WO2005024102A1 - Corps moules, en particulier fibres et leurs structures en surface, a proprietes thermoregulatives - Google Patents

Corps moules, en particulier fibres et leurs structures en surface, a proprietes thermoregulatives Download PDF

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Publication number
WO2005024102A1
WO2005024102A1 PCT/DE2004/001893 DE2004001893W WO2005024102A1 WO 2005024102 A1 WO2005024102 A1 WO 2005024102A1 DE 2004001893 W DE2004001893 W DE 2004001893W WO 2005024102 A1 WO2005024102 A1 WO 2005024102A1
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WO
WIPO (PCT)
Prior art keywords
network
shaped body
phase change
body according
fibers
Prior art date
Application number
PCT/DE2004/001893
Other languages
German (de)
English (en)
Inventor
Detlev Gersching
Frank Meister
Original Assignee
Thüringisches Institut Für Textil - Und Kunststoff - Forschung E.V.
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=34202272&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2005024102(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Thüringisches Institut Für Textil - Und Kunststoff - Forschung E.V. filed Critical Thüringisches Institut Für Textil - Und Kunststoff - Forschung E.V.
Priority to EP04786178A priority Critical patent/EP1658395B1/fr
Priority to DE502004001972T priority patent/DE502004001972D1/de
Priority to DE112004002148T priority patent/DE112004002148D2/de
Priority to PL04786178T priority patent/PL1658395T3/pl
Priority to US10/570,374 priority patent/US20060279017A1/en
Publication of WO2005024102A1 publication Critical patent/WO2005024102A1/fr

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F4/00Monocomponent artificial filaments or the like of proteins; Manufacture thereof
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F2/00Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F4/00Monocomponent artificial filaments or the like of proteins; Manufacture thereof
    • D01F4/04Monocomponent artificial filaments or the like of proteins; Manufacture thereof from casein

Definitions

  • Shaped bodies in particular fibers and their fabrics, with thermoregulatory properties
  • the invention relates to moldings having improved thermoregulatory properties, composed of network-forming polymers and phase change materials incorporated therein, which can be processed as fibers into textile fabrics having heat-storing and heat-giving properties and which give improved textiles improved comfort, as well as in other applications have a high level of functionality in terms of heat storage and disposal.
  • phase change materials can absorb or release relatively large amounts of heat as their phase state or conformation changes at a constant temperature.
  • an increased heat capacity is found, which finds its physically measurable expression in the enthalpy of fusion occurring and allows the storage or release of larger amounts of heat than the normal heat capacity of the material outside the temperature range of the phase transition or the conformational change would correspond.
  • phase change material paraffins or salts or solutions of suitable salts can be used.
  • the temperature range of the phase transition from the solid to the molten state can be adjusted in a targeted manner to the respective required temperature at which the heat is to be released or stored by varying the chain length.
  • Salts or their solutions can be selected specifically according to the desired temperature range of the conformational change.
  • the microencapsulated form is particularly suitable.
  • phase change material is enclosed in ceramic or polymer spheres with diameters in the ⁇ m range and thus brought into a manageable form which allows inclusion in crosslinked polymeric matrix materials, wherein the efficiency of the thermoregulation of the type and amount of the enclosed PCM Material is dependent.
  • US 5,885,475 describes apparel composed of fibers consisting of a polymer blend additionally containing phase change material.
  • the fiber-forming substances are made selected from the group of synthetic melt-spinnable thermoplastic polymers.
  • Multicomponent fibers with increased, reversible thermal properties and textile fabrics produced therefrom are described in WO 03027365, US 200212079 and US 200129648.
  • the fiber bodies consisting of a multiplicity of elongated components, contain at least in one of these stretched components a temperature-regulating material distributed therein.
  • This may be a phase change material and optionally the classes of hydrocarbons, hydrated salts, waxes, oils, water, fatty acids, fatty acid esters, 2-basic acids and esters, halides, clusters and semiclusters, gas clusters, stearin anhydrite, ethylene carbonate, higher alcohols, polymers and metals and mixtures thereof.
  • the arrangement of the various components of the fiber can optionally take place in a core-sheath structure, polysetational, bundled or strip-shaped at different shaped cross-section.
  • the matrix material of the described multicomponent fiber can consist of different, linear chain molecules.
  • a disadvantage of these fibers and textile fabrics made therefrom is that only a portion of the fibers formed therefrom contain phase change material as a result of the described arrangement of the individual components and the proportion of temperature-regulating material in the overall fiber is naturally limited. Due to the presence of multicomponent structures of a plurality of elongated constituents, the proportion of phase change material that can be introduced into the polymer structure is limited to a proportion of at most 50 percent by mass, based on the respective matrix material.
  • WO 02095314 and CH 0200245 likewise describe processes in which the temperature-regulating properties are to be achieved by printing on a textile fabric with microencapsulated phase change material. The temperature-regulating effect is thus achieved by applying a coating containing phase change material.
  • phase change material can be fixed on the surface of the structures, in particular if only a part of the surface is printed with a suspension of microencapsulated phase change materials and thus the temperature regulating effect, based on the Amount of material, comparatively localized.
  • the printing of a textile surface with a suspension of microencapsulated phase materials applied in a comparatively large layer thickness has a disadvantageous effect on the flexibility of textile products made therefrom and thus also on the wearing properties.
  • suspensions of microencapsulated phase change materials applied to textile surfaces have only limited mechanical resistance and are washable.
  • PCM fibers described so far are manufactured on the basis of synthetic polymer fibers.
  • matrix materials such as cellulose and / or globular proteins are not mentioned as a polymer matrix.
  • network-forming structures can be prepared, for example, from cellulosic molding and spinning compositions by dissolving cellulose in tertiary amine oxides, preferably N-methylmorpholine-N-oxide, and a non-solvent, preferably water.
  • a spinning solution of cellulose in N-methylmorpholine-N-oxide and water is deformed by a dry-wet spinning process, coagulated in, for example, an aqueous spinning bath, the solvent completely removed by washing several times and the solidified shaped bodies dried.
  • the shaped bodies thus obtained then have a network structure characterized by hydrogen bonds.
  • the globular proteins have, as the name implies, a spherical tertiary structure and occur in nature in relatively frequent numbers. Examples are the casein (milk protein), the zein (corn protein) and the ardenin (peanut protein).
  • the object of the invention is to develop moldings having improved thermoregulatory properties which contain an increased proportion of introduced phase change material compared to fibers produced on a synthetic basis and thus should have an increased thermo-regulating potential while avoiding the cited disadvantages of the prior art.
  • attention should be paid to the use of naturally occurring raw materials and, in as few process steps as possible, environmentally friendly fibers with the described properties should be produced by using natural resources.
  • the object is achieved by introducing phase change materials up to a content of 200% by mass into network-forming polymers, the network being formed by the chemical coupling of functional groups, hydrogen bonds or helically interconnected polymeric or oligomeric structures.
  • a suitable network-forming polymeric matrix material is native cellulose. This forms bonds which on the one hand cause cross-linking of the polymer structure and on the other hand cause the formation of a superstructure by the formation of hydrogen bonding. By this structure formation, the embedding of even larger amounts of microencapsulated phase change materials is possible. The microencapsulation causes the demarcation between the phase change material and the polymer matrix.
  • phase change material for example, example, paraffins of different chain length application, wherein the temperature of the phase transition depends on the chain length of the molecules and can be adjusted by changing the chain lengths the required temperature range of the phase transition.
  • inorganic hydrated salts are applicable, which can be selected depending on the desired temperature range of the conformational change. Due to their higher density compared to paraffins, it is possible in particular to introduce far more than 50% by mass of phase change material into the polymer matrix.
  • globular proteins which are numerous and naturally obtainable in nature. Starting from a primary structure based on peptide bonds, a secondary structure in the form of folds of the amino acid chain, which is based on hydrogen bonding, forms a spatially cross-linked tertiary structure, which is stabilized, for example, by disulfide bonds, hydrogen bonds, or ionic or hydrophobic interactions.
  • precrosslinked globular proteins are likewise soluble in tertiary amine oxides and can be shaped by a dry-wet process.
  • the solution of the precrosslinked globular protein can be added as a further constituent of a polysaccharide such as cellulose. This gives the possibility of being able to influence the properties of the moldings in a targeted manner.
  • a cellulose solution in a water-containing tertiary amine oxide phase change materials up to a content of 200 Percent mass, based on the mass of the cellulose containing added and this solution over an air gap warped and then precipitated the cellulose with the trapped phase change material in a precipitation bath, for example from water or a water / alcohol mixture to form physical networks.
  • a precipitation bath for example from water or a water / alcohol mixture to form physical networks.
  • crosslinking of the polymeric matrix results in complete and mechanically stable entrapment of the microencapsulated phase change materials coupled with optimum heat transfer to or away from the phase change material.
  • precrosslinked globular proteins in N-methylmorpholine-N-oxide optionally with the addition of polysaccharides such as cellulose, are converted into a spinning solution and spun into filaments by known processes.
  • the native polymer-based PCM fibers produced according to the invention have a wide range of uses, for example for fabrics for the production of textiles, for nonwovens, in textiles for the automotive industry, in yarns and blended yarns.
  • phase-change heat characterizing the thermoregulatory properties of the native PCM fibers of the present invention is up to a factor of 8 higher than that of the synthetic polymer-based PCM fibers.
  • the dissolving vessel is evacuated to 20 mbar and heated in the course of 6 hours from 20 ° C to 94 ° C at a stirrer speed of 18 min -1 and the evaporating water condensed in a connected condenser.
  • the spinning solution obtained has a viscosity of 1560 Pas and a refractive index of 1.484.
  • the spinning solution is extruded at 80 ° C through a spinneret with a number of holes of 150 and a hole diameter of 200 microns via an air gap in a precipitation bath of water.
  • the take-off speed is 25 m / min resulting in a 3.75 draft in the air gap.
  • the spun fibers have a denier of about 14 dtex and are washed in subsequent rinse baths and then cut into stacks.
  • the phase change heat of the obtained fibers is 30 J / g.
  • the cellulose fibers without introduced phase change material have a heat capacity of 6 J / g.
  • the fineness-related tear strengths of the resulting fibers are about 15 cN / tex.
  • the modified fibers could be processed into a needle-punched nonwoven having a basis weight of 300 g / m 2 .
  • Example 2 100 g of casein are dispersed in 250 ml of water and crosslinked by addition of 2 g of glutaraldehyde and 0.1 g of MgCl 2 at 25 ° C. After pressing to a moisture content of 50%, the casein is suspended in 430 g of 60% NMMNO. As a stabilizer, 0.5 g of propyl gallate is added. The suspension 100 g of a micro-encapsulated phase change material, such as Lurapret TX PMC 28 ® from BASF AG, added, corresponding to a content of 100 percent by mass of phase change material, based on the protein in the solution.
  • a micro-encapsulated phase change material such as Lurapret TX PMC 28 ® from BASF AG
  • the suspension is transferred in a jacketed kneading apparatus under a vacuum of 30 mbar and a temperature of 90 ° C by distilling off 130 g of water in a spinning solution.
  • the homogeneity of the spinning solution is checked by light microscopy and is usually reached 15 minutes after the end of the distillation.
  • the solution is by a
  • casein 50 g of casein are dispersed in 250 ml of water and crosslinked by addition of 1 g of glutaraldehyde and 0.1 g of MgCl 2 at 25 ° C. After pressing to a moisture content of 50%, the casein is suspended in 430 g of 60% NMMNO. In addition, 25 g of dry ground sulphite be (DP 760) and 100 g microencapsulated phase change material such as Lurapret TX PMC 28 ® from BASF AG, was added.
  • DP 760 dry ground sulphite be
  • microencapsulated phase change material such as Lurapret TX PMC 28 ® from BASF AG
  • the fibers have a strength of 30 cN / tex.
  • the titer is about 20 dtex.
  • the heat capacity of the modified fibers is 70 J / g versus 7 J / g for unmodified fibers.
  • 7607 g of a 60% solution of N-methylmorpholine-N-oxide are introduced together with 784 g of average grade 500 polymerisation pulp with the addition of 4.6 g of propyl gallate into a 37 l stirred volume dissolving vessel.
  • the dissolving vessel is evacuated to 20 mbar and heated in the course of 6 hours from 20 ° C to 94 ° C at a stirrer speed of 18 min -1 and condenses the evaporating water in a condenser. A total of 2361 g of water are evaporated.
  • the spinning solution obtained has a viscosity of 8072 Pas, the refractive index of the spinning solution was 1.487.
  • a stock solution of 1500 g of an 80% solution of N-methylmorpholine-N-oxide and 750 g of a microencapsulated phase change material such as Lurapret ® TX PMC 28 from BASF AG, and 45 g of xanthan gum is prepared. Both solutions are extruded after intimate mixing in a dynamic mixer at 80 ° C through a spinneret with a number of holes of 150 and a hole diameter of 200 microns, warped over an air gap, regenerated in an aqueous precipitation bath and washed solvent-free with distilled water. The adjustment of the mixing ratio is such that the extruded fibers have a concentration of microencapsulated phase change material of 60% based on cellulose.
  • the spun fibers have a fineness of about 10 dtex and are cut into stacks after washing.
  • the phase change heat of the obtained fibers is 80 J / g.
  • the cellulose fibers without introduced phase change material have a heat capacity of 6 J / g in the corresponding temperature range.
  • the fineness-related tear strengths of the resulting fibers are about 15 cN / tex.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Artificial Filaments (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Nonwoven Fabrics (AREA)

Abstract

L'invention concerne des corps moulés qui sont édifiés à partir de polymères natifs réticulaires, de telle façon que le réseau soit formé par couplage chimique de groupes fonctionnels, de ponts hydrogène, ou de structures polymères ou oligomères liées entre elles en hélice, et que jusqu'à 200 pourcent en masse, par rapport au polymère réticulaire, d'un matériau à transition de phase microencapsulé, soient inclus dans la matrice polymère. Des polymères réticulaires peuvent être, par exemple, des polysaccharides et/ou des protéines globulaires. Les fibres obtenues se caractérisent par une thermorégulation améliorée par rapport aux fibres connues jusqu'à présent.
PCT/DE2004/001893 2003-08-30 2004-08-25 Corps moules, en particulier fibres et leurs structures en surface, a proprietes thermoregulatives WO2005024102A1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
EP04786178A EP1658395B1 (fr) 2003-08-30 2004-08-25 Methode pour la preparation de corps moules a proprietes thermoregulatives
DE502004001972T DE502004001972D1 (de) 2003-08-30 2004-08-25 Verfahren zur herstellung von formkörpern mit thermoregulativen eigenschaften
DE112004002148T DE112004002148D2 (de) 2003-08-30 2004-08-25 Formkörper, insbesondere Fasern und deren Flächengebilde, mit thermoregulativen Eigenschaften
PL04786178T PL1658395T3 (pl) 2003-08-30 2004-08-25 Sposób wytwarzania wytworów formowanych o właściwościach termoregulacyjnych
US10/570,374 US20060279017A1 (en) 2003-08-30 2004-08-25 Moulded bodies, in particular fibres and the structures thereof exhibiting thermoregulation properties

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10340110.5 2003-08-30
DE10340110 2003-08-30

Publications (1)

Publication Number Publication Date
WO2005024102A1 true WO2005024102A1 (fr) 2005-03-17

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ID=34202272

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/DE2004/001893 WO2005024102A1 (fr) 2003-08-30 2004-08-25 Corps moules, en particulier fibres et leurs structures en surface, a proprietes thermoregulatives

Country Status (6)

Country Link
US (1) US20060279017A1 (fr)
EP (1) EP1658395B1 (fr)
AT (1) ATE344844T1 (fr)
DE (3) DE112004002148D2 (fr)
PL (1) PL1658395T3 (fr)
WO (1) WO2005024102A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006066291A1 (fr) * 2004-12-23 2006-06-29 Lenzing Aktiengesellschaft Corps moule en cellulose et procede de fabrication dudit corps
EP1651806A4 (fr) * 2003-08-07 2008-10-22 Outlast Technologies Inc Fibres cellulosiques possedant des proprietes thermiques reversibles ameliorees et leurs procedes de formation
US7579078B2 (en) 2001-09-21 2009-08-25 Outlast Technologies, Inc. Temperature regulating cellulosic fibers and applications thereof
US9434869B2 (en) 2001-09-21 2016-09-06 Outlast Technologies, LLC Cellulosic fibers having enhanced reversible thermal properties and methods of forming thereof

Families Citing this family (8)

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TWI287996B (en) * 2005-10-19 2007-10-11 Taiwan Textile Res Inst Temperature regulating gel and article comprising the same
US20090051068A1 (en) * 2006-01-12 2009-02-26 Thüringisches Institute Für Textil-Und Kunststoff-Forschung E.V. Method for Producing Molded Bodies from Proteins
FR2911153B1 (fr) * 2007-01-10 2009-04-10 Lainiere De Picardie Bc Soc Pa Substrat textile incorporant une composition de regulation thermique entourant des ilots de transfert.
DE102007054702B4 (de) 2007-11-14 2018-10-18 Smartpolymer Gmbh Verfahren zur Herstellung von cellulosischen Formkörpern, cellulosischer Formkörper und dessen Verwendung
AT509289B1 (de) 2009-12-28 2014-06-15 Chemiefaser Lenzing Ag Funktionalisierter cellulosischer formkörper und verfahren zu seiner herstellung
DE102010054661A1 (de) * 2010-12-15 2012-06-28 Anke Domaske Verfahren zur Herstellung von Milchproteinfasern und daraus gewonnene Milchproteinfaserprodukte
JP6722680B2 (ja) 2014-10-03 2020-07-15 エリー フーズ インターナショナル、インコーポレイテッドErie Foods International,Inc. 高タンパク食品
DE102018100140B3 (de) 2017-12-14 2019-03-28 Institut Für Luft- Und Kältetechnik Gemeinnützige Gmbh Lüftungsanlage mit Wärmespeicher

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EP0306202A2 (fr) * 1987-08-31 1989-03-08 Triangle Research And Development Corporation Fibres à caractéristiques de stockage de chaleur réversibles et tissus fabriqués avec ces fibres
US4908238A (en) * 1984-07-02 1990-03-13 The United States Of America As Represented By The Secretary Of Agriculture Temperature adaptable textile fibers and method of preparing same
US5885475A (en) * 1995-06-06 1999-03-23 The University Of Dayton Phase change materials incorporated throughout the structure of polymer fibers
WO2003027365A1 (fr) * 2001-09-21 2003-04-03 Outlast Technologies, Inc. Fibres a plusieurs constituants presentant des proprietes thermiques reversibles et procedes de fabrication

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US5354524A (en) * 1993-05-24 1994-10-11 Alan Sellars Monitoring concentration of dope in product manufacture
GB9617043D0 (en) * 1996-08-14 1996-09-25 Courtaulds Plc Manufacture ofd extruded articles
US6077597A (en) * 1997-11-14 2000-06-20 Outlast Technologies, Inc. Interactive thermal insulating system having a layer treated with a coating of energy absorbing phase change material adjacent a layer of fibers containing energy absorbing phase change material
US20030124278A1 (en) * 2002-01-02 2003-07-03 Clark Dustin L. Thermal barriers with solid/solid phase change materials
US20030124318A1 (en) * 2002-01-02 2003-07-03 Magill Monte C. Thermal barriers with reversible enhanced thermal properties

Patent Citations (4)

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Publication number Priority date Publication date Assignee Title
US4908238A (en) * 1984-07-02 1990-03-13 The United States Of America As Represented By The Secretary Of Agriculture Temperature adaptable textile fibers and method of preparing same
EP0306202A2 (fr) * 1987-08-31 1989-03-08 Triangle Research And Development Corporation Fibres à caractéristiques de stockage de chaleur réversibles et tissus fabriqués avec ces fibres
US5885475A (en) * 1995-06-06 1999-03-23 The University Of Dayton Phase change materials incorporated throughout the structure of polymer fibers
WO2003027365A1 (fr) * 2001-09-21 2003-04-03 Outlast Technologies, Inc. Fibres a plusieurs constituants presentant des proprietes thermiques reversibles et procedes de fabrication

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7790283B2 (en) 2000-09-21 2010-09-07 Outlast Technologies, Inc. Cellulosic fibers having enhanced reversible thermal properties and methods of forming thereof
US7579078B2 (en) 2001-09-21 2009-08-25 Outlast Technologies, Inc. Temperature regulating cellulosic fibers and applications thereof
US8173257B2 (en) 2001-09-21 2012-05-08 Outlast Technologies, Inc. Cellulosic fibers having enhanced reversible thermal properties and methods of forming thereof
US9434869B2 (en) 2001-09-21 2016-09-06 Outlast Technologies, LLC Cellulosic fibers having enhanced reversible thermal properties and methods of forming thereof
US9920455B2 (en) 2001-09-21 2018-03-20 Outlast Technologies, LLC Cellulosic fibers having enhanced reversible thermal properties and methods of forming thereof
US10208403B2 (en) 2001-09-21 2019-02-19 Outlast Technologies, LLC Cellulosic fibers having enhanced reversible thermal properties and methods of forming thereof
EP1651806A4 (fr) * 2003-08-07 2008-10-22 Outlast Technologies Inc Fibres cellulosiques possedant des proprietes thermiques reversibles ameliorees et leurs procedes de formation
WO2006066291A1 (fr) * 2004-12-23 2006-06-29 Lenzing Aktiengesellschaft Corps moule en cellulose et procede de fabrication dudit corps

Also Published As

Publication number Publication date
EP1658395A1 (fr) 2006-05-24
DE102004041684A1 (de) 2005-03-17
DE502004001972D1 (de) 2006-12-21
DE112004002148D2 (de) 2006-07-13
PL1658395T3 (pl) 2007-04-30
EP1658395B1 (fr) 2006-11-08
ATE344844T1 (de) 2006-11-15
US20060279017A1 (en) 2006-12-14

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