EP2632866A2 - Thermal fiber drawing (tfd) with added core break-up process and particles therefrom - Google Patents

Thermal fiber drawing (tfd) with added core break-up process and particles therefrom

Info

Publication number
EP2632866A2
EP2632866A2 EP11837022.0A EP11837022A EP2632866A2 EP 2632866 A2 EP2632866 A2 EP 2632866A2 EP 11837022 A EP11837022 A EP 11837022A EP 2632866 A2 EP2632866 A2 EP 2632866A2
Authority
EP
European Patent Office
Prior art keywords
core
fiber
particles
tfd
extended
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP11837022.0A
Other languages
German (de)
French (fr)
Other versions
EP2632866A4 (en
Inventor
Ayman Abouraddy
Guangming TAO
Daosheng S. DENG
Yoel Fink
Esmaeil H. BANAEI
Steven G. Johnson
Soroush SHABAHANG
Joshua J. KAUFMAN
Xiangdong Liang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Massachusetts Institute of Technology
University of Central Florida Research Foundation Inc
Original Assignee
University of Central Florida Research Foundation Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by University of Central Florida Research Foundation Inc filed Critical University of Central Florida Research Foundation Inc
Publication of EP2632866A2 publication Critical patent/EP2632866A2/en
Publication of EP2632866A4 publication Critical patent/EP2632866A4/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • B01J2/006Coating of the granules without description of the process or the device by which the granules are obtained
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2/00Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/12Powdering or granulating
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/12Powdering or granulating
    • C08J3/126Polymer particles coated by polymer, e.g. core shell structures
    • DTEXTILES; PAPER
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02JFINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J1/00Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
    • D02J1/22Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
    • D02J1/224Selection or control of the temperature during stretching
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2300/00Characterised by the use of unspecified polymers
    • C08J2300/22Thermoplastic resins

Definitions

  • Disclosed embodiments relate to thermal fiber drawing (TFD)-related processing and particles therefrom.
  • TFD thermal fiber drawing
  • microparticles and nanoparticles generally rely on nucleation, chemical reactions, or self-assembly.
  • the particles produced using such approaches are typically characterized by a large dispersion in the size and shape distribution, and are generally hampered by coalescence and agglomeration during particle growth.
  • TFD thermal fiber drawing
  • TFD is a process in which a macrostructured preform comprising a multi-material fiber (outer cladding and at least one inner core) is heated and drawn into an extended length to form an extended multi- material fiber.
  • TFD has been demonstrated to be capable of producing extremely long lengths (e.g., hundreds of meters) of uniform and ordered nano-filaments, generally from glassy insulating (dielectric) materials.
  • Disclosed TFD-based methods processes may be contrasted from known TFD methods.
  • the preform is thermally drawn in a high- viscosity regime (> 10 6 Pa s) and the extended multi-material fiber emerging from the heating zone is cooled quickly to arrest the development of any axial instability.
  • disclosed methods instead promote axial instability by maintaining the extended fiber at an elevated temperature for an extended period of time, allowing the core(s) to break up into uniformly sized droplets which are "frozen" in situ upon cooling to form a plurality of microparticles or nanoparticles embedded in the outer cladding.
  • the fiber core(s) and cladding correspond to the dispersed and continuous phases, respectively.
  • the core particles may be then released if desired by removing the cladding, such as by solvent removal.
  • Disclosed methods allow for the fabrication of embedded particle arrangements comprising monodisperse particles over a wide and selectable range of sizes, extending from about 5 nm to about 1 mm, and from a variety of materials, including, but not limited to glasses, polymers, liquids, and metals.
  • the particles are spherical in shape, and are molecularly smooth providing a root mean square (rms) roughness ⁇ 1 nm.
  • the core comprises a plurality of cores, and after disclosed thermally treating provides a three dimensional distribution of core particles embedded in the cladding layer.
  • the three dimensional distribution of core particles can include includes periodicity providing a standard deviation of center-to-center particle spacing ⁇ 5 of the average center to center particle spacing in at least a first and a second dimension transverse to the length direction of the extended multi-material fiber.
  • Disclosed embodiments are top- down non-lithographic approaches which may be contrasted with conventional techniques for forming such particles that are bottom-up and rely on nucleation, chemical reactions, or self- assembly of the particles.
  • FIG. 1 is a flow chart that shows steps in an example TFD-based method for the efficient and scalable fabrication of microparticles or nanoparticles, according to an example embodiment.
  • FIG. 2A shows an example fiber tapering setup
  • FIG. 2B a scanned optical micrograph of a fiber cross section with a 20- ⁇ core diameter
  • FIG. 2C a scanned image of a typical fiber taper
  • FIG. 2D shows a magnified scanned image of the taper center (corresponding to the dotted box in FIG. 2C) showing the core broken into a periodic string of core droplets oriented along the axial (drawing) direction, according to example embodiments.
  • FIGs. 3A-E are scanned optical micrographs of the side view of fiber tapers produced at different temperatures, but with the same tapering speed (2 mm/s) and tapering distance (15 mm) showing different stages of the core breakup process, according to example embodiments.
  • FIGs. 4A and 4B are scanned SEM micrograph of 27,000 200-nm-diameter intact glass cores exposed from a 1-mm-outer-diameter fiber cross section after dissolving the polymer cladding, according to example embodiments. Periodicity of the glass (G) in the transverse directions is demonstrated.
  • FIG. 5 is a scanned high-magnification SEM micrograph of a portion of the fiber core shown in FIGs. 4A and 4B.
  • the stacked fibers in the preform were found to produce a hexagonal lattice (see dashed lines).
  • 200-nm glass cores are located as shown in the inset.
  • FIGs. 6A-D are scanned SEMs of well-ordered, three-dimensional particle emulsion held in the polymer cladding, according to example embodiments.
  • FIG. 6A is a scanned SEM micrograph of a 1-mm-diameter fiber cross section containing 80 7 ⁇ - diameter cores.
  • FIGs. 6C and 6D are scanned transmission optical micrographs of the fiber side view before and after breakup (via global heating), respectively, showing the resulting spatial distribution of particles immobilized in the cladding (scaffold) is well-ordered in all 3 dimensions.
  • Disclosed embodiments include TFD-based methods applied to multi-material fibers for the efficient and scalable fabrication of microparticles or nanoparticles.
  • Disclosed methods include an added thermally-based process applied to the extended multi-material fiber having an extended core generated by TFD, that results in the extended core breaking up into a plurality of microparticles or nanoparticles that are embedded in the cladding layer.
  • Disclosed processes may be contrasted with known TFD processes by the addition of a thermally-based process after the TFD of the multi-material fiber that has been found to result in the extended core of the drawn multi-material fiber breaking up into a plurality of particles.
  • FIG. 1 is a flow chart that shows steps in an example TFD-based method 100 for the efficient and scalable fabrication of microparticles or nanoparticles, according to an example embodiment.
  • Step 101 comprises providing a multi-material fiber having at least one core comprising a first material and an outer first cladding layer comprising a second material different from the first material outside the core.
  • the first and second material generally have similar softening temperatures that allows for the first and second materials to be consolidated together and then co-drawn from the same fiber preform, such as a softening temperature within 50 °C of one another.
  • Step 101 can comprise preparing a multi-material macroscopic preform with a core assembled from the intended particle constituent materials encased in a scaffold material that provides a cladding layer.
  • Step 102 comprises TFD the multi-material fiber to increase a length of the multi-material fiber to form an extended multi-material fiber having an extended core such that the core diameter (or other cross section dimension) in the extended core is reduced to approach that of the desired particle size.
  • the temperature selected is high enough to allow for the preform to be drawn continuously into a fiber.
  • the fiber can be rapidly cooled (e.g. with active cooling) after TFD to arrest the development of axial instability.
  • the TFD can optionally include two or more TFD steps.
  • Step 103 comprises thermally treating the extended multi-material fiber under conditions (e.g., temperature, time, and tapering speed) that cause an axial breaking up of the extended core to form a plurality of core particles embedded in the cladding.
  • the maximum temperature utilized in step 103 is generally higher than the maximum temperature used in step 102, such as by a temperature higher by at least 10 °C.
  • the thermal treatment of the drawn fiber controllably induces the break-up of the extended core(s).
  • the extended core breaks-up into an orderly (periodic) sequence of oriented, smooth-surfaced structured spherical particles held immobile in the cladding.
  • the thermally treating can comprise holding a temperature fixed along a fiber axis of the multi-material fiber, and using a sufficient heating time to form the plurality of core particles.
  • the thermally treating can comprise applying a temperature gradient along a fiber axis of the multi-material fiber.
  • the core particles may be released from the cladding.
  • the core particles embedded in the cladding may be released by dissolving the cladding material in a suitable solvent that does not affect the core particles.
  • the breaking up of the extended core(s) of the drawn multi-material fiber into a plurality of particles is believed to be based on Plateau-Rayleigh (PR) capillary instability during the TFD-based tapering of a multi-material fiber.
  • the fiber core can comprise a glass and the cladding comprises an amorphous thermoplastic polymer.
  • PR instability is believed to be manifested in the breakup of the core into a periodic string of size-tunable micro-scale droplets embedded along the fiber axis.
  • size tuning can be provided by TFD processing such that the extended core(s) has a cross sectional dimension (e.g., a diameter) that approaches the desired particle size.
  • Fiber tapering is a process that allows for obtaining a wider range of parameters as compared to fiber drawing.
  • steps in an example fiber tapering apparatus 100 are shown.
  • a fiber 110 is inserted in a movable heating zone 115 for a fixed (predetermined) time before both ends of the fiber are pulled symmetrically in opposite directions by the motor 130 together with rollers 132, cabling 133 and end holders 134 as shown in FIG. 2A.
  • a first parameter is the temperature T, which determines the viscosity of the respective fiber materials.
  • the second parameter is the tapering distance L which is defined as the length by which the fiber is elongated after softening, that determines the final diameter (or other cross sectional area) of the fiber taper.
  • a third parameter is the tapering speed v, which determines the dwelling time in the heating zone 115. Once the tapering ends, the heating zone is removed and the extended fiber can be cooled, such as in air. Alternatively, active cooling may be used.
  • a first parameter is the temperature T, which as with TFD determines the viscosity of the respective fiber materials.
  • a second optional parameter is the tapering speed v.
  • An example fiber used in experiments performed comprised a glassy chalcogenide semiconductor (As 2 Se 3 ) core having a diameter in the range 5 ⁇ - 20 ⁇ with a thermoplastic polymer cladding comprising PES having an outer diameter of 1 mm as depicted in FIG. 2B.
  • An example of a typical taper is shown in FIG. 2C, with the central tapered section 230 observed so that the continuous and uniform extended glass core shown evolved after post tapering thermally processing into a periodic string of core droplet particles 237 as depicted in FIG. 2D. It is noted that the apparent size of the core in FIG. 2C and the droplets in FIG. 2D are larger than their actual sizes due to magnification resulting from the curvature of the fiber outer surface.
  • Disclosed embodiments also include compositions of matter comprising a plurality of core particles embedded in a scaffold.
  • an embedded particle arrangement comprises a multi-material fiber having a length > one hundred times its cross sectional area, where the multi-material fiber includes a cladding material providing a continuous phase for said multi-material fiber, and a plurality of particles along at least a portion of the fiber length embedded in the cladding material.
  • the plurality of particles are separated from one another, have a median size from 5 nm to 1 mm, are spherical in shape, and are molecularly smooth providing a root mean square (rms) roughness ⁇ 1 nm.
  • the cladding material in one embodiment comprises a polymer, such as a thermoplastic polymer.
  • the plurality of particles are arranged in a three dimensional distribution.
  • the three dimensional distribution of particles can include periodicity providing a standard deviation of center-to-center particle spacing ⁇ 5% of the average center to center particle spacing in at least a first and a second dimension transverse to the length dimension of the multi-material fiber.
  • the transverse periodicity is controllable at the fabrication stage through the stack-and-draw process.
  • a periodicity of ⁇ 15% (such as about 10%) of the average center- to-center particle spacing can also be provided in the length dimension of the multi-material fiber.
  • the plurality of particles can be uniformly sized providing a ⁇ 10% standard deviation in particle size with respect to an average (mean) size of the particles.
  • the particles in the embedded particle arrangement include a first hemisphere comprising a first material and a second hemisphere comprising a second material different from said first material.
  • the first material can comprises a first glass and the second material comprises a second glass.
  • Disclosed particles can comprise spherical particles including a first hemisphere comprising a first material and a second hemisphere comprising a second material different from the first material.
  • the first material can comprise a first glass and the second material a second glass different from the first glass to provide "Janus particles" that are generally defined as spherical glass particles with one of the hemispheres being one material and the other hemisphere being another material.
  • Disclosed processing may also be extended to multiple sectors (e.g., 3, 4, 5 ...) of a cylinder to form spherical particles with more sophisticated sub-structure.
  • Example applications include cosmetics, biomedical (e.g., drug delivery), chemical and biological catalysts, and paints ( particles are held as a colloid in a solution).
  • As 2 Se 3 is known to has a melting point of about 360 °C and a glass transition temperature of about 180 °C.
  • the PES used had a glass transition temperature of about 230 °C.
  • Static heating was also studied. Static heating as used herein refers to the only parameter being varied is the temperature (no pulling/tapering). The Inventor measured the breakup time ⁇ over the range of temperatures for fibers with initial core diameter ⁇ , where ⁇ was measured from the start of heating until initiation of breakup. The measurements revealed that ⁇ depends inversely on temperature.
  • the Inventor also examined the effect of each fiber tapering parameter (L, T, and v) while holding the other two parameters fixed.
  • the Inventor adopted a simple model for this system based on a quasi-static extension to the static Tomotika model. This model decouples the effect of heating on the core from the dynamics of tapering.
  • the Inventor thus used the static results for the temperature-dependent instability time ⁇ and then added the geometric effect of size change during tapering.
  • This model yields results in quantitative agreement with our observations despite its simplicity within the margin of error in the measurements performed.
  • the final diameter of the fiber taper is also approximately constant. At high speeds, the dwelling time may be less than ⁇ for the final core diameter, and the core thus remains intact. At lower speeds, the fiber dwells for a longer time in the heating zone thus having the opportunity to reach ⁇ and thus breakup. The breakup of the larger-diameter core during tapering results in longer period, and then the droplets further separate if the tapering process continues. The period was found to be inversely proportional with the drawing speed.
  • microparticles or nanoparticles may be used to fabricate microparticles or nanoparticles.
  • the particle size as disclosed herein may be tuned by adjusting the tapering parameters, and the physical process described here hence offers an unconventional non- lithographic, top-down approach to fabricating micro and nano-structures using non- traditional materials combinations.
  • the Inventor produced core particles at three different sizes, 5, 2, and 1 ⁇ , where particle size was tuned by varying the tapering speed.
  • the size of particles that may be fabricated using disclosed methods extends over a very wide range, such as extending from 1 mm down to approximately 5 nm.
  • the particles can be highly spherical particles.
  • the Inventor demonstrated the above-described process with a polymer core.
  • the Inventor observed the same particle generation phenomena occurred with polymer cores that occurred with glass cores. Therefore, disclosed fiber tapering processes can also be used to fabricate micro- and nano-particles of polymers.
  • the shape of the cylinder of the material can be selected that is desire to break up before the first fiber drawing step.
  • two hemi-spheres of different materials can be used.
  • the result is "Janus- particles", which are particles formed of two hemispheres of different core materials.
  • the process may also be extended to multiple sectors of a cylinder to form spherical particles with a sophisticated sub-structure.
  • Disclosed embodiments include TFD-based methods to form high-density macroscopic arrays of well-ordered nanowires that can range from about 5 nm to 1 mm.
  • a centimeter-scale macroscopic cylindrical preform containing the nanowire material in the core encased in a polymer scaffold cladding was thermally drawn in the viscous state to a fiber.
  • TFD process continuous reduction of the diameter of an amorphous semiconducting chalcogenide glass was demonstrated.
  • Thermally drawing was used to generate hundreds of meters of continuous sub-5-nm-diameter nanowires. Using this approach macroscopic lengths of high- density, well-ordered, globally oriented nanowire arrays can be produced.
  • FIGs. 4A-6D demonstrate core periodicity following disclosed processing applied to a fiber preform including a large number of glass cores encased in a polymer cladding.
  • the resulting particles are ordered since the instability growth is dominated by a single wavelength.
  • particle order is imposed upon the cores during the stacking process to form the preform.
  • FIGs. 4A and 4B are scanned SEM micrograph of 27,000 200-nm-diameter intact glass cores exposed from a 1-mm-outer-diameter fiber cross section after dissolving the polymer cladding.
  • G represents glass
  • As 2 Se 3 As 2 Se 3
  • P the polymer PES. Periodicity of the glass in the transverse directions is demonstrated.
  • FIG. 5 is a scanned high-magnification SEM micrograph of a portion of the fiber core shown in FIGs. 4A and 4B.
  • the stacked fibers in the preform were found to produce a hexagonal lattice (see dashed lines).
  • 200-nm glass cores are located as shown in the inset.
  • FIGs. 6A-D are scanned SEMs of well-ordered, three-dimensional particle emulsion held in the polymer cladding.
  • FIG. 6A is a scanned SEM micrograph of a 1-mm- diameter fiber cross section containing 80 7 ⁇ m-diameter cores.
  • FIGs. 6C and 6D are scanned transmission optical micrographs of the fiber side view before and after breakup (via global heating), respectively, showing the resulting spatial distribution of particles held immobilized in the cladding (scaffold) is well-ordered in all 3 dimensions.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Crystallography & Structural Chemistry (AREA)
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  • Inorganic Fibers (AREA)

Abstract

A thermal fiber drawing (TFD)-based method for forming particles includes providing a multi-material fiber having at least one core including a first material and an outer first cladding layer including a second material different from the first material outside the core. TFD is used to increase a length of the multi-material fiber to form an extended multi-material fiber having an extended core such that the core diameter or other core cross sectional dimension approaches the desired particle size after subsequent break-up. The extended multi-material fiber is thermally treated under conditions that cause a breaking up of the extended core to form a plurality of core particles embedded in the cladding layer. The core particles can optionally be removed from the cladding layer.

Description

THERMAL FIBER DRAWING (TFD) WITH ADDED CORE BREAK-UP PROCESS AND
PARTICLES THEREFROM
FIELD
[0001] Disclosed embodiments relate to thermal fiber drawing (TFD)-related processing and particles therefrom.
BACKGROUND
[0002] Known approaches forming microparticles and nanoparticles generally rely on nucleation, chemical reactions, or self-assembly. The particles produced using such approaches are typically characterized by a large dispersion in the size and shape distribution, and are generally hampered by coalescence and agglomeration during particle growth.
SUMMARY
[0003] Disclosed embodiments include thermal fiber drawing (TFD)-based methods for the efficient and scalable fabrication of microparticles or nanoparticles. TFD is a process in which a macrostructured preform comprising a multi-material fiber (outer cladding and at least one inner core) is heated and drawn into an extended length to form an extended multi- material fiber. TFD has been demonstrated to be capable of producing extremely long lengths (e.g., hundreds of meters) of uniform and ordered nano-filaments, generally from glassy insulating (dielectric) materials.
[0004] Disclosed TFD-based methods processes may be contrasted from known TFD methods. In order to ensure the integrity of the core(s), in known TFD methods the preform is thermally drawn in a high- viscosity regime (> 106 Pa s) and the extended multi-material fiber emerging from the heating zone is cooled quickly to arrest the development of any axial instability. In contrast, disclosed methods instead promote axial instability by maintaining the extended fiber at an elevated temperature for an extended period of time, allowing the core(s) to break up into uniformly sized droplets which are "frozen" in situ upon cooling to form a plurality of microparticles or nanoparticles embedded in the outer cladding. The fiber core(s) and cladding correspond to the dispersed and continuous phases, respectively. The core particles may be then released if desired by removing the cladding, such as by solvent removal.
[0005] Disclosed methods allow for the fabrication of embedded particle arrangements comprising monodisperse particles over a wide and selectable range of sizes, extending from about 5 nm to about 1 mm, and from a variety of materials, including, but not limited to glasses, polymers, liquids, and metals. In most embodiments the particles are spherical in shape, and are molecularly smooth providing a root mean square (rms) roughness < 1 nm.
[0006] In one embodiment the core comprises a plurality of cores, and after disclosed thermally treating provides a three dimensional distribution of core particles embedded in the cladding layer. The three dimensional distribution of core particles can include includes periodicity providing a standard deviation of center-to-center particle spacing <5 of the average center to center particle spacing in at least a first and a second dimension transverse to the length direction of the extended multi-material fiber. Disclosed embodiments are top- down non-lithographic approaches which may be contrasted with conventional techniques for forming such particles that are bottom-up and rely on nucleation, chemical reactions, or self- assembly of the particles.
BRIEF DESCRIPTION OF THE DRAWINGS
[0007] FIG. 1 is a flow chart that shows steps in an example TFD-based method for the efficient and scalable fabrication of microparticles or nanoparticles, according to an example embodiment.
[0008] FIG. 2A shows an example fiber tapering setup, FIG. 2B a scanned optical micrograph of a fiber cross section with a 20-μιη core diameter, FIG. 2C a scanned image of a typical fiber taper, while FIG. 2D shows a magnified scanned image of the taper center (corresponding to the dotted box in FIG. 2C) showing the core broken into a periodic string of core droplets oriented along the axial (drawing) direction, according to example embodiments.
[0009] FIGs. 3A-E are scanned optical micrographs of the side view of fiber tapers produced at different temperatures, but with the same tapering speed (2 mm/s) and tapering distance (15 mm) showing different stages of the core breakup process, according to example embodiments.
[0010] FIGs. 4A and 4B are scanned SEM micrograph of 27,000 200-nm-diameter intact glass cores exposed from a 1-mm-outer-diameter fiber cross section after dissolving the polymer cladding, according to example embodiments. Periodicity of the glass (G) in the transverse directions is demonstrated.
[0011] FIG. 5 is a scanned high-magnification SEM micrograph of a portion of the fiber core shown in FIGs. 4A and 4B. The stacked fibers in the preform were found to produce a hexagonal lattice (see dashed lines). At each lattice site 80 200-nm glass cores are located as shown in the inset.
[0012] FIGs. 6A-D are scanned SEMs of well-ordered, three-dimensional particle emulsion held in the polymer cladding, according to example embodiments. FIG. 6A is a scanned SEM micrograph of a 1-mm-diameter fiber cross section containing 80 7 μιη- diameter cores. FIG. 6B is a higher-magnification scanned SEM micrograph of the 80 cores, G=As2Se3 and P= polyethersulfone (PES). FIGs. 6C and 6D are scanned transmission optical micrographs of the fiber side view before and after breakup (via global heating), respectively, showing the resulting spatial distribution of particles immobilized in the cladding (scaffold) is well-ordered in all 3 dimensions.
DETAILED DESCRIPTION
[0013] Disclosed embodiments in this Disclosure are described with reference to the attached figures, wherein like reference numerals are used throughout the figures to designate similar or equivalent elements. The figures are not drawn to scale and they are provided merely to illustrate the disclosed embodiments. Several aspects are described below with reference to example applications for illustration. It should be understood that numerous specific details, relationships, and methods are set forth to provide a full understanding of the disclosed embodiments. One having ordinary skill in the relevant art, however, will readily recognize that the subject matter disclosed herein can be practiced without one or more of the specific details or with other methods. In other instances, well-known structures or operations are not shown in detail to avoid obscuring structures or operations that are not well-known. This Disclosure is not limited by the illustrated ordering of acts or events, as some acts may occur in different orders and/or concurrently with other acts or events. Furthermore, not all illustrated acts or events are required to implement a methodology in accordance with this Disclosure.
[0014] Notwithstanding that the numerical ranges and parameters setting forth the broad scope of this Disclosure are approximations, the numerical values set forth in the specific examples are reported as precisely as possible. Any numerical value, however, inherently contains certain errors necessarily resulting from the standard deviation found in their respective testing measurements. Moreover, all ranges disclosed herein are to be understood to encompass any and all sub-ranges subsumed therein. For example, a range of "less than 10" can include any and all sub-ranges between (and including) the minimum value of zero and the maximum value of 10, that is, any and all sub-ranges having a minimum value of equal to or greater than zero and a maximum value of equal to or less than 10, e.g., 1 to 5.
[0015] Disclosed embodiments include TFD-based methods applied to multi-material fibers for the efficient and scalable fabrication of microparticles or nanoparticles. Disclosed methods include an added thermally-based process applied to the extended multi-material fiber having an extended core generated by TFD, that results in the extended core breaking up into a plurality of microparticles or nanoparticles that are embedded in the cladding layer. Disclosed processes may be contrasted with known TFD processes by the addition of a thermally-based process after the TFD of the multi-material fiber that has been found to result in the extended core of the drawn multi-material fiber breaking up into a plurality of particles.
[0016] FIG. 1 is a flow chart that shows steps in an example TFD-based method 100 for the efficient and scalable fabrication of microparticles or nanoparticles, according to an example embodiment. Step 101 comprises providing a multi-material fiber having at least one core comprising a first material and an outer first cladding layer comprising a second material different from the first material outside the core. The first and second material generally have similar softening temperatures that allows for the first and second materials to be consolidated together and then co-drawn from the same fiber preform, such as a softening temperature within 50 °C of one another. Step 101 can comprise preparing a multi-material macroscopic preform with a core assembled from the intended particle constituent materials encased in a scaffold material that provides a cladding layer.
[0017] Step 102 comprises TFD the multi-material fiber to increase a length of the multi-material fiber to form an extended multi-material fiber having an extended core such that the core diameter (or other cross section dimension) in the extended core is reduced to approach that of the desired particle size. The temperature selected is high enough to allow for the preform to be drawn continuously into a fiber. The fiber can be rapidly cooled (e.g. with active cooling) after TFD to arrest the development of axial instability. The TFD can optionally include two or more TFD steps.
[0018] Step 103 comprises thermally treating the extended multi-material fiber under conditions (e.g., temperature, time, and tapering speed) that cause an axial breaking up of the extended core to form a plurality of core particles embedded in the cladding. The maximum temperature utilized in step 103 is generally higher than the maximum temperature used in step 102, such as by a temperature higher by at least 10 °C. In this step the thermal treatment of the drawn fiber controllably induces the break-up of the extended core(s). In a typical embodiment the extended core breaks-up into an orderly (periodic) sequence of oriented, smooth-surfaced structured spherical particles held immobile in the cladding. The thermally treating can comprise holding a temperature fixed along a fiber axis of the multi-material fiber, and using a sufficient heating time to form the plurality of core particles. In another embodiment the thermally treating can comprise applying a temperature gradient along a fiber axis of the multi-material fiber.
[0019] In optional step 104, the core particles may be released from the cladding. For example, the core particles embedded in the cladding may be released by dissolving the cladding material in a suitable solvent that does not affect the core particles.
[0020] Although not necessary to practice disclosed embodiments, the breaking up of the extended core(s) of the drawn multi-material fiber into a plurality of particles is believed to be based on Plateau-Rayleigh (PR) capillary instability during the TFD-based tapering of a multi-material fiber. In one particular embodiment the fiber core can comprise a glass and the cladding comprises an amorphous thermoplastic polymer. PR instability is believed to be manifested in the breakup of the core into a periodic string of size-tunable micro-scale droplets embedded along the fiber axis. As disclosed above, size tuning can be provided by TFD processing such that the extended core(s) has a cross sectional dimension (e.g., a diameter) that approaches the desired particle size.
[0021] Fiber tapering is a process that allows for obtaining a wider range of parameters as compared to fiber drawing. Referring to FIG. 2A, steps in an example fiber tapering apparatus 100 are shown. In fiber tapering a fiber 110 is inserted in a movable heating zone 115 for a fixed (predetermined) time before both ends of the fiber are pulled symmetrically in opposite directions by the motor 130 together with rollers 132, cabling 133 and end holders 134 as shown in FIG. 2A.
[0022] There are generally at least three controllable fiber tapering parameters that may be used for process control of TFD. A first parameter is the temperature T, which determines the viscosity of the respective fiber materials. The second parameter is the tapering distance L which is defined as the length by which the fiber is elongated after softening, that determines the final diameter (or other cross sectional area) of the fiber taper. A third parameter is the tapering speed v, which determines the dwelling time in the heating zone 115. Once the tapering ends, the heating zone is removed and the extended fiber can be cooled, such as in air. Alternatively, active cooling may be used.
[0023] There are generally at least two parameters other than time that may be used for process control of thermally treating of the extended multi-material fiber to cause a breaking up of the extended core to form a plurality of core particles. A first parameter is the temperature T, which as with TFD determines the viscosity of the respective fiber materials. A second optional parameter is the tapering speed v.
[0024] An example fiber used in experiments performed comprised a glassy chalcogenide semiconductor (As2Se3) core having a diameter in the range 5 μιη - 20 μιη with a thermoplastic polymer cladding comprising PES having an outer diameter of 1 mm as depicted in FIG. 2B. An example of a typical taper is shown in FIG. 2C, with the central tapered section 230 observed so that the continuous and uniform extended glass core shown evolved after post tapering thermally processing into a periodic string of core droplet particles 237 as depicted in FIG. 2D. It is noted that the apparent size of the core in FIG. 2C and the droplets in FIG. 2D are larger than their actual sizes due to magnification resulting from the curvature of the fiber outer surface.
[0025] Disclosed embodiments also include compositions of matter comprising a plurality of core particles embedded in a scaffold. In one embodiment an embedded particle arrangement comprises a multi-material fiber having a length > one hundred times its cross sectional area, where the multi-material fiber includes a cladding material providing a continuous phase for said multi-material fiber, and a plurality of particles along at least a portion of the fiber length embedded in the cladding material. The plurality of particles are separated from one another, have a median size from 5 nm to 1 mm, are spherical in shape, and are molecularly smooth providing a root mean square (rms) roughness < 1 nm.
[0026] The cladding material in one embodiment comprises a polymer, such as a thermoplastic polymer. For embodiments corresponding to use of performs including a plurality of cores, the plurality of particles are arranged in a three dimensional distribution. The three dimensional distribution of particles can include periodicity providing a standard deviation of center-to-center particle spacing <5% of the average center to center particle spacing in at least a first and a second dimension transverse to the length dimension of the multi-material fiber. As described above, the transverse periodicity is controllable at the fabrication stage through the stack-and-draw process. A periodicity of < 15% (such as about 10%) of the average center- to-center particle spacing can also be provided in the length dimension of the multi-material fiber. The plurality of particles can be uniformly sized providing a <10% standard deviation in particle size with respect to an average (mean) size of the particles. [0027] In one embodiment, the particles in the embedded particle arrangement include a first hemisphere comprising a first material and a second hemisphere comprising a second material different from said first material. For example, the first material can comprises a first glass and the second material comprises a second glass.
[0028] Disclosed particles can comprise spherical particles including a first hemisphere comprising a first material and a second hemisphere comprising a second material different from the first material. In this embodiment the first material can comprise a first glass and the second material a second glass different from the first glass to provide "Janus particles" that are generally defined as spherical glass particles with one of the hemispheres being one material and the other hemisphere being another material. Disclosed processing may also be extended to multiple sectors (e.g., 3, 4, 5 ...) of a cylinder to form spherical particles with more sophisticated sub-structure.
[0029] Applications for disclosed particles are numerous. Example applications include cosmetics, biomedical (e.g., drug delivery), chemical and biological catalysts, and paints ( particles are held as a colloid in a solution).
EXAMPLES
[0030] Disclosed embodiments are further illustrated by the following specific
Examples, which should not be construed as limiting the scope or content of this Disclosure in any way.
[0031] Example parameters tested include an initial As2Se3 core diameter of 40 μιη and PES cladding tapered at a fixed speed v=2 mm/s and tapering distance d=\5 mm, but with varying temperature T. As2Se3 is known to has a melting point of about 360 °C and a glass transition temperature of about 180 °C. The PES used had a glass transition temperature of about 230 °C. When the fiber temperature rises sufficiently above both of the glass transition temperatures and the viscosity decreases sufficiently, PR instability is believed to be initiated through perturbations at the core/cladding interface.
[0032] Referring to FIGs. 3A and 3B, it was found that at relatively low temperatures, such as 261 °C and 264 °C, respectively, the viscosity of the As2Se3 core is relatively large and the extended core remained intact during tapering, so that no core droplets were observed. However, as the temperature was increased, a gradual growth in the PR instability shown began at about 268 °C apparently resulting in the periodic string of periodic core droplets shown being formed, as shown in FIGs. 3C-E.
[0033] Static heating was also studied. Static heating as used herein refers to the only parameter being varied is the temperature (no pulling/tapering). The Inventor measured the breakup time τ over the range of temperatures for fibers with initial core diameter μιη, where τ was measured from the start of heating until initiation of breakup. The measurements revealed that τ depends inversely on temperature.
[0034] In order to analyze these results quantitatively, the inventor adopted as a model the linear stability analysis of Tomotika [S. Tomotika, Proc. Roy. Soc. Lond. A 150, 322 (1935)], which describes a stationary viscous thread embedded in an unbound viscous fluid. According to this analysis, perturbations at the interface between the two fluids (core and cladding here) grow on a time-scale τ that depends on the perturbation wavelength λ, the viscosities of the two fluids (glass core ng and polymer cladding ηρ, the thread diameter (core diameter D, assuming an unbound cladding for simplicity), and surface tension γ. The wavelength with the largest growth rate (minimum τ quickly dominates the instability and results in the core breaking up into a periodic sequence of droplets with separation λ. In calculations performed by the Inventor the following values of the parameters were used: ϋ=10μιη, surface tension between As2Se3 and PES γ=0.1 N/m and ηρ=105 Pa s for PES. While the temperature dependence of ηρ over the temperature range of interest was ignored, T|g for As2Se3 changes considerably over the same range and was obtained from an empirical Arrhenius formula. Using these values the instability growth time as a function of temperature was calculated and the results compared the results to the experimental data. The predictions of the Tomotika model are in quantitative agreement with the data. The Inventor further calculated τ over the same temperature range for other initial core diameters. To a reasonable degree of accuracy, it was found that τ depends linearly on D at a fixed temperature.
[0035] The Inventor also examined the effect of each fiber tapering parameter (L, T, and v) while holding the other two parameters fixed. The Inventor adopted a simple model for this system based on a quasi-static extension to the static Tomotika model. This model decouples the effect of heating on the core from the dynamics of tapering. The Inventor thus used the static results for the temperature-dependent instability time τ and then added the geometric effect of size change during tapering. The inventor found that this model yields results in quantitative agreement with our observations despite its simplicity within the margin of error in the measurements performed.
[0036] The effect of tapering distance L while holding v=l mm/s and T=285°C was studied. The static results indicated that breakup occurs after about 80 s at this temperature with the initial core diameter D=10 μιη. As the diameter decreases during tapering, τ decreases accordingly. The Inventor found that the core remains intact until L=21 mm at which point it breaks up into a series of droplets with an average separation of 7.1 μιη. After breakup has occurred in the taper, further elongation was found to only increase the droplet separation.
[0037] Making use of the above-described quasi-static model, and making use of the approximately linear relation between τ and diameter D, an estimate for D at the moment of breakup can be generated. Taking τ=21 s, Dfinal ~ 2.6μιη is estimated. This estimate depends only on the measured instability time and the assumptions of the static Tomotika' model. The Inventor also arrived at an independent estimate from a different route. Geometric considerations coupled with the simplifying but reasonable assumption that the temperature of the heating zone is uniform and the taper material exiting the heating zone cools down immediately lead to the initial and final core diameters being related by a factor of the form e" L h, where h is the length of the heating zone. Thus Dfinal=De~L h=10 e f 21 17) ~ 2.9μιη, consistent with the considerations described above. The last data point (at L·=2^μ ) was higher than expected since the fiber undergoes rapid plastic deformation before mechanical fracture with further tapering.
[0038] The effect of T for fixed v=l mm/s and d=23 mm was next considered where the final taper diameter remains approximately constant. At low temperatures, the viscosity of the core was found to be relatively large and the core to remain intact. As the temperature increased, the PR instability grows until droplets are formed and the average period of the droplets increases with temperature. This may be understood as follows: viscosity decreases exponentially with T and the Tomotika model indicates that lower viscosity leads to linearly shorter instability time. The instability thus develops quickly at a larger diameter corresponding to a longer period. The period hence will exponentially increase with temperature. Furthermore, if the breakup occurs early on in the tapering process at higher temperature, then further tapering leads to further separation between the core droplets.
[0039] The effect of v while holding d=23 mm and T=285°C was next considered.
The final diameter of the fiber taper is also approximately constant. At high speeds, the dwelling time may be less than τ for the final core diameter, and the core thus remains intact. At lower speeds, the fiber dwells for a longer time in the heating zone thus having the opportunity to reach τ and thus breakup. The breakup of the larger-diameter core during tapering results in longer period, and then the droplets further separate if the tapering process continues. The period was found to be inversely proportional with the drawing speed.
[0040] As noted above disclosed methods may be used to fabricate microparticles or nanoparticles. The particle size as disclosed herein may be tuned by adjusting the tapering parameters, and the physical process described here hence offers an unconventional non- lithographic, top-down approach to fabricating micro and nano-structures using non- traditional materials combinations. To demonstrate control over particle size, the Inventor produced core particles at three different sizes, 5, 2, and 1 μιη, where particle size was tuned by varying the tapering speed.
[0041] There are unique features of the disclosed fiber tapering based particle fabrication approach. First, it is amenable to a wide range of materials. Demonstrations have included chalcogenide glasses, low-melting-temperature metals, polymers. Secondly, since the process can start from a macroscopic rod that is drawn into a fiber, particles of complex structure may be obtained through preparing the rod with the prescribed structure. Thirdly, although the process described herein is generally not efficient in producing particles in terms of volume conversion, the efficiency may be increased by using multi-core fibers where three different cores, all of which can undergone breakup. One may further increase the number of cores until they become hydrodynamically coupled during tapering and the assumption of an unbound cladding breaks down, a limit which has not been investigated heretofore.
[0042] As disclosed above, the size of particles that may be fabricated using disclosed methods extends over a very wide range, such as extending from 1 mm down to approximately 5 nm. The particles can be highly spherical particles.
[0043] Moreover, the same procedure may be used with a wide variety of materials.
The Inventor demonstrated the above-described process with a polymer core. The Inventor observed the same particle generation phenomena occurred with polymer cores that occurred with glass cores. Therefore, disclosed fiber tapering processes can also be used to fabricate micro- and nano-particles of polymers.
[0044] Since disclosed fiber tapering processes are top-down approaches that starts from a structure at the macroscopic scale, the shape of the cylinder of the material can be selected that is desire to break up before the first fiber drawing step. For example, as described above, two hemi-spheres of different materials can be used. The result is "Janus- particles", which are particles formed of two hemispheres of different core materials. The process may also be extended to multiple sectors of a cylinder to form spherical particles with a sophisticated sub-structure.
[0045] Disclosed embodiments include TFD-based methods to form high-density macroscopic arrays of well-ordered nanowires that can range from about 5 nm to 1 mm. A centimeter-scale macroscopic cylindrical preform containing the nanowire material in the core encased in a polymer scaffold cladding was thermally drawn in the viscous state to a fiber. By cascading several iterations of the TFD process, continuous reduction of the diameter of an amorphous semiconducting chalcogenide glass was demonstrated. Starting from a 10-mm-diameter rod thermally drawing was used to generate hundreds of meters of continuous sub-5-nm-diameter nanowires. Using this approach macroscopic lengths of high- density, well-ordered, globally oriented nanowire arrays can be produced.
[0046] Experimental results are provided below described relative to FIGs. 4A-6D which demonstrate core periodicity following disclosed processing applied to a fiber preform including a large number of glass cores encased in a polymer cladding. In the axial (length; drawing) direction the resulting particles are ordered since the instability growth is dominated by a single wavelength. In the transverse dimensions particle order is imposed upon the cores during the stacking process to form the preform.
[0047] FIGs. 4A and 4B are scanned SEM micrograph of 27,000 200-nm-diameter intact glass cores exposed from a 1-mm-outer-diameter fiber cross section after dissolving the polymer cladding. G represents glass, As2Se3, and P the polymer PES. Periodicity of the glass in the transverse directions is demonstrated.
[0048] FIG. 5 is a scanned high-magnification SEM micrograph of a portion of the fiber core shown in FIGs. 4A and 4B. The stacked fibers in the preform were found to produce a hexagonal lattice (see dashed lines). At each lattice site 80 200-nm glass cores are located as shown in the inset.
[0049] FIGs. 6A-D are scanned SEMs of well-ordered, three-dimensional particle emulsion held in the polymer cladding. FIG. 6A is a scanned SEM micrograph of a 1-mm- diameter fiber cross section containing 80 7^m-diameter cores. FIG. 6B is a higher- magnification scanned SEM micrograph of the 80 cores, G=As2Se3 and P=PES. FIGs. 6C and 6D are scanned transmission optical micrographs of the fiber side view before and after breakup (via global heating), respectively, showing the resulting spatial distribution of particles held immobilized in the cladding (scaffold) is well-ordered in all 3 dimensions.
[0050] While various disclosed embodiments have been described above, it should be understood that they have been presented by way of example only, and not limitation. Numerous changes to the subject matter disclosed herein can be made in accordance with this Disclosure without departing from the spirit or scope of this Disclosure. In addition, while a particular feature may have been disclosed with respect to only one of several implementations, such feature may be combined with one or more other features of the other implementations as may be desired and advantageous for any given or particular application.
[0051] Thus, the breadth and scope of the subject matter provided in this Disclosure should not be limited by any of the above explicitly described embodiments. Rather, the scope of this Disclosure should be defined in accordance with the following claims and their equivalents.
[0052] The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting. As used herein, the singular forms "a," "an," and "the" are intended to include the plural forms as well, unless the context clearly indicates otherwise. Furthermore, to the extent that the terms "including," "includes," "having," "has," "with," or variants thereof are used in either the detailed description and/or the claims, such terms are intended to be inclusive in a manner similar to the term "comprising."
[0053] Unless otherwise defined, all terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art to which embodiments of the invention belongs. It will be further understood that terms, such as those defined in commonly used dictionaries, should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and will not be interpreted in an idealized or overly formal sense unless expressly so defined herein.

Claims

1. A method of fabricating particles, comprising: providing a multi-material fiber having at least one core comprising a first material and an outer first cladding layer comprising a second material different from said first material outside said core; thermal fiber drawing (TFD) said multi-material fiber to increase a length of said multi-material fiber to form an extended multi-material fiber having an extended core, and thermally treating said extended multi-material fiber under conditions that cause a breaking up of said extended core to form a plurality of core particles embedded in said outer first cladding layer.
2. The method of claim 1, wherein said TFD comprises a first TFD step and at least a second TFD step, further comprising: after said first TFD, removing said outer first cladding layer to release said extended core from said extended multi-material fiber; placing said extended core in a second outer cladding layer, and performing said second TFD step on said extended core while within said second outer cladding layer.
3. The method of claim 1, wherein a maximum temperature during said TFD is less than a maximum temperature during said thermally treating.
4. The method of claim 1, wherein said thermally treating comprises holding a temperature fixed along a fiber axis of said multi-material fiber, and using a sufficient heating time to form said plurality of core particles.
5. The method of claim 1, wherein said first material comprises a chalcogenide glass and said second material comprises a thermoplastic polymer.
6. The method of claim 5, further comprising dissolving said thermoplastic polymer after said thermally treating.
7. The method of claim 1, wherein said at least one core comprises two half cylinders each comprising a different material aligned with respect to one another to provide a cylindrical core.
8. The method of claim 7, wherein said different materials comprise a first glass and a second glass, and wherein said plurality of core particles comprise spherical particles including a first hemisphere comprising said first glass and a second hemisphere comprising said second glass.
9. The method of claim 1, wherein said at least one core comprises a plurality of said cores, wherein said thermally treating provides a three dimensional distribution of said plurality of core particles embedded in said outer first cladding layer.
10. The method of claim 9, wherein said three dimensional distribution of said plurality of core particles includes periodicity providing a standard deviation of center-to- center particle spacing < 5% of said average center to center particle spacing in at least a first and a second dimension transverse to said length direction of said extended multi-material fiber.
11. An embedded particle arrangement, comprising: a multi-material fiber having a length > one hundred times its cross sectional area, said multi-material fiber including: a cladding material providing a continuous phase for said multi- material fiber, and a plurality of particles along at least a portion of said length embedded in said cladding material, wherein said plurality of particles are separated from one another, have a median size from 5 nm to 1 mm, are spherical in shape, and are molecularly smooth providing a root mean square (rms) roughness < 1 nm.
12. The embedded particle arrangement of claim 11, wherein said cladding material comprises a thermoplastic polymer.
13. The embedded particle arrangement of claim 11, wherein said plurality of particles are arranged in a three dimensional distribution.
14. The embedded particle arrangement of claim 13, wherein said three dimensional distribution of said plurality of particles includes periodicity providing a standard deviation of center- to-center particle spacing < 5% of said average center to center particle spacing in at least a first and a second dimension transverse to said length dimension of said multi-material fiber.
15. The embedded particle arrangement of claim 14, wherein a periodicity of < 15% of said average center-to-center particle spacing is provided in said length dimension of said multi-material fiber.
16. The embedded particle arrangement of claim 11, wherein said plurality of particles are uniformly sized providing provide a standard deviation in particle size < 10% of an average size of said plurality of particles.
17. The embedded particle arrangement of claim 11, wherein said plurality of particles include a first hemisphere comprising a first material and a second hemisphere comprising a second material different from said first material.
18. The embedded particle arrangement of claim 17, wherein said first material comprises a first glass and said second material comprises a second glass.
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