EP1601824B1 - The method of making modified cellulose fibers - Google Patents
The method of making modified cellulose fibers Download PDFInfo
- Publication number
- EP1601824B1 EP1601824B1 EP03816268A EP03816268A EP1601824B1 EP 1601824 B1 EP1601824 B1 EP 1601824B1 EP 03816268 A EP03816268 A EP 03816268A EP 03816268 A EP03816268 A EP 03816268A EP 1601824 B1 EP1601824 B1 EP 1601824B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- cellulose
- spinning
- nano
- weight
- fibers
- 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.)
- Revoked
Links
- 229920003043 Cellulose fiber Polymers 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 238000009987 spinning Methods 0.000 claims abstract description 84
- 229920002678 cellulose Polymers 0.000 claims abstract description 51
- 239000001913 cellulose Substances 0.000 claims abstract description 51
- LFTLOKWAGJYHHR-UHFFFAOYSA-N N-methylmorpholine N-oxide Chemical compound CN1(=O)CCOCC1 LFTLOKWAGJYHHR-UHFFFAOYSA-N 0.000 claims abstract description 28
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000000975 dye Substances 0.000 claims abstract description 8
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 7
- 239000002696 acid base indicator Chemical group 0.000 claims abstract description 5
- 239000003899 bactericide agent Chemical group 0.000 claims abstract description 5
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 5
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 5
- 239000000203 mixture Substances 0.000 claims abstract description 5
- 239000002904 solvent Substances 0.000 claims abstract description 5
- 239000000919 ceramic Substances 0.000 claims abstract description 4
- 230000003750 conditioning effect Effects 0.000 claims abstract description 4
- 238000001035 drying Methods 0.000 claims abstract description 4
- 238000001704 evaporation Methods 0.000 claims abstract description 4
- 239000004332 silver Substances 0.000 claims abstract description 4
- 229910052709 silver Inorganic materials 0.000 claims abstract description 4
- 239000004094 surface-active agent Substances 0.000 claims abstract description 4
- 238000001914 filtration Methods 0.000 claims abstract description 3
- 239000000243 solution Substances 0.000 claims description 67
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 24
- 238000000034 method Methods 0.000 claims description 17
- 239000002105 nanoparticle Substances 0.000 claims description 17
- 239000003607 modifier Substances 0.000 claims description 13
- 239000000377 silicon dioxide Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 8
- 230000004048 modification Effects 0.000 claims description 6
- 238000012986 modification Methods 0.000 claims description 6
- KJFMBFZCATUALV-UHFFFAOYSA-N phenolphthalein Chemical compound C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)C2=CC=CC=C2C(=O)O1 KJFMBFZCATUALV-UHFFFAOYSA-N 0.000 claims description 6
- 235000012239 silicon dioxide Nutrition 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 5
- PRZSXZWFJHEZBJ-UHFFFAOYSA-N thymol blue Chemical compound C1=C(O)C(C(C)C)=CC(C2(C3=CC=CC=C3S(=O)(=O)O2)C=2C(=CC(O)=C(C(C)C)C=2)C)=C1C PRZSXZWFJHEZBJ-UHFFFAOYSA-N 0.000 claims description 5
- 239000002071 nanotube Substances 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 2
- 150000001721 carbon Chemical class 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract description 2
- 239000000835 fiber Substances 0.000 description 71
- 239000002245 particle Substances 0.000 description 24
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 14
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 12
- 239000000843 powder Substances 0.000 description 12
- 239000003242 anti bacterial agent Substances 0.000 description 10
- 230000000844 anti-bacterial effect Effects 0.000 description 10
- 230000008569 process Effects 0.000 description 10
- XEFQLINVKFYRCS-UHFFFAOYSA-N Triclosan Chemical compound OC1=CC(Cl)=CC=C1OC1=CC=C(Cl)C=C1Cl XEFQLINVKFYRCS-UHFFFAOYSA-N 0.000 description 8
- 239000000049 pigment Substances 0.000 description 8
- 239000004753 textile Substances 0.000 description 7
- 239000011787 zinc oxide Substances 0.000 description 7
- 239000006229 carbon black Substances 0.000 description 6
- 230000003385 bacteriostatic effect Effects 0.000 description 5
- 229910052681 coesite Inorganic materials 0.000 description 5
- 229910052906 cristobalite Inorganic materials 0.000 description 5
- 238000010348 incorporation Methods 0.000 description 5
- 229910052682 stishovite Inorganic materials 0.000 description 5
- 229910052905 tridymite Inorganic materials 0.000 description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 239000002041 carbon nanotube Substances 0.000 description 4
- 229910021393 carbon nanotube Inorganic materials 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000004408 titanium dioxide Substances 0.000 description 4
- 229910052593 corundum Inorganic materials 0.000 description 3
- 239000001023 inorganic pigment Substances 0.000 description 3
- 239000012860 organic pigment Substances 0.000 description 3
- 230000005855 radiation Effects 0.000 description 3
- 229910001845 yogo sapphire Inorganic materials 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 206010061592 cardiac fibrillation Diseases 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000001143 conditioned effect Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000002600 fibrillogenic effect Effects 0.000 description 2
- LNTHITQWFMADLM-UHFFFAOYSA-N gallic acid Chemical compound OC(=O)C1=CC(O)=C(O)C(O)=C1 LNTHITQWFMADLM-UHFFFAOYSA-N 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 229910052596 spinel Inorganic materials 0.000 description 2
- JKFYKCYQEWQPTM-UHFFFAOYSA-N 2-azaniumyl-2-(4-fluorophenyl)acetate Chemical compound OC(=O)C(N)C1=CC=C(F)C=C1 JKFYKCYQEWQPTM-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 229920000433 Lyocell Polymers 0.000 description 1
- 229910026161 MgAl2O4 Inorganic materials 0.000 description 1
- 241000218657 Picea Species 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- QOSMNYMQXIVWKY-UHFFFAOYSA-N Propyl levulinate Chemical compound CCCOC(=O)CCC(C)=O QOSMNYMQXIVWKY-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910021612 Silver iodide Inorganic materials 0.000 description 1
- FOIXSVOLVBLSDH-UHFFFAOYSA-N Silver ion Chemical compound [Ag+] FOIXSVOLVBLSDH-UHFFFAOYSA-N 0.000 description 1
- SEQDDYPDSLOBDC-UHFFFAOYSA-N Temazepam Chemical compound N=1C(O)C(=O)N(C)C2=CC=C(Cl)C=C2C=1C1=CC=CC=C1 SEQDDYPDSLOBDC-UHFFFAOYSA-N 0.000 description 1
- 238000005411 Van der Waals force Methods 0.000 description 1
- MQIGIUNAEDOSKG-UHFFFAOYSA-K [Zn+2].[Ag+].[O-]P([O-])([O-])=O Chemical compound [Zn+2].[Ag+].[O-]P([O-])([O-])=O MQIGIUNAEDOSKG-UHFFFAOYSA-K 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- KECAIQNCFZTEBM-UHFFFAOYSA-N antimony;chromium Chemical compound [Sb]#[Cr] KECAIQNCFZTEBM-UHFFFAOYSA-N 0.000 description 1
- TUFZVLHKHTYNTN-UHFFFAOYSA-N antimony;nickel Chemical compound [Sb]#[Ni] TUFZVLHKHTYNTN-UHFFFAOYSA-N 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011852 carbon nanoparticle Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003631 expected effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 229940074391 gallic acid Drugs 0.000 description 1
- 235000004515 gallic acid Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000009878 intermolecular interaction Effects 0.000 description 1
- 238000009940 knitting Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000003094 microcapsule Substances 0.000 description 1
- ZBJVLWIYKOAYQH-UHFFFAOYSA-N naphthalen-2-yl 2-hydroxybenzoate Chemical compound OC1=CC=CC=C1C(=O)OC1=CC=C(C=CC=C2)C2=C1 ZBJVLWIYKOAYQH-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 150000003377 silicon compounds Chemical class 0.000 description 1
- 150000003378 silver Chemical class 0.000 description 1
- 229940045105 silver iodide Drugs 0.000 description 1
- GGCZERPQGJTIQP-UHFFFAOYSA-N sodium;9,10-dioxoanthracene-2-sulfonic acid Chemical compound [Na+].C1=CC=C2C(=O)C3=CC(S(=O)(=O)O)=CC=C3C(=O)C2=C1 GGCZERPQGJTIQP-UHFFFAOYSA-N 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 229960003500 triclosan Drugs 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
Definitions
- the subject of the present invention is the method of making modified cellulose fibres from cellulose solutions in N-methylmorpholine-N-oxide.
- NMMO N-methylmorpholine-N-oxide
- One known process for manufacturing cellulose fibres from cellulose solutions in N-methylmorpholine-N-oxide consists of mixing cellulose with an aqueous solution of NMMO, evaporating excess water from the cellulose solution, filtrating the spinning solution, which is then forced through the spinneret holes into the airspace, followed by treatment in a spinning bath, drying and conditioning.
- modifiers such as titanium dioxide and organic or inorganic dyes in the form of particles or microcapsules with a diameter over I ⁇ m are added to the spinning solution (Textiles Magazine 2004, No 4, p.7); the modifiers may also include synthetic polymers with various molecular weights, as mentioned in the patent specification US 6245837 B1.
- Cellulose fibres such as Lyocell, produced from cellulose solutions in NMMO, are susceptible to fibrillation.
- the textile processing of such fibres creates technological problems connected with dusting and fluffing from yarns made from these fibres, especially in the production of knitted fabrics.
- low- or high-molecular modifiers are added to the spinning solution to change the structure of these fibres, and consequently to reduce their susceptibility to fibrillation.
- Patent specification US 5 047 197 suggests the addition of polyethylene glycol with a molecular weight of 1:4.5 million to the spinning solution to improve the flow of the spinning solution through the spinneret capillaries, which would at the same time modify the fibre microcrystalline structure.
- Patent Application DE 19542533 A1 describes the production of cellulose fibres by the NMMO process, in which carbon black particles with a diameter of about 20 nm are added to the spinning solution to modify the fibres' microcrystalline structure. This process yields electro-conductive fibres in which carbon black particles are distributed either throughout the fibre's whole volume or in its core.
- One drawback of such an incorporation of carbon nano-particles into the spinning solution, as described by D. Vorbach and E. Tanger in Chemical Fibres International 1998, No 48, p.120, is that these particles agglomerate in the polar medium of NMMO, which makes it necessary to add carbon black in quite a high quantity, over 30% by wt., in order to obtain good electro-conductivity of fibres.
- This high carbon particle content in the fibre-forming polymer reduces the tensile strength and knot breaking strength of fibres, making them unsuitable for textile processing. Such a modification results in weak and breakable fibres.
- Such undesirable fibre properties are due to the mechanical disintegration of carbon black into particles with an average diameter of 20 nm.
- the mechanical disintegration of solid particles of organic or inorganic pigments e.g. carbon black, titanium dioxide, zinc oxide, coloured pigments based on spinel (MgAl 2 O 4 ) or nickel-antimony yellow (Pigment Yellow 53/77780) or chromium-antimony yellow (Pigment Yellow 24/77310), makes it impossible to prepare a homogeneous pigment in terms of particle size.
- the circular particles of modifier isolate particular cellulose macromolecules in the fibre, and eliminate possible intermolecular bonds via Van der Waals forces; this leads to the deterioration of mechanical fibre properties such as tensile strength and knot breaking strength.
- Patent Application WO 96/27638 states that the drop in fibre tensile strength and knot breaking strength, as well as the disturbance of the fibre spinning process, result from the agglomeration of mechanically-disintegrated neutral pigments, e.g. titanium dioxide, barium sulphate, carbon black etc.
- Patent Application WO 96/27638 proposes producing modified fibres by incorporating mechanically disintegrated particles, into the spinning solution. Unfortunately, this method also fails to guarantee fibres with good properties, as solid coated particles or particles dispersed in a matrix are also agglomerated in a polar medium like the cellulose-NMMO-water system. This system causes the coat or matrix to dissolve, while the modifier molecules are agglomerated to form a heterogeneous dispersion in the fibre-forming polymer, which considerably reduces the properties of the modified fibres.
- Patent Application WO 01/06054 A1 states that the use of nano-particles for surface modification of textiles ensures that these textile products have excellent performance properties. Although the effect of surface modification of fibres and textiles with nano-particles is very resistant to washing under household conditions, it is not resistant to use and wear, during which the expected effect disappears due to superficial abrasion.
- the method of making modified cellulose fibres from cellulose solutions in N-methylmorpholine-N-oxide consists of mixing cellulose with an aqueous solution of NMMO, evaporating the resultant cellulose solution to obtain a cellulose content of 12-20% by wt.
- modifiers in the form of ceramic oxides, metal oxides or a mixture of these oxides, if necessary containing an addition of surface-active agents, carbon, if necessary modified with silver, bactericidal agents, acid-base indicators, thermochromic dyes in a quantity no higher than 10% by wt. in relation to the weight of cellulose, according to the present invention characterised by the fact, that modifiers have nano particle size and they are added to cellulose, solvent or the spinning solution.
- Ceramic oxides preferably silica, metal oxides or mixtures of these are used in the form of nano particle size or a suspension of this nano particle size in water or an aqueous NMMO solution.
- Carbon is used in the form of fibrous nano-tubes.
- As an acid-base indicator are preferably used thymol blue or phenolphthalein.
- This method according to the invention allows relatively simply modified cellulose fibres with specific properties to be produced, owing to the incorporation of modifiers in the form of nano- particles into cellulose, solvent or the spinning solution.
- the process according to which modifiers in the form of nano-particles, prepared by hydrolysis (among other things) of silicon- or organometallic compounds (as reported by the Journal of Nano-Crystalline Solids 1998, No 194, p. 72-77), are added to cellulose, solvent or the spinning solution, provides a durable modification of the fibre properties, and causes no deterioration in fibre tensile strength and knot breaking strength, which has turned out to be an unexpected effect.
- the nano-particle size of modifiers used in the process according to the invention ensures that the modified cellulose fibres which are produced show excellent properties specific to the given modifier. At the same time, not only are the mechanical properties of fibres not deteriorated, but they are in fact improved, which is also an unexpected effect.
- the incorporation of carbon nano-tubes of a fibrous character, prepared under special conditions ensures that the fibres produced show excellent mechanical and electrical properties.
- the vacuum pump therein was switched on, and to start with the crusher was heated till the inside temperature reached 100° C, subsequently the temperature inside the crusher was raised till it reached 130° C.
- the spinning solution made by this method contained 15% cellulose by weight, having been thoroughly filtered by acid resisting screen unit it was forced into the spinning head of worm spinning frame, where it was forced through the 0,16 mm holes in the spinning nozzle at temperature 100°C, placed 20 mm above the spinning bath, into the aqueous spinning bath of 80°C comprising 4% NMMO by weight.
- the formed fibers were rinsed in the rinsing bath of 80° C, taken up on the reel with the speed of 80 m/min, subsequently dried and conditioned.
- the received fibers were circular in section, white and lustreless, tensile strength being 32 cN/tex, elongation 12 % and fibrillization 2-3, whereas the fibrillization of unmodified fibers is 6.
- the received spinning solution was filtered as in Example I, subsequently at temperature 110°C forced through the holes in the spinning nozzle, placed 20 mm above the spinning bath, into the spinning bath as in Example I.
- the next step was as in Example I.
- the speed of fiber forming was 120 m/ min.
- the received fibers were circular in section, tensile strength being 36 cN/tex, elongation 13 % and fibrillization 3-4.
- the spinning solution was prepared as in Example I, but at the same time, while dissolving the cellulose, aqueous supension of silicon dioxide SiO 2 with nano particle size (the molecules diameter being 78 nm), was added to the crusher in such quantity that SiO 2 content was equal to 5 weight % in ratio to the cellulose by weight.
- the surfactant under the trade name Berol V-4026 was introduced along with the silicon suspension in the amount 1 weight % in ratio to the cellulose weight.
- the received spinning solution was filtered as in example I, subsequently at temperature 110° C forced through the holes in the spinning nozzle, placed 45 mm above the spinning bath, into the spinning bath as in Example I.
- the next step was as in Example 1.
- the speed of fiber forming was 160 m/ min.
- the received fibers were described as-having tensile strength 38 cN/tex, elongation 12 % and fibrillization 3-4.
- the received spinning solution was filtered as in example 1, subsequently at temperature 110° C forced through the holes in the spinning nozzle, placed 150 mm above the spinning bath, into the spinning bath at temperature 30°C containing 6% NMMO.
- the next step was as in Example 1.
- the speed of fiber forming was 150 m/ min.
- the received fibers were described as having tensile strength 36 cN/tex, elongation 10 % and fibrillization 3-4. Moreover they were described as having 50% greater ability to disperse UV radiation as compared to fibers received by all known methods.
- the received spinning solution was filtered as in Example I, subsequently at temperature 110° C forced through the holes in the spinning nozzle, placed 60 mm above the spinning bath, into the spinning bath of 20° C, containing 4,5 % NMMO.
- the next step was as in Example I.
- the speed of fiber forming was 180 m/min.
- the received fibers were described as having tensile strength 33 cN/tex, elongation 10%, fibrillization 3 and 37% greater ability to disperse UV radiation as compared to standard cellulose fibers.
- the spinning solution was prepared as in Example 1, but at the same time, in the place of aqueous supension of silicon dioxide, aqueous solution of aluminium trioxide Al 2 O 3 with nano particle size, the particles being 37 nm, was added in such quantity that Al 2 O 3 content was equal to 1,5 weight % in ratio to the cellulose by weight.
- the received spinning solution was filtered as in example I, subsequently at temperature 110°C forced through the holes in the spinning nozzle, placed 40 mm above the spinning bath, into the spinning bath of 20°C, containing 4% NMMO.
- the next step was as in Example I.
- the speed of fiber forming was 80 m/min.
- the received fibers circular in section, were described by the tensile strength 39 cN/tex, elongation 14 % and fibrillization 3.
- the received spinning solution was filtered as in example I, subsequently at temperature 110°C forced through the holes in the spinning nozzle, placed 20 mm above the spinning bath, into the spinning bath of 20° C, containing 4% NMMO.
- the next step was as in Example I.
- the speed of fiber forming was 140 m/min.
- the received fibers were described as having tensile strength 42 cN/tex, elongation 10%, fibrillization 3 and ability to disperse UV radiation 40% greater as compared to standard cellulose fibers.
- the solutions were mixed at 117°C for 70 minutes under lowered pressure.
- Antibacterial activity of produced fibers towards Escherichia coli was estimated based on the Japanese standard JIS L1902; 1998. It was stated that the fibers originating from the spinning solution already containing 0.5 weight % of antibacterial agent showed high both bactericidal and bacteriostatic activity. It was stated, moreover, that adding even 5 weight % of a bactericide agent into the spinning solution does not cause any significant changes in physico-mechanical parameters as compared to cellulose fibers produced without Irgasan.
- Example VIII The process of fiber making was repeated as in Example VIII, but instead of Irgasan silver iodide AgJ in the shape of powder, the grain diameter being up to 98 nm, was added to the spinning solution in the amount 0,2-5 weight % in ratio to the cellulose weight.
- Antibacterial activity of produced fibers was estimated as in Example VIII. It was stated that the fibers received from the spinning solution already containing 0.5 weight % of antibacterial agent showed high both bactericidal and bacteriostatic activity. It was stated, moreover, that adding 5 weight % of AgJ to the spinning solution causes only slight reduction of fiber elongation at breaking, and of water retention, as compared to other fibers produced without AgJ.
- Example VIII The process of fiber making was repeated as in Example VIII, but, instead of Irgasan, Al 2 O 3 , doped with silver ion, under the trade name Biostat, in the shape of powder, the grain diameter being 57 nm, was added to the spinning solution in the amount 0,2-5 weight % in ratio to the cellulose weight: Antibacterial activity of produced fibers was estimated as in Example VIII. It was stated that the fibers originating from the spinning solution already containing 0.5 weight % of antibacterial agent showed high both bactericidal and bacteriostatic activity. It was stated, moreover, that adding 5 weight % of Biostat causes only slight change in physicomechanical parameters of fibers as compared to other fibers produced without Biostat.
- Example VIII The process of fiber making was repeated as in Example VIII, but, instead of Irgasan, silver-zinc phosphate under the trade name Novaron, in the shape of powder, the grain diameter being 132 nm, was added to the spinning solution in the amount 0,2-5 weight % in ratio to the cellulose weight.
- Irgasan silver-zinc phosphate under the trade name Novaron
- Antibacterial activity of produced fibers was estimated as in Example VIII. It was stated that the fibers originating from the spinning solution already containing 0.5 weight % of antibacterial agent showed high bactericidal and bacteriostatic activity. The addition of even 5 weight % of Novaron caused insignificant physico-mechanical changes of the fibers as compared to other fibers produced without Novaron.
- Example number The antibacterial agent used The amount of antibacterial agent in the spinning solution Linear mass (dtex) Tensile (tearing) strength (cN/tex) Elongation % Sorption in 65% RH [%] Retention [%] Fibres without antibacterial agent 2,97 36,82 12,87 10,69 73,21 VIII Irgasan DP 300 0,5 3,40 32,73 10,75 10,70 72,32 IX AgJ 0,5 2,71 38,64 9,73 10,57 67,82 X Biostat 0,5 3,79 31,54 7,01 XI Novaron 0,5 2,20 39,21 7,16
- Carbon nanotubes in the shape of powder was introduced into the cellulose solution in NMMO, prepared as in Example I, in the amount 3 weight % in ratio to the cellulose by weight, and the whole lot was exposed to mixing.
- the received spinning solution was filtered, subsequently forced through the 18-hole spinning nozzle with the speed of 87m/min into the spinning bath at temperature 20°C
- the distance between the spinneret and the aqueous bath was 100 mm.
- the produced fibers were rinsed under stress in water bath at temperature 80° C, subsequently they were dried and conditioned. Subsequently mechanical and electrical properties of the fibers were measured.
- the received fibers were described as having tensile strength 36 cN/tex and elongation 10%.
- the fibers conducted the current, their resistance was 10 3 ⁇ cm whereas the resistance of fibers not containing carbon nanotubes was 10 10 ⁇ cm
- the spinning solution was prepared as in Example XII, and at the same time carbon nanotubes, modified by metallic silver, in the shape of powder, were introduced into the cellulose solution in NMMO in the amount 3 weight % in ratio to the cellulose by weight, Nanotubes were modified in such way that they were impregnated by aqueous solution of silver salt, subsequently the silver salts were reduced. Fibers were formed from the filtered spinning solution following Example XII. It was stated that tensile strength of the received fibers was 36 cN/tex , elongation was 8% and their resistance rose to 10 -2 ⁇ cm
- the spinning solution was prepared as in Example I, with such difference, that instead of thymol blue, phenolphthalein in the shape of powder, the particles diameter being 96 nm, was introduced in the amount 0,3 weight % in ratio to the cellulose by weight. Fibers were formed from the filtered spinning solution following example XII.
- Tensile strength of the received fibers was 32cN/tex , elongation was 10%.
- the produced fibers were white, and turned red, if dipped in an aqueous solution at the pH of 10, whereas if dipped in an aqueous solution at the pH of 8 they turned blue, what proved that the received fibers are the pH sensors.
- thermochromic dye BT-31 in the shape of powder, the particles diameter being 173 nm, was introduced in the amount 3 weight % in ratio to the cellulose by weight. Fibers were formed from the filtered spinning solution following example XII.
- the produced fibers were pale blue, and turned white at the temperature 31° C. It proved that the received fibers are temperature sensors. Tensile strength of the received fibers was 35cN/tex , elongation was 12 %.
- thermochromic dye Bt-43 in the shape of powder, the particles diameter being 85 nm, was introduced in the amount 2 weight % in ratio to the cellulose by weight. Fibers were formed from the filtered spinning solution following example XII.
- the produced fibers were pale blue, and turned white at the temperature 43° C. In the temperature rising above 43° C they become colorless, and if the temperature was lowered below 43° C they became pale blue again. It proved that the received fibers had stable thermochromic properties. Tensile strength of the received fibers was 35cN/tex , elongation was 12 %.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Textile Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Artificial Filaments (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
- The subject of the present invention is the method of making modified cellulose fibres from cellulose solutions in N-methylmorpholine-N-oxide.
- One known process for manufacturing cellulose fibres from cellulose solutions in N-methylmorpholine-N-oxide (NMMO) consists of mixing cellulose with an aqueous solution of NMMO, evaporating excess water from the cellulose solution, filtrating the spinning solution, which is then forced through the spinneret holes into the airspace, followed by treatment in a spinning bath, drying and conditioning. In order to produce fibres with modified properties, modifiers such as titanium dioxide and organic or inorganic dyes in the form of particles or microcapsules with a diameter over I µm are added to the spinning solution (Textiles Magazine 2004, No 4, p.7); the modifiers may also include synthetic polymers with various molecular weights, as mentioned in the patent specification US 6245837 B1.
- When manufacturing cellulose fibres by the process delineated in the present invention, the incorporation of either organic or inorganic, low- or high-molecular compounds into the spinning solution in the form of particles with diameters higher than 1 µm would result in unpredictable changes to the fibre properties, in comparison to those of fibres obtained without these modifiers.
- Cellulose fibres such as Lyocell, produced from cellulose solutions in NMMO, are susceptible to fibrillation. The textile processing of such fibres creates technological problems connected with dusting and fluffing from yarns made from these fibres, especially in the production of knitted fabrics. To overcome this problem, low- or high-molecular modifiers are added to the spinning solution to change the structure of these fibres, and consequently to reduce their susceptibility to fibrillation.
- Patent specification US 5 047 197 suggests the addition of polyethylene glycol with a molecular weight of 1:4.5 million to the spinning solution to improve the flow of the spinning solution through the spinneret capillaries, which would at the same time modify the fibre microcrystalline structure.
- Patent Application DE 19542533 A1 describes the production of cellulose fibres by the NMMO process, in which carbon black particles with a diameter of about 20 nm are added to the spinning solution to modify the fibres' microcrystalline structure. This process yields electro-conductive fibres in which carbon black particles are distributed either throughout the fibre's whole volume or in its core. One drawback of such an incorporation of carbon nano-particles into the spinning solution, as described by D. Vorbach and E. Tanger in Chemical Fibres International 1998, No 48, p.120, is that these particles agglomerate in the polar medium of NMMO, which makes it necessary to add carbon black in quite a high quantity, over 30% by wt., in order to obtain good electro-conductivity of fibres. This high carbon particle content in the fibre-forming polymer reduces the tensile strength and knot breaking strength of fibres, making them unsuitable for textile processing. Such a modification results in weak and breakable fibres. Such undesirable fibre properties are due to the mechanical disintegration of carbon black into particles with an average diameter of 20 nm. The mechanical disintegration of solid particles of organic or inorganic pigments, e.g. carbon black, titanium dioxide, zinc oxide, coloured pigments based on spinel (MgAl2O4) or nickel-antimony yellow (Pigment Yellow 53/77780) or chromium-antimony yellow (Pigment Yellow 24/77310), makes it impossible to prepare a homogeneous pigment in terms of particle size. Mechanically disintegrated pigments added to the spinning solution to modify fibre properties show a wide distribution of particle size, as illustrated by Gauss' distribution curve. As a result, particles with high diameters deteriorated the physico-mechanical properties of the fibres, making them unsuitable for textile processes such as spinning, weaving or knitting. Solid particles of inorganic or organic pigments, disintegrated mechanically, e.g. in a ball mill, have almost circular shapes. The incorporation of such shaped pigments into the spinning solution prior to fibre formation disturbs the development of oriented crystalline structure of fibres, lowering the intermolecular interactions between cellulose macromolecules.
- In such a case, the circular particles of modifier isolate particular cellulose macromolecules in the fibre, and eliminate possible intermolecular bonds via Van der Waals forces; this leads to the deterioration of mechanical fibre properties such as tensile strength and knot breaking strength.
- Patent Application WO 96/27638 states that the drop in fibre tensile strength and knot breaking strength, as well as the disturbance of the fibre spinning process, result from the agglomeration of mechanically-disintegrated neutral pigments, e.g. titanium dioxide, barium sulphate, carbon black etc. Patent Application WO 96/27638 proposes producing modified fibres by incorporating mechanically disintegrated particles, into the spinning solution. Unfortunately, this method also fails to guarantee fibres with good properties, as solid coated particles or particles dispersed in a matrix are also agglomerated in a polar medium like the cellulose-NMMO-water system. This system causes the coat or matrix to dissolve, while the modifier molecules are agglomerated to form a heterogeneous dispersion in the fibre-forming polymer, which considerably reduces the properties of the modified fibres.
- The properties of both nano-particles and supramolecular particles of organic or inorganic pigments such as titanium dioxide, zinc oxide or dyes are completely different from those of the molecules of pigments and dyes produced by traditional technologies, added in accordance with Patent Application WO 96/27638 to the spinning solution in order to prepare modified fibres.
- Patent Application WO 01/06054 A1 states that the use of nano-particles for surface modification of textiles ensures that these textile products have excellent performance properties. Although the effect of surface modification of fibres and textiles with nano-particles is very resistant to washing under household conditions, it is not resistant to use and wear, during which the expected effect disappears due to superficial abrasion.
- The method of making modified cellulose fibres from cellulose solutions in N-methylmorpholine-N-oxide consists of mixing cellulose with an aqueous solution of NMMO, evaporating the resultant cellulose solution to obtain a cellulose content of 12-20% by wt. and water content below 13% by wt., filtrating the spinning solution and extruding it through spinneret holes into airspace, from which it is led into an aqueous spinning bath followed by rinsing, drying and conditioning, the modification effect being obtained by adding modifiers in the form of ceramic oxides, metal oxides or a mixture of these oxides, if necessary containing an addition of surface-active agents, carbon, if necessary modified with silver, bactericidal agents, acid-base indicators, thermochromic dyes in a quantity no higher than 10% by wt. in relation to the weight of cellulose, according to the present invention characterised by the fact, that modifiers have nano particle size and they are added to cellulose, solvent or the spinning solution. Ceramic oxides, preferably silica, metal oxides or mixtures of these are used in the form of nano particle size or a suspension of this nano particle size in water or an aqueous NMMO solution. Carbon is used in the form of fibrous nano-tubes. As an acid-base indicator are preferably used thymol blue or phenolphthalein.
- This method according to the invention allows relatively simply modified cellulose fibres with specific properties to be produced, owing to the incorporation of modifiers in the form of nano- particles into cellulose, solvent or the spinning solution. The process , according to which modifiers in the form of nano-particles, prepared by hydrolysis (among other things) of silicon- or organometallic compounds (as reported by the Journal of Nano-Crystalline Solids 1998, No 194, p. 72-77), are added to cellulose, solvent or the spinning solution, provides a durable modification of the fibre properties, and causes no deterioration in fibre tensile strength and knot breaking strength, which has turned out to be an unexpected effect. The nano-particle size of modifiers used in the process according to the invention ensures that the modified cellulose fibres which are produced show excellent properties specific to the given modifier. At the same time, not only are the mechanical properties of fibres not deteriorated, but they are in fact improved, which is also an unexpected effect. The incorporation of carbon nano-tubes of a fibrous character, prepared under special conditions (Carbon 38 (2000), 1933- 1937), ensures that the fibres produced show excellent mechanical and electrical properties.
- The method according to the invention is illustrated by the examples given below which do not limit its range.
- 60 cellulose parts by weight with the degree of polymerization of 800 comprising 8% humidity by weight were introduced into the crusher connected with the vacuum pump and equipped with indirect heating; thereto subsequently 720 parts by weight of 50% aqueous NMMO solution and 20 parts by weight of 30% aqueous water suspension of silicon dioxide with nano particle size were added, the molecules diameter being 7 nm.
- Having set in motion the crusher mixers, the vacuum pump therein was switched on, and to start with the crusher was heated till the inside temperature reached 100° C, subsequently the temperature inside the crusher was raised till it reached 130° C.
- After approximately 60 minutes the water content in the system cellulose-NMMO-water diminished to 10 weight %, the cellulose was thoroughly solved, and the pulp in the crusher became light brown in color, and it had viscosity 1300 Pa x s. The spinning solution made by this method contained 15% cellulose by weight, having been thoroughly filtered by acid resisting screen unit it was forced into the spinning head of worm spinning frame, where it was forced through the 0,16 mm holes in the spinning nozzle at temperature 100°C, placed 20 mm above the spinning bath, into the aqueous spinning bath of 80°C comprising 4% NMMO by weight. The formed fibers were rinsed in the rinsing bath of 80° C, taken up on the reel with the speed of 80 m/min, subsequently dried and conditioned.
- The received fibers were circular in section, white and lustreless, tensile strength being 32 cN/tex, elongation 12 % and fibrillization 2-3, whereas the fibrillization of unmodified fibers is 6.
- Aqueous supension of silicon dioxide SiO2 with nano particle size, the molecules diameter being 50 nm, was introduced into the cellulose solution in NMMO, prepared in the same conditions as in Example I, in such an amount that the SiO2 content was 3 weight % in ratio to the cellulose weight, and the whole lot was mixed. The received spinning solution was filtered as in Example I, subsequently at temperature 110°C forced through the holes in the spinning nozzle, placed 20 mm above the spinning bath, into the spinning bath as in Example I. The next step was as in Example I. The speed of fiber forming was 120 m/ min. The received fibers were circular in section, tensile strength being 36 cN/tex, elongation 13 % and fibrillization 3-4.
- The spinning solution was prepared as in Example I, but at the same time, while dissolving the cellulose, aqueous supension of silicon dioxide SiO2 with nano particle size (the molecules diameter being 78 nm), was added to the crusher in such quantity that SiO2 content was equal to 5 weight % in ratio to the cellulose by weight. At the same time the surfactant under the trade name Berol V-4026 was introduced along with the silicon suspension in the amount 1 weight % in ratio to the cellulose weight. The received spinning solution was filtered as in example I, subsequently at temperature 110° C forced through the holes in the spinning nozzle, placed 45 mm above the spinning bath, into the spinning bath as in Example I. The next step was as in Example 1. The speed of fiber forming was 160 m/ min.
- The received fibers were described as-having tensile strength 38 cN/tex, elongation 12 % and fibrillization 3-4.
- Titan dioxide TiO2 in the shape of powder, the grain diameter being 17 nm, was introduced into the cellulose solution in NMMO, prepared in the same conditions as in Example I, in the amount 1 weight % in ratio to the cellulose by weight, and the whole lot was exposed to mixing. The received spinning solution was filtered as in example 1, subsequently at temperature 110° C forced through the holes in the spinning nozzle, placed 150 mm above the spinning bath, into the spinning bath at temperature 30°C containing 6% NMMO. The next step was as in Example 1. The speed of fiber forming was 150 m/ min.
- The received fibers were described as having tensile strength 36 cN/tex, elongation 10 % and fibrillization 3-4. Moreover they were described as having 50% greater ability to disperse UV radiation as compared to fibers received by all known methods.
- Aqueous supension of zinc oxide ZnO with powder, the particles diameter being 30 nm, was introduced into the cellulose solution in NMMO, prepared as in Example I, in such an amount that the ZnO content was 1 weight % in ratio to the cellulose weight, and the whole lot was mixed. The received spinning solution was filtered as in Example I, subsequently at temperature 110° C forced through the holes in the spinning nozzle, placed 60 mm above the spinning bath, into the spinning bath of 20° C, containing 4,5 % NMMO. The next step was as in Example I. The speed of fiber forming was 180 m/min.
- The received fibers were described as having tensile strength 33 cN/tex, elongation 10%, fibrillization 3 and 37% greater ability to disperse UV radiation as compared to standard cellulose fibers.
- The spinning solution was prepared as in Example 1, but at the same time, in the place of aqueous supension of silicon dioxide, aqueous solution of aluminium trioxide Al2O3 with nano particle size, the particles being 37 nm, was added in such quantity that Al2O3 content was equal to 1,5 weight % in ratio to the cellulose by weight. The received spinning solution was filtered as in example I, subsequently at temperature 110°C forced through the holes in the spinning nozzle, placed 40 mm above the spinning bath, into the spinning bath of 20°C, containing 4% NMMO. The next step was as in Example I. The speed of fiber forming was 80 m/min.
- The received fibers, circular in section, were described by the tensile strength 39 cN/tex, elongation 14 % and fibrillization 3.
- Aqueous supension of zinc oxide, titan dioxide and silicon dioxide (ZnO, TiO2, SiO2) by component weight in ratio I: I: I, with powder of, the particles diameter being 7-50 nm, was introduced into the cellulose solution in NMMO, prepared in the same conditions as in Example I, in such an amount that the oxides content was 3 weight % in ratio to the cellulose weight. The received spinning solution was filtered as in example I, subsequently at temperature 110°C forced through the holes in the spinning nozzle, placed 20 mm above the spinning bath, into the spinning bath of 20° C, containing 4% NMMO. The next step was as in Example I. The speed of fiber forming was 140 m/min.
- The received fibers were described as having tensile strength 42 cN/tex, elongation 10%, fibrillization 3 and ability to disperse UV radiation 40% greater as compared to standard cellulose fibers.
- Solutions containing 12 weight parts of spruce cellulose (DP 840), 76 weight parts of NMMO, 12 weight parts of water, propyl ester of gallic acid under the trade name Tenox in the amount 1 weight % in ratio to cellulose weight and a bactericide agent triclosan under the trade name Irgasan DP 300 in the shape of powder, the particles diameter being 137 nm, in the amount 0,5-5 weight % in ratio to the cellulose weight were prepared. The solutions were mixed at 117°C for 70 minutes under lowered pressure. From the originated spinning solutions after filtration fibers were formed by forcing the spinning solutions at temperature 115°C through the 18-hole spinning nozzle, the hole diameter being 0,4 mm and the duct length being 3,5 mm, with the speed 82 m/min into the coagulation bath containing water at temperature 20°C. The distance between the spinneret and the coagulation bath was 100 mm. The produced fibers were rinsed in water bath at temperature 80°C, subsequently they were dried.
- Antibacterial activity of produced fibers towards Escherichia coli was estimated based on the Japanese standard JIS L1902; 1998. It was stated that the fibers originating from the spinning solution already containing 0.5 weight % of antibacterial agent showed high both bactericidal and bacteriostatic activity. It was stated, moreover, that adding even 5 weight % of a bactericide agent into the spinning solution does not cause any significant changes in physico-mechanical parameters as compared to cellulose fibers produced without Irgasan.
- The process of fiber making was repeated as in Example VIII, but instead of Irgasan silver iodide AgJ in the shape of powder, the grain diameter being up to 98 nm, was added to the spinning solution in the amount 0,2-5 weight % in ratio to the cellulose weight.
- Antibacterial activity of produced fibers was estimated as in Example VIII. It was stated that the fibers received from the spinning solution already containing 0.5 weight % of antibacterial agent showed high both bactericidal and bacteriostatic activity. It was stated, moreover, that adding 5 weight % of AgJ to the spinning solution causes only slight reduction of fiber elongation at breaking, and of water retention, as compared to other fibers produced without AgJ.
- The process of fiber making was repeated as in Example VIII, but, instead of Irgasan, Al2O3, doped with silver ion, under the trade name Biostat, in the shape of powder, the grain diameter being 57 nm, was added to the spinning solution in the amount 0,2-5 weight % in ratio to the cellulose weight: Antibacterial activity of produced fibers was estimated as in Example VIII. It was stated that the fibers originating from the spinning solution already containing 0.5 weight % of antibacterial agent showed high both bactericidal and bacteriostatic activity. It was stated, moreover, that adding 5 weight % of Biostat causes only slight change in physicomechanical parameters of fibers as compared to other fibers produced without Biostat.
- The process of fiber making was repeated as in Example VIII, but, instead of Irgasan, silver-zinc phosphate under the trade name Novaron, in the shape of powder, the grain diameter being 132 nm, was added to the spinning solution in the amount 0,2-5 weight % in ratio to the cellulose weight.
- Antibacterial activity of produced fibers was estimated as in Example VIII. It was stated that the fibers originating from the spinning solution already containing 0.5 weight % of antibacterial agent showed high bactericidal and bacteriostatic activity. The addition of even 5 weight % of Novaron caused insignificant physico-mechanical changes of the fibers as compared to other fibers produced without Novaron.
- Bactericidal properties of fibers made in Examples VIII-XI were shown in tab. 1, and physico-mechanical properties of these fibers, according to the amount of antibacterial agent added, in tab. 2.
Table 1. Example number The antibacterial agent used The amount of antibacterial agent in the spinning solution [%] Amount of bacteria on the fiber sample Fiber bacteriostatic activity [S] Fiber bactericidal activity [L] VIII Irgasan DP 300 0,5 <20 6,8 4,0 IX AgJ 0,5 <20 6,5 3,5 X Biostat 0,5 <20 7,0 3,5 XI Novaron 0,5 <20 7,0 3,5 Table 2. Example number The antibacterial agent used The amount of antibacterial agent in the spinning solution Linear mass (dtex) Tensile (tearing) strength (cN/tex) Elongation % Sorption in 65% RH [%] Retention [%] Fibres without antibacterial agent 2,97 36,82 12,87 10,69 73,21 VIII Irgasan DP 300 0,5 3,40 32,73 10,75 10,70 72,32 IX AgJ 0,5 2,71 38,64 9,73 10,57 67,82 X Biostat 0,5 3,79 31,54 7,01 XI Novaron 0,5 2,20 39,21 7,16 - Carbon nanotubes in the shape of powder was introduced into the cellulose solution in NMMO, prepared as in Example I, in the amount 3 weight % in ratio to the cellulose by weight, and the whole lot was exposed to mixing. The received spinning solution was filtered, subsequently forced through the 18-hole spinning nozzle with the speed of 87m/min into the spinning bath at temperature 20°C The distance between the spinneret and the aqueous bath was 100 mm. The produced fibers were rinsed under stress in water bath at temperature 80° C, subsequently they were dried and conditioned. Subsequently mechanical and electrical properties of the fibers were measured.
- The received fibers were described as having tensile strength 36 cN/tex and elongation 10%. The fibers conducted the current, their resistance was 103 Ω·cm whereas the resistance of fibers not containing carbon nanotubes was 1010 Ω·cm
- The spinning solution was prepared as in Example XII, and at the same time carbon nanotubes, modified by metallic silver, in the shape of powder, were introduced into the cellulose solution in NMMO in the amount 3 weight % in ratio to the cellulose by weight, Nanotubes were modified in such way that they were impregnated by aqueous solution of silver salt, subsequently the silver salts were reduced. Fibers were formed from the filtered spinning solution following Example XII.
It was stated that tensile strength of the received fibers was 36 cN/tex , elongation was 8% and their resistance rose to 10-2 Ω·cm - The spinning solution was prepared as in Example I, with such difference, that instead of thymol blue, phenolphthalein in the shape of powder, the particles diameter being 96 nm, was introduced in the amount 0,3 weight % in ratio to the cellulose by weight. Fibers were formed from the filtered spinning solution following example XII.
- Tensile strength of the received fibers was 32cN/tex , elongation was 10%. The produced fibers were white, and turned red, if dipped in an aqueous solution at the pH of 10, whereas if dipped in an aqueous solution at the pH of 8 they turned blue, what proved that the received fibers are the pH sensors.
- The spinning solution was prepared as in Example I, with such difference, that instead of thymol blue, thermochromic dye BT-31 in the shape of powder, the particles diameter being 173 nm, was introduced in the amount 3 weight % in ratio to the cellulose by weight. Fibers were formed from the filtered spinning solution following example XII.
- The produced fibers were pale blue, and turned white at the temperature 31° C. It proved that the received fibers are temperature sensors. Tensile strength of the received fibers was 35cN/tex , elongation was 12 %.
- The spinning solution was prepared as in Example XIV, with such difference, that instead of thymol blue, thermochromic dye Bt-43 in the shape of powder, the particles diameter being 85 nm, was introduced in the amount 2 weight % in ratio to the cellulose by weight. Fibers were formed from the filtered spinning solution following example XII.
- The produced fibers were pale blue, and turned white at the temperature 43° C. In the temperature rising above 43° C they become colorless, and if the temperature was lowered below 43° C they became pale blue again. It proved that the received fibers had stable thermochromic properties. Tensile strength of the received fibers was 35cN/tex , elongation was 12 %.
Claims (3)
- A method of making modified cellulose fibres from cellulose solutions in N-methylmorpholine-N-oxide, consisting of mixing cellulose with an aqueous solution of NMMO, evaporating the resultant cellulose solution to obtain a cellulose content of 12-20% by wt and water content below 13.3% by wt., filtering the spinning solution and extruding it through the capillaries of spinneret into the airspace, from which it is led into an aqueous spinning bath, finally rinsing, drying and conditioning, with the modification effect being obtained by adding modifiers, characterised in that the modifying compounds are selected from the group of oxides, metal oxides or their mixtures, if necessary containing an addition of surfactants, carbon, in the form of nano-tubes of a fibrous character if necessary carbon modified with silver, bactericidal agents, acid-base indicators, and thermochromic dyes have nano-particles size and they are added to cellulose, solvent or the spinning solution in a quantity not higher than 10% by wt. in relation to the weight of cellulose.
- The method as claimed in claim 1 characterised in that ceramic oxides, advantageously silicon dioxide, metal oxides or their mixtures are used in the form of nano-particle size or suspension of this nano-particle size in water or an aqueous solution of N-methyl morpholine-N-oxide;
- The method as claimed in claim 1 characterised in that as an acid-base indicator are preferably used thymol blue or phenolphthalein with nano-particle size.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL35908003 | 2003-03-10 | ||
PL359080A PL201205B1 (en) | 2003-03-10 | 2003-03-10 | Method for manufacture of modified cellulose fibres |
PCT/PL2003/000060 WO2004081267A1 (en) | 2003-03-10 | 2003-06-25 | The method of making modified cellulose fibers |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1601824A1 EP1601824A1 (en) | 2005-12-07 |
EP1601824B1 true EP1601824B1 (en) | 2007-01-17 |
Family
ID=32986092
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03816268A Revoked EP1601824B1 (en) | 2003-03-10 | 2003-06-25 | The method of making modified cellulose fibers |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1601824B1 (en) |
AT (1) | ATE351933T1 (en) |
DE (1) | DE60311324T2 (en) |
PL (1) | PL201205B1 (en) |
WO (1) | WO2004081267A1 (en) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB0417477D0 (en) * | 2004-08-05 | 2004-09-08 | Tencel Ltd | Anti-microbial fibres |
KR100575377B1 (en) * | 2004-12-24 | 2006-05-02 | 주식회사 효성 | Method for producing cellulose fiber containing nanoparticles |
AT502743B1 (en) | 2005-08-26 | 2008-06-15 | Chemiefaser Lenzing Ag | CELLULOSIC FORM BODY, METHOD FOR THE PRODUCTION THEREOF AND THE USE THEREOF |
DE102006014171A1 (en) * | 2006-03-24 | 2007-09-27 | Thüringisches Institut für Textil- und Kunststoff-Forschung e.V. | Panel radiator for use in the field of heating voltage, has electrically conductive cellulose non-woven material that forms electrical resistance required for heating, and two electrical strips, which electrically contacts the material |
DE102006033591B4 (en) * | 2006-07-18 | 2008-10-16 | Thüringisches Institut für Textil- und Kunststoff-Forschung e.V. | Process for stabilizing the spinning solution in the production of cellulosic composite moldings |
DE102006046358B3 (en) * | 2006-09-28 | 2007-11-29 | Thüringisches Institut für Textil- und Kunststoff-Forschung e.V. | Process for the preparation of functional cellulosic moldings |
WO2008100163A1 (en) | 2007-02-13 | 2008-08-21 | Instytut Wlókien Naturalnych | Method of manufacturing silver nanoparticles, cellulosic fibers and nanofibers containing silver nanoparticles, fibers and nanofibers containing silver nanoparticles, use of silver nanoparticles to the manufacture of cellulosic fibers and nanofibers, and wound dressing containing silver nanoparticles |
DE102007011848A1 (en) * | 2007-03-12 | 2008-09-25 | Wiberg Gmbh | Method for preventing the growth of microorganisms on the outside of a food casing |
DE102007019768A1 (en) | 2007-04-25 | 2008-11-13 | Thüringisches Institut für Textil- und Kunststoff-Forschung e.V. | A process for producing a high whiteness bioactive cellulosic fiber |
EP2162574B8 (en) * | 2007-07-03 | 2012-10-10 | Aditya Birla Science & Technology CO. LTD. | A viscose fiber with modified property and a process for making therefor |
DE102007054702B4 (en) | 2007-11-14 | 2018-10-18 | Smartpolymer Gmbh | Process for the preparation of cellulosic shaped bodies, cellulosic shaped bodies and their use |
AT508497A1 (en) * | 2009-06-15 | 2011-01-15 | Chemiefaser Lenzing Ag | PROTECTION TISSUE AGAINST ULTRAVIOLETTE RADIATION BASED ON ARTIFICIAL CELLULOSE FIBERS |
JP5544510B2 (en) * | 2010-03-30 | 2014-07-09 | 国立大学法人信州大学 | Composite fiber and method for producing composite fiber |
CN104264259A (en) * | 2014-10-15 | 2015-01-07 | 钱景 | Graphene and salix psammophila regenerated cellulose blended fiber and preparation method thereof |
CN104233492B (en) * | 2014-10-15 | 2016-01-06 | 钱景 | A kind of nanometer silver antimicrobial salix monogolica regenerated celulose fibre and preparation method thereof |
AT516414B1 (en) | 2014-10-28 | 2017-07-15 | Chemiefaser Lenzing Ag | Liquid-soaked non-woven fabric containing zinc oxide-containing cellulose fibers |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06220712A (en) * | 1993-01-22 | 1994-08-09 | Asahi Chem Ind Co Ltd | Synthetic resin fiber |
PL322109A1 (en) * | 1995-03-04 | 1998-01-05 | Akzo Nobel Nv | Composition containing fine solid particles |
JP3051709B2 (en) * | 1997-09-30 | 2000-06-12 | 憲司 中村 | Antimicrobial cellulose fiber and method for producing the same |
AT407997B (en) * | 1999-08-10 | 2001-07-25 | Chemiefaser Lenzing Ag | COLORED CELLULOSIC SHAPED BODIES |
JP3852681B2 (en) * | 2001-10-12 | 2006-12-06 | 東洋紡績株式会社 | Polybenzazole fiber |
-
2003
- 2003-03-10 PL PL359080A patent/PL201205B1/en not_active IP Right Cessation
- 2003-06-25 WO PCT/PL2003/000060 patent/WO2004081267A1/en active IP Right Grant
- 2003-06-25 AT AT03816268T patent/ATE351933T1/en not_active IP Right Cessation
- 2003-06-25 EP EP03816268A patent/EP1601824B1/en not_active Revoked
- 2003-06-25 DE DE60311324T patent/DE60311324T2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
ATE351933T1 (en) | 2007-02-15 |
PL359080A1 (en) | 2004-09-20 |
DE60311324T2 (en) | 2007-11-15 |
PL201205B1 (en) | 2009-03-31 |
DE60311324D1 (en) | 2007-03-08 |
WO2004081267A1 (en) | 2004-09-23 |
EP1601824A1 (en) | 2005-12-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1601824B1 (en) | The method of making modified cellulose fibers | |
KR101555001B1 (en) | Lyocell fiber | |
US20070170609A1 (en) | Method for producing cellulose fiber | |
JP5100872B2 (en) | Cellulose dyeing formation | |
US20100124861A1 (en) | Method for the production of a bioactive cellulose fiber with a high degree of whiteness | |
US7713459B2 (en) | Cellulose fiber for using as industrial materials | |
KR100749714B1 (en) | Articles with antibacterial and antifungal activity | |
CN1442518A (en) | Manufacturing method of antibacteria fiber containing nano particles | |
CN115028968A (en) | Antibacterial functional master batch, preparation method thereof, antibacterial polyester fiber and fabric | |
KR100769974B1 (en) | Manufacturing method of lyocell filament for clothing with excellent uniformity | |
JP2001011734A (en) | Antimicrobial polyamide fiber | |
JP2000119914A (en) | Production of antibacterial polyamide fiber | |
CN1053714C (en) | Far infrared fiber with good spinning property and its manufacture | |
DE2039105B2 (en) | METHOD OF MANUFACTURING SILK POLYAMIDE FIBER | |
US5240665A (en) | Process of making cellulose acetate fibers from spinning solutions containing metal oxide precursor | |
US3575898A (en) | Polyvinyl chloride-antimony oxide flame-retardant mixtures for cellulosic spinning dopes | |
KR100575377B1 (en) | Method for producing cellulose fiber containing nanoparticles | |
CN115821424B (en) | Environmentally friendly antibacterial colored polylactic acid fiber and preparation method thereof | |
JP5183329B2 (en) | Wet spinning method of antibacterial acrylic fiber | |
AT410806B (en) | Viscose or lyocell cellulose fibers useful for making textiles comprise a deodorizing ceramic material and a bacteriostatic organic material | |
JPH02269141A (en) | Antimicrobial molded product and production thereof | |
JP4515182B2 (en) | Cellulose sheath core fiber and method for producing the same | |
WO2001064775A1 (en) | Method for producing a cellulose solution in an aqueous amine oxide, said solution having an increased thermal stability | |
KR20090025966A (en) | Cellulose-based filament fibers, preparation method thereof and tire cords comprising the same | |
JPH11158722A (en) | Antimicrobial cellulose acetate fiber, its production and woven fabric by using antimicrobial cellulose acetate fiber |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20050830 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PT RO SE SI SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL LT LV MK |
|
DAX | Request for extension of the european patent (deleted) | ||
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PT RO SE SI SK TR |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: LI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: CH Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REF | Corresponds to: |
Ref document number: 60311324 Country of ref document: DE Date of ref document: 20070308 Kind code of ref document: P |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070417 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION Effective date: 20070418 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070428 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070618 |
|
NLV1 | Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act | ||
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PLBI | Opposition filed |
Free format text: ORIGINAL CODE: 0009260 |
|
PLAX | Notice of opposition and request to file observation + time limit sent |
Free format text: ORIGINAL CODE: EPIDOSNOBS2 |
|
26 | Opposition filed |
Opponent name: OSTTHUERINGISCHE MATERIALPRUEFGESELLSCHAFT FUER TE Effective date: 20071015 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070630 |
|
PLBB | Reply of patent proprietor to notice(s) of opposition received |
Free format text: ORIGINAL CODE: EPIDOSNOBS3 |
|
PLAY | Examination report in opposition despatched + time limit |
Free format text: ORIGINAL CODE: EPIDOSNORE2 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070418 Ref country code: FR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070907 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070625 |
|
PLBC | Reply to examination report in opposition received |
Free format text: ORIGINAL CODE: EPIDOSNORE3 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 20080627 Year of fee payment: 6 |
|
PLAB | Opposition data, opponent's data or that of the opponent's representative modified |
Free format text: ORIGINAL CODE: 0009299OPPO |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20080521 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20080521 Year of fee payment: 6 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20080521 Year of fee payment: 6 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070625 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070117 Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20070718 |
|
BERE | Be: lapsed |
Owner name: POLITECHNIKA LODZKA Effective date: 20090630 Owner name: INSTYTUT WLOKIEN NATURALNYCH Effective date: 20090630 |
|
RDAF | Communication despatched that patent is revoked |
Free format text: ORIGINAL CODE: EPIDOSNREV1 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20090625 |
|
RDAG | Patent revoked |
Free format text: ORIGINAL CODE: 0009271 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: PATENT REVOKED |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20090625 |
|
27W | Patent revoked |
Effective date: 20100210 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100101 Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20090625 Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20090630 |