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“Lyocell Fiber”

Abstract: The invention concerns a Lyocell fibre, containing a material selected from the group consisting of pearl powder, ground nacre and mixtures thereof. For the manufacture of the fibre according to the invention, a process is used comprising the steps of - manufacturing a spinning solution of cellulose in an aqueous tertiary amine oxide, preferably N-methylmorpholine-N-oxide (NMMO) - spinning the spinning solution to fibres, and being characterized in that a material selected from the group consisting of pearl powder, ground nacre and mixtures thereof is admixed to the spinning solution and/or to a precursor thereof.

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Patent Information

Application #
Filing Date
17 February 2010
Publication Number
29/2010
Publication Type
INA
Invention Field
TEXTILE
Status
Email
Parent Application
Patent Number
Legal Status
Grant Date
2019-07-01
Renewal Date

Applicants

LENZING AKTIENGESELLSCHAFT
Werkstrasse 2  A-4860 Lenzing  Austria

Inventors

1. FIRGO  Heinrich
Billroth-Strasse 4  A-4840 Vöcklabruck  Austria
2. FUCHS  Heidrun
Parkstrasse 15  A-4840 Vöcklabruck  Austria

Specification

Lyocell Fibre

The present invention relates to a Lyocell fibre.

Fibres of the Lyocell genus are produced by a solvent-spinning process, wherein the cellulose is dissolved directly in an aqueous tertiary amine-oxide without the formation of a derivative, and the solution is spun. Such fibres are also referred to as “solvent-spun” fibres. „Lyocell“ is the generic name allocated by BISFA (The International Bureau for the Standardization of man made fibres) for cellulose fibres which are produced by dissolving cellulose in an organic solvent without the formation of a derivative and extruding fibres from said solution by means of a dry-wet spinning process or a melt-blown process. In this regard, an organic solvent is understood to be a mixture of an organic chemical and water. At present, N-methyl-morpholine-N-oxide (NMMO) is used as an organic solvent on a commercial scale.

In said process, the solution of the cellulose is usually extruded by means of a forming tool, whereby it is moulded. Via an air gap, the moulded solution gets into a precipitation bath, where the moulded body is obtained by precipitating the solution. The moulded body is washed and optionally dried after further treatment steps. A process for the production of Lyocell fibres is described, for instance, in US A 4,246,221. Lyocell fibres are distinguished by a high tensile strength, a high wet-modulus and a high loop strength.

It is well-known to modify cellulosic fibres and also Lyocell fibres via the incorporation of various additives.

In this respect, EP 1 259 264 B1 discloses Lyocell fibres which contain a material of sea plants or shells of sea animals. As sea plants, mussels are mentioned amongst others. Shells of mussles, however, contain all the contaminations that are deposited on the outer side of the shell, i.e. the side being in contact with the water.

CN 1772980 A discloses a viscose fibre containing pearl powder.

Also CN 1450212 A discloses fibres containing pearl powder. However, the fibres mentioned in CN 1450212 A are non-cellulosic synthetic fibres.

Pearl powder (i.e. ground pearls) is well-known since long time from Chinese medicine as health- and beauty-promoting and, therefore, is used in cosmetic products. This material mainly consists of CaCO3 and of proteins.

The manufacturing processes for making viscose fibres and, especially, making non-cellulosic synthetic fibres differ significantly from the manufacturing process for making Lyocell fibres. Especially, in the viscose process various substances that are detrimental to the environment must be used for the production of the spinning solution. Furthermore, the manufacturing processes of these fibre types are carried out at conditions that are detrimental to the components of the pearl powder and, therefore, reduce the yield and worsen the properties of the product, respectively. Incorporating pearl powder into non-cellulosic synthetic fibres results in a low bioavailability of the powder, because the powder is encased within the fibres and, due to the hydrophobicity of such fibres, only a limited exchange with the environment is possible. In the viscose process, on the other hand, the precipitation of the fibres in an acid precipitation bath containing H2SO4 damages the CaCO3 contained in the pearl powder. In any event, the CaCO3 is partly dissolved, and also one must expect partial precipitation in the form of CaSO4.

Furthermore, the properties of the various fibre types differ significantly from each other.

It is an object of the present invention to provide a fibre in which pure pearl material is present with a high bioavailability and wherein said fibre can be produced with a process that preserves the pearl material as much as possible.

This object is solved by a Lyocell fibre which contains a material selected from the group consisting of pearl powder, ground nacre and mixtures thereof.

The fibre according to the present invention, thus, contains a high-purity material of pearls or nacre, respectively. Nacre and pearls, respectively, are exclusively made of the innermost layer facing the mollusc, called the hypostracum. The hypostracum, in an amount of 95%, consists of pseudo-hexagonal plates of calcium carbonate having a thickness of 500 nm and exhibiting the crystalline form of aragonite. The plates are embedded in an organic matrix of proteins and chitin. Pearls essentially consist of nacre with an amount of 80-95% CaCO3 which is present in the crystalline form of aragonite, eventually with a small amount of calcite (http://de.wikipedia.org/wiki/Perle; http://de.wikipedia.org/wiki/perlmutt). Having been formed concluded in the interior of the mussel(shell), the pearl – in contrast to mussle shells as a whole - develops protected from detrimental influences of the environment and therefore does not contain contaminations.

The material of pearls or nacre, respectively, may preferably be present in an amount of from 0.07 wt.% to 5 wt.%, based on fibre.

It is especially preferred that the material is an ultra-fine powder having an average particle size of from 0.04 to 1.5 µm, preferably 0.4 to 1.0 µm. Such powders are commercially available under the name "Nano-Pearl-Powder" or can be manufactured by adequate grinding of pearls and/or nacre, respectively.

As is well known, the process for manufacturing Lyocell fibres, in contrast to the process for manufacturing viscose fibre, is not based on a prior derivatization and can be carried out in an environmentally sound manner.

The process for the manufacture of the Lyocell fibre according to the present invention, therefore, comprises the known steps of

- manufacturing a spinning solution of cellulose in an aqueous tertiary amine oxide, preferably N-methylmorpholine-N-oxide (NMMO) and
- spinning the spinning solution to fibres,

and is characterized in that a material selected from the group consisting of pearl powder, ground nacre and mixtures thereof is admixed to the spinning solution and/or to a precursor thereof.

As a "precursor" of the spinning solution, starting and intermediate materials for the manufacture of the spinning solution are to be understood, especially

- the starting cellulose material employed, e.g. pulp
- the solvent employed (aqueous tertiary amine oxide, in the following the term "NMMO" is used as an abbreviation for all suitable amine oxides)
- a mixture of the starting cellulose material with the solvent NMMO, especially a suspension of the cellulose in an aqueous NMMO, starting from which the solution can be made.

The material of pearls and/or nacre may preferably be admixed in an amount of from 0.1 wt.% to 5 wt.%, based on cellulose. Typical losses of yield can be observed in an amount of from 5 to 30%, especially only about 10%.

The material preferably is employed in the form of a powder. Preferably the average particle size of the powder ranges from 0.04 to 1.5 µm, especially preferred 0.4 to 1.0 µm.

Prior to being admixed to the suspension or the precursor thereof, respectively, the powder may preferably be converted into the form of an aqueous suspension. This suspension is then admixed.

The present invention, furthermore, relates to the use of the Lyocell fibre according to the invention as a product with cosmetic effect in a textile article and/or in a non-woven cosmetic product.

Pearl powder has been referred to as being effective for softening the skin, regenerating skin cells, inhibiting melanin synthesis and, therefore, inhibiting the forming of age spots, and also sometimes as having antioxidative effect. The spectrum of effects can be ascribed to the topical application of bioavailable essential amino acids and trace elements.

With regard to the use as a cosmetic it has been shown that particle sizes in the nano-region (40-80 nm) increase the absorption speed of Ca and amino acids through the skin, as compared with particles in the micrometer size (http://www.karipearl.com/medicine.html).

The purity and the special composition of essential amino acids, mineral compounds, trace elements and the high amount of calcium render the pearl and the nacre, respectively, especially valuable for the skin.

The material of pearls and/or nacre which is incorporated into the Lyocell fibre is able, via a slow-release effect, to release steadily, and in small doses, mineral compounds, essential amino acids and calcium to the skin. Thus, the skin is continuously supplied with these micronutrients.

Examples:

General method:

The fibre according to the invention can be produced by admixing 0.5 to 5% of a powder of ground pearls (in the following referred to as "Nano Pearl Powder") into the Lyocell spinning dope and spinning the dope by employing common spinning parameters. It was found that the admixing has no significant effect on the stability of the spinning dope.

Example 1 – Spinning in a Davenport apparatus

Production of the spinning dope:

3 wt.% (based on the weight of cellulose) Nano Pearl Powder were admixed into a spinning dope as follows: 0.78 g Nano Pearl Powder (manufacturer: Messrs. Fenix, particle size according to the product information: 40 nm to 80 nm) were slurried in 5 ml de-ionized water in an ultrasonic bath.

For making the solution, first about 50% aqueous NMMO were mixed in a manner known per se with a stabilizer (0.1%). Afterwards the slurry of Nano Pearl Powder was admixed and finally the pulp was added. The mixture was mixed for 1 h at room temperature and 250 mbar and then heated to 70°C. Afterwards the solution was produced in a manner known per se by evaporating water. The solution was heated for some more time. The resulting solution is optically clear and free from particles > 3 µm.

The solution contained 77% NMMO, 13% cellulose, 10% water, 0.1% stabilizer (all based on weight of the solution) and 3 wt.% Nano-Pearl-Powder (based on weight of cellulose).

The solution was spun by means of a Davenport spinning apparatus in a manner known per se through a spinneret at 115°C and via an air gap. The spinneret employed had a hole diameter of 100 µm.

The fibres produced were washed in a manner known per se and cut.

The resulting fibre hat a fineness of 1.35 dtex and exhibited satisfactory tenacity properties.

Analysis of the raw material (Nano Pearl Powder) and the fibre produced therefrom gave the following results:


Example 2 – Spinning in a small pilot plant

A spinning solution was produced, having the following composition:

13% pulp
10.5% H2O
76.5% NMMO
3% Nano Pearl Powder (based on weight of cellulose)

The spinning solution, furthermore, contained a stabilizer as known per se.

The Nano Pearl Powder was first dispersed in 78% NMMO by means of an Ultra Turrax T 50 mixer. Then the pulp was added, a suspension was prepared, and a solution was produced from the suspension in a manner known per se.

The ready solution was spun at a spinning temperature of 120°C. The resulting fibre had a fineness of 1.35 dtex and exhibited satisfactory tenacity properties.

Balance of calcium yield

The Nano Pearl Powder employed contains 40% calcium. A loss of calcium in the washing baths in an amount of 12.7% was determined.


WE CLAIM:-

1. Lyocell fibre, containing a material selected from the group consisting of pearl powder, ground nacre and mixtures thereof.

2. Lyocell fibre according to claim 1, characterized in that the material is present in an amount of from 0.07 wt.% to 5 wt.%, based on fibre.

3. Lyocell fibre according to claim 1 or 2, characterized in that the material has an average particle size of from 0.04 to 1.5 µm, preferably 0.4 to 1.0 µm.

4. Process for the manufacture of a Lyocell fibre according to any of the preceding claims, comprising the steps of

- manufacturing a spinning solution of cellulose in an aqueous tertiary amine oxide, preferably N-methylmorpholine-N-oxide (NMMO)
- spinning the spinning solution to fibres,

characterized in that a material selected from the group consisting of pearl powder, ground nacre and mixtures thereof is admixed to the spinning solution and/or to a precursor thereof.

5. Process according to claim 4, characterized in that the material is admixed in an amount of from 0.1 wt.% to 5 wt.%, based on cellulose.

6. Process according to claim 4 or 5, characterized in that the material is employed in the form of a powder with an average particle size of from 0.04 to 1.5 µm, preferably 0.4 to 1.0 µm.

7. Process according to claim 6, characterized in that the powder is converted into the form of an aqueous suspension prior to being admixed to the spinning solution or the precursor thereof, respectively.

8. Use of a Lyocell fibre according to any of claims 1 to 3 as a product with cosmetic effect in a textile article and/or in a non-woven cosmetic product.

Documents

Application Documents

# Name Date
1 318-MUMNP-2010-FORM-PCT-ISA-237(14-05-2010).pdf 2010-05-14
2 318-MUMNP-2010-FORM-PCT-IB-338(14-05-2010).pdf 2010-05-14
3 318-MUMNP-2010-CORRESPONDENCE(14-05-2010).pdf 2010-05-14
4 Other Patent Document [13-02-2017(online)].pdf 2017-02-13
5 318-MUMNP-2010-Certified Copy of Priority Document (MANDATORY) [21-11-2017(online)].pdf 2017-11-21
6 318-MUMNP-2010-Information under section 8(2) (MANDATORY) [18-12-2017(online)].pdf 2017-12-18
7 318-MUMNP-2010-OTHERS [20-12-2017(online)].pdf 2017-12-20
8 318-MUMNP-2010-FER_SER_REPLY [20-12-2017(online)].pdf 2017-12-20
9 318-MUMNP-2010-CLAIMS [20-12-2017(online)].pdf 2017-12-20
10 Form-5.pdf 2018-08-10
11 Form-3.pdf 2018-08-10
12 Form-1.pdf 2018-08-10
13 318-MUMNP-2010-WO INTERNATIONAL PUBLICATION REPORT A1(2-8-2011).pdf 2018-08-10
14 318-MUMNP-2010-ORIGINAL UNDER RULE 6 (1A)-ENGLISH TRANSLATION-041217.pdf 2018-08-10
15 318-MUMNP-2010-FORM 1(4-5-2010).pdf 2018-08-10
15 318-MUMNP-2010-FORM 3(19-7-2010).pdf 2018-08-10
16 318-MUMNP-2010-FORM 26(4-5-2010).pdf 2018-08-10
16 318-MUMNP-2010-FORM 13(31-7-2012).pdf 2018-08-10
17 318-MUMNP-2010-FORM 18(2-8-2011).pdf 2018-08-10
18 318-MUMNP-2010-FORM 13(31-7-2012).pdf 2018-08-10
19 318-MUMNP-2010-FORM 1(4-5-2010).pdf 2018-08-10
20 318-MUMNP-2010-FORM 1(31-7-2012).pdf 2018-08-10
21 318-MUMNP-2010-FER.pdf 2018-08-10
22 318-MUMNP-2010-CORRESPONDENCE(4-5-2010).pdf 2018-08-10
23 318-MUMNP-2010-CORRESPONDENCE(31-7-2012).pdf 2018-08-10
24 318-MUMNP-2010-CORRESPONDENCE(2-8-2011).pdf 2018-08-10
25 318-MUMNP-2010-CORRESPONDENCE(19-7-2010).pdf 2018-08-10
26 318-MUMNP-2010-HearingNoticeLetter.pdf 2019-01-18
27 318-MUMNP-2010-REQUEST FOR ADJOURNMENT OF HEARING UNDER RULE 129A [05-03-2019(online)].pdf 2019-03-05
28 318-MUMNP-2010-ExtendedHearingNoticeLetter_16Apr2019.pdf 2019-04-12
29 318-MUMNP-2010-Written submissions and relevant documents (MANDATORY) [26-04-2019(online)].pdf 2019-04-26
30 318-MUMNP-2010-ExtendedHearingNoticeLetter_27-06-2019.pdf 2019-06-27
31 318-MUMNP-2010-PatentCertificate01-07-2019.pdf 2019-07-01
32 318-MUMNP-2010-IntimationOfGrant01-07-2019.pdf 2019-07-01
33 318-MUMNP-2010-RELEVANT DOCUMENTS [15-03-2020(online)].pdf 2020-03-15

Search Strategy

1 PatSeer_17-03-2017.pdf

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