U.S. patent number 3,793,678 [Application Number 05/209,935] was granted by the patent office on 1974-02-26 for pulp picking apparatus with improved fiber forming duct.
Invention is credited to David W. Appel.
United States Patent |
3,793,678 |
Appel |
February 26, 1974 |
PULP PICKING APPARATUS WITH IMPROVED FIBER FORMING DUCT
Abstract
An apparatus and method for airlaying wood pulp fibers which
avoids fiber floccing is disclosed. Wood pulp sheets are
divellicated with a picker roll and the individual fibers are
conveyed through a forming duct to a collecting screen. The
position of the forming duct with respect to the picker roll and
the size of the duct are such that the fibers separated from the
sheets maintain substantially the same velocity during their travel
through the forming duct. A process air duct for supplying air to
transport the fibers to the collecting surface is used; and, when
high picking rates are desired, a supplemental air duct is also
employed.
Inventors: |
Appel; David W. (Neenah,
WI) |
Family
ID: |
22780936 |
Appl.
No.: |
05/209,935 |
Filed: |
December 20, 1971 |
Related U.S. Patent Documents
|
|
|
|
|
|
|
Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
|
882265 |
Dec 4, 1969 |
|
|
|
|
Current U.S.
Class: |
425/82.1;
19/306 |
Current CPC
Class: |
D01G
25/00 (20130101); D01G 1/02 (20130101) |
Current International
Class: |
D01G
25/00 (20060101); D01G 1/00 (20060101); D01G
1/02 (20060101); D01g 025/00 () |
Field of
Search: |
;57/50,58.95
;19/156.3,156.4,89,88 ;241/18,47,57,49 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Newton; Dorsey
Attorney, Agent or Firm: C. Frederick Leydig et al.
Parent Case Text
RELATED APPLICATIONS
Appel, U.S. Pat. Ser. No. 882,265, filed Dec. 4, 1969 , now
abandoned entitled "Pulp Picking Apparatus With Improved Fiber
Forming Duct," of which the present application is a
continuation-in-part.
Appel and Sanford, U.S. Pat. Ser. No. 882,258, filed Dec. 4, 1969,
now U.S. Pat. No. 3,606,175, entitled "Picker for Divellicating
Pulp."
Claims
I claim as my invention:
1. In an apparatus for forming an airlaid web which comprises a
rotatable divellicating means having teeth thereon for separating a
compacted fiber sheet into its individual fibers, a housing
enclosing the divellicating means and providing a passage between
the housing and the divellicating means, a foraminous moving
surface for collecting the fibers to form a web thereon, a forming
duct positioned between the divellicating means and the moving
surface through which the separated fibers leaving the
divellicating means are transported to the moving surface and
communicating with the passage, a suction means disposed below the
foraminous surface to assist in collecting the fibers on the
surface and wherein the rotation of the divellicating means creates
a pumping action in the passage to provide moving process air for
transporting the separated fibers through the forming duct to the
collecting surface and the pumping action tends to cause part of
the process air to enter the passage, the improvement comprising
said forming duct having a limited area path through which the
separated fibers and process air are transported to the collecting
surface, the width of said forming duct being approximately equal
to the height of the teeth of said divellicating means, a process
air duct communicating with the passage and means for supplying air
to said process air duct at a pressure and a rate sufficient to
substantially prevent process air in said forming duct from
entering the passage.
2. The apparatus of claim 1 wherein said forming duct and process
air duct have a common wall and said process air duct is positioned
to cause the process air to communicate with the passage adjacent
the point at which said forming duct communicates with the
passage.
3. The apparatus of claim 1 and wherein the longitudinal axis of
said forming duct is inclined with respect to the perpendicular to
the foraminous surface.
4. In an apparatus for forming an airlaid web which comprises a
rotatable divellicating means having teeth thereon for separating a
compacted fiber sheet into its individual fibers, a housing
enclosing the divellicating means and providing a passage between
the housing and the divellicating means, a foraminous moving
surface for collecting the fibers to form a web thereon, a forming
duct positioned between the divellicating means and the moving
surface through which the separated fibers leaving the
divellicating means are transported to the moving surface and
communicating with the passage, a suction means disposed below the
foraminous surface to assist in collecting the fibers on the
surface and wherein the rotation of the divellicating means creates
a pumping action in the passage to provide moving process air for
transporting the separated fibers through the forming duct to the
collecting surface and the pumping action tends to cause part of
the process air to enter the passage, the improvement comprising
said forming duct having a limited area path through which the
separated fibers and process air are transported to the collecting
surface, a process air duct communicating with the passage, means
for supply air to said process air duct at a pressure and at a rate
sufficient to substantially prevent process air in said forming
duct from entering the passage, a supplemental air duct
communicating with said forming duct and positioned to allow air to
enter said forming duct at a point adjacent the entry of the
separated fibers into said forming duct and in the same direction
as the process air, said forming duct width being up to about four
times the height of the divellicating means teeth and means for
supplying air to said supplemental air duct to provide entry of the
supplemental air into said forming duct at substantially the same
velocity as the process air.
Description
DESCRIPTION OF THE INVENTION
The present invention is directed to the preparation of wood pulp
fiber webs and, more particularly, to an apparatus and process for
preparing a loose batt or web of wood pulp fibers characterized by
its uniformity and substantial freedom from fiber floccing.
Techniques for divellicating wood pulp and reassembling the same in
the form of soft webs of relatively individualized fibers are well
known. Customarily, compacted wood pulp sheets are fed to a hammer
mill or picker roll which divellicates the sheets into individual
fibers. The fibers are thereafter deposited on a supporting surface
such as a foraminous screen. The screen generally has suction means
associated with it so as to facilitate fiber formation thereon and
is usually moving continuously in a direction generally transverse
to the direction of fiber delivery.
While the known methods seek to form webs wherein the fibers are in
a highly uniform arrangement, as a practical matter, significant
fiber clumping or agglomeration, generally referred to as fiber
floccing, occurs. Such fiber floccing is at least partly a result
of fiber entanglement as the fibers are conveyed from the picker
roll to the supporting surface. Also, webs formed by conventional
methods usually have a non-uniform distribution of basis weight
across the width of the webs.
While the fiber webs prepared by conventional processes can be used
in a number of applications, there are some uses wherein a web
substantially free of fiber floccing and highly uniform across its
width would be desirable. In particular, as described in the U.S.
Pat. application of C. E. Dunning, titled "Air Formed Webs and
Method For Making Such Webs," Ser. No., 882,257, filed Dec. 4,
1969, useful paper products with a desirable combination of
strength, tactile, and absorbency characteristics can be prepared
from soft webs of wood pulp fibers. While conventionally prepared
fiber webs can be used in the aforementioned paper making process,
the use of highly uniform webs substantially free from fiber
floccing would be advantageous.
Accordingly, it is an object of the present invention to provide a
uniform web of individual fibers which is substantially free of
fiber floccing. It is a further object to provide a method and
apparatus for preparing such fiber webs. It is a still further
object of the present invention to provide a method and apparatus
whereby individual fibers from divellicated pulp sheets can be
conveyed directly after their separation from the sheets to a fiber
supporting surface at sustantially the same velocity at which they
are separated.
Other objects and advantages will become apparent upon reading the
following detailed description and upon reference to the drawings,
in which:
FIG. 1 is a schematic side elevation view and illustrates one
embodiment of the apparatus of the present invention showing a
radial pulp feed and a forming duct positioned normal to the
collecting surface;
FIG. 2 is a schematic side elevation view and shows another
embodiment of the apparatus of the present invention having a
radial pulp feed and forming duct inclined with respect to the
collecting surface;
FIG. 3 is a schematic side elevation view and illustrates a further
embodiment of the apparatus of the present invention including a
spiral pulp feed and a normal forming duct and
FIG. 4 is a schematic side elevation view and shows still another
embodiment of the apparatus of the present invention showing a
spiral pulp feed and an inclined forming duct.
While the invention is susceptible to various modifications and
alternative forms, specific embodiments thereof have been shown by
way of example in the drawings and will herein be described in
detail. It should be understood, however, that it is not intended
to limit the invention to the particular forms disclosed, but, on
the contrary, the intention is to cover all modifications,
equivalents and alternatives falling within the spirt and scope of
the invention as expressed in the appended claims.
Turning to the drawings, FIG. 1 illustrates an apparatus useful for
divellicating pulp sheet according to the present invention. As
shown, the apparatus comprises a conventional picker roll 10 having
picking teeth 12. Pulp sheets 14 are radially fed, i.e., along a
picker roll radius, to the picker roll 10 by means of the rolls 16.
The picker teeth 12 divellicate the pulp sheets 14 into individual
fibers 22. After separation from the sheets, the fibers are
conveyed to the moving foraminous screen 20 through the forming
duct 18. A housing 23 encloses the picker roll 10 and provides a
passage 25 between the housing and the picker roll surface. Process
air 24 is supplied to the picker roll in the passage 25 via duct 26
in sufficient quantity to serve as a medium for conveying the
fibers 22 through the forming duct 18 at a velocity approaching
that of the picker teeth. The air may be supplied by any
conventional means as, for example, a blower 27. Suction means 28
positioned below the screen 20 at the duct exit of a sufficient
capacity to accept the air flow from the duct aid in the formation
of the fibers into a web 30 on the moving foraminous collecting
screen 20.
It has been found that, in order, to avoid fiber floccing, the
individual fibers should be conveyed through the forming duct 18 at
substantially the same velocity at which they leave the picker
teeth 12 after separation from the pulp sheets 14, i.e., the fibers
should maintain their velocity in both magnitude and direction from
the point where they leave the picker teeth. Moreover, as used
herein, "substantially the same" means that the velocity at which
the fibers separate from the pulp sheets does not change by more
than about 50 percent and, preferably, by not more than about 20
percent, in the forming duct. This is in contrast with conventional
forming apparatus in which, due to flow separation, fibers do not
travel in an ordered manner from the picker to the supporting
surface; and, consequently, fibers velocities change as much as 100
percent or more during conveyance to a supporting surface.
In accordance with one aspect of the present invention, fiber
velocity is maintained sustantially the same by suitable
positioning and sizing of the duct. To this end, the forming duct
is positioned such that its longitudinal axis is substantially
parallel to the plane which is tangent to the picker teeth at the
point at which the fibers leave the influence of the picker teeth.
In such a position, fiber velocity is not changed by impingement on
the duct walls. Thus, where the pulp sheets 14 (FIG. 1) are
radially fed to the picker in a plane which is substantially
parallel to the screen 20, the plane which is tangent to the picker
teeth 12 at the point of contact with the pulp sheets is
perpendicular to the screen 20. Accordingly, since for the
schematic embodiment illustrated in FIG. 1, the point of picker
contact with the sheets is also the point at which the separated
fibers leave the influence of the picker teeth, the longitudinal
axis of the forming duct is normal to the screen 20. However, if
after separation from the pulp sheets, the fibers are constrained
to remain under the influence of the picker teeth, e.g., as in FIG.
1, of U.S. Pat. No. 3,268,954 to Joa and further embodiments
described herein, then the axis of the forming duct is
appropriately adjusted so as to be in the direction of fiber
velocity at that point where constraint is no longer present
Aside from the above discussed parallel relationship of the
longitudinal axis of the duct, the duct size is also important. As
shown in FIG. 1, the width of the duct is approximately equal to
the height of the picker teeth 12, the passage between the picker
teeth and the picker roll housing being very small. With such a
duct width, the velocity of the process air supplied through
process air duct 26 remains substantially constant in its travel
with the picker and thence through the duct 18. Furthermore, since
as indicated earlier, the velocity of the process air approaches
that of the picker teeth which, in turn, is about that of the
separated fibers, the process air causes no substantial variations
in fiber velocity as it conveys the fibers in the duct to the
screen. With duct widths approximately equal to the height of the
picker teeth, e.g., no more than about 1.5 times the tooth height,
air velocities in the forming duct of at least 70 percent of the
picker tooth velocity are useful in the illustrated apparatus.
Duct length and transverse width, i.e., the width in a direction
along the picker roll axis, are also important in order to achieve
an optimum web. Preferably, the duct length should be as short as
the overall equipment design will allow. For the apparatus
schematically illustrated in FIG. 1, the shortest duct length is
limited by the radius of the picker roll. In order to achieve a
high degree of cross-width uniformity in the resultant web, the
transverse duct width preferably should not exceed the width of the
pulp sheets fed to the picker roll.
Again referring to the apparatus illustrated in FIG. 1, it is
preferred that picker teeth with relatively large heights, e.g.,
greater than one fourth inch, be used. Such heights permit the use
of wider forming ducts which, in turn, minimize the interaction of
fibers with the duct walls. Further embodiments, discussed
hereinafter, illustrate other means for minimizing this
interaction.
Additional aspects of the present invention are illustrated in FIG.
2. As in FIG. 1, pulp sheets 14 are radially fed to the picker roll
10 having teeth 12 by means of the rolls 16. However, as shown in
FIG. 2, the plane of the pulp sheets fed to the picker is not
parallel to the moving screen 20, and, consequently, the plane
tangent to the picker teeth at their point of contact with pulp
sheets is inclined with respect to the perpendicular to the moving
screen. Thus, in accordance with the above discussion, the position
of the forming duct is such that its longitudinal axis is also
inclined with respect to the perpendicular to the moving screen;
the angle of inclination being substantially the same as that of
the plane tangent to the teeth at the point of contact with the
pulp sheet.
The use of an inclined forming duct as illustrated in FIG. 2 is
particularly useful where high picking rates are employed and the
screen 20 is moving at a high speed. Fibers impinging upon the
screen from an inclined forming duct have a component of velocity
in the direction of screen movement and, accordingly, fiber
disruption is minimized.
An additional aspect of the present invention is also illustrated
in FIG. 2, and involves the introduction of the process air through
duct 24 at a point 32 which is close to the entrance to the forming
duct 18. In this embodiment the upstream wall 33 of the forming
duct is common to the process air duct. An arrangement such as
depicted is particularly suitable when the picker roll is to be
rotated at high speeds and/or large teeth heights are used. Under
such circumstances, the pumping effect of the rotating roll tends
to carry air and fibers from the forming duct into the picker
housing. This can result in fiber clumps developing in the housing
and the consequent conveyance of such clumps around the picker
teeth and through the duct. By introducing the process air near the
entrance to the forming duct, the pumping effect of the roll can be
counteracted and fiber circulation around the housing prevented.
Also, in such a position, the process air serves to strip clinging
fibers from the picker teeth. Simple experimentation can be used to
establish the appropriate process air flow rate to obtain an
optimum web under the desired operating conditions. Also, the
appropriate flow rate can be visually determined by providing a
window (not shown) in the housing so that the interior of the
forming duct can be observed. In this instance, the flow rate is
set so that fibers do not buildup on the nose 35 of the forming
duct wall 33.
It should be appreciated that positioning the entrance of the
process air duct 24 to the passage 25 a distance away from the
communication of the forming duct with the passage (as in FIG. 1)
may also be employed to prevent fibers and process air from being
drawn into the passage from the forming duct. Positioning of the
process air duct against the forming duct (as in FIG. 2) is,
however, preferred. This allows the usage of less air pressure
since the FIG. 1 embodiment must overcome the pumping action in the
portion of the passage from the forming duct entrance to the point
at which the process air is admitted
The positioning of the entrance of the process air duct adjacent
the forming duct, as in FIG. 2, has the further advantage in that
control of the process air in the cross-direction is enhanced.
Thus, while the FIG. 1 embodiment is capable of providing
uniformity of air pressure across the machine width, the air
supplied must overcome the pumping action caused by the rotating
picker, a pumping action which may be variable. Use of this
embodiment accordingly requires more pressure than is theoretically
necessary to provide a safety factor insuring that process air and
fibers all across the width are not allowed to enter the passage
25. This can result in localized areas having excessive air
pressure, causing undesirable air turbulence in the forming duct
which could disturb the desired uniformity of the fiber
transportation to the foraminous collecting surface.
Positioning the process air duct as close to the forming duct as
possible, as in the FIG. 2 embodiment, obviates these potential
problems. The air is supplied where it is needed and may be
provided at a rate and pressure sufficient to prevent process air
and fibers from entering the passage 25. There is no need to supply
excess air to oppose the pumping action generated by the picker
from the entrance of the passage 25 at the forming duct to the
entrance of the process air duct since this distance is minimal in
the FIG. 2 embodiment.
In accordance with a further aspect of the present invention, means
are provided to further insure that the air pressure entering the
passage 25 is substantially uniform in the widthwise direction. To
this end, and as shown in FIG. 2, the process air duct 24 is
considerably larger in size than the duct entrance to the passage
(shown at point 32). The process air duct 24 should be sufficiently
larger than the duct entrance so that there is less than about 1 or
2 percent variation in pressure across the width, preferably less
than 1 percent. This can be accomplished by having the duct width
10 times that of the entrance to the passage 25. Variations of
about 3 to 4 percent begin to disturb the desired uniformity of the
formed web.
According to a still further feature of the present invention,
means are provided to supply supplemental air to the forming duct.
The use of supplemental air is particularly desirable at high
picking rates. With high picking rates and the associated high
fiber concentrations in the forming duct, more floccing tends to
occur through such mechanisms as mechanical entanglement and fiber
attraction due to static charge. Using supplemental air allows a
wider duct so that the fiber concentration is diminished through
the mild mixing of the two air streams at their adjacent boundaries
and results in a desirably greater degree of fiber separation and
less fiber interaction. To this end, and as is shown in FIG. 2,
supplemental air is introduced into the forming duct 18 through a
supplemental air duct 34, communicating with the forming duct
adjacent the entry of the separated fibers and the process air into
the forming duct. The speed and direction of the supplemental air
must be substantially the same as the speed and direction of the
process air and fibers so as to avoid turbulence or severe mixing
which would result in fiber floccing. The interior wall 37 of the
supplemental air duct 34 is contoured to provide a smooth flow and
terminates at a point 39 where the supplemental air and process air
merge.
The use of supplemental air allows the forming duct to have a width
of up to about four times the height of the picking teeth. Thus,
for picker teeth heights of one-fourth inch, the duct width may be
about 1 inch. The source of air may be any conventionally used
source such as, for example, a blower 41, the sole requirement
being that the capacity is sufficient to achieve the requisite air
velocity.
FIGS. 3 and 4 illustrate further embodiments of the present
invention. As shown therein, the pulp sheets 14 are spirally fed to
the picker 10 rather than radially fed as shown in FIGS. 1 and 2.
The various aspects and advantages of spiral pulp feeds are set
forth in detail in the Appel and Sanford patent previously
identified. Briefly, spiral feeding permits high picking rates
without fiber breakage, scorching, or burning. Referring to FIGS. 3
and 4, such spiral picking is accomplished by use of a pulp sheet
feed guide 36, the geometry of which is described in the
aforementioned patent, which spirally guides the pulp sheets 14
into contact with the picker teeth 12. At the end 38 of the feed
guide 36, there is approximately zero clearance between the guide
and the picker teeth.
As illustrated in FIGS. 3 and 4, when using a spiral feed the
longitudinal axis of the forming duct 18 is parallel to the plane
tangent to the picker teeth at the point of approximately zero
clearance between the teeth and the guide. Although, picking of the
sheets starts at the entrance to the feed guide, separated fibers
do not leave the influence of the teeth until the point of
approximately zero clearance is reached. Also, as illustrated, an
inclined forming duct, a supplemental air supply, and an
appropriate positioning of the process air entrance can be
advantageously used with spiral pulp feed.
Thus, as described above, the illustrated apparatus can be used to
form uniform webs which are substantially free from fiber floccing.
The webs so formed can be of any weight desired, varying from an
essentially single fiber layer to thick batts. As an illustrative
example, the apparatus depicted in FIG. 1 wherein the picker roll
is 12 inches in diameter, 13 inches long, and has teeth with a
height of three/eights inch can be used to divellicate a
combination of 4 wood pulp sheets, each of which is 0.0009 inch
thick with a basis weight of 70 lbs. per 2,880 ft..sup.2. When
doing such, a speed of 8,000 FPM (teeth speed) and a forming duct
width of one half inch are useful.
* * * * *