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EP 0 158 938 B1 |
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EUROPEAN PATENT SPECIFICATION |
(45) |
Mention of the grant of the patent: |
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20.12.1989 Bulletin 1989/51 |
(22) |
Date of filing: 04.04.1985 |
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(51) |
International Patent Classification (IPC)4: D21F 11/00 |
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(54) |
Apparatus for the manufacture of fibrous webs
Vorrichtung zur Herstellung von Faserbahnen
Dispositif pour la fabrication de nappes fibreuses
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Designated Contracting States: |
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AT BE CH DE FR GB IT LI NL SE |
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Priority: |
16.04.1984 US 600679
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Date of publication of application: |
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23.10.1985 Bulletin 1985/43 |
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Proprietor: James River-Norwalk, Inc. |
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Norwalk
Connecticut 06856 (US) |
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Inventors: |
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- Cheshire, James Oscar
Neenah
Wisconsin 54956 (US)
- Marinack, Robert John
Oshkosh
Wisconsin 54901 (US)
- Van den Akker, Johannes Archibald
Appleton
Wisconsin 54911 (US)
- Lindgren, Douglas Leroy
Appleton
Wisconsin 54911 (US)
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(74) |
Representative: Schupfner, Gerhard D. et al |
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Patentanwälte
Müller, Schupfner & Gauger
Postfach 17 53 21236 Buchholz 21236 Buchholz (DE) |
(56) |
References cited: :
DE-A- 2 620 033
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US-A- 3 938 782
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Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
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[0001] This invention relates to an apparatus for forming and directing a foam-fiber furnish
onto a forming wire in the manufacture of a fibrous web, with a slice positioned and
operative to deposit said foam-fiber furnish onto said forming wire; and a headbox
channel in direct fluid flow communication with said slice and including an inner
wall portion; a plurality of foam-forming openings in fluid flow connection with said
headbox channel and positioned and adapted to receive a foamable liquid-fiber furnish
and to form and forcible direct foam-fiber furnish having a relatively low viscosity
into said channel to impinge upon said inner wall portion and flow throughout said
channel, the recited impingement being effective to create turbulence in the low-viscosity
foam-fiber furnish in said channel immediately upon its flow through said slice, whereby
random orientation of the fibers in the furnish is insured throughout said channel
and as it flows through said slice for deposit on said forming wire.
[0002] In the manufacture of fibrous webs, such as paper, from a foam-fiber furnish deposited
on a forming wire from the slice of a conventional foam-forming headbox, it has been
found difficult to maintain a desired random orientation of fibers ensuring optimum
MD/CD tensile strength of the formed sheet at the preferred, relatively high wire
speeds associated with papermaking. Efforts at achieving a desired fiber orientation
have involved delivering the foam-fiber furnish to the slice, immediately upon creation
of the furnish.
[0003] DE-A-2 620 033 discloses an apparatus for forming and directing a foam-fibre furnish
onto a forming wire in the manufacture of a fibrous web, with a slice positioned and
operative to deposit said foam-fibre furnish onto said forming wire. A headbox channel
in direct fluid flow communication with the slice includes inner wall portions. A
plurality of foam-forming openings is in fluid flow connection with said headbox channel
and is positioned and adapted to receive the foamable liquid-fibre furnish and to
form and forcibly direct foam-fibre furnish having a relatively low viscosity into
said channel, whereby the foam-fibre furnish impinges upon the inner wall portion
and flows throughout said channel through the slice. The recited impingement creates
turbulence in the low-viscosity foam-fibre furnish whereby random orientation of the
fibres in the furnish is insured throughout said channel and as it flows through said
slice for deposit on said forming wire.
[0004] The invention contemplates an improvement on the foregoing explained apparatus in
such a manner that a better turbulent flow of the foam-fiber furnish is created to
obtain a better random fiber orientation.
[0005] The improvement is characterized in that each of said foam-forming openings are nozzles,
which comprises means defining a generally tubular fluid passage having regions of
alternate lesser and greater cross sectional areas.
[0006] Such nozzles with alternate cross sectional areas create a turbulent flow immediately
and especially prior said foam-fiber furnish passes said slice.
[0007] It is important, how the inner wall portion of the headbox channel is formed. Preferred
embodiments of the invention are therefore characterized in that the inner wall portion
is substantially planar, curved or cylindrical.
[0008] Furthermore the turbulent flow will advantageously be improved with a feature characterized
in that said channel is provided with a second array of foam forming nozzles positioned
to direct foam-fiber furnish onto an opposing wall of said channel, or with a feature
characterized in that a plurality of rows of foam forming nozzles extend longitudinally
of said cylindrical channel and so positioned as to direct foam-fiber furnish into
said channel in a radial direction.
[0009] Another preferred embodiment of the invention is achieved with the feature, characterized
in that said foam forming nozzles are so positioned as to direct a stream of foam-fiber
furnish into said channel to impinge upon at least one stream of foam-fiber furnish
from another of said foam-forming nozzles.
[0010] A further preferred embodiment of the invention is characterized in that said second
array of nozzles is arranged to forcibly discharge foam-fiber furnish in a non-intersecting
path relative to paths of flow of foam-fiber furnish from said first array of nozzles.
[0011] The invention apparatus will furthermore be especially effective by a construction
characterized in that each said nozzle is about 7.6 cm (about 3 inches) long, said
bore is generally cylindrical, said lesser cross sectional areas are of about 1.3
cm (about 1/2 inch) diameter, said greater cross sectional areas are of about 1.9
cm (about 3/4 inch) diameter, and said regions are spaced axially of the nozzle about
1.3 cm (about 1/ 2 inch), and further wherein the recited connection of said nozzles
with said headbox is about 5 cm (about 2 inches) from said inner wall portion.
[0012] A further preferred embodiment of the headbox channel is characterized by an apparatus
according to Claim 1, including wall portions of the headbox defining the channel
in substantially direct fluid flow communication with said slice, at least one pair
of said wall portions being in mutually confronting spaced relation; and an array
of foam forming nozzles connected through one of the confronting wall portions to
said headbox channel and positioned and operative to impinge upon the other of said
confronting wall portions.
[0013] A further preferred embodiment of the invention is characterized in that said channel
further is defined by an additional pair of closely spaced confronting wall portions
extending transversely of said first recited pair of wall portions; and at least one
wall portion of the second recited pair having connected therethrough to said channel
a second array of foam forming nozzles positioned and adapted to direct foam-fiber
furnish for impingement on the opposite wall portion of said second pair and flow
through said slice.
[0014] Further preferred embodiments of the invention are characterized in that said impact
surface is substantially perpendicular to the polar axis of a nozzle and that said
forming wire is linearly movable at a predetermined speed, and the speed at which
said furnish is deposited is in excess of the speed of movement of said forming wire.
Brief description of the drawing
[0015]
Figure 1 is a diagrammatic showing of a web forming apparatus embodying the invention;
Figure 2 is a detailed showing, on an enlarged scale and partly in section, of a portion
of the apparatus seen in Figure 1, and illustrating important structural features
of the invention.
Figure 3 is a top plan view of the portion of apparatus seen in Figure 2; and
Figures 4 to 7 are showings similar to Figure 2, and illustrating modified embodiments
of the invention.
Detailed description of the several embodiments
[0016] With more detailed reference to the drawing, there is seen in Figure 1 a web forming
apparatus 10 comprising a headbox 11 provided with a channel 11 a leading to throat
12a of an adjustable slice 12 positioned and operative to discharge a foam-fiber furnish
onto a forming wire 13 as it passes over a breast roll 14. Adjustment of the slice
is afforded by a roof or upper wall 12b of throat 12a mounted for pivotal movement
about hinge P, and positionable by a conventional jack means 12c. Suction boxes 15
and 16 are disposed beneath wire 13, and are connected to a vacuum source 17 for receiving
both foam and liquid derived from collapsed foam, and drained through the wire. Drained
foam and liquid are returned by a pump 18 through conduit 19 to an in-line mixer 20
for reuse, where additional fiber, either dry or as a dispersion, and air are introduced
through pipe 33 to conduit 19, by means of a known metering device such as is seen
at 32, to form a dispersion of air and fiber in water containing a surfactant in creation
of a foamable furnish. From mixer 20, the foamable furnish is fed under pressure by
a pump 21 through an input conduit 22 to a manifold 23. It will be understood that
elements of the web forming apparatus thus far described are conventional, as exemplified
by the referenced U.S. Patent No. 3,938,782.
[0017] In especial accordance with the present invention, and with reference also to Figures
2 and 3, improvement over the art resides in that manifold 23 leads to parallel arrays
of foamable liquid-fiber furnish inlet nozzles 24 having tubular passages such as
bores 25 of alternately increased and decreased cross sectional areas. By such a bore
configuration, the decreased cross sectional areas in combination with the increased
cross sectional areas respectively effect alternate increases and decreases in the
flow speed of the foamable furnish within the nozzles, thereby creating foam-forming
tubulence. This same bore configuration is shear inducing, thereby lowering the apparent
viscosity of the foam leaving the nozzles.
[0018] Further to the nozzles 24, they function as the sole foam forming devices in the
present invention, and are disposed in direct fluid flow communication with the channel
11a of headbox 11 defined by substantially planar, generally parallel, relatively
closely spaced upper and lower, horizontally extending wall portions 26 and 27, respectively,
side wall portions 28 and 29, and front and rear wall portions 30 and 31, respectively.
Construction and arrangement of the wall portions is such that the channel 11 a has
its major extent in a direction transverse the direction of forming wire movement.
[0019] The inlet connections of the one array of eleven nozzles 24 to the headbox extend
through wall 26 in such a manner that foam-fiber furnish is directed from nozzles
24 at relatively low viscosity, transversely of the direction of extent of and onto
a confronting, interior surface of wall portion 27 of headbox channel 11a. By such
cooperative disposition, wall portion 27 serves as a turbulent flow inducing impact
surface for the foam-fiber furnish. While the several walls or wall portions have
been described and illustrated as being planar and parallel, it should be understood
that they may be positioned out of parallel, or may be curved. For example, headbox
channel 11a might be defined by a generally cylindrical wall portion.
[0020] The inlet connections of the other array of twelve nozzles 24 to the headbox extend
through wall 31 to direct foam-fiber furnish onto confronting wall 30, which also
functions as an impact surface extending transversely of the direction of entry of
foam-fiber furnish from the one array of eleven nozzles 24. As is best seen in Figure
3, the nozzles 24 further are arranged such that the nozzle axes of the one array
are between and generally in a plane perpendicular to the general plane of the nozzle
axes of the other array.
[0021] In a preferred embodiment, the axes of the eleven nozzles 24 of the one array are
spaced along the headbox about 5 cm (two inches) apart, as are similarly spaced the
twelve nozzles of the other array; by this spacing, the headbox extends about 61 cm
(two feet) in the cross machine direction. Additional arrays or fractions thereof
may be provided in accommodation of other machine widths. Each of nozzles 24 is about
7.6 cm (3 inches) in length and has a generally undulatory bore configuration defined
by alternate convergent and divergent frustoconical sections. Generally, the narrower
sections of lesser cross sectional area are about 1.3 cm (1/2 inch) diameter, and
the wider sections of greater cross sectional area are about 1.9 cm (3/4 inch) diameter,
with a distance between sections of about 1.3 cm (1/2 inch). The distance between
the discharge end of each bore 25 and a confronting baffle or wall of channel 11a
is about 5 cm (2 inches). By such disposition of the nozzles the streams of foam-fiber
furnish flowing from the nozzles at low viscosity impinge partially on one another
and fully on the confronting impact surfaces or walls of the headbox channel at relatively
short distances from the slice 12.
[0022] Since foam flowing from nozzles 24 is at its lowest apparent viscosity, a condition
under which it is most likely to become turbulent, the abrupt changes of direction
due to the hereinabove described impingements advantageously create considerable turbulence
in channel 11a immediately prior to flow of the foam-fiber furnish through the relatively
short throat 12a to slice 12 for uniform distribution onto forming wire 13. Throat
12a of slice 12 is about 41 cm (16 inches) long so that the foam with its dispersion
of randomly oriented fibers advantageously travels a relatively short distance from
the headbox channel through the slice throat, thereby minimizing unidirectional orientation
as the foam tends to revert to laminar flow in the slice throat. Hence, apparatus
embodying the invention achieves desirable, relatively low MD/ CD ratios of fibrous
webs with minimization of the number of moving parts.
[0023] In the additional, modified embodiments of the invention as seen in Figures 4 to
6, the foam forming nozzles are in fluid flow communication with the headbox channel
at different locations than those hereinabove described. In the additional, modified
embodiment seen in Figure 7, the headbox channel is generally cylindrical, affording
curved walls as briefly described hereinabove, and the axes of the nozzles are located
along the length of the channel as are the axes of the nozzles in Figures 1 to 3.
[0024] In Figure 4, the several walls 126 through 131 of headbox 111, similar to the one
described in connection with Figures 1 to 3, define a channel 111 a leading to throat
112a for feeding foam-fiber furnish through adjustable slice 112 onto forming wire
113 moving on breast roll 114. Nozzles 124 are similar to the hereinabove described
foam forming nozzles 24, and, while arranged in staggered array, are provided only
in top wall 126, whereby foam-fiber furnish introduced into the channel impinges upon
lower wall 127 as an impact surface.
[0025] In Figure 5, reference numerals refer to like numerals as seen in Figures 1, or 3,
but with the prefix 2 applied. It is seen that foam forming nozzles 224 are so positioned
that one array is connected to the headbox channel 2121a through top wall 226 and
the other array is offset as respects the one array and is connected to the channel
through bottom wall 227. In this construction the foam-fiber furnish introduced to
the headbox channel through upper nozzles 224 impinges upon lower wall 227 and flows
through throat 212a, while furnish introduced through lower nozzles 224 impinges on
upper wall 226 and mingles with the furnish introduced through the upper nozzles as
it flows through throat 212a.
[0026] In Figure 6, elements are designated with numerals used to designate like elements
of Figures 1, 2 and 3, but with the prefix 3 applied, and it is seen that all nozzles
324 are connected to the headbox channel 311 a through wall 331 for impingement of
the foam fiber furnish onto opposite wall 330.
[0027] In Figure 7, elements are designated with numerals used to designate like elements
of Figures 1, 2, and 3, but with the prefix 4 applied. In Figure 7, the horizontally
extending headbox channel 411 a is defined by curved wall portions of a hollow cylindrical
structure about 5.7 cm (2 1/4 inches) in diameter and closed at its ends by walls,
one of which is seen at 428. A cylindrical channel advantageously affords a compact
arrangement for three arrays of foaming nozzles 424 of the type hereinabove described,
and whose centerlines are spaced about 5.7 cm (2 1/4 inches) apart along the length
of the channel. The arrays are disposed in fluid flow communication with channel 411
in upper left and right quadrants and in the lower right quadrant of the cylindrical
wall portions of the channel so that each nozzle is effective to direct foam-fiber
furnish transversely of the polar axis of the cylindrical structure onto an opposed
curved, cylindrical wall portion serving as an impact surface. The entrance of the
slice throat 412a occupies the lower left quadrant. While the nozzles are shown in
the same plane for the sake of convenience, it will be understood that the nozzles
of each array are staggered as respects the nozzles of the other arrays, so that the
spacing between centerlines of the nozzles as between arrays is about 1.9 cm (3/4
inch).
[0028] In any of the embodiments shown in Figures 1 to 6, the impact surface is relatively
closely spaced from the region of introduction of the foaming nozzle to the relatively
low-volume headbox channel, which impact surface also is substantially perpendicular
to the axis of a nozzle. In the embodiment shown in Figure 7, essentially the same
spatial relationship exists, with the tangent to the cylindrical surface at the center
of the impact being substantially perpendicular to the axis of a nozzle. By such cooperative
dispositions of the nozzles and impact surfaces, taken with a headbox channel of relatively
small volume, turbulent foam flow is achieved throughout the channel and well into
the slice throat. This turbulent flow advantageously maximizes random orientation
of fibers well into the slice throat and as they exit the slice for deposition on
the forming wire.
1. Apparatus for forming and directing a foam-fiber furnish onto a forming wire in
the manufacture of a fibrous web, with a slice (12) positioned and operative to deposit
said foam-fiber furnish onto said forming wire (13, 113, 213, 313, 413); and a headbox
channel (11a, 111a, 211a, 311a, 411 a) in direct fluid flow communication with said
slice (12) and including an inner wall portion (27, 30, 127, 227, 330); a plurality
of foam-forming openings (24, 124, 224, 324, 424) in fluid flow connection with said
headbox channel (11a, 111a, 211a, 311a, 411a) and positioned and adapted to receive
a foamable liquid-fiber furnish and to form and forcible direct foam-fiber furnish
having a relatively low viscosity into said channel to impinge upon said inner wall
portion (27,30,127, 227, 330) and flow throughout said channel, the recited impingement
being effective to create turbulence in the low-viscosity foam-fiber furnish in said
channel immediately upon its flow through said slice (12,112, 212, 312, 412) whereby
random orientation of the fibers in the furnish is insured throughout said channel
and as it flows through said slice for deposit on said forming wire (13, 113, 213,
313, 413);
characterized in that each of said foam-forming openings (24, 124, 224, 324, 424)
are nozzles, which comprises means defining a generally tubular fluid passage having
regions of alternate lesser and greater cross sectional areas.
2. Apparatus of Claim 1, characterized in that said inner wall portion (27, 30, 127,
227, 330) is substantially planar.
3. Apparatus of Claim 1, characterized in that said inner wall portion is curved.
4. Apparatus of Claim 3, characterized in that said curved inner wall portion is a
cylindrical section.
5. Apparatus according to any of Claims 1 to 4 characterized in that said channel
(11a, 211a, 311a, 411a) is provided with a second array of foam forming nozzles (124,
224, 324, 424) positioned to direct foam-fiber furnish onto an opposing wall (127,
227, 330) of said channel (111a, 211a, 311a, 411a).
6. Apparatus according to Claim 4 characterized in that a plurality of rows of foam
forming nozzles (424) extend longitudinally of said cylindrical channel (411a) so
positioned as to direct foam-fiber furnish into said channel (411a) in a radial direction.
7. Apparatus according to any of Claims 1-5 characterized in that said foam forming
nozzles (24, 424) are so positioned as to direct a stream of foam fiber furnish into
said channel (11a, 411a) to impinge upon at least one stream of foam-fiber furnish
from another of said foam-forming nozzles.
8. Apparatus according to any of Claims 1-5 characterized in that said second array
of nozzles (124, 224, 324) is arranged to forcibly discharge foam-fiber furnish in
a non-intersecting path relative to paths of flow of foam-fiber furnish from said
first array of nozzles.
9. Apparatus according to Claim 1, wherein each said nozzle (24,124,224,324) is about
7.6 cm (about 3 inches) long, said bore (25, 125, 225, 325) is generally cylindrical,
said lesser cross sectional areas are of about 1.3 cm (about 1/2 inch) diameter, said
greater cross sectional areas are of about 1.9 cm (about 3/4 inch) diameter, and said
regions are spaced axially of the nozzle about 1.3 cm (about 1/2 inch), and further
wherein the recited connection of said nozzles with said headbox (11, 111, 211, 311)
is about 5 cm (about 2 inches) from said inner wall portion.
10. Apparatus according to Claim 1 characterized by including wall portions (26, 27,
30; 126, 127; 227, 330, 331) of the headbox defining the channel (11a, 111a, 211a,
311a) in substantially direct fluid flow communication with said slice, at least one
pair of said wall portions being in mutually confronting spaced relation; and an array
of foam forming nozzles (24, 124, 224, 324, 424) connected through one of the confronting
wall portions (26, 126, 227, 331) to said headbox channel and positioned and operative
to impinge upon the other of said confronting wall portions (27, 30, 127, 330).
11. Apparatus according to Claim 10, characterized in that said channel (311a) further
is defined by an additional pair of closely spaced confronting wall portions (330,
331) extending transversely of said first recited pair of wall portions (326, 327);
and at least one wall portion (331) of the second recited pair having connected therethrough
to said channel a second array of foam forming nozzles positioned and adapted to direct
foam-fiber furnish for impingement on the opposite wall portion (330) of said second
pair and flow through said slice (312).
.12. Apparatus of Claim 10 characterized in that said impact surface is substantially
perpendicular to the polar axis of a nozzle.
13. Apparatus of Claim 1 or 10 characterized in that said forming wire (13, 113, 213,
313, 413) is linearly movable at a predetermined speed, and the speed at which said
furnish is deposited is in excess of the speed of movement of said forming wire.
1. Vorrichtung zum Formen und Leiten eines Schaumfaserstoffs auf ein Formsieb bei
der Herstellung einer Faserstoffbahn, wobei eine Stauvorrichtung (12) so angeordnet
ist, daß sie den Schaumfasserstoff aus das Formsieb (13, 113, 213, 313, 413) aufgibt,
und ein Stoffauflaufkanal (11a, 111a, 211a, 311a, 411a) in direkter Fluidströmungsverbindung
mit der Stauvorrichtung (12) steht und einen Innenwandabschnitt (27, 30, 127, 227,
330) aufweist; mit mehreren schaumbildenden Öffnungen (24, 124, 224, 324, 424), die
mit dem Stoffauflaufkanal (11 a, 111 a, 211a, 311a, 411a) in Fluidströmungsverbindung
stehen und so angeordnet und ausgelegt sind, daß sie einen schäumbaren Flüssigfasereintrag
erhalten und einen Schaumfaserstoff relativ niedriger Viskosität unter Druck in den
Kanal richten, so daß er auf den Innenwandabschnitt (27, 30, 127, 227, 330) aufprallt
und den gesamten Kanal durchfließt, wobei der genannte Aufprall eine Turbulenz in
dem niedrigviskosen Schaumfaserstoff im Kanal unmittelbar beim Durchfließen der Stauvorrichtung
(12, 112, 212, 312, 412) erzeugt, so daß eine Wirrlage der Fasern im Stoff durch den
gesamten Kanal und während des Durchfließens der Stauvorrichtung zur Aufgabe auf das
Formsieb (13, 113, 213, 313, 413) gewährliestet ist
dadurch gekennzeichnet, daß sämtliche schaumbildenden Öffnungen (24, 124, 224, 324,
424) Düsen sind, die einen im wesentlichen rohrförmigen Fluidkanal definierende Mittel
aufweisen, die Bereiche mit alternierend kleineren und größeren Querschnittsflächen
haben.
2. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß der Innenwandabschnitt
(27, 30,127, 227, 330) im wesentlichen eben ist.
3. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß der Innenwandabschnitt
gekrümmt ist.
4. Vorrichtung nach Anspruch 3, dadurch gekennzeichnet, daß der gekrümmte Innenwandabschnitt
ein Zylinderabschnitt ist.
5. Vorrichtung nach einem der Ansprüche 1-4, dadurch gekennzeichnet, daß der Kanal
(11a, 211a, 311a, 411a) eine zweite Reihe schaumbildende Düsen (124, 224, 324, 424)
aufweist, die so angeordnet sind, daß sie Schaumfaserstoff auf eine gegenüberstehende
Wand (127, 227, 330) des Kanals (111a, 211a, 311a, 411a) richten.
6. Vorrichtung nach Anspruch 4, dadurch gekennzeichnet, daß mehrere Reihen von schaumbildenden
Düsen (424) in Längsrichtung des zylindrischen Kanals (411a) verlaufen und so angeordnet
sind, daß sie Schaumfaserstoff in Radialrichtung in den Kanal (411a) richten.
7. Vorrichtung nach einem der Ansprüche 1-5, dadurch gekennzeichnet, daß die schaumbildenden
Düsen (24, 424) so angeordnet sind, daß sie einen Schaumfaserstoffstrom so in den
Kanal (11a, 411a) richten, daß dieser auf wenigstens einen Schaumfaserstoffstrom aus
einer anderen der schaumbildenden Düsen auftrifft.
8. Vorrichtung nach einem der Ansprüche 1-5, dadurch gekennzeichnet, daß die zweite
Reihe Düsen (124, 224, 324) so angeordnet ist, daß sie Schaumfaserstoff in eine Bahn
auspressen, die keine der Strömungsbahnen von Schaumfaserstoff aus der ersten Reihe
Düsen schneidet.
9. Vorrichtung nach Anspruch 1, dadurch gekennzeichnet, daß jede Düse (24, 124, 224,
324) eine Länge von ca. 7,6 cm (ca. 3") hat, die Bohrung (25, 125, 225, 325) im wesentlichen
zylindrisch ist, die kleineren Querschnittsflächen einen Durchmesser von ca. 1,3 cm
(ca. 1/2") und die größeren Querschnittsflächen einen Durchmesser von ca. 1,9 cm (ca.
3/4") haben und die genannten Bereiche in Axialrichtung der Düse um ca. 1,3 cm (ca.
1/2") beabstandet sind, und daß der Anschluß der Düsen an den Stoffauflauf (11, 111,
211, 311) ca. 5 cm (ca. 2") von dem Innenwandabschnitt entfernt ist.
10. Vorrichtung nach Anspruch 1, gekennzeichnet durch den Kanal (11a, 111a, 211a,
311a) definierende Wandabschnitte (26, 27, 30; 126, 127; 227, 330, 331) in im wesentlichen
direkter Fluidströmungsverbindung mit der Stauvorrichtung, wobei wenigstens ein Paar
der Wandabschnitte einander mit Abstand gegenübersteht; und eine Reihe von schaumbildenden
Düsen (24, 124, 224, 324, 424), die durch einen der gegenüberstehenden Wandabschnitte
(26, 126, 227, 331) an den Stoffauflaufkanal angeschlossen und so positioniert sind,
daß der Aufprall auf den anderen der gegenüberstehenden Wandabschnitte (27, 30, 127,
330) erfolgt.
11. Vorrichtung nach Anspruch 10, dadurch gekennzeichnet, daß der Kanal (311a) ferner
durch eine zusätzliches Paar von eng beabstandeten gegenüberstehenden Wandabschnitten
(330, 331), die quer zu dem erstgenannten Paar von Wandabschnitten (326, 327) verlaufen,
definiert ist; und daß durch wenigstens einen Wandabschnitt (331) des zweitgenannten
Paars eine zweite Reihe von schaumbildenden Düsen an den Kanal angeschlossen und so
angeordnet und ausgelegt ist, daß Schaumfaserstoff aus ihnen so gerichtet wird, daß
er auf den gegenüberstehenden Wandabschnitt (330) des zweiten Paars aufprallt und
durch die Stauvorrichtung (312) fließt.
12. Vorrichtung nach Anspruch 10, dadurch gekennzeichnet, daß die Aufprallfläche im
wesentlichen senkrecht zu der Polarachse einer Düse ist.
13. Vorrichtung nach Anspruch 1 oder Anspruch 10, dadurch gekennzeichnet, daß das
Formsieb (13, 113, 213, 313, 413) mit vorbestimmter Geschwindigkeit linear bewegbar
ist und daß die Geschwindigkeit, mit der der Eintrag aufgebracht wird, höher als die
Laufgeschwindigkeit des Formsiebs ist.
1. Appareil pour former et diriger une composition de mousse-fibre sur une toile de
formation dans la fabrication d'une nappe fibreuse, une règle (12) étant placée et
intervenant de façon à déposer ladite composition de mousse-fibre sur ladite toile
de formation (13, 113, 213, 313, 413); et un canal de caisse d'arrivée (11a, 111a,
211a, 311a, 411a) en communication directe d'écoulement de fluide avec ladite règle
(12) et comportant une partie de paroi intérieure (27, 30, 127, 227, 330); plusieurs
ouvertures (24, 124, 224, 324, 424) de formation de mousse en liaison d'écoulement
de fluide avec ledit canal (11a, 111a, 211a, 311a, 411a) de caisse d'arrivée et placées
et conçues pour recevoir une composition de liquide pouvant mousser et de fibre et
pour former et diriger à force la composition de mousse-fibre, ayant une viscosité
relativement basse, dans ledit canal afin qu'elle heurte ladite partie de paroi intérieure
(27, 30, 127, 227, 330) et s'écoule dans ledit canal, le heurt cité ayant pour effet
d'engendrer une turbulence dans la composition de mousse-fibre à basse viscosité dans
ledit canal dès qu'il s'écoule à travers ladite règle (12, 112, 212, 312, 412) afin
qu'une orientation aléatoire des fibres dans la composition soit assurée dans tout
ledit canal et lorsque la composition s'écoule à travers ladite règle pour se déposer
sur ladite toile de formation (13, 113, 213, 313, 413);
caractérisé en ce que chacune desdites ouvertures (24, 124, 224, 324, 424) de formation
de mousse est une buse qui comprend des moyens définissant une passage de fluide globalement
tubulaire ayant des zones de sections transversales alternativement plus petites et
plus grandes.
2. Appareil selon la revendication 1, caractérisé en ce que ladite partie de paroi
intérieure (27, 30, 127, 227, 330) est sensiblement plane.
3. Appareil selon la revendication 1, caractérisé en ce que ladite partie de paroi
intérieure est incurvée.
4. Appareil selon la revendication 3, caractérisé en ce que ladite partie de paroi
intérieure incurvée est un tronçon cylindrique.
5. Appareil selon l'une quelconque des revendications 1 à 4, caractérisé en ce que
ledit canal (11a, 211a, 311a, 411a) comporte une seconde rangée de buses (124, 224,
324, 424) de formation de mousse disposées de façon à diriger une composition de mousse-fibre
sur une paroi opposée (127, 227, 330) dudit canal (111a, 211a, 311a, 411a).
6. Appareil selon la revendication 4, caractérisé en ce que plusieurs rangées de buses
(424) de formation de mousse s'étendent longitudinalement audit canal cylindrique
(411a) afin d'être placées de manières diriger la composition de mousse-fibre dans
ledit canal (411a) dans une direction radiale.
7. Appareil selon l'une quelconque des revendications 1-5, caractérisé en ce que lesdites
buses (24, 424) de formation de mousse sont disposées de façon à diriger un courant
de composition de mousse-fibre dans ledit canal (11a, 411a) afin qu'il heurte au moins
un courant de composition de mousse-fibre provenant d'une autre desdites buses de
formation de mousse.
8. Appareil selon l'une quelconque des revendications 1-5, caractérisé en ce que ladite
seconde rangée de buses (124, 224, 324) est agencée de façon à décharger à force la
composition de mousse-fibre en un trajet ne coupant pas les trajets d'écoulement de
la composition de mousse-fibre provenant de ladite première rangée de buses.
9. Appareil selon la revendication 1, dans lequel chacune des buses (24, 124, 224,
324) a une longueur d'environ 7,6 cm (environ 3 inches), ladite lumière (25, 125,
225, 325) est globalement cylindrique, lesdites sections transverales plus petites
ont un diamètre d'environ 1,3 cm (environ 1/2 inch), lesdites sections transversales
plus grandes ont un diamètre d'environ 1,9 cm (environ 3/4 inch), et lesdites zones
sont espacées axialement à la buse d'environ 1,3 cm (environ 1/2 inch), et dans lequel,
en outre, la liaison citée desdites buses avec ladite caisse d'arrivé (11, 111, 211,
311) est à environ 5 cm (environ 2 inches) de ladite partie de la paroi intérieure.
10. Appareil selon la revendication 1, caractérisé en ce qu'il comporte des parties
de parois (26, 27, 30; 126, 127; 227, 330, 331) de la caisse d'arrivée définissant
le canal (11a, 111a, 211a, 311a) en communication d'écoulement de fluide sensiblement
directe avec ladite régle, au moins une paire desdites parties de parois étant dans
une disposition mutellement en vis-à-vis; et une rangée de buses (24, 124, 224, 324,
424) de formation de mousse étant reliée à travers l'une des parties de parois en
vis-à-vis (26, 126, 227, 331) audit canal de la caisse d'arrivée et étant placée et
intervenant de façon à amener la composition à heurter l'autre desdites parties de
parois en vis-à-vis (27, 30, 127, 330).
11. Appareil selon la revendication 10, caractérisé en ce que ledit canal (311 a)
est en outre défini par une paire supplémentaire de parties de parois (330, 331) en
vis-à-vis, rapprochées, s'étendant transversalement à ladite première paire citée
de parties de parois (326, 327); et au moins une partie de paroi (331) de la seconde
paire citée comportant, reliée à traves elle audit canal, une seconde rangée de buses
de formation de mousse placées et conçues pour diriger une composition de mouse-fibre
afin qu'elle heurte la partie de paroi opposée (330) de ladite seconde paire et s'écoule
à travers ladite régie (312).
12. Appareil selon la revendication 10, caractérisé en ce que ladite surface d'impact
est sensiblement perpendiculaire à l'axe polaire d'une buse.
13. Appareil selon la revendication 1 ou 10, caractérisé en ce que ladite toile (13,113,213,313,
413) de formation est mobile linéairement à une vitesse prédéterminée, et la vitesse
à laquelle ladite composition est déposée est supérieure à la vitesse du mouvement
de ladite toile de formation.