BACKGROUND OF THE INVENTION
(a) Field of the Invention
[0001] The present invention relates to a high-strength polyester fiber for a rope being
used for anchoring, mooring, or towing a ship, and a preparation method thereof. More
specifically, the present invention relates to a polyester fiber of high elastic recovery
(recovered work ratio) having superior mechanical properties and wear resistance,
a low moisture absorption rate, a light resistance, a shock absorption performance,
and the like, and a preparation method thereof.
(b) Description of the Related Art
[0002] A marine rope being used for anchoring, mooring, or towing a ship or an industrial
rope being used in various construction sites has been developed in the direction
of securing the superior mechanical property of high strength.
[0003] Particularly, in many fields of ships, a wire rope has been largely used because
it can secure a high strength and a superior fatigue resistance, and a fiber rope
consisting of a high performance nylon fiber or a polyolefin fiber has been used even
in the case of using a synthetic fiber rope. But, there are problems that the wire
rope is corroded by water and too rigid to hold the movement of a ship caused by a
wave or a tidal difference and it may cause damage to a ship, and it is difficult
to operate because of the weight of the rope itself. Existing nylon fiber ropes may
cause a problem of frequent replacement because it has a large strength diminution
rate to ultraviolet (UV) rays and the strength of the rope deteriorates excessively,
and thus it loses the ability to hold the ship if it is used for a long time. Furthermore,
since the nylon fiber rope has a high moisture absorption rate, it is not easy to
operate when it is used for mooring or anchoring a ship, and it may cause a personal
accident if the rope is frozen in a wet form in winter.
[0004] Meanwhile, a polyester represented by polyethylene terephthalate (hereinafter, 'PET')
is being used widely to fibers, films, or resins because it is superior in mechanical
properties and chemical resistance. For example, in the case of fiber, it is being
used widely not only for clothes but also for various industrial materials such as
a tire cord, a belt, a hose, a rope, and the like. However, the existing polyester
fiber shows a low elongation property of high modulus and thus it cannot respond sufficiently
to the deformation caused by the movement of a ship according to the change of the
sea during anchoring a ship, and there is a problem of fiber breaking.
[0005] Therefore, we need the study for developing a high performance synthetic fiber which
can improve the shock absorption performance against the change of external environment
and can give superior mechanical properties and operation performance when the fiber
is used to the marine rope being used for anchoring, mooring, or towing a ship, or
the industrial rope.
SUMMARY OF THE INVENTION
[0006] It is an aspect of the present invention to provide a polyester fiber showing the
characteristics of high strength, high elongation, and high elastic recovery, and
having superior mechanical properties and wear resistance, a low moisture absorption
rate, a light resistance, a shock absorption performance, and the like, so as to be
used to the marine rope or the industrial rope.
[0007] It is another aspect of the present invention to provide a method of preparing said
polyester fiber.
[0008] It is still another aspect of the present invention to provide a fiber rope including
said polyester fiber.
[0009] The present invention provides a polyester fiber, wherein the recovered work ratio
at the elongation corresponding to 10% of the maximum load measured at room temperature
is 70% or more, the recovered work ratio at the elongation corresponding to 20% of
the maximum load is 50% or more, and the recovered work ratio at the elongation corresponding
to 30 % of the maximum load is 40 % or more.
[0010] The present invention also provides a method of preparing said polyester fiber, including
the steps of preparing a polyester undrawn fiber by melt-spinning a polyester polymer
having an intrinsic viscosity of 1.2 dl/g or more at 270 to 310 °C, and drawing the
polyester undrawn fiber.
[0011] The present invention also provides a polyester fiber rope including said polyester
fiber.
BRIEF DESCRIPTION OF THE DRAWINGS
[0012]
Fig. 1 is a schematic process drawing illustrating the preparation process of the
polyester fiber according to one embodiment of the present invention.
Fig. 2 is an example of strength-elongation curve of a general fiber, the elastic
recovery (recovered work ratio, %) can be calculated from the area of the strength-elongation
curve.
Fig. 3 represents the strength-elongation curve of the polyester fiber according to
Example 4 of the present invention.
Fig. 4 represents the strength-elongation curve of the polyester fiber according to
Comparative Example 1 of the present invention.
DETAILED DESCRIPTION OF THE EMBODIMENTS
[0013] Hereinafter, the polyester fiber which can be used to the marine rope or an industrial
rope, the method of preparing the same, and the fiber rope including the same are
explained in more detail, according to concrete embodiments of the present invention.
However, the followings are only for the understanding of the present invention and
the scope of the present invention is not limited to or by them, and it is obvious
to a person skilled in the related art that the embodiments can be variously modified
in the scope of the present invention.
[0014] In addition, "include" or "comprise" means to include any components (or ingredients)
without particular limitation unless there is no particular mention about them in
this description, and it cannot be interpreted as a meaning of excluding an addition
of other components (or ingredients).
[0015] In the present invention, 'polyester fiber' means a fibrous polymer obtained by the
esterification reaction of a diol compound and a dicarboxylic acid such as terephthalic
acid generally. The polyester fiber corresponds to a basic fiber component for preparing
'the marine rope or the industrial rope' of the present invention. The polyester has
a superior resistance against moisture and thus it is more preferable to prepare the
fiber rope for replacing the marine wire rope.
[0016] In the present invention, any common polyester fiber may be used as the polyester
fiber, for example, a polyalkylene terephthalate such as polyethylene terephthalate
(PET), polyethylene naphthalate (PEN), polybutylene terephthalate (PBT), polycyclohexanedimethylene
terephthalate (PCT), and the like, or a copolyester including the same as the main
component may be used. Particularly, polyethylene terephthalate is more preferable
to be used to the marine rope in the aspect of the properties of strength, elongation,
and so on.
[0017] However, the polyester has lower polymerization efficiency than nylon, and the degradation
of the molecular chain occurs much more because of severe hydrolysis by heat and moisture
when it is made into a fiber, and thus it is difficult to obtain molecular chains
having high molecular weight. Therefore, high drawing ratio is applied during the
spinning process in order to obtain high strength with short molecular chain, and
the properties of high strength, low elongation, and high modulus are obtained by
this. Like this, it has been difficult to obtain the polyester fiber having high recovered
work ratio because existing polyesters have short molecular chains. Meanwhile, nylon
can show the properties of high strength, high elongation, and high recovered work
ratio in addition to low modulus. If a ship is anchored by using the rope made of
the fiber having low recovered work ratio like existing polyester fibers, the rope
may be broken by the wild sea or a repetitive change of external environment due to
its elastic recovery and it may cause a breakage of the ship because it is impossible
to act as a buffer to the external shock and the external environmental shock is directly
delivered to the ship.
[0018] Accordingly, the present invention can be applied effectively to the preparation
of the marine fiber rope or the industrial fiber rope which can maintain sufficient
strength and elongation against the external environment change and can maintain the
long time shock absorption performance, by optimizing the properties of the polyester
fiber, especially, the recovered work ratio, to high levels in order to have superior
recovery rate against the repetitive change.
[0019] Particularly, as experimental results of the present inventors, it is revealed that
lower moisture absorption rate and more improved light resistance can be obtained
in company with superior mechanical properties by preparing the marine or industrial
rope by using the polyester fiber having a certain characteristic.
[0020] Therefore, according to one embodiment of the present invention, the present invention
provides a polyester fiber having a certain characteristic. The polyester fiber may
be the fiber wherein the recovered work ratio at the elongation corresponding to 10%
of the maximum load measured at room temperature is 70% or more, the recovered work
ratio at the elongation corresponding to 20% of the maximum load is 50% or more, and
the recovered work ratio at the elongation corresponding to 30% of the maximum load
is 40 % or more.
[0021] Such polyester fiber may preferably include polyethylene terephthalate (PET) as the
main component. At this time, various additives may be included with PET in the preparation
process, and the fiber may include 70 mol% or more, preferably 90 mol% or more, of
PET in order to secure superior mechanical properties when it is made into the polyester
fiber rope. Hereinafter, the term of polyethylene terephthalate (PET) means that 70mol%
or more of polyethylene terephthalate is included, without particular explanation.
[0022] Since the polyester fiber according to one embodiment of the present invention is
prepared under the below melt-spinning and drawing conditions, it becomes to show
far superior elastic recovery against a repetitive deformation at room temperature
to existing polyester fibers.
[0023] Existing polyesters generally show low elastic recovery characteristic due to its
short molecular chain, and it becomes inferior in the long time shock absorption performance
and wear resistance remarkably when they are made into the fiber rope. However, the
polyester fiber obtained through the controlled melt-spinning and drawing process
shows high elastic recovery characteristic and it can raise the shock absorption performance
of the rope and can extend the life time of the rope owing to said characteristic.
Furthermore, the polyester fiber of the present invention has the characteristic of
minimized drawing in company with said high elastic recovery. Due to such high elastic
recovery, the polyester fiber can resolve the problems of low wear resistance and
deteriorated shock absorption performance shown in the fiber rope including the fiber
having low elastic recovery, high modulus, and low elongation at break, and it is
possible to obtain more improved shock absorption performance and extended life time
of the rope in company with superior mechanical properties. Namely, the polyester
fiber may show the recovered work ratio of 70% or more, preferably 75% or more, and
more preferably 80% or more, at the elongation corresponding to 10% of the maximum
load measured at room temperature. Furthermore, the polyester fiber may show the recovered
work ratio of 50% or more, preferably 52% or more, and more preferably 54% or more,
at the elongation corresponding to 20% of the maximum load. The polyester fiber also
may show the recovered work ratio of 40 % or more, preferably 41% or more, and more
preferably 42 % or more, at the elongation corresponding to 30% of the maximum load.
Due to such high elastic recovery (recovered work ratio), the polyester fiber can
resolve the problems of low wear resistance and deteriorated shock absorption performance
shown in the fiber rope including the existing fiber having high modulus and low elongation
at break, and it is possible to obtain more improved shock absorption performance
and extended life time of the rope in company with superior mechanical properties.
[0024] At this time, the elastic recovery (recovered work ratio) of the polyester fiber
may be a percentage value (%) of recovered work per total work in the stress-elongation
graph obtained by a tensile test, as represented by the following Calculation Formula
1:

[0025] Here, the total work is the value corresponding to the area of the strength-elongation
curve of the fiber measured according to American Society for Testing and Materials
standard ASTM D 2256 method at room temperature, as illustrated in Fig. 2. Furthermore,
the recovered work is the value corresponding to the area of the strength-elongation
curve measured after repeating the elongation corresponding to 10%, 20%, or 30% of
the maximum load respectively and the release 10 times, as illustrated in Fig. 2.
In the marine rope for anchoring or mooring a ship, if the recovered work ratio of
the fiber is low like the existing polyester fibers, it cannot respond sufficiently
to the deformation caused by the movement of the ship according to the change of the
sea during anchoring the ship, and it loses the ability to hold the ship during anchoring
the ship because it loses the elastic recovery after a period of use.
[0026] Particularly, the polyester fiber of the present invention is characterized in that
the elastic recovery (work recovery) is optimized to maintain the initial designed
properties even in the repetitive deformation and to be able to absorb the shock by
the deformation, so that it can be used to the marine rope for anchoring, mooring,
or towing a ship or to the industrial rope being used in various construction sites.
In this aspect, the polyester fiber may have the recovered work ratio of 70% or more,
50% or more, and 40% or more respectively at the elongation corresponding to 10%,
20%,and 30% of the maximum load measured at room temperature, namely, the maximum
tensile strength in the strength-elongation curve measured at room temperature. The
reason for applying the elongation to the fiber until 30% is for considering the conditions
for the rope design and the degree of maximum deformation during mooring a ship, and
it is known in the field of shipbuilding industry that the recovered work ratio at
the elongation corresponding to 10% of the maximum load is more important matter,
because the deformation by external environment that the ship encounters most frequently
during mooring in the sea is the level of within 10% of the maximum load. For more
concrete example, namely, in the case of designing the rope for holding a ship, it
is possible to design the rope in the light of that the force for holding a ship against
the movement by a tidal difference needs just within 10% of the maximum load and the
force for holding a ship against the movement by the wind and waves by typhoon needs
30% of the maximum load when anchoring a ship.
[0027] Furthermore, the polyester fiber may show more improved intrinsic viscosity in comparison
with formerly known polyester fibers, namely, it may show the intrinsic viscosity
of 0.8 dl/g or more or 0.8 dl/g to 1.2 dl/g, preferably 0.85 dl/g or more or 0.85
dl/g to 1.15 dl/g, and more preferably 0.90 dl/g or more or 0.90 dl/g to 1.10 dl/g.
So that the rope prepared by using the polyester fiber exhibits high mechanical properties
and has superior wear resistance, it is preferable to have the intrinsic viscosity
of such range.
[0028] The intrinsic viscosity of the fiber is preferably 0.8 dl/g or more so as to exhibit
high strength with low elongation and satisfy the demanded strength for the marine
or industrial fiber rope, and if not, it cannot help exhibiting the properties with
high-drawing. Like this, it is possible to increase the entanglement and disorder
between molecular chains and prevent the slip between molecular chains due to an external
deformation, by means of securing long molecular chain by applying a low-drawing.
If not, namely, if it has short molecular chains, the slip occurs between molecular
chains by the external deformation and the shape is deformed, and it cannot function
as a buffer to the external deformation because the mechanical and physical properties
change, particularly, the elasticity deteriorates, according to this. Therefore, it
is preferable to exhibit high strength property with a low-drawing by means of maintaining
the intrinsic viscosity of the fiber to be 0.8 dl/g or more. Furthermore, it is preferable
that the intrinsic viscosity of the polyester fiber is 1.2 dl/g or less, because when
the intrinsic viscosity is over 1.2 dl/g, the drawing tension may increase during
the drawing process and may cause a problem on the process. Particularly, the polyester
fiber of the present invention can secure high strength characteristic sufficient
to be effectively used for anchoring, mooring, or stowing a ship and can have more
improved shock absorption property against the rolling of the ship due to the change
of external environment, by maintaining the intrinsic viscosity of such high level.
[0029] Accordingly, it becomes possible to prepare the marine or industrial rope having
superior mechanical properties, a wear resistance, and a shock absorption effect at
the same time, by using the polyester fiber showing such high elastic recovery and
high elongation, and preferably a high intrinsic viscosity. Therefore, if the polyester
fiber is used to the rope, it decreases the deterioration in the strength caused by
the moisture absorption and the ultraviolet rays remarkably and can secure the superior
mechanical properties and strength maintenance rate as the marine or industrial rope.
Simultaneously, the polyester fiber of the present invention improves the shock absorption
performance against the rolling of the ship or the supporter according to the external
change such as a tidal current or an air circulation and can decrease the occurrence
of the fiber breaking remarkably.
[0030] Meanwhile, the polyester fiber according to one embodiment of the present invention
may show the tensile tenacity of 8.0 g/ d or more or 8.3 g/d to 11.0 g/d, and preferably
8.5 g/d or more or 8.5 g/d to 10.0 g/d. Furthermore, the polyester fiber may show
the elongation of 15% or more or 15% to 30%, and preferably 16 % or more or 16 % to
28%. The polyester fiber may show the dry heat shrinkage rate of 7% or less or 1.5%
to 7%. The dry heat shrinkage rate is based on the value measured under the condition
of giving the fixed load of 0.01 g/d at 177°C for 2 minutes.
[0031] As disclosed above, the polyester fiber of the present invention not only can have
superior tenacity and properties but also can show superior performance in wear resistance
and UV strength maintenance rate when it is prepared into the fiber rope, by securing
the intrinsic viscosity, the initial modulus, and the elongation in the optimum range.
[0032] The monofilament fineness of the polyester fiber may be 21 DPF or less or 3 to 21
DPF, and preferably 20 DPF or less or 4 to 20 DPF. In order to use the polyester fiber
to the marine rope or the industrial rope effectively, high denier is preferable in
the aspect of the productivity and low denier is preferable in the aspect of the property
exhibition, and thus the applicable total fineness of the polyester fiber may be 900
denier or more or 900 to 4,500 denier, and preferably 1,000 denier or more or 1,000
to 4,000 denier. Since the more number of the fiber filaments, the softer feel, but
too many filaments are not good in the spinability and the wear resistance, the total
number of the filaments may be 110 to 550, and preferably 120 to 550.
[0033] Furthermore, the polyester fiber may further include an additive with necessity in
order to prevent the fiber damage during spinning, improve the friction resistance,
and minimize the strength deterioration. Particularly, the polyester fiber, namely,
the polyester raw fiber may include one or more inorganic additives selected from
the group consisting of TiO
2, SiO
2, BaSO
4, and so on. At this time, the inorganic additive may be included with the content
of 100 to 1,500 ppm, and preferably of 200 to 1,200 ppm, in the polyester fiber. The
content of the inorganic additive may be 100 ppm or more, preferably 200 ppm or more,
in the aspect of the spinability, and it may be 1,500 ppm or less, and preferably
1,200 ppm or less, in the aspect of the superior strength exhibition.
[0034] Meanwhile, the polyester fiber according to one embodiment disclosed above may be
prepared by the method of preparing a polyester undrawn fiber by melt-spinning a polyester
polymer and drawing the polyester undrawn fiber. As disclosed above, the concrete
condition or the processing method of the steps is directly or indirectly reflected
in the properties of the polyester fiber, and the polyester fiber having above properties
can be prepared.
[0035] Particularly, it is revealed that the polyester fiber having the characteristic that
the elastic recovery against the repetitive deformation is remarkably superior to
the existing polyester fibers, namely, the characteristic that the recovered work
ratio at the elongation corresponding to 10% of the maximum load measured at room
temperature is 70% or more, the recovered work ratio at the elongation corresponding
to 20% of the maximum load is 50% or more, and the recovered work ratio at the elongation
corresponding to 30% of the maximum load is 40% or more, can be obtained through the
process optimization disclosed above. Therefore, such polyester fiber can show the
high recovered work ratio, the high strength, and the high elongation range at the
same time, and it can be applied to the marine rope or the industrial rope having
superior mechanical properties, a wear resistance, and a shock absorption performance
preferably.
[0036] Each step of the preparation method of the polyester fiber is explained more in detail
as follows.
[0037] The method of preparing the polyester fiber includes the steps of preparing a polyester
undrawn fiber by melt-spinning a polyester polymer having an intrinsic viscosity of
1.2 dl/g or more at 270 to 310 °C, and drawing the polyester undrawn fiber.
[0038] First of all, the implementation of the melt spinning and drawing processes of the
present invention can be explained briefly by referring the annexed figures, so that
a person skilled in the related art to which the present invention pertains can easily
carryout the same.
[0039] Fig. 1 is a schematic process drawing for representing the preparation process of
the polyester fiber including the melt-spinning and drawing steps according to one
embodiment of the present invention. As illustrated in Fig. 1, the present preparation
method of the polyester fiber for the rope may include the processes of melting the
polyester chip prepared by the method disclosed above, cooling the molten polymer
spun through a die with quenching-air, providing a spinning oil to the undrawn fiber
by using the oil rolls 120 (or oil-jets), and dispersing the spinning oil provided
to the undrawn fiber uniformly on the surface of the fiber with uniform air pressure
by using the pre-interlacer 130. Subsequently, the fiber may be prepared finally by
intermingling the fiber with a uniform pressure in the second interlacer 150 and winding
the same with the winder 160, after carrying out a drawing process through the multi-step
drawing apparatuses 141 -146.
[0040] At first, the preparation method of the present invention prepares the polyester
undrawn fiber by melt-spinning the high viscosity polymer including polyethylene terephthalate.
[0041] At this time, in order to obtain the polyester undrawn fiber satisfying low initial
modulus and high elongation range, it is preferable to carry out the melt-spinning
process at low temperature range so as to minimize the thermal degradation of the
polyester polymer. Particularly, in order to minimize the deterioration of the intrinsic
viscosity and the CEG (Carboxyl End Group) content of the high viscosity polyester
polymer during the process, namely, in order to maintain the high intrinsic viscosity
and the low CEG content of the polyester polymer, the melt-spinning may be carried
out at low spinning temperature, for example, at the temperature of 270 to 310 °C,
preferably of 280 to 305 °C, and more preferably of 282 to 298 °C. Here, the spinning
temperature means the temperature of the extruder, and if the melt-spinning process
is carried out at the temperature over 310 °C, it causes plentiful thermal degradations
of the polyester fiber and the decrease of the intrinsic viscosity, the decrease in
molecular weight and the increase in CEG content may get bigger, the surface of the
fiber is damaged, and it may cause the deterioration of overall properties. On the
contrary, if the melt-spinning process is carried out at the temperature below 270
°C, it may be difficult to melt the polyester polymer and the spinability may deteriorate
due to N/Z surface cooling. Therefore, it is preferable to carry out the melt-spinning
process within said temperature range. The polyester polymer preferably includes polyethylene
terephthalate (PET) as the main component. At this time, various additives may be
included with PET in the preparation process, and the fiber may include 70 mol% or
more, preferably 90 mol% or more, of PET in order to secure the superior mechanical
properties when it is made into the polyester fiber rope.
[0042] Furthermore, the polyester polymer may include one or more inorganic additives selected
from the group consisting of TiO
2, SiO
2, BaSO
4, and so on with necessity. At this time, the inorganic additive may be included with
the content of 100 to 1,200 ppm, and preferably of 200 to 1,000 ppm in the polyester
fiber. The content of the inorganic additive may be 100 ppm or more, and preferably
200 ppm or more, in the aspect of spinability, and it may be 1,500 ppm or less, and
preferably 1,200 ppm or less, in the aspect of superior strength exhibition.
[0043] As the results of experiments, it is revealed that, by carrying out the melt-spinning
process of PET at such low temperature range, the degradation reaction of the polyester
polymer is minimized so as to secure the high molecular weight and maintain the high
intrinsic viscosity and the high strength fiber can be obtained without applying high
drawing ratio in succeeding drawing process and since the drawing process can be carried
out with low drawing ratio, the modulus can be lowered effectively and the polyester
fiber satisfying the properties disclosed above can be obtained.
[0044] Furthermore, the melt-spinning process may be carried out with low spinning speed
so as to carry out the process under lower spinning tension, namely, so as to minimize
the spinning tension, in the aspect of minimizing the degradation reaction of the
polyester polymer. For example, the melt-spinning speed of the polyester polymer may
be controlled to be 300 to 1,000 m/min, and preferably to be 350 to 700 m/min. Since
the melt-spinning process of the polyester polymer is carried out selectively under
low spinning tension and low spinning speed, the degradation reaction of the polyester
polymer can be minimized.
[0045] Meanwhile, the undrawn fiber obtained after the melt-spinning process may show the
intrinsic viscosity of 0.8 dl/g or more or 0.8 dl/ g to 1.2 dl/g, preferably of 0.85
dl/g or more or 0.85 dl/ g to 1.2 dl/g, and more preferably or 0.9 dl/g or more or
0.90 dl/g to 1.2 dl/g.
[0046] Particularly, it is preferable to use the high viscosity polyester polymer, for example,
the polyester polymer having the intrinsic viscosity of 1.2 dl/g or more, in the preparation
process of the undrawn fiber, in order to prepare the high strength and low modulus
polyester fiber, as disclosed above. And, it becomes possible to reveal the high strength
with low drawing ratio and lower the modulus effectively by maintaining the high viscosity
range to the maximum through the melt-spinning and drawing processes using the high
viscosity polyester polymer. However, it is more preferable that the intrinsic viscosity
is 2.0 dl/g or less in order to prevent the molecular chain scission caused by the
temperature rise for melting the polyester polymer and the pressure increase by the
discharge rate at the spinning pack.
[0047] And, it is preferable that the PET chip is spun through a spinning die designed for
that the polyester fiber has the monofilament fineness of 21 DPF or less or 3 to 21
DPF, preferably of 20 DPF or less or 4 to 20 DPF. Namely, the monofilament fineness
of the fiber is preferably 4.0 DPF or more in order to reduce the possibility of the
fiber breaking during the spinning process or by the interference between the fibers
during a cooling process, and the monofilament fineness is preferably 20 DPF or less
in order to increase the cooling efficiency.
[0048] Furthermore, the process for preparing the PET undrawn fiber may further include
a cooling process after the melt-spinning process of PET. Said cooling process is
carried out preferably by providing a cooling air of 15 to 60 °C. At this time, the
cooling air volume is controlled preferably to be 0.4 to 1.5 m/s in each temperature
condition of the cooling air. With this, the PET undrawn fiber showing all the properties
according to one embodiment of the present invention can be prepared more easily.
[0049] Meanwhile, after preparing the polyester undrawn fiber through such spinning step,
the drawn fiber is prepared by drawing the undrawn fiber. At this time, the drawing
process may be carried out with the total drawing ratio of 5.0 to 6.5, and preferably
of 5.0 to 6.2. The polyester undrawn fiber is maintaining the high intrinsic viscosity
and the low initial modulus by the optimized melt-spinning process. Therefore, if
the drawing process is carried out with high drawing ratio over 6.5, a fiber breaking
or hairiness may occur because it reaches an overdrawn level and the low elongation
and high modulus fiber may be obtained due to the high orientation. Particularly,
in the case of that the elongation of the fiber decreases and the modulus increases
under the condition of high drawing ratio, the wear resistance and the strength maintaining
rate may become not good when it is applied to the fiber rope. On the other hand,
if the drawing process is carried out with relatively low drawing ratio, the strength
of the polyester fiber prepared by the method may be lowered partially because the
degree of orientation of the fiber is low. However, it is preferable in the aspect
of the properties that the drawing process is carried out with the drawing ratio of
5.0 to 6.5, because it is possible to prepare the high strength and low modulus polyester
fiber suitable to be applied to the marine or industrial fiber rope, for example,
by carrying out the drawing process with the drawing ratio of 5.0 or more.
[0050] According to another preferable embodiment of the present invention, in order to
prepare the low modulus polyester fiber with a direct spin-draw process while satisfying
high strength and low shrinkage characteristic at the same time, the method may include
a drawing process through the multi-step godet rollers, a heat-setting process, a
relaxation process, after melt-spinning the high viscosity polyethylene terephthalate
polymer chips and before winding the fiber on the winder.
[0051] The drawing process may be carried out after passing the undrawn fiber through the
godet-rollers with 0.2% to 2.0% of oil pickup amount.
[0052] The relaxation ratio in the relaxation process is preferably 1% to 14%. If the relaxation
ratio is below 1%, it is difficult to exhibit the shrinkage ratio and it may be difficult
to prepare the high elongation low modulus fiber because of high degree of orientation
of the fiber like in the high drawing ratio condition. If the relaxation ratio exceeds
14%, the fiber vibration intensifies on the godet rollers and it is difficult to secure
the workability.
[0053] Furthermore, the heat-setting process that heat-treats the undrawn fiber at the temperature
of about 170 to 250 °C may be carried out in the drawing process. At this time, the
heat-setting process may be carried out preferably at the temperature of 175 to 240
°C, and more preferably at 180 to 245 °C. Here, if the temperature is below 170 °C,
it may be difficult to achieve the shrinkage rate because the thermal effect is insufficient
and the relaxation efficiency deteriorates. On the other hand, if the temperature
exceeds 250 °C, the strength of the fiber may be deteriorated by thermal degradation
and the workability may decrease because the tar formed on the roller increases.
[0054] At this time, the winding speed may be 2,000 to 4,000 m/min, and preferably 2,500
to 3,700 m/min.
[0055] Meanwhile, since the polyester fiber of the present invention shows the characteristics
of high strength, high elongation, high recovered work ratio, it may be used preferably
to the industrial materials for various uses such as the marine rope being used in
anchoring, mooring, of towing a ship, or the industrial rope being used in various
construction sites.
[0056] Particularly, the polyester fiber of the present invention may be made into the marine
or industrial polyester fiber rope through a plaiting and twisting process. The fiber
rope may be prepared by carrying out the plaiting and twisting process with one identical
apparatus.
[0057] In the case of the fiber rope made of the polyester fiber of the present invention,
the strength at break per unit diameter (mm) may be 0.67 ton/mm or more or 0.67 to
1.2 ton/mm, preferably 0.69 ton/mm or more, and more preferably 0.72 ton/mm or more.
The elongation at break may be 18% or more or 18% to 45%, preferably 20 % or more,
and more preferably 24% or more. The moisture absorption rate of the fiber rope may
be 2% or less, preferably 1% or less, and more preferably 0.5% or less. The moisture
absorption rate of the fiber rope is based on the value measured under the conditions
of 25 °C and relative humidity of 65%RH. The strength maintenance of the fiber rope
may be 90% or more, preferably 95% or more, and more preferably 98% or more. The strength
maintenance rate of the fiber rope may be obtained by measuring the degree of strength
decrease after wetting or UV irradiation.
[0058] For example, the degree of the strength decrease by wetting may be measured by carrying
out the tensile test at room temperature immediately after wetting the fiber rope
in the water of room temperature for 30 minutes. The strength maintenance after wetting
of the fiber rope of the present invention may be 90% or more, preferably 95% or more,
and more preferably 98% or more. Furthermore, the degree of strength decrease may
also be measured after irradiating the fiber rope with xenon arc light at 40 °C and
65%RH for 100 hours. The strength maintenance after UV irradiation of the fiber rope
of the present invention may be 90 % or more, preferably 95% or more, and more preferably
98 % or more.
[0059] The fiber rope made of the polyester fiber may have the recovered work ratio of 80%
or more, preferably 85% or more, and more preferably 90% or more, at the elongation
corresponding to 10% of the maximum load measured at room temperature. Furthermore,
the fiber rope may have the recovered work ratio of 60% or more, preferably 61 % or
more, and more preferably 62% or more, at the elongation corresponding to 20% of the
maximum load. The fiber rope made of the polyester fiber of the present invention
may have the recovered work ratio of 50% or more, preferably 51% or more, and more
preferably 52% or more, at the elongation corresponding to 30 % of the maximum load.
[0060] At this time, the elastic recovery (recovered work ratio) of the polyester fiber
rope may be the percentage value (%) of the recovered work per the total work in the
stress-elongation graph obtained by the tensile test, as represented by the following
Calculation Formula 2:

[0061] Here, the total work is the value corresponding to the area of the strength-elongation
curve that is obtained by measuring the strength at break and the elongation at break
of the rope at room temperature, as illustrated in Fig. 2. In above formula 2, the
recovered work is the value corresponding to the area of the strength-elongation curve
measured after repeating the elongation corresponding to 10%, 20%, or 30% of the maximum
load respectively and the release 10 times, as illustrated in Fig. 2. In the marine
rope for anchoring or mooring a ship, if the recovered work ratio of the fiber is
low like the existing polyester fiber ropes, it cannot respond sufficiently to the
deformation caused by the movement of the ship according to the change of the sea
during anchoring the ship, and it loses the ability to hold the ship during anchoring
the ship because it loses the elastic recovery after a period of use.
[0062] Since the polyester fiber rope of the present invention has the minimized moisture
absorption rate in company with the superior elongation at break and the strength
maintenance rate, the life of the rope can be extended and it becomes possible to
secure sufficient stability for anchoring, mooring, towing a ship or in various construction
sites, through the superior mechanical properties and the effective response to the
change of external environment.
[0063] In the present invention, items besides above disclosure can be added or subtracted
with necessity and the present invention does not limit them particularly.
EFFECTS OF THE INVENTION
[0064] According to the present invention, the polyester fiber having the superior wear
resistance and strength maintenance rate in company with the superior mechanical properties
is provided by optimizing the elastic recovery, the elongation at break and the strength
to be a certain high level.
[0065] Such polyester fiber can have a sufficient strength and elongation, and can secure
superior mechanical properties and shock absorption performance because it is optimized
to have a high strength, a high elastic recovery, and a high elongation. By this,
it becomes possible to prepare the rope which can minimize the fiber breaking, can
improve the shock absorption performance noticeably, and can secure the superior life
and the sufficient stability of the rope, even if there is a change of external environment
such as the rough sea and the severe rolling of a ship.
[0066] Hereinafter, preferable examples and comparative examples are presented for understanding
the present invention. However, the following examples are only for illustrating the
present invention and the present invention is not limited to or by them.
Examples 1-5
[0067] After preparing a polyester undrawn fiber by the method of melt-sinning a polyester
polymer having a certain intrinsic viscosity and cooling the same, a polyester fiber
was prepared by drawing the undrawn fibers with a certain drawing ratio while heat-treating
the same. At this time, the intrinsic viscosity of the polyester polymer, spinning
speed and spinning tension in the melt-spinning process, spinning temperature condition,
drawing ratio, heat-treating temperature followed the conditions in the follow Table
1, and the other conditions were dealt with in accordance with common conditions for
preparing a polyester fiber.
[Table 1]
Classifications |
Example 1 |
Example 2 |
Example 3 |
Example 4 |
Example 5 |
PET Content (mol%) |
100 |
100 |
100 |
100 |
100 |
Intrinsic Viscosity of Chip (dl/g) |
1.20 |
1.23 |
1.27 |
1.30 |
1.35 |
Spinning Temperature (°C) |
285 |
286 |
288 |
290 |
292 |
Drawing Ratio |
5.8 |
5.75 |
5.73 |
5.67 |
5.60 |
Heat-treatment Temperature (°C) |
235 |
236 |
237 |
243 |
245 |
[0068] The properties of the polyester fibers prepared according to Examples 1-5 were measured
according to the following methods, and the measured properties are listed in the
following Table 2.
1) Tensile Strength and Elongation at Break
[0069] The tensile strength and the elongation at break of the polyester fibers were tested
by using a universal testing machine (UTM) (INSTRON Ltd.) according to ASTM D 2256
method. At this time, the sample length was 250 mm, the straining speed was 300 mm/min,
and the initial load was set-up to 0.05 g/d.
2) Elastic Recovery
[0070] After measuring the strength-elongation curve according to ASTM D 2256 method at
room temperature and checking the maximum load and the total work, the strength-elongation
curve was measured again and the recovered work was calculated after repeating the
elongation corresponding to 10%, 20%,or 30% of the maximum load respectively and the
release 10 times, and the recovered work ratio (%) of the fiber was calculated according
to Calculation Formula 1:

3) Dry Heat Shrinkage Rate
[0071] Dry heat shrinkage rate was measured by using a Testrite MK-V device (Testrite Co.,
UK) under the condition of providing the fixed load of 0.01 g/d at 177 °C for 2 minutes
4) Intrinsic Viscosity
[0072] After extracting the spinning oil from the specimen with carbon tetrachloride and
dissolving the specimen in ortho-chlorophenol at 160±2°C, the viscosity of the specimen
in a capillary was measured by using an automatic viscometer (Skyvis-4000) at the
temperature of 25°C, and the intrinsic viscosity (IV) of the fiber was calculated
according to the following Calculation Formula 3:

5) Fineness of Monofilament
[0073] After taking 9000m of the fiber bundle by using a bobbin, the fineness of monofilament
was calculated by dividing the weight of the fiber bundle by the number of filaments.
[Table 2]
Classifications |
Example 1 |
Example 2 |
Example 3 |
Example 4 |
Example 5 |
Intrinsic Viscosity of Fiber (dl/g) |
0.85 |
0.88 |
0.92 |
0.97 |
1.01 |
Tensile Tenacity of Fiber (g/d) |
9.2 |
9.3 |
9.2 |
9.4 |
9.4 |
Elongation at Break of Fiber (%) |
16.3 |
17 |
17.5 |
18.2 |
19.5 |
Dry Heat Shrinkage Rate of Fiber (%) |
5.0 |
5.5 |
5.8 |
5.4 |
5.0 |
Monofilament Fineness of Fiber (DPF) |
12.5 |
10.4 |
13.0 |
12.5 |
10.4 |
Total Fineness of Fiber (de) |
1,500 |
2,000 |
2,500 |
3,000 |
4,000 |
Recovered Work Ratio at 10% of Maximum Load (%) |
88 |
91 |
94 |
97 |
99 |
Recovered Work Ratio at 20% of Maximum Load (%) |
54 |
56 |
58 |
59 |
60 |
Recovered Work Ratio at 30% of Maximum Load (%) |
40 |
41 |
43 |
44 |
46 |
Comparative Examples 1-5
[0074] The polyester fibers of Comparative Examples 1-5 were prepared substantially according
to the same method as in Examples 1-5, except the conditions listed in the following
Table 3.
[Table 3]
Classifications |
Comparati ve Example 1 |
Comparati ve Example 2 |
Comparati ve Example 3 |
Comparati ve Example 4 |
Comparati ve Example 5 |
PET Content (mol%) |
100 |
100 |
100 |
100 |
100 |
Intrinsic Viscosity of Chip (dl/g) |
0.95 |
0.97 |
0.99 |
1.01 |
1.02 |
Spinning Temperature (°C) |
285 |
287 |
289 |
290 |
292 |
Drawing Ratio |
6.23 |
6.20 |
6.18 |
6.15 |
6.13 |
Heat-treatment Temperature (°C) |
210 |
213 |
215 |
218 |
220 |
[0075] The properties of the polyester fibers prepared according to Comparative Examples
1-5 are listed in the following Table 4.
[Table 4]
Classifications |
Comparati ve Example 1 |
Comparati ve Example 2 |
Comparati ve Example 3 |
Comparati ve Example 4 |
Comparati ve Example 5 |
Intrinsic Viscosity of Fiber (dl/g) |
0.60 |
0.65 |
0.70 |
0.85 |
0.88 |
Tensile Tenacity of Fiber (g/d) |
7.7 |
8.4 |
8.8 |
9.0 |
9.5 |
Elongation at Break of Fiber (%) |
14.3 |
12.5 |
12.7 |
13.7 |
11.5 |
Dry Heat Shrinkage Rate of Fiber (%) |
9.0 |
9.8 |
9.6 |
9.0 |
8.9 |
Monofilament Fineness of Fiber (DPF) |
3.7 |
2.8 |
3.9 |
52 |
52 |
Total Fineness of Fiber (de) |
1,400 |
1,400 |
1,000 |
5,000 |
5,000 |
Recovered Work Ratio at 10% of Maximum Load (%) |
64 |
65 |
65 |
68 |
64 |
Recovered Work Ratio at 20% of Maximum Load (%) |
44 |
45 |
47 |
46 |
44 |
Recovered Work Ratio at 30% of Maximum Load (%) |
39 |
39 |
36 |
37 |
35 |
[0076] Furthermore, Figs. 3 and 4 represent the strength-elongation curve of the polyester
fibers according to Example 4 and Comparative Example 1 measured at room temperature.
It is recognizable that the fiber of the present invention having long molecular chain
(high viscosity) shows high strength and elongation and has high recovered work ratio
as represented in Fig. 3, but the common polyester fiber of Comparative Example 1
shows remarkably deteriorated strength and elongation because of its low viscosity
and short molecular chain length as represented in Fig. 4.
Preparation Examples 1-5
[0077] The polyester fibers prepared according to Examples 1-5 were made into the fiber
ropes by applying S-twist in the first plaiting and Z-twist in the second plaiting.
At this time, 7 ply of the fibers were S-twisted in the first plaiting, 4 ply of the
S-twisted yarns were Z-twisted in the second plaiting, 16 ply of the plaited yarns
were made into one strand, and 8 ply of the strands were made into the rope finally.
The fiber ropes were prepared to have identical final fineness and the diameter of
the ropes was 36mm.
[0078] The properties of the polyester fiber ropes prepared according to above method were
measured by the following method.
a) Strength at Break and Elongation at Break
[0079] The strength at break and the elongation at break of the fiber rope were measured
by the method of fixing both ends of the rope to loops and moving one loop with a
speed of 1 m/min until the rope was broken.
b) Elastic Recovery
[0080] After checking the maximum load by measuring the strength at break and the elongation
at break of the rope, the recovered work ratio (%) of the rope was calculated according
to Calculation Formula 1 after repeating the elongation corresponding to 10%, 20%,
or 30% of the maximum load respectively and the release 10 times:

c) Moisture Absorption Rate
[0081] The weight of the rope was measured at the condition of 25 °C and relative humidity
of 65%RH. And then, the rope was dried at 100 °C for 6 hours by using a dryer and
the weight of the rope was measured. The moisture absorption rate at 25 °C and 65%RH
was calculated according to the following Calculation Formula 4:

d) Strength Maintenance Rate after Wetting
[0082] Tensile test was carried out according to the same method as in above strength measurement
immediately after wetting the rope in the water of room temperature for more than
30 minutes, and the strength maintenance rate after wetting was calculated according
to the following Calculation Formula 5:

e) Strength Maintenance Rate after UV Irradiation
[0083] The strength of the fiber rope was measured according to the same method as in above
strength measurement after irradiating the fiber rope with xenon arc light at 40 °C
and 65%RH for 100 hours. The strength maintenance after UV irradiation was calculated
according to the following Calculation Formula 6:

[0084] The properties of the fiber ropes of Preparation Examples 1-5 which were prepared
by using the polyester fibers of Examples 1-5 are listed in the following Table 5.
[Table 5]
Classifications |
Preparatio n Example 1 |
Preparatio n Example 2 |
Preparatio n Example 3 |
Preparatio n Example 4 |
Preparatio n Example 5 |
Strength at Break of Rope (Ton) |
26.6 |
26.8 |
27.8 |
28.5 |
29.5 |
Elongation at Break of Rope (%) |
23.5 |
24.6 |
25.3 |
26.1 |
27.4 |
Elastic Recovery at 10% of Maximum load (%) |
93 |
95 |
97 |
99 |
100 |
Elastic Recovery at 20% of Maximum load (%) |
63 |
66 |
74 |
70 |
78 |
Elastic Recovery at 30% of Maximum load (%) |
53 |
58 |
64 |
66 |
71 |
Moisture Absorption Rate (%) |
0.4 |
0.4 |
0.4 |
0.4 |
0.4 |
Strength Maintenance Rate After Wetting (%) |
100.1 |
99.8 |
99.9 |
100.3 |
100.5 |
Strength Maintenance Rate After UV irradiation (%) |
99.5 |
99.9 |
99.6 |
99.7 |
99.5 |
Comparative Preparation Examples 1-5
[0085] The fiber ropes were prepared substantially according to the same method as in Preparation
Examples 1-5, except that the polyester fibers of Comparative Examples 1-5 were used
respectively. The properties are listed in the following Table 6.
Comparative Preparation Example 6
[0086] The fiber rope was prepared substantially according to the same method as in
[0087] Preparation Examples 1-5, except that the nylon fiber (1,700d, strength 9.0g/d, elongation
26%) was used. The properties are listed in the following Table 6.
[0088] The properties of the fiber ropes of Comparative Preparation Examples 1-6 which were
prepared by using the polyester fibers of Comparative Examples 1-5 and nylon fiber
are listed in the following Table 6.
[Table 6]
Classifications |
Compa rative Prepara tion Exampl e1 |
Compa rative Prepara tion Exampl e2 |
Compa rative Prepara tion Exampl e3 |
Compa rative Prepara tion Exampl e4 |
Compa rative Prepara tion Exampl e5 |
Compa rative Prepara tion Exampl e6 |
Strength at Break (Ton) |
22.0 |
23.8 |
24.3 |
24.0 |
24.5 |
28.3 |
Elongation at Break (%) |
13.5 |
13.6 |
14.4 |
15.2 |
15.8 |
32.4 |
Elastic Recovery at 10% of Maximum load (%) |
74 |
77 |
78 |
75 |
78 |
85 |
Elastic Recovery at 20% of Maximum load (%) |
54 |
57 |
58 |
55 |
458 |
61 |
Elastic Recovery at 30% of Maximum load (%) |
45 |
47 |
46 |
48 |
49 |
53 |
Moisture Absorption Rate (%) |
0.4 |
0.4 |
0.4 |
0.4 |
0.4 |
4.2 |
Strength Maintenance Rate After Wetting (%) |
97.5 |
97.4 |
97.6 |
97.7 |
97.1 |
74.9 |
Strength Maintenance Rate After UV irradiation (%) |
96.2 |
96.4 |
96.8 |
97.2 |
97.5 |
74.3 |
[0089] As shown in Table 5, it is recognizable that the fiber ropes of Preparation Examples
1-5 made of the polyester fibers of Examples 1-5 having the high elastic recovery
show very superior properties, namely, the strength at break of 26.6 ton to 29.5 ton
and the elongation at break of 23.5% to 27.4%. At the same time, it is also recognizable
that the fiber ropes of Preparation Examples 1-5 show very low level of moisture absorption
rate at 25°C and 65%RH and very superior strength maintenance rate after wetting and
strength maintenance rate after UV irradiation, for example, the moisture absorption
rate at 25°C and 65%RH is about 0.4%, the strength maintenance rates after wetting
is 99.8% to 100.5%, and the strength maintenance rates after UV irradiation is 99.5%
to 99.9%. By this, it is recognizable that the fiber ropes of Preparation Examples
1-5 have superior light resistance, hydration resistance, wear resistance, low moisture
absorption rate, shock absorption performance, and the like in company with the superior
mechanical properties.
[0090] On the other hand, as shown in Table 6, it is recognized that the fiber ropes of
Comparative Preparation Examples 1-5 made of the polyester fibers of Comparative Examples
1-5 do not satisfy such characteristics. Particularly, it is recognizable that the
strength at break of the ropes of Comparative Preparation Examples 1-5 is merely 22.0
ton to 24.5 ton, the elongation at break is merely 13.5% to 15.8%, and thus the toughness
of the fiber rope is markedly inferior. If the toughness of the fiber rope is inferior
like this, it may be impossible to secure the mechanical properties sufficient for
anchoring or mooring a ship or for construction sites.
[0091] Furthermore, it is recognized that the fiber rope of Comparative Preparation Example
6 made of nylon fiber, one of common synthetic fiber, has markedly inferior properties,
for example, the moisture absorption rate at 25°C and 65%RH is 4.2%, the strength
maintenance rates after wetting is 74.3% and the strength maintenance rates after
UV irradiation is 74.9%. If the strength maintenance is inferior like this, it may
cause a problem of that the mechanical properties decrease rapidly under the rough
environment condition of the dockside for anchoring a ship.