[0001] An apparatus of the present invention relates to an apparatus for producing fiber
aggregate, and more particularly, it relates to an apparatus for continuously producing
fiber aggregate in which most fibers are one-dimensionally oriented. "One-dimensional
orientation" means that many fibers are oriented in about the same direction. This
definition applies not only to the fiber aggregate but also to the orientation step
to be mentioned later.
[0002] Heretofore, fiber aggregate of short fibers or whiskers has been produced by using
one of the conventional apparatuses mentioned below.
[0003] The first one is a centrifugal forming apparatus as shown in Fig.4 (disclosed in
Japanese Patent Laid-open No.65200/1985). In operation of this apparatus, an aqueous
suspension of silicon carbide whiskers or the like is fed through the supply pipe
24 to the porous cylindrical vessel 23 which is lined with the filter film 25 and
disposed in the outer cylinder 21. The hollow fiber aggregate 26 is formed by centrifugal
action. Water is discharged from the water outlet 22.
[0004] The second one is a suctional forming apparatus as shown in Fig. 5. In operation
of this apparatus, a prescribed amount of fiber-containing fluid 34 is fed to the
cylinder 31, and a pressure is applied to the fluid 34 by the pressing plunger 32
arranged above the cylinder 31. At the same time, the filtrate is removed by suction
through the filter 33 disposed at the bottom of the cylinder 31. Thus the fibers in
the fluid are oriented and aggregated.
[0005] The fiber aggregate formed by the above-said centrifugal forming apparatus or suctional
forming apparatus is not composed of one-dimensionally oriented fibers, but is composed
mainly of two- or three-dimensionally oriented fibers. The fiber aggregate with such
orientation has a disadvantage that it does not provide a sufficient strength in the
desired one-dimensional direction when incorporated into fiber-reinforced metal
(referred to as FRM hereinafter). Additional disadvantages are the low volume ratio
of fiber and the excessive spring back at the time of compression molding.
[0006] With the conventional apparatuses, it was impossible to produce one-dimensionally
oriented fiber aggregate and it was only possible to produce two- or three-dimensionally
oriented fiber aggregate. It was also impossible to produce fiber aggregate continuously.
[0007] It is an object of the present invention to provide an apparatus for producing fiber
aggregate in which most fibers are one-dimensionally oriented. The fiber aggregate
produced by using the apparatus of this invention has a high fiber volume ratio and
a low degree of spring back. When incorporated into FRM, it provides FRM having a
high strength in the desired one dimension. With the apparatus of the present invention,
it is possible to produce one-dimensionally oriented fiber aggregate continuously
by using the sheet drive unit which moves the long filter sheet horizontally.
[0008] The apparatus of the present invention for producing oriented fiber aggregate comprises
an orientation vessel, at least one pair of positive electrode and negative electrode,
and a sheet drive unit. The orientation vessel includes a supply part, an orientation
part and a discharge part. The supply part is placed at the upper part of the vessel
and it receives a dielectric fluid in which whiskers, short fibers or the like are
dispersed, and supplies the dielectric fluid downward. The discharge part discharges
the dielectric fluid downward. The dielectric fluid moves downward from the supply
part to the discharge part through the orientation part. The electrodes are installed
vertically at a certain distance apart horizontally in the orientation part of the
orientation vessel. The sheet drive unit moves a long filter sheet horizontally between
the orientation part and the discharge part in the orientation vessel. The filter
sheet permitting the dielectric fluid to pass therethrough and permitting the fibers
to aggregate thereon.
[0009] The invention will be described in further detail with reference to the accompanying
drawings, in which:
Fig. 1 is a schematic sectional view of the apparatus of the invention for producing
oriented fiber aggregate.
Fig. 2 is a schematic sectional view of the apparatus used in the example for producing
oriented fiber aggregate.
Fig. 3 is a schematic sectional view of another embodiment of the apparatus of the
invention for producing oriented fiber aggregate.
Fig. 4 is a partly cutaway sectional view of the conventional centrifugal forming
apparatus.
Fig. 5 is a schematic sectional view of the conventional suctional forming apparatus.
[0010] The apparatus for producing oriented fiber aggregate as shown in Fig. 1, the orientation
vessel includes a supply part 4 placed above which receives a dielectric fluid 3 in
which are dispersed short fibers 2 or the like and supplies the dielectric fluid downward,
a discharge part 6 which discharges the dielectric fluid downward, and an orientation
part 5 through which the dielectric fluid moves downward from the supply part 4 to
the discharge part 6.
[0011] The supply part 4 should have such a structure as to receive the dielectric fluid
in which fibers are dispersed. An alternative structure may be possible in which there
is disposed above the supply part 4 a dispersion unit to disperse fibers into the
dielectric fluid or a supply unit (not shown) to supply the dielectric fluid.
[0012] In addition, the supply part may have a resistance flow regulator to reduce the flow
rate of the dielectric fluid in which fibers are dispersed.
[0013] The resistance flow regulator is designed to reduce the flow rate of the incoming
fluid and prevent the turbulence that would otherwise occur in random directions in
the orientation vessel, whereby permitting the adequate dispersion of fibers.
[0014] The resistance flow regulator may have a horizontal baffle plate which shifts the
flow of the fiber-dispersing dielectric fluid entering from above into the horizontal
direction. The horizontal baffle plate may have a "V" shape or may be a horizontal
plate. In addition, the horizontal baffle plate may have holes of desired shape.
[0015] The resistance flow regulator may be a suspending regulator 15 having a large number
of through holes as shown in Fig. 2. The through holes may be arranged vertically
or aslant in left direction or left and right directions.
[0016] As shown in Fig. 1, the discharge part has usually a drain pipe 61 connected to the
bottom of the orientation part. Incidentally, the supply part, orientation part, and
discharge part are not specifically limited in shape and size, and they are properly
selected according to the object and application.
[0017] The positive and negative electrodes are installed in the orientation part of the
orientation vessel. They extend vertically and are spaced horizontally at certain
intervals. There are at least one pair of positive and negative electrodes. The positive
and negative electrodes are usually of plate shape. Usually two or more pairs of positive
and negative electrodes are installed alternately at certain intervals as shown in
Fig. 1. In this case it is possible to reduce the distance between the positive and
negative electrodes in each orientation part. This is convenient because the one-dimensional
orientation can be carried out with a comparatively small electric field. The positive
and negative electodes can be made of a common material such as copper.
[0018] As shown in Fig. 1, the sheet drive unit 11 is installed between the orientation
part 5 and the discharge part 6 in the orientation vessel 7. It horizontally drives
the long filter sheet 10 which permits the dielectric fluid to pass therethrough and
the fibers to aggregate thereon.
[0019] There is disposed the filter plate 12 or filter belt 12a at the upper end of the
discharge part 6, as shown in Fig. 1 or 2. the filter plate 12 may be constructed
such that the filter sheet 10 slidingly moves on it.
[0020] The sheet drive unit 11 may have, at the downstream side of the filter sheet 10,
a cover part to supply a long covering sheet 13 which covers the fibers which have
aggregated on the filter sheet 10, as shown in Fig. 1. The covering with the covering
sheet 13 may be carried out at the plaace where the fiber aggregate 16 has emerged
from the case 1 of the orientation vessel 7, as shown in Fig. 1, or at the entrance
of the compression vessel 17 which arranged at the downstream side of the filter sheet
in the case 1, as shown in Fig. 3. The latter case is preferable because it is possible
to produce fiber aggregate having a greater compression ratio.
[0021] The apparatus of the invention may be provided with a high voltage source supply
device (not shown) to generate an electric field between the positive electrode 8
and negative electrode 9 as shown in Fig. 1.
[0022] The apparatus of the invention as shown in Fig. 2 is operated in the following manner
to produce the fiber agregate in which most fibers are one- dimensionally oriented.
[0023] The first step of the process of the invention for producing fiber aggregate is the
dispersion step in which short fibers, whiskers, or the like are dispersed into a
dielectric fluid.
[0024] The fibers used in the dispersion step are short fibers or whiskers or a mixture
thereof. Short fibers and whiskers of any kind can be used. They are not specifically
limited in diameter and length. Also, they are not limited in material so long as
they are capable of static orientation in the dielectric fluid when a high voltage
is applied across the positive and negative electrodes. The material of the fiber
includes, for example, alumina, silica, alumina-silica, beryllia, carbon, silicon
carbide, glass, and metals. Either fibers of single material or a mixture of fibers
of different materials may be used.
[0025] The dielectric fluid means a fluid which exhibits the dielectric properties upon
application of a high voltage. Examples of the dielectric fluid include carbon tetrachloride,
fluorine- and chlorine-substituted hydrocarbon, n-haxane, and cyclohexane. Preferable
among them is carbon tetrachloride. Fluorine- and chlorine - substituted hydrocarbons
are preferable from the standpoint of handling safety.
[0026] Fibers of some kinds or state may need surface treatment to loosen fibers sticking
together. To facilitate the dispersion of fibers, a proper amount of surface active
agent, especially a nonionic surface active agent, should be added to the dielectric
fluid.
[0027] The second step of the process of the invention is the orientation step, in which
the dielectric fluid containing the fibers dispersed therein is placed in a space
between a positive electrode and a negative electrode across which a high voltage
is applied, so that individual fibers in the dielectric fluid are statically oriented,
with one end pointing to the positive electrode and the other end pointing to the
negative electrode. The state in which most fibers are oriented in one direction across
the positive and negative electrodes is referred to as "one-dimensional orientation".
[0028] In the orientation step, usually an electric field of about 0.1 to 5 kV/cm² is generated
between the positive and negative electrodes. An electric field weaker than 0.1 kV/cm²
is not enough for the static orientation of fibers; and an electric field stronger
than 5 kV/cm² disturbs the dielectric fluid and interferes with the orientation of
fibers. Preferred electric field is about 1 to 2 kV/cm². It is suitable for static
orientation of fibers with a minimum disturbance of the dielectric fluid. The intensity
of electric field should be properly established according to the dielectric properties
of the fibers and dielectric fluid to be used and the thickness of the fiber aggregate
to be produced.
[0029] Furthermore, electric potential difference can be very small between the positive
and negative electrodes when more than two pair of electrodes are used to shorten
the distance between each pair of the electrodes in each orientation vessel.
[0030] The individual fibers which have been statically oriented as mentioned above are
mostly strung to one another in one direction (referred to as electrode direction
hereinafter) perpendicular to the direction in which the fibers settle. The stringing
fibers settle faster than discrete fibers.
[0031] In the third step, the statically oriented fibers are continuously aggregated on
the filter sheet while the oriented state of the fibers are being maintained, and
there is continuously obtained fiber aggregate in which many fibers are one-dimensionally
oriented.
[0032] The aggregating step may be accomplished by filtering by suction the dielectric fluid
containing fibers oriented in the orientation step, in the direction perpendicular
to the orientation direction of the fiber, whereby the oriented fibers 2a are collected
on the filter sheet 10. The dielectric fluid in the orientation vessel 7 is discharged
and then the gate (not shown) of the case 1 is opened and the filter sheet 10 is continuously
moved horizontally, whereby the fiber aggregate 16 is continuously taken off. In this
case it is preferable to compress the fiber aggregate 16 with the compression roller
14c.
[0033] The fiber aggregate produced by the aggregating step may be in the form of comparatively
thick mat shape or comparatively thin film shape.
[0034] The thus produced fiber aggregate in which many fibers are one-dimensionally oriented
is used, as such or after cutting to a desired shape or placing one top of another,
as the molded fiber reinforcement for FRM.
[0035] The apparatus of the invention for producing one-dimensionally oriented fiber aggregate
comprises an orientation vessel including a supply part, orientation part, and discharge
part; at least one pair of positive electrode and negative electrode; and a sheet
drive unit moving a long filter sheet horizontally between the orientation part and
the discharge part in the orientation vessel, above-mentioned filter sheet permitting
the dielectric fluid to pass therethrough and permitting the fibers to aggregate thereon.
[0036] The apparatus of the present invention makes it possible to aggregate fibers on the
filter sheet in such a manner that many fibers are one-dimensionally oriented and
causes the sheet drive unit to move the filter sheet horizontally. Thus it permits
the continuous production of fiber aggregate in which many fibers are one-dimensionally
oriented.
[0037] The apparatus of the present invention provides fiber aggregate in which many fibers
are one-dimensionally oriented, so that the fiber aggregate has less entanglement
of fibers and has a high fiber volume ratio. Therefore, the fiber aggregate provides
FRM of high strength.
[0038] The apparatus of the present invention provides fiber aggregate having less entanglement
of fibers. Therefore, it has a low degree of spring back, and it provides FRM of high
precision.
[0039] Having generally described this invention, a further understanding can be obtained
by reference to certain specific examples which are provided herein for purposes of
illustration only and are not intended to be limiting unless otherwise specified.
[0040] The invention is now described with reference to the following examples.
[0041] The apparatus used in this example is shown in Fig. 2. This apparatus is made up
of the following componenents.
(1) The resistance flow regulator 15 (suspending flow regulator) to control the flow
rate of the incoming fiber-dispersed dielectric fluid;
(2) The orientation vessel 7 which consists of the supply part 4, the discharge part
6, and the orientation part 5. (The supply part 4 receives through the suspending
flow regulator 15 the dielectric fluid 3 in which short fibers 2, etc., are dispersed,
and supplies the dielectric fluid 3 downward. The discharge part 6 discharges the
dielectric fluid 3 downward. The orientation part 5 permits the dielectric fluid 2
to move from the supply part 4 to the discharge part 6.);
(3) Three sets (or five pairs) of positive electrodes 8 and negative electrodes 9
installed alternately in the vertical direction at intervals in the horizontal direction
in the orientation part 5 of the orientation vessel 7;
(4) The sheet drive unit 11 to move the long filter sheet 10 in the horizontal direction.
The filter sheet 10 is placed between the orientation part 5 and the discharge part
6 in the orientation vesel 7. It permits the dielectric fluid 3 to pass therethrough
and the fibers to aggregate thereon; and
(5) The high voltage source apply device (not shown) to apply a high voltage across
the electrodes 8 and 9.
[0042] The filter sheet 10 is disposed on the porous belt 12a such as cloth. The porous
belt 12a and the filter sheet 10 are supported on the filter plate 12 disposed at
the top of the discharge part 6. The porous belt 12a is driven by the drive pulley
14e and the idle pulley 14d.
[0043] The sheet drive unit 11 has at the downstream side of the filter sheet 10, the covering
part to supply the long covering sheet 13 which covers the fibers which have aggregated
on the filter sheet 10. The covering part comprises the covering sheet supply pulley
14b and the like. In addition, the sheet drive unit 11 has the compression rollers
14c and 14e to compress the fiber aggregate 16 covered with the covering sheet 13.
There is the drain pipe 61 at the bottom of the case 1, and it is sucked by a suction
unit (not shown).
[0044] Carbon tetrachloride was placed in the space between the electrodes in the static
orientation apparatus. An electric field of about 0.1 to 5 kV/cm² was generated. The
dielectric fluid 3 into which the fibers 2 have been dispersed was poured into the
supply part 4 through the suspending flow regulator 15.
[0045] Using this apparatus, fiber aggregate was produced in the following manner.
[0046] Aluminum short fibers without surface treatment (having an average diameter of about
3 µm and a length of 10 to 500 µm) are added to carbon tetrachloride along with a
small amount of nonionic surface active agent. The fibers are dispersed by stirring.
[0047] The fiber-dispersed dielectric fluid fed from the supply part 4 is continuously sent
to the orientation part 5. Owing to the electric field generated between the positive
electrode 8 and the negative electrode 9 in the orientation part 5, the fibers undergo
static orientation, with one end of the fiber pointing to the positive electrode and
the other end pointing to the negative electrode. The statically oriented fibers 2a
become strung while they were settling, and the strung fibers settled in the state
of one-dimensional orientation in the direction across the positive and negative electrodes.
The dielectric fluid is sent further downward, and the dielectric fluid alone is passed
through the filter sheet 10 and sent to the discharge part 6. The statically oriented
fibers are aggregated on the filter sheet 10 in the one-dimensionally oriented state.
In this way there was obtained fiber aggregate 16 in the mat type form.
[0048] Since suction is applied to the lower part of the porous belt 12 through the drain
pipe 61, the dielectric fluid is discharged from the orientation vessel 7, and then
the gate on the side wall of the orientation vessel 7 is opened to permit the movement
of the filter sheet. Thus the fiber aggregate 16 is forced out by the filter belt
12a. The fiber aggregate 16 is subsequently covered with the covering sheet 13 and
compressed by the compressing rollers 14c and 14e.
[0049] The above-mentioned apparatus is made up of the orientation vessel, three sets (five
pairs) of positive and negative electrodes, and the sheet drive unit to move the long
filter sheet in the horizontal direction, above-mentioned filter sheet being installed
between the orientation part and the discharge part in the orientation vessel and
permitting the dielectric fluid to pass therethrough and the fibers to aggregate thereon.
Therefore, the apparatus continuously provides fiber aggregate in which many fibers
are one-dimensionally oriented well.
[0050] In addition, the apparatus is provided with the covering part to cover the fiber
aggregate with the covering sheet and the compressing rollers to compress the covered
fiber aggregate. Therefore, it can produce continuously easy-to-wind fiber aggregate
which is free of foreign matters and has a high fiber volume ratio.
[0051] The fiber aggregate in this example is one-dimensionally oriented, and consequently
it has a higher fiber volume ratio and a lower degree of spring back than the conventional
ones. Thus it provides FRM of high precision.
[0052] Having now fully described the invention, it will be apparent to one of ordinary
skill in the art that many changes and modifications can be made thereto without departing
from the spirit or scope of the invention as set forth herein.
1. An apparatus for producing oriented fiber aggregate which comprises:
an orientation vessel,
at least one pair of positive electrode and negative electrode, and
a sheet drive unit,
said orientation vessel including a supply part placed above which receives a dielectric
fluid in which are dispersed whiskers, short fibers, or a mixture thereof and supplies
the dielectric fluid downward, a discharge part which discharges the dielectric fluid
downward, and an orientation part through which the dielectric fluid moves downward
from the supply part to the discharge part;
said electrodes being installed vertically at a certain distance apart horizontally
in the orientation part of the orientation vessel;
said sheet drive unit moving a long filter sheet horizontally between the orientation
part and the discharge part in the orientation vessel;
said filter sheet permitting the dielectric fluid to pass therethrough and permitting
the fibers to aggregate thereon;
in operation of the apparatus, oriented fiber aggregate is produced by continuously
feeding the dielectric fluid with fibers dispersed therein from the supply part to
the orientation part, causing the fibers to statically orient with one end thereof
pointing to the positive electrode and the other end thereof pointing to the negative
electrode by means of the high voltage applied across the positive electrode and the
negative electrode in the orientation part, sending the fiber-containing dielectric
fluid downward while keeping the oriented state, passing the dielectric fluid alone
through the filter sheet and sending the filtered dielectric fluid to the discharge
part, aggregating the statically oriented fibers on the filter sheet, moving the filter
sheet horizontally by means of the sheet drive unit, whereby fiber aggregate in which
many fibers are one-dimensionally oriented is continuously produced on the filter
sheet.
2. An apparatus for producing oriented fiber aggregate as claimed in Claim 1, wherein
both the positive electrode and the negative electrode are in the plate form and two
or more positive electrodes and negative electrodes are installed alternately at certain
intervals.
3. An apparatus for producing oriented fiber aggregate as claimed in Claim 1, wherein
a filter plate is installed at the top of the discharge part so that the filter sheet
moves on the filter plate while being supported on the filter plate.
4. An apparatus for producing oriented fiber aggregate as claimed in Claim 1, wherein
the sheet drive unit has, at the downstream side of the filter sheet, a cover part
to supply a long covering sheet which covers the fibers which have aggregated on the
filter sheet.