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 therefromInfo
- 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- Withdrawn
Links
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- 238000000034 method Methods 0.000 title claims abstract description 49
- 238000012681 fiber drawing Methods 0.000 title claims abstract description 8
- 230000008569 process Effects 0.000 title description 22
- 239000000463 material Substances 0.000 claims abstract description 91
- 239000000835 fiber Substances 0.000 claims abstract description 89
- 238000005253 cladding Methods 0.000 claims abstract description 44
- 239000007771 core particle Substances 0.000 claims abstract description 18
- 239000011521 glass Substances 0.000 claims description 25
- 238000010438 heat treatment Methods 0.000 claims description 16
- 238000009826 distribution Methods 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 239000012798 spherical particle Substances 0.000 claims description 6
- 229920001169 thermoplastic Polymers 0.000 claims description 6
- 239000005387 chalcogenide glass Substances 0.000 claims description 3
- 238000013459 approach Methods 0.000 abstract description 10
- 239000011162 core material Substances 0.000 description 76
- 229920000642 polymer Polymers 0.000 description 14
- 239000011859 microparticle Substances 0.000 description 9
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- 230000009477 glass transition Effects 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 125000003821 2-(trimethylsilyl)ethoxymethyl group Chemical group [H]C([H])([H])[Si](C([H])([H])[H])(C([H])([H])[H])C([H])([H])C(OC([H])([H])[*])([H])[H] 0.000 description 2
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- 239000002657 fibrous material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
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- 238000004886 process control Methods 0.000 description 2
- 238000004626 scanning electron microscopy Methods 0.000 description 2
- 238000001338 self-assembly Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 229920012266 Poly(ether sulfone) PES Polymers 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/006—Coating of the granules without description of the process or the device by which the granules are obtained
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/12—Powdering or granulating
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/12—Powdering or granulating
- C08J3/126—Polymer particles coated by polymer, e.g. core shell structures
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
- D02J1/00—Modifying 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
- D02J1/22—Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch
- D02J1/224—Selection or control of the temperature during stretching
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2300/00—Characterised by the use of unspecified polymers
- C08J2300/22—Thermoplastic 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)
- Reinforced Plastic Materials (AREA)
- Glanulating (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Artificial Filaments (AREA)
- Inorganic Fibers (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US40687210P | 2010-10-26 | 2010-10-26 | |
| PCT/US2011/057895 WO2012058314A2 (en) | 2010-10-26 | 2011-10-26 | Thermal fiber drawing (tfd) with added core break-up process and particles therefrom |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP2632866A2 true EP2632866A2 (en) | 2013-09-04 |
| EP2632866A4 EP2632866A4 (en) | 2017-11-22 |
Family
ID=45994726
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP11837022.0A Withdrawn EP2632866A4 (en) | 2010-10-26 | 2011-10-26 | Thermal fiber drawing (tfd) with added core break-up process and particles therefrom |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP2632866A4 (en) |
| JP (1) | JP5863814B2 (en) |
| IL (1) | IL225937A (en) |
| WO (1) | WO2012058314A2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014160504A1 (en) * | 2013-03-13 | 2014-10-02 | Massachusetts Institute Of Technology | High-pressure in-fiber particle generation with dimensional control |
| WO2015006758A1 (en) * | 2013-07-12 | 2015-01-15 | University Of Central Florida Research Foundation, Inc. | Functionalized polymer particles for biosensing |
| WO2020013980A1 (en) * | 2018-07-09 | 2020-01-16 | Corning Incorporated | Organic-inorganic composites and methods of manufacturing thereof |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6248696B1 (en) * | 1994-07-15 | 2001-06-19 | Basf Corporation | 7-forming, superconducting filaments through bicomponent dry spinning |
| EP1110113A4 (en) * | 1998-06-29 | 2005-03-09 | Univ Syracuse | METHOD FOR PRODUCING A CYLINDRICAL OPTICAL FIBER CONTAINING AN OPTICALLY ACTIVE FILM |
| JP3657164B2 (en) * | 2000-02-22 | 2005-06-08 | セントラル硝子株式会社 | Non-metallic particle precipitated glass and method for producing the same |
| US6550279B1 (en) * | 2000-09-01 | 2003-04-22 | Corning Incorporated | Process for drawing optical fiber from a multiple crucible apparatus with a thermal gradient |
| JP2002104842A (en) * | 2000-09-27 | 2002-04-10 | Mitsubishi Chemicals Corp | Glass composition containing semiconductor ultrafine particles |
| AU2003280449A1 (en) * | 2002-06-28 | 2004-01-19 | Mosaic Systems Bv | Functional porous fibres |
| JP2004044035A (en) * | 2002-07-15 | 2004-02-12 | Nippon Ester Co Ltd | Conductive conjugate fiber |
| US7567740B2 (en) * | 2003-07-14 | 2009-07-28 | Massachusetts Institute Of Technology | Thermal sensing fiber devices |
| WO2005049513A2 (en) * | 2003-07-14 | 2005-06-02 | Massachusetts Institute Of Technology | Optoelectronic fiber codrawn from conducting, semiconducting, and insulating materials |
| US7399443B2 (en) * | 2004-02-27 | 2008-07-15 | Lucent Technologies Inc. | Carbon particle fiber assembly technique |
| US8101388B2 (en) * | 2007-09-28 | 2012-01-24 | Ut-Battelle, Llc | Method and structure for extracting molecular species |
| JP4450060B2 (en) * | 2007-11-30 | 2010-04-14 | トヨタ自動車株式会社 | Method for producing metal nanoparticle-supported carbon nanofiber |
| JP2010119970A (en) * | 2008-11-20 | 2010-06-03 | Teijin Fibers Ltd | Deodorizing fiber and manufacturing method therefor |
-
2011
- 2011-10-26 EP EP11837022.0A patent/EP2632866A4/en not_active Withdrawn
- 2011-10-26 JP JP2013536781A patent/JP5863814B2/en not_active Expired - Fee Related
- 2011-10-26 WO PCT/US2011/057895 patent/WO2012058314A2/en not_active Ceased
-
2013
- 2013-04-24 IL IL225937A patent/IL225937A/en active IP Right Grant
Non-Patent Citations (1)
| Title |
|---|
| See references of WO2012058314A2 * |
Also Published As
| Publication number | Publication date |
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| EP2632866A4 (en) | 2017-11-22 |
| JP2014504336A (en) | 2014-02-20 |
| JP5863814B2 (en) | 2016-02-17 |
| IL225937A (en) | 2016-08-31 |
| WO2012058314A3 (en) | 2012-07-12 |
| IL225937A0 (en) | 2013-06-27 |
| WO2012058314A2 (en) | 2012-05-03 |
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