Background of the Invention
In the typical papermaking machine, an aqueous suspension of fibers is transformed into a paper web as it is processed through the different sections of the machine. One section of the papermaking machine is the dryer section wherein a wet paper web is passed about and held in intimate heat transfer relation with upper and lower arrays of heated cylinders in order to remove water from the paper web. The dryer section normally includes an upper and lower array of heated cylinders arranged and spaced in staggered, parallel rows which have a solid imperforate surface for contacting the paper web. Several dryer sections may be found in a papermaking machine in series and stages. The paper web is passed generally to and fro between the arrays of dryer cylinders in a generally serpentine manner to ensure that both sides of the paper web contact the cylinders. As the paper web passes over the dryer cylinders, it is held in intimate heat transfer contact therewith by a belt, commonly referred to as a dryer felt or dryer fabric which has been made endless by techniques which are well known in the field of papermaker's felts and clothing.
In the past, dryer fabrics generally have been substantially impervious structures of either woven or needle construction. However, the impervious structures, commonly known as dryer felts, do not ventilate sufficiently and thus serve to confine heated vapors in certain "pockets" created in the dryer section which cause uneven drying and affect paper quality. Thus, the trend is toward open weave fabrics which have been found to have desirable characteristics and many non-woven structures, such as needle felts, plastic perforated and helical belts, and the like have also been found suitable due to their increased permeability. Typically, these plastic, non-woven fabrics have yielded permeabilities as high as a thousand cublic feet per minute.
The non-woven plastic helical fabric is desirable because it has fewer if any "knuckles," as in the case of woven fabric, and thus provides increased surface area for contacting and holding the paper. This paper supporting surface is also smoother and reduces markings on the paper. The plastic material and belt construction hold up extremely well under the stresses encountered when traveling endlessly at high speeds, typically 3000 fpm, about the belt rollers in contacting the paper web.
The high permeability of non-woven plastic belting provides increased pocket ventilation and hence drying, but can also lead to increased fluttering of the paper web sheet against the dryer fabric through a phenomena known as air "pumping." This is due to frictional drag on the air surrounding the moving fabric which causes the air to move with the fabric. As the fabric contacts the cylinders or belt rolls, this air is forced through the fabric with the air movement away from the roll or dryer at a converging nip and toward the roll or dryer at a diverging nip. The effect of these forces is the net inflow of air into a dryer pocket, resulting in an outlow of air at the front and back sides of the machine. This turnover of air or air "pumping" is appreciable with highly permeable fabrics travelling at high speeds which can cause disruptive sheet flutter. If a highly permeable dryer fabric is operated at high speeds with a paper web of low strength, the paper web may break, be damaged, or be marked by fluttering against the fabric.
Heretofore, there has been no practical manner of varying the permeability of the basic fabric and, thus, provide fabric for a complete range of applications and control sheet flutter. For example, a dryer section closest to the wet section of a papermaking machine typically requires a fabric characterized by low permeability owing to its relative weak strength of the paper at this stage. High permeability is desired at dryer sections at the latter drying stages and for heavier paper grades. Finer paper grades do not contain as much water and thus do not require a fabric of high permeability nor is such desired since paper flutter of the light sheet is likely.
In an unrelated use, the wire mesh openings of a wire conveyor belt have been obstructed by plastic rods and the pressure of freezing air flow therethrough increased to minimize the variability of the air flow and provide the the result of uniform freezing of layered food conveyed thereon in U.S. Pat. No. 4,186,566, which is directed to apparatus for quick freezing foods.
Accordingly, an important object of the present invention is to provide a construction for a plastic non-woven dryer fabric for a papermaking machine and method by which a desired permeability characteristic may be built into the fabric.
Another important object of the present invention is to provide a non-woven dryer fabric and method having a permeability ranging from as low as 50 to as high as 1000 cfm.
Yet another important object of the present invention is to provide a plastic non-woven dryer fabric with a closed mesh which advantageously withstands the high stresses and temperatures on a papermaking machine.
Still another important object of the present invention is to provide a non-woven polymeric dryer fabric having a closed mesh to control sheet flutter and provide a smooth surface to dry and produce very fine paper.
Yet another important object of the present invention is the method of constructing a basic dryer fabric wherein the permeability of the fabric may be subsequently altered to provide a fabric having a desired permeability for a particular application.
Summary of the Invention
According to the present invention, the above objectives are accomplished by providing a non-woven dryer fabric which includes a plurality of helixes formed from a polymeric material having sufficient plasticity to withstand the stress of continuous travel about belt rollers and heated cylinders on a papermaking machine without permanent deformation or heat damage. The helixes are joined together by pintle means and the loops of the helixes are closed by means of filler strands of synthetic material which are inserted in the helix loops which can be utilized according to the method to produce a complete range of fabric permeabilities suitable for any papermaking application. The strands may be advantageously heat treated to expand and substantially fill the helical loops for maximum fabric closure and low permeability characteristics. Alternately, any one of a complete range of permeabilities may be had according to the filling technique to provide fabric for any papermaking application. The polymeric helixes and strands may be sealed together at the edges of the dryer fabric by passing a hot knife along the edge and applying cement to make an integral fabric structure.
Brief Description of the Drawings
FIG. 1 is a perspective view illustrating a dryer section of a papermaking machine incorporating a non-woven dryer fabric constructed in accordance with the invention;
FIG. 2 is a top plan view of a dryer fabric constructed according to the present invention;
FIG. 3 is a perspective view illustrating a dryer fabric constructed according to the present invention;
FIG. 4 is a schematic elevation illustrating a dryer fabric constructed according to the present invention which is illustrated as pressing a paper web against a heated cylinder of the dryer section of a papermaking machine;
FIG. 5 is an elevation illustrating a dryer fabric according to the present invention and means of closing the open mesh portion of the fabric by heat treatment of a filler; and
FIG. 6 is an elevation illustrating an alternate dryer fabric and heat-treated filler therefor.
Description of a Preferred Embodiment
The invention relates to a method and construction of a dryer fabric for a dryer section of a papermaking machine. Since such papermaking machines are well known in the art, only so much of a papermaking machine as is necessary to an understanding of the invention will be illustrated.
Accordingly, FIG. 1 is a simplified view of a portion of a dryer section of a papermaking machine wherein a continuous sheet-like web W of paper material is traveling from left to right. Several of such sections may be utilized in succession to dry the paper in stages. The dryer section includes an upper and lower array of horizontally disposed heated dryer cylinders which may be either of a perforated or imperforated construction. The upper array of heater cylinders includes cylinders 10, 12 and 14 with the lower array including cylinders 16 and 18. The continuous web of paper is received from the press section of the machine and is passed in a serpentine manner about the dryer cylinders as illustrated. The web first passes over and about upper cylinder 10, under cylinder 16, and then over cylinder 12 and so forth in a serpentine manner until it leaves the dryer section of the papermaking machine. Water and other fluids within the paper web are evaporated due to the paper contacting the cylinders.
The web W is guided through the dryer section and held in contact with the heated cylinders 10, 12, and 14 by means of an upper fluid permeable dryer fabric or belt 22, and a lower fluid permeable belt 24 guides and holds the paper web in contact with the lower cylinders 16 and 18. The dryer fabrics 22 and 24 are identical in their fabric construction as made in accordance with the present invention as will be more fully explained hereinafter. By contacting the paper Web W, the dryer fabrics press and maintain the web in intimate heat transfer relationship with the dryer cylinders whereby the cylinders remove water or other fluids from the web.
Felt rollers for the dryer fabric are provided on the machine such as 26 for the upper fabric and 28 for the lower fabric. The felt rollers maintain sufficient tension on the dryer fabric to ensure that the paper web W is maintained in good heat transfer contact with the dryer cylinders.
The drying process is outwardly from the heated cylinders through the paper web and through the dryer fabric. The "pockets" referred to in the background material are typically created in the enclosed areas bounded by the dryer fabric, paper web, and the heat cylinders, for example, area 25 bounded by fabric 22, cylinder 16, and the web W in FIG. 1. Accordingly, the dryer fabric must have a sufficient permeable construction in order to ventilate these pockets. But the permeability of the fabric should not be so high that the previously described disruptive sheet "flutter" between the paper web and the dryer fabric can occur whereby marking of the paper and derrogation of quality result.
In conventional woven dryer fabrics, dryer fabric construction is described in terms of yarns or filaments extending in the machine direction (the direction in which the web travels) and yarns or filaments extending in the cross-wise direction (across the width or transverse to the direction in which the web travels).
Referring now in more detail to the present invention, a dryer fabric 22, 24 is illustrated in FIG. 2 wherein the fabric consists of a series of helix means in the form of helical strips 30 which extend cross-wise in the fabric across the entire width thereof. The individual helical links 30 are constructed from a suitable polymeric material such as a monofilament polyester in order to have sufficient plasticity to withstand the stress of endless travel over the felt rollers under extreme temperatures and an acceptable shrink range. A suitable material is type 933 polyester monofilament made by American Hoechst Co. having a 0.7 mm diameter. Joint means for joining the adjacent helix lengths successively together in the machine direction is provided by pintles 32. The pintles are monofilament and extend through the overlapping loops of adjacent helix strips joining same together successively to make dryer fabric of a desired dimension in the machine direction which is ultimately made endless by joining the fabric end-to-end. Typically, such fabrics range from 8 to 340 inches cross-wise (width) and from 18 to 70 yards from end-to-end (circumference).
As illustrated, each helix strip 30 includes loops or spirals 34 which have an upper run 34a and lower run 34b which are generally parallel to present a flat and smooth paper contacting surface for the fabric. An open mesh 36 is defined in the fabric face between adjacent pintle joints and runs of the loops across the length and width of the fabric through which air and/or vaporized water are transferred outwardly from the paper web as best seen in FIG. 4.
In accordance with the present invention, a method and structure is provided by which the permeability of a basic non-woven plastic fabric may be varied and by which detrimental sheet flutter may be controlled. The open mesh of the fabric is closed by the insertion of filler means in the form of monofilament strands 38 extending across the entire width of the fabric in a cross-wise direction. The strands may be any suitable polymeric material which is compatible with the environment of the dryer section of the papermaking machine such as nylon, polyester, or polypropylene.
Different arrangements have been found, according to the present invention, as an expedient to producing dryer fabric having permeability characteristics over a complete range of dryer and paper grade applications. As illustrated in FIGS. 2 and 3, the monofilament strands include a flat nylon strip 38 inserted in the helix loops 34 between adjacent pintles 32 in the cross-wise direction. Such has been found satisfactory to produce a permeability of approximately 450 cu. ft./min. (cfm). FIG. 4 illustrates a dryer fabric wherein a pair of filler strands 40 are inserted between adjacent pintle joints 32 in the cross-wise direction wherein the two strands have a somewhat flattened circular cross-section which have been found to produce a permeability of approximately 700 cfm. The fabric is illustrated as holding the paper web W in intimate contact with the heated surface 10a of cylinder 10.
Referring now to FIG. 5, a highly advantageous form of the invention is illustrated wherein a dryer fabric of lower permeability is produced by inserting a low melt polymeric material such as a nylon or polypropylene strand 42 in the cross-wise direction across the fabric in a generally flat configuration. By low-melt, it is meant a strand of polymeric material which will begin to melt and flow at about 350 to 375 degrees farenheit, i.e. the operating temperature of the dryer section.
The polyester helical fabric is initially placed on a conventional stretcher frame in its finished end-less construction and heated to a temperature of approximately 400 to 450 degrees farenheit at a pressure of 40 to 45 pounds per linear inch until the desired dimension of the fabric in the machine direction is obtained. The pressure (tension) and temperature are then reduced to a level at which the fabric will operate in a typical dryer section and the fabric removed. By this process, the basic dryer fabric is heat set and thus thermally stable whereby its dimensions will remain unchanged within required tolerances during use under normal dryer operating pressure temperature, i.e. 250 to 350 degrees farenheit. Filler strands 42 are then inserted and subjected to heat treatment at a temperature of 350 to 400 degrees farenheit which causes the low-melt monofilament to flow and expand much like a balloon being blown up at 44. Thus, the temperature range for treating the low-melt filler does not affect the stability of the basic fabric. Heatsetting may be done prior to or simultaneously with heat treating of the low-melt nylon filler strand. If done simultaneously, the heat treatment is continued beyond that required for the low-melt filler to heat set the fabric.
Since it is virtually impossible for the helix loops to be uniform throughout the fabric and owing to the small size of the helix loops, it is difficult to fit each helix strip with a relative large filler strand to make fabric having a low permeability. However, by using a heat-treated strand, a filler strand of smaller cross-sectional configuration can be used which easily inserts and slides inside each of the loops, regardless of their non-uniformity, across the fabric. While the strand would not close the mesh sufficiently in its untreated state, when heated and allowed to flow, such affords substantial mesh closure and low permeability characteristics. In such a manner, it has been possible to make dryer fabric with a permeability as low as 50 cfm. Round, easily insertable strands 46 may also be utilized and heat-treated at 48. Heat-treated strands have been found to expand vertically between upper and lower loop runs to tighten and interlock the fabric which is an expedient to fabric integrity and in providing a stable fabric paper contacting surface on high speed, end-less travel machines.
After the fabric construction is complete, according to the structure and method herein, the fabric is trimmed to the ordered width and a hot knife is passed along the edges to seal the edges joining the filler strand and helix strips as integral fabric structure. In addition, a width of cement may be applied to the fabric edges for increased stability.
Thus, it can be seen that a highly advantageous dryer fabric and method may be had for a non-woven dryer fabric wherein the permeability characteristics of the basic fabric may be modified to provide a complete range of dryer fabric permeabilities for virtually all papermaking applications.
While a preferred embodiment of the invention has been described using specific terms, such description is for illustrative purposes only, and it is to be understood that changes and variations may be made without departing from the spirit or scope of the following claims.