[0001] This invention is concerned with paper making machines of the type having a "flat
wire" or "open wire" forming section, which includes means to remove water from the
stock by the use of suction.
[0002] In this type of machine, as opposed to "twin wire" machines, or "gap formers", an
aqueous slurry known as the stock, which contains both fibers and other substances
in an amount of from about 0.1% to 1.5% by weight, is fed from a head box slice onto
a single moving forming fabric. Water is progressively removed from the stock through
the forming fabric in what is known as the "forming section" of the paper making machine.
In this forming section, a variety of drainage devices are used, until the stock contains
from about 2% to about 4% by weight of solid material. At that point, the distribution
and orientation of the fibers and other solids in the still very wet stock is largely
determined, and will not change very much in the remaining paper forming steps unless
other devices such as a dandy roll, or "top wire", is brought into contact with the
stock. Thus at this point the formation of the paper is largely completed.
[0003] In outline, a conventional open wire forming section includes a forming fabric which
is supported at the head box slice end by a breast roll, which is followed in sequence
by a "forming board" and a series of drainage devices, which may be drainage foils
or table rolls, and suction boxes. More recently, forming sections have included a
forming board followed by suction boxes of the type described by Johnson, in U.S.
Patent 4,140,573. These suction boxes heretofore have been distributed along the length
of the forming section with gaps, or undrained spaces, in between them.
[0004] The one reported attempt to use vacuum assisted drainage for the full length of an
open wire forming section appears to have been a failure. Such a paper making machine
is described by E.J. Justus in U.S. 3,052,296 (issued in 1962, assigned to Beloit
Iron Works). As described by Justus, the forming fabric is to be supported on a "continuous
or substantially uninterrupted" series of suction boxes, starting as near to the head
box slice as is practicable. These suction boxes are provided with a foraminous surface
to support the forming fabric, for which several designs are proposed. Justus proffers
several advantages for such a machine: an increase in fiber retention on the forming
fabric of up to 70%, as compared to the usual figure of less than about 50%, reduced
wire marking on the paper, and "better" paper. A further point made by Justus is that
his essentially flat surfaced suction boxes do not cause the phenomenon known as "kick-up"
in the stock associated with the table rolls then used as the primary dewatering devices.
Kick-up results from the vertical deflection of the forming fabric caused by the suction
produced by the roll as described in U.S. 2,928,465. When kick-up occurs, what is
observed is an essentially vertical movement of both the forming fabric and the stock
carried on it in the vicinity of a table roll: this movement can become so violent
that it will literally lift the stock off the forming fabric. Such an occurrence is
not conducive to the making of good paper. In a later communication originating from
Beloit Iron Works (reported by P. Wrist in "The Formation and Structure of Paper",
British Paper and Board Makers Association, London, England, 1962, at pages 863, 864)
it is noted that although many of the benefits proffered by the all-vacuum assisted
drainage technique proposed by Justus indeed are obtained, nevertheless "the formation
of the [paper] sheet deteriorated to an unacceptable level." (Communication to P.
Wrist, from Beloit Iron Works). In other words it proved to be impossible to make
acceptable quality paper using the modified paper making machine proposed by Justus.
Perhaps as a consequence of this failure, this approach to stock dewatering was not
pursued further. Even Justus turned his attention to other methods (e.g. as in U.S.
3,102,066).
[0005] It has now been realized that the failure of the Justus attempts may be directly
attributed to at least two seemingly unrelated causes. First, Justus in setting out
to avoid the then known problems of heavy suction and kick-up becoming prevalent with
table rolls (and which were becoming a handicap serving to limit paper making speed,
since as the linear speed of the forming fabric increases the suction and kick-up
effects become more violent) endeavoured to eliminate all stock agitation in the forming
section.
[0006] It has now been known for some time that improved paper making operations can result
if some deliberate and controlled agitation is introduced into the stock on the forming
fabric whilst it is still in a highly fluid state.
[0007] It has now been discovered that the precise spacing of the devices used to generate
stock agitation has a very important effect on paper sheet quality. When the devices
are spaced apart in a uniform manner, they act in a periodic or harmonic relationship
to each other, so that later devices (that is, ones further from the head box slice)
can either reinforce and add to the stock agitation produced by earlier devices, or
diminish and dampen that agitation. This provides a controlled and uniform stock agitation
that is both easily generated and easily controlled, to benefit the paper sheet formation.
[0008] Second, Justus recommends to use a vacuum level ranging from a low level of effectively
zero in a suction box adjacent the head box slice rising to a figure of 2 inches of
mercury at the 3% point, that is a value of about 70 cms of water. It has been discovered
that this is also a mistake, and that with dewatering devices somewhat similar to
those advocated by Justus a far lower level of vacuum is often sufficient, rising
from a very low level adjacent the head box slice to a value of no more than 50 cms
of water at the end of the forming section. It has been discovered that much lower
levels of vacuum than those suggested by Justus can be used with great benefit in
retention and wire mark provided the above mentioned agitation or kick-up can be achieved.
This can be achieved by the use of the static drainage unit known as the Isoflo (Trade
Mark) which is described by Johnson in U.S. 4,140,573.
[0009] Thus it has now been discovered that if first, the correct level of vacuum is used
in the suction boxes and second, the path through which the forming fabric moves whilst
the stock is still highly fluid is properly controlled to provide some agitation in
the stock, then a forming section can be successfully operated with continuous vacuum
assisted drainage. By this means, it becomes possible to increase the area of the
forming fabric that is subjected to vacuum assisted drainage by an amount of often
more than 30%, the actual figure varying from machine to machine. Additionally, fiber
retention is also significantly improved.
[0010] Retention is fundamental in paper making. The commonly used definition in paper making
for first pass retention (FPR) is

[0011] Values for FPR can range from 30 % in the case of papers with a high filler content
to over 90% for some long fibered grades. Several factors affect the FPR including
the type of stock, the kind of forming fabric, the use of chemical retention aids,
the amount of stock agitation, the amount of suction used in forming the paper, and
particularly the velocity induced in the stock by that suction while forming. Improving
retention from 45% to 70% reduces the consistency of the recirculating white water
considerably if the amount of slice opening is left unchanged. (By "consistency" in
this context is meant the total suspended solids content in percent by weight in the
stock or in the white water, as appropriate). This has beneficial effects on the entire
paper mill and reduces the amount of fiber and filler loss. Alternatively, the paper
maker may cut down on the slice opening and use less water to form the paper. Thus
one benefit of this invention, which allows using low vacuums while still achieving
good formation, is to reduce the velocity of drainage thereby improving retention
and wire mark.
[0012] Thus, according to a first aspect of the present invention there is provided a paper
making machine having an open surface forming section, including at least a travelling
continuous forming fabric which passes over a breast roll adjacent a head box having
a head box slice through which aqueous stock is deposited onto the forming fabric,
and a plurality of stock dewatering devices beneath the forming fabric which include
white water drainage means, a foraminous dewatering device adjacent the head box slice
including a plurality of stationary drainage elements disposed in a supporting relationship
substantially transversely of the forming fabric, a foraminous surface on the stock
dewatering devices adapted to support the forming fabric and to provide both apertures
through which the forming fabric drains and a vacuum tight seal between the forming
fabric and the drainage means, and a vacuum means, including both vacuum supply means,
vacuum control means, and a vacuum seal means for the white water drainage means,
whereby a vacuum below ambient atmospheric pressure is provided in each drainage means;
wherein, in said forming section, the solids content of the stock deposited from the
head box through the head box slice onto the forming fabric rises from an initial
low value to a value of from about 2% to about 4%; charactrized in that (i) the foraminous
surface supporting the forming fabric provides a path through which the forming fabric
moves which causes a controlled level of uniformly spaced periodic harmonic agitation
within the stock on the forming fabric; (ii) the stock dewatering devices comprise
a suction box extending from adjacent the foraminous dewatering device to the end
of the forming section, which suction box includes a plurality of evacuated chambers
and (iii) the vacuum means provides a vacuum in the evacuated chambers of the suction
box controlled to a value that rises progressively along the length of the suction
box from a minimum of 0.49 kPa (5 cms water gauge) below ambient atmospheric pressure
adjacent the foraminous dewatering device to a maximum value of 4.9 kPa (50 cms water
gauge) below ambient atmospheric pressure at the end of the forming section.
[0013] In one embodiment, the suction box comprises a plurality of contiguously adjacent
suction boxes, each of which is the full width of the forming section. Alternatively,
in a second embodiment, a series of vacuum-tight transverse divisions can be provided
in a single large suction box. Thus the suction box comprises a sequence of separated
drainage chambers, to each of which a controlled level of vacuum is applied, rising
stepwise from a level of no more than 0.49 kPa (5 cms water gauge) below ambient atmospheric
pressure adjacent the head box slice to no more than 4.9 kPa (50 cms water gauge)
below ambient atmospheric pressure at the other end of the suction box, that is at
the end of the forming section. Each drainage chamber is also provided with a separate
vacuum-tight drainage means.
[0014] In a preferred embodiment, the foraminous surface comprises a slotted type fabric-supporting
cover comprising a series of spaced apart forming fabric-supporting blades having
generally planar top surfaces transverse to the direction of travel of the fabric
in a common essentially horizontal plane providing therebetween suction-accessible
gaps in which the forming fabric is substantially unsupported and is drawn downward
to form stock-agitating undulations in said gaps, the cover including water seal-forming
blades disposed intermediately in the gaps between the fabric-supporting blades and
having top surfaces transverse to the direction of travel of the fabric at a lower
level than the top surfaces of the fabric-supporting blades, and at least forming
water seals at the downward undulations of the forming fabric thereby interrupting
the suction temporarily to limit drainage while causing vertical agitation of fibers
on the fabric passing through the forming section. In a most preferred embodiment,
the fabric supporting blades are spaced apart equally from each other for the length
of the forming section. This provides the desired and required agitation in the stock,
since the forming fabric and the paper stock thereon undulate in a periodic or harmonic
manner for the length of the forming section.
[0015] In certain circumstances it is contemplated that it may not prove to be either practicable
or desirable to utilize a full length open surface forming section using vacuum assisted
drainage, for example when modifying an existing paper making machine. Furthermore,
it has to be noted that obtaining and controlling the very small vacuum levels needed
adjacent a head box slice itself is quite difficult. As noted above, a pressure difference
of less than 0.49 kPa (5 cms water gauge) below ambient atmospheric pressure, or approximately
only 0.5% of an atmosphere, is being used. The basic concepts of this invention can
still be used, nevertheless, in paper making machines having an open surface forming
section wherein a vacuum assisted section is preceded by a short dewatering section
using other static dewatering devices.
[0016] According to a second aspect of the present invention there is provided a process
for improving paper formation in a paper making machine having an open surface forming
section including at least a travelling continuous forming fabric which passes over
a breast roll adjacent a head box having a head box slice through which aqueous stock
is deposited onto the forming fabric, and a plurality of stock dewatering devices
beneath the forming fabric which include white water drainage means, a foraminous
dewatering device adjacent the head box slice including a plurality of stationary
drainage elements disposed in a supporting relationship substantially transversely
of the forming fabric, a foraminous surface on the stock dewatering devices adapted
to support the forming fabric and to provide both apertures through which the forming
fabric drains and a vacuum tight seal between the forming fabric and the drainage
means, and a vacuum means, including both vacuum supply means, vacuum control means,
and vacuum seal means for the white water drainage means, whereby a vacuum below atmospheric
pressure is provided in each drainage means; wherein in said forming section, the
solids content of the stock deposited from the head box through the head box slice
onto the forming fabric rises from an initial low value to a value of from about 2%
to about 4%, said process comprising discharging onto the moving forming fabric an
aqueous paper making fiber stock across the width of the forming fabric, and causing
the forming fabric to move through the forming section, characterized in that (i)
a controlled level of uniformly spaced periodic harmonic agitation is created in the
stock, by causing the forming fabric to follow a path constructed and arranged to
induce the desired agitation and (ii) a controlled level of vacuum below ambient atmospheric
pressure is applied below the forming fabric by means of a suction box extending from
adjacent the foraminous dewatering device to the end of the forming section, the vacuum
applied rising from a minimum of 0.49 kPa (5 cms water gauge) below ambient pressure
adjacent the foraminous dewatering device, to a maximum value of 4.9 kPa (50 cms water
gauge) below ambient atmospheric pressure at the end of the forming section.
[0017] In a preferred embodiment, the vacuum in the suction box is controlled in such a
way that it rises in a stepwise fashion in the separate sections of the box along
the length of the forming section, from the initial low value of below 0.49 kPa below
ambient atmospheric pressure (5 cms water gauge) to a maximum value of no more than
4.9 kPa below ambient atmospheric pressure (50 cms water gauge). Desirably, there
are as many vacuum levels as possible, preferably more than three, and most preferably
at least five.
[0018] The invention will now be described by way of reference to the attached drawings
in which:
Figure 1 shows diagrammatically the initial part of a conventional prior art paper
making machine;
Figure 2 shows a conventional prior art foil blade;
Figure 3 shows a so-called Isoflo unit according to US-A-4 140 573;
Figure 4 shows schematically harmonic stock agitation associated with a series of
foils;
Figure 5 shows diagrammatically a paper making machine modified according to one aspect
of this invention;
Figure 6 shows a modification to the machine of Figure 5; and
Figure 7 shows a detail of Figure 5.
[0019] In these Figures, relevant like parts have been given the same numbers.
[0020] In Figure 1, the forming section of a conventional prior art open surface paper making
machine is shown, incorporating a forming fabric 1, which moves in the direction of
the arrows shown at 1A and 1B. The forming fabric moves over a breast roll 2, and
various tensioning and idling rollers 3. The stock is deposited onto the forming fabric
1 from the head box shown diagrammatically at 4, through a slice 5, which extends
across the forming fabric 1. Beneath the forming fabric in the dewatering zone are
placed a sequence of drainage devices 6, 7, 8, 9, 10, 11 and 12, provided with white
water drains 15, 16, 17, 18 and 19. The first of these drainage devices, 6, comprises
a forming board, the second, 7, comprises a open foil unit, and the remainder are
so-called Isoflo units (Trade Mark). Boxes 8 to 12 are also provided with a controlled
vacuum, through the vacuum pipes 20, 21, 22, 23 and 24 respectively. The vacuum applied
will typically range from zero to 5 cms water gauge in box 8, to no more than 50 cms
water gauge in box 12; the white water drains 15, 16, 17, 18 and 19 contain suitable
vacuum legs. A key feature of this conventional prior art open surface paper making
machine is that not all of the forming section is being actively drained. The drainage
and suction boxes are separated by the spans marked a, b, c, d, e and f which represent
undrained areas, apart from any water which may happen to drain through under gravity.
In the prior art machine shown, these spans represent nearly 30% of the total area
of the forming section.
[0021] In this machine, which is typical of existing prior art machines, three different
forms of drainage element are used, in sequence away from the head box slice 5. The
first of these is a set of conventional flat forming board blades associated with
box 6.
[0022] In box 7 the drainage elements 25 are conventional foil blades broadly conforming
to the design shown is section in Figure 2. These foils comprise a supporting bar
28 with a tee-shaped head, onto which is slid the foil blade proper, 29. This includes
a flat face 30 onto which the forming fabric 1 rests, and a divergent trailing face
31. In the figure the divergent angle Z is shown exaggeration for clarity. Generally
it is far smaller than it is shown, ranging from about 1 degree to about 5 degrees,
with angles of 2 to 2.5 degrees being commonly used. As the forming fabric moves over
the foil in the direction of the arrow 32, as a consequence of hydraulic phenomena
created in the nip provided by the trailing face 31, water is sucked from the stock
through the forming fabric.
[0023] In boxes 8 through 12 a so-called Isoflo unit is used, which is described in detail
in Johnson, U.S. 4,140,573. This is shown in Figure 3 (which corresponds broadly to
Johnson's Figure 4), and can be seen to incorporate two groups of static devices 26
and 27. Devices 26 and 27 are each supported on a tee-bar 28; these tee bars 28 are
supported across the width of the box by suitably placed supports 33. Although similar
in appearance to the foil blades of Figure 2, the static devices 26 and 27 differ
in two separate ways. The top faces of all of these devices which bear against the
forming fabric 1 are generally planar and either in the plane of the forming fabric
(devices 26) or a little below it (devices 27). As shown in Figure 3 the vertical
lowering of the devices 27 is indicated at A, which is exaggerated for clarity. In
practise, this distance generally will range from about 0.5 mm to about 5.0 mm. The
forming fabric in moving over such a foraminous surface undulates between successive
devices 26, and the intervening devices 27 are so placed vertically as to provide
a water seal to the underside of the forming fabric. Sealing elements, not shown,
are also provided along the sides of the boxes in between the drainage devices, parallel
to the sides of the forming fabric. Water is drawn from the stock through the forming
fabric by the application of vacuum to the box.
[0024] There is a further feature which is common to both of these forms of static drainage
devices. Figure 4 shows diagrammatically the harmonic, or periodic, stock agitation
that can be generated by a regular and uniform spacing of the vertical pulses generated
by foil blades supporting a forming fabric. In Figure 4, a small section of the forming
fabric 1 is shown moving in the direction of arrow 1A. The forming fabric passes over
a series of foil blades all uniformly spaced apart by the distance Y, as indicated
between foil blades 45 and 46 mounted on the tee bars 41 and 42. Because the stock
agitation is generated by vertical movement of the forming fabric caused by the foil
blades, which are each spaced apart by the constant distance Y, the area of vertical
stock agitation shown by 48 is followed by another area 50. Similarly, the quiescent
zone 49 is followed by another quiescent zone 51, following the area 50. As Figure
4 indicates, both the areas of vertical agitation 48 and 50 and the zones of quiescence
49 and 51 are each spaced apart at the same distance Y. As shown in Figure 4, with
no foil blade on the tee bar 43, vertical agitation of the stock still occurs at the
location 52 (which is differently shaded in Figure 4 to emphasize that there is no
foil blade on tee bar 43), although the amplitude of the agitation at the location
52 is somewhat less than is obtained with a foil blade in place on tee bar 43. The
occurrence of this activity in the vicinity of the tee bar 43 (which has no foil blade)
is referred to as occurring at a "ghost blade". It is also important to note that
these areas of agitation and quiescence in the stock do not move with the forming
fabric, but rather remain in essentially the same place. A similar quiescent zone
53 follows the "ghost blade", and foil induced agitation 54 occurs in the vicinity
of foil 47.
[0025] For the Johnson Isoflo device shown in Figure 3, the area of the stock vertical agitation
is due to the downward deflection of the fabric as it moves from fabric support surfaces
26 to surfaces 27, and periodicity similar to that of Figure 4 is observed.
[0026] Thus it has been found that spacing of the various support surfaces for the forming
fabric can be used to generate, to optimize and to control the agitation occurring
in the stock on the forming fabric. The dewatering support surfaces can be placed
to control the vertical movement which is initiated by earlier drainage devices.
[0027] This flexibility of control of the amount of vertical agitation permitted to occur
in the stock on the forming fabric allows for better dewatering of the stock as it
travels on the forming fabric through the forming section. Two possible ways of utilizing
this invention are shown in Figures 5 and 6. Each of these figures shows essentially
the same portion of a paper making machine as is shown in Figure 1, but with certain
differences. In common with Figure 1, the forming fabric 1 passes over the rollers
3, around the breast roll 2, and then past the head box slice 5, at which point the
stock is deposited onto it. Drainage is initiated by the forming board section on
box 6, and continued by the foils associated with box 7; it is to be noted that boxes
6 and 7 are still separated by the gap a.
[0028] The remainder of the forming section comprises a single extended suction box 100,
which is separated into the sequence of separate chambers 8, 9, 10, 11 and 12, either
by using a single continuous suction box with dividers, or by using a plurality of
smaller boxes, butting up closely to each other. These suction units also differ from
the arrangement shown in Figure 3 in another way. In that figure, the first support
surface 26 is an upper one, and is followed by a lower one, 27. As described by Johnson
in U.S. 4,140,573, the last support surface in the box is also an upper one. When
a sequence of boxes of this type are brought into the contiguous relationship of this
invention, one of these surfaces becomes redundant, since the last support surface
in any one box also becomes the first support surface for the next one. This is shown
more clearly in Figure 7.
[0029] There are two different ways in which the continuous suction box of this invention
can be utilized to improve the sort of machine shown in Figure 1. In Figure 5, the
gaps c through f have been eliminated by lengthening the boxes 8 through 12, and therefore
the overall length of the forming section has not been changed. Alternatively, the
same effect could be achieved by adding another box to match the span of gaps c through
f, and moving boxes 9, 10 and 11 to accommodate it. In either case, the length of
the forming section is retained unchanged. The other option is simply to move the
suction boxes 8 through 12 together to eliminate gaps c through f. Whilst this is
effective, it has two disadvantages. The first is that it will still leave an equivalent
length of forming fabric (corresponding substantially to the eliminated gap length)
effectively unused, unless the somewhat drastic step of reducing overall machine length
is also taken. The second is that although the same amount of water is being removed
from the stock, the use of an overall shorter forming section means that water is
being removed more rapidly, than is the case if the length of the forming section
is retained unchanged. It appears to be advantageous to retain the forming section
length, since removing the same amount of water over a longer length of forming fabric
reduces the rate at which that water is removed. Decreasing the drainage rate generally
improves the quality of the paper being made, since better paper mat formation occurs
and wire marking is lessened. Further, the FPR figures also improve; it appears to
be feasible to obtain an improvement of the order of 20% with the method of this invention.
[0030] In Figure 5 two of the noted gaps which are not actively drained are still present
in the forming fabric: these are a and b. As is shown in Figure 6, it is also possible
to eliminate gap b, and hence to lengthen the suction box 100 a little further. The
same considerations will also apply concerning whether the gap b is removed by lengthening
box 100, by adding another box, or by laterally displacing box 100 as are mentioned
above in respect of Figure 5. It appears to be preferable to lengthen box 100, to
remove gap b. It should also be noted that if gap b is to be eliminated, then the
last foil in box 7, which will generally be over the wall of box b adjacent the gap,
will become redundant, as the arrangement shown broadly in Figure 7 needs to be used,
with a fabric support blade over the contiguous walls of chamber 7 and the suction
box 100.
1. A paper making machine having an open surface forming section, including at least
a travelling continuous forming fabric (1) which passes over a breast-roll (2) adjacent
a head box (4) having a head box slice (5) through which aqueous stock is deposited
onto the forming fabric, and a plurality of stock dewatering devices beneath the forming
fabric which include white water drainage means, a foraminous dewatering device (6,7)
adjacent the head box slice including a plurality of stationary drainage elements
disposed in a supporting relationship substantially transversely of the forming fabric,
a foraminous surface (26,27) on the stock dewatering devices adapted to support the
forming fabric and to provide both aperture through which the forming fabric drains
and a vacuum tight seal between the forming fabric and the drainage means, and a vacuum
means, including both vacuum supply means, vacuum control means, and vacuum seal means
for the white water drainage means whereby a vacuum below ambient atmospheric pressure
is provided in each drainage means; wherein in said forming section, the solid content
of the stock deposited from the head box through the head box slice onto the forming
fabric rises from an initial low value to a value of from about 2% to about 4%;
characterized in that
(i) the foraminous surface (26,27) supporting the forming fabric provides a path through
which the forming fabric moves which causes a controlled level of uniformly spaced
periodic harmonic agitation (48,50) within the stock on the forming fabric;
(ii) the stock dewatering devices comprise a suction box (100) extending from adjacent
the foraminous dewatering device (6,7) to the end of the forming section, which suction
box includes a plurality of evacuated chambers (8,9,10,11,12); and
(iii) the vacuum means provides a vacuum in the evacuated chambers of the suction
box controlled to a value that rises progressively along the length of the suction
box from a minimum of 0.49 kPa (5cms water gauge) below ambient atmospheric pressure
adjacent the foraminous dewatering device to a maximum value of 4.9 kPa (50 cms water
gauge) below ambient atmospheric pressure at the end of the forming section.
2. An apparatus according to Claim 1 characterized in that the suction box (100) comprises
either a single box (100) extending from adjacent the foraminous dewatering device
(6,7) to the end of the forming section which is provided with a plurality of pressure
tight transverse divisions between each of which a separate controlled vacuum can
be applied and each of which has a separate white water drainage means (15,16,17,18,19),
or a plurality of contiguously adjacent boxes extending from adjacent the foraminous
dewatering device, to each of which a separate controlled vacuum can be applied, and
each of which has a separate white water drainage means (15,16,17,18,19).
3. An apparatus according to Claim 1 characterized in that the dewatering device (6,7)
comprises two separately drained and separated static drainage devices comprising
a forming board section (6) adjacent the head box slice (5), and a separate foil section
(7) spaced therefrom, in which section each foil (29) comprises a flat support surface
(30), and a trailing portion (31) (in the direction of forming fabric travel) diverging
from the plane of the fabric (1) at an angle greater than zero degrees and less than
5 degrees.
4. An apparatus according to Claim 1 characterized in that the foraminous surface on
the suction box comprises a slotted-type fabric cover comprising a series of spaced
forming fabric-supporting blades (26) having a generally planar top surface transverse
to the direction of travel of the fabric in a common essentially horizontal plane
providing therebetween suction-accessible gaps in which the forming fabric is substantially
unsupported and is drawn downward to form stock-agitating undulations in said gaps,
said cover including water seal forming blades (27) disposed intermediately in said
gaps between the fabric supporting blades and having top surfaces transverse to the
direction of travel of the fabric at a lower level than the top surfaces of the fabric
supporting blades and at least forming water seals at the downward undulations of
the forming fabric, thereby interrupting the suction temporarily to limit drainage
while causing vertical agitation of fibers on the fabric passing through the forming
section; wherein both the first, the last, and any intermediate support-blades placed
over either an internal transverse vacuum tight division or a pair of contiguous transverse
walls of two adjacent suction boxes, are all forming fabric-supporting blades (26).
5. An apparatus according to Claim 3 characterized in that in the foil section, the separate
foils (29) are so placed as to contribute toward controlled agitation of the stock
on the forming fabric.
6. A process for improving paper formation in a paper making machine having an open surface
forming section including at least a travelling continuous forming fabric (1) which
passes over a breast-roll (2) adjacent a head box (4) having a head box slice (5)
through which aqueous stock is deposited onto the forming fabric, and a plurality
of stock dewatering devices beneath the forming fabric which include white water drainage
means, a foraminous dewatering device (6,7) adjacent the head box slice including
a plurality of stationary drainage elements disposed in a supporting relationship
substantially transversely of the forming fabric, a foraminous surface (26,27) on
the stock dewatering devices adapted to support the forming fabric and to provide
both apertures through which the forming fabric drains and a vacuum tight seal between
the forming fabric and the drainage means, and a vacuum means, including both vacuum
supply means, vacuum control means, and vacuum seal means for the white water drainage
means whereby a vacuum below ambient atmospheric pressure is provided in each drainage
means; wherein, in said forming section, the solid content of the stock deposited
from the head box through the head box slice onto the forming fabric rises from an
initial low values to a value of from 2% to about 4%, said process comprising discharging
onto the moving forming fabric an aqueous paper making fiber stock across the width
of the forming fabric, and causing the forming fabric to move through the forming
section, characterized in that
(i) a controlled level of uniformly spaced periodic harmonic agitation is created
in the stock, by causing the forming fabric to follow a path constructed and arranged
to induce the desired agitation;
(ii) a controlled level of vacuum below ambient atmospheric pressure is applied below
the forming fabric by means of a suction box extending from adjacent the foraminous
dewatering device to the end of the forming section, the vacuum applied rising from
a minimum of 0.49 kPa (5 cms water gauge) below ambient pressure adjacent the foraminous
dewatering device, to a maximum value of 4.9 kPa (50 cms water gauge) below ambient
atmospheric pressure at the end of the forming section.
7. A process according to Claim 6 characterized in that the suction box (100) comprises
either a single box extending from adjacent the foraminous dewatering device (6,7)
to the end of the forming section which is provided with a plurality of pressure tight
transverse divisions between each of which a separate controlled vacuum can be applied
and each of which has a separate white water drainage means (15,16,17,18,19), or a
plurality of contiguously adjacent boxes extending from adjacent the foraminous dewatering
device, to each of which a separate controlled vacuum can be applied, and each of
which has a separate white water drainage means (15,16,17,18,19).
8. A process according to Claim 6, characterized in that:
(a) an aqueous paper making fiber stock is discharged onto the moving forming fabric
across the width thereof;
(b) the forming fabric moves over a foraminous dewatering device comprising in combination
a forming board section, adjacent the head box slice, and a foil unit section in which
section each foil comprises a flat support surface, and a trailing portion (in the
direction of forming fabric travel) diverging from the plane of the fabric at an angle
greater than zero degrees and less than 5 degrees;
(c) the forming fabric moves thereafter over a continuous suction box including a
plurality of chambers to each of which a controlled level of vacuum is applied at
uniformly spaced apart zones transverse to the direction of the travel of the fabric
and permitting the fabric to sag in gaps between the supported zones and forming vertical
fabric undulations in said gaps, thereby inducing uniformly spaced periodic harmonic
agitation in the stock;
(d) water seal means are provided intermediately of the gaps in a plane below where
the fabric is supported to interrupt the suction;
(e) vacuum is applied in said gaps to the underside of the forming fabric to draw
the fabric downwardly between the gaps, the suction applied in each gap being interrupted
by the water seal forming means as the aqueous paper-making suspension of fibers is
dewatered; and
(f) controlling the vacuum applied in the chambers below gaps so that the applied
vacuum rises progressively from a minimum value of 0.49 kPa (5 cms water gauge) below
ambient atmospheric pressure adjacent the foil unit, to a maximum value of no more
than 4.9 kPa (50 cms water gauge) below ambient atmospheric pressure at the end of
the forming section.
1. Papierherstell-Maschine mit einem offenflächigen Siebabschnitt, die enthält mindestens
ein wanderndes kontinuierliches Siebtuch (1), welches über eine Brustwalze (2) hinwegtritt,
die einem Auflaufkasten (4) mit einem Stoffauflaufschlitz (5) benachbart ist, durch
welchen wäßriger Papierstoff auf das Siebtuch aufgelegt wird, und eine Vielzahl von
Papierstoff-Entwässerungsgeräten unterhalb des Siebtuchs, welche enthalten Siebwasser-Entwässerungsmittel,
ein mit Öffnungen versehenes Entwässerungsgerät (6, 7) benachbart dem Auflaufschlitz,
welches eine Vielzahl von stationären Entwässerungselementen enthält, die in einer
Stützbeziehung im wesentlichen quer zu dem Siebtuch angeordnet sind, eine mit Öffnungen
versehene Fläche (26, 27) an den Papierstoff-Entwässerungsgeräten, die ausgelegt ist
zum Abstützen des Siebtuchs und zum Schaffen sowohl der Öffnungen, durch welche das
Siebtuch entwässert, als auch einer Unterdruckabdichtung zwischen dem Siebtuch und
dem Entwässerungsmittel, und ein Unterdruckmittel, das sowohl Unterdruck-Zuführmittel,
als auch Unterdruck-Steuermittel und Unterdruck-Dichtmittel für das Siebwasser-Entwässerungsmittel
enthält, wodurch ein unter Umgebungsdruck liegender Unterdruck in jedem Entwässerungsmittel
geschaffen wird; wobei in dem Siebtuchabschnitt der Feststoffanteil des aus dem Auflaufkasten
durch den Auflaufkastenschlitz auf das Siebtuch abgeschiedenen Papierstoffs von einem
anfangs niedrigen Wert auf einen Wert von etwa 2% bis etwa 4% ansteigt; dadurch gekennzeichnet,
daß
(i) die mit Durchbrüchen versehene Fläche (26, 27), welche das Siebtuch abstützt,
einen Weg schafft, durch den sich das Siebtuch bewegt, der ein gesteuertes Niveau
von gleichmäßig mit Abständen voneinander versehener periodischer harmonischer Bewegungsbeeinflussung
(48, 50) innerhalb des Papierstoffs auf dem Siebtuch verursacht;
(ii) die Papierstoff-Entwässerungsgeräte umfassen einen Saugkasten (100), der sich
von der Nachbarschaft zu dem mit Öffnungen versehenen Entwässerungsgerät (6, 7) bis
zum Ende des Siebtuchabschnitts erstreckt, welcher Saugkasten eine Vielzahl von unterdruckbeaufschlagten
Kammern (8, 9, 10, 11, 12) enthält; und
(iii) das Unterdruckmittel einen Unterdruck in den unterdruck-beaufschlagten Kammern
des Saugkastens schafft, der auf einen Wert gesteuert wird, welcher in Längsrichtung
des Saugkastens von einem Minimalwert von 0,49 kPa (15 cm Wassersäule) unter Umgebungsdruck
benachbart dem mit Öffnungen versehenen Entwässerungsgerät auf einen Maximalwert von
4,9 kPa (50 cm Wassersäule) unter Umgebungsdruck am Ende des Siebabschnitts ansteigt.
2. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß der Saugkasten (100) umfaßt
entweder einen Einzelkasten (100), der sich von dem Anschlu an das mit Öffnungen versehene
Entwässerungsgerät (6, 7) zu dem Ende des Siebabschnitts erstreckt und mit einer Vielzahl
von druckdichten Querteilungen versehen ist, zwischen welchen jeweils ein separat
gesteuerter Unterdruck angelegt werden kann und von denen jedes ein getrenntes Siebwasser-Ablaufmittel
(15, 16, 17, 18, 19) besitzt, oder eine Vielzahl von aneinander anstoßenden benachbarten
Kästen, die sich von der Nachbarschaft zu dem mit Öffnungen versehenen Entwässerungsgerät
erstrecken, von denen an jeden ein separat gesteuerter Unterdruck angelegt werden
kann und jedes ein separates Siebwasser-Ablaufmittel (15, 16, 17, 18, 19) besitzt.
3. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß das Entwässerungsgerät (6,
7) umfaßt zwei mit separatem Ablauf versehene und getrennte statische Ablaufgeräte,
welche einen Siebtuch-Auflagenabschnitt (6) benachbart dem Auflaufkastenschlitz (5)
umfassen, und einen getrennten Foil-Abschnitt (7) mit Abstand davon, in welchem Abschnitt
jedes Foil (29) eine ebene Stützfläche (30) umfaßt und einen Nachlaufabschnitt (31)
(in Laufrichtung des Siebtuchs), das von der Ebene des Tuchs (1) mit einem Winkel
größer als 0° und kleiner als 5° abweicht.
4. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß die mit Öffnungen versehen
Fläche an dem Saugkasten umfaßt eine geschlitzte Gewebeauflagedecke, welche umfaßt
eine Reihe von mit Abstand voneinander versehenen Siebtuch-Stützleisten (26) mit einer
allgemein planaren oberen Fläche quer zur Laufrichtung des Gewebes in einer gemeinsamen
im wesentlichen horizontalen Ebene, die dazwischen saugzugängliche Spalte schaffen,
in welchem das Siebtuch im wesentlichen unabgestützt ist und nach unten gezogen wird,
um den Papierstoff bewegende Wellungen in den Spalten zu bilden, wobei die Auflagedecke
enthält Wasserabdicht-Siebleisten (27), die in den Spalten zwischen den Gewebeabstützleisten
angeordnet sind und obere Flächen quer zur Laufrichtung des Gewebes besitzen an einem
niedrigeren Niveau als die Oberflächen der Gewebestützleisten und mindestens Wasserabdichtungen
an den nach unten gehenden Wellungen des Siebtuchs bilden, dadurch die Saugwirkung
zeitweilig unterbrechen, um die Entwässerung zu begrenzen, während sie gleichzeitig
eine Vertikalbewegung der Fasern an dem sich durch den Siebabschnitt bewegenden Tuch
verursachen; wobei sowohl die erste, wie auch die letzte und irgendwelche Zwischenstützleisten,
die entweder über eine innere unterdruckdichte Querteilwand oder zwei aneinanderstoßende
Querwände von zwei benachbarten Saugkästen gesetzt sind, alle zusammen Tuchabstützleisten
(26) bilden.
5. Vorrichtung nach Anspruch 3, dadurch gekennzeichnet, daß in dem Foilabschnitt die
separaten Foils (29) so gesetzt sind, daß sie zur gesteuerten Bewegungsbildung des
Papierstoffs an dem Siebtuch beitragen.
6. Verfahren zum Verbessern der Papierausbildung in einer Papierherstell-Maschine mit
einem offenflächigen Siebabschnitt, der mindestens ein kontinuierliches wanderndes
Siebtuch (1) enthält, welches über eine Brustwalze (2) benachbart einem Auflaufkasten
(4) mit einem Auflaufkastenschlitz (5) geht, durch welchen Schlitz ein wäßriger Papierstoff
auf das Siebtuch aufgebracht wird, und eine Vielzahl von Papierstoff-Entwässerungsgeräten
unterhalb des Siebtuchs, welche enthalten Siebwasser-Ablaufmittel, ein dem Auflaufkastenschlitz
benachbartes, mit Öffnungen versehenes Entwässerungsgerät (6, 7), das eine Vielzahl
von stationären Ablaufelementen enthält, die in einer Stützbeziehung im wesentlichen
in Querrichtung des Siebtuchs angeordnet sind, eine mit Öffnungen versehene Fläche
(26,27) an den Papierstoff-Entwässerungsgeräten, die ausgelegt ist, das Siebtuch abzustützen
und sowohl Öffnungen zu schaffen, durch welche das Siebtuch entwässert, wie auch eine
Unterdruckabdichtung zwischen dem Siebtuch und dem Ablaufmittel, und ein Unterdruckmittel
einschließlich sowohl eines Unterdruck-Zuführmittels, wie auch eines Unterdruck-Steuermittels
und eines Unterdruck-Abdichtmittels für die Siebwasser-Ablaufmittel, wodurch ein unter
Umgebungsdruck liegender Unterdruck in jedem Ablaufmittel geschaffen wird; wobei in
dem Siebabschnitt der Feststoffgehalt des von dem Auflaufkasten durch den Auflaufkastenschlitz
auf das Siebtuch aufgebrachte Papierstoffs ansteigt von einem anfänglichen niedrigen
Wert auf einen Wert von etwa 2% bis etwa 4%, welches Verfahren umfaßt, daß auf das
sich bewegende Siebtuch ein wäßriger Papierherstell-Faserstoff über die Breite des
Siebtuchs ausgelassen wird und das Siebtuch zur Bewegung durch den Siebabschnitt veranlaßt
wird,
dadurch gekennzeichnet, daß
(i) ein gesteuertes Niveau von mit gleichförmigem Abstand versehener periodischer
harmonischer Bewegungsbildung in dem Papierstoff dadurch geschaffen wird, daß das
Siebtuch veranlaßt wird, einem zum Einführen der gewünschten Bewegungsbildung aufgebauten
und eingerichteten Weg zu folgen;
(ii) ein gesteuertes unter Umgebungsdruck liegendes Unterdruckniveau unter dem Siebtuch
aufgebracht wird mittels eines Saugkastens, der sich von der Nähe des mit Öffnungen
versehenen Entwässerungsgerätes bis zum Ende des Siebabschnitts erstreckt, wobei der
angelegte Unterdruck von einem Minimalwert von 0,49 kPa (5 cm Wassersäule) unter Umgebungsdruck
benachbart dem mit Öffnungen versehenen Entwässerungsgerät auf einen Maximalwert von
4,9 kPa (50 cm Wassersäule) unter Umgebungsdruck am Ende des Siebabschnitts ansteigt.
7. Verfahren nach Anspruch 6, dadurch gekennzeichnet, daß der Saugkasten (100) entweder
einen Einzelkasten umfaßt der sich von der Nachbarschaft zu dem mit Öffnungen versehenen
Entwässerungsgerät (6, 7) zu dem Ende des Siebabschnitts erstreckt und mit einer Vielzahl
von druckdichten Querteilwänden versehen ist, zwischen welchen ein separat gesteuerter
Unterdruck angewendet werden kann und von denen jede ein separates Siebwasser-Ablaufmittel
(15, 16, 17, 18, 19) besitzt, oder eine Vielzahl von aneinander anstoßenden benachbarten
Kästen, die sich von der Nachbarschaft zu dem mit Öffnungen versehenen Entwässerungsgerät
erstrecken, an denen jeweils ein separat gesteuerter Unterdruck angelegt werden kann
und von denen jedes ein separates Siebwasser-Ablaufmittel (15, 16, 17, 18, 19) besitzt.
8. Verfahren nach Anspruch 6, dadurch gekennzeichnet, daß:
(a) ein wäßriger Papierherstell-Faserstoff auf das sich bewegende Siebtuch über dessen
gesamte Breite ausgelassen wird;
(b) das Siebgewebe sich über ein mit Öffnungen versehenes Entwässerungsgerät bewegt,
welches in Kombination umfaßt einen Siebleistenabschnitt benachbart zum Auflaufkastenschlitz
und einen Foileinheiten-Abschnitt, in welchen Abschnitt jedes Foil umfaßt eine ebene
Stützfläche und einen Nachlaufabschnitt (in der Laufrichtung des Siebtuchs), der von
der Ebene des Tuchs mit einem Winkel größer als 0° und kleiner als 5° abweicht;
(c) das Siebgewebe sich danach über einen kontinuierlichen Saugkasten bewegt, der
eine Vielzahl von Kammern enthält, von denen an jede ein gesteuertes Unterdruckniveau
angelegt wird, in mit gleichmäßigem Abstand voneinander versehenen Zonen quer zur
Laufrichtung des Tuchs, und zugelassen wird, daß das Tuch in die Spalte zwischen den
abgestützten Zonen einsackt und vertikale Tuchwellungen in den Spalten bildet, um
dadurch mit gleichmäßigem Abstand versehene periodische harmonische Bewegungsbildung
in den Papierstoff einzuführen;
(d) Wasserdichtmittel zwischen den Spalten in einer Ebene vorgesehen sind, die unter
der liegt, wo das Tuch abgestützt ist, um die Saugwirkung zu unterbrechen;
(e) Unterdruck in den Spalten an die Unterseite des Siebtuchs angelegt wird, um das
Tuch zwischen den Spalten nach unten zu ziehen, wobei die in jedem Spalt angelegte
Saugwirkung durch das die Wasserdichtung bildende Mittel unterbrochen wird, wenn die
wäßrige Papierherstell-Faseraufschlämmung entwässert wird; und
(f) der an die Kammern unter den Spalten angelegte Unterdruck so gesteuert wird, daß
der angelegte Unterdruck fortschreitend von einem Minimalwert von 0,49 kPa (5 cm Wassersäule)
unter Umgebungsdruck benachbart der Foil-Einheit auf einen Maximalwert von nicht mehr
als 4,9 kPa (50 cm Wassersäule) unter Umgebungsdruck am Ende des Siebabschnitts ansteigt.
1. Machine à papier comprenant une section de formage à surface ouverte, comprenant au
moins un tissu de formage continu (1) en déplacement qui passe sur un rouleau de tête
(2) au voisinage d'une bâche d'alimentation (4) laquelle présente une fente (5) à
travers laquelle de la pâte à papier aqueuse est déposée sur le tissu de formage,
et comprenant une pluralité de dispositifs d'élimination d'eau pour la pâte à papier,
au-dessous du tissu de formage et qui incluent des moyens de drainage pour les eaux
de blanchiment, un dispositif poreux pour l'évacuation d'eau (6, 7) adjacent à la
fente de la bâche d'alimentation et comprenant une pluralité d'éléments de drainage
stationnaires disposés en une relation de supportage sensiblement transversalement
par rapport au tissu de formage, une surface poreuse (26, 27) sur les dispositifs
d'évacuation d'eau pour la pâte à papier, adaptée à supporter le tissu de formage
et à assurer à la fois les ouvertures à travers lesquelles le tissu de formage est
drainé et un joint étanche au vide entre le tissu de formage et les moyens de drainage,
et comprenant un système de vide, comprenant des moyens d'alimentation de vide, des
moyens de commande de vide, et des moyens de joints à vide pour les moyens de drainage
de l'eau de blanchiment, grâce à quoi on alimente dans chaque dispositif de drainage
un vide au-dessous de la pression atmosphérique ambiante, et dans ladite section de
formage, la teneur en solides de la pâte à papier déposée depuis la bâche d'alimentation
à travers la fente sur le tissu de formage s'élève depuis une valeur initiale faible
jusqu'à une valeur comprise entre environ 2% et environ 4%;
caractérisée en ce que
(i) la surface poreuse (26, 27) qui supporte le tissu de formage fournit un trajet
le long duquel se déplace le tissu de formage et lequel provoque un niveau contrôlé
d'agitations harmoniques périodiques uniformément espacées (48, 50) au sein de la
pâte à papier sur le tissu de formage;
(ii) des dispositifs d'évacuation comprenant une boîte de succion (100) qui s'étend
depuis le voisinage du dispositif poreux d'évacuation d'eau (6, 7) jusqu'à l'extrémité
de la section de formage, ladite boîte de succion comprenant une pluralité de chambres
évacuées (8, 9, 10, 11, 12); et
(iii) le système à vide établissant un vide dans les chambres évacuées de la boîte
de succion, commandé à une valeur qui s'élève progressivement le long de la longueur
de la boîte de succion depuis un minimum de 0,49 kPa (5 cm de colonne d'eau) au-dessous
de la pression atmosphérique ambiante au voisinage du dispositif poreux d'évacuation
d'eau jusqu'à une valeur maximum de 4,9 kPa (50 cm de colonne d'eau) au-dessous de
la pression atmosphérique ambiante à l'extrémité de la section de formage.
2. Appareil selon la revendication 1, caractérisé en ce que la boîte de succion (100)
comprend soit une boîte unique (100) qui s'étend depuis le voisinage du dispositif
poreux d'évacuation d'eau (6, 7) jusqu'à l'extrémité de la section de formage et qui
est pourvue d'une pluralité de divisions transversales étanches à la pression entre
chacune desquelles on peut appliquer un vide commander séparément, et qui comporte
chacune des moyens de drainage séparés (15, 16, 17, 18, 19) pour l'eau de blanchiment,
soit une pluralité de boîtes adjacentes et contiguës qui s'étendent depuis le voisinage
du dispositif poreux d'évacuation d'eau, dans chacune desquelles peut être admis un
vide commandé séparément, et qui comportent chacune des moyens de drainage séparés
(15, 16, 17, 18, 19) pour l'eau de blanchiment.
3. Appareil selon la revendication 1, caractérisé en ce que le dispositif d'évacuation
d'eau (6, 7) comprend deux dispositifs de drainage statiques, séparés et séparément
drainés, qui comprennent une partie constituant une planche de formage (6) au voisinage
de la fente (5) de la bâche d'alimentation, et une section séparé à feuilles (7) espacée
de la précédente, dans laquelle chaque feuille (29) comprend une surface de support
(30) plane, et une partie de queue (31) (dans la direction de déplacement du tissu
de formage) qui diverge du plan du tissu (1) sous un angle supérieur à 0° et inférieur
à 5°.
4. Appareil selon la revendication 1, caractérisé en ce que la surface poreuse sur la
boîte de succion comprend une couverture en tissu du type présentant des fentes, qui
comprend une série de lamelles (26) espacées qui supportent le tissu de formage, les
lamelles ayant une surface au sommet généralement plane et transversale à la direction
de déplacement du tissu, dans un plan commun essentiellement horizontal, et assurant
entre elles des intervalles accessibles à la succion, dans lesquels le tissu de formage
est sensiblement non-supporté et est tiré vers le bas afin de former dans lesdits
intervalles des ondulations qui agitent la pâte à papier, ladite couverture comprenant
des lamelles (27) qui forment une étanchéité vis-à-vis de l'eau disposées de façon
intermédiaire dans lesdits intervalles entre les lamelles qui supportent le tissu
et qui ont des surfaces au sommet transversales à la direction du déplacement du tissu
et à un niveau inférieur aux surfaces au sommet des lamelles qui supportent le tissu,
et formant au moins des joints à eau au niveau des ondulations inférieures du tissu
de formage, en interrompant ainsi temporairement la succion afin de limiter le drainage
tout en entraînant une agitation verticale des fibres du tissu qui passe à travers
la section de formage; et en ce que la première lamelle de support, la dernière lamelle
de support et toute lamelle de support intermédiaire placée au-dessus d'un compartiment
inteme transversal étanche au vide ou une paire de parois transversales contiguës
de deux boîtes de succion adjacentes, forment toutes des lamelles (26) qui supportent
le tissu.
5. Appareil selon la revendication 3, caractérisé en ce que dans la section à feuilles,
les feuilles séparées (29) sont placées de manière à contribuer à une agitation contrôlée
de la pâte à papier sur le tissu de formage.
6. Procédé pour améliorer la formation de papier dans une machine à papier ayant une
section de formage à la surface ouverte qui comprend au moins un tissu de formage
continu (1) en déplacement qui passe sur un rouleau de tête (2) adjacent à une bâche
d'alimentation (4) qui comporte une fente (5) à travers laquelle de la pâte à papier
aqueuse est déposée sur le tissu de formage, et une pluralité de dispositifs d'évacuation
d'eau hors de la pâte à papier au-dessous du tissu de formage et comprenant des moyens
de drainage pour l'eau de blanchiment, un dispositif poreux d'évacuation d'eau (6,
7) adjacent à la fente de la bâche d'alimentation et comprenant une pluralité d'éléments
de drainage stationnaires disposés en relation de supportage sensiblement transversalement
au tissu de formage, une surface poreuse (26, 27) sur les dispositifs d'évacuation
d'eau étant adaptée à supporter le tissu de formage et à fournir à la fois les ouvertures
à travers lesquelles le tissu de formage est drainé et un joint étanche au vide entre
le tissu de formage et les moyens de drainage, et un système à vide comprenant des
moyens de fourniture de vide, des moyens de commande de vide, et des moyens formant
joints pour les moyens de drainage de l'eau de blanchiment, grâce à quoi un vide au-dessous
de la pression atmosphérique ambiante est appliquée dans chacun des moyens de drainage;
procédé dans lequel, dans ladite section de formage, la teneur en solides de la pâte
à papier déposée depuis la bâche d'alimentation et à travers la fente sur le tissu
de formage augmente depuis une valeur initiale faible jusqu'à une valeur comprise
entre environ 2% et environ 4%, ledit procédé comprenant les opérations consistant
à décharger sur le tissu de formage en déplacement une pâte à papier fibreuse et aqueuse
sur la largeur du tissu de formage, et à amener le tissu de formage à se déplacer
le long de la section de formage, caractérisé en ce que :
(i) un niveau contrôlé d'agitations harmoniques périodiques uniformément espacées
est provoqué dans la pâte à papier, en amenant le tissu de formage à suivre un trajet
construit et agencé de manière à induire les agitations désirées;
(ii) un niveau contrôlé de vide au-dessous de la pression atmosphérique ambiante est
appliquée au-dessous du tissu de formage au moyen d'une boîte de succion qui s'étend
depuis le voisinage du dispositif poreux d'évacuation d'eaujusqu'à l'extrémité de
la section de formage, le vide appliqué augmentant depuis un minimum de 0,049 kPa
(5 cm de colonne d'eau) au-dessous de la pression ambiante au voisinage du dispositif
poreux d'évacuation d'eau, jusqu'à une valeur maximum de 4,9 kPa (50 cm de colonne
d'eau) au-dessous de la pression atmosphérique ambiante à l'extrémité de la section
de formage.
7. Procédé selon la revendication 6, caractérisé en ce que la boîte de succion (100)
comprend soit une boîte unique qui s'étend depuis le voisinage du dispositif poreux
d'évacuation d'eau (6, 7) jusqu'à l'extrémité de la section de formage et qui comprend
une pluralité de sections transversales étanches à la pression, entre chacune desquelles
on peut appliquer un vide commandé séparément, et qui comportent chacune des moyens
de drainage séparés (15, 16, 17, 18, 19) pour l'eau de blanchiment, soit une pluralité
de boîtes adjacentes et contiguës qui s'étendent depuis le voisinage du dispositif
poreux d'évacuation d'eau, à chacune desquelles peut être appliqué un vide séparément
commandé, et qui comportent chacune un moyen de drainage séparé (15, 16, 17, 18, 19)
pour l'eau de blanchiment.
8. Procédé selon la revendication 6, caractérisé en ce que :
(a) on décharge une pâte à papier fibreuse et aqueuse sur le tissu de formage en déplacement
et sur la largeur de celui-ci;
(b) le tissu de formage se déplace sur un dispositif poreux d'évacuation d'eau qui
comprend en combinaison une section constituée par une plaque de formage, adjacente
à la fente de la bâche d'alimentation, et une section à feuilles dans laquelle chaque
feuille comprend une surface de support plane, et une partie de queue (dans la direction
de déplacement du tissu de formage) qui diverge du plan du tissu sous un angle supérieur
à 0° et inférieur à 5°,
(c) le tissu de formage se déplace ensuite au-dessus d'une boîte de succion continue
comprenant une pluralité de chambres à chacune desquelles on applique un niveau de
vide commandé, suivant des zones écartées de façon uniforme transversalement à la
direction de déplacement du tissu, et permettant au tissu de s'affaisser dans les
intervalles entre les zones supportées et formant dans lesdits intervalles des ondulations
verticales dans le tissu, induisant par conséquent des agitations harmoniques périodiques
uniformément espacées dans la pâte à papier;
(d) des moyens formant joint vis-à-vis de l'eau sont prévus en position intermédiaire
dans les intervalles dans un plan au-dessous du lieu où le tissu est supporté afin
d'interrompre la succion;
(e) on applique du vide dans lesdits intervalles et à la face inférieure du tissu
de formage afin de tirer le tissu vers le bas entre les intervalles, la succion appliquée
dans chaque intervalle étant interrompue par les moyens formant joint tandis que la
suspension aqueuse des fibres est égouttée;
(f) on commande le vide appliqué dans les chambres au-dessous des intervalles de telle
manière que le vide appliqué augmente progressivement depuis une valeur minimum de
0,49 kPa (5 cm de colonne d'eau) au-dessous de la pression atmosphérique ambiante
au voisinage de l'unité à feuilles, jusqu'à une valeur maximum qui ne dépasse pas
4,9 kPa (50 cm de colonne d'eau) au-dessous de la pression atmosphérique ambiante
à l'extrémité de la section de formage.