This application claims priority from U.S. provisional patent application serial No. 62/762,815 filed on day 22, 5, 2018 and U.S. provisional patent application serial No. 62/702,337 filed on day 23, 7, 2018, the disclosures of both provisional patent applications being incorporated herein by reference in their entireties.
Detailed Description
Definition of
The term "linear" as used herein to describe the state of the bicomponent filaments, fibers or tapes of the present invention refers to the near or substantially linear state of the formed bicomponent filaments, fibers or tapes of the present invention, which state can be visually observed or qualitatively and/or quantitatively determined. In other words, the phrase "linear or substantially linear bicomponent filament, fiber or tape" or similar terms as used herein may refer to a formed bicomponent filament, fiber or tape which is found, qualitatively and/or quantitatively, to be in a straight or nearly straight arrangement or along a straight or nearly straight line.
The terms "filament" and "fiber" (sometimes used interchangeably herein) as used herein refer to a three-dimensional structure having an elongated morphology. In certain contexts, the term "filament" or "fiber" may also refer to a fine, filamentous object or article.
As used herein, the term "elastomer" or "elastomer component" (or sometimes they are used interchangeably) refers to a material that exhibits the properties of elasticity, low young's modulus (i.e., the ratio of tensile stress to tensile strain), and is capable of deforming when stress is applied and returning to its original shape (i.e., length, volume, shape, etc.) when the stress is removed. Examples of elastomers useful in the present invention include, but are not limited to, polyester or polyether-based polyurethanes.
The terms "shape memory polymer" or "shape memory polymer component" (or sometimes they are used interchangeably) as used herein refer to a unique class of polymers or materials that have the ability to fix a temporary shape and then return to a previous state due to an external stimulus (e.g., heat, radiation, solvent, electrical current, light, magnetic field, or a change in pH). Examples of shape memory polymers useful in the present invention include, but are not limited to, polyester-based or polyether-based shape memory polyurethanes, including, but not limited to, polycaprolactone-based shape memory polymers.
The scope of the invention is not limited by any of the following descriptions. The following examples or embodiments are provided for illustration only.
Reference will now be made in detail to the accompanying drawings. Fig. 1A to 1C schematically depict examples of the configuration of linear bicomponent filaments, fibers or tapes of the present invention. A linear bicomponent filament, fiber or ribbon includes an elastomeric portion and a shape memory polymer portion such that the filament undergoes a deformation-based (stretch-induced) crimp, assuming a substantially helical configuration after being elongated by about 50% to about 300%. Upon heating to a temperature above the recovery temperature, the material reverts to a permanent, approximately linear configuration.
Fig. 1A and 1B show a cross-section of a filament or fiber 100 and fig. 1C shows a cross-section of a tape 200. In each of these arrangements, the shape memory polymer region is indicated by reference numeral 10 and the elastomeric component is indicated by reference numeral 20.
As shown in fig. 1A to 1C, the bicomponent filaments of the present invention can take a variety of configurations. For example, in FIG. 1A, the shape memory polymer 10 is formed in a region offset from the core of the fiber or filament; similarly, in FIG. 1B, the shape memory polymer 10 is also offset from the central core region of the belt. That is, the shape memory polymer region 10 is always asymmetrically positioned with respect to the center of the cross-sectional area of the filament, fiber or tape. In these embodiments, the bicomponent filaments may be made from a weight ratio of 90% to 10% to 90% of a thermoplastic polyurethane elastomer (TPU) and a shape memory polymer. The cross-section may be side-by-side (fig. 1A) or eccentric sheath/core (fig. 1B). For the two-component tape of the present invention (e.g., FIG. 1C), it can also be made from a thermoplastic polyurethane elastomer (TPU) and a shape memory polymer in a weight ratio of 90%: 10% to 10%: 90%.
Fig. 2A-2E illustrate some embodiments of placing or positioning the elastomer and shape memory polymer asymmetrically from a cross-sectional perspective to form a bicomponent filament or fiber. In these embodiments, each of the elastomeric fibers and the shape memory polymer fibers are longitudinally aligned with one another, and the number of fibers between the two polymer fibers is not equal, e.g., in a ratio of 2:1, 3:1, 4:1, 1:2, 1:3, 1:4, etc. In other words, the ratio of elastomeric fibers to shape memory polymer fibers is x: y or y: x, where x is at least 1 less or greater than y in these embodiments. It should be understood that the ratio between the elastomeric fibers and the shape memory polymer fibers need not be an integer in terms of weight ratio. A prerequisite for forming the bicomponent filaments, fibers or tapes of the present invention is to asymmetrically position or arrange the elastomer and shape memory polymer relative to the cross-section of the bicomponent filament, fiber or tape such that the bicomponent filament, fiber or tape of the present invention assumes a linear or substantially linear state or shape in the absence of a corresponding external stimulus, curls and forms a corresponding number of spirals upon being held for a time and released after being stretched or elongated by about 50% to about 300% of its original length, and upon being heated to about 25 to about 90oC is capable of returning to its linear or substantially linear state or shape when the shape returns to temperature.
The present invention relates to a process for the production of filaments, fibres, tapes made of co-extruded shape memory polymers and elastomers having the function of "stretch induced crimp and heat induced de-crimp". This intelligent function stems from a bicomponent filament structure in which the elastomer portion retains good elasticity at various temperatures from room temperature to 90 degrees Celsius, while the shape memory polymer remains below TrProvides pseudoplasticity at a temperature above TrProvides elasticity at the temperature of (a). Therefore, at room temperature (below T)r) After stretching and release, the pseudoplasticity on the shape memory polymer side tends to remain elongated while the elasticity on the elastomeric side is more or less reduced. Thus, self-curling is caused. Subsequently, if the crimped filament, fiber or tape is heated to TrIn the above, the pseudoplasticity of the shape memory polymer is removed and becomes elastic, whichThe pushed coil shape immediately straightens.
As shown in fig. 3, the bicomponent filaments of the present invention are immediately formed into a coiled shape from a substantially linear shape by stretching to a certain value, for example, 50% to 300%, at room temperature and then releasing it to a free-standing state (301). Subsequently, for a coiled shape, the de-coiling process can be easily achieved by heating the filament above the shape recovery temperature of the shape memory polymer (302). In the present invention, the shape-memory polymer used has a shape-recovery temperature higher than room temperature, for example, 25 to 90 degrees celsius.
For bicomponent filament extrusion, a spinneret with a side-by-side or eccentric sheath/core bicomponent configuration is used. TPU with excellent elasticity would be suitable candidates, for example Elastollan C80A10, C85A10, Estane S385A. The shape memory polymer may include Tg(glass transition as trigger temperature) type, e.g. Diaplex 2520, 3520, 4520, or Tm(melting point as trigger temperature) type, e.g. polycaprolactone based shape memory polymers, such as Zhu, Y., Hu, J.,&yeung, K. (2009) ("Effect of soft segment crystallization and hard segment physical crosslinking on shape memory function of antibacterial segmented polyurethane ionomers") ",Acta Biomaterialia5(9), 3346), which is incorporated herein by reference in its entirety. Since curling is caused by stretching, stretching ability and thermoplasticity are prerequisites.
The following examples illustrate the invention in more detail:
estane S385A was selected for the elastomer portion. The hardness was 85A. The ultimate elongation was 780%. Such as literature (Zhu, y., Hu, j.,& Yeung, K. (2009), “Effect of soft segment crystallization and hard segment physical crosslink on shape memory function in antibacterial segmented polyurethane ionomers”, Acta Biomaterialia5(9), 3346) using a shape memory polymer based on polycaprolactone diol (Mn =10000) in the portion of the shape memory polymerThe polymer comprises MDI (4, 4' -methylene bis (phenyl isocyanate)), BDO (1, 4-butanediol) or N, N-bis (2-hydroxyethyl) -isonicotinamide (BIN) in a hard chain segment. T of the shape memory Polymer usedrIs 48 degrees celsius, or the shape memory polymer portion may be T having a temperature of 45 degrees celsiusgDiaplex MM 4520.
Table 1 physical properties of example 1 to example 7.
Examples
|
Shape of
|
Elastic body
|
SMP (shape memory Polymer)
|
Elastomer to SMP weight ratio
|
After diameter (filament) thickness
Degree (with)
|
Elongation%
|
Diameter of the helix
|
Number of spirals per centimeter
|
Shape recovery temperature
|
1
|
Filament yarn
|
Estane®S385A
|
Based on the interior of poly-hexaneEster SMP-1
|
7:3
|
1.2mm
|
100
|
3mm
|
9
|
48℃
|
2
|
Filament yarn
|
Estane®S385A
|
**SMP-2
|
8:2
|
1.2mm
|
100
|
5mm
|
10
|
45℃
|
3
|
Filament yarn
|
Estane®S385A
|
**SMP-2
|
8:2
|
1.2mm
|
150
|
4mm
|
11
|
45℃
|
4
|
Filament yarn
|
Estane®S385A
|
**SMP-2
|
8:2
|
1.2mm
|
200
|
3mm
|
12
|
45℃
|
5
|
Belt
|
Estane®S385A
|
Polycaprolactone-based SMP-3
|
6:4
|
0.7mm
|
100
|
7mm
|
7
|
43℃
|
6
|
Belt
|
Estane®S385A
|
Polycaprolactone-based SMP-3
|
6:4
|
0.7mm
|
200
|
5mm
|
9
|
43℃
|
7
|
Belt
|
Estane®S385A
|
Polycaprolactone-based SMP-3
|
6:4
|
0.7mm
|
300
|
3mm
|
13
|
43℃
|
8
|
Belt
|
Estane®S385A
|
Polycaprolactone-based SMP-3
|
7:3
|
0.9mm
|
100
|
3mm
|
13
|
80℃
|
9
|
Filament yarn
|
Estane®S385A
|
#SMP-4
|
55:45
|
0.100mm
|
100
|
0.508mm
|
32
|
40℃
|
10
|
Filament yarn
|
Estane®S385A
|
Based on polyhexamethylene adipate
SMP-5
|
55:45
|
0.105mm
|
100
|
0.509mm
|
28
|
40℃ |
Note that: -
Polycaprolactone-based SMP-1 was obtained from: zhu, Y., Hu, J.,& Yeung, K., “Effect of soft segment crystallization and hard segment physical crosslink on shape memory function in antibacterial segmented polyurethane ionomers”, Acta Biomaterialia, 2009, 5(9), 3346;
SMP-2 is Diaplex ™ SMP 4520;
polycaprolactone-based SMP-3 was obtained from: zhu Y, Hu J, Choi K F, et al, Crystallization and differentiation of the Crystallization soft segment in a shape-memory polyurethane ion meter [ J]. Journal of Applied Polymer Science, 2008, 107(1):599-609;
#SMP-4 was a dual SMP blend using Diaplex ™ SMP4520 and 3520 in a weight ratio of 50/50;
##SMP-5 is obtained from: chen S., Hu J., Liu Y., et al, Effect of SSL and HSC on morphology and properties of PHA-based SMPU synthesized by bulk polymerization method [ J]. Journal of Polymer Science Part B: Polymer Physics, 2007, 45, 444。
Example 1
For bicomponent filaments with a diameter of 1.2mm, the elastomer Estane S385A and the polycaprolactone-based shape memory polymer were coextruded at a weight ratio of 7:3 (melt flow pump control) using side-by-side nozzles. All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The filaments were cooled from the nozzle by cold water at a temperature of about 15 degrees celsius without any drawing process. The bicomponent filaments prepared may exhibit a "smart-spiral" function wherein upon stretching to 100% elongation and release may yield a coiled shape of 9 spirals per cm with a spiral diameter of 3mm, heating to a shape that returns to straight at about 48-80 degrees celsius.
Example 2
For pairs with a diameter of 1.2mmComponent filaments, elastomer Estane using eccentric nozzle®S385A was coextruded with Diaplex MM4520 shape memory polymer at a weight ratio of 8:2 (melt flow pump control). All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The filaments were cooled from the nozzle by cold water at a temperature of about 15 degrees celsius without any drawing process. The bicomponent filaments prepared may exhibit a "smart-coil" function wherein upon stretching to 100% elongation and release may produce a coiled shape of 10 coils per cm with a coil diameter of 5mm, heating to about 45-50 degrees celsius to return to a straight shape.
Example 3
For bicomponent filaments of 1.2MM diameter, the elastomers Estane S385A and Diaplex MM4520 shape memory polymer were coextruded in a weight ratio of 8:2 (melt flow pump control) using an eccentric nozzle. All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The filaments were cooled from the nozzle by cold water at a temperature of about 15 degrees celsius without any drawing process. The bicomponent filaments prepared may exhibit a "smart-coil" function wherein upon stretching to 150% elongation and release may yield a coiled shape of 11 coils per cm with a coil diameter of 4mm, heating to about 45 degrees celsius to return to a straight shape.
Example 4
For bicomponent filaments with a diameter of 1.2mm, the elastomer Estane was extruded using an eccentric nozzle®S385A was coextruded with Diaplex MM4520 shape memory polymer at a weight ratio of 8:2 (melt flow pump control). All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3)190-. The screw rotation speed is 180-200 rpm. The filaments were cooled from the nozzle by cold water at a temperature of about 15 degrees celsius without any drawing process. The bicomponent filaments prepared may exhibit a "smart-spiral" function wherein upon stretching to 200% elongation and release may yield a coiled shape with a spiral diameter of 3mm, 12 spirals per cm, heating to a shape that returns to straight at about 45-60 degrees celsius.
For elastomer Estane using an eccentric nozzle®S385A and polyurethane based shape memory polymer bicomponent filaments with a diameter of 1.2mm were coextruded at a weight ratio of 8:2 (melt flow pump control), the helix diameter and the number of helices per cm were measured (fig. 4A). The helix diameter decreases from 5mm to 3mm and the number of helices per cm increases from 10 to 12 as the elongation percentage is from 100 to 200%.
Example 5
For a two-component tape having a thickness of 0.7mm, the elastomer Estane was grooved using a layer-by-layer grooved die®S385A was coextruded with a polycaprolactone-based shape memory polymer at a weight ratio of 6:4 (melt flow pump control). All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The tape was cooled from the nozzle by cold water at a temperature of about 15 c without any stretching process. The prepared two-component tape may exhibit a "smart-spiral" function, wherein upon stretching to 100% elongation and release may yield a coiled shape with 7 spirals per cm with 7mm spiral diameter, heating to about 43 degrees celsius to return to a straight shape.
Example 6
For a bi-component tape having a thickness of 0.7mm, elastomeric Estane S385A and polycaprolactone-based shape memory polymer were coextruded using a layer-by-layer slot die in a weight ratio of 6:4 (melt flow pump control). All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The tape was cooled from the nozzle by cold water at a temperature of about 15 c without any stretching process. The prepared two-component tape may exhibit a "smart-spiral" function, wherein stretching to 200% elongation and release may yield a coiled shape with a spiral diameter of 5mm, 9 spirals per cm, heating to about 43 degrees celsius to return to a straight shape.
Example 7
For a bi-component tape having a thickness of 0.7mm, elastomeric Estane S385A and polycaprolactone-based shape memory polymer were coextruded using a layer-by-layer slot die in a weight ratio of 6:4 (melt flow pump control). All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The tape was cooled from the nozzle by cold water at a temperature of about 15 c without any stretching process. The prepared two-component tape may exhibit a "smart-spiral" function, wherein stretching to 300% elongation and release may yield a coiled shape with a spiral diameter of 3mm, 13 spirals per cm, heating to about 43 degrees celsius to return to a straight shape.
The spiral diameter and the number of spirals per centimeter were measured on bicomponent tapes of 0.7mm thickness coextruded with elastomer Estane S385A and polycaprolactone-based shape memory polymer in a weight ratio of 6:4 (melt flow pump control) using a layer-by-layer slot die (FIG. 4B). The helix diameter decreases from 7mm to 3mm and the number of helices per cm increases from 7 to 13 as the elongation percentage is from 100 to 200%.
Example 8
For a bi-component tape having a thickness of 0.9mm, elastomeric Estane S385A and polycaprolactone-based shape memory polymer were coextruded using a layer-by-layer slot die in a weight ratio of 7:3 (melt flow pump control). All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The tape was cooled from the nozzle by cold water at a temperature of about 15 c without any stretching process. The prepared two-component tape may exhibit a "smart-spiral" function, wherein upon stretching to 100% elongation and release may yield a coiled shape with a spiral diameter of 3mm, 13 spirals per cm, heating to a shape that returns to straight at about 40-80 degrees celsius.
Example 9
For bicomponent filaments of 0.1mm diameter, elastomer Estane S385A was co-extruded with 50/50 weight ratio of Diaplex shape memory polymer 4520 and 3520 double shape memory polymer blends in a weight ratio of 55:45 (melt flow pump control) using side-by-side nozzles. All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The filaments were cooled from the nozzle by cold water at a temperature of about 15 degrees celsius without any drawing process. The bicomponent filaments prepared may exhibit a "smart-spiral" function wherein upon stretching to 100% elongation and release may yield a coiled shape of 32 spirals per centimeter having a spiral diameter of 0.508 mm, heating to a shape that returns to straight at about 40 degrees celsius.
Example 10
For bicomponent filaments with a diameter of 0.105mm, the elastomer Estane S385A and the shape memory polymer based on polyhexamethylene adipate were coextruded using a side-by-side nozzle in a weight ratio of 55:45 (melt flow pump control). All pellets must be dried at 104 degrees celsius for 2-4 hours before processing. The barrel temperature of the extruder is 180-195 ℃ (zone 1), 185-200 ℃ (zone 2), 190-205 ℃ (zone 3) and 190-200 ℃ (mold zone). The screw rotation speed is 180-200 rpm. The filaments were cooled from the nozzle by cold water at a temperature of about 15 degrees celsius without any drawing process. The bicomponent filaments prepared may exhibit a "smart-spiral" function wherein upon stretching to 100% elongation and release may yield a coiled shape of 28 spirals per centimeter having a spiral diameter of 0.508 mm, heating to a shape that returns to straight at about 40 degrees celsius.
It will be apparent to those skilled in the art that many more modifications besides those already described are possible without departing from the inventive concepts herein. The inventive subject matter, therefore, is not to be restricted except in the spirit of the present disclosure. Moreover, in interpreting the disclosure, all terms should be interpreted in the broadest possible manner consistent with the context. In particular, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a reference to an element, component, or step is intended to refer to that element, component, or step as it may exist, or utilized, or combined with other elements, components, or steps that are not expressly referenced.