[0001] The present invention relates to a process for the treatment of a fibrous structure
containing polyester.
[0002] According to the art the treatment of a polyester fibrous structure with an alkaline
reagent (in the following termed as "alkali treatment") developes a soft handle (in
the meaning of grip and/or feeling) of said polyester fibrous structure by partial
dissolution and removal of fiber material. Said alkali treatment is primarily important
for the manufacture of polyester fibrous structures comprising essentially one type
of polyester. Furthermore, it is known that the treatment of a fiber mixture consisting
of alkali easily soluble fibers and of alkali hardly soluble fibers with alkali can
lead to an excellent soft handle by dissolution and removal of the easily soluble
fibers. However, the latter treatment does not only need considerably long time in
order to completely dissolve the easily soluble fibers, but also may attack the hardly
soluble fibers in some extent; especially in case of hardly soluble fibers comprising
polyester said alkali treatment may lead to an unexpected deterioration of the physical
properties of the hardly soluble polyester fibers. On the other hand, if somebody
tries to shorten the period of treatment by making the easily soluble fibers still
more soluble in alkali the resulting very easily soluble fibers cannot withstand the
conventional conditions during mixing, blending, knitting and weaving processes due
to a deterioration of their physical properties. Furthermore, said very easily soluble
fibers suffer from certain difficulties during the fiber spinning (extruding) process.
At present, this latter method is not practically applied, though an outstanding soft
handle can be obtained.
[0003] The alkali treatment of conjugated (composite) fibers consisting of an alkali easily
soluble component and of an alkali hardly soluble component in order to remove one
component thereof and to obtain micro (ultra) fine and/or special shaped fibers rises
a still more serious problem, since those fine fibers which are designated to remain
within the alkali treated fibrous product are very often easily dissolved.
[0004] It is an object of the present invention to provide a process for the treatment of
a fibrous structure which structure comprises two components or more at least one
component thereof is intended to be removed, which treatment includes the removal
of said component(s) , and which process facilitates the removal of said component(s)
, avoids any significant deterioration of the physical properties of the remaining
component(s) and/or results in a better handle of the final product,
[0005] It is a further object of the present invention to provide said respective process
for the treatment of a fibrous structure which comprises a mixture of individual fibers
consisting of different materials.
[0006] It is a further object of the present invention to provide said respective process
for the, treatment of a fibrous structure which contains multi-component fibers, for
example so-called island-in-the-sea type fibers.
[0007] It is a still further object of the present invention to provide said respective
process for the treatment of a fibrous structure in order to remove at least one component
thereof, which represents a polyester.
[0008] As a result of intensive studies by the inventors to solve the above-mentioned problems
and objects a process has been established which allows to selectively dissolve only
the easily soluble component, especially an easily soluble polyester in a short time.
Therefore, the foregoing elucidated problems and objects are solved or greatly reduced
by the present invention.
[0009] In order to give a summary, the present invention provides a process for the treatment
of a fibrous structure which structure comprises two components or more, at least
one component thereof is a polyester containing S0
3M groups wherein M represents hydrogen or a metal, which process includes a pre-treatment
of the fibrous structure with a degrading ageht for said certain polyester prior to
the further treatment for the removal of said certain polyester preferably by a treatment
with an alkaline reagent (alkali treatment).
[0010] The process according to the present invention results not only in a soft and bonny
polyester fibrous structure with sufficient resilience but also enhance this the efficiency
of the alkali treatment.
[0011] Further objects, features and advantages of the present invention will be apparent
from the following detailed description of preferred embodiments thereof taken in
connection with the accompanying drawing wherein:
Figures 1 to 9 present cross-section views of exemplary conjugated fibers suited for
the treatment by the process of the present invention;
Figures 10 to 12 present cross-section views of the product obtained by removal of
the sea-component of the conjugated fiber according to figure 3.
[0012] According to the present invention the term "fibrous structure" is intended to include
the whole fiber itself and processed goods such as yarn, staple fiber, tow, top, woven
fabric, knitted fabric, and non-woven fabric, made from those fibers. Every type of
said fibrous structure may contain finishing agents such as silicone resin, melamine
resin and urethane resin. According to a distinctive feature of the present invention
the fibrous structure comprises two components or more at least one thereof is a polyester
containing S0
3M groups wherein M represents hydrogen or a metal. The arrangement of said components
within the fibrous structure includes mixtures of these separately spun components
obtained by subsequent mixing or blending processes or the like. Another type of arrangement
is a fibrous structure formed from conjugated fibers consisting of said two or more
components one of which is a 503M group containing polyester. A further type of arrangement
comprises a fibrous structure obtained by mixing conjugated fibers and ordinary fibers.
In other words, there are several types of the fibrous structure containing as the
removable component a S0
3M group containing polyester together with one or more other component(s) and the
present invention is not limited to any particular arrangement of said components.
[0013] In the fibers having a cross-section according to one of the figures 1 to 9 the component
A represents the easily soluble component which should be removed by the alkali treatment.
In the special case of conjugated fibers having the typical island-in-the-sea type
structure (for example according to figures 1, 2, 5 and 9), the sea component A is
generally the easily soluble component.
[0014] The easily soluble polyester component which should be removed by the alkali treatment
is a polyester containing S0
3M groups wherein M represents a metal, particularly an.alkali metal or an alkaline
earth metal or the hydrogen atom. Having in mind both, the spinnability of the fibers
forming the fibrous structure and the effectiveness of the alkali treatment after
the pre-treatment for degrading of the polyester component said removable polyester
component should be polyethylene terephthalate copolymerized with preferably 1-15
molar % more preferably with 3-5 molar % of 5-(sodium sulfo)isophthalic acid. The
one or more other component(s) forming the fibrous structure can be selected from
synthetic fibers such as polyester, polyamide and polyacryl fibers or from semi-synthetic
fibers such as acetate fibers, regenerated fibers such as rayon fibers and/or from
natural fibers such as cotton, wool and silk fibers, the material of all of said fibers
is rather more hardly soluble with respect to the alkaline reagent than the easily
soluble polyester component which should be removed by the alkali treatment.
[0015] The benefits of the' present invention are particularly remarkable in connection
with polyester fibers which actually are hardly soluble but not highly resistant with
respect to the alkaline reagent and the conditions used in the alkali treatment.
[0016] The terms "easily soluble" and "hardly soluble" as used herein describe the solubility
of the components forming the fibrous structure at the situation before the removal
treatment with alkaline reagent but after the pre-treatment with the degrading agent.
[0017] The alkali treatment results in a hydrolysis of the selected polyester with an alkaline
reagent. Good results may be obtained with an alkali treatment using the following
conditions: (1) maintaining the fibrous structure for 30-120 min within a boiling
aqueous solution of an alkaline reagent such as for example sodium hydroxide, or (2)
impregnating the fibrous structure with an alkaline reagent and maintaining the impregnated
fibrous structure for 10-30 hours at 40-60°C or (3) impregnating the fibrous structure
with an alkaline reagent and allowing the action of dry heat or superheated steam
for 1-5 min at 130-200°C. Without intending any limitation the alkaline reagent for
the alkali treatment can be selected from typical and known alkaline substances such
as alkali metal hydroxides for example sodium hydroxide, potassium hydroxide, and
the like or alkaline earth metal hydroxide for example calcium hydroxide, barium hydroxide
and the like or other basic salts for example sodium carbonate, potassium carbonate
and the like. Beside$ the above-stated and preferably used conditions for the alkali
treatment any other suited method for removal of at least one component of the fibrous
structure can be applied, provided stable working conditions are maintained and the
remaining fiber(s) of the treated fibrous structure remains essentially uneffected.
[0018] A key feature of the process according to the present invention is thepre-treatment
of the fibrous structure prior to the mentioned alkali treatment, The intention of
said pre-treatment is a degrading of the selected polyester which should be removed
afterwards. The degrading may yield in a lower average molecular weight of said certain
polyester and/or may in any other way promote the effect of the alkali treatment.
The degrading agents suited for the pre-treatment of polyester in the process of the
present invention include for example amines such as ethylenediamine, ethylene- triamine
and the like, further monoethanolamine and similar compounds, further zinc salts such
as zinc chloride, zinc sulfate, zinc nitrate and the like, further oxidizing agents
such as hydrogen peroxide, sodium hypochlorit, sodium chlorit, and further typical
acidic compounds, for example inorganic acids such as hydrochloric acid, sulfuric
acid, nitric acid, phosphoric acid and the like or organic acids, for example formic
acid, oxalic acid and the like. Especially acidic compounds have proven to be particularly
appropriate, because they selectively degrade the S0
3M groups containing polyester. Therefore said acidic compounds are preferably used
as degrading agents in the pre-treatment of the process according to the present invention.
[0019] The degrading pre-treatment can be effected in several ways, for example by the following
processes:
(1) By immersing the fibrous structure for about 10-120 min into a boiling aqueous
solution containing the degrading agent;
(2) by adding the degrading agent to the fibrous structure and the subsequent action
of saturated vaporfor about 1to30 min at 100-130°C;
(3) by adding the degrading agent to the fibrous structure and the subsequent action
of dry heat or superheated steam for about 1-10 min at 130-220°C;
(4) or by adding the degrading agent to the fibrous structure followed by the continued
reaction for 10-30 hours at 40-60°C.
[0020] The degrading pre-treatment is by no way limited to the above-listed methods. Indeed
any suited process can be applied which results in a lowering of the average molecular
weight of the selected polyester by the action of the degrading agent(s). Regarding
the treatment with acid in a boiling aqueous solution preferred conditions look for
a treatment at a pH-value below 2 for about 30 min at 110-140°C or at a pH-value of
about 3 for 60 min at 110-140°C. The addition of selected additives to the treating
bath for example such as carrier agent, surfactant agent or quaternary ammonium salt
can even improve the results of the action of the degrading agent.
[0021] In the following there are stated some results of the characteristic features of
the process according to the present invention in comparison with conventional processes:
(1} According to a conventional process the treatment of a fibrous structure comprising
blended yarn or mixed filament yarn in order to remove the desired component needs
a rather long treatment period which often yields to an substantial deterioration
of the remaining fibers. To the contrary the process according to the present invention
requires a significant shorter treatment period and provides a fibrous structure with
a better handle without loss of physical properties of the remaining fibers.
[0022] This highly desired result is obtained without any impairing of spinning and/or weaving
conditions of the fibers. As stated earlier some very easily soluble fibers can be
rapidly removed by an alkali treatment however the manufacturing conditions of those
very easily soluble fibers provides difficulties with respect to stable spinning or
weaving conditions. To the contrary, the process according to the present invention
does not impair the manufacturing of the fibers, because the distinctive pre-treatment
with a selected degrading agent for the polyester promotes the hydrolysis rate in
an alkaline environment.
[0023] (2) The process according to the present invention proves to be particularly effective
for the treatment of island-in-the-sea-type conjugated fiber both components thereof
comprises polyester wherein one polyester component is more easily soluble in the
alkaline reagent used for alkali treatment. If somebody tries to remove the easily
soluble component (A) of island-in-the-sea-type fibers according to figure 3 only
the fibers shown in figure 11 can be obtained, because in addition to the component
(A) a part of the hardly soluble component (B) is also dissolved during the alkali
treatment. To the contrary the process according to the present invention allows a
complete removal of the component (A) prior to the hydrolysis of component (B) starts
and therefore the inventive process finally leads to fibers having a cross-section
according to figure 10. In fact the process according to the present invention allows
to maintain the original shape of the island components during the removal of the
sea component. Therefore, if an island-in-the-sea-type fiber as shown in figure 1
is treated along the process according to the present invention, the respective independent
islands can be obtained separately with minimum damage of the island component in
the outside portion thereof. To the contrary, the conventional process sometimes dissolve
the outside portion of the island component before the island component located within
the inner section of the fiber have been separated.
[0024] (3) The degrading pre-treatment according to the present invention increases the
effectiveness of the subsequent alkali treatment, this means the so-called alkali
reduction rate of the selected polyester. It is known in the art, that said alkali
reduction rate can also be increased by the conventional process, if a quaternary
ammonium salt is used during the alkali treatment. The presence of the ammonium salt
increases the alkali reduction rates of both components, the polyester intended to
be removed and the other component which should remain in the treated fibrous structure.
To the contrary the degrading pre-treatment according to the present invention allows
to increase selectively the alkali reduction rate of only the one component, which
should be removed afterwards. Therefore, the conventional process does not attain
the same effect as the process according to the present invention, even if the conventional
process uses a quaternary ammonium salt during the alkali treatment.
[0025] The following examples are provided for a further illustration of the process according
to the present invention. These examples serve only for illustration purposes and
are not to be construed as limiting the scope of the present invention.
Example 1.
[0026] A fabric in taffeta weave has been woven from island-in-the-sea-type fibers (75 denier,
36 filaments) as shown in figure 3, using said fibers for both warp and weft yarn.
The specifications of the used fibers are the following:
Component A: Polyethylene terephthalate copolymerized with 4 molar % of 5-(sodium
sulfo) isophthalic acid;
Component B: Polyethylene terephthalate; Ratio A:B: 30:70
[0027] For effecting the degrading pre-treatment said fabric was immersed in a boiling 1
% aqueous sulfuric acid solution for 60 min. Subsequently the alkali treatment was
effected in order to completely remove the component A by immersing said pre-treated
fabric in a boiling 1.5 % aqueous sodium hydroxide solution for 4 min. After removal
from the alkaline bath and drying the fabric shows a weight reduction in the amount
of 30.5 %. Thereafter the fabric was dyed using an conventional method. The dyed fabric
provided a mild color tone, high water absorption, excellent handle (in the meaning
of grip and/or feeling) and was free from the problems originated from yarn slippage
and a reduction of yarn tenacity. An investigation of the cross-section of the obtained
fibers yields sharp edges such as shown in figure 10.
Comparative example 1:
[0028] The fabric as mentioned in example 1 has been treated directly with the boiling 1.5
% aqueous sodium hydroxide solution therefore omitting any degrading pre-treatment
with sulfuric acid. The complete removal of the component A took 110 min and yielded
a weight reduction of the treated and dried fabric in the amount of 48%. This far
higher weight reduction indicates that the alkali treatment does not only remove the
component A but also remove in an significant amount the component B.
Comparative example 2:
[0029] The fabric according to example 1 has been treated in the boiling 1.5 % aqueous sodium
hydroxide solution in the additional presence of 0.8 % DYK-1125 (a quaternary ammonium
salt available from Ippo Co., Ltd.). The component A was completely removed in a short
period of 15 min. However the treated and dried fabric shows a weight reduction in
the large amount of 65 %, indicating that the component B has been removed in a rather
high extent.
[0030] The fabrics obtained to comparative examples 1 and 2 have been dyed by an conventional
method. The dyed fabrics show a considerable yarn slippage and poor tenacity. The
tenacity has been determined with the Elmendorf tearing tester apparatus. The results
are the following:

[0031] The process according to the comparative examples 1 and 2 realize the valuable properties
of the inventive treated product in a far less amount. The fibers obtained by the
comparative examples 1 and 2 show a fiber cross-section in some extent as shown in
figures 11 and 12, indicating that the original shape of component B has been deformed.
Example 2:
[0032] From the starting components 20 % staple fiber of polyethylene terephthalate copolymerized
with 4 molar % of 5-(sodium sulfo) isophthalic acid, and 80 % wool fiber blended yarn
has been prepared. Said yarn was woven into a twill structure and from the obtained
twill structure a fabric has been manufactured by conventional twilling process.
[0033] In order to effect the degrading pre-treatment according to the present invention
said fabric was immersed in a boiling 0.5 % aqueous hydrochloric acid solution for
60 min. The subsequent alkali treatment for completely removal of the polyester component
was effected by immersing the pre-treated fabric in a boiling 0.1 % aqueous sodium
hydroxide solution for 35 min. Thereafter the fabric was dyed by a conventional method.
The obtained wool fabric showed an outstanding capability connected with an excellent
handle.
Comparative example 3:
[0034] The same fabric as mentioned in example 2 was treated directly in the boiling 0.1
% aqueous sodium hydroxide solution for 35 min omitting any degrading pre-treatment
with aqueous hydrochloric acid solution. Said alkali treatment was insufficient to
remove the polyester component completely. After a conventional dyeing process the
obtained dyed fabric do not show the characteristic features of the fabric obtained
by the inventive process.
Comparative example 4:
[0035] The same fabric as mentioned in example 2 was treated in a boiling 1.5 % aqueous
sodium hydroxide solution omitting any degrading pre-treatment with hydrochloric acid
solution. The alkali treatment was effected for a sufficient period in order to remove
the polyester component completely. The investigation of the weight reduction proved,
that said longer alkali treatment removed in addition a significant part of the wool
component. The finally obtained fabric was completely different to the product of
the process according to the present invention.
Example 3:
[0036] A sample hosiery was prepared by knitting island-in-the-sea-type fibers (225 denier,
24 filaments) having a cross-section as shown in figure 1. The specifications of the
used fibers are as follows:
Component A: Polyethylene terephthalate copolymerized with 4 molar % of 5-(sodium
sulfo) isophthalic acid;
Component B: Polyethylene terephthalate;
Ratio A:B: 22:78;
Denier of component B in monofilament: 0.2 den;
Component B: 36 filaments.
[0037] The degrading.pre-treatment of said sample hosiery was effected by immersing said
hosiery in a 10 % aqueous phosphoric acid solution for 30 min at 130°C. The subsequent
alkali treatment was effected by introducing the pre-treated sample in a boiling 1.5
% aqueous sodium hydroxide solution for 4 min. The combined results of both treatments
is a complete removal of the component A and a final product comprising a beatiful
hosiery knit consisting of micro fine fibers. The weight reduction amounts 22.2 %.
An investigation of the cross-section of the remaining micro fine fibers proved that
the island portions have not been reduced substantially; the tenacity of these micro
fine fibers amount 730 g/ filament.
Comparative example 5:
[0038] A further sample of the same hosiery as used in example 3 was treated directly in
the boiling 1.5 % aqueous sodium hydroxide solution, therefore omitting any degrading
pre-treatment with aqueous phosphoric acid solution. In order to succeed in a complete
removal of the component A an alkali treatment period as long as 150 min was necessary.
Said long alkali treatment yielded in a weight reduction of 44.0 %, proving a significant
removal of polyethylene terephthalate microfine fibers. In fact a weight lost of the
micro fine fibers in an average value of approximately 30 % has been established.
The tenacity of the remaining micro fine fibers has been decreased as low as 330 g/filament.
[0039] In addition,the micro fine fibers obtained by the process of the present invention
according to the example 3 showed a uniform fiber thickness of 0.2 den, while the
respective micro fine fibers obtained according to the comparative example 5 showed
a large fluctuation of fiber thickness in the range of 0.1-0.2 den.
[0040] Although the present invention has been described with reference to the specific
details of particular embodiments it will be obvious to those skilled in the art that
various changes and modifications may be made therein without departing from the invention,
and it is, therefore, aimed in the appended claims to cover all such changes and modifications
as fall within the true spirit and scope of the present invention.
1. A process for the treatment of a fibrous structure which structure comprises two
components or more at least one component thereof comprises a polyester, in order
to remove the polyester component, characterized in that
the removable polyester component contains S03M groups wherein M represents hydrogen or a metal, and prior to that removal treatment
there is provided a pre-treatment of the fibrous structure with a degrading agent
for said S03M qroups containing polyester.
2. A process according to claim 1,
wherein said removal treatment is effected by the action of an alkaline reagent.
3. A process according to claim 1 or 2,
wherein said degrading agent comprises an acid medium.
4. A process according to claim 3,
wherein said acid medium is an inorganic acid.
5. A process according to claim 4,
wherein said inorganic acid is used in the form of a diluted boiling aqueous acidic
solution.
6. A process according to anyohe of the claims 1 to 5, wherein the fibrous structure
comprises a mixture of two or more types of polyester fibers consisting of different
polyester compositions.
7. A process according to anyone of the claims 1 to 5, wherein the fibrous structure
comprises multi-component fibers made from two or more polyester components having
different polyester compositions.
8. A process according to claim 7,
wherein the multi-component fiber provides a plurality of cores within the fiber cross-section,
and the S03M groups containing polyester forms the material between said cores.
9. A process according to claim 7 or 8,
wherein the multi-component fiber comprises at least 5 cores within the fiber cross-section.
10. A process according to claim 7 or 8,
wherein the multi-component fiber comprises at least 10 cores within the fiber cross-section.