U.S. patent number 3,862,472 [Application Number 05/321,258] was granted by the patent office on 1975-01-28 for method for forming a low basis weight non-woven fibrous web.
This patent grant is currently assigned to Scott Paper Company. Invention is credited to Brian E. Boehmer, Henry J. Norton.
United States Patent |
3,862,472 |
Norton , et al. |
January 28, 1975 |
**Please see images for:
( Certificate of Correction ) ** |
METHOD FOR FORMING A LOW BASIS WEIGHT NON-WOVEN FIBROUS WEB
Abstract
A method for forming a low basis weight nonwoven web of randomly
arranged, intermingled fibers including a major proportion by
weight of short cellulosic fibers of a papermaking length less than
one-quarter inch, and a minor proportion by weight of longer
reinforcing fibers having an average length greater than
one-quarter inch. The method includes the steps of: (1) forming
separate batts of the short cellulosic fibers and the longer
reinforcing fibers; (2) blending together the fibers in the batts
in a randomly arranged and intermingled fashion; (3) conveying the
blended fibers in a gaseous carrier medium to a foraminous support
member; (4) passing the gaseous medium through the support member
to condense the fibers on the support member into a fibrous feed
mat having an average basis weight which is the greater of 12
oz/yd.sup.2 and at least three times the average basis weight of
the low basis weight fibrous web to be formed; (5) separating the
fibers from the feed mat; (6) conveying the separated fibers in a
gaseous carrier medium to a second foraminous support member; and
(7) passing the gaseous medium through the second support member to
condense the blended fibers on the second support member into the
low basis weight nonwoven fibrous web.
Inventors: |
Norton; Henry J. (Wilmington,
DE), Boehmer; Brian E. (Huron, OH) |
Assignee: |
Scott Paper Company (Delaware
County, PA)
|
Family
ID: |
23249857 |
Appl.
No.: |
05/321,258 |
Filed: |
January 5, 1973 |
Current U.S.
Class: |
19/145.5;
19/305 |
Current CPC
Class: |
D21H
15/00 (20130101); D21H 15/06 (20130101); D04H
1/43835 (20200501); D04H 1/4258 (20130101); D04H
1/425 (20130101); D21H 5/2635 (20130101) |
Current International
Class: |
D04H
1/42 (20060101); D01g 013/00 () |
Field of
Search: |
;19/145.5,147.5,155,156-156.4 ;156/62.2 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
110,428 |
|
Apr 1964 |
|
CS |
|
209,246 |
|
Mar 1968 |
|
SU |
|
Primary Examiner: Newton; Dorsey
Attorney, Agent or Firm: Faigus; Martin L. Foley; William
J.
Claims
Having described our invention, I claim:
1. A method for forming a low basis weight nonwoven fibrous web
including a major proportion by weight of short cellulosic fibers
of a papermaking length less than one-quarter inch and a minor
proportion by weight of longer reinforcing fibers having an average
fiber length of over one-quarter inch, said method comprising the
steps of:
A. forming a loosely compacted batt of substantially individualized
short cellulosic fibers of a papermaking length less than
one-quarter inch;
B. forming a loosely compacted batt of reinforcing fibers having an
average fiber length of over one-quarter inch;
C. separating and blending the fibers in the batts of short
cellulosic fibers and longer reinforcing fibers to form a gaseous
suspension of randomly arranged and intermingled fibers in which a
major proportion of the fibers by weight are the short cellulosic
fibers, and a minor proportion of the fibers by weight are the
longer reinforcing fibers;
D. conveying the gaseous suspension of randomly arranged and
intermingled short and longer fibers toward a foraminous support
member through which the gaseous carrier medium passes, and upon
which the fibers are deposited in a fibrous feed mat of randomly
arranged and intermingled short and longer fibers, said feed mat
comprising a major proportion by weight of the short cellulosic
fibers and a minor proportion by weight of the longer reinforcing
fibers, said feed mat having an average basis weight which is the
greater of 12 oz./yd..sup.2 and at least three times the average
basis weight of the low basic weight nonwoven fibrous web to be
formed; and
E. separating fibers from the feed mat and conveying them in a
gaseous carrier medium to a second foraminous support member
whereat the gaseous medium-passes through the foraminous support
member and the fibers are deposited on said support member to form
the low basis weight nonwoven fibrous web.
2. The method according to claim 1, wherein said short cellulosic
fibers are wood pulp.
3. The method according to claim 2, wherein the reinforcing fibers
are rayon fibers.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to a method for forming a nonwoven fibrous
web, and more specifically to a method for forming a low basis
weight nonwoven fibrous web of randomly arranged, intermingled
fibers including a major proportion by weight of short cellulosic
fibers of a papermaking length less than one-quarter inch, and a
minor proportion by weight of longer reinforcing fibers having an
average length greater than one-quarter inch.
"Low-basis weight," as used in this application to describe the
fibrous web, relates to an average basis weight in the range of
from about 1 oz/yd.sup.2 to about 6 oz/yd.sup.2.
2. Description of the Prior Art
Low basis weight nonwoven fibrous webs formed predominately of
short-length cellulosic fibers less than one-quarter inch, and
including a minor proportion by weight of longer reinforcing fibers
having an average length greater than one quarter inch are becoming
extremely popular. Such webs can be used by themselves, or in
conjunction with other materials, as substitutes for conventional
textile fabrics in articles such as disposable diapers, sanitary
napkins, industrial wipers, household wipers, cosmetic pads and the
like.
In one prior art approach to forming low basis weight nonwoven
fibrous webs, separate batts of the short fibers and longer fibers
are directed into a working station consisting of one or more
pinned working rolls for separating the fibers and intimately
blending them together. The blended fibers are then directed into
the storage compartment of a Rando-Feeder, which is manufactured by
the Curlator Company of Rochester, N.Y. The blended fibers are fed
from the storage compartment of the Rando-feeder by elevator and
stripper aprons therein to a bridge section including a condensor
roll with vacuum applied therethrough. A feed mat of the blended
fibers is formed in the bridge section and is then directed into a
Rando-Webber, which is also manufactured by the Curlator Company.
The Rando-Webber employs a rotating lickerin roll to doff fibers
from the feed mat, and these fibers are conveyed in a gaseous
carrier medium through a duct to a foraminous support member. The
gaseous medium passes through the support member, and the fibers
are condensed thereon in the form of a low basis weight nonwoven
fibrous web.
Employing a blending device in combination with a Rando-Feeder and
Rando-Webber requires two separate fiber metering operations; one
for achieving the desired blend ratio of long and short fibers to
be directed into the Rando-Feeder, and one for achieving the
desired feed mat weight in the bridge section of the Rando-Feeder.
Metering for proper feed mat weight requires the regulation of
elevator and stripper apron speeds, regulation of the level of
vacuum applied through the condenser in the bridge section and
regulation of condenser speed in said bridge section. Such an
arrangement is not as desirable as one in which the fibers are
blended and formed into a feed mat in one continuous operation,
i.e., without storing the fibers in a storage compartment between
the blending and feed mat forming operations.
Circulatory motion is imparted to the fibers by the action of the
elevator and stripper aprons in the Rando-Feeder. This circulatory
motion causes the formation of highly intangled clumps of fibers.
In many instances, these clumps are not broken up during the
formation of the fibrous web, and therefore, are included in the
finished fibrous web. The inclusion of these clumps in the fibrous
web results in unacceptable basis weight variations in both the
cross-machine-direction and machine-direction. In addition, the
presence of fibrous clumps in the finished web creates an
aesthetically unpleasing appearance.
The circulatory motion imparted to the fibers by the elevator and
stripper aprons shakes the short fibers from the blend and deposits
them in the trash chute of the Rando-Feeder. This causes a
considerable wastage of short fibers.
Applicant has further discovered that the elevator and stripper
aprons, aside from causing the formation of fibrous clumps, is an
unacceptable feed means for directing a substantially uniform
supply of fibers into the bridge section of the Rando-Feeder.
Consequently, the feed mat formed in the bridge section has
unacceptable variations in basis weight in both the
cross-machine-direction and machine-direction. The unacceptable
variations in basis weight in the feed mat results in the formation
of a fibrous web which also has unacceptable variations in basis
weight. Starting this another way, the uniformity in basis weight
of the finished fibrous web is dependent, to a large extent, upon
the uniformity in basis weight of the feed mat, and therefore,
nonuniformity in the feed mat results in nonuniformity in the
finished web.
A second prior art approach for forming low basis weight nonwoven
fibrous webs eliminates the step of forming a feed mat. According
to this approach, individual batts of the short cellulosic fibers
and the longer reinforcing fibers are fed together in the form of a
laminate directly into a web-forming device, such as a
Rando-Webber. The web forming device functions to separate the
fibers from the laminate and blend them together. The blended
fibers are conveyed in a gaseous carrier medium to a foraminous
support member through which the gaseous carrier medium passes, and
upon which the fibers are condensed into a low basis weight
nonwoven fibrous web.
Applicant has found that it is extremely difficult to achieve
acceptable basis weight variations in a low basis weight nonwoven
fibrous web by omitting the intermediate step of forming a feed mat
of blended fibers having a basis which is the greater of 12
oz/yd.sup.2 and at least three times the average basis weight of
the fibrous web to be formed. To further explain, it is known in
the air-laying art that basis weight variations can be more closely
controlled at higher basis weight levels than at lower basis weight
levels. Applicant has found that when uniform air flow conditions
exist in the Rando-Webber, the percentage basis weight variation in
the finished fibrous web is approximately the same as the
percentage basis weight variation in the feed mat. Therefore, first
forming a feed mat having a greater basis weight than the low basis
weight nonwoven web to be formed permits better control in the
formation of the low basis weight web than a process which omits
the formation of the feed mat.
In addition, applicant has found that feeding a laminate of long
and short fiber batts over the nose bar of the Rando-Webber is
difficult and unreliable. The laminate tends to jam and buckle as
it is being directed by feed rolls over the nose bar to thereby
cause machine downtime, and therefore increased production costs.
The reason for this jamming and buckling is not understood.
A further disadvantage of forming a low basis weight nonwoven
fibrous web directly from a laminate of short and long fiber batts
is that an unacceptable number of unopened fiber clumps are formed
in the web.
SUMMARY OF THE INVENTION
Applicant's invention resides in a process for forming low basis
weight nonwoven fibrous webs in which separate fibrous batts of
short cellulosic fibers of a papermaking length less than
one-quarter inch and longer reinforcing fibers having an average
length over one-quarter inch are directed into a fiberizing and
blending device for forming a gaseous suspension of blended short
and longer fibers; directing the gaseous suspension of blended
fibers directly to a foraminous support member through which the
gaseous carrier medium passes and upon which the fibers are
condensed to form a blended fibrous feed mat, said feed mat having
an average basis weight which is the greater of 12 oz/yd.sup.2 and
at least three times the average basis weight of the low basis
weight fibrous web to be formed; feeding the fibrous feed mat
directly into a web forming device in which the fibers of the feed
mat are separated and blended; and conveying the blended fibers in
a gaseous carrier medium to a second foraminous support member
through which the gaseous carrier medium passes, and upon which the
fibers are condensed to from the low basis weight nonwoven fibrous
web.
In applicant's invention, the blended short and longer fibers are
not directed into a storage compartment, such as the storage
compartment of a Rando-Feeder. Therefore, fibers are not permitted
to circulate in a storage area and form fiber clumps. In addition,
the separation of large quantities of short fibers from the blend
is eliminated.
In applicant'process, a feed mat of blended fibers having the
desired weight is formed directly from a gaseous suspension of the
blended fibers immediately after the short and longer fibers have
been opened and blended. This continuous method of feed mat
formation has been found to be highly superior to directing blended
fibers into a storage compartment of a Rando-feeder, and then
metering the fibers from the storage compartment into the bridge
section to achieve a desired feed mat weight.
In applicant's process, a feed mat is formed with an average basis
weight which is the greater of 12 oz/yd.sup.2 and at least three
times the average basis weight of the fibrous web to be formed.
Below this feed mat basis weight level a greater concentration of
fiber clumps appears in the finished web. This creation of fiber
clumps is believed to be caused by the action of the rotating
lickerin roll in pulling clumps of fibers from the feed mat when an
inadequate supply of fibers is directed to the lickerin roll.
Also, as explained earlier, when uniform air flow conditions exist
in the Rando-Webber, the percentage basis weight variation in the
low basis weight nonwoven fibrous web is approximately the same as
the percentage basis weight variation in the feed mat from which it
is formed. The percentage basis weight variation can be more easily
minimized in a higher basis weight feed mat formed directly after
blending the long and short fibers, than in a low basis weight
nonwoven web formed directly after blending. Therefore, the instant
invention of first forming a feed mat results in the formation of a
low basis weight nonwoven fibrous web of greater uniformity than
the prior art process of omitting the formation of a feed mat.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a block diagram of the sequential process steps performed
in forming a low basis weight nonwoven fibrous web according to a
preferred method of this invention;
FIG. 2 is a schematic view showing apparatus for sequentially
blending fibrous batts of the short and longer fibers, forming a
blended feed mat, and forming a blended low basis weight nonwoven
fibrous web from the feed mat;
FIG. 2a is an enlarged view of the blocked portion of FIG. 2
identified as 2a showing the fibrous batts of short and longer
fibers as they are directed into the blending station according to
one preferred method of this invention; and
FIG. 2b is an enlarged view of the blocked portion of FIG. 2
identified as ab showing the blended fibrous feed mat which is
formed.
DESCRIPTION OF THE PREFERRED EMBODIMENTS OF THE INVENTION
For the purpose of description, the method of this invention will
be described in connection with the formation of a low basis weight
fibrous web comprising predominately wood pulp fibers (short
cellulosic fibers of a papermaking length less than one-quarter
inch) and a minor proportion of longer rayon fibers (longer
reinforcing fibers having an average length over one-quarter inch).
Wood pulp is preferred as the short cellulosic fiber of papermaking
length less than one-quarter inch because it is readily available,
highly absorbent and relatively inexpensive. However, other short
cellulosic fibers of a papermaking length, such as cotton linters,
can be employed in the method of this invention.
Rayon is preferred as the longer reinforcing fiber because of low
cost. The rayon fibers have an average length over one-quarter
inch, and preferably over one-half inch. The upper length
limitation is not critical, being dictated by the specific
properties desired in the fibrous web. In the preferred embodiment
of this invention the rayon employed is 1-1/2 inch - 3 denier.
Other long fibers (average length over one-quarter inch) can be
used in this invention. The particular long fiber which is used is
not critical to this invention.
Referring to FIG. 1, the process steps through "Rayon Batt-Pulp
Batt Blending" have been practiced in the prior art. The present
invention resides in the manner of handeling the rayon batt-pulp
batt blend through formation into a finished, low basis weight
nonwoven fibrous web. However, the purpose of completeness, the
process steps employed for forming the rayon batt-pulp batt blend
will now be described.
Referring to FIG. 1, commercially available baled rayon is fed
through a rayon opening step. Any suitable rayon opening equipment
can be utilized; however, in the preferred embodiment of this
invention the baled rayon is fed through a Rando-Prefeeder, which
opens the rayon slightly, and then through a Rando-Opener-Blender,
which completes the opening operation. Both the Rando-Prefeeder and
Rando-Opener-Blender are manufactured by the Curlator Company of
Rochester, N.Y. The opened rayon is then fed through a chute feed
onto a conveyor for forming a fibrous batt of the rayon fibers. One
chute feed which has been found to be satisfactory is the
CMC-Evenfeed manufactured by CMC Corporation, of Charlotte, N.C.
The rayon batt is a loosely compacted sheet of randomly arranged
opened rayon fibers.
Pulp lap, whether in sheet or roll or form, is fiberized, i.e.,
separated into substantially individual fibers, in a fiberizing
device, such as a Joa fiberizer manufactured by Joa, Inc. of North
Wales, Fla. The specific fiberizer utilized does not form a
limitation on the present invention, and can include other
apparatus such as hammermills, disk refiners, and other fiberizers
employing lickerin rolls. The fiberized wood pulp is conveyed in a
gaseous medium (e.g., air) toward a foraminous conveyor through
which the gaseous medium passes, and upon which a wood pulp batt of
loosely compacted fibers is formed.
Referring to FIGS. 2 and 2a, the fibrous batt of rayon 10 is
superposed upon the fibrous batt of wood pulp 12. The fibrous batts
are directed into a blending device 14 which includes a central
drum 16 having pins or teeth 18 projecting outwardly from the
periphery thereof. In addition, the blending device 14 includes a
plurality of satellite worker rolls 20 disposed about the periphery
of the central drum 16, and these satellite rolls are provided with
pins, teeth, or the like 22 which cooperate with the pins 18 on the
central drum to separate fibers from the superposed batts of rayon
and wood pulp, and intimately blend the separated fibers
together.
The description provided thus far represents known technology in
establishing substantially homogeneous blends of long and short
fibers. The above sequentially described steps are preferred in
applicant's invention, but can me modified. For example, the rayon
opening step may be accomplished by the use of a single device, as
opposed to utilizing the Rando-Prefeeder and Rando-opener-Blender.
Moreover, when long fibers other than rayon are utilized, the
opening step may be omitted completely. In addition, the individual
batts of long and short fibers need not be superposed upon each
other prior to being directed into the blending device 14. It is
possible to feed the batts separately into the blending device 14
from separate stations to accomplish the objective of forming a
homogeneous blend of individualized long and short fibers.
Moreover, equipment other than the above-described equipment can be
utilized to achieve the objectives described thus far. For example,
the blending device 14 shown in FIG. 2 can be replaced by other
types of devices. For example, the device described in U.S. Pat.
No. 3,641,628, issued to Fehrer on Feb. 15, 1972, can be employed
to blend fibers, or the fibers can be blended in a device employing
a rotary lickerin roll, such as a Rando-Webber.
In applicant's invention a foraminous support member in the form of
a cylindrical condenser roll 24, is positioned at the downstream
exit end of the blending device 14. A streama of air is injected
into the blending device adjacent the downstream end thereof
through an inlet conduit 26 to aid in doffing the blended fibers
from the pinned central drum 16, and to establish a gaseous
suspension of the blended fibers. A vacuum is applied through a
vacuum conduit 28 disposed within the condensor roll 24 to aid in
directing the gaseous suspension of blended fibers toward the
condensor roll 24. The gaseous carrier medium passes through the
condensor roll 24 and a blended fibrous feed mat 30 (FIGS. 2 and
2b) is formed on the surface.
The blended feed mat 30 has an average basis weight which is the
greater of 12 oz/yd.sup.2 and at least three times the average
basis weight of the low basis weight fibrous web 48 to be formed.
The feed mat 30 is comprised of over 50 percent by weight of wood
pulp fibers. Preferably the wood pulp is present in about 75
percent to about 90 percent by weight; the remainder of the fiber
blend being the longer rayon fibers.
"Average Basis Weight" of the fibrous web is determined by removing
circular, 2 inch diameter web samples along the entire
cross-machine-direction of the fibrous web in three separate areas
which are spaced from each other along the machine direction. The
cross-machine-direction spacing between samples is approximately
3-1/2 inches from center to center. In this manner, approximately
12 or 13 2-inch diameter samples are taken in the
cross-machine-direction of a blended web 40 inches wide. The basis
weight of each of the samples is determined, and the arithmetic
mean of all samples taken is the "Average Basis Weight."
Referring to FIG. 2, the blended feed mat 30 is directed over a
supporting surface 32 into a web forming device shown schematically
at 34. The web forming device 34 includes a lickerin roll 36 which
is rotated to doff individual fibers from the feed mat 30. The
individual fibers are suspended in an air stream which is generated
by the rotating lickerin roll 36 and fan 38. The air suspended
stream of fibers 39 is directed through a duct 40 toward a
foraminous support member 42. Movement of the air suspended stream
of fibers 39 toward the foraminous support member 42 is enhanced by
applying a partial vacuum through vacuum box 44 which is positioned
below a web forming run 46 of the foraminous support member 42.
This partial vacuum is created by fan 38. The air of the stream of
fibers 39 passes through the foraminous support member and is
circulated through the fan to the positive pressure side thereof,
and past the lickerin roll in a continuous, closed circuit
arrangement. The fibers in the stream are deposited on the web
forming run 46 of the foraminous support member 42 in the form of a
low basis weight, nonwoven fibrous web 48. One or more of the rolls
supporting the foraminous support member 42 are driven to convey
the foraminous support member in the direction indicated by arrows
50.
The low basis weight nonwoven fibrous web 48 can be directed to
post-treatment stations (not shown) such as adhesive application
stations, embossing stations and the like. According to one
preferred embodiment of this invention, the fibrous web iss first
embossed, and then sprayed with adhesive, as disclosed in pending
U.S. Pat. application Ser. No. 23,751, and U.S. Pat. No. 3,721,242,
which issued on Mar. 20, 1973 from U.S. Pat. application Ser. No.
23,752. Both the above mentioned application and patent are
assigned to Scott Paper Company.
It is extremely important in this invention that the average basis
weight of the feed mat be the greater of 12 oz/yd.sup.2 and at
least three times the average basis weight of the low basis weight
nonwoven fibrous web. Below this feed mat basis weight level a
greater concentration of fiber clumps appears in the finished web..
This creation of fiber clumps is believed to be caused by the
action of the rotating lickerin roll in pulling clumps of fibers
from the feed mat when an inadequate supply of fibers is directed
to the lickerin roll.
It is known that the speed of the lickerin roll in the Rando-Webber
has a direct affect on long fiber length in the finished web. The
lickerin roll of the Rando-Webber tends to cut the longer fibers,
and the degree of cutting is directly related to the lickerin
speed, i.e., the greater the lickerin speed the greater the cutting
action on the longer fibers. Excessive cutting of the longer fibers
tends to adversely affect the properties, such as tear strength, of
the finished web. Tear strength is an important property in
products such as diaper covers. Therefore, it is desirable to
minimize the lickerin speed of the Rando-Webber in order to reduce
the damage of the longer reinforcing fibers.
At a predetermined speed of web formation, the speed of the
lickerin roll of the Rando-Webber required to comb out clumps
present in the feed mat is directly dependent upon the number of
such clumps present in the feed mat and the degree of entanglement
of fibers in the clumps. The greater the number of clumps and
degree of fiber entanglement in the clumps, the higher the required
lickerin speed. It is also known that at increased web formation
speeds the lickerin speed must be increased to form a web of
comparable basis weight and quality as is formed at lower formation
speeds. Therefore, the quality (specific number of fiber clumps) of
the feed mat has a direct affect on both production speed and
physical properties of the final web. For example, it was possible
to produce fibrous webs having a basis weight of 2 oz/yd.sup.2 with
an acceptable concentration of fiber clumps when using a
Rando-Feeder feed mat at production speeds of up to about 100 feet
per minute. However, when utilizing feed mats manufactured
according to the process of this invention, fibrous webs having a
basis weight of approximately 2 oz/yd.sup.2 with an acceptable
concentration of fiber clumps have been made at speeds exceeding
200 feet per minute. According to applicant's invention, low basis
weight nonwoven fibrous webs having a percent basis weight
variation no greater than 10 percent have been consistently
achieved at web forming speeds in excess of 100 feet per minute,
and approaching 200 feet per minute.
"Percent Basis Weight Variation" is calculated by taking 2 inch
diameter samples across the entire cross-machine-direction of the
finished web in three separate machine-direction locations, as
described above in connection with the calculation of the average
basis weight. The average basis weight is subtracted from the basis
weight of the sample having the greatest difference from the
average basis weight, and this difference is then divided by the
average basis weight.
* * * * *