[0001] This invention pertains to a liquid composition that may be applied to threads and
plied yarns using kiss roll application methods. The composition does not require
heat to liquify it during the application and provides superior performance over traditional
"hot melt" compositions.
[0002] Typically a wax/silicone coating is placed on a thread to improve certain characteristics
of the thread such as the breaking strength, coefficient of friction, amount of wear
and to add antistatic properties. The wax/silicone coating is applied to the thread
by two methods known in the art; kiss roll (hot melt) methods and exhaust finish methods.
[0003] The kiss roll application methods comprise using a mixture comprising a wax, a linear
polydimethylsiloxane and a stabilizer or surfactant. The mixture, which is typically
a solid at room temperature, is heated to liquify. The mixture is then picked up on
a roller across which the thread is drawn before being wound onto a spool. One of
the disadvantages of these "hot melt" mixtures is that they must be heated prior to
application. Another disadvantage to using a hot melt mixture is that the thread winders
must be run at significantly slow speeds to prevent slinging off of the mixture. When
the mixture splatters it solidifies and creates a clean up problem which results in
costly clean up time.
[0004] The exhaust finish application methods use an emulsion comprising a wax, a linear
polydimethylsiloxane, water and a cationic surfactant. The wax may be added to the
emulsion as, a solid or it may be pre-emulsified in water. These emulsions are liquid
at room temperature and usually contain large amounts of water in the continuous phase.
The exhaust finish emulsions are applied by placing the emulsion in a bath and then
dipping a "spool" of thread into the bath and allowing it to sit in the bath for a
period of time until the active ingredient is fully exhausted onto the thread and
a clear liquid remains. Typically the bath of the emulsion is heated during the application
period. The thread is then dried and wound onto the final spools. When used, the exhaust
emulsions typically provide superior thread sewing performance results than the kiss
roll mixtures. However, the exhaust finish emulsions are higher priced, they are cationic
and therefore lead to waste water problems, they are difficult for the thread manufacturers
to handle and they typically do not result in an even application on the thread.
[0005] Because of the high amount of water in the continuous phase of the exhaust emulsions
and their cationic nature it is not possible to apply the exhaust finish emulsions
using kiss roll application methods. Applying exhaust finish emulsions using kiss
roll application methods will typically lead to rusting and other complications with
the kiss roll production equipment.
[0006] US-A-4 434 008 to Dumm et al. teaches an exhaust emulsion composition comprising,
on a water free basis, (a) about 5 to 80 weight percent of a silicone oil having a
viscosity of from about 500 to 50,000 mm²/sec at 25°C.; (b) about 10 to 80 weight
percent of a wax with a melting point of not less than about 40°C.; (c) about 1 to
10 weight percent of fatty acids with 6 to 22 carbon atoms; (d) about 0.4 to 12 weight
percent of cationic imidazolinium salts; and (e) from about 0 to 10 weight percent
of ethoxylated fatty amines. The composition is produced by emulsifying (in water)
the silicone oil with a portion of the fatty acid and imidazolinium salt and emulsifying
(in water) the wax with the remainder of the fatty acid and imidazolinium salt and
then combining the two emulsions together. The compositions typically comprise 30
percent or more water in the continuous phase.
[0007] There has been a long felt need in the art for a high performance composition that
is liquid at room temperature and can be easily applied using the kiss roll application
methods without corroding or otherwise destructing the application equipment. It is
further desired to have a composition that can be applied at high spool winder speeds.
[0008] It is an object of this invention to show high performance liquid compositions which
can be applied to thread and plied yarn at room temperature using kiss roll application
methods.
[0009] This invention provides a thread treating composition which is liquid at room temperature
comprising
(A) at least 60 percent by weight of a silicone oil having a viscosity of 5 x 10⁻⁶
to 5 x 10⁻³ m²/s (5 to 5,000 centistokes) at 25°C;
(B) at least 5 percent by weight of a wax emulsion in which the wax is selected from
paraffin waxes, microcrystalline waxes, semicrystalline waxes, polyethylene waxes,
ester waxes, and natural waxes, which have a melting point of higher than 40°C; and
(C) 0.5 to 5 percent by weight of a silicone surfactant,
the sum of the components adding up to 100 percent by weight.
[0010] This liquid composition can be applied to threads and plied yarns (herein referred
to as threads) using kiss roll methods.
[0011] Component (A) of this composition is a silicone oil with a viscosity of 5 x 10⁻⁶
to 5 x 10⁻³ m²/s (5 to 5,000 centistokes) at 25°C, preferably 2 x 10⁻⁵ to 1 x 10⁻⁴
m²/s (20 to 100 centistokes) at 25 °C. The silicone oil preferably is a linear dimethylpolysiloxane
oil. A portion of the methyl groups can be replaced by alkyl groups with a longer
chain length and/or by phenyl groups. The terminal chain ends of the silicone oil
are typically formed by trimethyl silyl groups. However, hydroxyl groups may be present
on the terminal chain ends.
[0012] The silicone oil is present in the composition at level of at least 60 percent by
weight. The silicone oils can be exemplified by, but not limited to, polydimethylsiloxanes,
DOW CORNING® 200 FLUIDS, hydroxyl endblocked polydimethylsiloxanes and mixtures thereof.
[0013] Component (B) of this invention is a wax emulsion comprising a wax which typically
has a melting point of higher than 40°C. and water. Useful waxes are petroleum waxes
such as a paraffin waxes, microcrystalline waxes and semicrystalline waxes; synthetic
waxes such as polyethylene waxes, Fischer-Tropsch Waxes (polyethylene), and chemically
modified hydrocarbon waxes (ester waxes); natural waxes such as beeswax and carnauba;
and mixtures thereof. The waxes are supplied as an emulsion in water typically comprising
10 to 80 percent by weight of the wax, preferably 50 to 80 percent by weight. Preferred
wax emulsions are those that contain paraffin at levels of 50 to 70 percent by weight.
The emulsions of the waxes may be produced using methods known in the art or they
are commercially available.
[0014] The wax emulsion is typically present at 5 to 40 percent by weight based on the total
composition. The wax emulsions may be exemplified by Rayolan® CPN produced by Boehme
Filatex, Inc. (50% paraffin, cationic), Uscosoft® HTW produced by Ivax Inc. (28% High
Density Polyethylene Emulsion), Uscosoft® LPD produced by Ivax Inc. (40% Low Density
Polyethylene Emulsion), Michem® Emulsion 47960 produced by Michelman Industries (60%
paraffin, nonionic), Emulsion 150-50 produced by Chemical Corporation of America (50%
paraffin, m.p. 66°C (150°F), nonionic), and Emulsion 135-50 produced by Chemical Corporation
of America (50% paraffin, m.p. 57°C (135°F), nonionic).
[0015] Component (C) is an silicone surfactant. Silicone surfactants are well known in the
art. For example they may be polydiroganosiloxane-polyoxyalkylene copolymers such
as those described in US-A-4 265 878 to Keil; organopolysiloxane-polyoxyalkylene block
copolymers such as those described in US-A-4 532 132 to Keil; and siloxane copolymers
such as those described in US-A-4 087 478 to Keil.
[0016] The silicone surfactant is usually used at levels of 0.5 to 5, percent by weight
based on the total composition.
[0017] The liquid composition of this invention is prepared by thoroughly dispersing the
organic compatible silicone surfactant (C) with the silicone oil (A) using agitation
or other similar means. The wax emulsion is then added into the silicone oil/surfactant
mixture. The final composition is then dispersed or emulsified using a homogonizer,
sonolator or other dispersion means.
[0018] The liquid compositions of this invention are useful for thread lubricants which
are applied using kiss roll application methods. The liquid composition is typically
applied on the thread at concentration of 2 to 15 percent by weight of the thread,
depending on the type of thread being treated. One skilled in the art will be able
to determine the amount necessary to create the best properties in the thread. Since
the composition is liquid, it is not necessary to heat them for the application however,
mild heat, preferably less than 50°C., can be used if desired.
[0019] So that those skilled in the art can understand and appreciate the invention taught
herein, the following examples are presented.
[0020] The term "parts" used herein refers to parts by weight.
Example 1
[0021] Four liquid compositions in Table 1 ere prepared by mixing a silicone surfactant,
DOW CORNING® Q2-3201 SURFACTANT, with a polydimethylsiloxane (3.5 x 10⁻⁴ m²/s (350
cs) at 25°C.) until homogeneous. The wax emulsion was added and the mixture was agitated
vigorously for an additional 15 minutes. The compositions were applied to a spun polyester
thread at a 5% add on level using an ATLAB® finish applicator (simulated kiss roll
application method). The treated thread was evaluated for the Drag Value (the value
that relates to final tension of the thread after it has been pulled over the guides
of an industrial sewing machine). The value reported is an average of the three measurements.
The drag value was also measured on untreated thread and on a thread that was treated
with a commercially available exhaust finish emulsion which was applied using exhaust
finish technology. Results are given in Table 1.
Table 1
| |
Silicone Oil |
Wax Emulsion |
Silicone Surfactant |
% Finish on Yarn |
Drag Value |
| I |
78 |
10(A) |
2 |
4.1 |
240 |
| II |
88 |
10(A) |
2 |
6.3 |
205 |
| III |
78 |
20(B) |
2 |
7.8 |
260 |
| IV |
78 |
20(C) |
2 |
1.6 |
230 |
| V |
Untreated |
755 |
| VI |
Commercially Available Exhaust Finish |
181 |
| (A) Rayolan CPN® produced by Boehme Filatex, Inc. |
| (B) Uscosoft LPD® produced by Ivax Inc. |
| (C) Uscosoft HTW® produced by Ivax Inc. |
Example 2
[0022] Eight liquid compositions in Table 2 were prepared by mixing the silicone surfactant
with the polydimethylsiloxane until homogeneous. The wax emulsion was added and the
mixture was agitated vigorously for an additional 15 minutes. The compositions were
applied to a spun polyester thread at a 5% add on level using a kiss roll application
method. The treated thread was evaluated for the Drag Value (the value that relates
to final tension of the thread after it has been pulled over the guides of an industrial
sewing machine). Results are given in Table 2.
Table 2
| |
Silicone Oil |
Wax Emulsion |
Silicone Surfactant |
Drag Value |
| VII |
78(i) |
20(D) |
2(a) |
260 |
| VIII |
79.5(i) |
20(D) |
0.5(a) |
205 |
| IX |
78(i) |
20(E) |
2(a) |
210 |
| X |
78(ii) |
20(E) |
2(a) |
205 |
| XI |
78(ii) |
20(E) |
2(a) |
240 |
| XII |
78(iii) |
20(A) |
2(a) |
240 |
| XIII |
89(iii) |
10(A) |
1(a) |
260 |
| XIV |
78(iii) |
20(A) |
2(b) |
230 |
| (A) Rayolan® CPN produced by Boehme Filatex, Inc. |
| (D) Emulsion 150-50 by Chemical Corporation of America |
| (E) Emulsion 130-50 by Chemical Corporation of America |
| (i) Polydimethylsiloxane having a viscosity of 5 x 10⁻⁴ m²/s (500 centistokes) at
25°C. |
| (ii) Polydimethylsiloxane having a viscosity of 3.5 x 10⁻⁴ m²/s (350 centistokes)
at 25°C. |
| (iii) Polydimethylsiloxane having a viscosity of 5 x 10⁻⁵ m²/s (50 centistokes) at
25°C. |
| (a) DOW CORNING® Q2-3201 INTERMEDIATE |
| (b) DOW CORNING® 3815C INTERMEDIATE |
Example 3
[0023] A liquid composition was prepared by mixing 81 parts of a polydimethylsiloxane having
a viscosity of 5 x 10⁻⁵ m²/s (50 centistokes) at 25°C. with 2 parts of a silicone
surfactant, DOW CORNING® Q2-3201 INTERMEDIATE, until the silicone surfactant is well
dispersed. A commercially available paraffin wax emulsion, Michem® Emulsion 47960
produced by Michelman Industries was added slowly and stirred for 30 minutes. The
resulting mixture was passed through a sonolator at 5.5MPa (800 PSI), 0.001 orifice.
(Sample XV)
[0024] The liquid composition, Sample XV, was applied at a 5.6% finish level to pink, black
and white spun polyester sewing thread using a kiss roll applicator. Thread count
was 41/2. A comparative test was also done by applying a nonionic silicone/wax emulsion,
50% solids, to the same type of thread at a 5% solids level using a kiss roll applicator.
Results are given in Table 3. Corrosion and mildew are problems identified with use
of the comparative fluid.
Table 3
| Finish |
Friction Index |
| |
White |
Pink |
Black |
| XV |
247 |
273 |
242 |
| Silicone/Wax Emulsion |
305 |
283 |
274 |
Example 4
[0025] The same liquid composition that was prepared in Example 3 (Sample XV) was applied
to a spun polyester (spun poly) and a polyester wrapped polyester (poly/poly) thread
at a 8% finish level using a kiss roll applicator. For comparison a commercially used
hot melt silicone/wax product, 100% solids, was applied at an 8% finish level using
the kiss roll applicator. Tego®-1894, an exhaust finish emulsion (50% solids), produced
by Goldschmidt Corporation was applied at an 8% finish level using a dye bath (exhaust
finish method). Comparative results are given in Table 4.
Table 4
| Finish |
Coefficient of Friction |
| |
Poly/Poly |
Spun Poly |
| XV |
0.19 |
0.18 |
| Hot Melt |
- |
0.20 |
| Tego-1894® |
- |
0.18 |
Example 5
[0026] The same liquid composition that was prepared in Example 3 (Sample XV) was applied
to a polyester wrapped polyester (poly/poly) thread at a 6% finish level using a kiss
roll applicator. For comparison an exhaust emulsion finish product produced by Boehme
Filatex, Inc., Rayolan® T-24, was applied at an 6% finish level using exhaust finish
(dye bath) methods. Results are given in Table 5.
Table 5
| Finish |
Drag Value |
| XV |
240-250 |
| Rayolan® T-24 |
250-280 |
1. A thread treating composition which is liquid at room temperature comprising
(A) at least 60 percent by weight of a silicone oil having a viscosity of 5 x 10⁻⁶
to 5 x 10⁻³ m²/s (5 to 5,000 centistokes) at 25°C;
(B) at least 5 percent by weight of a wax emulsion in which the wax is selected from
paraffin waxes, microcrystalline waxes, semicrystalline waxes, polyethylene waxes,
ester waxes, and natural waxes, which have a melting point of higher than 40°C; and
(C) 0.5 to 5 percent by weight of a silicone surfactant,
the sum of the components adding up to 100 percent by weight.
2. A composition as claimed in Claim 1 wherein the silicone oil has a viscosity of 5
x 10⁻⁶ to 5 x 10⁻⁴ m²/s (5 to 500 centistokes), and the wax emulsion is a paraffin
wax emulsion.
3. A method of treating thread by applying to the thread the composition as described
in Claim 1, using a kiss roll.
1. Mittel zur Behandlung von Fäden, das bei Raumtemperatur flüssig ist, enthaltend
(A) mindestens 60 Gewichtsprozent eines Siliconöls mit einer Viskosität von 5 x 10⁻⁶
bis 5 x 10⁻³ m²/s (5 bis 5.000 Centistoke) bei 25°C;
(B) mindestens 5 Gewichtsprozent einer Wachsemulsion, wobei das Wachs ausgewählt ist
aus Paraffinwachsen, mikrokristallinen Wachsen, halbkristallinen Wachsen, Polyethylenwachsen,
Esterwachsen und natürlichen Wachsen, die einen Schmelzpunkt von mehr als 40°C haben;
und
(C) 0,5 bis 5 Gewichtsprozent eines Silicons als oberflächenaktiven Stoff,
wobei die Summe der Bestandteile sich zu 100 Gewichtsprozent addiert.
2. Mittel nach Anspruch 1, wobei das Siliconöl eine Viskosität von 5 x 10⁻⁶ bis 5 x 10⁻⁴
m²/s (5 bis 500 Centistoke) hat und die Wachsemulsion eine Emulsion eines Paraffinwachses
ist.
3. Verfahren zur Behandlung eines Fadens, bei dem man das im Anspruch 1 beschriebene
Mittel unter Verwendung einer Berührungsrolle auf den Faden aufbringt.
1. Composition de traitement du fil qui est liquide à la température ordinaire, comprenait
(A) au moins 60% en poids d'une huile de silicone ayant une viscosité de 5 x 10⁻⁶
à 5 x 10⁻³ m²/s (5 à 5 000 centistokes) à 25°C;
(B) au moins 5% en poids d'une émulsion de cire dans laquelle la cire est sélectionnée
entre les cires de paraffine, les cires microcristallines, les cires semi-microcristallines,
les cires de polyéthylène, les cires d'esters et les cires naturelles, qui ont un
points de fusion supérieur à 40°C; et
(C) 0,5 à 5% en poids d'un surfactant au silicone,
la somme des composant atteignant 100% en poids.
2. Composition selon Revendication 1, dans laquelle l'huile de silicone a une viscosité
de 5 X 10⁻⁶ à 5 x 10⁻⁴ m²/s (5 à 500 centistokes), et où l'émulsion de cire est une
émulsion de cire de paraffine.
3. Procédé de traitement du fil par application au fil de la composition décrite dans
la Revendication 1, à l'aide d'un rouleau applicateur.