BACKGROUND OF THE INVENTION
1. Field of the Invention
[0001] This invention relates to an acrylic synthetic fiber, especially an acrylic synthetic
fiber having vein-like or straw-like voids extending substantially in parallel to
the longitudinal axis of the fiber, which can be easily split into finer fibers by
an external force, and a process for the preparation of this acrylic synthetic fiber.
Furthermore, the present invention relates to a pulpy acrylic synthetic fibrous article
having excellent properties as the starting material for a friction material, paper
or nonwoven fabric. Moreover, the present invention relates to a friction material
comprising this pulpy acrylic synthetic fibrous article as a base material.
2. Description of the Related Art
[0002] Hollow acrylic fibers are known, for example, from Japanese Unexamined Patent Publication
51-149922 and Japanese Unexamined Patent Publication No. 57-89612. The conventional
hollow acrylic fibers include a fiber having cell-like independent voids in the interior
thereof and a tubular fiber having in the interior thereof a hole continuous along
the fiber axis.
[0003] The hollow acrylic fiber having cell-like independent voids has only a few large
voids in the transverse section thereof, as disclosed in, for example, Japanese Unexamined
Patent Publication No. 51-149922.
[0004] The hollow acrylic fiber disclosed in Japanese Unexamined Patent Publication No.
57-89612 has in the transverse section thereof several of relatively large voids,
as shown in the drawings of the patent publication, and this fiber cannot be easily
split.
[0005] Voids in these known hollow fibers are cell-like voids or long voids extending along
the longitudinal direction of the fiber, and the length of these voids is about 40
to about 50 µm at most.
[0006] The objects of forming voids in fibers in the conventional techniques are to decrease
the weight, improve the heat-insulating property, impart a water-absorbing property,
give a soft touch, and give a dry touch. To attain these objects, acrylic synthetic
fibers having voids as disclosed in the above-mentioned patent publications provide
excellent results.
[0007] Recently, the need for a fiber having a variety of greatly improved properties has
increased, and attention is now focused on a fiber having characteristics such that,
after a formation of a fiber structure or after a further formation of the fiber structure
into a fibrous product such as a knitted or woven fabric, the fiber can be split into
finer fibers by various means. Fibers having such properties are characterized in
that the freedom of processability is increased, whereby the fibers can be split into
finer fibers at an optional processing stage after a formation of fiber structures,
and fibrous products having excellent properties not attainable from conventional
fibers can be provided.
[0008] From this viewpoint, the hollow acrylic synthetic fibers disclosed in the above-mentioned
patent publications have problems in that they cannot be split into finer fibers by
an external force, for example, by beating and rubbing.
[0009] The main reasons why the fibers disclosed in the above-mentioned patent publications
cannot be easily split into finer fibers by an external force are that (1) the proportion
of voids in the transverse section of fiber is small and (2) the voids are cell-like
voids and do not extend far in the longitudinal direction of the fiber.
[0010] Fibers that can be split into finer fibers by an external force are known from, for
example, Japanese Unexamined Patent Publication No. 47-32122 and Japanese Unexamined
Patent Publication No. 55-30460.
[0011] The fiber disclosed in Japanese Unexamined Patent Publication No. 47-32122 is a conjugate
fiber in which, in the transverse section of a single filament, a water-insoluble
polymer is separated into several parts by a water-soluble polyamide extending in
radial directions. The fiber disclosed in Japanese Unexamined Patent Publication No.
55-30460 is a fibrilated conjugate fiber composed of a polyamide and a polymer having
no affinity with the polyamide.
[0012] The costs of these fibers are inevitably high, mainly for the following reasons.
Namely, since the fibers are formed by bonding at least two polymers having different
characteristics, different polymers must be used, and a special spinneret must be
used for the conjugation. Moreover, it is difficult to maintain a constant ratio between
the two components, and when both components are made finer and bonded together, an
advanced technique is necessary for adjusting the ratio between the two components.
[0013] Prior to the present invention, a fiber composed of an acrylic polymer, that can
be easily split into finer fibers by an external force, was not known.
SUMMARY OF THE INVENTION
[0014] The primary object of the present invention is to provide an acrylic polymer fiber
that can be easily split into fine fibers by an external force.
[0015] It was found that, if openings having an indeterminate shape are formed in the transverse
section of the fiber and each opening has a vein-like or straw-like void extending
substantially in parallel to the longitudinal axis of the fiber in the interior of
the fiber, this fiber can be easily split into finer fibers by an external force.
[0016] More specifically, in accordance with one aspect of the present invention, there
is provided an acrylic synthetic fiber having in the transverse section thereof a
multiplicity of openings having an indeterminate shape and a size of 0.1 to 1.6 µm,
wherein in the interior of the fiber, each opening forms a vein-like or straw-like
void extending substantially in parallel to the longitudinal axis of the fiber and
having a length of at least 60 µm.
[0017] In accordance with another aspect of the present invention, there is provided a process
for the preparation of an acrylic synthetic fiber, which comprises a) dissolving in
a suitable solvent an acrylic polymer comprising at least 60% by weight of an acrylonitrile
unit and 5% to 20% by weight, based on the weight of the acrylic polymer, of a polyalkylene
glycol having a number average molecular weight of 5,000 to 50,000, b) aging the formed
spinning solution for at least 4 hours, and c) extruding the spinning solution into
a coagulating medium through a spinneret.
BRIEF DESCRIPTION OF THE DRAWINGS
[0018]
Figure 1 is an electron microscope photograph of the longitudinal section of the acrylic
synthetic fiber prepared in Example 1 according to the process of the present invention;
Fig. 2 is a similar photograph of the transverse section of the acrylic synthetic
fiber shown in Fig. 1;
Fig. 3 is a similar photograph of the fiber obtained by splitting the acrylic synthetic
fiber shown in Fig. 1;
Fig. 4 is an electron microscope photograph of the transverse section of the acrylic
synthetic fiber prepared in Example 2 according to the present invention;
Fig. 5 is a similar photograph of the fiber obtained by splitting the acrylic synthetic
fiber shown in Fig. 4;
Figs. 7 through 9 are electron microscope photographs of the transverse sections of
the acrylic synthetic fibers prepared in Example 3 according to the process of the
present invention;
Figs. 6 and 10 are similar photographs of the transverse sections of the comparative
acrylic synthetic fibers obtained in Example 3;
Figs. 12 and 13 are electron microscope photographs of the transverse sections of
the acrylic synthetic fibers prepared in Example 4 according to the process of the
present invention;
Fig. 11 is similar photograph of the transverse section of the comparative acrylic
synthetic fiber obtained in Example 4;
Fig. 14 is an electron microscope photograph (100 magnifications) of the shape and
construction of the acrylic synthetic fibrous article prepared in Example 6;
Fig. 15 is an electron microscope photograph (5,000 magnifications) of the longitudinal
section of the acrylic synthetic fiber prepared in Example 5; and
Fig. 16 is a similar photograph (3,000 magnifications) of the transverse section of
the acrylic synthetic fiber shown in Fig. 15; and
Fig. 17 is an electron microscope photograph (200 magnifications) of the fiber obtained
by splitting the acrylic synthetic fiber shown in Figs. 15 and 16.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0019] The acrylic synthetic fiber of the present invention will now be described in detail.
[0020] The acrylic polymer constituting the acrylic synthetic fiber of the present invention
is a homopolymer of acrylonitrile or is a copolymer comprised of at least 60% by weight
(all of "%" given hereinafter are by weight unless otherwise indicated) of acrylonitrile
and up to 40% of an ethylenic monomer copolymerizable with acrylonitrile, or a mixture
of two or more of such polymers.
[0021] Ethylenic monomers copolymerizable with acrylonitrile are known monomers. For example,
there can be mentioned acrylic acid, methacrylic acid, esters thereof (such as methyl
acrylate, ethyl acrylate, methyl methacrylate and ethyl methacrylate), vinyl acetate,
vinyl chloride, vinylidene chloride, acrylamide, methacrylamide, methacrylonitrile,
allylsulfonic acid, methallylsulfonic acid, styrenesulfonic acid, vinylpyridine, 2-methyl-5-vinylpyridine
and N,N-dimethylaminoethyl methacrylate.
[0022] As pointed out hereinbefore, the acrylic synthetic fiber of the present invention
is characterized in that, in the section of the fiber cut orthogonally to the longitudinal
axis of the fiber (hereinafter referred to as "the transverse section of the fiber"),
many openings having an indeterminate shape are formed and each opening forms a vein-like
or straw-like void extending substantially in parallel to the longitudinal axis of
the fiber.
[0023] In the transverse section of the fiber of the present invention, the sectional shape
of the void of each opening is indeterminate. More specifically, the sectional shapes
of voids of the openings include substantially circular shapes, flat shapes, shapes
of repeated bends having acute edges, shapes having a large section, shapes having
a small section and the like, as shown in Fig. 2 of the accompanying drawings, and
the shape and size of the voids are not constant but irregular. Since many such indeterminate
voids are present, splitting can be easily performed by an external force. It is especially
preferred that sectional shapes of the voids be defined by repeated bends having acute
edges. If the voids have such a sectional shape, the fiber can be split more easily.
[0024] The size (diameter) of the voids is not particularly critical, so long as the requirements
described hereinafter are satisfied, but to split the fiber easily and obtain fine
fibers by splitting, preferably many fine voids are present. Note, even if relatively
large voids are present, the intended objects can be attained if fine voids are present
around these relatively large voids.
[0025] As shown in Fig. 1 of the accompanying drawings, each of the above-mentioned openings
forms a vein-like or straw-like void extending substantially in parallel to the longitudinal
axis of the fiber in the interior of the fiber.
[0026] The length of the voids along the longitudinal axis of the fiber (hereinafter referred
to as "the void length") should be such that the fiber can be easily split. These
slender voids are distinguishable over the conventional voids which are formed to
have a relatively large and independent cell-like shape for imparting a soft touch
and attaining a heat-insulating effect. In the fiber of the present invention, the
void length is at least 60 µm. If the void length is smaller than 60 µm, splitting
of the fiber is very difficult even if the void number is increased.
[0027] The larger the void length, the more easily split the fiber, as long as the void
length is at least 60 µm. Therefore, most preferably the voids are continuous substantially
along the entire length of the fiber.
[0028] In the transverse section of the fiber, voids should be present in a large number
such that the fiber can be easily split, but the necessary number of voids depends
on the void length and cannot be easily stipulated. If the void length is large, the
fiber can be easily split even when the number of voids is relatively small, but,
in general, preferably at least 100 voids are present. Where the number of voids is
smaller than 100, splitting of the fiber is very difficult even if the voids are continuous
voids having a length of at least 60 µm. If at least 100 voids are present in the
transverse section, the more easily split the fiber, and further, the finer the split
fibers.
[0029] To obtain fine split fibers, preferably the voids are uniformly dispersed in the
transverse section of the fiber.
[0030] In the acrylic synthetic fiber of the present invention, the void ratio, that is,
the ratio of the sectional area of the void to the total area of the transverse section
of the fiber, is preferably 5 to 80%. If the void ratio is lower than 5%, the void
number is small and splitting of the fiber is difficult. If the void ratio is higher
than 80%, the preparation of the fiber per se is difficult.
[0031] The void ratio referred to herein is defined by the following formula:

[0032] The apparent denier is calculated from the sectional area of the single fiber and
the true denier is calculated by the weight method. The determination is performed
with respect to 10 sample fibers of one lot, and the mean value is calculated.
[0033] The size (diameter) of the voids in the transverse section of the fiber cannot be
clearly specified because the voids have an indeterminate shape, but preferably the
average diameter of the circumscribed circle of the voids is at least about 0.1 µm.
[0034] As pointed out hereinbefore, the acrylic synthetic fiber of the present invention
is characterized by the void length, the number of voids, and the cross-sectional
shape of the voids. The fiber can be easily split by an external force due to the
combination of these characteristic features, and the split fiber can be used in the
form of an assembly of fine fibers or a dispersion of fine fibers.
[0035] In the present invention, the external force means the stress imposed on the fiber
at the fiber-processing step, for example, by a disk refiner used in the paper-making
industry or a columnar stream punching of high-pressure water adopted in the nonwoven
fabric-manufacturing process.
[0036] The acrylic synthetic fiber of the present invention can be used in the fields of
clothing nonwoven fabrics, paper products and the like while the foregoing characteristic
properties are utilized.
[0037] The process for the preparation of the acrylic synthetic fiber of the present invention
will now be described.
[0038] As pointed out hereinbefore, the acrylic polymer used in the present invention is
a polymer comprising at least 60% of acrylonitrile. If the amount of acrylonitrile
is smaller than 60%, the softness and wooly touch inherently possessed by the acrylic
synthetic fiber are lost. The upper limit of the amount of acrylonitrile is not critical.
The acrylic polymer used in the present invention can be a mixture comprising at least
two kinds of acrylic polymers. In this case, the content of acrylonitrile should be
at least 60% based on the total weight of the polymer mixture.
[0039] The polymer is dissolved in a known solvent for acrylic polymers, for example, an
organic solvent such as dimethylformamide, dimethylacetamide or dimethylsulfoxide,
a concentrated aqueous solution of an inorganic salt such as a rhodanate, zinc chloride,
or a concentrated aqueous solution of an inorganic acid such as nitric acid, whereby
a spinning solution is prepared. An optimum concentration of the polymer in the spinning
solution depends on the kind of the solvent, but in general, preferably the polymer
concentration is 10 to 30%.
[0040] A polyalkylene glycol is added to this spinning solution. The addition of the polyalkylene
glycol is one of important requirements for the preparation of the acrylic synthetic
fiber of the present invention. Especially, the molecular weight and amount of the
polyalkylene glycol added make great contributions to formation of voids.
[0041] The polyalkylene glycol is preferably a random or block copolymer comprising ethylene
oxide and propylene oxide at a weight ratio of from 80/20 to 20/80. The number average
molecular weight of the polyalkylene glycol is 5,000 to 50,000, preferably 10,000
to 20,000. If the number average molecular weight of the polyalkylene glycol is lower
than 5,000, voids continuously extending in the longitudinal direction of the fiber
cannot be formed, and a microporous fiber having very fine, substantially spherical
voids is formed. If the number average molecular weight of the polyalkylene glycol
is higher than 50,000, a fiber having large vein-like voids is obtained, and in the
transverse section of the obtained fiber, only a few of the needed of voids are present.
This fiber cannot be split into fine fibers by an external force such as a columnar
stream of a liquid. Especially, if the number average molecular weight of the polyalkylene
glycol is 10,000 to 20,000, a fiber having fine and slender voids which are continuous
along the longitudinal direction of the fiber and having an indeterminate cross-sectional
shape in the transverse section of the fiber can be obtained.
[0042] To prepare the acrylic synthetic fiber of the present invention, the spinning solution
formed by dissolving the polyalkylene glycol must be aged for at least 4 hours.
[0043] By the term "aging" as used herein is meant that the spinning solution formed by
dissolving the acrylic polymer and polyalkylene glycol is not violently stirred or
shaken but, for example, the spinning solution is allowed to stand or is gently moved,
for example, gently delivered through a pipe.
[0044] The reason why an acrylic synthetic fiber having the above-mentioned voids can be
obtained by thus aging the spinning solution in the present invention has not been
elucidated, but it is considered that the reason is probably as follows. Namely, if
the spinning solution is aged for at least 4 hours, cohesion of the polyalkylene glycol
occurs, and when the spinning solution passes through a pipe and is spun into a coagulating
medium from a spinneret, the shearing force acts on the spinning solution and fine
streaks of the polyalkylene glycol are formed. Then, a phase separation occurs between
the two polymers, because of a difference of coagulating characteristics, that is,
coagulation of the acrylic polymer and non-coagulation of the polyalkylene glycol,
whereby voids having a complicated shape as mentioned above are formed.
[0045] Thus, the spinning solution must be aged for at least 4 hours before the spinning.
[0046] In the foregoing points, the process and fiber of the present invention are essentially
distinguishable over the process and fiber disclosed in Japanese Unexamined Patent
Publication No. 57-89612. More specifically, in the process disclosed in Japanese
Unexamined Patent Publication No. 57-89612, a polyalkylene oxide having a number average
molecular higher than 100,000 is used. If a polyalkylene oxide having such a high
molecular weight is used, the polyalkylene oxide is dispersed in the form of spheres
in the spinning solution, as taught in the above-mentioned patent publication. Accordingly,
when this spinning solution is spun in a coagulating bath, spheres of the polyalkylene
oxide are present in the fiber, and the polyalkylene oxide is eluted in the coagulating
bath, water-washing bath or drawing bath and there remain spherical voids or voids
elongated in the longitudinal direction of the fiber according to the degree of drawing.
[0047] In contrast, in the present invention, since the polyalkylene glycol used has a low
molecular weight such as a number average molecular weight of 5,000 to 50,000, the
polyalkylene glycol is dissolved in the spinning solution to form a homogeneous solution,
and if this solution is aged, cohesion of the polyalkylene glycol occurs in the spinning
solution. By aging the spinning solution for at least 4 hours, fine streaks are formed
by the cohesion of the polyalkylene glycol. When this spinning solution is extruded
into the coagulating bath, in the coagulated fiber, a phase separation into the acrylic
polymer and the streak-like polyalkylene glycol occurs, and simultaneously, by elution
of the polyalkylene glycol, fine voids are formed in the coagulated fiber.
[0048] The aging time is at least 4 hours and the upper limit of the aging time is not critical,
but preferably 6 to 10 hours.
[0049] In the present invention, the amount of the polyalkylene glycol added is 5 to 20%,
preferably 10 to 15%, based on the acrylic polymer. If the amount of the polyalkylene
glycol added is smaller than 5%, the number of voids present in the transverse section
of the fiber is small, and a fiber having many voids, for example, at least 100 voids,
cannot be obtained. If the amount of the polyalkylene glycol added is larger than
20%, the number of openings increases but the number of openings is too large and
the fiber is split during the preparation or the spinning cannot be carried out stably.
If the amount of the polyalkylene glycol added is 10 to 15%, the best balance between
the number of openings and the spinning stability is maintained.
[0050] In the foregoing description, the polyalkylene glycol is added after the preparation
of the spinning solution but the mixing method is not limited to this method, and
the spinning solution can be prepared according to a method in which the polyalkylene
glycol is mixed with the acrylic polymer and the mixture is dissolved in a solvent
for the polymer, or a method in which the polyalkylene glycol is dissolved in advance
in a solvent for the acrylic polymer and the acrylic polymer is then dissolved in
the solution.
[0051] The spinning solution is extruded into a coagulating medium for the spinning solution
through a spinneret, and the extrudate is passed through water-washing, drawing and
drying steps and is heat-set according to need.
[0052] In this preparation process, the polyalkylene glycol is eluted from the coagulated
fiber during the coagulating, water-washing and drawing steps. Steps subsequent to
the spinning step, as adopted in the conventional process for the preparation of acrylic
synthetic fibers, can be directly adopted in the present invention.
[0053] Namely, in the present invention, as the means for spinning the spinning solution,
there can be adopted the wet spinning method comprising extruding the spinning solution
into a dilute aqueous solution of a solvent, the dry spinning method comprising extruding
the spinning solution into an inert gas such as air or nitrogen gas, and the dry-wet
spinning method comprising extruding the spinning solution into the above-mentioned
inert gas and then introducing the extrudate into a dilute aqueous solution of a solvent.
The coagulated fiber obtained by the spinning is washed with water and then drawn,
water-washed and simultaneously drawn, or drawn and then water-washed, whereby the
solvent is removed.
[0054] The drawing is carried out in water, a solvent-containing aqueous solution or steam
at 50 to 150°C at a draw ratio of several to ten-odd times. The drawing can be performed
in a single stage or a plurality of stages. Moreover, several drawing media can be
used in combination. The drawn fiber is dried, and if desired, the dried fiber is
subjected to the secondary drawing or to the heat treatment, whereby the acrylic synthetic
fiber of the present invention can be obtained.
[0055] The acrylic synthetic fibrous article of the present invention will now be described.
[0056] By the term "acrylic fibrous article" used herein is meant a pulpy fibrous article
prepared from the above-mentioned acrylic synthetic fiber. More specifically, the
acrylic fibrous article of the present invention is characterized as having as a trunk
an acrylic synthetic fiber having in the transverse section thereof a multiplicity
of openings having an indeterminate shape and a size of 0.1 to 1.6 µm, wherein in
the interior of the fiber, each opening forms a vein-like or straw-like void extending
substantially in parallel to the longitudinal axis of the fiber and having a length
at least 60 µm, and the surface of the trunk has a multiplicity of fine fibrils branched
from the trunk and the trunk is partially split in the longitudinal direction of the
trunk and separated into a plurality of fibers.
[0057] The acrylic synthetic fibrous article of the present invention can be easily prepared
by applying an external force to the above-mentioned acrylic synthetic fiber, for
example, by beating the acrylic synthetic fiber by a disk refiner customarily adopted
in the paper-making industry or by punching the acrylic synthetic fiber by a high-pressure
water columnar stream adopted in the nonwoven fabric-preparing process. At this step,
the amount of generated fibrils, the fineness of the fibrils and the frequency of
splitting of the trunk can be adjusted by appropriately selecting the conditions of
the external force applied to the fiber.
[0058] Figure 14 is an electron microscope photograph (100 magnifications) of the fibrous
article obtained by beating the fiber shown in Fig. 2. As is seen from Fig. 14, a
multiplicity of fine fibrils branched from the fiber are formed on the surface of
the fiber, and it is seen that the acrylic synthetic fiber constituting the trunk
is partially split into a plurality of finer fibers.
[0059] The fine fibrils branched from the acrylic synthetic fiber or trunk may have many
voids extending along the longitudinal axis of the fiber, as well as the acrylic synthetic
fiber or trunk, or the fine fibrils may not have such voids.
[0060] The acrylic synthetic fiber is split in a plurality of finer fibers at an optional
position in the longitudinal direction of the fiber, but this splitting position is
not critical.
[0061] The fact that the trunk fiber is split in a plurality of fine fibers at an optional
position means that the fiber has an improved softness and pliability, and a paper
or sheet product or nonwoven fabric having high elasticity and bulkiness can be obtained
from this fiber.
[0062] The friction material of the present invention will now be described.
[0063] This frictional material is prepared from the above-mentioned acrylic synthetic fiber.
[0064] More specifically, the frictional material of the present invention is characterized
as comprising an acrylic synthetic fibrous article, a resin and a filler, said acrylic
synthetic fibrous article having as a trunk an acrylic fiber having in the transverse
section thereof a multiplicity of openings having an indeterminate shape and a size
of 0.1 to 1.6 µm, wherein in the interior of the fiber, each opening forms a vein-like
or straw-like void extending substantially in parallel to the longitudinal axis of
the fiber and having a length of at least 60 µm, and the surface of the trunk has
a multiplicity of fine fibrils branched from the trunk and the trunk is partially
split in the longitudinal direction of the trunk and separated into a plurality of
fibers.
[0065] By using the fiber having the above-mentioned specific shape as the substrate of
the friction material, the friction coefficient and abrasion resistance are highly
improved in the obtained friction material.
[0066] The reason for this improvement has not been elucidated, but it is considered that
the reason is probably as follows. Namely, since the acrylic synthetic fiber of the
present invention has many vein-like voids in the trunk, the resin and filler are
allowed to intrude into these voids, and since many fine fibrils are present on the
surface of the trunk, the resin and filler intrude into spaces defined by the trunk
and fibrils. Accordingly, the fibrous article, resin and filler are very closely integrated
as a whole.
[0067] The transverse section and longitudinal section of each of the fine fibers formed
at the split portion of the acrylic fiber or trunk depend on the splitting degree,
but if the splitting degree is low, for example, if the trunk fiber is split into
2 to 10 fine fibers, these sections are substantially the same as those of the original
fiber (trunk) except that the number of openings in the transverse section should
naturally be smaller than the number of openings in the transverse section of the
original fiber (trunk). If the splitting degree is very high, openings are not found
in transverse sections of some of fine fibers formed by splitting.
[0068] In the transverse sections of fine fibrils branched from the trunk, openings are
found or not found, and the presence or absence of openings depends on the branching
degree. Namely, where the fibrils are relatively thick, openings are found, and where
the fibrils are very fine, openings are not found. Generally, these fine and thick
fibrils are mingled.
[0069] The acrylic synthetic fibrous article of the present invention is contained preferably
in an amount of 10 to 70%, more preferably 20 to 60%, in the friction material. If
the content of the fiber is lower than 10%, no substantial improvement of the friction
coefficient or abrasion resistance is obtained even by using the fiber as base material.
If the fiber content exceeds 70%, the resulting product is not suitable as the friction
material because the amount of the fiber is too large. Preferably, the content of
the resin is 20 to 70%, and the content of the filler is 10 to 50%.
[0070] A resin customarily used for friction materials can be used in the present invention.
For example, phenolic resins, epoxy resins, polyimide resins, melamine resins, natural
rubbers and synthetic rubbers can be used.
[0071] In the present invention, the filler is used for improving the characteristics of
the friction material. In general, at least one member selected from the group consisting
of metal powders, silica, clay, wollastonite, mica, talc, diatomaceous earth, calcium
carbonate, cashew dust and graphite can be used as the filler.
[0072] For improving the characteristics of the friction material, other fibrous material
such as a glass fiber, a metal fiber, a carbon fiber, a flame-retardant fiber, a polyvinyl
alcohol fiber, a polyamide fiber, a polyester fiber, an acrylic fiber or cotton can
be incorporated.
[0073] In the acrylic synthetic fibrous article of the present invention, the acrylic fiber
as the trunk has many vein-like or straw-like voids. Accordingly, the resin and filler
are allowed to intrude easily into these voids. Moreover, the resin and filler intrude
into spaces formed by partial splitting of the trunk and the fine fibrils branched
from the trunk. Accordingly, the fibrous article, resin and filler are very closely
and intimately mingled and integrated with one another. Therefore, the friction material
has a high friction coefficient and an excellent abrasion resistance.
[0074] The acrylic synthetic fibrous article used for the friction material of the present
invention can be prepared by beating the above-mentioned acrylic synthetic fiber by
a disk refiner customarily used in the paper-making industry. At this step, the degree
of formation of fine fibrils and the degree of splitting of the trunk are changed
according to the properties required for the friction material. In general, these
degrees are preferably such that the freeness, used for indicating the beating degree
of pulp in the paper-making industry, is about 600 to about 200 cc, but the freeness
is not limited to within this range, and may be larger than 600 cc or smaller than
200 cc. Namely, the freeness can be appropriately set according to the properties
required for the friction material. Note, the freeness referred to herein is the value
determined according to the method of JIS P8121-1976.
[0075] The acrylic synthetic fibrous article is mixed with the resin and filler and molded
into a friction material.
[0076] The friction material can be prepared according to a process in which a substrate
comprising the acrylic synthetic fibrous article and filler, for example, a paper-like
sheet or a nonwoven fabric, is prepared and the substrate is impregnated with the
resin, molded and then cured, a method in which the acrylic synthetic fibrous article
is mixed with the resin and filler, and the mixture is molded and then curing, and
other known methods.
[0077] The present invention will now be described in detail with reference to the following
examples that by no means limit the scope of the invention.
Acrylic synthetic fiber and process for preparation thereof
Example 1
[0078] A polymer comprising 95.0% of acrylonitrile, 4.5% of methyl acrylate and 0.5% of
sodium methallylsulfonate and a polyethylene oxide/polypropylene oxide/polyethylene
oxide block polyether (number average molecular weight = 10,000, polyethylene oxide/polypropylene
oxide ratio = 70/30) were dissolved in dimethylformamide to form a spinning solution
containing 23% of the acrylic polymer and 2.3% of the block polyether. The spinning
solution was allowed to stand for 6 hours and then was extruded into a coagulating
bath maintained at 35°C and having a dimethylformamide concentration of 75% through
a spinneret. The extrudate was washed with water, drawn at a draw ratio of 12 in boiling
water and dried in hot air at 80°C to obtain a fiber having a fineness of 1.5 d.
[0079] An electron microscope photograph (4,000 magnifications) of the longitudinal section
of the fiber cut in the longitudinal direction (hereinafter referred to as "longitudinal
section") is shown in Fig. 1, and a similar photograph of the transverse section of
the fiber is shown in Fig. 2.
[0080] In Fig. 1, black portions are spaces, and it is seen that these spaces are continuous
streak-like spaces extending substantially in parallel to one another along the longitudinal
axis of the fiber. When the longitudinal section of the fiber was observed, these
spaces were found to have a length of at least 60 µm.
[0081] In Fig. 2, black portions are openings, and it is seen that these openings include
substantially circular openings, flat openings, openings having a shape of repeated
bends having acute edges, openings having a large section, openings having a small
section, and various openings having an indeterminate shape, are irregularly mingled
with one another.
[0082] The void ratio of the obtained fiber was 35%.
[0083] The fiber was treated with a high-pressure water stream jetted under a pressure of
50 kg/cm² from a nozzle having an orifice diameter of 0.15 mm 10 times, whereby the
fiber was split into fine fibers to form an assembly of fine-denier fibers.
[0084] Figure 3 is an electron microscope photograph (200 magnifications) of the obtained
assembly. As is seen Fig. 3, the fiber of the present invention can be easily split
by an external force to form an assembly of finer continuous fibers.
Example 2
[0085] The same acrylic polymer as used in Example 1 and an ethylene oxide/propylene oxide
random copolymer polyether (number average molecular weight = 10,000, ethylene oxide/propylene
oxide ratio = 75/25) were dissolved in a 67% aqueous solution of nitric acid to form
a spinning solution having an acrylic polymer concentration of 16% and a random copolymer
polyether concentration of 2.4%. The spinning solution was allowed to stand for 4
hours and then was extruded into a 37% aqueous solution of nitric acid maintained
at 0°C through a spinneret. The extrudate was washed with water, drawn at a draw ratio
of 10 and dried by hot air at 70°C to obtain a fiber having a fineness of 3.5 d. The
void ratio of the fiber was 40%.
[0086] An electron microscope photograph (1,000 magnifications of the transverse section
of the obtained fiber is shown in Fig. 4. When the longitudinal section of the fiber
was observed, continuous streak-like spaces having a length of at least 60 µm were
found.
[0087] The obtained fiber was treated with a high-pressure water stream 5 times in the same
manner as described in Example 1 to obtain an assembly of finely split fibers. An
electron microscope photograph (200 magnifications) of the obtained assembly is shown
in Fig. 5.
[0088] For comparison, the above procedures were repeated in the same manner except that
the aging time of the spinning solution was changed to 3 hours. The transverse section
of the obtained fiber and several large and long voids. This fiber could not be split
by a high pressure water stream.
Example 3
[0089] An acrylic polymer comprising 97% of acrylonitrile, 2.5% of methyl acrylate and 0.5%
of sodium allylsulfonate and an ethylene oxide/propylene oxide random copolymer polyether
having an ethylene oxide/propylene oxide copolymerization ratio of 75/25 and a number
average molecular weight of 3,000, 5,000, 30,000, 50,000 or 60,000 were dissolved
in a 67% aqueous solution of nitric acid at 0°C to form a spinning solution. In the
spinning solution, the acrylic polymer concentration was 18% and the polyalkylene
glycol concentration was 1.8%.
[0090] The spinning solution was slowly delivered in a pipe over a period of 5 hours and
then was extruded into a 38% aqueous solution of nitric acid at 0°C through a spinneret.
The extrudate was washed with water, drawn at a draw ratio of 8 in boiling water and
dried in hot air at 70°C to obtain a fiber.
[0091] Electron microscope photographs of the transverse sections of the obtained fibers
are shown in Figs. 6 through 10, and the obtained fibers are summarized in Table 1.
In Table 1, the amount of the polyalkylene glycol added is expressed in terms of %
based on the acrylic polymer. When the longitudinal sections of the fibers shown in
Figs. 7, 8 and 9 where observed, continuous streak-like spaces having a length of
at least 60 µm were found.
[0092] These fibers were treated with a high-pressure water stream in the same manner as
described in Example 1. The fibers of the present invention were split into finer
fibers, but little splitting of the comparative fibers occurred.
Table 1
| Run No. |
Molecular weight |
Polyalkylene glycol Amount added ** (%) |
Fineness (denier) |
Electron microscope photograph |
Void ratio (%) |
| |
|
|
|
Magnifications |
Fig. No. |
|
| 1* |
3,000 |
10 |
1 |
5000 |
6 |
2.4 |
| 2 |
5,000 |
10 |
1 |
5000 |
7 |
15 |
| 3 |
30,000 |
10 |
3.5 |
1000 |
8 |
38 |
| 4 |
50,000 |
10 |
1 |
5000 |
9 |
20 |
| 5* |
60,000 |
10 |
1 |
5000 |
10 |
3.8 |
| * comparative example |
| ** based on the weight of the polymer |
Example 4
[0093] An acrylic polymer comprising 96% of acrylonitrile, 3.5% of vinyl acetate and 0.5%
of sodium styrene-sulfonate and an ethylene oxide/propylene oxide random copolymer
polyalkylene glycol (ethylene oxide/propylene oxide ratio = 75/25, number average
molecular weight = 20,000) were dissolved in a 67% aqueous solution of nitric acid
at 0°C to form a spinning solution. In the spinning solution, the concentration of
the acrylic polymer was 16% and the concentration of the polyalkylene glycol was 3,
5, 20 or 24 %. The obtained spinning solution was allowed to stand for 5 hours and
extruded into a 38% aqueous solution of nitric acid at 0°C through a spinneret. The
extrudate was washed with water, drawn at a draw ratio of 10 in boiling water, and
dried in hot air at 70°C to form a fiber.
[0094] When the polyalkylene glycol concentration was 24%, yarn breakage occurred during
the spinning operation and it was difficult to carry out a stable spinning operation.
[0095] Electron microscope photographs of the transverse sections of the obtained fibers
are shown in Figs. 11 through 13. The obtained fibers are summarized in Table 2. When
the longitudinal sections of the fibers shown in Figs. 12 and 13 were observed, continuous
streak-like spaces having a length of at least 60 µm were found.
[0096] Then the fibers were treated with a high-pressure water stream in the same manner
as described in Example 1. The fibers of the present invention were split into finer
fibers, but when the polyalkylene glycol concentration was 3%, the number of voids
was small and the fiber could not be split into finer fibers.
Table 1
| Run No. |
Molecular weight |
Polyalkylene glycol Amount added ** (%) |
Fineness (denier) |
Electron microscope photograph |
Void ratio (%) |
| |
|
|
|
Magnifications |
Fig. No. |
|
| 1* |
20,000 |
3 |
1.5 |
5000 |
11 |
2.4 |
| 2 |
20,000 |
5 |
3 |
1000 |
12 |
8 |
| 3 |
20,000 |
20 |
7 |
5000 |
13 |
60 |
| 4* |
20,000 |
24 |
- |
- |
- |
|
| * comparative example |
| ** based on the weight of the polymer |
Example 5
[0097] A polymer comprising 95.0% of acrylonitrile, 4.5% of methyl acrylate and 0.5% of
sodium methallylsulfonate and a polyethylene oxide/polypropylene oxide/polyethylene
oxide block copolymer polyether (number average molecular weight = 10,000, polyethylene
oxide/polypropylene oxide ratio = 70/30) were dissolved in dimethylformamide to form
a spinning solution having an acrylic polymer concentration of 23% and a block copolymer
polyether concentration of 2.3%.
[0098] The spinning solution was allowed to stand for 4 hours and then was extruded into
a coagulating bath maintained at 24°C and having a dimethylformamide concentration
of 76% through a spinneret. The coagulated fiber was washed with water, drawn at a
draw ratio of 9 in boiling water and dried in hot air at 80°C to obtain a fiber having
a fineness of 1.5 denier.
[0099] Figure 15 shows an electron microscope photograph (5,000 magnifications) of the longitudinal
section of the fiber cut along the longitudinal axis of the fiber, and Fig. 16 shows
a similar photograph (3,000 magnifications) of the transverse section of the fiber.
[0100] In Fig. 15, the two photographs are linked together at the respective alternate long
and short dash lines (a-a). In Fig. 15, the black portions are spaces, and it is seen
that these spaces are continuous streak-like spaces extending substantially in parallel
to one another along the longitudinal axis of the fiber. These spaces had a length
of at least 60 µm.
[0101] In Fig. 16, black portions are opening, and it is seen that these openings include
substantially circular openings, flat openings, openings having a shape of repeated
bends having acute edges, openings having a large section, openings having a small
section, and various openings having an indeterminate shape are irregularly mingled
with one another.
[0102] The void ratio of the obtained fiber was 37%.
[0103] Then the fiber was treated with a high-pressure water stream jetted under a pressure
of 50 kg/cm² from a nozzle having an orifice diameter of 0.15 mm 10 times, whereby
the fiber was split into finer fibers to form an assembly of fine-denier fibers.
[0104] Figure 17 is an electron microscope photograph (100 magnifications) of the obtained
assembly of fine-denier fibers.
Acrylic synthetic fibrous article
Example 6
[0105] The acrylic synthetic fiber prepared in Example 1 was cut to 15 mm, and 10 parts
of the cut fiber was dispersed in 90 parts of water, and the fiber dispersion was
treated by a paper-making disk refiner having a disk clearance adjusted to 0.1 mm
and beaten so that the freeness was 450 cc.
[0106] Since the fiber of the present invention had voids, the fiber was easily split at
the beating step and fibrils were formed very easily.
[0107] Figure 14 shows an electron microscope photograph (100 magnifications) of the fibrous
article formed by the beating. From this photograph, it is seen that many fine fibrils
branched from the thick fiber (the original acrylic synthetic fiber as the trunk)
were formed on the surface of the trunk, and that the trunk fiber was partially split
in the longitudinal direction and separated into the fibers.
[0108] The aqueous dispersion containing the beaten fiber was passed through an ordinary
paper-making machine and then dried by not air at 85°C to obtain a sheet-like product
having a basis weight of 45 g/m². The obtained sheet-like product was a pliable and
elastic paper-like nonwoven fabric having a soft touch.
[0109] When the sheet-like product was dried after the paper-making operation, no substantial
shrinkage was observed in the longitudinal or transverse direction of the sheet-like
product, and the paper-like sheet product had a very uniform plane.
Friction material
Example 7
[0110] In a Henschel mixer, 50% of the acrylic synthetic fibrous article prepared in Example
6, 25% of a phenolic resin and 25% of calcium carbonate as the filler were sufficiently
mixed, and the mixture was compression-molded in a mold at 150°C under 5 kg/cm² for
10 minutes to form a pad of a disk brake for an automobile.
[0111] When this pad was subjected to the constant-speed friction test according to method
of JIS D-4411, it was found that the friction coefficient at 250°C was 0.45 and the
abrasion loss was 1.48 x 10⁻⁷ cm³/kg·m.
Example 8
[0112] The procedures of Example 7 were repeated in the same manner except that the fiber
was cut into 5 mm and the fiber concentration in the dispersion was changed to 1%,
whereby a brake pad was prepared.
[0113] When the brake pad was tested in the same manner as described in Example 7, it was
found that the friction coefficient was 0.45 and the abrasion loss was 1.46 x 10⁻⁷
cm³/kg·m. Friction materials having the same performances were obtained with a good
reproducibility.
Example 9
[0114] A brake pad was prepared by treating a mixture comprising 40% of the acrylic synthetic
fiber prepared in Example 6, 15% of a glass fiber, 22% of diatomaceous earth and 23%
of a phenolic resin in the same manner as described in Example 7.
[0115] When the obtained brake pad was subjected to the abrasion test, it was found that
the friction coefficient was 0.45 and the abrasion loss was 1.46 x 10⁻⁷ cm³/kg·m.
[0116] As apparent from the foregoing description, the following effects can be obtained
according to the present invention.
[0117] 1. The acrylic synthetic fiber of the present invention can be easily split into
fibers continuous in the longitudinal direction by an external force such as a high-pressure
water stream.
[0118] Furthermore, according to the preparation process of the present invention, by spinning
a spinning solution containing a specific polyalkylene glycol after aging, a fiber
having many voids having an indeterminate shape in the transverse section of the fiber
and being continuous in the longitudinal direction of the fiber can be easily obtained.
[0119] 2. The acrylic synthetic fibrous article of the present invention is suitable for
the production of a nonwoven fabric or paper-like product having a high elasticity
and bulkiness, and the acrylic synthetic fibrous article of the present invention
has characteristics suitable for a resin reinforcer and the like.
[0120] 3. Since the friction material of the present invention is formed by using the fibrous
article comprising fibers having a specific shape and structure, uniform mixing and
close and integral conjugation can be accomplished, and therefore, the friction coefficient
and abrasion resistance are greatly improved in the friction material of the present
invention.