speed variation ; measuring moisture profile ; drawing windows; controlling tension
Classifications
U.S. Classification34/422, 34/118, 34/114, 162/207
International ClassificationD21F1/36
Cooperative ClassificationD21F1/365
European ClassificationD21F1/36B