BACKGROUND OF THE INVENTION
Field of the Invention
[0001] The present invention relates to a method for manufacturing bulky nonwoven fabrics.
More specifically, this invention is concerned with a method for manufacturing bulky
nonwoven fabrics suitable for surfacings for disposable diapers, interlinings or waddings
for clothing and so on.
Statement of the Prior Art
[0002] In recent years, there have been developed spun bonding techniques for making nonwoven
fabrics by drawing and stretching a fiber bundle comprising a plurality of single
fibers spun out of a spinneret with a high-speed stream of air and depositing it on
a net conveyor to form a web, followed by heat treatments, some of which have been
carried out on an industrial scale. According to one of the spun bonding techniques
known for obtaining bulky nonwoven fabrics (Japanese Patent Application Laid-Open
No. 1471/1973), for example, latently crimpable composite fibers are deposited on
a net conveyor to form a web, which is then heat-treated into a crimped nonwoven fabric.
According to another spun bonding technique (Japanese Patent Application Laid-Open
No. 282350/1988), apparently crimping composite fibers are formed into a fiber bundle,
which is then deposited on a net conveyor to form a web to be processed into an nonwoven
fabric.
[0003] When a nonwoven fabric having little unevenness of weight per unit area referring
as unit-weight hereafter is to be obtained by such spun bonding techniques, it is
then required to prevent the once deposited web from being disturbed or blown off
by a high-speed stream of air reflected off the upper face of the net conveyor. To
this end, an exhaust device is provided back side of a region of the net conveyor
against which the web is to be blown, thereby passing and sucking a substantially
whole portion of the air stream through the net conveyor.
[0004] According to the conventional spun bonding techniques, the web is pressed against
the net conveyor by the force of a high-speed air stream blown against it and the
suction force of the exhaust device, as mentioned above. In consequence, the web is
delivered to the next heat treatment step while it remains firmly engaged with the
net conveyor. Accordingly, when a bulky nonwoven fabric is to be made with latenly
crimpable fibers, any free development of crimps is inhibited even though the fibers
are heat-treated so as to develop crimps, since they are firmly engaged and entangled
in the net. This tends to offer such disadvantages as insufficient bulking, occurrence
of unevenness of shrinkage and density on the web, and transfer of the network pattern
of the net conveyor to the back side of the nonwoven fabric. Such disadvantages are
liable to occur particularly in manufacturing bulky nonwoven fabrics of low unit-weight,
which are used as the surfacings for disposable diapers, etc., and moreover have an
influence upon commercial value. It is thus strongly desired to eliminate such disadvantages.
SUMARY OF THE INVENTION
[0005] As a result of intensive studies made so as to solve the above problems of the prior
art, the present inventors have found that the desired object is achievable by the
provision of a method for manufacturing nonwoven fabrics in which a fiber bundle comprising
a plurality of composite fibers spun out of a spinneret is drawn by a drawing force
of a high-speed air stream and blown against a working net conveyor while said air
stream is sucked and removed from below the net conveyor to deposit said fiber bundle
on the net conveyor to form a web, and the web is then heat-treated to develop crimps,
and the fibers thermally adhere together at their points of contact, said method being
characterized in that an air stream is blown against said web from below said net
conveyor for a time before the heat-treatment, with an intensity sufficient to float
said web of which bottom face (as explained later) rises above said net conveyor by
0.2 to 30 mm.
BRIEF DESCRIPTION OF THE DRAWINGS
[0006] The present invention will now be explained specifically but not exclusively with
reference to the accompanying drawings, in which:
Figure I is a schematic view illustrative of one embodiment of the nonwoven fabric
making system used in the present invention, and
Figures II-a, b and c each provide a perspective illustration of the air stream blower
used with the above system.
DETAILED EXPLANATION OF THE INVENTION
[0007] With two extruders (not shown), two sorts of thermoplastic resins are supplied to
a composite spinneret 1, out of which a fiber bundle 2 comprising a plurality of heat-bondable
composite fibers is spun. The fiber bundle 2 is then drawn by a high-speed air stream
sucker 3 and blown against and deposited on a working net conveyor 4 to form a web
5. At a position of the net conveyor 4 against which the fiber bundle 2 is blown,
a substantial portion of the high-speed air stream is sucked and removed by an exhaust
unit 8 located back side thereof, whereby the web 5 is brought into close contact
with the net conveyor 4 to stabilize its shape. The thus shape-stabilized web 5 moves
with the net conveyor 4. Subsequently, the web 5 is made to float above the net conveyor
4 according to the characteristic feature of the present invention. More specifically,
with an air stream blower 9 located before the position at which the web 5 reaches
a heating furnace 6, an air stream is blown against the web 5 from below the net conveyor
4 to make the web 5 to float in such a manner that the bottom face of the web 5 rises
above the net conveyor 4 by 0.2 to 30 mm. (It is here to be noted that in a strict
sense, there is no continuous bottom face, but, in the present diclsoure, the assumed
plane contacting the bottom of the web 5 is referred to as the bottom face of the
web). At a floating height less than 0.2 mm, it is impossible to completely set free
fibers entangled at a lower portion of the web 5 in the net, so that the shrinkage
of the web becomes incomplete at the next heat treatment step, thus giving a nonwoven
fabric which is of inferior bulkiness or has unevenness of unit-weight due to unevenness
of the shrinkage or a network pattern of the net conveyor 4. At a floating height
exceeding 30 mm, on the other hand, the entanglement of fibers in the web 5 becomes
so loose that the web 5 is unstable in shape, thus making it impossible to obtain
any uniform nonwoven fabric. Thus the web 5 is floated for a time above the net conveyor
4 in this manner, then the fibers are prevented from being entangled in the net. After
passing above the air stream blower 9, the web 5 is relocated on the net conveyor
4, while the fibers are not entangled in the net. In this state, the web 5 is delivered
with the net conveyor 4 into a heating furnace 6, wherein it is heat-treated to permit
free development of crimps without being adversely affected, while the fibers are
fixed together by the heat-adhesion of a low-melting component at their points of
contact, thus giving a nonwoven fabric (7) of sufficient bulkiness.
[0008] The air stream blower 9 used may be of any type that the desired amount of an air
stream is blown against the web uniformly across its widthwise direction. For instance,
use may be made of a blower having a nozzle including a number of holes, as shown
in Figure II-a, a blower having a slitted nozzle, as shown in Figure II-b and a blower
having a multiplicity of nozzles located in the lengthwise direction of the web, as
shown in Figure II-c.
[0009] As the high-speed air stream sucker 3, use may be made of any one of known devices
generally used for spun bonding.
[0010] As the heating furnace 6, an infrared type heater or a device using hot air as the
heat source is preferable, since they do not mechanically hinder the development of
crimps in fibers by heat treatments. On the other hand, a hot calender roll is not
desired because of causing damage to the bulkiness of nonwoven fabrics. Figure 1 is
a schematic view of the heating furnace 6 having two stages of far-infrared type heaters.
[0011] The heat-bondable composite fibers used to obtain bulky nonwoven fabrics in the present
invention are obtained by composite-spinning two or more sorts of thermoplastic resins
having a difference of 10°C or more, preferably 15°C or more, between their melting
points, the types of the composite fibers being in the form of a parallel, sheath-core
or islands-in-sea form in which a low-melting resin occupies greater part than a half
of the fibers' surfaces. Such composite fibers can successfully develop crimps through
the heat-treatment of conditions suitably selected in the above heating furnace,
and can be bonded and fixed together at their points of contact by the melt of the
low-melting resin alone, thus giving a bulky and strong nonwoven fabric. Examples
of combinations of such thermoplastic resins are crystalline polypropylene/high density
polyethylene, crystalline polypropylene/ethylene-vinyl acetate copolymers, polyethyleneterephthalate/high
density polyethylene, nylon 66/nylon 6, and others. The fineness of a single filament
of the composite fibers and the number of crimps developed by heat treatments are
suitably selected from a range 0.1 to 15 deniers and a range of 4 to 60 crimps/25
mm, respectively, depending upon the purposes of nonwoven fabrics. The density of
nonwoven fabrics may suitably be selected from a wide range depending upon the purposes,
e.g., a range of 0.005 to 0.02 g/cm³ for the purpose of clothing waddings, a range
of 0.01 to 0.05 g/cm³ for the purpose of sanitary material surfacings and a range
of 0.04 g/cm³ or more for the purpose of clothing interlinings.
EXAMPLES
[0012] The present invention will more be specifically explained with reference to the following
examples. It is understood that physical values mentioned below were measured in the
following manners.
Density: Five square samples of 20 cm × 20 cm were measured in terms of unit-weight
in g/m² and thickness in cm. Density was then calculated from the following equation:
Density in g/cm³ = Unit-weight/Thickness × 10,000
Five calculated values were averaged.
Strength and Elongation:
[0013] Five test pieces, each of 5 cm × 20 cm, were obtained from a sample in its warp and
weft directions according to the measuring method JIS L 1085 (tesing procedures for
nonwoven fabric interlinings) - "Tensile Strength and Elongation" -, and were then
tested at a grip gap of 10 cm and a tensile speed of 30 cm/min. to determine their
breaking strength in kg/5 cm and elongation in %, which were then averaged.
Example 1
[0014] A bulky nonwoven fabric was manufactured with a system similar to that shown in Figure
1. Crystalline polypropylene (with a melt flow rate (MFR for short) of 22 as measured
under the conditions specified in JIS K 7210, Condition 14 in Table 1) and high density
polyethylene (with an MFR of 20 as measured under the conditions specified in JIS
K 7210, Condition 4 in Table 1) were respectively supplied from extruders (A) and
(B), both not shown, to a side-by-side type of composite spinneret 1 having 198 holes
in a constant amount of 40 g/min. to spin composite fibers comprising the above two
components and having a fineness of 1.8 d/f (deniers per filament) into a fiber bundle
2. With a high-speed air stream sucker 3 operating at an air speed of 2,020 m/min.,
the fiber bundle 2 was blown onto a net conveyor 4 moving at 11.5 m/min. to form a
web 5. With an exhaust unit 8 located below the position at which the fiber bundle
2 was blown against the net conveyor 4, the blowing air was sucked and removed to
fix the web 5 on the net conveyor 4, while air was blown against the net conveyor
4 from below with an air stream blower 9 before the web reached a heating furnace
6, thereby floating the web 5 about 3 mm above. As the air stream blower 9, use was
made of a unit comprising three pipes arranged side by side in the moving direction
of the web 5, each having a nozzle including a number of holes, as shown in Figure
II-a. After passing above the air stream blower 9, the web 5 was again settled on
the net conveyor. Then, the web 5 was passed through a heating furnace 6 provided
with a far-infrared type heater and adjusted to 140°C at the first stage and 150°C
at the second stage for a period of 70 seconds for heat treatments. Finally, the web
5 was cooled off to obtain an nonwoven fabric 7. In the composite fiber, sprial crimps
of 24 crimps/25 mm were developed by such heat treatments. In the nonwoven fabric
7, the composite fibers were fixed together at their points of contact by the heat-adhesion
of high density polyethylene. The thus obtained nonwoven fabric had a unit-weight
of 23 g/m², a thickness of 1.53 mm, a density of 0.015 g/cm³, a strength of 2,450
g/5 cm in the warp direction and 1,510 g/5 cm in the weft direction, and an elongation
of 70 % in the warp direction and 46 % in the weft direction, and the nonwoven fabric
was uniform and free from any wrinkle and network pattern on its both front and back
sides. This nonwoven fabric was found to be best- suited for disposable diapers surfacings.
Example 2
[0015] With a similar system as used in Example 1, polyethylene terephthalate (with an intrinsic
viscosity of 0.65) and linear low-density polyethylene (with an MFR of 20 as measured
under the conditions specified in JIS K 7210, Condition 4 in Table 1) were respectively
supplied from extruders (A) and (B) in a constant quantity of 40 g/min. for composite
spinning. The obtained web 5 was processed at a drawing air stream speed of 1,450
m/min., a net conveyor speed of 6.8 m/min. and a floating height of web of about 8
mm, and was then thermally treated through a heating furnace 6 adjusted to 142°C at
both the first and second stages for a period of 2 minutes to obtain a nonwoven fabric
7. In the composite fiber, spiral crimps of 20 crimps/25 mm were developed by such
heat treatments.
[0016] The nonwoven fabric 7 had a unit-weight of 40 g/m², a thickness of 2.35 mm, a density
of 0.017 g/cm³, a strength of 5,860 g/5 cm in the warp direction and 3,260 g/5 cm
in the weft direction, and an elongation of 47 % in the warp direction and 44 % in
the weft direction, and was so free from any wrinkle and network pattern on its both
front and back sides that it was uniform. This nonwoven fabric was found to be best-suited
for middle layer material in disposable diapers or clothing interlinings.
Example 3
[0017] With a similar system as used in Example 1, crystalline polypropylene (with an MFR
of 21) and propylene copolymer (with an MFR of 11 and consisting of 92 wt. % of propylene,
3.5 wt. % of ethylene and 4.5 wt. % of butene-1)were supplied from extruders (A) and
(B), respectively. The obtained web 5 was processed under the same conditions as applied
in Example 1, provided that it was floated about 5-mm above a net conveyor 4, thereby
obtaining a nonwoven fabric 7. Under such conditions, spiral crimps of 36 crimps/25
mm were developed in the composite fiber. The thus obtained nonwoven fabric 7 had
a unit-weight of 26 g/m², a thickness of 2.0 mm, a density of 0.013 g/cm³, a strength
of 2,410 g/5 cm in the warp direction and 1,430 g/5 cm in the weft direction, and
an elongation of 36 % in the warp direction and 32 % in the weft direction, and was
so free from any wrinkle and network patteren on its both front and back sides that
it was uniform. This nonwoven fabric was found to be best-suited for surfacings or
middle layer material in disposable diapers.
Comparative Example 1
[0018] A nonwoven fabric was obtained under the same conditions as applied in Example 1,
provided however that no air was blown against a web 5 deposited on a net conveyor
4 to float the former above the latter. The obtained nonwoven fabric had a unit-weight
of 21 g/m², a thickness of 0.81 mm, a density of 0.026 g/cm³, a strength of 3,020
g/5 cm in the warp direction and 1,930 g/5 cm in the weft direction, and an elongation
of 63 % in the warp direction and 32 % in the weft direction, and was slightly wrinkled
on its front side and scattered with network spots on its back side. This nonwoven
fabric could not be used as disposable diapers' surfacings because of having large
strength but being inferior in bukiness and uniformity.
[0019] Thus, according to the present invention, bulky, uniform and light nonwoven fabrics
can be obtained while maintaining the economical efficiency of spun bonding techniques.