TECHNICAL FIELD
[0001] The present invention relates to a sheet-shaped item and a method for the production
thereof.
BACKGROUND ART
[0002] Sheet-shaped items that consist mainly of nonwoven fabrics of ultrafine fibers and
elastomeric polymers have good features such as high durability and high uniformity
that cannot be matched by natural leathers and have been used in a variety of products
including seat materials and facing materials for vehicles, interior materials, shoes,
and clothing. In particular, for napped sheet-shaped items, which are produced by
polishing etc. of the surface of a sheet-shaped item to raise the ultrafine fibers
on the surface, a variety of materials have been proposed to suit different purposes,
ranging, for example, from those having uniform, even surfaces to those having irregular
surfaces such as the sheet-shaped item disclosed in Patent document 1, which has a
touch like the mellow smoothness of nubuck.
[0003] Of these, disclosed items having uniform, even surfaces include, for example, sheet-shaped
items suitable for polishing purposes having napped surfaces in which nanofiber-level
ultrafine fibers are densely aligned, such as those disclosed in Patent documents
2 and 3.
PRIOR ART DOCUMENTS
PATENT DOCUMENTS
[0004]
Patent document 1: International Publication WO 2016/051711
Patent document 2: Japanese Unexamined Patent Publication (Kokai) No. 2016-47560
Patent document 3: Japanese Unexamined Patent Publication (Kokai) No. 2015-209594
SUMMARY OF INVENTION
PROBLEMS TO BE SOLVED BY THE INVENTION
[0005] By the way, techniques for providing sheet-shaped items having improved gloss to
develop an elegant, refined appearance have been called for in order to allow suede-like
sheet-shaped items having smooth, uniform surfaces as disclosed in Patent documents
2 and 3, rather than sheet-shaped items having nonuniform, irregular surfaces as disclosed
in Patent document 1, to be applied to production of interior materials, shoes, and
clothing. However, the conventional sheet-shaped items having smooth, uniform surfaces
are suited for polishing purposes and therefore, they are inferior in properties such
as light-fastness and gloss required by interior materials, shoes, and clothing and
have to be improved in abrasion resistance to prevent breakage during practical use.
[0006] Thus, the main object of the present invention is to provide a sheet-shaped item
having an elegant appearance, more specifically a sheet-shaped item having dramatically
improved surface features such as densely packed ultrafine fibers, gloss, and abrasion
resistance.
MEANS OF SOLVING THE PROBLEMS
[0007] As a result of intensive studies aiming to meet the above object, the inventors found
that the conventional sheet-shaped items for polishing purposes fail to have adequate
gloss because the average fiber length of ultrafine fibers in the nap layer is so
short that rays of light incident on the sheet-shaped items undergo diffuse reflection
and also found that the quantities of the elastomeric polymers used as binder are
so small that adequate abrasion resistance cannot be achieved. More specifically,
they arrived at the present invention after finding that for the development of a
suede-like artificial leather having a surface with a dense touch and elegant, excellent
gloss, it is important that the surface coverage and fiber length of ultrafine fibers
in the nap layer are in specific ranges and also that the quantity of the elastomeric
polymer contained is in a specific range to ensure abrasion resistance.
[0008] The main object of the present invention is to solve the aforementioned problem.
[0009] The sheet-shaped item according to the present invention is a sheet-shaped item including
ultrafine fiber bundles each containing a plurality of ultrafine fibers of a thermoplastic
resin, the sheet-shaped item having a base material layer and a nap layer, the base
material layer containing a fiber entanglement of the ultrafine fiber bundles, the
nap layer including a nap formed only of the ultrafine fibers and covering at least
one surface of the sheet-shaped item, and all of the requirements (1) to (3) given
below being satisfied:
- (1) the ultrafine fibers have an average single fiber diameter of 0.1 µm or more and
10 µm or less,
- (2) of the ultrafine fibers, those ultrafine fibers contained in the nap layer have
an average fiber length of 250 µm or more and 500 µm or less, and
- (3) in the nap layer, the surface coverage of the ultrafine fibers is 60% or more
and 100% or less.
[0010] In a preferred embodiment of the sheet-shaped item according to the present invention,
the sheet-shaped item consists mainly of the ultrafine fiber bundles and an elastomeric
polymer, and the elastomeric polymer is contained in the interior of the fiber entanglement.
[0011] In a preferred embodiment of the sheet-shaped item according to the present invention,
the ultrafine fiber bundles contain 10 or more and 400 or less ultrafine fibers per
bundle.
[0012] In a preferred embodiment of the sheet-shaped item according to the present invention,
the ultrafine fibers in the nap layer have a CV (coefficient of variation) in the
average fiber length of 30% or less.
[0013] In a preferred embodiment of the sheet-shaped item according to the present invention,
the elastomeric polymer added accounts for more than 0 mass% and 60 mass% or less
relative to the ultrafine fibers.
[0014] The production method for the sheet-shaped item according to the present invention
is a method for producing the aforementioned sheet-shaped item characterized in that
a silicone-based lubricant is added to 0.01 mass% or more and 3.0 mass% or less relative
to the mass of the sheet-shaped item, followed by buffing treatment of the product
surface after drying the sheet-shaped item.
[0015] In a preferred embodiment of the production method for the sheet-shaped item according
to the present invention, the grinding rate in buffing the product surface is 20 g/m
2 or more and 250 g/m
2 or less.
[0016] In a preferred embodiment of the production method for the sheet-shaped item according
to the present invention, the buffing treatment of the product surface is performed
at least twice or more in multiple stages using sandpapers of increasingly finer grits
or of the same grit number.
ADVANTAGEOUS EFFECTS OF THE INVENTION
[0018] According to the present invention, by adjusting the surface coverage of the ultrafine
fibers and the fiber length of ultrafine fibers in the nap layer to the aforementioned
ranges, it is possible to provide a sheet-shaped item that has an elegant appearance,
i.e. dramatically improved ultrafine fiber denseness and gloss on the surface of the
sheet-shaped item and shows high abrasion resistance during practical use, so that
it can be suitably used for such products as interior materials, shoes, and clothing.
BRIEF DESCRIPTION OF THE DRAWINGS
[0019] [Fig. 1] Fig. 1 is a conceptual diagram illustrating the method for measuring the
average fiber length of ultrafine fibers in the nap layer of the sheet-shaped item
according to the present invention.
DESCRIPTION OF PREFERRED EMBODIMENTS
[0020] The sheet-shaped item according to the present invention is a sheet-shaped item including
ultrafine fiber bundles each containing a plurality of ultrafine fibers of a thermoplastic
resin, the sheet-shaped item having a base material layer and a nap layer, the base
material layer containing a fiber entanglement of the ultrafine fiber bundles, the
nap layer including a nap formed only of the ultrafine fibers and covering at least
one surface of the sheet-shaped item, and all of the requirements (1) to (3) given
below being satisfied:
- (1) the ultrafine fibers have an average single fiber diameter of 0.1 µm or more and
10 µm or less,
- (2) of the ultrafine fibers, those ultrafine fibers contained in the nap layer have
an average fiber length of 250 µm or more and 500 µm or less, and
- (3) in the nap layer, the surface coverage of the ultrafine fibers is 60% or more
and 100% or less.
[0021] This structure allows the sheet-shaped item to have a good appearance characterized
by high ultrafine fiber denseness and gloss as described above. The constitution of
the sheet-shaped item according to the present invention is described in detail below.
(Thermoplastic resin)
[0022] The sheet-shaped item according to the present invention contains ultrafine fibers
of a thermoplastic resin to constitute the sheet-shaped item, and examples of the
thermoplastic resin include polyesters such as polyethylene terephthalate, polybutylene
terephthalate, polytrimethylene terephthalate, and polylactic acid, polyamides such
as polyamide 6, polyamide 66, and polyamide 12, polyolefins such as acrylic, polyethylene,
and polypropylene, and melt-spinnable resins such as polyphenylene sulfide (PPS) and
thermoplastic cellulose. In particular, polyesters are preferred from the viewpoint
of strength, dimensional stability, and light resistance. From the viewpoint of environment
protection, fibers produced from recycled materials or plant-derived materials may
be used. Many of the condensation polymers such as polyesters and polyamides that
are used to produce fibers are preferred because they have high melting points and
high heat resistance. Furthermore, ultrafine fibers of different materials may be
used in combination.
[0023] In another preferred embodiment, the thermoplastic resins may contain inorganic particles
such as titanium oxide particles, lubricants, pigments, thermal stabilizers, UV absorbers,
conductive agents, heat storage agents, and antibacterial agents depending on desired
physical properties to be imparted to the sheet-shaped item.
(Ultrafine fibers)
[0024] For the present invention, it is important that the ultrafine fibers have an average
single fiber diameter of 0.1 µm or more and 10 µm or less. Controlling the average
single fiber diameter at 10 µm or less, preferably 8.0 µm or less, and more preferably
7.0 µm or less, serves to obtain a sheet-shaped item having a high-quality surface
that is dense and soft to the touch. When forming a nap layer on the surface, furthermore,
the number of napped fibers per unit area is increased and this leads to a more even
surface.
[0025] On the other hand, controlling the average single fiber diameter of the ultrafine
fibers at 0.1 µm or more, preferably 1.0 µm or more, allows the resulting sheet-shaped
item to have a high monofilament strength and stiffness, and ensures high post-dyeing
color development performance, high fiber dispersibility during raising treatment
performed by, for example, grinding with sandpaper etc., and easy untangling.
[0026] Note that the value of the average single fiber diameter of ultrafine fibers to be
adopted for the present invention should be measured as described below:
- (a) the surface of the sheet-shaped item is photographed by a scanning electron microscope
(SEM),
- (b) 100 ultrafine fibers are selected randomly and the single yarn diameters of the
100 ultrafine fibers are measured, and
- (c) the arithmetic average of the 100 measurements are calculated and rounded off
to one decimal place to give the average single fiber diameter.
[0027] If the ultrafine fibers have modified cross sections as described below, however,
the diameter and the area of the circumscribed circle about the cross section of each
fiber is calculated and the equivalent diameter calculated from the ratio of the actual
area of the cross section of the fiber to the area of the circumscribed circle is
used to determine the average single fiber diameter of these fibers.
[0028] Examples of the cross-sectional shapes of ultrafine fibers used for the present invention
include, in addition to circle, ellipse, flattened shape, polygon such as triangle,
sector, cruciform, and other modified shapes, of which appropriate one is selected
to allow the sheet-shaped item to have desired properties.
[0029] For the present invention, ultrafine fibers used to constitute a fiber entanglement
are in the form of ultrafine fiber bundles each containing a plurality of ultrafine
fibers. Such a ultrafine fiber bundle containing a plurality of ultrafine fibers is
in the form of a so-called bundle in which a plurality of ultrafine fibers are at
least partially in contact with each other. Specifically, they may be joined by, for
example, partial fusion or they may be coagulated.
[0030] For the present invention, it is preferable for an ultrafine fiber bundle to contain
10 fibers per bundle or more and 400 fibers per bundle or less, more preferably 15
fibers per bundle or more and 200 fibers per bundle or less. If the number of fibers
is less than 10 fibers per bundle, the ultrafine fibers will be low in denseness and,
for example, mechanical properties such as abrasion resistance tend to deteriorate.
If the number of fibers is more than 400 fibers per bundle, on the other hand, the
fiber-opening property during the napping step will deteriorate, and the fiber distribution
in the napped surface tends to be low in uniformity.
(Sheet-shaped item)
[0031] The sheet-shaped item according to the present invention consists mainly of a base
material layer and a nap layer. The base material layer is in the form of a fiber
entanglement of the ultrafine fiber bundles. The nap layer includes a nap formed only
of the ultrafine fibers and covers at least one surface of the sheet-shaped item.
[0032] For the present invention, it is important that the average fiber length of ultrafine
fibers in the nap layer is 250 µm or more and 500 µm or less. Here, the present inventors
examined the average fiber length of ultrafine fibers contained in the nap layer to
allow quantitative evaluation of indicators of gloss. Having gloss means having a
surface with a high specular reflectance, which indicates that the nap layer has an
even surface. Accordingly, the surface tends to increase in gloss with an increasing
fiber length of ultrafine fibers. If the average fiber length of ultrafine fibers
contained in the nap layer is 500 µm or more, however, the ultrafine fibers are so
long that they have a rumpled appearance and therefore, it is not preferred. If it
is less than 250 µm, the surface of the nap layer decreases in evenness and light
undergoes diffuse reflection on the surface of the nap layer, leading to insufficient
gloss. Controlling the average fiber length of ultrafine fibers contained in the nap
layer at 250 µm or more and 500 µm or less, preferably 300 µm or more and 400 µm or
less, serves to obtain a sheet-shaped item having a high gloss.
[0033] With reference to the conceptual diagram given in Fig. 1, the average fiber length
(µm) of the ultrafine fibers in the nap layer is determined according to the procedure
described below, and the value thus obtained is adopted.
- (a) Brush the napped fibers against the grain using a lint brush to align them to
each other.
- (b) Photograph a cross section of the sheet-shaped item by SEM at a magnification
of 40.
- (c) In the SEM image taken above, draw a line L connecting the roots of the ultrafine
fibers in the nonwoven fabric or, if fiber bundles are present, connecting the top
ends of the fiber bundles.
- (d) Draw a line U connecting the top ends of the napped fibers that are located at
the front in the observed plane.
- (e) Draw a plurality of thickness-directional parallel lines Pn (P1, P2, P3, ...,
P15) at intervals of 200 µm.
- (f) Measure the length of the L-U segment of each line Pn.
- (g) Select nine different lines Pn, measure the length of the segment of each line,
and calculate their arithmetic average.
- (h) Perform this procedure for 10 positions distributed evenly over the sheet-shaped
item.
- (i) Calculate the arithmetic average of these arithmetic average values and round
it off to one decimal place to represent the average fiber length (µm) of the ultrafine
fibers in the nap layer.
[0034] A sufficiently high degree of gloss can be developed by controlling the CV in the
average fiber length of ultrafine fibers in the nap layer at 30% or less, more preferably
25% or less. The CV in the average fiber length of ultrafine fibers as referred to
herein is determined by measuring the aforementioned average fiber length values,
calculating the arithmetic average and standard deviation, and dividing the standard
deviation by the average to give a quotient expressed in percentage (%). The uniformity
increases as this value decreases.
[0035] For the present invention, it is important that the surface coverage of the ultrafine
fibers in the nap layer is 60% or more and 100% or less. If the surface coverage of
the ultrafine fibers is adjusted to 60% or more, preferably 65% or more, a dense nap
is formed and it is possible to obtain a sheet-shaped item having an elegant surface
appearance and a very soft-to-touch surface and undergoing little loss of fibers.
Regarding the surface coverage of the ultrafine fibers, the napped surface was enlarged
by SEM at an observing magnification of 30 to 70 so that the existence of napped fibers
was visible. The ratio of the combined area of the napped fiber portions to the total
area of 4 mm
2 was calculated by image analysis software and it was adopted as the coverage of napped
fibers. The ratio of the combined area can be calculated by separating the napped
portions and non-napped portions by analyzing the photographed SEM image using ImageJ
image analysis software and binarizing the data with a threshold of 100. When calculating
the coverage of napped fibers, substances that are not napped fibers may be included
as napped fibers in the calculation and may have a large influence on the coverage
of napped fibers. In such a case, the image was modified manually and it is re-calculated
assuming that such a portion is a non-napped portion.
[0036] The aforementioned ImageJ image analysis software can be cited as a good example
of an image analysis system, but the image analysis system to be used here is not
limited to the ImageJ image analysis software as long as it contains image processing
software having the function of calculating the ratio between areas prescribed pixels.
Note that the ImageJ image processing software is a generally used program developed
by the National Institutes of Health, USA. The ImageJ image processing software has
the function of defining a necessary region in a photographed image and performing
pixel analysis.
[0037] It is preferable that the sheet-shaped item according to the present invention has
an elastomeric polymer in addition to ultrafine fiber bundles and that the elastomeric
polymer is contained in the interior of the aforementioned fiber entanglement.
[0038] Specifically, it is preferable that the elastomeric polymer accounts for more than
0 mass% and 60 mass% or less relative to the mass of the ultrafine fibers in the fiber
entanglement. When the elastomeric polymer accounts for more than 0 mass%, preferably
3 mas% or more, relative to the mass of the ultrafine fibers, it is possible to impart
a moderate degree of compressive property to the sheet-shaped item. Regarding the
mass of the elastomeric polymer necessary to achieve high abrasion resistance, it
becomes possible to impart moderate degrees of compressive property and abrasion resistance
to the sheet-shaped item when the elastomeric polymer contained therein accounts for
more than 20 mass%, preferably 25 mass% or more, relative to the mass of the ultrafine
fibers in the fiber entanglement. In the case where the mass of the elastomeric polymer
accounts for more than 60 mass%, the fibers may not have good fiber-opening property
during the napping step and the flexibility of the sheet-shaped item may decrease.
[0039] In the case where the sheet-shaped item is to be used after being dyed, the amount
of the elastomeric polymer may be preferably small because a difference in color tone
can occur between the fibers in the fiber entanglement and the elastomeric polymer
after dyeing. From the viewpoint of environmental consideration, on the other hand,
the inclusion of an excessive amount of an elastomeric polymer is not preferred because
the consumption of organic substances in the production process will increase. In
the case where fibers produced from recyclable materials or plant-derived materials
are adopted, their recycling and disposal become easier to perform as the amount of
the elastomeric polymer decreases.
[0040] The elastomeric polymer may contain, if necessary, pigments such as carbon black,
dye, fungicide, antioxidant, UV absorber, light-resistant agents such as photostabilizer,
flame retardant, penetrant, lubricant, antiblocking agents such as silica and titanium
oxide, water repellent agent, viscosity adjusting agent, surface active agents such
as antistatic agent, antifoam agent, fillers such as cellulose, coagulation modifier,
and inorganic particles of silica, titanium oxide, etc.
[0041] Elastomeric polymers that can be used for the present invention include polyurethane-based
elastomers, polyurea, polyacrylic acid, ethylene-vinyl acetate elastomer, acrylonitrile-butadiene
elastomer, styrene-butadiene elastomer, polyvinyl alcohol, and polyethylene glycol,
of which polyurethane-based elastomers are preferred from the viewpoint of durability
and compressive property. The elastomeric polymer may contain a plurality of elastomeric
polymers.
[0042] The polyurethane-based elastomers that are used particularly preferably for the present
invention include polyurethane and polyurethane-polyurea elastomer.
[0043] For the sheet-shaped item according to the present invention, it is important that
the number of times torn with a Schiefer type abrasion tester is 20 or more per 0.10
mm thickness of the sheet-shaped item as determined by the test specified in ASTM
D4158-08 (2016) "Standard Guide for Abrasion Resistance of Textile Fabrics (Uniform
Abrasion)" (abrasion resistance evaluation method) using a sandpaper of grit number
180 under a load of 2 lbs. A sheet-shaped item having high tear resistance can be
obtained when the number of times torn with a Schiefer type abrasion tester per 0.10
mm thickness of the sheet-shaped item is 20 or more, more preferably 25 or more, and
still more preferably 35 or more.
[0044] The number of times torn with a Schiefer type abrasion tester (times/0.10 mm) was
measured as follows: performing an abrasion test using a Schiefer type abrasion tester
in which the abrasion face (diameter 50 mm) of the nap layer of a sheet-shaped item
is abraded against a sandpaper of grit number 180 used as abradant under a load of
2 lbs, counting the number of times until the abrasion testing machine stops as a
result of tearing of the sheet-shaped item to actuate the limiter, and dividing it
by the thickness of the sheet-shaped item to calculate the number of times torn with
a Schiefer type abrasion tester per 0.10 mm of the thickness (times/0.10 mm).
(Production method for sheet-shaped item)
[0045] The production method for the sheet-shaped item is described in more detail below.
(a) A step for forming a fiber entanglement of ultrafine fiber-generating fibers
[0046] In the production method for the sheet-shaped item according to the present invention,
it is preferable that a fiber entanglement of ultrafine fiber-generating fibers is
formed first. Doing so makes it possible to form a fiber entanglement containing entangled
ultrafine fiber bundles more easily compared with forming a fiber entanglement directly
from ultrafine fibers.
[0047] It is particularly preferable that the aforementioned ultrafine fiber-generating
fibers are islands-in-the-sea fibers. There are different types of islands-in-the-sea
fibers including islands-in-the-sea composite fibers, which are produced using a spinneret
designed for islands-in-the-sea composites in which the two components, i.e. sea component
and island component, are disposed side by side as they are spun into a yarn, and
mixed yarn fibers, which are produced by spinning a combined batch of the two components,
i.e. sea component and island component. Of these islands-in-the-sea fibers, islands-in-the-sea
composite fibers are preferred because ultrafine fibers that are controlled with high
accuracy can be obtained and also because sufficiently long ultrafine fibers can be
obtained to contribute to increased strength of nonwoven fabrics and sheet-shaped
items containing nonwoven fabrics.
[0048] Regarding the ratio between the sea component and the island component in the islands-in-the-sea
composite fibers, it is preferable that the mass ratio of the island fibers to the
islands-in-the-sea composite fibers is preferably 0.2 or more and 0.9 or less, more
preferably 0.2 or more and 0.8 or less. If this mass ratio is 0.2 or more, the sea
component removal ratio can be decreased to ensure improved productivity. If the mass
ratio is 0.9 or less, it is preferable because the fiber-opening property of the island
fibers will improve and the confluence of streams of the island component can be prevented.
[0049] Here, for the aforementioned islands-in-the-sea composite fibers, materials of the
island component that forms ultrafine fibers in the step described later are as listed
above as examples of thermoplastic resin. On the other hand, useful materials of the
sea component include polyethylene, polypropylene, polystyrene, polystyrene copolymers,
polyester copolymers produced through copolymerization of sodium sulfoisophthalic
acid, polyethylene glycol, etc., and polylactic acid. It is preferable to use polystyrene
or a polystyrene copolymer as the sea component in order to realize a high degree
of shrinkage in the densification-shrinkage treatment step described later.
[0050] For the formation of the aforementioned fiber entanglement of ultrafine fiber-generating
fibers, it is preferable to form a nonwoven fabric etc. of ultrafine fiber-generating
fibers. Doing so makes it possible to improve the surface quality of the sheet-shaped
item by raising it in the subsequent step.
[0051] Examples of the aforementioned nonwoven fabric include nonwoven fabrics produced
by a papermaking technique, short fiber nonwoven fabrics produced by forming a laminated
web from short fibers using a carding machine, cross wrapper, or the like, followed
by needle punching, water jet punching, or the like, and long fiber nonwoven fabrics
produced by the spunbond method, melt blowing method, or the like, from which an appropriate
one may be selected so that the intended properties will be developed, but short fiber
nonwoven fabrics are preferred from the viewpoint of texture and quality.
[0052] In the short fiber nonwoven fabrics, the fiber length of ultrafine fiber-generating
fibers is preferably 8 mm or more and 90 mm or less. By adjusting the fiber length
to 8 mm or more, it becomes possible to obtain a sheet-shaped item having high abrasion
resistance attributed to entanglement. By adjusting the the aforementioned fiber length
to 90 mm or less, on the other hand, it becomes possible to obtain a sheet-shaped
item having good compressive property and surface quality. The fiber length is more
preferably 25 mm or more and 90 mm or less. Fibers having a fiber length of less than
8 mm cannot be entangled easily and such fibers tend to come off easily during the
production process of the sheet-shaped item. On the other hand, fibers having a fiber
length of more than 90 mm can be entangled easily, but a nap layer formed thereof
tends to be low in abrasion resistance and inferior in surface quality.
[0053] It is preferable for the needles used for the needle punching treatment to have 1
to 9 needle barbs. By using a needle having one or more needle barbs, it becomes possible
to perform efficient entanglement of the fibers. By using a needle having 9 or less
needle barbs, on the other hand, damage to the fibers can be reduced.
[0054] The number of punches is preferably 1,000 punches/cm
2 or more and 6,000 punches/cm
2 or less. If the number of punches is 1,000 punches/cm
2 or more, high denseness will be realized and highly precise finishing can be achieved.
On the other hand, if the number of punches is 6,000 punches/cm
2 or less, it serves to prevent a decline in processability, damage to fibers, and
decrease in strength.
[0055] When performing the water jet punching treatment, it is preferable to use water in
a columnar form. Specifically, water is preferably squirted under a pressure of 2
MPa to 60 MPa through a nozzle having a diameter of 0.05 mm to 1.0 mm.
[0056] The nonwoven fabric formed of ultrafine fiber-generating fibers treated by needle
punching or water jet punching preferably has an apparent density of 0.15 g/cm
3 or more and 0.45 g/cm
3 or less. An apparent density of 0.15 g/cm
3 or more serves to form a nonwoven fabric having high morphological stability and
dimensional stability and also serves to prevent nonuniform processing and formation
of scratch defects during the polishing step. On the other hand, an apparent density
of 0.45 g/cm
3 or less serves to maintain adequate spaces among fibers to accommodate an elastomeric
polymer.
[0057] From the viewpoint of increasing the denseness, the nonwoven fabric of ultrafine
fiber-generating fibers obtained in this way may be shrunken by either or both of
dry heat and wet heat to achieve a higher density. In addition, the nonwoven fabric
may be compressed in the thickness direction by calendering etc.
(b) A step for integrating a fiber entanglement and a reinforcing layer as a layer
stack
[0058] The sheet-shaped item according to the present invention may have a reinforcing layer
in the interior or on the surface with the aim of improving the strength etc., and
the fiber entanglement formation step may be followed by a step for integrating it
with this reinforcing layer as a layer stack. The aforementioned reinforcing layer
may be in the form of woven fabric, knitted fabric, nonwoven fabric (including paper),
or a film-like material such as plastic film and thin metal sheet.
[0059] In the case where the reinforcing layer is in the form of woven or knitted fabric
of fibers, the yarn used in them is preferably a synthetic fiber such as polyester,
polyamide, polyethylene, polypropylene, or a copolymer thereof. In particular, it
is preferable to adopt synthetic fibers of polyester, polyamide, or a copolymer thereof,
which may be used alone or as a composite or a mixture thereof. The yarn used in the
woven or knitted fabric may be in the form of filament yarn, spun yarn, mixed yarn
of filaments and short fibers, etc. It is preferable for the fibers used in these
yarns to have an average monofilament diameter of about 0.1 µm or more and 20 µm or
less from the viewpoint of texture of the sheet-shaped item.
[0060] When the needle punching technique is used for the stack integration step, the woven
or knitted fabric may be broken by the needles, depending on the type of the yarn
used, and this may cause a decrease in the strength of the sheet-shaped item. As a
means of suppressing this, it is preferable for the woven or knitted fabric to be
formed of a twisted yarn.
[0061] In the case where the yarn used in the woven or knitted fabric is a twisted yarn,
the monofilaments constituting the yarn may not be bound sufficiently and may be easily
caught and damaged by the needles if its twist count is 500 T/m or less. On the other
hand, an excessively large twist count may lead to an excessively stiff yarn, and
this is not preferred because the resulting sheet-shaped item will not have a soft
texture. Accordingly, the twist count of such a twisted yarn is preferably 500 T/m
or more and 4,500 T/m or less, more preferably 1,000 T/m or more and 4,000 T/m or
less, still more preferably 1,500 T/m or more and 4,000 T/m or less, and most preferably
2,000 T/m or more and 4,000 T/m or less.
[0062] Regarding the fineness of the yarn constituting the woven or knitted fabric (total
fineness in the case of multifilament), the metsuke (weight per unit surface area)
of the woven or knitted fabric working as a reinforcing layer and also the metsuke
of the sheet-shaped item will increase when the fineness is 200 dtex or more. As a
result, the sheet-shaped item becomes so high in rigidity that it will be difficult
for the sheet-shaped item to be flexible enough to serve as material for interior
finishing, shoes, and clothing. Accordingly, it is preferably 30 dtex or more and
150 dtex or less, more preferably 50 dtex or more and 130 dtex or less. The monofilaments
constituting the yarn used in the woven or knitted fabric used for the present invention
may have an average monofilament fineness of 1 dtex or more and 10 dtex or less. Also
usable are ultrafine fibers having a monofilament fineness of 0.001 dtex or more and
1 dtex or less.
[0063] The woven or knitted fabric used for the present invention may be a woven or knitted
fabric containing composite fibers in which two or more polymers are combined in the
form of side-by-side type or core-in-sheath type composite fiber (hereinafter occasionally
referred to as "composite fiber of side-by-side type etc."). For example, in the case
of a composite fiber of side-by-side type etc. containing two or more polymers having
different intrinsic viscosities (IV), different inner strains are caused in the two
components as the stress is concentrated on the component having a higher viscosity
during drawing. Because of this inner strain, the higher-viscosity component will
undergo a larger shrinkage due to a difference in the elastic recovery after the drawing
step and a difference in heat shrinkage in the heat treatment step, and the strain
is caused in monofilaments, thereby leading to the formation of coil-shaped crimps.
[0064] Furthermore, examples of the woven fabric that can be used for the present invention
include plain, twill, or satin fabrics, and various other woven fabrics based on the
woven structures thereof. On the other hand, examples of the knitted fabric include
those produced by warp knitting, weft knitting (such as tricot), or lacemaking, and
various other knitted fabrics based on the knitted structures thereof. Of these, woven
fabrics are preferred from the viewpoint of workability, and plain weave fabrics are
particularly preferred from the viewpoint of cost.
(c) A step for adding a water soluble resin
[0065] In the case of the production of a sheet-shaped item including the aforementioned
fiber entanglement that contains an elastomeric polymer in the interior thereof, it
is preferable that the elastomeric polymer is substantially absent inside the fiber
bundles of ultrafine fibers in a nonwoven fabric (fiber entanglement) formed of entangled
fiber bundles of ultrafine fiber so that the surface of the resulting sheet-shaped
item has a dense and uniform fiber distribution. If the elastomeric polymer is present
inside the fiber bundles, the elastomeric polymer must be adhered to the ultrafine
fibers. As a result, surface fibers will be easily torn off during the buffing step
and a nap layer will not be formed easily.
[0066] To produce a structure in which the elastomeric polymer is substantially absent inside
the fiber bundles of ultrafine fibers, a preferred method, for example, is to perform
a step for adding a water soluble resin to a nonwoven fabric of ultrafine fiber-generating
type islands-in-the-sea composite fibers prior to the step for adding an elastomeric
polymer. By incorporating this step for adding a water soluble resin, the surfaces
of the fibers contained in the fiber bundles of ultrafine fibers and those contained
in the woven or knitted fabric will be protected by the water soluble resin, and the
surface regions where the fibers are in direct contact with the elastomeric polymer
will be located discontinuously, instead of continuously, on the surfaces of the fibers
contained in the fiber bundles of ultrafine fibers and those contained in the woven
or knitted fabric, thus serving to maintain an appropriate adhesion area. The time
point of applying the water soluble resin may be either before or after the ultrafine
fiber-generating treatment step, which will be described later, as long as it is before
adding the elastomeric polymer.
[0067] Examples of the water soluble resin include polyvinyl alcohol, polyethylene glycol,
saccharide, and starch. Of these, polyvinyl alcohols having a saponification degree
of 80% or more are preferred.
[0068] A preferred method is adding polyvinyl alcohol to protect most of the circumferential
surface of each fiber, then dissolving and removing the sea component of the islands-in-the-sea
composite fibers using a solvent that cannot dissolve polyvinyl alcohol, subsequently
impregnating them with a solution of an elastomeric polymer, coagulating them in water
or in an aqueous organic solvent solution, and removing the polyvinyl alcohol.
[0069] Here, the amount of polyvinyl alcohol added preferably accounts for 0.1 mass% or
more and 70 mass% or less relative to the mass of the fibers contained in the nonwoven
fabric.
(d) A step for generating ultrafine fibers
[0070] In the case where islands-in-the-sea composite fibers are used as ultrafine fiber-generating
fibers, the step for generating ultrafine fibers from the ultrafine fiber-generating
fibers by, for example, dissolving and removing the sea component from the islands-in-the-sea
composite fibers is carried out either before or after the steps for adding an elastomeric
polymer and a silicone-based lubricant, which will be described later, and either
before or after the buffing step, which will be described later.
[0071] The aforementioned solvent used for dissolving the sea component is an organic solvent
such as toluene and trichloroethylene when the sea component is a polyolefin such
as polyethylene, polystyrene, etc. An aqueous alkali solution of sodium hydroxide
or the like can be used when the sea component is, for instance, polylactic acid or
copolymerized polyester.
[0072] This step can be carried out by immersing the fiber entanglement of ultrafine fiber-generating
fibers in a solvent as listed above, followed by squeezing the liquid.
[0073] Useful instruments for this step include continuous dyeing machine, vibro washer
type sea remover, jet dyeing machine, wins dyeing machine, and jigger dyeing machine.
(e) A step for adding an elastomeric polymer
[0074] In addition, the elastomeric polymer may also be added to the interior of the aforementioned
fiber entanglement or to the interior of the fiber entanglement integrated with a
reinforcing layer to form a stack.
[0075] The polyurethane-based elastomer used for the present invention is a polyurethane-based
elastomer dissolved in a solvent or a water-dispersible polyurethane-based elastomer.
Useful examples include organic solvent-type polyurethane resin (Crisvon (registered
trademark) MP-812 NB, manufactured by DIC Corporation) and water-dispersible polyurethane
resin (Hydran (registered trademark) WLI-602, manufactured by DIC Corporation).
[0076] When the polyurethane-based elastomer used is an organic solvent-type one, it is
preferable to apply the wet coagulation technique that is designed to realize coagulation
by immersion in water. When the polyurethane-based elastomer used is a water-dispersible
polyurethane, it is preferable to apply the steam coagulation technique. When using
a water-dispersible polyurethane-based elastomer, it is preferably one having heat-sensitive
coagulation property. If the water-dispersible polyurethane-based elastomer used does
not have heat-sensitive coagulation property, migration occurs to cause concentration
on the surface layer of the fiber entanglement when the solution of the polyurethane-based
elastomer is subjected to dry coagulation, and the resulting sheet-shaped item containing
the polyurethane-based elastomer tends to harden.
[0077] Here, heat-sensitive coagulation is a property such that as a solution of a polyurethane-based
elastomer is heated, the solution of a polyurethane-based elastomer decreases in flowability
and starts to coagulate after reaching a certain temperature (heat-sensitive coagulation
temperature).
[0078] The heat-sensitive coagulation temperature of a solution of a water-dispersible polyurethane-based
elastomer is preferably 40°C or higher and 90°C or lower. If the heat-sensitive coagulation
temperature is adjusted to 40°C or higher, the solution of the polyurethane-based
elastomer will be highly stable during storage, making it possible to restrict the
sticking of the polyurethane-based elastomer to the machine during operation. On the
other hand, if the heat-sensitive coagulation temperature is adjusted to 90°C or lower,
the migration of the polyurethane-based elastomer in a fiber entanglement can be restrained,
allowing it to be localized in the interior.
[0079] In order to adjust the heat-sensitive coagulation temperature as stated above, a
heat-sensitive coagulation agent may be added as appropriate. Examples of the heat-sensitive
coagulation agent include inorganic salts such as sodium sulfate, magnesium sulfate,
calcium sulfate, and calcium chloride; and radical reaction initiators such as sodium
persulfate, potassium persulfate, ammonium persulfate, azobisisobutyronitrile, and
benzoyl peroxide.
[0080] There are no specific limitations on the wet coagulation temperature when using a
solvent-type polyurethane-based elastomer. In the case of a water-dispersible polyurethane-based
elastomer, furthermore, it is only required to be higher than the heat-sensitive coagulation
temperature of the polyurethane-based elastomer and it is preferably, for example,
40°C or higher and 100°C or lower. By adjusting the temperature of wet coagulation
in hot water to 40°C or higher, more preferably 80°C or higher, the time required
for the coagulation of the polyurethane-based elastomer can be shortened to further
restrain its migration.
[0081] The temperature of steam coagulation is only required to be equal to or higher than
the heat-sensitive coagulation temperature of the water-dispersible polyurethane-based
elastomer, and it is preferably, for example, 40°C or higher and and 200°C or lower.
By adjusting the temperature of steam coagulation to 40°C or higher, more preferably
80°C or higher, the time required for the coagulation of the polyurethane-based elastomer
can be shortened to further restrain its migration. On the other hand, by adjusting
the temperature of steam coagulation to 200°C or lower, more preferably 160°C or lower,
thermal degradation of the polyurethane-based elastomer can be prevented.
[0082] Polyurethane-based elastomers preferred for the present invention include those polyurethane-based
elastomers that can be obtained by reaction of a polymer diol, an organic diisocyanate,
and a chain extender.
[0083] Examples of the above polymer diol include polycarbonate-based diols, polyester-based
diols, polyether-based diols, silcone-based diols, and fluorine-based diols, as well
as copolymers of combinations thereof. In particular, the use of a polycarbonate-based
diol or a polyether-based diol is preferred from the viewpoint of hydrolysis resistance,
and the use of a polycarbonate-based diol is preferred from the viewpoint of abrasion
resistance.
[0084] A polycarbonate-based diol as described above can be produced, for example, through
ester exchange reaction between alkylene glycol and carbonic ester or through reaction
of phosgene or a chloroformic ester with alkylene glycol.
[0085] For example, useful alkylene glycols include linear alkylene glycols such as ethylene
glycol, propylene glycol, 1,4-butane diol, 1,5-pentane diol, 1,6-hexane diol, 1,9-nonane
diol, and 1,10-decane diol; branched alkylene glycols such as neopentyl glycol, 3-methyl-1,5-pentane
diol, 2,4-diethyl-1,5-pentane diol, and 2-methyl-1,8-octane diol; alicyclic diols
such as 1,4-cyclohexane diol; aromatic diols such as bisphenol A; and others such
as glycerin, trimethylol propane, and pentaerythritol. For the present invention,
each of these diols may be either a polycarbonate-based diol that is produced from
a single alkylene glycol or a copolymerized polycarbonate-based diol that is produced
from two or more types of alkylene glycols.
[0086] Examples of such polyester-based diols include polyester diols produced by condensing
one of various low molecular weight polyols and a polybasic acid.
[0087] For example, one or a plurality selected from the following can be used as the low
molecular weight polyols described above: ethylene glycol, 1,2-propylene glycol, 1,3-propylene
glycol, 1,3-butane diol, 1,4-butane diol, 2,2-dimethyl-1,3-propane diol, 1,6-hexane
diol, 3-methyl-1,5-pentane diol, 1,8-octane diol, diethylene glycol, triethylene glycol,
dipropylene glycol, tripropylene glycol, cyclohexane-1,4-diol, and cyclohexane-1,4-dimethanol.
[0088] In addition, an adduct formed by adding one of various alkylene oxides to bisphenol
A is also usable.
[0089] Furthermore, for example, one or a plurality selected from the following can be used
as the polybasic acid described above: succinic acid, maleic acid, adipic acid, glutaric
acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, dodecane dicarboxylic
acid, phthalic acid, isophthalic acid, terephthalic acid, and hexahydroisophthalic
acid.
[0090] Examples of polyether-based diols that can be used for the present invention include
polyethylene glycol, polypropylene glycol, polytetramethylene glycol, and copolymerized
diols that are formed by combining these substances.
[0091] It is preferable for the polymer diol to have a number average molecular weight in
the range of 500 or more and 4,000 or less in the case where the molecular weight
of the polyurethane-based elastomer is constant. If the number average molecular weight
is preferably adjusted to 500 or more, more preferably 1,500 or more, it serves to
prevent the resulting sheet-shaped item from becoming stiff. In addition, a number
average molecular weight of 4,000 or less, preferably 3,000 or less, allows the polyurethane-based
elastomer to maintain strength.
[0092] Examples of organic diisocyanates that can be used for the present invention include
aliphatic diisocyanates such as hexamethylene diisocyanate, dicyclohexylmethane diisocyanate,
isophorone diisocyanate, and xylylene diisocyanate; and aromatic diisocyanates such
as diphenylmethane diisocyanate and tolylene diisocyanate, which may be used in combination.
[0093] Preferred chain extenders include amine-based chain extenders such as ethylene diamine
and methylene bisaniline; and diol-based chain extenders such as ethylene glycol.
In addition, a polyamine that is obtained by reacting polyisocyanate and water can
also be used as a chain extender.
[0094] The polyurethane used for the present invention may be employed in combination with
a crosslinking agent with the aim of improving water resistance, abrasion resistance,
hydrolysis resistance, etc. The crosslinking agent may be either an external crosslinking
agent to be added to the polyurethane-based elastomer as a third component or an internal
crosslinking agent that introduces a reaction point to act as a crosslinking structure
in the polyurethane molecular structure in advance. The use of an internal crosslinking
agent is preferred because crosslinking points can be formed uniformly in the polyurethane
molecular structure, thereby mitigating the decrease in flexibility.
[0095] A compound containing an isocyanate group, an oxazoline group, a carbodiimide group,
an epoxy group, a melamine resin, or a silanol group can be used as such a crosslinking
agent.
(f) A step for adding a silicone-based lubricant
[0096] In the case of performing "(b) A step for adding a water soluble resin", that is,
in the case of producing a sheet-shaped item including the aforementioned fiber entanglement
that contains an elastomeric polymer in the interior thereof, it is preferable that
a silicone-based lubricant is added to the sheet after coagulating the elastomeric
polymer in the fiber entanglement impregnated therewith, so that it account for 0.01
mass% or more and 3.0 mass% or less relative to the mass of the sheet-shaped item.
If added to 0.01 mass% or more, the silicone-based lubricant covers the surface of
the coagulated elastomeric polymer to ensure easy separation between the elastomeric
polymer and ultrafine fibers in the nap layer formation step, which will be described
later, thus serving for efficient dispersion of the ultrafine fibers to facilitate
the formation of a uniform nap layer. On the other hand, if added to more than 3.0
mass%, the silicone acts for increasing slippage, making the formation of a uniform
nap layer difficult. It is more preferable that the silicone-based lubricant accounts
for 0.1 mass% or more and 2.0 mass% or less relative to the mass of the sheet-shaped
item. For example, SM7036EX, manufactured by Toray Coatex Co., Ltd., can serve as
the silicone-based lubricant.
[0097] The available methods for adding a silicone-based lubricant include the method of
impregnating the sheet with a silicone oil solution and the method of adding it by
spraying, of which the method of impregnating the sheet with a silicone oil solution
is preferred to ensure uniform addition.
[0098] It is preferable that the addition of silicone oil is performed immediately after
coagulating the elastomeric polymer. In the case where polyurethane is coagulated
in water, for example, it is preferable that the addition of silicone oil is performed
before the heating for drying moisture.
(g) A step for cutting in half
[0099] In the case where an elastomeric polymer and/or silicone-based lubricant is added
to the fiber entanglement after the ultrafine fiber-developing step, the sheet-shaped
item may be cut in half, or cut into more than two parts, in the thickness direction
after that step. Doing this is preferred because sheet-shaped items can be produced
more efficiently.
(h) A step for forming a nap layer
[0100] The sheet-shaped item according to the present invention has a base material layer
and a nap layer as described above, and the nap layer includes a nap formed only of
the ultrafine fibers and covers at least one surface of the sheet-shaped item.
[0101] Such a nap is generally produced by buffing. The buffing technique referred to herein
is preferably performed by, for example, grinding the sheet surface of an ultrafine
fiber nonwoven fabric using a sandpaper or a roll sander. In particular, the use of
a sandpaper for raising a sheet surface serves to produce a uniform, dense nap.
[0102] As described above, the addition of a silicone-based lubricant to the sheet-shaped
item before the raising step serves to ensure easy separation between the elastomeric
polymer and the ultrafine fibers and develop a glossy, thick nap. It also serves to
protect the ultrafine fiber surface, develop fusion bonding inhibiting effect, and
improve the fiber-opening property of the fibers due to its lubricating effect. The
addition of an antistatic agent before raising the sheet-shaped item is also preferred
because it works to prevent grinding powder generated from the ground sheet-shaped
item from depositing on the sandpaper.
[0103] To allow the napped surface to have a uniform, dense nap with a high coverage of
napped fibers, the surface of the fiber entanglement, such as nonwoven fabric, or
the entity of the fiber entanglement may be treated in a wet state in water or a chemical
solution, but it is preferable that the sheet is in a dry state in the raising step.
If the sheet is in a wet state, the sandpaper will also become wet and suffer breakage
during continuous processing, resulting in a shortened paper life. In addition, drying
will be necessary after the raising step in order to remove water, which is not preferred
because it will lead to a decrease in production efficiency.
[0104] A smaller grinding load is preferred in order to form a uniform nap over the surface
of the sheet. A good method for decreasing the grinding load is to adopt a multi-stage
buffing step that includes at least two or more, preferably three or more, buffing
stages, and furthermore, a highly uniform nap can be produced by using sandpapers
of increasingly finer grits or of the same grit number in the multiple stages. Regarding
the grit number of sandpaper, it is preferable that the sandpaper to be used has a
grit P in the range of 120 to 600 as specified in JIS R6252 (2006) "Polishing paper".
[0105] To allow the ultrafine fibers in the nap layer of a sheet surface to have a CV in
the average fiber length of ultrafine fibers of 30% or less, it is preferable that
the grinding rate in the buffing step is 20 g/m
2 or more and 250 g/m
2 or less, preferably 30 g/m
2 or more and 100 g/m
2 or less. A grinding rate of less than 20 g/m
2 leads to a large variation in the fiber length of ultrafine fibers in the nap layer
and a large proportion of incident light to the napped surface undergoing diffuse
reflection, resulting in an insufficient gloss. In addition, there will occur defects
such as exposed polyurethane in the surface.
(i) Dyeing step
[0106] The sheet-shaped item may be dyed to suit particular needs. A preferred dyeing method
for the sheet-shaped item is the use of a jet dyeing machine because such a machine
serves to knead the sheet-shaped item while dyeing it so that the sheet-shaped item
is softened. The elastomeric polymer may degrade if the dyeing temperature for the
sheet-shaped item is too high, whereas dyeing may not be achieved completely if it
is too low, and therefore, it is preferable to use an appropriate temperature to suit
the type of the fiber. In general, the dyeing temperature is preferably 80°C or higher
and 150°C or lower, more preferably 110°C or higher and 130°C or lower.
[0107] An appropriate dye may be selected to suit the type of the fibers contained in the
sheet-shaped item. For example, a dispersed dye may be used for a polyester-based
fiber, and an acidic dye or a metal-containing dye may be used for a polyamide-based
fiber. Moreover, a combination of these dyes may also be employed.
[0108] It is also preferable that a dyeing auxiliary is used in the step for dyeing the
sheet-shaped item. The use of a dyeing auxiliary can serve to improve the uniformity
and reproducibility of dyeing. In addition, finishing with a softening agent (such
as silicone), an antistatic agent, a water repellent, a flame retardant, a light resistance
agent, an antimicrobial agent, etc. may be performed simultaneously with dyeing in
the same bath or after the dyeing step.
[0109] Here, it is preferable that the sheet-shaped item according to the present invention
is free of partial crimped portions or resin-coated portions in the napped surface.
Here, such partial crimped portions include hot embossed portions. Surface irregularities
can be formed on the surface of the sheet-shaped item by partial crimping or resin
coating, but such treatment can create portions where no nap is present on the surface.
In such nap-free portions, it may be impossible to develop denseness and gloss as
intended by the present invention. However, when the intended uses merely require
partial presence of a good texture, an appropriate treatment as described above may
be conducted as necessary.
[0110] The apparent density of the sheet-shaped item according to the present invention
is preferably 0.100 g/cm
3 or more and 0.900 g/cm
3 or less, more preferably 0.200 g/cm
3 or more and 0.700 g/cm
3 or less. An apparent density of 0.100 g/cm
3 or more allows the sheet-shaped item to have good denseness and mechanical property,
whereas an apparent density of 0.900 g/cm
3 or less prevents its texture from becoming stiff.
[0111] For the present invention, the apparent density of the sheet-shaped item should be
measured as described below:
- (A) Measure the metsuke (weight per unit surface area) of the sheet-shaped item by
the method specified in JIS L 1096 (2010) "Fabric test method for woven fabrics and
knitted fabrics" 8.3.2. Specifically, two 20 cm × 20 cm test pieces sampled and separately
subjected to mass measurement (g), and their arithmetic average was expressed in mass
per m2 (g/m2).
- (B) Measure the thickness of the sheet-shaped item at five equally-spaced measuring
points aligned in the width direction under a 10 kPa load using a thickness gauge
(with a disk diameter of 9 mm or more) graduated at intervals of 0.01 mm, followed
by calculating the arithmetic average.
- (C) Calculate the apparent density by the equation given below from the metsuke and
thickness of the sheet-shaped item determined in (A) and (B) and round off the calculation
to the three decimal places.

[0112] It is preferable for the sheet-shaped item to have a thickness of 0.1 mm or more
and 7 mm or less. A thickness of 0.1 mm or more, preferably 0.3 mm or more, allows
the sheet-shaped item to have high morphological stability and dimensional stability.
On the other hand, a thickness of 7 mm or less, preferably 5 mm or less, allows the
sheet-shaped item to have high moldabililty.
[0113] The sheet-shaped item according to the present invention has an elegant appearance
and very even texture to the touch and also has high abrasion resistance, thus serving
suitably as material for clothes such as shirts, jackets, uppers and trims of various
shoes including casual shoes, sports shoes, men's shoes, and women's shoes, bags,
belts, wallets, and accessories of clothes such as buttons and pockets.
Examples
[0114] The sheet-shaped item according to the present invention will be described in more
detail later with reference to Examples, although the present invention is not limited
to these Examples. First, the evaluation methods and evaluation conditions used in
Examples are described below. For the various properties, measurements were taken
by the methods described above unless otherwise specified.
<Evaluation methods>
(1) Average single fiber diameter
[0115] A scanning electron microscope (VE-7800, manufactured by Keyence Corporation) was
used for measuring the average single fiber diameter.
(2) Intrinsic viscosity (IV) of polymer
[0116] A 0.8 g amount of a specimen polymer was dissolved in 10 mL of o-chlorophenol (hereinafter
occasionally abbreviated as OCP) and the relative viscosity ηr at a temperature of
25°C was determined using an Ostwald viscometer and the equation given below, followed
by calculating the intrinsic viscosity (IV) by the equation given below:
- ηr = η/η0 = (t×d) / (t0×d0)
- intrinsic viscosity (IV) = 0.0242ηr + 0.2634
(Here, η is the viscosity of the polymer solution; η
0 is the viscosity of the OCP; t is drop time (seconds) of the solution; d is the density
(g/cm
3) of the solution; t
0 is the drop time (seconds) of the OCP; and do is the density (g/cm
3) of the OCP.)
(3) Melt flow rate (MFR) of polymer
[0117] The quantity (g) of resin extruded in 10 minutes was measured according to the MFR
measuring method specified in ISO 1133 (2005) "Plastics - determination of the melt
mass-flow rate (MFR) and the melt volume-flow rate (MVR) of thermoplastics". The measuring
run was performed 3 times repeatedly and the arithmetic average of the measurements
was adopted as the MFR (g/10 min).
(4) Average fiber length (µm) of ultrafine fibers in nap layer and CV (%) in average
fiber length of ultrafine fibers
[0118] A VE-7800 scanning electron microscope manufactured by Keyence Corporation was used
for measuring the average fiber length (µm) of ultrafine fibers and CV (%) in average
fiber length of ultrafine fibers.
(5) Surface coverage (%) of ultrafine fibers in nap layer
[0119] AVE-7800 scanning electron microscope manufactured by Keyence Corporation and ImageJ
image processing software were used for measuring the surface coverage (%).
(6) Appearance quality
[0120] The quality of a sample was rated according to the three stage (A, B, and C) criterion
shown below based on visual inspection and sensory evaluation by a total of 20 raters
made up of 10 healthy male adults and 10 healthy female adults. The rating given by
the greatest number of raters was taken as the final rating in external appearance
quality. A sample judged to be acceptable was given the rating of A.
- A: Fibers are dispersed favorably and have high denseness and gloss.
- B: Fibers are dispersed favorably, but have slightly inferior denseness and gloss.
- C: Fibers are very poorly dispersed overall, and have inferior denseness and gloss.
<Abbreviations of chemical substances>
[0121]
- PU: polyurethane
- DMF: N,N-dimethyl formamide
- PET: polyethylene terephthalate
- PVA: polyvinyl alcohol
[Example 1]
[0122] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 36-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 55/45, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0123] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet.
[0124] This sheet was shrunk in hot water at 96°C and then impregnated with a 10% aqueous
solution of PVA, followed by drying in hot air at a temperature of 110°C for 10 minutes
to provide a sheet in which the mass of the PVA accounted for 30 mass% of the mass
of the sheet. This sheet was immersed in trichloroethylene to dissolve and remove
the sea component to provide a sea-free sheet containing ultrafine fibers entangled
in a woven fabric. SEM observation of a cross section of the sea-free sheet showed
that it had an average single fiber diameter of 2.1 µm.
[0125] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 12%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF were removed in hot water and then the sheet was impregnated with
a silicone oil emulsion liquid having a concentration adjusted to 1 mass%, followed
by adding a silicone-based lubricant in such a manner that it accounted for 0.5 mass%
relative to the total of the mass of the fibers and the mass of the polyurethane.
Subsequently, drying was performed in hot air at 110°C for 10 minutes to provide a
sheet in which the mass of the polyurethane accounted for 30 mass% relative to the
mass of the island component of the sheet (total mass of the ultrafine fibers and
the above-mentioned woven or knitted fabric).
[0126] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 100 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 180, 180, and 240
to form a napped surface.
[0127] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.360 g/cm
3.
[0128] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 370 µm, CV in the average fiber length of ultrafine fibers of 15%,
surface coverage of ultrafine fibers in the nap layer of 80%, number of times torn
with a Schiefer type abrasion tester of 65 times/0.10 mm, and appearance quality rating
of A.
[Example 2]
[0129] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 36-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 55/45, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0130] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet.
[0131] This sheet was shrunk in hot water at 96°C and then impregnated with a 10% aqueous
solution of PVA, followed by drying in hot air at a temperature of 110°C for 10 minutes
to provide a sheet in which the mass of the PVA accounted for 25 mass% of the mass
of the sheet. This sheet was immersed in trichloroethylene to dissolve and remove
the sea component to provide a sea-free sheet containing ultrafine fibers entangled
in a woven fabric. SEM observation of a cross section of the sea-free sheet showed
that it had an average single fiber diameter of 2.1 µm.
[0132] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 10%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF were removed in hot water and then the sheet was impregnated with
a silicone oil emulsion liquid having a concentration adjusted to 1 mass%, followed
by adding a silicone-based lubricant in such a manner that it accounted for 0.2 mass%
relative to the total of the mass of the fibers and the mass of the polyurethane.
Subsequently, drying was performed in hot air at 110°C for 10 minutes to provide a
sheet in which the mass of the polyurethane accounted for 25 mass% relative to the
mass of the island component of the sheet (total mass of the ultrafine fibers and
the above-mentioned woven or knitted fabric).
[0133] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 60 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 180, 180, and 240
to form a napped surface.
[0134] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.360 g/cm
3.
[0135] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 260 µm, CV in the average fiber length of ultrafine fibers of 20%,
surface coverage of ultrafine fibers in the nap layer of 73%, number of times torn
with a Schiefer type abrasion tester of 40 times/0.10 mm, and appearance quality rating
of A.
[Example 3]
[0136] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 36-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 55/45, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0137] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet.
[0138] This sheet was shrunk in hot water at 96°C and then impregnated with a 15% aqueous
solution of PVA, followed by drying in hot air at a temperature of 110°C for 10 minutes
to provide a sheet in which the mass of the PVA accounted for 40 mass% of the mass
of the sheet. This sheet was immersed in trichloroethylene to dissolve and remove
the sea component to provide a sea-free sheet containing ultrafine fibers entangled
in a woven fabric. SEM observation of a cross section of the sea-free sheet showed
that it had an average single fiber diameter of 2.1 µm.
[0139] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate
and polyester-based polyurethane in DMF with a solid content adjusted to 9.5%, followed
by coagulating the polyurethane in an aqueous solution with a DMF concentration of
30%. Subsequently, the PVA and DMF were removed in hot water and then the sheet was
impregnated with a silicone oil emulsion liquid having a concentration adjusted to
1 mass%, followed by adding a silicone-based lubricant in such a manner that it accounted
for 0.6 mass% relative to the total of the mass of the fibers and the mass of the
polyurethane. Subsequently, drying was performed in hot air at 110°C for 10 minutes
to provide a sheet in which the mass of the polyurethane accounted for 23 mass% relative
to the mass of the island component of the sheet (total mass of the ultrafine fibers
and the above-mentioned woven or knitted fabric).
[0140] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 70 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 180, 180, and 240
to form a napped surface.
[0141] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.360 g/cm
3.
[0142] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 400 µm, CV in the average fiber length of ultrafine fibers of 10%,
surface coverage of ultrafine fibers in the nap layer of 90%, number of times torn
with a Schiefer type abrasion tester of 45 times/0.10 mm, and appearance quality rating
of A.
[Example 4]
[0143] Nylon 6 having an MFR of 58.3 g/10 minutes, used as island component, and polystyrene
copolymerized with 22 mol% 2-ethylhexyl acrylate (Co-PSt) having an MFR of 300 g/10
minutes, used as sea component, were melt-spun through a spinneret designed for 36-island
islands-in-the-sea composite fiber with an island/sea mass ratio of 30/70, followed
by drawing, crimping, and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea
composite fiber having a monofilament fineness of 24 µm.
[0144] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 85°C and then impregnated
with a 15% aqueous solution of PVA, followed by drying in hot air at a temperature
of 110°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 50 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 1.0 µm.
[0145] This sea-free sheet containing ultrafine fibers was immersed in a solution of polyether
and polyester-based polyurethane in DMF with a solid content adjusted to 9%, followed
by coagulating the polyurethane in an aqueous solution with a DMF concentration of
30%. Subsequently, the PVA and DMF were removed in hot water and then the sheet was
impregnated with a silicone oil emulsion liquid having a concentration adjusted to
0.5 mass%, followed by adding a silicone-based lubricant in such a manner that it
accounted for 0.1 mass% relative to the total of the mass of the fibers and the mass
of the polyurethane. Subsequently, drying was performed in hot air at 100°C for 10
minutes to provide a sheet in which the mass of the polyurethane accounted for 20
mass% relative to the mass of the island component of the sheet (total mass of the
ultrafine fibers and the above-mentioned woven or knitted fabric).
[0146] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 30 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 150, 180, and 180
to form a napped surface.
[0147] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
85°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.300 g/cm
3.
[0148] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 280 µm, CV in the average fiber length of ultrafine fibers of 28%,
surface coverage of ultrafine fibers in the nap layer of 62%, number of times torn
with a Schiefer type abrasion tester of 20 times/0.10 mm, and appearance quality rating
of A.
[Example 5]
[0149] Nylon 6 having an MFR of 58.3 g/10 minutes, used as island component, and polystyrene
copolymerized with 22 mol% 2-ethylhexyl acrylate (Co-PSt) having an MFR of 300 g/10
minutes, used as sea component, were melt-spun through a spinneret designed for 280-island
islands-in-the-sea composite fiber with an island/sea mass ratio of 30/70, followed
by drawing, crimping, and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea
composite fiber having a monofilament fineness of 24 µm.
[0150] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 85°C and then impregnated
with a 12% aqueous solution of PVA, followed by drying in hot air at a temperature
of 100°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 40 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 1.0 µm.
[0151] This sea-free sheet containing ultrafine fibers was immersed in a solution of polyether
and polyester-based polyurethane in DMF with a solid content adjusted to 10%, followed
by coagulating the polyurethane in an aqueous solution with a DMF concentration of
30%. Subsequently, the PVA and DMF were removed in hot water and then the sheet was
impregnated with a silicone oil emulsion liquid having a concentration adjusted to
0.1 mass%, followed by adding a silicone-based lubricant in such a manner that it
accounted for 0.01 mass% relative to the total of the mass of the fibers and the mass
of the polyurethane. Subsequently, drying was performed in hot air at 110°C for 10
minutes to provide a sheet in which the mass of the polyurethane accounted for 35
mass% relative to the mass of the island component of the sheet (total mass of the
ultrafine fibers and the above-mentioned woven or knitted fabric).
[0152] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 40 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 150, 180, and 180
to form a napped surface.
[0153] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
85°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.300 g/cm
3.
[0154] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 260 µm, CV in the average fiber length of ultrafine fibers of 10%,
surface coverage of ultrafine fibers in the nap layer of 70%, number of times torn
with a Schiefer type abrasion tester of 30 times/0.10 mm, and appearance quality rating
of A.
[Example 6]
[0155] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 50-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 80/20, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0156] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 96°C and then impregnated
with a 5% aqueous solution of PVA, followed by drying in hot air at a temperature
of 110°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 30 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 7.0 µm.
[0157] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 11%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF were removed in hot water and then the sheet was impregnated with
a silicone oil emulsion liquid having a concentration adjusted to 5 mass%, followed
by adding a silicone-based lubricant in such a manner that it accounted for 2.0 mass%
relative to the total of the mass of the fibers and the mass of the polyurethane.
Subsequently, drying was performed in hot air at 110°C for 10 minutes to provide a
sheet in which the mass of the polyurethane accounted for 40 mass% relative to the
mass of the island component of the sheet (total mass of the ultrafine fibers and
the above-mentioned woven or knitted fabric).
[0158] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 160 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 120, 150, and 180
to form a napped surface.
[0159] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 1.0 mm and an apparent density of 0.400 g/cm
3.
[0160] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 350 µm, CV in the average fiber length of ultrafine fibers of 25%,
surface coverage of ultrafine fibers in the nap layer of 65%, number of times torn
with a Schiefer type abrasion tester of 80 times/0.10 mm, and appearance quality rating
of A.
[Example 7]
[0161] Nylon 6 having an MFR of 58.3 g/10 minutes, used as island component, and polystyrene
copolymerized with 22 mol% 2-ethylhexyl acrylate (Co-PSt) having an MFR of 300 g/10
minutes, used as sea component, were melt-spun through a spinneret designed for 100-island
islands-in-the-sea composite fiber with an island/sea mass ratio of 30/70, followed
by drawing, crimping, and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea
composite fiber having a monofilament fineness of 24 µm.
[0162] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 85°C and then impregnated
with a 20% aqueous solution of PVA, followed by drying in hot air at a temperature
of 100°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 60 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 1.0 µm.
[0163] This sea-free sheet containing ultrafine fibers was immersed in a solution of polyether
and polyester-based polyurethane in DMF with a solid content adjusted to 9%, followed
by coagulating the polyurethane in an aqueous solution with a DMF concentration of
30%. Subsequently, the PVA and DMF were removed in hot water and then the sheet was
impregnated with a silicone oil emulsion liquid having a concentration adjusted to
3 mass%, followed by adding a silicone-based lubricant in such a manner that it accounted
for 1.0 mass% relative to the total of the mass of the fibers and the mass of the
polyurethane. Subsequently, drying was performed in hot air at 110°C for 10 minutes
to provide a sheet in which the mass of the polyurethane accounted for 5 mass% relative
to the mass of the island component of the sheet (total mass of the ultrafine fibers
and the above-mentioned woven or knitted fabric).
[0164] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 50 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 150 and 180 to form
a napped surface.
[0165] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
85°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.300 g/cm
3.
[0166] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 400 µm, CV in the average fiber length of ultrafine fibers of 25%,
surface coverage of ultrafine fibers in the nap layer of 99%, number of times torn
with a Schiefer type abrasion tester of 10 times/0.10 mm, and appearance quality rating
of A.
[Example 8]
[0167] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 36-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 55/45, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0168] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet.
[0169] This sheet was shrunk in hot water at 96°C and then immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 2.1 µm.
[0170] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 20 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 180, 180, and 240
to form a napped surface.
[0171] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.360 g/cm
3.
[0172] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 250 µm, CV in the average fiber length of ultrafine fibers of 29%,
surface coverage of ultrafine fibers in the nap layer of 62%, number of times torn
with a Schiefer type abrasion tester of 7 times/0.10 mm, and appearance quality rating
of A.
[Example 9]
[0173] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 16-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 80/20, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0174] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2, followed by combining the web with a plain weave fabric (in which a multifilament
(84 dtex, 72 filaments) with a twist count of 2,500 T/m formed of a single fiber formed
of single component with an intrinsic viscosity (IV) of 0.65 is used as warp and weft
with a weaving density of 97 ends/2.54 cm × 76 picks/2.54 cm) to provide a sheet.
This sheet was shrunk in hot water at 96°C and then impregnated with a 5% aqueous
solution of PVA, followed by drying in hot air at a temperature of 110°C for 10 minutes
to provide a sheet in which the mass of the PVA accounted for 20 mass% of the mass
of the sheet. This sheet was immersed in trichloroethylene to dissolve and remove
the sea component to provide a sea-free sheet containing ultrafine fibers entangled
in a woven fabric. SEM observation of a cross section of the sea-free sheet showed
that it had an average single fiber diameter of 4.4 µm.
[0175] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 11%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF were removed in hot water and then the sheet was impregnated with
a silicone oil emulsion liquid having a concentration adjusted to 1 mass%, followed
by adding a silicone-based lubricant in such a manner that it accounted for 0.2 mass%
relative to the total of the mass of the fibers and the mass of the polyurethane.
Subsequently, drying was performed in hot air at 110°C for 10 minutes to provide a
sheet in which the mass of the polyurethane accounted for 27 mass% relative to the
mass of the island component of the sheet (total mass of the ultrafine fibers and
the above-mentioned woven or knitted fabric).
[0176] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 60 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 120, 150, and 180
to form a napped surface.
[0177] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 1.0 mm and an apparent density of 0.400 g/cm
3.
[0178] The resulting sheet-shaped item had an average fiber length of ultrafine fibers
in the nap layer of 450 µm, CV in the average fiber length of ultrafine fibers of
20%, surface coverage of ultrafine fibers in the nap layer of 80%, number of times
torn with a Schiefer type abrasion tester of 55 times/0.10 mm and appearance quality
rating of A.
[Example 10]
[0179] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 16-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 80/20, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0180] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2, followed by combining the web with a plain weave fabric (in which a multifilament
(84 dtex, 72 filaments) with a twist count of 2,500 T/m formed of a single fiber formed
of single component with an intrinsic viscosity (IV) of 0.65 is used as warp and weft
with a weaving density of 97 ends/2.54 cm × 76 picks/2.54 cm) to provide a sheet.
This sheet was shrunk in hot water at 96°C and then impregnated with a 5% aqueous
solution of PVA, followed by drying in hot air at a temperature of 110°C for 10 minutes
to provide a sheet in which the mass of the PVA accounted for 20 mass% of the mass
of the sheet. This sheet was immersed in trichloroethylene to dissolve and remove
the sea component to provide a sea-free sheet containing ultrafine fibers entangled
in a woven fabric. SEM observation of a cross section of the sea-free sheet showed
that it had an average single fiber diameter of 4.4 µm.
[0181] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 11%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF were removed in hot water and then the sheet was impregnated with
a silicone oil emulsion liquid having a concentration adjusted to 1 mass%, followed
by adding a silicone-based lubricant in such a manner that it accounted for 0.05 mass%
relative to the total of the mass of the fibers and the mass of the polyurethane.
Subsequently, drying was performed in hot air at 110°C for 10 minutes to provide a
sheet in which the mass of the polyurethane accounted for 27 mass% relative to the
mass of the island component of the sheet (total mass of the ultrafine fibers and
the above-mentioned woven or knitted fabric).
[0182] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 80 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 120, 120, and 150
to form a napped surface.
[0183] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 1.0 mm and an apparent density of 0.400 g/cm
3.
[0184] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 300 µm, CV in the average fiber length of ultrafine fibers of 28%,
surface coverage of ultrafine fibers in the nap layer of 63%, number of times torn
with a Schiefer type abrasion tester of 50 times/0.10 mm, and appearance quality rating
of A.
[Comparative example 1]
[0185] Nylon 6 having an MFR of 58.3 g/10 minutes, used as island component, and polystyrene
copolymerized with 22 mol% 2-ethylhexyl acrylate (Co-PSt) having an MFR of 300 g/10
minutes, used as sea component, were melt-spun through a spinneret designed for 500-island
islands-in-the-sea composite fiber with an island/sea mass ratio of 30/70, followed
by drawing, crimping, and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea
composite fiber having a monofilament fineness of 24 µm.
[0186] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 85°C and then impregnated
with a 12% aqueous solution of PVA, followed by drying in hot air at a temperature
of 100°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 45 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 0.5 µm.
[0187] This sea-free sheet containing ultrafine fibers was immersed in a solution of polyether
and polyester-based polyurethane in DMF with a solid content adjusted to 9%, followed
by coagulating the polyurethane in an aqueous solution with a DMF concentration of
30%. Subsequently, the PVA and DMF were removed in hot water and then the sheet was
impregnated with a silicone oil emulsion liquid having a concentration adjusted to
1.0 mass%, followed by adding a silicone-based lubricant in such a manner that it
accounted for 0.2 mass% relative to the total of the mass of the fibers and the mass
of the polyurethane. Subsequently, drying was performed in hot air at 110°C for 10
minutes to provide a sheet in which the mass of the polyurethane accounted for 25
mass% relative to the mass of the island component of the sheet (total mass of the
ultrafine fibers and the above-mentioned woven or knitted fabric).
[0188] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 15 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 150 and 180 to form
a napped surface.
[0189] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
85°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.300 g/cm
3.
[0190] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 200 µm, CV in the average fiber length of ultrafine fibers of 35%,
surface coverage of ultrafine fibers in the nap layer of 70%, number of times torn
with a Schiefer type abrasion tester of 23 times/0.10 mm, and appearance quality rating
of B.
[Comparative example 2]
[0191] Nylon 6 having an MFR of 58.3 g/10 minutes, used as island component, and polystyrene
copolymerized with 22 mol% 2-ethylhexyl acrylate (Co-PSt) having an MFR of 300 g/10
minutes, used as sea component, were melt-spun through a spinneret designed for 300-island
islands-in-the-sea composite fiber with an island/sea mass ratio of 30/70, followed
by drawing, crimping, and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea
composite fiber having a monofilament fineness of 24 µm.
[0192] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 85°C and then impregnated
with a 12% aqueous solution of PVA, followed by drying in hot air at a temperature
of 100°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 40 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 1.0 µm.
[0193] This sea-free sheet containing ultrafine fibers was immersed in a solution of polyether
and polyester-based polyurethane in DMF with a solid content adjusted to 9%, followed
by coagulating the polyurethane in an aqueous solution with a DMF concentration of
30%. Subsequently, the PVA and DMF were removed in hot water and then drying was performed
in hot air at 110°C for 10 minutes to provide a sheet in which the mass of the polyurethane
accounted for 30 mass% of the mass of the island component of the sheet (total mass
of the ultrafine fibers and the above-mentioned woven or knitted fabric).
[0194] Then, the resulting sheet was cut in half in the thickness direction and the half-cut
sheet was infiltrated with water so that the mass of the sheet containing water reached
200% of its dry mass, followed by squeezing the liquid. Then, the cut surface was
ground at a rate of 15 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 150, 180, and 180
to form a napped surface.
[0195] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
85°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.300 g/cm
3.
[0196] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 150 µm, CV in the average fiber length of ultrafine fibers of 40%,
surface coverage of ultrafine fibers in the nap layer of 80%, number of times torn
with a Schiefer type abrasion tester of 25 times/0.10 mm, and appearance quality rating
of C.
[Comparative example 3]
[0197] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 25-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 80/20, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0198] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 96°C and then impregnated
with a 5% aqueous solution of PVA, followed by drying in hot air at a temperature
of 110°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 35 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 5.0 µm.
[0199] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 10%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF was removed using hot water. Subsequently, drying was performed in
hot air at 110°C for 10 minutes to provide a sheet in which the mass of the polyurethane
accounted for 15 mass% relative to the mass of the island component of the sheet (total
mass of the ultrafine fibers and the above-mentioned woven or knitted fabric).
[0200] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 15 g/m
2 using an endless sandpaper belt having sandpaper grit number of 120 to form a napped
surface.
[0201] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 1.0 mm and an apparent density of 0.400 g/cm
3. Subsequently, the raised surface of the dyed fiber base material was embossed using
an embossing roll with a design simulating a shallow contraction creases along pores
in natural leather. The embossing roll had a protruding portion with a width of 220
µm and a pressing depth of 750 µm, and the protruding portion accounted for 13% of
the total area. Embossing was performed under the conditions of an embossing roll
surface temperature of 140°C, a pressure of 0.3 MPa, and an embossing roll speed of
1.5 m/min to produce a sheet-shaped item.
[0202] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 300 µm, CV in the average fiber length of ultrafine fibers of 40%,
surface coverage of ultrafine fibers in the nap layer of 50%, number of times torn
with a Schiefer type abrasion tester of 16 times/0.10 mm, and appearance quality rating
of C.
[Comparative example 4]
[0203] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 25-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 55/45, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0204] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 96°C and then impregnated
with a 10% aqueous solution of PVA, followed by drying in hot air at a temperature
of 110°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 30 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 2.0 µm.
[0205] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 10%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF were removed in hot water and then the sheet was impregnated with
a silicone oil emulsion liquid having a concentration adjusted to 10 mass%, followed
by adding a silicone-based lubricant in such a manner that it accounted for 6.0 mass%
relative to the total of the mass of the fibers and the mass of the polyurethane.
Subsequently, drying was performed in hot air at 110°C for 10 minutes to provide a
sheet in which the mass of the polyurethane accounted for 20 mass% relative to the
mass of the island component of the sheet (total mass of the ultrafine fibers and
the above-mentioned woven or knitted fabric).
[0206] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 20 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 180 and 180 to form
a napped surface.
[0207] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.360 g/cm
3.
[0208] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 600 µm, CV in the average fiber length of ultrafine fibers of 40%,
surface coverage of ultrafine fibers in the nap layer of 45%, number of times torn
with a Schiefer type abrasion tester of 28 times/0.10 mm, and appearance quality rating
of C.
[Comparative example 5]
[0209] Polyethylene terephthalate (PET) having an intrinsic viscosity (IV) of 0.718, used
as island component, and polystyrene having an MFR of 18 g/10 minutes, used as sea
component, were melt-spun through a spinneret designed for 25-island islands-in-the-sea
composite fiber with an island/sea mass ratio of 55/45, followed by drawing, crimping,
and subsequent cutting to 51 mm to prepare raw stock of islands-in-the-sea composite
fiber having a monofilament fineness of 3.1 dtex.
[0210] This raw stock of islands-in-the-sea composite fiber was processed by carding and
cross-wrapping to provide a laminated web, which was then needle-punched at a punch
density of 600 punches/cm
2 and further needle-punched at a punch density of 2,900 punches/cm
2 to produce a sheet. This sheet was shrunk in hot water at 96°C and then impregnated
with a 3% aqueous solution of PVA, followed by drying in hot air at a temperature
of 110°C for 10 minutes to provide a sheet in which the mass of the PVA accounted
for 10 mass% of the mass of the sheet. This sheet was immersed in trichloroethylene
to dissolve and remove the sea component to provide a sea-free sheet containing ultrafine
fibers entangled in a woven fabric. SEM observation of a cross section of the sea-free
sheet showed that it had an average single fiber diameter of 2.0 µm.
[0211] This sea-free sheet containing ultrafine fibers was immersed in a solution of polycarbonate-based
polyurethane in DMF with a solid content adjusted to 10%, followed by coagulating
the polyurethane in an aqueous solution with a DMF concentration of 30%. Subsequently,
the PVA and DMF were removed in hot water and then the sheet was impregnated with
a silicone oil emulsion liquid having a concentration adjusted to 5 mass%, followed
by adding a silicone-based lubricant in such a manner that it accounted for 2.0 mass%
relative to the total of the mass of the fibers and the mass of the polyurethane.
Subsequently, drying was performed in hot air at 110°C for 10 minutes to provide a
sheet in which the mass of the polyurethane accounted for 65 mass% relative to the
mass of the island component of the sheet (total mass of the ultrafine fibers and
the above-mentioned woven or knitted fabric).
[0212] Then, the resulting sheet was cut in half in the thickness direction and the cut
surface of the half-cut sheet was ground at a rate of 20 g/m
2 using endless sandpaper belts having sandpaper grit numbers of 150, 180, 240, 320,
and 600 to form a napped surface.
[0213] The sheet thus obtained was dyed using a jet dyeing machine under the condition of
110°C and then dried by a drying machine to produce a sheet-shaped item having a thickness
of 0.5 mm and an apparent density of 0.360 g/cm
3.
[0214] The resulting sheet-shaped item had an average fiber length of ultrafine fibers in
the nap layer of 330 µm, CV in the average fiber length of ultrafine fibers of 40%,
surface coverage of ultrafine fibers in the nap layer of 45%, number of times torn
with a Schiefer type abrasion tester of 100 times/0.10 mm, and appearance quality
rating of C.
[Table 1]
|
Example 1 |
Example 2 |
Example 3 |
Example 4 |
Example 5 |
Example 6 |
Example 7 |
Example 8 |
Example 9 |
Example 10 |
Number of ultrafine fiber (per bundle) |
36 |
36 |
36 |
36 |
280 |
50 |
100 |
36 |
16 |
16 |
Average single fiber diameter (µm) |
2.1 |
2.1 |
2.1 |
1 |
1 |
7 |
1 |
2.1 |
4.4 |
4.4 |
Elastomeric polymer diol |
poly carbonate-based |
poly carbonate-based |
polycarbonate/ polyester-based |
polyether/ polyester-based |
polyether/ polyester-based |
poly carbonate-based |
Polyether/ polyester-based |
- |
poly carbonate-based |
poly carbonate-based |
Elastomeric polymer added (%) |
30 |
25 |
23 |
20 |
35 |
40 |
5 |
0 |
27 |
27 |
Average fiber length in nap laver (um) |
370 |
260 |
400 |
280 |
260 |
350 |
400 |
250 |
450 |
300 |
CV in average fiber length in nap layer (%) |
15 |
20 |
10 |
28 |
10 |
25 |
25 |
29 |
20 |
28 |
Napped surface coverage of ultrafine fibers in nap layer (%) |
80 |
73 |
90 |
62 |
70 |
65 |
99 |
62 |
80 |
63 |
Existence/absence of silicone-based lubricant |
existent |
existent |
existent |
existent |
existent |
existent |
existent |
absent |
existent |
existent |
Amount of silicone-based lubricant added (%) |
0.5 |
0.2 |
0.6 |
0.1 |
0.01 |
2.0 |
1.0 |
0 |
0.2 |
0.05 |
Product surface ground rate in buffing step (g/m2) |
100 |
60 |
70 |
30 |
40 |
160 |
50 |
20 |
60 |
80 |
Repetitions of buffing |
3 |
3 |
2 |
3 |
3 |
3 |
2 |
3 |
3 |
3 |
Exposed polyurethane in surface |
absent |
absent |
absent |
absent |
absent |
absent |
absent |
absent |
absent |
absent |
Number of times torn with Schiefer type abrasion tester (per 0.10 mm) |
65 |
40 |
45 |
20 |
30 |
80 |
10 |
7 |
55 |
50 |
Appearance |
A |
A |
A |
A |
A |
A |
A |
A |
A |
A |
[Table 2]
|
Comparative example 1 |
Comparative example 2 |
Comparative example 3 |
Comparative example 4 |
Comparative example 5 |
Number of ultrafine fibers (per bundle) |
500 |
300 |
25 |
25 |
25 |
Average single fiber diameter (µm) |
0.5 |
1 |
5 |
2 |
2 |
Elastomeric polymer diol |
polyether/ polyester-based |
polyether/ polyester-based |
polycarbonate-based |
poly carbonate-based |
poly carbonate-based |
Elastomeric polymer added (%) |
25 |
30 |
15 |
20 |
65 |
Average fiber length in nap layer (µm) |
200 |
150 |
300 |
600 |
330 |
CV in average fiber length in nap layer (%) |
35 |
40 |
40 |
40 |
40 |
Napped surface coverage of ultrafine fibers in nap layer (%) |
70 |
80 |
50 |
45 |
45 |
Existence/absence of silicone- based lubricant |
existent |
absent |
absent |
existent |
existent |
Amount of silicone-based lubricant added (%) |
0.2 |
0 |
0 |
6.0 |
2.0 |
Product surface ground rate in buffing step (g/m2) |
15 |
15 |
15 |
20 |
20 |
Repetitions of buffing |
2 |
3 |
1 |
2 |
5 |
Exposed polyurethane in surface |
existent |
existent |
existent |
absent |
existent |
Number of times torn with Schiefer type abrasion tester (per 0.10 mm) |
23 |
25 |
16 |
28 |
100 |
Appearance |
B |
C |
C |
C |
C |
INDUSTRIAL APPLICABILITY
[0215] The sheet-shaped item according to the present invention has an elegant appearance
and very even texture to the touch and also shows high moldability and accordingly,
it can be suitably used mainly as interior materials with highly elegant appearance
of epidermis materials for furniture, chairs and walls, and also seats, ceilings,
interiors, etc. of vehicles including automobiles, trains, and aircraft; shirts, jackets,
uppers and trims, etc. of casual shoes, sports shoes, men's shoes, women's shoes,
etc., bags, belts, wallets, etc., and clothing materials used as parts thereof; and
industrial materials such as wiping cloth, filters, and CD curtains.