U.S. patent application number 16/434756 was filed with the patent office on 2019-09-19 for microfibrous fabric having a suede appearance, within the colour range of grey and black, with a high light fastness, and prepar.
The applicant listed for this patent is ALCANTARA S.P.A.. Invention is credited to Carmine Carlo AMMIRATI, Walter CARDINALI, Omar TEOFRASTI.
Application Number | 20190284754 16/434756 |
Document ID | / |
Family ID | 40301772 |
Filed Date | 2019-09-19 |
United States Patent
Application |
20190284754 |
Kind Code |
A1 |
AMMIRATI; Carmine Carlo ; et
al. |
September 19, 2019 |
MICROFIBROUS FABRIC HAVING A SUEDE APPEARANCE, WITHIN THE COLOUR
RANGE OF GREY AND BLACK, WITH A HIGH LIGHT FASTNESS, AND
PREPARATION METHOD THEREOF
Abstract
A high-quality artificial leather is described, having a suede
appearance and colors within the grey-black range, the light
fastness of the colors according to the method SAE J 1885 225.6
KJ/m.sup.2 being higher than or equal to 4; the lightfastness of
the colors according to the method SAE J 1885 488.8 KJ/m.sup.2
being not lower than 3; said artificial leather having a tassel on
the surface of the leather itself. The average length of the tassel
is between 200 and 500 microns. The soft segments consist of at
least one polycarbonate diol selected from polyalkylene carbonate
diols and at least one polyester diol; the hard segments consist of
urethane groups deriving from the reaction between free isocyanate
groups and water; and the total content of carbon black is between
0.025 and 6% by weight.
Inventors: |
AMMIRATI; Carmine Carlo;
(Terni, IT) ; TEOFRASTI; Omar; (Avigliano Umbro,
IT) ; CARDINALI; Walter; (Cerqueto di Marsciano,
IT) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
ALCANTARA S.P.A. |
Milano |
|
IT |
|
|
Family ID: |
40301772 |
Appl. No.: |
16/434756 |
Filed: |
June 7, 2019 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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15469063 |
Mar 24, 2017 |
10351993 |
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16434756 |
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12993213 |
Nov 17, 2010 |
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PCT/IT2008/000739 |
Dec 3, 2008 |
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15469063 |
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Current U.S.
Class: |
1/1 |
Current CPC
Class: |
D01F 8/14 20130101; D06N
3/147 20130101; D06N 3/007 20130101; D06N 3/14 20130101; D01F 8/10
20130101; D10B 2505/12 20130101; D06N 3/0063 20130101; D06N 3/0075
20130101; D06N 3/0011 20130101; Y10T 428/24994 20150401; D06N
2211/00 20130101; D01D 5/082 20130101; D06N 2203/068 20130101; D06N
2201/0227 20130101; D06N 3/0004 20130101; D06N 3/146 20130101; D06N
3/0036 20130101; D06N 3/148 20130101 |
International
Class: |
D06N 3/00 20060101
D06N003/00; D06N 3/14 20060101 D06N003/14; D01F 8/10 20060101
D01F008/10; D01D 5/08 20060101 D01D005/08; D01F 8/14 20060101
D01F008/14 |
Foreign Application Data
Date |
Code |
Application Number |
Jun 10, 2008 |
IT |
MI2008A001055 |
Claims
1. A non-woven artificial leather having a suede appearance and
comprising a non-woven microfibrous component and an elastomeric
matrix, wherein said artificial leather has a color shade within
the grey-black range, the light fastness of the color shade being
higher than or equal to 4, according to the method SAE J 1885 225.6
KJ/m.sup.2, and not lower than 3, according to the method SAE J
1885 488.8 KJ/m.sup.2; wherein said non-woven microfibrous
component comprises 0.05 to 2% by weight carbon black; wherein said
elastomeric matrix comprises at least one polyurethane and from
0.02% to 10% by weight of carbon black; and wherein said non-woven
artificial leather has a tassel on the surface of the leather
having an average length of 210 to 500 microns.
2. The artificial leather according to claim 1, wherein said tassel
has an average length of 300 to 500 microns.
3. The artificial leather according to claim 1, wherein said tassel
has an average length of 210 to 400 microns.
4. The artificial leather according to claim 1, wherein said tassel
has an average length of 300 to 400 microns.
5. The artificial leather according to claim 1, wherein said tassel
has an average length of 350 to 400 microns.
6. The artificial leather according to claim 1, wherein said tassel
has an average length of 300 to 350 microns.
7. The artificial leather according to claim 1, wherein said tassel
has an average length of 320 to 370 microns.
8. The artificial leather according to claim 1, wherein the
elastomeric matrix and the non-woven microfibrous component are
present in a ratio ranging from 20/80 to 50/50 by weight.
9. The artificial leather according to claim 1, wherein the
non-woven microfibrous component comprises polyester microfibres
having a count of 0.01 to 0.50 dtex.
10. The artificial leather according to claim 1, wherein the
microfibrous component comprises polyethylene terephthalate
microfibres.
11. The artificial leather according to claim 1, wherein the
microfibrous component comprises 0.15 to 1.50% by weight carbon
black.
12. The artificial leather according to claim 1, wherein the
elastomeric matrix comprises 0.02 to 7% by weight carbon black.
13. The artificial leather according to claim 1, wherein the
elastomeric matrix comprises 0.02 to 6% by weight carbon black.
14. The artificial leather according to claim 1, wherein the
elastomeric matrix comprises at least one polyurethane; said at
least one polyurethane being made up soft and hard segments; said
soft segments comprising at least one polyalkylenecarbonate diol
and at least one polyester diol, and said hard segments comprising
urethane and/or ureic groups derived from the reaction between free
isocyanate groups and water.
15. The artificial leather according to claim 14, wherein the at
least one polyester diol is selected from the group consisting of
polyhexamethylene adipate diol (PHA), poly(3-methylpentamethylene)
adipate diol (PMPA), polyneopentyl adipate diol (PNA), and
polycaprolactone diol (PCL); the at least one polyalkylenecarbonate
diol is selected from the group consisting of polytetramethylene
carbonate diol (PTMC), polypentamethylene carbonate diol (PPMC),
polyhexamethylene carbonate diol (PHC), polyheptamethylene
carbonate diol, polyoctamethylene carbonate diol, polynonamethylene
carbonate diol, polydecamethylene carbonate diol,
poly-(2-methyl-pentamethylene carbonate)diol, and
poly-(2-methyl-1-octamethylene carbonate) diol; and the isocyanate
groups are derived from methylene-bis-(4-phenylisocyanate) (MDI)
and/or from toluene diisocyanate (TDI).
16. The artificial leather according to claim 1, wherein the
overall content of carbon black ranges from 0.025 to 6% by
weight.
17. The artificial leather according to claim 1, wherein the
overall content of carbon black ranges from 0.085 to 3.75% by
weight.
18. The artificial leather according to claim 1, wherein the carbon
black has an average dimension lower than 0.4 microns.
19. The artificial leather according to claim 1, wherein the color
shade is characterized by a value of "L" <70, wherein said value
is measured before the artificial leather is subjected to an
over-dyeing treatment.
20. The artificial leather according to claim 19, wherein the color
shade is characterized by a value of "L" <55, wherein said value
is measured before the artificial leather is subjected to an
over-dyeing treatment.
Description
[0001] This application is a continuation application of U.S.
patent application Ser. No. 15/469,063, filed Mar. 24, 2017, which
is a divisional of U.S. patent application Ser. No. 12/993,213,
filed Nov. 17, 2010, which a 35 U.S.C. .sctn. 371 national-stage of
International PCT Application No. PCT/IT2008/000739, filed Dec. 3,
2008, which claims priority to Italian Patent Application No.
MI2008A001055, filed Jun. 10, 2008, all of which are herein
incorporated by reference in their entirety.
[0002] The present invention relates to a high-quality artificial
leather, having a suede appearance and colours within the range of
grey and black, characterized by an high colour fastness when
exposed to light and a long durability, destined for use in car
interiors.
[0003] The definition "high fastness" means high resistance of the
colour shade to undergoing variations following prolonged exposure
to light.
[0004] The definition "high durability" means high resistance of
the suede leather, capable of lasting for long periods of time,
even following long and repeated exposure to light and particularly
oxidizing and/or hydrolyzing environments.
[0005] The process necessary for producing artificial leather with
a high fastness is also part of the present invention.
[0006] The synthetic leather with a suede appearance, object of the
present invention, even if characterized by the properties of high
fastness to light and a long durability, can be compared, in its
most general characteristics, to already known composite structures
consisting of a surface having a high microfibre density and a
matrix of the elastomeric type binding the same microfibre
structure. The methods already used for the production of
high-quality synthetic leathers having a suede effect (see, for
example, EP-A-0584511, EP-A-1323859, US-B-7144535, US-A-3531368,
US-A-3716614) are all characterized by a process which can be
schematized as follows: [0007] A1) Spinning of a bi-component fibre
of the "sea-island" type, in which the "island" component consists
of a polyester and/or polyamide and the "sea" component of a
polymer immiscible in the island component and capable of
dissolving in suitable solvents of an organic or inorganic nature.
The micro-fibres obtained after dissolution of the sea component
have counts typically lower than 0.5 dtex. [0008] A2) Preparation
of a felt characterized by well-defined density values and a
unitary weight, by means of a mechanical needling process capable
of connecting the microfibres obtained in item A1. [0009] A3)
Impregnation of the felt with a binder capable of withholding the
"islands" during the subsequent elimination phase of the "sea"
component. Said binder, which also has the function of suitably
reinforcing the felt to such an extent as to allow its immersion in
the solvent used for eliminating the "sea", can be of two different
typologies. [0010] The first is typically based on polyvinyl
alcohol, which is removed in a subsequent step of the process.
[0011] The second is typically based on polyurethane which
partially or totally remains in the final product, even after the
subsequent process steps. [0012] A4) Dissolution of the "sea"
component in a suitable organic (generally trichloroethylene) or
inorganic (acidic or basic aqueous solution, or simply in hot
water) solvent to give the microfibrous material. [0013] A5)
Impregnation of the above-mentioned microfibrous material with a
polyurethane (PU) solution in organic solvents (dimethyl formamide,
DMF); as an alternative, said impregnation can be effected with
polyurethane in emulsion or aqueous dispersion (PUD). [0014] A6)
Elimination of the binder used in point A3 if the binder is not PU
or PUD and of the solvent possibly used in step A5. [0015] A7) The
microfibrous material impregnated with polyurethane is cut into two
equal portions, by means of a longitudinal cut, parallel to the
surfaces. [0016] A8) Grinding of the surfaces of the product by
means of suitable treatment with abrasive papers, in order to
confer the suede appearance to the structure. [0017] A9) Final
dyeing of the product. [0018] A10) Finishing treatment (coupling
with other substrates, printing, etc..).
[0019] With reference to the dyeing process, it should be pointed
out that the methods generally used for dyeing non-woven fabrics
based on polyester, include dyeing the micro-fibrous component
(tassel) by immersion of the material in baths containing dyes of
the "dispersed" type. The use of dispersed dyes only, does not
require any dyeing of the polyurethane matrix which therefore
maintains its original colour as it cannot be solidly dyed using
this group of dyes. The dyeing process is concluded by a reducing
cleaning step carried out by means of sodium hydrosulphite in NaOH,
with the aim of removing the excess of dyes still present and
unfixed on the material.
[0020] The colouring difference between tassel and polyurethane
matrix is normally critical, as the visibility of the background
influences negatively the aesthetical impact of the final
product.
[0021] In order to minimize the above-mentioned colour difference
between tassel and polyurethane matrix, various countermeasures are
normally adopted: [0022] addition of organic or inorganic pigments
to the polyurethane itself, before the impregnation process; [0023]
resort to a second dyeing bath after the standard bath described
above, in which so-called "pre-metallized" dyes are used, capable
of dyeing the polyurethane base and thus limiting the deterioration
in quality attributable to the colour difference (see patents IT
1097917, IT 1256230); [0024] optimization of the tassel length, in
order to find the correct compromise between "coverage" of the PU
background, imitation of real suede leather and protection of the
writing and mottling effects: an excessively short tassel, in fact,
it does not reduce the visibility of the PU on the "noble" surface
of the product and decreases its qualitative level because it
reduces both two effects mentioned above.
[0025] With reference to the last aspect described, it should be
noted that, due to its high surface density, the micro-fibrous
component strongly characterizes the quality of the "visible" side
of synthetic leathers with a suede appearance, contributing, much
more than the binding matrix, to the conferment of properties such
as colour shade, mottling, the writing effect and soft feel, which
represent the main parameters for a qualitative evaluation of this
type of non-woven fabric.
[0026] The products obtained as describe above, normally have some
limits in the invariability of the colour shade after light
exposure. This limited colour fastness to light significantly
conditions the applicative potentialities, in particular to the
field of car interiors, which represents one of the reference
markets for high-quality synthetic leathers which are widely used
in the lining of car interiors.
[0027] For this reason, the colour fastness after exposure to light
of synthetic leathers is carefully evaluated by means of various
analytical methods which comprise the exposure of test samples to
artificial light sources under controlled irradiation and humidity
conditions.
[0028] Unfortunately, there is currently no single analytical
method for the evaluation of colour fastness to light and each car
producer adopts a specific method. Normally the various methods use
Xenon lamps in order to reproduce the solar irradiation spectrum as
accurate as possible; the irradiation spectrum can also include
radiations with wave- lengths ranging from 270 to 700 nm and the
temperature of the exposure chamber can reach 60-70.degree. C.
[0029] In Europe, the most widely-used methods are DIN 75 202 PV
1301, D47 1431 and SAE J1885. In the USA market the most
widely-spread method is FLTM B0116-01 in addition to SAE J1885. The
following table shows the main test conditions:
TABLE-US-00001 Black Chamber Exposure Method Apparatus Lamp panel
temperature Humidity time Irradiation DIN75202 Xenotest Beta Xenon
100 .+-. 2.degree. C. 65 .+-. 5.degree. C. 20 .+-. 10% 1, 2 and 3
60 W/m.sup.2 PV 1303 (Heraeus) Fakra cycles 300 / 400 nm D47 1431
Atlas CI3000 Xenon 100 .+-. 2.degree. C. 66.degree. C. .+-.
2.degree. C. 30 .+-. 10% 150 hrs 1.4 W/m.sup.2, (Heraeus) 420 nm
SAEJ1885 Atlas CI3000 Xenon light 62 .+-. 2.degree. C. 50 .+-. 5%
225.6 KJ/m.sup.2 0.55 W/m.sup.2, (Heraeus) 89 .+-. 2.degree. C. 38
.+-. 2.degree. C. 95 .+-. 5% 340 nm dark 38 .+-. 2.degree. C. light
62 .+-. 2.degree. C. 50 .+-. 5% 488.8 KJ/m.sup.2 0.55 W/m.sup.2, 89
.+-. 2.degree. C. 38 .+-. 2.degree. C. 95 .+-. 5% 340 nm dark 38
.+-. 2.degree. C. FLTM Atlas CI4000 Xenon + light 62 .+-. 2.degree.
C. 50 .+-. 5% 451-902 KJ/m.sup.2 1.06 W/m.sup.2, BO116-01 auxiliary
89 .+-. 2.degree. C. 38 .+-. 2.degree. C. 95 .+-. 5% 420 nm lamp
dark 38 .+-. 2.degree. C. light 62 .+-. 2.degree. C. 50 .+-. 5%
942-3224 KJ/m.sup.2 1.06 W/m.sup.2, 89 .+-. 2.degree. C. 38 .+-.
2.degree. C. 95 .+-. 5% 420 nm dark 38 .+-. 2.degree. C.
[0030] The evaluation of the colour fastness to light is effected
by comparing the colour variation before and after exposure with
the grey scale ISO 105A02.
[0031] Various countermeasures are now adopted in order to maximize
the resistance of the colour shade following exposure to light. One
of the most common and efficient is to add organic or inorganic
pigments to the polymer used for the production of microfibres,
upstream of the spinning phase (mass dye technology).
[0032] The mass dye technology does in fact allows the use of
organic or inorganic pigments having a high fastness to light,
which cannot normally be applied in water bath dyeing.
[0033] For the classical dyeing of polyester, in fact, it is only
possible to use organic dyes, dispersible in water, capable of
being diffused inside the polyester fibre. In the case of the
dyeing of a polyester microfibre, it is necessary to provide of
molecules having small dimensions in order to obtain good dyeing
yields in a short time.
[0034] The use of additional polymers with pigments in the spinning
process, however, has also considerable drawbacks, such as: [0035]
increase in the obstruction process of the filtering screens
situated upstream of the spinnerets for protective purposes. The
acceleration of the obstruction phenomena implies an increase in
the frequency with which the filter screens must be substituted and
therefore a considerable increase in the production costs; [0036]
decrease in the mechanical properties of the micro-fibrous
component of the fibre with a consequent reduction of the
mechanical properties of the synthetic leather produced with
it.
[0037] In order to limit the drawbacks listed, an accurate
selection of the pigment used is necessary, with particular
reference to the dimensions of its particles and to its
filterability, as well as the percentage of its addition to the
polymer. It should in fact be considered that higher pigment
contents allow the production of synthetic fibres characterized by
deeper colour shades but they also imply more frequent obstructions
of the filtering systems positioned for the protection of the
spinnerets and greater reductions in the mechanical properties of
the same fibres.
[0038] The production of high-quality synthetic leathers therefore
requires an optimal compromise between the two mentioned factors,
also resorting to alternative solutions, when necessary, for
obtaining a certain colour shade. As the "overall" colour shade of
a synthetic suede leather can be attributed to both the
microfibrous (main) component and to the polyurethane matrix, one
of the possible known solutions for obtaining dark colours is to
limit the micro-fibrous tassel length, so as to only partially
cover the polyurethane base and to profit by the contribution of
its "background" colour to obtain the desired colour shade (see
patent EP 1403421 in which the tassel length is from 10 to 200
.mu.m). The expedient described above, however, has also serious
drawbacks as it strongly conditions the qualitative level of the
synthetic leather due to the limited writing and mottling effect
obtained by means of a reduced length of the tassel.
[0039] The measurement of the colour shade is normally carried out
by instrumental reading of the colour and by visual comparison with
a reference standard (mainly in the case of synthetic leather with
a suede appearance such as that object of the present invention).
Instruments and reading techniques are well-known to experts in the
field. The need for a visual comparison is due to the different
sensitivity of the human eye with respect to the instruments on the
market, but, above all, to the specific surface of these types of
materials which are characterized by the presence of tassels, which
leads the eye to perceive different colour shades according to the
inclination of the microfibre with respect to the observer. Several
models have been prepared in order to reproduce, by means of
instrumental analyses, the same colour perception of the human eye.
One of the most simple and widespread is called CIELAB system. This
system is based on the representation of colours by means of three
coordinates defined by the letters L, a and b, arranged in a
Cartesian reference system. L represents luminosity and can have
values from 100 (white) to 0 (black), whereas the other two
coordinates (a, b), perpendicular to the former, identify the
chromaticity of the colour and can have values ranging from +80 to
-80: negative values for a denote the presence of a green
component; positive values of a red component; negative values for
b denote the presence of a blue component; positive values of a
yellow component. The colour difference between two measurements
can be expressed as Cartesian distance between the coordinates
relating to the two measures. Even if this model has not yet
substituted visual comparison with respect to a standard sample
effected by an expert (mainly during the formulating phase of the
colour formulation), it is very useful in the preliminary
evaluation of the material analyzed and for providing an assessment
term in the discussion and comparison with other subjects (such as
customers and suppliers).
[0040] In addition to the property of colour fastness to light, all
high-quality synthetic suede leathers, in order to be widely used,
must have a high and long-lasting mechanical resistance. This
characteristic, commonly identified as "durability" can be
evaluated by subjecting the synthetic leather to aging according to
two types of tests: [0041] UV aging, carried out in a particular
apparatus (Xenotest .beta.) under well-defined conditions of
relative humidity (20.+-.10%), temperature (100.+-.3.degree. C.),
irradiation (60 W/m.sup.2) and time (138 hours), corresponding to a
duration cycle of 3 fakra. [0042] hydrolyzing aging (Jungle test)
carried out in a climatic camera under well-defined conditions of
temperature (75.+-.1.degree. C.), relative humidity (90.+-.3%) and
duration (5-7-10 weeks).
[0043] The aging of the material is then analyzed in terms of
variation of appearance, abrasion resistance, variation of the
physical-mechanical properties and, with respect to the
polyurethane matrix only, variation of average Molecular Weights of
the polymeric chains.
[0044] At present, the objective of a satisfactory durability of
synthetic leathers has already been reached by using suitable
polyurethane matrices, characterized in that they include "hard"
segments, consisting of urethane and/or ureic groups (obtained from
the reaction between free isocyanate groups and water) and "soft"
segments consisting of a mixture of
polycarbonate-diols/polyester-diols in a ratio ranging from 80/20
to 20/80 (see U.S. Pat. No. 7,144,535).
[0045] So far, polyurethane matrices capable of conferring
properties of high durability, have never been used for the
production of synthetic leather also characterized, by a high
colour fastness to light obtained by the addition of pigments to
the molten polymer used for the production of the microfibre.
[0046] An object of the present invention is to provide a
high-quality artificial leather with a suede appearance mainly
intended to use in the field of car interiors, with colours in the
range of grey and black, at the same time having a high fastness to
light and a long durability.
[0047] It has been discovered that, by suitably combining the right
quantitative ratios, according to the colour shade to be dyed, the
use of carbon black in the micro-fibre, with the possible use of
the same carbon black in the matrix, a polyurethane matrix suitably
selected and a tassel length within a well-defined range, it is
possible to provide a processing intermediate which, when
subsequently over-dyed with the addition of dispersed dyes, in the
colours within the grey and black range, can produce an artificial
leather with a suede appearance capable of complying with the
requirements of light fastness, durability, appearance and feel
required in the field of car interiors.
[0048] The present invention therefore relates a high-quality
artificial leather with a suede appearance and within the range of
grey and black colours, the colour fastness to light, according to
the method SAE J 1885 225.6 KJ/m.sup.2 being higher than or equal
to 4; the colour fastness to light, according to the method SAE J
1885 488.8 KJ/m.sup.2 not being lower than 3; said artificial
leather having a tassel on the surface of the leather itself; said
artificial leather comprising a microfibrous and an elastomeric
matrix; the above micro-fibrous component consisting of polyester
microfibres, preferably of polyethylene terephthalate, having a
count of 0.01 to 0.50 dtex; said elastomeric matrix consisting of
polyurethane; said polyurethane being made up of soft segments and
hard segments; the ratio between the elastomeric matrix and the
micro-fibrous component ranging from 20/80 to 50/50 in mass; the
microfibrous component containing the carbon black pigment in a
percentage of 0.05 to 2.00% in mass, preferably from 0.15 to 1.50%;
the elastomeric matrix containing the carbon black pigment in a
percentage of 0 to 10% by weight, preferably from 0 to 7% by
weight, even more preferably from 0.02 to 6% by weight; the carbon
black always having an average dimension lower than 0.4 microns;
said artificial leather being characterized by: [0049] (a) the
average length of the tassel ranges from 200 to 500 microns,
preferably from 210 to 400 microns; [0050] (b) the soft segments
consisting of at least one polycarbonate diol selected from
polyalkylene carbonate diols and at least one polyester diol;
[0051] (c) the hard segments consisting of urethane and/or ureic
groups, the latter deriving from the reaction of free isocyanate
groups and water; [0052] (d) the total carbon black content ranges
from 0.025 to 6% by weight, preferably from 0.075 to 4.25% by
weight, even more preferably from 0.085 to 3.75% by weight.
[0053] The high quality of the artificial leather with a suede
appearance of the present invention is associated with a complex
set of technical-sensorial factors among which an evident
superficial mottling, a high writing effect, a particularly soft
and pleasant feel. These effects are mainly due to the microfibrous
component (tassel) of the artificial leather, with particular
reference to its surface density and length, from 200 to 500
microns, preferably from 210 to 400 microns. An excessively short
and/or low-density tassel, would not allow a complete covering of
the polyurethane background, with a consequent qualitative decrease
in the noble surface of the product, from both aesthetical and
sensorial point of view. On the other hand, an excessively long
tassel would contribute to reduce the quality of the synthetic
leather as it would be responsible for a "poor" appearance, unlike
natural suede products.
[0054] Another fundamental characteristic of the artificial leather
with a suede appearance of the present invention, is its high aging
resistance, capable of lasting for long periods of time, even after
long and repeated exposure to light and to particularly oxidizing
and/or hydrolyzing environments, without jeopardizing the
characteristic of softness conferred by the microfibrous component.
This result has been obtained by using the particular polyurethanes
of the present invention, characterized by soft and hard
segments.
[0055] The durability of the suede leather of the present invention
proves to be 3 (internal reference photographic standards) in terms
of abrasion resistance, after aging under UV rays or after
hydrolyzing aging. Furthermore, there is a retention of 80% of the
physical-mechanical characteristics after UV aging or hydrolyzing
aging. [0056] All these properties are described in more detail in
the experimental section.
[0057] As far as the components of the artificial leather of the
present invention are concerned, the microfibrous component
consists of microfibres of one or more polymers selected from
polyethylene terephthalate, polytrimethylene terephthalate,
polybutylene terephthalate, preferably polyethylene
terephthalate.
[0058] With respect to the elastomeric matrix, this consists of
polyurethane. This term (polyurethane) refers to both real
polyurethanes and also polyurethane-ureas. The polyurethanes are
characterized by the presence of urethane bonds, formed, for
example, by the reaction between isocyanate groups and hydroxyl
groups, whereas the polyurethane-ureas also contain ureic bonds
obtained, for example, from the reaction of isocyanate groups and
amines or water.
[0059] The polyurethanes are made up of soft segments and hard
segments. The soft segments consist, at least, of one polyalkylene
carbonate diol and, of one polyester diol.
[0060] Typical examples of polyalkylene carbonate diols are
polytetramethylene carbonate diol (PTMC), polypentamethylene
carbonate diol (PPMC), polyhexamethylene carbonate diol (PHC),
polyheptamethylene carbonate diol, polyoctamethylene carbonate
diol, polynonamethylene carbonate diol, polydeca methylene
carbonate diol, poly-(3-methyl-pentamethylene carbonate) diol
(PMPC), poly-(2-methyl-pentamethylene carbonate) diol,
poly-(2-methyl-1-octamethylene carbonate) diol.
[0061] The polymeric diols used for the synthesis of the
polyurethanes described in the examples of the experimental part,
normally have a numeral average molecular weight ranging from 1,000
to 3,000, preferably between 1,750 and 2,250.
[0062] The hard segments refer to portions of polymeric chains
deriving from the reaction of an organic diisocyanate such as, for
example, methylene-bis-(4-phenyl isocyanate) (MDI) or toluene
diisocyanate (TDI) with a diamine or glycolic chain. It is in fact
well-known that the completion of the polyurethane synthesis can be
effected by means of diamines, thus obtaining polyurethane-ureas,
or with glycols, obtaining, in this way, polyurethanes in the true
sense.
[0063] Diamines possibly used as chain extenders in the production
of polyurethane-ureas are, among aliphatic diamines,
ethylenediamine (EDA), 1,3-cyclohexanediamine (1,3-CHDA),
1,4-cyclohexanediamine (1,4-CHDA), isoforondiamine (IPDA),
1,3-propylenediamine (1,3-PDA), 2-methylpentamethylenediamine
(MPDM), 1,2-propylenediamine (1,2-PDA) and blends thereof. Typical
examples of aromatic diamines to be used as chain extenders are
3,3'-dichloro-4,4'-diaminodiphenyl methane, methylene-bis(4-phenyl
amine) (MPA), 2,4-diamino-3,5-diethyl toluene,
2,4-diamino-3,5-di(methylthio)toluene. The above amines can be
added as such or produced in situ by reaction of the corresponding
isocyanate and water.
[0064] The chain extension in polyurethanes in the true sense, can
also be obtained with diols such as ethylene glycol, tetramethylene
glycol and mixtures thereof. Finally, the chain extension can also
be obtained with dicarboxylic acids such as malonic acid, succinic
acid, adipic acid.
[0065] The hard segments can also include molecules with a
hydrophilic nature and/or charged molecules, capable of making the
polyurethanes easily dispersible or emulsifiable in water, both in
absence and in presence of external surface-active agents. Among
molecules having negatively charged groups capable of facilitating
the dispersion of the polymer in water, 2,2-dimethylol-propanoic
acid, 2,2-dimethylol-butanoic acid, compounds functionalized with
sulphonic groups, can be mentioned. Among molecules having
positively charged groups diethanol amine, N-methyl-diethanolamine
and, in general, dihydroxy alkyl amines, di-amino-alkyl amines and
the salts of quaternary ammonium, can be mentioned. Among molecules
of a hydrophilic nature, polyoxyalkyl ethers are included.
[0066] The reactions used for preparing polyurethanes and
polyurethane-ureas are normally carried out in inert, aprotic
solvents, such as dimethyl acetamide (DMAc), dimethyl formamide
(DMF), N-methyl pyrrolidone (NMP), acetone, methyl-ethyl-ketone
(MEK). Alternatively, the process can be carried out by dispersing
or emulsifying the synthesis intermediates in an aqueous
environment or a mixture of water and suitable surface-active
agents; a further alternative of the process can be to synthesize
the polymers or their intermediates in a solvent, subsequently
dispersing the same in water or a mixture of water with suitable
surfactants, finally removing the solvent by evaporation.
[0067] The polymers thus produced can also be subjected to
cross-linking to be carried out in emulsion or dispersion, or after
application to the non-woven fabric, with the purpose of increasing
its resistance to the process conditions and/or with the purpose of
conferring to the impregnated non-woven fabric, higher resistance
characteristics to the action of atmospheric agents and
solvents.
[0068] As far as the carbon black is concerned, this pigment is
characterized by the very reduced dimension of its elemental
particles (normally smaller than 0.4 microns) and by their good
dispersibility (necessary for avoiding an excess aggregation of the
same elemental particles, with consequent fluctuation of the colour
and decrease in the physical-mechanical properties of the polymer).
As is known, carbon black is a black pigment which can be used for
conferring colourings within the grey/black range to synthetic
fibres, whose intensity is in relation to the concentration of
pigment in the polymer and yarn count (denier) of the fibres. In
particular, deeper colour shades can be obtained by increasing the
percentage of the pigment in the polymer and/or increasing the
count of the fibres. The pigment is present in the microfibrous
component in quantities ranging from 0.05 to 2.0% by weight, and it
is present in the elastomeric component in a quantity of 0 to 10%
by weight, in relation to the final colour desired. By changing the
quantity of carbon black in the microfibre and/or in the
elastomeric portion, it is possible to obtain a large range of
colour shades within light greys and blacks.
[0069] This limit, from the colour point of view, does not effect
the field of car interiors, a particularly difficult field where
high light fastness is required, but where the chromatic request is
strongly concentrated within the range of grey and black. Recent
data relating to the European, American and Asian markets, indicate
the following colour requests for synthetic leather with a suede
appearance:
[0070] grey-black shade: 60-80%
[0071] beige shade: 15-30%
[0072] other shades: 5-10%.
[0073] In any case, the total quantity of carbon black in the
artificial leather according to the present invention, is from
0.025 to 6%, preferably from 0.075 to 4.25%, even more preferably
from 0.085 to 3.75% by weight, otherwise the mechanical properties
would decrease.
[0074] The present invention also relates to a process of
production of artificial leather with a suede appearance, with
colours within the range of grey and black as defined above,
comprising the following steps: [0075] (1) production of a
microfibrous intermediate product consisting of microfibres with
the addition of carbon black, said carbon black being contained in
the micro-fibre in a quantity of 0.05% to 2% by weight, preferably
from 0.15 to 1.50% by weight, said microfibres being selected from
microfibres of polyethylene terephthalate, polytrimethylene
terephthalate, polybutylene terephthalate, said microfibrous
intermediate being obtained by the spinning of fibres obtained by
extrusion of a polymer among those indicated above (defined as
island component) with the addition of carbon black, said carbon
black having an average particle-size lower than 0.4 microns, and a
binding polymer of the microfibres (sea component) which is
subsequently eliminated during the processing steps by extraction
with an organic solvent; [0076] (2) impregnation of the
microfibrous intermediate product with the addition of carbon black
as per item (1), with a solution and/or dispersion comprising one
or more polyurethanes and carbon black, the latter being present in
a quantity of 0 to 10% by weight, preferably from 0 to 7% by
weight, even more preferably from 0.02 to 6% by weight with respect
to the polyurethane, and having an average particle-size lower than
0.4 microns; the weight ratio between polyurethane and the
microfibrous intermediate ranging from 20/80 to 50/50 in mass; said
polyurethane being made up of soft segments and hard segments, said
soft segments consisting of at least one polyalkylene carbonate
diol and at least one polyester diol; said hard segments consisting
of urethane and/or ureic groups deriving from the reaction between
free isocyanate groups and water; subsequent elimination of the
solvent to give a raw semifinished product; [0077] (3) grinding of
the surface of the above raw semifinished product to give synthetic
leather with the characteristic of a suede appearance, the length
of the tassel of the above-mentioned synthetic leather being from
200 to 500 .mu.m, preferably from 210 to 400 .mu.m.
[0078] Step 1 initially comprises (step 1a) the preparation of a
microfibrous intermediate consisting of microfibres of one or more
polymers selected from polyethylene terephthalate, polytrimethylene
terephthalate, polybutylene terephthalate, preferably polyethylene
terephthalate, with the addition of carbon black. In order to
improve the mechanical properties of the fibres obtained with the
above, these polymers may be preliminarily subjected to a
post-polymerization process in solid state, to increase the length
of the polymeric chains.
[0079] The production of the microfibres includes the spinning of
multicomponent fibres by extrusion of a polyester among those
mentioned above (defined as island component) with the addition of
carbon black, in percentages ranging from 0.05/2.00%, preferably
0.15/1.50% with a polymer binding the microfibres, which is then
eliminated during the subsequent working steps (sea component).
[0080] In another preferred embodiment, the production of the above
microfibres can be effected by using a suitable mixture of two
polyesters selected from those listed above, one of which, defined
as masterbatch, contains carbon black in a percentage ranging from
10 to 50%. To avoid jeopardizing the physical-mechanical properties
of the fibre, and making the following processing phases difficult,
it is preferable for said masterbatch to have an Inherent Viscosity
value (I.V.) not lower than the other polymer one. This can be
achieved by subjecting said masterbatch to polymerization in the
solid state.
[0081] More specifically, the optimum percentages of pigment added
to the microfibre have been selected with the aim of: [0082]
achieving a considerable enhancement in the light fastness; [0083]
obtaining a wide range of shades between light grey to black (also
using a final over-dyeing treatment of the fibres themselves);
[0084] obtaining a high reproducibility of the colour through the
precise definition of the formulations in the final over-dyeing
step; [0085] reducing the consumption of dispersed dyes in the
over-dyeing step; [0086] minimizing the problems of obstruction of
the spinneret; [0087] minimizing the fibre types to produce with a
different pigment content (in order to minimize the production
costs).
[0088] In the most typical cases, the binding polymer (sea
component) consists of polystyrene or a modified polyester or a
polymer of the family of polyhydroxyalcanoates. The above-mentioned
binder must, in any case, be immiscible with the polymer forming
the microfibrous component and must be present in percentages
between 10-90% by weight (preferably 15-50%). The structure of the
microfibre/binder system, is preferably of the "island-sea" type:
the overall section of the fibre after spinning (sea +islands) is
circular and contains circular islands (micro-fibres with the
addition of carbon black) in its interior, surrounded by the sea
(binder) which holds and keeps the islands separate from each
other.
[0089] As an alternative to the technology described, the fibres,
after spinning, can have elongated or trilobated hollow
sections.
[0090] The distribution of the bi-component in the section can also
be "radial" type (with alternating components "in segments" in a
circular section), "skin-core" (with the microfibrous component
surrounded by an external crown consisting of the binder) or
multi-layers (with the two components forming parallel and
alternating layers).
[0091] The fibre collected under the spinneret is then drawn
according known technologies and finally crimped and cut in order
to produce staple fibre.
[0092] The stretching ratio normally applied is within the range of
2.1/5.1
[0093] The crimp number is between 4/15 per centimetre.
[0094] The staple fibre normally has a count within the range of
1.5/11.0 dtex, preferably between 2.7/6.7 dtex; a length between
30/150 mm preferably between 30/100 mm.
[0095] An intermediate felt is produced (step 1b) with a non-woven
structure, by means of mechanical needle punching or by water jet
punching of the microfibrous intermediate containing carbon black
prepared in step (1a). The felt intermediate has density values
within the range of 0.150/0.350 g/cm.sup.3, typically between
0.150/0.200 g/cm.sup.3 and Unitary Weights within the range of
550/950 g/m.sup.2, typically between 570/630 g/m.sup.2.
The felt intermediate is impregnated according point A3) of the
known production method of synthetic leathers with a suede
appearance already described. The "sea" component of the
bi-component fibres is then dissolved according to point A4) of the
same production method.
[0096] Step 2 consists in the impregnation of the micro-fibrous
intermediate containing carbon black produced in step 1) with a
solution and/or dispersion comprising one or more polyurethanes
and, if necessary, carbon black. Said impregnation is effected
using one or more solutions of one or more polyurethanes in organic
solvents, for example dimethyl formamide. Alternatively, this
impregnation can be effected with one or more polyurethanes in an
emulsion or water dispersion. As far as the polyurethane is
concerned, information should be caught in the product claim.
[0097] The subsequent operation consists of eliminating the solvent
and/or dispersant and/or emulsifying agent, previously used and
eliminating the binder possibly used in item A3), thus obtaining a
"greige" type intermediate product. The latter is subjected to
grinding to "extract" the tassel from the polyurethane matrix in
which it has been impregnated, in order to confer a microfibre
length of 200 to 500 microns, preferably from 210 to 400 microns,
to the synthetic suede leather of the present invention.
[0098] The suede leather thus obtained can be subjected to a
further dyeing step, preferably effected in a "circular" dyeing
apparatus, equipped with a Venturi nozzle, for example the
equipment of Hisaka Works ltd.
[0099] The dyeing cycle consists of a first dyeing step, in which
the "greige" type intermediate product is put in contact with a
mixture of dispersed dyes, surface-active agents, which disperse
the dye and facilitate its contact with the fibre, pH conditions
suitable for allowing the dye to penetrate inside the same fibre
and dyeing auxiliaries. The maximum dyeing temperature, normally
between 100/140.degree. C., is selected so as to heat the polymers
forming the micro-fibres above their glass transition temperatures,
thus facilitating the diffusion of the dye in the polymer. In
practice, the "greige" type intermediate is circulated in the
dyeing equipment for about 1 hour at the maximum dyeing temperature
and, subsequently, subjected to cleaning treatment with sodium
hydrosulphite in a basic environment.
[0100] A great advantage for the process of the present invention
regards the dye amount consumption. With the same final colour
(from grey to black) of the suede leather of the present invention,
the process described above allows a lower consumption of dispersed
dyes, because the product to be dyed already has a grey shade due
to the presence of carbon black. Furthermore, the lesser use of
dispersed dyes (or their total absence) as a result of a colouring
due to carbon black, allows the suede leather of the present
invention to have a high colour fastness to light.
[0101] For illustrative purposes, a preferred but non-limiting
version of the overall process including the present invention, is
schematized hereunder. [0102] B1) Feeding of a mixture consisting
of chips of virgin polymer, typically PET and chips of masterbatch
(polymer, typically PET, with the addition of carbon black) to a
spinning line. The masterbatch, with a high content of carbon
black, is quantitatively added to the virgin polymer so that,
downstream of the extrusion process, the content of the pigment
dispersed in the micro-fibrous component is within the range
mentioned above. [0103] B2) Spinning of a bi-component fibre
effected by means of the well-known spinning technology of the
"sea-island" type, wherein the "sea" component consists of
polystyrene and the "island" component consists of polyethylene
terephthalate with the addition of carbon black. The "islands" thus
produced form so-called microfibres "dyed in mass", having counts
typically falling within the range of 0.10/0.20 dtex. [0104] B3)
Preparation of an intermediate felt, typically by means of a
mechanical needle punching process, with the fibres obtained as
described in the previous item. The intermediate felt has a
preferable density within the range of 0.150/0.200 g/cm.sup.3 and
Unitary Weights within the range of 580/630 g/cm.sup.2. [0105] B4)
Processing of the intermediate felt according to the process
described in items A3-A4-A5-A6-A7-A8 of known high-quality
synthetic suede leathers, with particular attention, in point A8,
effecting the grinding with such conditions able to confer to the
microfibre tassel in the product a length ranging from 200 and 500
microns. [0106] B5) Final overdyeing of the microfibrous component
forming the synthetic leather with a suede appearance, by means of
technologies traditionally used for the achieving of the desired
final colour shade.
[0107] The following examples are provided for a better
understanding of the present invention.
EXAMPLES
[0108] The following table indicates the abbreviations used for
identifying the raw materials in the examples
TABLE-US-00002 ABBREVIATIONS RAW MATERIAL c.b. Carbon black PET
Polyethylene terephthalate PS Polystyrene PVA Polyvinyl alcohol DMF
N,N-Dimethylformamide PHC Polyhexamethylene carbonate glycol PNA
Polyneopentyladipate glycol MDI 4-4' Diphenylmethanediisocyanate
DBA N,N-Dibutylamine
Comparative Example 1 (Standard product)
[0109] A bi-component fibre of the "island-sea" type is produced by
extruding a pair of polymers insoluble with respect to each
other.
[0110] The polymers used are PET and PS, which are extruded and
spun to produce a fibre whose sea component consists of PS and the
island component PET. The PET has an I.V. value equal to 0.7 dl/g.
The fibre thus obtained has the following characteristics: [0111]
1. Yarn count: 4.2 dtex [0112] 2. Length: 51 mm [0113] 3. Maximum
load strength: 2.08 g/dtex [0114] 4. Maximum load elongation: 62%
[0115] 5. Crimp number: about 4-5/cm [0116] 6. PET microfibre
strength at maximum load: 3.89 g/dtex [0117] 7. PET micro-fibre
elongation at maximum load: 72%
[0118] In particular, the fibre is made up of 57 parts by weight of
PET and 43 parts by weight of PS. The fibre, if observed in
section, reveals the presence of 16 PET micro-fibres englobed in
the PS matrix.
[0119] An intermediate felt is prepared with the bi-component
fibre, subjected to needling to form a needled felt having a
density within the range of 0.180/0.200 g/cm.sup.3 and a Unit
Weight within the range of 580/630 g/m.sup.2.
[0120] The white-coloured needled felt (coordinate CIELAB L equal
to 96.3), is immersed in a water solution at 20% weight of
polyvinyl alcohol and then subjected to drying. The needled felt
thus treated is subsequently immersed in trichloroethylene until
the complete dissolution of the polystyrene matrix of the fibres.
The non-woven fabric formed is then dried, obtaining an
intermediate product called "semifinished product D" (coordinate
CIELAB L, after removal of the sea component, equal to 96.6).
[0121] A polyurethane elastomer is prepared separately, in the form
of a solution in DMF. In a first step (pre-polymerization) a
solution of PHC and PNA both having a molecular weight of 2,000 in
DMF are reacted, at a temperature of 65.degree. C. and under
stirring, with MDI in an isocyanate/diols molar ratio of 2.9/1.
Three hours after the beginning of the reaction, the pre-polymer
thus obtained is cooled to a temperature of 45.degree. C. and
diluted with DMF, until a 25% solution of pre-polymer is obtained
having a content of free NCO groups of 1.46%.
[0122] DBA and water dissolved in DMF are then slowly added,
maintaining a temperature of 45.degree. C., over a period of 5
minutes, in order to have a polyurethane-polyurea having a
calculated molecular weight equal to 43,000. After heating to
65.degree. C., the reactor is kept under stirring for a further 8
hours obtaining, in the end, a polyurethane-urea solution which is
stable with time having a viscosity at 20.degree. C. of 22,000
mPa*sec. The elastomer solution thus prepared is then diluted with
DMF containing Irganox.RTM. 1010 and Tinuvin.RTM. 326, with the
addition of carbon black in a percentage of 4.8% with respect to PU
alone, to form a solution at 14% by weight in PU. The polymer in
solution thus obtained, if coagulated with water, is capable of
generating structures with a high porosity.
[0123] The "semifinished product D" is immersed in the solution of
the polyurethane elastomer, squeezed by passage through a pair of
rolls and subsequently immersed in a water bath maintained at
40.degree. C., for one hour. A coagulated semi-finished product is
thus obtained which is passed through a water bath heated to
85.degree. C. to extract the residual solvent and polyvinyl
alcohol. The composite is then dried by passage through a heated
oven.
[0124] The "coagulated and dried semi-finished product" having a
thickness of 2.30 mm and grey-coloured due to the presence of
carbon black in the polyurethane matrix, is then longitudinally cut
to obtain two equal laminates, each having a thickness of 1.15 mm
which are then subjected to grinding to remove an aliquot of the
polyurethane matrix, extract the microfibre component thus forming
the tassel. The grinding process is effected by using suitable
abrasive papers under such conditions as to reduce the thickness of
the composite material to a value of 0.85 mm, producing a
microfibrous tassel having a length of 350/400 microns (CIELAB L
coordinate equal to 55.8).
[0125] The composite is finally treated in suitable dyeing machines
("jet"), in order to dye the microfibre, according to the
technology traditionally used for known synthetic leathers of the
suede type, within the grey or black range. In particular, the
composite is passed through the "Venturi Tube" for 1 hour,
operating at 125.degree. C. in an aqueous dye bath containing the
following dispersed dyes:
TABLE-US-00003 Red dispersed dye (anthraquinonic) 5.4% Blue
dispersed dye (anthraquinonic) 22.8% Yellow dispersed dye (amino
ketone) 9.4%
[0126] At the end of the dyeing, a dyed microfibrous non-woven
fabric is obtained, which, after further treatment under reducing
conditions with sodium hydrosulphite in an alkaline environment to
eliminate the excess dye, is subjected to finishing treatment.
[0127] The artificial leather thus obtained is subjected to
analysis of the physical-mechanical properties (UNI EN 29073-3) and
colour fastness to dry and wet rubbing (AATCC 8-2001), to soap
washing (AATCC 61-2001), dry washing and light (SAEJ-225.6
KJ/m.sup.2 and 448.8 KJ/m.sup.2).
[0128] The evaluations shown in the following tables, relating to
the dyed microfibrous non-woven product, were effected as
follows:
[0129] a) for the colour discharge on the test sample (multifibre
felt for the washings and cloth for the rubbings) the dirt on the
sample is evaluated by comparison with the ISO 105A03 grey
scale;
[0130] b) for the shade exchange of the sample before and after the
test, the ISO 105A02 grey scale is used.
[0131] The evaluation is effected by comparing the shade exchange
or the dirty level with the shade contrasts codified by the
appropriate grey scale; an evaluation equal to 5 corresponds to no
change in shade/colour transfer, whereas an evaluation of 1
corresponds to the maximum contrast found on the grey scale
used.
TABLE-US-00004 TEST Evaluation Longitudinal ultimate tensile
strength 410 N Transversal ultimate tensile strength 310 N
Longitudinal elongation at 50 N 4.9% Transversal elongation at 50 N
20.0% Wet rubbing AATCC 8-2001 (colour discharge) 4 Dry rubbing
AATCC 8-2001 (colour discharge) 4/5 Soap washing AATCC 61-2001
(colour exchange) 5 Dry washing AATCC 61-2001 (colour discharge)
3/4 Dry washing (shade exchange) 5 Dry washing (colour discharge)
3/4 Light fastness, SAE J 1885 225.6 KJ/m.sup.2 (shade exchange) 3
Light fastness, SAE J 1885 488.8 KJ/m.sup.2 (shade exchange)
2/3
Example 2 (Fast Colour from Master SSP with 1%.sup., c.b.in
Fibre)
[0132] A masterbatch consisting of PET chips with the addition of
carbon black at 30% by weight, is polymerized in the solid state in
order to increase its Inherent viscosity (I.V.).
[0133] Polymerization is effected in the solid state (SSP) at a
temperature of 203.degree. C. and a pressure of 42 mbar for 100
hours.
[0134] The trend of the SSP process is controlled by I.V.
measurements effected by means of the following analytic method:
0.5 g of masterbatch are finely ground with a specific "grinding
mill", and immersed in a 50cc solution of dichloroacetic acid,
maintaining them at 85.degree. C. for 6 hours and subsequently at
70.degree. C. in an ultrasound bath for a further 30 minutes in
order to complete the dissolution of the polymer. The solution thus
obtained is then analyzed by means of a capillary viscometer of the
"Ostwald" type.
[0135] By comparing the flow time used by the solution to cover a
certain portion of the capillary with the time used by the solvent
alone, the value of the specific viscosity is obtained. The I.V.
value is obtained from the latter value using appropriate
mathematical formulae.
[0136] The I.V. before and after the SSP treatment is obtained by
means of the above method. The results are as follows:
[0137] I.V. masterbatch as such=0.35 dl/g
[0138] I.V. masterbatch after SSP=0.71 dl/g
[0139] The chips of masterbatch polymerized in the solid state are
then added and suitably mixed, in a proportion of 1/30, with virgin
PET chips (I.V. equal to 0.7 dl/g). The chips thus mixed are then
extruded and spun together with a quantity of PS, according to the
procedure of the "sea-island" spinning technology, to produce a
bi-component fibre whose "sea" component consists of PS and the
island component consists of PET with the addition of c.b. The
fibre thus obtained has the following characteristics:
[0140] 1. Yarn count (denier): 4.2 dtex
[0141] 2. Length: 51 mm
[0142] 3. Maximum load strength: 2.18 g/tex
[0143] 4. Maximum load elongation: 70%
[0144] 5. Crimp number: about 4-5/cm
[0145] 6. PET microfibre strength under maximum load: 3.86
g/dtex
[0146] 7 Elongation of the PET microfibre under maximum load:
68%.
[0147] In particular, the fibre consists of 57 parts by weight of
PET with the addition of carbon black and 43 parts by weight of PS.
When observed in section, the fibre reveals the presence of 16
micro-fibres of "PET +carbon black" englobed in the PS matrix.
An intermediate felt is prepared with the bi-component fibre and is
subjected to needling to form a needled felt having a density
within the range of 0.170/0.190 c/cm.sup.3 and Unitary Weights
within the range of 580/630 g/m.sup.2.
[0148] The needled felt, having a dark grey colour due to the
presence of the fibre with the addition of carbon black (CIELAB L
coordinate equal to 35.7), is immersed in an aqueous solution at
20% by weight and then subjected to drying.
[0149] The needled felt thus treated is subsequently immersed in
trichloroethylene until the complete dissolution of the polystyrene
matrix of the fibres. The non-woven fabric thus formed is then
dried, obtaining an intermediate product called "semi-finished
product D" (CIELAB L coordinate, after removal of the sea
component, equal to 40.1).
[0150] A polyurethane elastomer is prepared separately, as already
described in example 1. The elastomer solution thus prepared is
then diluted with DMF containing Irganox.RTM. 1010 and Tinuvin.RTM.
326, with the addition of carbon black in a percentage of 4.8% with
respect to the PU alone, to form a solution in PU at 14% by weight.
The polymer in solution thus obtained, if coagulated in water, is
capable of generating structures with high porosities.
[0151] The "semi-finished product D" is immersed in the solution of
the polyurethane elastomer squeezed by passing it through a pair of
rolls and subsequently immersed for 1 hour in a water bath
maintained at 40.degree. C. A coagulated semifinished product is
thus obtained which is passed through a water bath heated to
85.degree. C. to extract the residual solvent and polyvinyl
alcohol. The composite material is then dried by passing it through
a heated oven.
[0152] The "coagulated and dried semifinished product", having a
thickness of 2.30 mm and a dark grey colour due to the presence of
carbon black both in the fibre and in the polyurethane matrix, is
then longitudinally cut to obtain two equal laminates, each having
a thickness of 1.15 mm which are then subjected to grinding to
remove an aliquot of the polyurethane matrix, to extract the
microfibre component thus forming the tassel. The grinding process
is effected using specific abrasive papers under such conditions as
to reduce the thickness of the composite material to a value of
0.85 mm, producing a microfibrous tassel having a length of 350/400
microns (CIELAB L coordinate equal to 33.8).
[0153] The composite is finally treated in suitable dyeing machines
("jet"), in order to over-dye the microfibre with the addition of
carbon black, according to the technology traditionally used for
known synthetic leathers, to give a suede type leather, coloured
within the range of grey or black. In particular, the composite is
passed through the "Venturi Tube" for 1 hour, operating at
125.degree. C. in an aqueous dyeing bath containing the following
dispersed dyes:
TABLE-US-00005 Red dispersed dye (anthraquinonic) 4% Blue dispersed
dye (anthraquinonic) 3% Yellow dispersed dye (amino ketone)
3.5%
[0154] At the end of the dyeing, a dyed microfibrous non-woven
product is obtained, which, after further treatment under reducing
conditions with sodium hydrosulphite in an alkaline environment to
eliminate the excess dye, is subjected to finishing treatment.
The artificial leather thus obtained is subjected to analysis of
the physical-mechanical properties and colour fastness, to rubbing,
soap washing and a combination of dry washing and light exposure as
widely described in example 1. The evaluations are shown in the
following table
TABLE-US-00006 TEST Valutazione Longitudinal ultimate tensile
strength 450 N Transversal ultimate tensile strength 248 N
Longitudinal elongation at 50 N 4.5% Transversal elongation at 50 N
24.0% Wet rubbing AATCC 8-2001 (colour discharge) 4 Dry rubbing
AATCC 8-2001 (colour discharge) 4/5 Soap washing AATCC 61-2001
(colour exchange) 5 Dry washing AATCC 61-2001 (colour discharge)
4/5 Dry washing (shade exchange) 5 Dry washing (colour discharge)
4/5 Light fastness, SAE J 1885 225.6 KJ/m.sup.2 (shade exchange)
4/5 Light fastness, SAE J 1885 488.8 KJ/m.sup.2 (shade exchange)
4
Example 3 (Fast Colour from Master SSP with 0.4% c. b. in Fibre and
Lighter Dyeing-Shade Colour).
[0155] The chips of masterbatch polymerized in the solid state as
described in example 2, are added and suitably mixed to chips of
virgin PET (I.V. equal to 0.7 dl/g), in a proportion of 1/75.
[0156] The chips thus mixed are then extruded and spun together
with PS, according to the procedure of the "sea-island" spinning
technology, to produce a bi-component fibre, whose "sea" component
consists of PS and the island component consists of PET with the
addition of c.b. The fibre thus obtained has the following
characteristics:
[0157] 1. Yarn count (denier): 4.2 dtex
[0158] 2. Length: 51 mm
[0159] 3. Maximum load strength: 2.09 g/tex
[0160] 4. Maximum load elongation: 71%
[0161] 5. Crimp number: about 4-5/cm
[0162] 6. PET microfibre strength under maximum load: 3.84
g/dtex
[0163] 7 Elongation of the PET microfibre under maximum load:
74%.
[0164] In particular, the fibre consists of 57 parts by weight of
PET with the addition of carbon black and 43 parts by weight of PS.
When observed in section, the fibre reveals the presence of 16
micro-fibres of "PET+carbon black" englobed in the PS matrix.
[0165] An intermediate felt is prepared with the bi-component fibre
and is subjected to needling to form a needled felt having a
density within the range of 0.204/0.208 c/cm.sup.3 and Unitary
Weights within the range of 550/580 g/m.sup.2.
[0166] The needled felt, having a dark grey colour due to the
presence of the fibre containing carbon black (CIELAB L coordinate
equal to 50.4), is immersed in an aqueous solution at 20% by weight
and then subjected to drying.
[0167] The needled felt thus treated is subsequently immersed in
trichloroethylene until the complete dissolution of the polystyrene
matrix of the fibres. The non-woven fabric thus formed is then
dried, obtaining an intermediate product called "semi-finished
product D" (CIELAB L coordinate, after removal of the sea
component, equal to 51.6).
[0168] A polyurethane elastomer is prepared separately, as already
described in example 1. The elastomer solution thus prepared is
then diluted with DMF containing Irganox.RTM. 1010 and Tinuvin.RTM.
326, with the addition of carbon black in a percentage of 0.3% with
respect to the PU alone, to form a solution in PU at 14% by weight
The polymer in solution thus obtained, if coagulated in water, is
capable of generating structures with high porosities.
[0169] The "semi-finished product D" is immersed in the solution of
the polyurethane elastomer squeezed by passing it through a pair of
rolls and subsequently immersed for 1 hour in a water bath
maintained at 40.degree. C. A coagulated semifinished product is
thus obtained which is passed through a water bath heated to
85.degree. C. to extract the residual solvent and polyvinyl
alcohol. The composite material is then dried by passing it through
a heated oven.
[0170] The "coagulated and dried semifinished product", having a
thickness of 2.30 mm and a dark grey colour due to the presence of
carbon black both in the fibre and in the polyurethane matrix, is
then longitudinally cut to obtain two equal laminates, each having
a thickness of 1.15 mm which are then subjected to grinding to
remove an aliquot of the polyurethane matrix, extract the
microfibre component and thus form the tassel. The grinding process
is effected by using specific abrasive papers under such conditions
as to reduce the thickness of the composite material to a value of
0.85 mm, producing a microfibrous tassel having a length of 300/350
microns (CIELAB L coordinate equal to 50.0).
[0171] The composite is finally treated in suitable dyeing machines
("jet"), in order to over-dye the microfibre containing carbon
black, according to the technology traditionally used for known
synthetic leathers, to give a suede-type leather, coloured within
the grey or black range.
[0172] Unlike what has been observed with the composite materials
previously illustrated, the lower amount of carbon black used makes
it necessary to use a higher quantity of dyes, if the final colour
desired is the same. Starting from a lighter grey shade, on the
contrary, a range of lighter colours can be obtained, by
over-dyeing, which would otherwise be impossible to produce
starting from the grey base of the composite previously illustrated
(example 2), in any case maintaining equally high colour fastness
performances.
[0173] In particular, the composite is passed through the "Venturi
Tube" for 1 hour, operating at 125.degree. C. in an aqueous dyeing
bath containing the following dispersed colours:
TABLE-US-00007 Red dispersed dye (anthraquinonic) 0.7% Blue
dispersed dye (anthraquinonic) 1.9% Yellow dispersed dye (amino
ketone) 0.5%
[0174] At the end of the dyeing, a dyed microfibrous non-woven
fabric is obtained, which, after further treatment under reducing
conditions with sodium hydrosulphite in an alkaline environment to
eliminate the excess dye, is subjected to finishing treatment. The
artificial leather thus obtained is subjected to analysis of the
physical-mechanical properties and colour fastness to rubbing, soap
washing and a combination of dry washing and light exposure as
widely described in example 1. The evaluations are indicated in the
following table
TABLE-US-00008 TEST Valutazione Longitudinal ultimate tensile
strength 410 N Transversal ultimate tensile strength 240 N
Longitudinal elongation at 50 N 5.5% Transversal elongation at 50 N
25.0% Wet rubbing AATCC 8-2001 (colour discharge) 4 Dry rubbing
AATCC 8-2001 (colour discharge) 4/5 Soap washing AATCC 61-2001
(colour exchange) 5 Dry washing AATCC 61-2001 (colour discharge)
4/5 Dry washing (shade exchange) 5 Dry washing (colour discharge)
4/5 Light fastness, SAE J 1885 225.6 KJ/m.sup.2 (shade exchange)
4/5 Light fastness, SAE J 1885 488.8 KJ/m.sup.2 (shade exchange)
4
[0175] By comparison, a composite produced with the same procedure,
starting however from virgin PET fibres (with no addition of carbon
black), required, in order to obtain the same colour shade, the use
of a dyeing bath with the following dispersed dyes
TABLE-US-00009 Red dispersed dye (anthraquinonic) 1.3% Blue
dispersed dye (anthraquinonic) 3.8% Yellow dispersed dye (amino
ketone) 1.3%
Example 4--(Non-Regraded Fast Colour with 1% Carbon Black in
Fibre)
[0176] The chips of masterbatch as such (containing PET with the
addition of carbon black at 30% by weight, I.V. equal to 0.35
dl/g), are added to and suitably mixed, in a proportion of 1/30,
with chips of virgin PET (I.V. of 0.7 dl/g).
[0177] The chips thus mixed are then extruded and spun together
with PS, according to the "sea-island" spinning technology, to
produce a bi-component fibre, whose sea component consists of PS
and the island component consists of PET with the addition of
carbon black. The fibre thus obtained has the following
characteristics:
[0178] 1. Yarn count (denier): 4.2 dtex
[0179] 2. Length: 51 mm
[0180] 3. Maximum load strength : 1.45 g/tex
[0181] 4. Maximum load elongation: 69%
[0182] 5. Crimp number: about 4-5/cm
[0183] 6. PET microfibre strength under maximum load: 2.55
g/dtex
[0184] 7 Elongation of the PET microfibre under maximum load:
72%.
[0185] In particular, the fibre consists of 57 parts by weight of
PET with the addition of carbon black and 43 parts by weight of PS.
When observed in section, the fibre reveals the presence of 16
micro-fibres of "PET +carbon black" englobed in the PS matrix.
[0186] An intermediate felt is prepared with the bi-component fibre
and is subjected to needling to form a needled felt having a
density within the range of 0.240/0.260 c/cm.sup.3 and Unitary
Weights within the range of 630/650 g/m.sup.2. Also during the
production of the felt, problems were observed relating to the
breakage of the microfibre, which causes a sudden increase in
density and frequent needle breaks.
[0187] The needled felt, having a dark-grey colour due to the
presence of the fibre with the addition of carbon black (CIELAB L
coordinate equal to 35.4), is immersed in an aqueous solution of
polyvinyl alcohol at 20% by weight and then subjected to
drying.
[0188] The needled felt thus treated is subsequently immersed in
trichloroethylene until the complete dissolution of the polystyrene
matrix of the fibres. The non-woven fabric thus formed is then
dried, obtaining an intermediate product called "semi-finished
product D" (CIELAB L coordinate, after removal of the sea
component, equal to 40.3).
[0189] A polyurethane elastomer is prepared separately, as already
described in example 1. The elastomer solution thus prepared is
then diluted with DMF containing Irganox.RTM. 1010 and Tinuvin.RTM.
326, with the addition of carbon black in a percentage of 4.8% with
respect to the PU alone, to form a solution in PU at 14% by weight.
The polymer in solution thus obtained, if coagulated in water, is
capable of generating structures with high porosities.
[0190] The "semi-finished product D" is immersed in the solution of
the polyurethane elastomer, squeezed by passing it through a couple
of rolls and subsequently immersed for 1 hour in a water bath
maintained at 40.degree. C. A coagulated semifinished product is
thus obtained which is passed through a water bath heated to
85.degree. C. to extract the residual solvent and polyvinyl
alcohol. The composite material is then dried by passing it through
a heated oven.
[0191] The "coagulated and dried semifinished product", having a
thickness of 2.30 mm and a dark grey colour due to the presence of
carbon black both in the fibre and in the polyurethane matrix, is
then longitudinally cut to obtain two equal laminates, each having
a thickness of 1.15 mm which are then subjected to grinding to
remove an aliquot of the polyurethane matrix, extract the
microfibre component and thus form the tassel. The grinding process
is effected by using suitable abrasive papers under such conditions
as to reduce the thickness of the composite material to a value of
0.85 mm, producing a microfibrous tassel having a length of 320/370
microns (CIELAB L coordinate equal to 34.0).
[0192] The composite is finally treated in suitable dyeing machines
("jet"), in order to over-dye the microfibre containing carbon
black, according to the technology traditionally used for known
synthetic leathers, to give a suede-type leather, coloured within
the grey or black range. In particular, the composite is passed
through the "Venturi Tube" for 1 hour, operating at 125.degree. C.
in an aqueous dyeing bath containing the following dispersed
colours:
TABLE-US-00010 Red dispersed dye (anthraquinonic) 4% Blue dispersed
dye (anthraquinonic) 3% Yellow dispersed dye (amino ketone)
3.5%
[0193] At the end of the dyeing, a dyed microfibrous non-woven
fabric is obtained, which, after further treatment under reducing
conditions with sodium hydrosulphite in an alkaline environment to
eliminate the excess dye, is subjected to finishing treatment.
[0194] The artificial leather thus obtained is subjected to
analysis of the physical-mechanical properties and colour fastness
to rubbing, soap washing and a combination of dry washing and light
exposure as widely described in example 1. The evaluations are
indicated in the following table
TABLE-US-00011 TEST Evaluation Longitudinal ultimate tensile
strength 424 N Transversal ultimate tensile strength 272 N
Longitudinal elongation at 50 N 3.6% Transversal elongation at 50 N
22.0% Wet rubbing AATCC 8-2001 (colour discharge) 4 Dry rubbing
AATCC 8-2001 (colour discharge) 4/5 Soap washing AATCC 61-2001
(colour exchange) 5 Dry washing AATCC 61-2001 (colour discharge)
4/5 Dry washing (shade exchange) 5 Dry washing (colour discharge)
4/5 Light fastness, SAE J 1885 225.6 KJ/m.sup.2 (shade exchange)
4/5 Light fastness, SAE J 1885 488.8 KJ/m.sup.2 (shade exchange)
4
[0195] The composite has a thickness of 0.82 mm.
Example 5 (Non-Regraded Fast Colour with 2% Carbon Black in
Fibre)
[0196] The chips of masterbatch as such (containing PET with the
addition of 30% by weight of carbon black, I.V. equal to 0.35
dl/g), are added to and suitably mixed, in a proportion of 1/15,
with chips of virgin PET (I.V. of 0.7 dl/g).
[0197] The chips thus mixed are then extruded and spun together
with PS, according to the "sea-island" spinning technology, to
produce a bi-component fibre, whose sea component consists of PS
and the island component consists of PET with the addition of
carbon black. The fibre thus obtained has the following
characteristics:
[0198] 1. Yarn count (denier): 4.2 dtex
[0199] 2. Length: 51 mm
[0200] 3. Maximum load strength : 1.4 g/tex
[0201] 4. Maximum load elongation: 62%
[0202] 5. Crimp number: about 4-5/cm
[0203] 6. PET microfibre strength under maximum load: 2.52
g/dtex
[0204] 7. Elongation of the PET microfibre under maximum load:
72%.
[0205] In particular, the fibre consists of 57 parts by weight of
PET containing carbon black and 43 parts by weight of PS. When
observed in section, the fibre reveals the presence of 16
microfibres of "PET +carbon black" englobed in the PS matrix.
[0206] An intermediate felt is prepared with the bi-component fibre
and is subjected to needling to form a needled felt having a
density within the range of 0.240/0.260 c/cm.sup.3 and Unitary
Weights within the range of 615/630 g/m.sup.2.
[0207] The needled felt, having a dark grey colour due to the
presence of the fibre containing carbon black (CIELAB L coordinate
equal to 25.0), is immersed in an aqueous solution of polyvinyl
alcohol at 20% by weight and then subjected to drying.
[0208] The needled felt thus treated is subsequently immersed in
trichloroethylene until the complete dissolution of the polystyrene
matrix of the fibres. The non-woven fabric thus formed is then
dried, obtaining an intermediate product called "semi-finished
product D" (CIELAB L coordinate, after removal of the sea
component, equal to 30.3).
[0209] A polyurethane elastomer is prepared separately, as already
described in example 1. The elastomer solution thus prepared is
then diluted with DMF containing Irganox.RTM. 1010 and Tinuvin.RTM.
326, with the addition of carbon black in a percentage of 4.8% with
respect to the PU alone, to form a solution in PU at 14% by weight.
The polymer in solution thus obtained, if coagulated in water, is
capable of generating structures with high porosities.
[0210] The "semi-finished product D" is immersed in the solution of
the polyurethane elastomer, squeezed by passing it through a pair
of rolls and subsequently immersed for 1 hour in a water bath
maintained at 40.degree. C. A coagulated semifinished product is
thus obtained which is passed through a water bath heated to
85.degree. C. to extract the residual solvent and polyvinyl
alcohol. The composite material is then dried by passing it through
a heated oven.
[0211] The "coagulated and dried semifinished product", having a
thickness of 2.30 mm and dark-grey colour due to the presence of
carbon black both in the fibre and in the polyurethane matrix, is
then longitudinally cut to obtain two equal laminates, each having
a thickness of 1.15 mm which are then subjected to grinding to
remove an aliquot of the polyurethane matrix, extract the
microfibrous component and thus form the tassel. The grinding
process is effected by using suitable abrasive papers under such
conditions as to reduce the thickness of the composite material to
a value of 0.85 mm, producing a microfibrous tassel having a length
of 320/370 microns (CIELAB L coordinate equal to 24.4).
[0212] The composite is finally treated in suitable dyeing machines
("jet") in order to over-dye the microfibre containing carbon
black, according to the technology traditionally used for already
known synthetic leathers, to give a suede-type leather coloured
within the grey and black range.
[0213] Unlike what has been observed with the composite products
described above, the higher quantity of carbon black used does not
allow the same colour range to be reproduced, starting from the
composite products already described. The colours listed in the
following table, for example, characterized by high sales volumes,
cannot be prepared starting from the present composite product due
to the greater brightness of the colour shade required with respect
to that of the composite produced (CIELAB L coordinate equal to
24.4)
TABLE-US-00012 Colour L 6650 29.86 6750 26.89 6950 32.87
[0214] For other colours, on the other hand, difficulties are
observed for reaching the desired colour shade by means of
over-dyeing due to the strong colour changes towards red and/or
blue shades of the composite product and to the poor contribution
of the dyes necessary for effecting the shade correction. The
smaller colour range which can be developed on this colour base of
the composite product, however, is coupled by a strong increase in
resistance on particularly dark colours (black in particular) which
in any case require considerable additions of dyes even when
starting from the composite product described in examples 2 and
4.
[0215] In particular, the composite is passed through the "Venturi
Tube" for 1 hour, operating at 125.degree. C. in an aqueous dyeing
bath containing the following dispersed dyes:
TABLE-US-00013 Red dispersed dye (anthraquinonic) 1% Blue dispersed
dye (anthraquinonic) 3% Yellow dispersed dye (amino ketone)
10.5%
[0216] At the end of the dyeing, a dyed microfibrous non-woven
fabric is obtained, which, after further treatment under reducing
conditions with sodium hydrosulphite in an alkaline environment to
eliminate the excess dye, is subjected to finishing treatment.
[0217] The artificial leather thus obtained is subjected to
analysis of the physical-mechanical properties and colour fastness
to rubbing, soap washing and the combination of dry washing and
light exposure as widely described in example 1. The evaluations
are indicated in the following table
TABLE-US-00014 TEST Evaluation Longitudinal ultimate tensile
strength 395 N Transversal ultimate tensile strength 240 N
Longitudinal elongation at 50 N 7.0% Transversal elongation at 50 N
32.0% Wet rubbing AATCC 8-2001 (colour discharge) 4 Dry rubbing
AATCC 8-2001 (colour discharge) 4/5 Soap washing AATCC 61-2001
(colour exchange) 5 Dry washing AATCC 61-2001 (colour discharge)
4/5 Dry washing (shade exchange) 5 Dry washing (colour discharge)
4/5 Light fastness, SAE J 1885 225.6 KJ/m.sup.2 (shade exchange)
4/5 Light fastness, SAE J 1885 488.8 KJ/m.sup.2 (shade exchange)
4/5
[0218] PET fibre (with no addition of carbon black) required, in
order to obtain the same colour shade, the use of a dyeing bath
with the following dispersed dyes:
TABLE-US-00015 Red dispersed dye (anthraquinonic) 5.7% Blue
dispersed dye (anthraquinonic) 12.8% Yellow dispersed dye (amino
ketone) 18.1%
Comparative Example 6 (Fast Colour From Master SSP with 1% Carbon
Black In Fibre and Short Tassel)
[0219] The composite product, prepared as described in example 2,
was ground under such conditions as to produce a micro-fibrous
tassel having a length ranging from 90 to 120 .mu.m (CIELAB L
coordinate equal to 33.4).
[0220] The composite is finally treated in suitable dyeing machines
("jet"), in order to over-dye the microfibre containing carbon
black, according to the technology traditionally used for known
synthetic leathers of the suede type, within the range of grey or
black. In particular, the composite is passed through the "Venturi
Tube" for 1 hour, operating at 125.degree. C. in an aqueous dyeing
bath containing the following dispersed dyes:
TABLE-US-00016 Red dispersed dye (anthraquinonic) 3.8% Blue
dispersed dye (anthraquinonic) 2.8% Yellow dispersed dye (amino
ketone) 3.2%
[0221] At the end of the dyeing, a dyed microfibrous non-woven is
obtained, which, after further treatment under reducing conditions
with sodium hydrosulphite in an alkaline environment to eliminate
the excess dye, is subjected to finishing treatment.
[0222] The artificial leather thus obtained shows an evident
qualitative decay from an aesthetical point of view due to the
excessive exposure of the polyurethane background and to the loss
of the writing and marbling effect caused by the particularly short
microfibrous tassel. Prototypes of composite products thus produced
were considered as being unsuitable by the final user and therefore
discarded.
[0223] The evaluation of the physical-mechanical properties and
colour resistance tests to rubbing, soap washing and a combination
of dry washings and light exposures (already widely described in
example 1), are indicated in the following table
TABLE-US-00017 TEST Evaluation Longitudinal ultimate tensile
strength 445 N Transversal ultimate tensile strength 250 N
Longitudinal elongation at 50 N 4.3% Transversal elongation at 50 N
23.0% Wet rubbing AATCC 8-2001 (colour discharge) 4 Dry rubbing
AATCC 8-2001 (colour discharge) 4/5 Soap washing AATCC 61-2001
(colour exchange) 5 Dry washing AATCC 61-2001 (colour discharge)
4/5 Dry washing (shade exchange) 5 Dry washing (colour discharge)
4/5 Light fastness, SAE J 1885 225.6 KJ/m.sup.2 (shade exchange)
4/5 Light fastness, SAE J 1885 488.8 KJ/m.sup.2 (shade exchange)
4
[0224] The composite product has a thickness of 0.78 mm.
Summarazing Table
[0225] The main characteristics of the composite materials
described above are summarized hereunder, for a clearer and more
convenient reading.
[0226] Comparative example 1 refers to the production of artificial
suede leather with no carbon black in the micro-fibrous part.
[0227] Comparative example 6 refers to the production of suede
leather having a tassel length of 90-120 microns.
TABLE-US-00018 TEST 1C 2 3 4 5 6C I.V. masterbatch (dl/g) -- 0.71
0.71 0.35 0.35 0.71 c.b. microfibre content (%) 0 1 0.4 1 2 1 c.b.
elastomer content (%) 4.8 4.8 0.3 4.8 4.8 4.8 c.b. total content
(%) 1.6 2.3 0.4 2.3 2.9 2.3 fibre count (dtex) 4.2 4.2 4.2 4.2 4.2
4.2 fibre toughness (g/dtex) 2.08 2.18 2.09 1.45 1.40 2.18 fibre
elongation (%) 62 70 71 69 62 70 PET microfibre toughness 3.89 3.86
3.84 2.55 2.52 3.86 (g/dtex) PET microfibre elongation 72 68 74 72
72 68 (%) felt luminosity (L) 96.3 35.7 50.4 35.4 25.0 35.7
composite luminosity (L) 55.8 33.8 50.0 34.0 24.4 33.4 tassel
length (.mu.m) 350-400 320-370 300-350 320-370 320-370 90-120
Fastness to light, SAE J 1885 3 4/5 4 (4/5*) 4/5 (4/5*) 4/5 225.6
KJ/m.sup.2 (shade exchange) Fastness to light, SAE J 1885 2/3 4 3/4
(4*) 4 (4/5*) 4 488.8 KJ/m.sup.2 (shade exchange)
[0228] increase in the colour fastness of the dye to light, even of
1-1.5 with respect to the grey scale (see examples 1C and 2);
[0229] by increasing the carbon black content in the fibre, the
colour fastness to light increases but the colour range which can
be obtained starting from the intermediate microfibrous compound
decreases (decrease in the luminosity value L of the same
intermediate product); [0230] the addition of masterbatch
containing carbon black causes a slight decrease in the
physical-mechanical properties of the fibre; [0231] the masterbatch
polymerization process in the solid state (see examples 2 and 3)
allows the production of a microfibre with improved mechanical
properties, comparable with that of the reference product, without
carbon black, described in comparative example 1.
* * * * *