WO1999066121A1 - Appareil et procede de production de turbulences de pate dans une section de mise en feuille a table plate - Google Patents

Appareil et procede de production de turbulences de pate dans une section de mise en feuille a table plate Download PDF

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Publication number
WO1999066121A1
WO1999066121A1 PCT/CA1999/000573 CA9900573W WO9966121A1 WO 1999066121 A1 WO1999066121 A1 WO 1999066121A1 CA 9900573 W CA9900573 W CA 9900573W WO 9966121 A1 WO9966121 A1 WO 9966121A1
Authority
WO
WIPO (PCT)
Prior art keywords
dewatering
plane
fabric
riser
stock
Prior art date
Application number
PCT/CA1999/000573
Other languages
English (en)
Inventor
James D. White
Douglas R. Mcpherson
Richard E. Pitt
Original Assignee
Jwi Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US09/290,898 external-priority patent/US6126786A/en
Application filed by Jwi Ltd. filed Critical Jwi Ltd.
Priority to DE69914295T priority Critical patent/DE69914295T2/de
Priority to CA002300280A priority patent/CA2300280C/fr
Priority to BRPI9906541-0A priority patent/BR9906541B1/pt
Priority to AU43548/99A priority patent/AU745683B2/en
Priority to AT99926201T priority patent/ATE258249T1/de
Priority to EP99926201A priority patent/EP1005588B1/fr
Priority to NZ502363A priority patent/NZ502363A/en
Publication of WO1999066121A1 publication Critical patent/WO1999066121A1/fr
Priority to NO20000778A priority patent/NO315570B1/no

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Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00—Wet end of machines for making continuous webs of paper
    • D21F1/48—Suction apparatus
    • D21F1/483—Drainage foils and bars
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00—Wet end of machines for making continuous webs of paper
    • D21F1/18—Shaking apparatus for wire-cloths and associated parts
    • D21F1/20—Shaking apparatus for wire-cloths and associated parts in Fourdrinier machines

Definitions

  • the present invention relates to an apparatus and method for generating stock turbulence in the forming section of an open surface paper making machine. More specifically, the present invention relates to an apparatus and method for generating sufficient turbulence in the stock layer of an open surface forming section of a papermaking machine to assist in deflocculating a relatively thick stock layer carried on a relatively slowly moving forming fabric. This invention thus finds application in the manufacture of relatively heavy paper, pulp and board products. Further, the apparatus can be adjustable, so that the amount of turbulence imparted into the stock layer may be controlled and optimized to suit the grade of product being made.
  • an aqueous stock containing both paper making fibers and other paper making solids in amounts of from about 0.1% to about 1.5% by weight, is fed from a headbox slice onto a horizontal moving forming fabric.
  • the moving forming fabric is supported by a forming board, followed by a series of drainage boxes.
  • the drainage boxes commonly include dewatering devices such as blades and foils mounted on the drainage box in contact with the machine side of the forming fabric. In some modern slow speed machines table rolls are also still used as dewatering and turbulence generating devices .
  • the forming section can also include other devices intended to generate at least some turbulence within the stock, such as formation showers .
  • water is removed from the stock until an incipient paper web is formed which contains from about 75% to about 85% water. The remainder of the water is removed in subsequent parts of the papermaking machine.
  • the thickness of the stock layer deposited from the head box slice onto the forming fabric is determined by the machine speed, the water content of the stock delivered from the head box, and the basis weight of the paper or board product being manufactured. Heavier grade products, such as linerboard, corrugating medium, market pulp grades, and paperboard products, require a greater initial stock thickness than lighter grades, such as newsprint.
  • a common means of creating turbulence within the stock on an open surface moving forming fabric is to locate dewatering elements (such as foils, agitator blades and the like) in supporting contact with the machine side of the moving forming fabric.
  • dewatering elements such as foils, agitator blades and the like
  • Devices of this type are described by Wrist, US 2,928,456; Sepall, US 3,573,159; Johnson, US 3,874,998; Saad, US 4,420,370; Kallmes, US 4,687,549 and US 4,838,996; and Fuchs, US 4,789,433.
  • Foils have a leading edge that skims liquid from the forming fabric; the trailing portion is declined downwards at an angle of from about 1° to about 8°, and serves to provide a suction effect which withdraws liquid from the stock and causes the fabric to deflect sufficiently to induce at least some turbulence within the stock.
  • Agitator blades are profiled so that some water is withdrawn and then redirected back through the forming fabric into the fluid stock layer.
  • a carefully profiled cross-machine direction channel is located in the blade surface to achieve this; the water thereby redirected back through the forming fabric creates turbulence in the stock on the fabric, which provides a deflocculating effect and serves to randomize the solids distribution.
  • Another means of inducing agitation is disclosed by Johnson, US 4,140,573.
  • At least one of the dewatering elements on a low vacuum dewatering box are lowered a small amount relative to those on either side so that, as the fabric passes over the sequence of elements, it is pulled down a small amount by the dewatering box vacuum and then released, causing some turbulence within the stock.
  • the apparatus relies on fluid flow into and out of the drainage gap and on the shape of the declining surface of the primary element within the drainage gap, to cause turbulence within the stock after the fluid has been returned through both the forming fabric and any incipient paper mat formed thereon to the stock.
  • the present invention seeks to provide an apparatus and a method for generating stock turbulence sufficient to cause at least some stock deflocculation, and to improve formation in an open surface paper making machine forming section in which the stock layer is relatively thick, and in which the forming fabric moves at a relatively low speed.
  • This invention thus seeks to improve formation in open surface papermaking machines which are used to make relatively heavier basis weight products such as board stock and the like.
  • This invention also seeks at least to alleviate, if not eliminate, sheet sealing by generating sufficient turbulence within the stock so as to redistribute the fibre mat forming a more or less impenetrable layer on the paper side of the forming fabric.
  • This invention consequently is of particular relevance to the use of stock compositions containing a significant content of relatively short fibers, or of recycled materials.
  • this invention seeks to provide an adjustable apparatus for generating a controllable level of stock turbulence sufficient to cause at least some stock deflocculation, and to improve formation in an open surface paper making machine forming section in which the stock layer is relatively thick, and in which the forming fabric moves at a relatively low speed.
  • a “relatively low speed” refers to an open surface forming fabric that is moving through the forming section at a linear speed of less than about 400m/min; a “relatively heavier basis weight product”, and a “relatively thick stock layer”, each refer to an open surface forming fabric machine that is being used to make a product with a finished basis weight over about 160 gsm, which will generally require a stock layer more than about 2.0cm thick adjacent the headbox slice. It should also be noted that although this invention is concerned with the manufacture of products with a relatively high basis weight it is not so limited, and under some circumstances is of benefit with lighter products, and at higher machine speeds.
  • an apparatus for generating turbulence in the stock on a forming fabric in an open surface forming section of a paper making machine including a relatively slowly moving forming fabric having a paper side and a machine side, a relatively thick stock layer on the paper side thereof, a dewatering box means located beneath the forming fabric connected to a controlled vacuum supply means operable to create a reduced pressure within the dewatering box, and a plurality of forming fabric supporting dewatering elements carried by the dewatering box consisting essentially of:
  • a lead-in dewatering element having a fabric supporting surface comprising in sequence: a doctoring leading edge; a substantially horizontal intermediate surface; and a declining trailing surface;
  • a riser dewatering element having a fabric supporting surface comprising in sequence a doctoring leading edge; an inclined surface; an exit surface; and a portion comprising the junction of the inclined and exit surfaces;
  • the declining trailing surface of the lead-in dewatering element and the declining surface of the or each intermediate dewatering element (s) define a second plane inclined at a pre-selected downward trailing angle with respect to the first plane;
  • the doctoring leading edge of the riser element is located above the trailing edge of the adjacent intermediate dewatering element, such that movement of the forming fabric from the trailing edge of the adjacent intermediate dewatering element to the doctoring leading edge of the riser element results in a vertical movement of the forming fabric, and of the incipient paper web and the stock carried thereon.
  • the at least one intermediate dewatering element located between the lead-in dewatering element and the riser element and spaced from each other dewatering element by a gap is adjustably attached to the dewatering box permitting location of the or each declining surface thereof in the desired second plane, and permitting movement to a different desired second plane.
  • the included angle between the first and second planes instead of being determined by the angle to which the intermediate element declining surface is cut, is determined by the setting of the adjustable attachment to the dewatering box.
  • the lead-in element since the lead-in element is not adjustably mounted, it is preferred that its declining trailing surface is arcuate.
  • the apparatus further includes a drainage restricting element, which is interposed between the riser element and the adjacent intermediate element, having a fabric supporting surface comprising in sequence: a doctoring leading edge; and an upwardly inclined surface; wherein the attachment of the drainage restricting element to the dewatering box is constructed and arranged to locate the upwardly inclined surface at an angle to the second plane so as to provide a shallow "V" angle therebetween conforming to the inclined surface of the riser element.
  • the attachment of the drainage restricting element to the dewatering box can be chosen from the group consisting of a fixed attachment, an adjustable attachment, and a second adjustable attachment incorporated into a first adjustable attachment for the intermediate elements.
  • all of the intermediate fabric supporting elements are of the same width in the machine direction.
  • all of the intermediate fabric supporting elements are not of the same width in the machine direction.
  • the or each intermediate fabric supporting element has a substantially flat declining surface.
  • at least one intermediate element has an agitator blade profile.
  • this invention seeks to provide a method for creating a desired level of turbulence in a stock layer carried on a forming fabric in an open surface forming section of a papermaking machine, consisting essentially of moving the forming fabric carrying the stock over at least one dewatering box means carrying a plurality of fabric supporting elements beneath, and in supportive contact with, the forming fabric, and applying a controlled vacuum supply to create a controlled reduced pressure in the dewatering box, the dewatering fabric supporting elements consisting essentially of:
  • a lead-in dewatering element having a fabric supporting surface comprising in sequence: a doctoring leading edge; a substantially horizontal intermediate surface; and a declining trailing surface;
  • a riser dewatering element having a fabric supporting surface comprising in sequence a doctoring leading edge; an inclined surface; a exit surface; and a portion comprising the junction of the inclined and exit surfaces;
  • the portion of the riser element located at the junction of the inclined and exit surfaces is chosen from an apex at the junction of the inclined surface and the exit surface, a short substantially horizontal surface linking the inclined surface and the exit surface, and a curved surface linking the inclined surface and the exit surface;
  • the declining trailing surface of the lead-in dewatering element and the declining surface of the or each intermediate dewatering element (s) define a second plane inclined at a pre-selected downward trailing angle with respect to the first plane;
  • the doctoring leading edge of the riser element is located above the trailing edge of the adjacent intermediate dewatering element, such that movement of the forming fabric from the trailing edge of the adjacent intermediate dewatering element to the doctoring leading edge of the riser element results in a vertical movement of the forming fabric, and of the incipient paper web and stock carried thereon.
  • the desired level of turbulence is created and controlled by at least one adjustable intermediate dewatering element located between the lead-in dewatering element and the riser element which is adjustably attached to the dewatering box permitting location of the or each declining surface thereof in the second plane; and the level of turbulence is controlled by adjusting the adjustable intermediate supporting element to a desired second plane location.
  • the desired level of turbulence is created by an apparatus further including a drainage restricting element, which is interposed between the riser element and the adjacent intermediate element, having a fabric supporting surface comprising in sequence: a doctoring leading edge; and an upwardly inclined surface; wherein the attachment of the drainage restricting element to the dewatering box is constructed and arranged to locate the upwardly inclined surface at an angle to the second plane so as to provide a shallow "V" angle therebetween in conformance with the inclined surface of the riser element.
  • the desired level of turbulence is created and controlled by:
  • a drainage restricting element which is interposed between the riser element and the adjacent intermediate element, having a fabric supporting surface comprising in sequence: a doctoring leading edge; and an adjustable upwardly inclined surface; wherein the level of turbulence is controlled by:
  • the angle between the first and second planes is from greater than 0° to about 10°-
  • One advantage that has been found with the apparatus of this invention is that with relatively thick stock layers once a desired level of turbulence has been induced in the stock, it is less difficult to maintain a desired level of turbulence further along the forming section.
  • the known devices are not always capable generating an acceptable level of turbulence, they are sufficient to maintain that level of turbulence once it has been generated.
  • the present invention thus can be used to optimize the performance of these prior art devices.
  • the shape of the exit surface on the riser blade will be determined by what follows the dewatering device of this invention in the forming section. For example, if it is immediately followed by a second set of the same elements so that the riser element is both the last element on one set, and the first element in the next set, the exit surface of the riser blade will be the same shape as that of the corresponding part of a lead-in element, so that it will have a substantially horizontal intermediate surface, and a declining trailing surface in the same second plane as the following elements. Alternatively, if it is followed by an undrained gap, or by a drainage box equipped with foils, the exit surface of the riser blade will be generally shaped as a foil blade, with a foiling angle generally of from about 0.5° to about 5°.
  • Figure 1 shows schematically a cross section in the machine direction of a stock turbulence generating unit in accordance with a first embodiment of the present invention
  • Figures 2, 3 and 4 show cross sections of the fabric supporting elements used in Figure 1;
  • FIGS 5 and 6 show alternative element arrangements to that shown in Figure 1;
  • Figure 7 shows schematically a cross section in the machine direction of a stock turbulence generating unit incorporating two sets of fabric supporting elements
  • Figure 8 shows schematically an intermediate element including an agitator blade profile
  • Figures 9 and 10 show schematically partially sectioned a stock turbulence generating unit in accordance with a second embodiment of the present invention
  • FIGS 11 and 12 show details of the pivot and adjustment device used in Figures 10 and 11;
  • Figure 13 shows schematically a cross section of the unit of Figures 9 - 12;
  • Figure 14 shows schematically a cross section in the machine direction of a stock turbulence generating unit in accordance with a third embodiment of the present invention
  • Figure 15 shows a cross section of the drainage restriction element shown in Figure 14.
  • Figure 16 shows alternative intermediate element arrangements applicable to Figures 1, 7 and 14 including agitator blade profiles for the intermediate elements.
  • machine direction means a direction along the machine substantially parallel with the direction of travel of the forming fabric
  • cross machine direction means a direction substantially perpendicular to the machine direction generally parallel to the plane of the forming fabric;
  • upstream refers to a direction closer to the headbox from a given point in the machine direction;
  • downstream refers to a direction further from the headbox in the machine direction
  • leading refers to an upstream element edge
  • paper side refers to the face of the forming fabric upon which the stock is deposited, and the paper web is formed
  • machine side refers to the side of the forming fabric in contact with the fabric supporting elements, and thus is the other side from the paper side.
  • the fabric supporting elements all extend in the cross machine direction for the full width of the forming fabric. Additionally, all of the angles shown have been enlarged for clarity.
  • FIG. 1 a first embodiment of this invention.
  • a forming section such as the headbox, headbox slice, breast roll, a forming board (if present) , a forming shower or showers, and any other drainage or formation devices are not shown.
  • the stock turbulence generating device 1 includes a dewatering box 2, which is provided with a hydraulically sealed drain 3 at the bottom, through which the water 3A drained from the stock escapes.
  • Dewatering box 2 is attached by the pipe 4 to a vacuum source which provides a controlled reduced pressure in the range of from ambient pressure to about 7.5 kPa below ambient pressure.
  • a desired level of turbulence is generated in the stock by the set of fabric supporting elements 5, 6, 7 and 8, which are mounted onto the top rail of the dewatering box 2 using a conventional T-bar arrangement, as at 9A, 9B and 9C.
  • the spacing of the T-bars and the widths of the elements determines the widths of the drainage gaps 10, 11, and 12. These gaps are sealed at their lateral edges with end deckles (not shown) .
  • gaps 10 and 11 are the same width and gap 12 is wider. The factors influencing the choice of gap widths is discussed below.
  • the elements 5, 6, 7 and 8 can be formed from high density polyethylene, with inserted ceramic wear surfaces, or any other material appropriate for forming fabric support surfaces.
  • element 5 is the lead-in blade
  • element 8 is the riser blade
  • elements 6 and 7 are the intermediate blades.
  • the forming fabric 13 moves in the direction of the arrow A with its machine side in contact with the supporting elements 5 - 8. Over the gap 12, the forming fabric 13 rises from the last intermediate element 7 onto the riser element 8. This vertical movement of the forming fabric, and of the incipient paper web and stock carried by it, induces turbulence within the stock adjacent to, and downstream of, the exit surface of the riser element 8.
  • the cross section of the lead-in element 5 is shown in Figure 2. This includes a doctoring leading edge 14, a flat intermediate surface 15, and a declining trailing surface 16. In this embodiment, the trailing surface is substantially flat, and is at an angle of inclination , relative to the surface 15.
  • the element is mounted onto the T-bar 9A so that the surface 15 is substantially horizontal.
  • the doctoring leading edge 14 removes at least some of water that has drained through the forming fabric upstream of the lead-in element.
  • the cross section of the riser element 8 is shown in Figure 3. This includes a doctoring leading edge 17, an inclined surface 18, an exit surface 19, and a portion 20 comprising the junction between the inclined and exit surfaces.
  • the portion 20 is the apex at the junction of the two surfaces 18, 19 on either side; alternative shapes are a short horizontal surface, and a curved surface.
  • the underlying requirement for the portion 20 of the riser element is that it provide a continuum of support for the forming fabric moving and bending over it, and that together with the substantially horizontal surface 15 of the lead-in element it defines the first plane, below which the fabric is deflected during its passage over the intermediate elements.
  • the exact shape of the portion 20 is chosen based on the constructional materials used, and the desired lengths of the inclined surface 18 and the exit surface 19.
  • the inclined surface 18 is at an angle ⁇ , which is measured between the inclined surface and the first plane defined by the surface 15 on the lead-in element, and the portion 20 of the riser element.
  • the shape of the exit surface 19 is discussed below.
  • FIG 1 two intermediate elements 6 and 7 are shown, which are generally the same.
  • the cross sections of these are generally the same, and that of intermediate element 6 is shown in Figure 4.
  • This includes a doctoring leading edge 21, a declining surface 22, and a trailing edge 23.
  • the set of three elements comprising the lead-in element and the two intermediate elements supported by the T-bars 9C are spaced apart so that the surface 16 and the two surfaces 22 are in a common second plane at the angle relative to the first plane.
  • the value chosen for the angle ⁇ is determined by the machine characteristics, which includes the overall separation of the lead-in and riser elements, the number of intervening intermediate elements, the machine speed, the thickness of the stock layer, and the level of turbulence desired in the product being made. Consequently, the value of ⁇ determines the vertical distance through which the forming fabric must rise from the locus where it loses contact with the last intermediate element, which is at or near to the trailing edge 23 of this element, to the doctoring leading edge 17 of the riser element. Generally, is in the range of from about 0.25° to about 10°. For most purposes it has been found that ⁇ is less than 6° and often is in the range of from about 2° to about 4°.
  • the gap widths between each of the elements making up the set, in combination with the applied vacuum, and the properties of the stock and of the furnish in the stock also affect both the amount of drainage that occurs, and the amount of turbulence that is generated.
  • the level of applied vacuum in combination with the gap widths must be sufficient to ensure that the forming fabric is in hydraulic contact with the fabric supporting surfaces of all of the elements.
  • the actual value of the applied vacuum also influences the level of turbulence, since it influences the transition of the forming fabric from the last intermediate element onto the riser element. At this point, the forming fabric has a shallow "V" shape, which is sharper or flatter depending at least in part on the vacuum applied.
  • the actual values chosen for , and of the other identified variables, will be determined by the amount of turbulence that is desired in the stock at that point in the forming section; some experimentation may be required to determine optimum values for a given set of paper making conditions .
  • the shape of the exit surface 19 of the riser element 8 depends to a large extent on what follows this element downstream in the forming section, for which there are several choices.
  • the riser element may be followed, for example, by another identical stock turbulence generating unit, an uncontrolled drainage gap, by a set of foils, or by an Isoflo (trade mark) drainage unit.
  • the next drainage unit is another more or less identical unit contiguous with, or even mounted on the same drainage box as the preceding unit, the riser element becomes common to both units.
  • the exit surface of the riser element is then profiled as if it is a lead-in element, so that it matches the chosen value of for the following unit, which may not be the same as that of the preceding unit.
  • the inclined surface of a riser element is generally at a fairly steep rising angle, as it defines the path of the rising forming fabric as shown in Figure 1.
  • the angle ⁇ shown in Figure 3 will generally be in the range of from about 0° to about 30°. In practice, an angle of from about 10° to about 20° is often sufficient.
  • the value of the angle ⁇ is determined by the vertical displacement of the forming fabric as it rises from the declining surface 22 of the last intermediate element to the surface 20 of the riser element.
  • the value of ⁇ should be selected to minimize fabric deflection with a low vacuum level. If in operation the fabric deflection is, or becomes greater than this, it is found that the forming fabric still engages with and follows the shape of this surface. However, some experimentation may be necessary to determine the optimum value of ⁇ for a given set of machine conditions .
  • the unit shown has two intermediate dewatering elements 6 and 7.
  • Figure 5 shows one intermediate dewatering element 6 between a lead-in element 5 and a riser element 8
  • Figure 6 shows a configuration using five intermediate elements 24, 25, 26, 27 and 28, in which all five intermediate elements are arranged to be in the second plane at a common angle to the first plane. It is also shown in Figure 6 that the intermediate elements need not all be the same width.
  • the first set of elements includes a lead-in element 5, and two intermediate elements 29 and 30.
  • the second set of elements includes again two intermediate elements 32 and 33, and a riser element 8.
  • the central element 31 functions as riser for the first set, and lead-in element for the second set. Its upstream inclines surface 18 is shaped to conform to a riser element, and its downstream declining trailing surface is shaped to conform to a lead-in element.
  • This arrangement also can be set up in two different ways:
  • a single dewatering box 2 can be used, with a single vacuum supply 4, as shown essentially in Figure 1; or
  • the vacuum applied to the two compartments need not be the same. It is also possible that the angles ⁇ : and ⁇ 2 , both of which are measured relative to the first plane as shown in Figure 7, need not be the same, depending on the level of turbulence desired in each unit.
  • the intermediate elements have an essentially planar forming fabric supporting surface.
  • an intermediate element with a so-called agitator blade profile with a single channel 35 can be used to induce additional turbulence.
  • Agitator blades having this surface profile are described, for example, by Johnson in US 3,874,998; other profiles are known and used. It appears that an agitator blade profile can enhance the turbulence effects provided by the turbulence generating unit of this invention.
  • the dewatering device may share a common dewatering box with a different dewatering device, such as an Isoflo (trade mark), agitator blades, or a set of foil blades.
  • a different dewatering device such as an Isoflo (trade mark), agitator blades, or a set of foil blades.
  • a stock turbulence generating unit according to the present invention was located downstream of a formation shower in an open surface forming section of a paper machine.
  • the unit used was that shown in Figure 7, but without the internal dividing wall 34, and only a single vacuum supply.
  • Two suction boxes provided with covers substantially as described by Johnson in U.S. 4,140,573 were located immediately downstream of the unit.
  • the machine speed of the forming section was approximately 320 m/min, and the paper board product had a basis weight of approximately 299 gsm.
  • the lead-in element was 38.1mm wide, with a declining surface 8.5mm wide.
  • the two intermediate elements were the same in each pair, and had a declining surface width of 150.9mm
  • the drainage gap between each of the elements was 9.5 mm, except for the gap downstream of each of the last intermediate elements, which was 12.7 mm. In both sets of elements, the value of was 2°.
  • the dewatering element acting as a common lead-in and riser element at the middle of the set had an inclined surface 9.5 mm wide, and the value of the angle ⁇ was 5° .
  • the downstream exit surface of this common element was substantially flat, and inclined downwardly at 2°, thus matching the value of .
  • the exit surface of the second riser blade was horizontal. All of the element widths and the element separation gaps are measured in the machine direction.
  • the vacuum level applied by the suction box was varied from ambient pressure to about 5 kPa below ambient pressure. It was found that when the formation shower located upstream was turned off, the visual appearance of the stock as it passed over the turbulence generating unit did not indicate any increased activity within the stock, however, it was found that both the drainage of the incipient sheet and quality of the resulting paper product, as evidenced by its formation and smoothness, improved as compared to its quality before the unit was installed. This indicated that the unit was effective in generating turbulence within the stock, and in preventing sheet sealing, despite the fact that the formation shower had been turned off.
  • the stock turbulence generating unit of this invention is effective both in imparting turbulence into the stock so as to improve formation and prevent sheet sealing, and can enhance the performance of other drainage and turbulence generating devices.
  • the location of the intermediate elements is determined by fixed structures, and the cross sectional profile of the intermediate elements determines the value of ⁇ . Since the value of is never very large, this construction requires precision machining and installation of the intermediate elements in order to provide a set of surfaces accurately located in the second plane.
  • each intermediate element is adjustably mounted onto the structure of the dewatering box. It is then feasible to control the value of by moving the whole intermediate element to provide an appropriate declining angle for the declining surface by adjusting the adjustable mounting, instead of constructing the element to provide the required fixed declining angle.
  • it is preferred that all of the intermediate elements are mounted onto a single adjustable mounting at the desired machine direction separation with their forming fabric supporting surfaces in a common plane. The desired value of ⁇ is then obtained by adjusting the mounting, or mountings, as required.
  • this configuration has the added advantage that the value of ⁇ can be readily changed so as to alter the level of generated turbulence. This can be required for several reasons, such as a change in product, a change in furnish for the same product, and less than perfect mixing in the headbox causing problems on the forming fabric.
  • this embodiment of this invention additionally provides a means whereby the level of turbulence created can be controlled, and either enhanced or diminished as paper making conditions require.
  • the unit includes a single dewatering box 2 supporting a lead-in element 5, three intermediate elements 35, 36 and 37 of which the middle one 36 is narrower than the other two, and a riser element 8.
  • the lead-in element 5 and the riser element 8 are supported by T- bar structures 9A and 9B, both of which are directly supported by the frame 38 on the top of the dewatering box 2.
  • the three intermediate elements are supported by similar T-bar structures 9C, each of which is mounted onto an adjustable supporting frame 40. At its upstream end, adjacent the lead-in element 5, the adjustable frame 40 is supported by a pivot assembly 41.
  • the adjustable frame 40 is provided with a vertical adjustment assembly 42, which in its turn is controlled by the adjustment bar 43 which is moved in the directions shown by arrow B by means of the handle 44.
  • the adjustment bar 43 is supported by suitable bearing surfaces (not shown) on the beam 45 carried by the supporting framework of the dewatering box top shown generally as 46.
  • the upstream pivot is shown in more detail in Figure 11.
  • the frame 40 pivots through a small arc (which provides sufficient angular movement to obtain any desirable value for ) about rod 47 which is supported by the wall of the dewatering box 2, as at 50.
  • the frame 40 is attached to the rod 47 by means of an adjustable bearer block 48 carried by a bracket 49.
  • the bearer block is held in place by the lockbolt 51 which passes through the slot 52. This form of attachment allows fine control of the location of the surface of element 35 relative to the declining surface of the lead-in element 5.
  • Figure 12 shows only one pivot assembly; in practice there will be at least two, and often more, so that the upstream end of frame 40 is adequately supported for the full width of the forming section.
  • the downstream vertical adjustment assembly is shown in more detail in Figure 12.
  • the vertical adjustment assembly 42 is attached to the downstream face of the frame 40 by the bolts 53 and 54 which are provided with enlarged holes 53A and 54A.
  • the assembly 42 also includes an angled slot 55, into which is fitted a captive pin 56.
  • the outer end of the pin 56 engages into the aperture 57 in the adjustment bar 43.
  • the enlarged holes 53A, 54A are provided to permit fine adjustment of the assembly 42 relative to the frame 40 so that the same value of is obtained across the full width of the forming section. If desired, the bar 43 can be locked in a particular setting by using any appropriate locking mechanism.
  • Figure 12 shows only one adjustment assembly; in practice there will be at least two, and often more, so that the downstream end of frame 40 is adequately supported for the full width of the forming section.
  • the adjustment bar 43 can be replaced by a screw thread system, which can be motorized, and the whole adjustment means can be replaced by a hydraulic or pneumatic system. If the vertical adjustment means is to be freely operable, the fact that it is placed in an environment where it can be clogged with solids from the stock should be borne in mind.
  • the cross section of the unit of Figures 9 - 12 is shown schematically in Figure 13.
  • the lead-in and riser elements 5 and 8 are supported by their T-bars 9A and 9B attached directly to the dewatering box 38.
  • the three intermediate elements 35, 36 and 37 are each supported by T-bars 9C carried on the subframe 40.
  • the subframe 40 is supported at its upstream end by the rod 47, about which it rotates to provide the required value for . It is supported at its downstream end by the adjustment assembly 42 controlled by the adjusting bar 43. The actual value for is determined by the position of the adjustment bar 43 relative to the vertical adjustment assembly 42.
  • the lead-in element is still fixed, and is unadjustable, so that its declining trailing surface is at a constant angle. In some circumstances, it has been found that this can result in the forming fabric deflection over the trailing edge of the lead-in element, which is not desirable for several reasons. It is therefore preferred that in this arrangement, as indicated at 70 (see also Figure 10), the lead-in element has an arcuate trailing edge.
  • the set of intermediate elements are made all the same, and are mounted onto the subframe so that all of their forming fabric engaging surfaces are in a common plane, which is conveniently substantially parallel to the frame itself.
  • a fourth drainage restricting element is included in the dewatering device, located in the gap between the riser element and the immediately preceding upstream intermediate element.
  • the inter-element spacing is chosen to be relatively large, or the value of combined with the machine direction length of the unit provides relatively high vertical distance between the last intermediate element and the doctoring leading edge of the riser element, a significant length of the forming fabric can be exposed to vacuum assisted drainage between the point where the machine side of the forming fabric loses contact with the last intermediate element adjacent its trailing edge, and the leading doctoring edge of the riser element. This allows an excessive amount of water to be withdrawn from the stock at this point.
  • the additional drainage restricting element is adjustably mounted. More preferably, more or less the same subframe assembly as that described for the intermediate elements is used for the additional drainage restricting element.
  • FIG 14 is shown a schematic cross section embodying a drainage restriction element.
  • the lead-in and riser elements 5 and 8 are supported by their T-bars 9A and 9B.
  • the three intermediate elements 35, 36 and 37 are each supported by T- bars 9C carried on the first subframe 40.
  • the first subframe 40 is supported at its upstream end by the rod 47, about which it rotates to provide the required value for . It is supported at its downstream end by the adjustment assembly 42 and the adjusting bar 43. The actual value for is determined by the position of the adjustment bar 43 relative to the vertical adjustment assembly 42.
  • the drainage restriction element 55 is supported by a T-bar 9D carried by a second subframe 56, which is rotatably supported at its downstream end (in much the same fashion as the first subframe 40) by the rod 57.
  • the angular position of the drainage restriction element indicated by the angle ⁇ between the surface 61 and the first plane, is controlled by the vertically adjustable upstream mounting 58 for the second subframe 56.
  • a similar arrangement to that described for the first subframe is conveniently used. In most cases, the angles ⁇ and ⁇ will be more or less the same.
  • the cross section of the drainage restriction element is shown in Figure 15.
  • the upstream face 59 includes a doctoring leading edge 60, which is followed by an upwardly inclined surface 61, which terminates in a trailing edge 62.
  • the element is suitably supported by a T-bar as at 9D.
  • the value of the angle ⁇ is chosen to allow a value for the angle y which provides a smooth transition of the moving forming fabric from the locus at which it loses contact with the last intermediate element 37 onto the inclined surface of the riser element 8.
  • the angle ⁇ can be quite small, and can be zero, so that the upwardly inclined surface is substantially perpendicular to the upstream face 59.
  • the point at which the forming fabric loses contact with the element 37 depends inter alia on the level of vacuum applied to the dewatering box.
  • Figure 16 shows schematically alternative intermediate element profiles to those shown in Figures 1, 7 and 14.
  • Figure 16 shows a seven element set.
  • the first set of elements comprises a lead-in element 5, and two intermediate elements 63, 64 each of which have an agitator blade profile.
  • the central element 31 is both riser element for the first set, and lead-in element for the second set.
  • the second set comprises two intermediate elements 65 and 66, followed by a riser element 8.
  • the elements 65 and 66 have a substantially planar surface.
  • the two sets are placed over a divided dewatering box 2 with separate drainage spaces 2A and 2B to which the same, or a different, level of vacuum can be applied.
  • the elements 63 and 64 can form the second set, with elements 65 and 66 forming the first set. From this it can be seen that combinations of element profiles can be used to generate a desired level of turbulence within the stock.
  • the present invention provides a number of advantages over the prior art.
  • the stock turbulence generating unit can be used to advantage to dewater and deflocculate thick and/or heavy grade stocks while applying low vacuum pressure, or, in some circumstances, minimal vacuum once the section is operating.
  • the ability to diminish the applied level of vacuum significantly reduces drainage and sheet sealing during passage of the stock over the unit.
  • the turbulence generated throughout the stock thickness can also be used to enhance the even and efficient deflocculation of the stock by other agitation devices located both upstream and downstream of the unit.

Landscapes

  • Paper (AREA)
  • Making Paper Articles (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Looms (AREA)

Abstract

L'invention concerne un procédé et un appareil servant à produire des turbulences dans une suspension de pâte afin de défloculer celle-ci dans une section de mise en feuille à surface ouverte d'une machine à fabriquer le papier. L'appareil comporte une caisse (2) à égoutter assurant une déshydratation par égouttage à vide, et qui comporte un ensemble d'éléments d'égouttage produisant des turbulences dans des couches relativement épaisses de pâte transportées à des vitesses de fonctionnement atteignant environ 400 m/min, en vue de produire des produits de papier qui présentent un grammage dépassant généralement environ 160 gsm. Chaque ensemble d'éléments comporte un élément (5) d'entrée, au moins un élément (6, 7) intermédiaire et un élément (8) de sortie. Le trajet du tissu (13) de formation est dévié vers le bas lorsqu'il passe au-dessus des éléments intermédiaires, qui sont inclinés selon un angle d'environ 0° à environ 10° à partir d'un plan défini par des surfaces de support du tissu de mise en feuille situées sur les éléments d'entrée et de montée. Ce mouvement vertical provoque des turbulences et des agitations dans la pâte, qui servent à défloculer celle-ci et à réduire une possibilité d'obturation de feuille. L'appareil peut être utilisé en combinaison avec d'autres dispositifs connus de mise en feuille et d'égouttage situés en amont ou en aval, de façon à augmenter leurs performances pour des couches de pâte plus épaisses et se déplaçant plus lentement.
PCT/CA1999/000573 1998-06-18 1999-06-17 Appareil et procede de production de turbulences de pate dans une section de mise en feuille a table plate WO1999066121A1 (fr)

Priority Applications (8)

Application Number Priority Date Filing Date Title
DE69914295T DE69914295T2 (de) 1998-06-18 1999-06-17 Vorrichtung und verfahren zur erzeugung von stoffturbulenz im blattbildner einer langsiebpapiermaschine
CA002300280A CA2300280C (fr) 1998-06-18 1999-06-17 Appareil et procede de production de turbulences de pate dans une section de mise en feuille a table plate
BRPI9906541-0A BR9906541B1 (pt) 1998-06-18 1999-06-17 aparelho para a geração de turbulência no material em um tecido de formação e método para a criação de um nìvel desejado de turbulência em uma camada de material transportada em um tecido de formação.
AU43548/99A AU745683B2 (en) 1998-06-18 1999-06-17 Apparatus and method of generating stock turbulence in a fourdrinier forming section
AT99926201T ATE258249T1 (de) 1998-06-18 1999-06-17 Vorrichtung und verfahren zur erzeugung von stoffturbulenz im blattbildner einer langsiebpapiermaschine
EP99926201A EP1005588B1 (fr) 1998-06-18 1999-06-17 Appareil et procede de production de turbulences de pate dans une section de mise en feuille a table plate
NZ502363A NZ502363A (en) 1998-06-18 1999-06-17 Apparatus for generating stock turbulence in a fourdrinier forming section of an open surface paper making machine
NO20000778A NO315570B1 (no) 1998-06-18 2000-02-17 Apparat og fremgangsmåte for generering av turbulens i et emne i en seksjonsom danner en fourdrinier

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US9935698A 1998-06-18 1998-06-18
US09/099,356 1998-06-18
US09/290,898 US6126786A (en) 1998-06-18 1999-04-14 Apparatus and method of generating stock turbulence in a fourdrinier forming section
US09/290,898 1999-04-14

Publications (1)

Publication Number Publication Date
WO1999066121A1 true WO1999066121A1 (fr) 1999-12-23

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PCT/CA1999/000573 WO1999066121A1 (fr) 1998-06-18 1999-06-17 Appareil et procede de production de turbulences de pate dans une section de mise en feuille a table plate

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EP (1) EP1005588B1 (fr)
AT (1) ATE258249T1 (fr)
AU (1) AU745683B2 (fr)
BR (1) BR9906541B1 (fr)
CA (1) CA2300280C (fr)
DE (1) DE69914295T2 (fr)
ES (1) ES2212563T3 (fr)
NO (1) NO315570B1 (fr)
NZ (1) NZ502363A (fr)
PT (1) PT1005588E (fr)
RU (1) RU2224062C2 (fr)
WO (1) WO1999066121A1 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002033167A2 (fr) * 2000-10-16 2002-04-25 Roy Van Essen Caisse d'egouttage reglable
DE10107328A1 (de) * 2001-02-16 2002-08-29 Voith Paper Patent Gmbh Verfahren und Vorrichtung zum Abführen von Siebwasser
DE10162133A1 (de) * 2001-12-18 2003-07-03 Voith Paper Patent Gmbh Verfahren und Maschine zur Herstellung einer Faserstoffbahn aus einer Faserstoffsuspension

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8236139B1 (en) 2008-06-30 2012-08-07 International Paper Company Apparatus for improving basis weight uniformity with deckle wave control

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3922190A (en) * 1972-05-01 1975-11-25 Inotech Process Ltd Vacuum drainage device having a plurality of stepped blades
US4687549A (en) * 1986-01-08 1987-08-18 M/K Systems, Inc. Hydrofoil blade

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3922190A (en) * 1972-05-01 1975-11-25 Inotech Process Ltd Vacuum drainage device having a plurality of stepped blades
US4687549A (en) * 1986-01-08 1987-08-18 M/K Systems, Inc. Hydrofoil blade

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002033167A2 (fr) * 2000-10-16 2002-04-25 Roy Van Essen Caisse d'egouttage reglable
WO2002033167A3 (fr) * 2000-10-16 2002-06-20 Essen Roy Van Caisse d'egouttage reglable
US6780286B2 (en) 2000-10-16 2004-08-24 Astenjohnson, Inc. Adjustable activity drainage box
USRE43679E1 (en) 2000-10-16 2012-09-25 Astenjohnson, Inc. Adjustable activity drainage box
DE10107328A1 (de) * 2001-02-16 2002-08-29 Voith Paper Patent Gmbh Verfahren und Vorrichtung zum Abführen von Siebwasser
US6638394B2 (en) 2001-02-16 2003-10-28 Voith Paper Patent Gmbh Method and apparatus for discharge of whitewater
DE10162133A1 (de) * 2001-12-18 2003-07-03 Voith Paper Patent Gmbh Verfahren und Maschine zur Herstellung einer Faserstoffbahn aus einer Faserstoffsuspension

Also Published As

Publication number Publication date
NO20000778L (no) 2000-04-14
AU745683B2 (en) 2002-03-28
DE69914295T2 (de) 2004-07-01
NO20000778D0 (no) 2000-02-17
CA2300280C (fr) 2007-09-11
ATE258249T1 (de) 2004-02-15
BR9906541B1 (pt) 2009-01-13
RU2224062C2 (ru) 2004-02-20
AU4354899A (en) 2000-01-05
PT1005588E (pt) 2004-05-31
EP1005588A1 (fr) 2000-06-07
NO315570B1 (no) 2003-09-22
CA2300280A1 (fr) 1999-12-23
BR9906541A (pt) 2000-10-17
ES2212563T3 (es) 2004-07-16
EP1005588B1 (fr) 2004-01-21
NZ502363A (en) 2001-07-27
DE69914295D1 (de) 2004-02-26

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