EP3536827A1 - Surface processing method for tantalum spinning head - Google Patents
Surface processing method for tantalum spinning head Download PDFInfo
- Publication number
- EP3536827A1 EP3536827A1 EP18761041.5A EP18761041A EP3536827A1 EP 3536827 A1 EP3536827 A1 EP 3536827A1 EP 18761041 A EP18761041 A EP 18761041A EP 3536827 A1 EP3536827 A1 EP 3536827A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- spinneret
- tantalum
- lithium
- film
- mixed melt
- 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.)
- Granted
Links
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 title claims abstract description 133
- 229910052715 tantalum Inorganic materials 0.000 title claims abstract description 127
- 238000009987 spinning Methods 0.000 title description 28
- 238000003672 processing method Methods 0.000 title 1
- 239000000835 fiber Substances 0.000 claims abstract description 70
- 238000000034 method Methods 0.000 claims abstract description 62
- 238000000576 coating method Methods 0.000 claims abstract description 57
- 239000011248 coating agent Substances 0.000 claims abstract description 54
- PBCFLUZVCVVTBY-UHFFFAOYSA-N tantalum pentoxide Inorganic materials O=[Ta](=O)O[Ta](=O)=O PBCFLUZVCVVTBY-UHFFFAOYSA-N 0.000 claims abstract description 40
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 36
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 36
- 150000001875 compounds Chemical class 0.000 claims abstract description 35
- 238000005498 polishing Methods 0.000 claims abstract description 31
- 238000004381 surface treatment Methods 0.000 claims abstract description 28
- 150000003839 salts Chemical class 0.000 claims abstract description 21
- 238000002848 electrochemical method Methods 0.000 claims abstract description 10
- IIPYXGDZVMZOAP-UHFFFAOYSA-N lithium nitrate Chemical group [Li+].[O-][N+]([O-])=O IIPYXGDZVMZOAP-UHFFFAOYSA-N 0.000 claims description 25
- 238000002166 wet spinning Methods 0.000 claims description 24
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 18
- 238000002048 anodisation reaction Methods 0.000 claims description 17
- 229910003002 lithium salt Inorganic materials 0.000 claims description 14
- 239000007788 liquid Substances 0.000 claims description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 9
- -1 oxygen-containing inorganic lithium salt Chemical class 0.000 claims description 8
- RHDUVDHGVHBHCL-UHFFFAOYSA-N niobium tantalum Chemical compound [Nb].[Ta] RHDUVDHGVHBHCL-UHFFFAOYSA-N 0.000 claims description 7
- 159000000002 lithium salts Chemical class 0.000 claims description 6
- 229910001257 Nb alloy Inorganic materials 0.000 claims description 5
- 239000003792 electrolyte Substances 0.000 claims description 5
- 239000008151 electrolyte solution Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 229910001362 Ta alloys Inorganic materials 0.000 claims description 4
- 150000002894 organic compounds Chemical class 0.000 claims description 3
- 239000010410 layer Substances 0.000 description 58
- 239000000243 solution Substances 0.000 description 32
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 18
- 238000005121 nitriding Methods 0.000 description 16
- 239000000126 substance Substances 0.000 description 16
- 230000007704 transition Effects 0.000 description 14
- 238000007743 anodising Methods 0.000 description 11
- 229920000297 Rayon Polymers 0.000 description 9
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 239000002585 base Substances 0.000 description 6
- JUWSSMXCCAMYGX-UHFFFAOYSA-N gold platinum Chemical compound [Pt].[Au] JUWSSMXCCAMYGX-UHFFFAOYSA-N 0.000 description 6
- 238000007380 fibre production Methods 0.000 description 5
- 229910000510 noble metal Inorganic materials 0.000 description 5
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910012463 LiTaO3 Inorganic materials 0.000 description 4
- 239000011247 coating layer Substances 0.000 description 4
- 239000003063 flame retardant Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- KEXXDMPEUZTTIS-UHFFFAOYSA-N ethane-1,2-diol;phosphoric acid Chemical compound OCCO.OP(O)(O)=O KEXXDMPEUZTTIS-UHFFFAOYSA-N 0.000 description 3
- 238000002074 melt spinning Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- SYTIQXASYKJXRY-UHFFFAOYSA-N [Au].[Rh].[Pt] Chemical compound [Au].[Rh].[Pt] SYTIQXASYKJXRY-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 239000004760 aramid Substances 0.000 description 2
- 229920003235 aromatic polyamide Polymers 0.000 description 2
- 230000000875 corresponding effect Effects 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000000578 dry spinning Methods 0.000 description 2
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 238000001891 gel spinning Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229920002972 Acrylic fiber Polymers 0.000 description 1
- 229910001020 Au alloy Inorganic materials 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910001252 Pd alloy Inorganic materials 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910001260 Pt alloy Inorganic materials 0.000 description 1
- 229910000629 Rh alloy Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 239000010407 anodic oxide Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 238000007542 hardness measurement Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 230000003746 surface roughness Effects 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 238000009489 vacuum treatment Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C28/00—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
- C23C28/04—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D only coatings of inorganic non-metallic material
- C23C28/042—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D only coatings of inorganic non-metallic material including a refractory ceramic layer, e.g. refractory metal oxides, ZrO2, rare earth oxides
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C28/00—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
- C23C28/04—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D only coatings of inorganic non-metallic material
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/26—Anodisation of refractory metals or alloys based thereon
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D9/00—Electrolytic coating other than with metals
- C25D9/04—Electrolytic coating other than with metals with inorganic materials
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D4/00—Spinnerette packs; Cleaning thereof
- D01D4/02—Spinnerettes
- D01D4/022—Processes or materials for the preparation of spinnerettes
Definitions
- the present invention relates to a surface treatment method of tantalum spinneret. More specifically, the present invention relates to a surface treatment method of tantalum spinneret for wet spinning or dry-wet spinning, and more particularly to a surface treatment method of tantalum spinneret.
- the process for producing chemical fiber is different, and the requirements for the spinneret (plate) are also different.
- chemical fiber production usually employs three processes, namely, melt spinning, dry spinning (also called dry-wet spinning), and wet spinning.
- melt spinning the spinneret used needs to withstand a pressure of up to several hundred atmospheric pressures. Therefore, the material for manufacturing the spinneret is required to have good physical and mechanical properties, and the thickness of the spinneret reaches 10 mm to 30 mm.
- wet spinning the spinneret used is subjected to much less pressure and its thickness is generally between 0.2 and 0.75 mm.
- the pressure that the spinneret needs to withstand and the thickness required for the spinneret are between those for the spinneret used for melt spinning and the spinneret used for the wet spinning. Since wet spinning is carried out in a strong acid and alkali environment, the spinneret used needs to have strong corrosion resistance. Therefore, in the early stage of chemical fiber production, in most wet spinning processes, for example, in the production process of viscose fiber, acrylic yarn, etc., the spinneret is made of a noble metal such as an alloy of gold, platinum, rhodium or palladium.
- the surface-treated tantalum spinneret can reduce the adsorption of charged waste around the micropores of the spinneret, or affect the deposition speed, and thus affect the plugging of the spinneret, thereby improving the spinnability index (such as broken filament, spinneret change rate, etc.).
- the surface treatment also has an effect on the surface roughness, and if the roughness is lowered, the spinnability is better.
- the processed tantalum spinneret has been tried to reduce the roughness of the micropore wall by the surface treatment process, thereby improving the spinnability of the spinneret, but there has been no effective method.
- the surface treatment after the spinneret processing needs to balance the surface properties, surface finish and surface hardness to obtain a suitable comprehensive and optimal effect, but the most critical aspects related to the spinnability of the spinneret are the surface properties and finish to meet the different requirements of different chemical fiber varieties.
- a nitriding only tantalum spinneret can be used for wet spinning of acrylic fibers, but for wet spinning of viscose fibers, the spinnability is poor.
- Patents ZL 85101505 , ZL 86102269 (hereinafter referred to as the first generation patent) and patent ZL 02106915.8 granted in 2006 (hereinafter referred to as the second generation patent) are widely used in the chemical fiber wet spinning in which spinnerets are prepared by replacing gold with tantalum.
- the produced tantalum spinneret coated with lithium-containing compound is similar to the noble metal gold-platinum (rhodium) alloy spinneret, and even superior to the noble metal gold-platinum (rhodium) alloy spinneret.
- the spinnability of the gold-platinum spinneret and the coated tantalum spinneret decreased, but the coated tantalum spinneret decreased more.
- spinning special fibers such as spinning matt fibers
- it is necessary to add a certain amount of titanium dioxide powder particles to the raw solution when spinning flame retardant fibers, it is necessary to add a certain amount of particulate flame retardant to the raw solution.
- the spinnability of the coated tantalum spinneret is significantly inferior to that of the gold-platinum spinneret.
- the spinneret change period of the above-mentioned coated tantalum spinneret is only 8 hours, otherwise the quality of the filament will be affected, but the gold-platinum spinneret can be spun for 16 to 24 hours. This is because the roughness of the micropore wall of the coated tantalum spinneret is larger than that of the gold-platinum spinneret. If the powdery additive is added during the spinning of the above special fiber, or if the particles appear in the raw solution since the spinning process is unstable, it is desirable that the roughness of the micropore wall of the spinneret is lower, otherwise the pores are more likely to be blocked, thereby affecting the spinnability of the spinneret.
- the present invention relates to a surface treatment method of tantalum spinneret, in particular to a surface treatment method of tantalum spinneret for wet spinning, wherein the method comprises the following steps:
- the method of the present invention further comprises a polishing step (d): subjecting the fiber outlet face of the tantalum spinneret treated in step (c) to a polishing treatment to remove the film layer containing lithium-containing compound on the surface of the fiber outlet face.
- step (a) the Ta 2 O 5 film formed on the tantalum spinneret is an amorphous Ta 2 O 5 film.
- a layer of amorphous Ta 2 O 5 film is formed on the tantalum spinneret by anodization in step (a).
- the tantalum spinneret is placed in an oxygen-containing electrolyte solution at room temperature to 380°C, preferably room temperature to 300°C, and an anode voltage of 3 to 800V is applied constantly for 0.01 to 2 hours, with a voltage-increasing current density of 1 to 200 mA/cm 2 to form a layer of amorphous Ta 2 O 5 film.
- step (a) if the solution temperature is high, the applied voltage should be low, and vice versa. For example, for a 0.01% H 3 PO 4 solution at room temperature, a voltage of up to 600V can be applied. Regardless of the solution, the applied voltage should be below the flashover voltage of the solution.
- the oxygen-containing electrolyte solution may be an aqueous solution, a non-aqueous solution, or a mixture of an aqueous electrolyte and an organic compound.
- the aqueous oxygen-containing electrolyte may be, for example, an aqueous solution of an acid, a base, or a salt.
- the solution temperature is from room temperature (about 25°C) to 95°C
- the anode voltage is 5 to 600V
- the constant voltage time is within 60 to 90 minutes.
- the temperature is too high, the water volatilizes too quickly.
- the anode voltage should be low.
- a high solution temperature, a high anode voltage, and a long constant voltage time tend to result in crystallization of the amorphous anodic oxide film, which should be prevented because the roughness is increased after crystallization or partial crystallization of the amorphous Ta 2 O 5 film.
- the non-aqueous oxygen-containing electrolyte may be anhydrous concentrated sulfuric acid or a molten salt or a mixture of a molten salt and a base, such as potassium nitrate, sodium nitrate, lithium nitrate, or a mixture thereof with a base such as lithium, sodium or potassium-containing base.
- the melting temperature should be controlled to the melting point of the molten salt to below 380°C, because tantalum will be significantly oxidized above 400°C. A voltage of 3 to 66V is applied.
- oxygen-containing electrolyte solution may be a mixture of an aqueous electrolyte and an organic compound such as ethanol, ethylene glycol, n-butanol or the like.
- the temperature of the aqueous solution should be below 95°C, otherwise the water volatilizes quickly, and it is difficult to control.
- step (c) When the coating temperature in step (c) is from 250°C to 430°C, preferably from 300°C to 400°C, more preferably from 300°C to 350°C, step (a) of forming a layer of Ta 2 O 5 film before coating on the tantalum spinneret may be omitted.
- the spinneret in step (c), is placed in an oxygen-containing inorganic lithium salt (such as LiNO 3 ) or a mixed melt of oxygen-containing inorganic lithium salt and lithium hydroxide, or a mixed melt liquid of a salt and lithium hydroxide or a mixed melt liquid of a lithium salt and an oxygen-containing salt at a temperature of 250°C to 650°C, preferably 250°C to 430°C, and an anode voltage of 1 to 66V is applied constantly for 0.01 to 200 hours, with a voltage-increasing current density of 1 to 1000 mA/cm 2 to form a film layer of lithium-containing compound.
- an oxygen-containing inorganic lithium salt such as LiNO 3
- a mixed melt liquid of a salt and lithium hydroxide or a mixed melt liquid of a lithium salt and an oxygen-containing salt at a temperature of 250°C to 650°C, preferably 250°C to 430°C
- an anode voltage of 1 to 66V is applied constantly for
- the mixed melt or the mixed melt liquid has a temperature of 300°C to 520°C, the applied anode voltage is 5 to 25V, and the voltage-increasing current density is 5 to 20 mA/cm 2 .
- an ultrasonic generator can be placed in the mixed melt or the mixed melt liquid in step (c).
- the molten salt electrochemical method in step (c) is a molten lithium salt electrochemical method.
- the surface treatment method of the present invention comprises subjecting the tantalum spinneret to a nitriding treatment prior to step (a), as in accordance with the method of step (b) of the specification of ZL02106915.8 .
- the nitriding treatment may not be performed prior to step (a). Whether or not nitriding treatment is carried out is determined according to different fiber spinning requirements.
- a fiber type having a low spinning speed and a low-pressure requirement may not be nitrided in advance, which can save costs.
- a relatively low temperature such as 400°C or lower is employed, a nitriding treatment may be employed in order to obtain a high hardness,
- the tantalum spinneret suitable for use in the present invention comprises a pure tantalum spinneret and a tantalum alloy spinneret, wherein the tantalum alloy spinneret is preferably a tantalum-niobium alloy spinneret.
- Table 1 shows that the film roughness of the coated tantalum spinneret of the present invention is nearly four times lower than those of the coated tantalum spinnerets of the prior art patents ZL 85101505 and ZL86102269 , and 1 to 2 times lower than that of the coated tantalum spinneret of the patent ZL02106915.8 .
- the film layer of the micropore wall of the spinneret has the same roughness as the film layer on the surface of the spinneret, or has a corresponding relationship.
- the roughness of the film layer of lithium-containing compound formed after subjecting the amorphous Ta 2 O 5 film which is obtained by using different anodization voltages in step (a) of the present invention to the treatment of step (c) is shown in Table 2.
- Table 2. Effect of different anodization voltages in step (a) on the roughness of film layer of lithium-containing compound Anodizing voltage 130V 240V 420V 30V (molten salt) Roughness 0.027 0.051 0.061 0.053 Note: 1.
- the voltage of the oxidation is increased, and the roughness of the film layer of lithium-containing compound after the coating is increased, so that the voltage of the anodization is not too high.
- Anodizing forms an amorphous Ta 2 O 5 film.
- the voltage for anodization in step (a) is preferably between 5 and 240V, wherein the treatment of the molten salt is to apply an anode voltage of 30V constantly for 1.5 hours at 300°C. If a higher anodization voltage such as 480V is used, the constant voltage time is shorter.
- the roughness of the obtained film layer of lithium-containing compound is affected by the solution temperature, the applied anode voltage, and the constant voltage time of step (c). That is, as the temperature rises, the anode voltage increases, and the time extension increases the roughness of the film layer of lithium-containing compound.
- Table 3 the change with voltage is shown in Table 3: Table 3. Changes of roughness of the film layer of lithium-containing compound in step (c) with anode voltage Anode voltage 10V 25V 30V Film layer roughness 0.027 0.096 0.127 Hardness (HV) 346.8 406.7 433.3 Note: 1.
- step (a) The anodization of step (a) was carried out in an aqueous solution of phosphoric acid ethylene glycol, and a voltage of 60V was applied thereto constantly for 1.0 hour. 2.
- the solution used in step (c) was pure LiNO 3 at 488°C and a constant voltage for 1.5 hours.
- step (b) of the present invention the amorphous Ta 2 O 5 film on the fiber outlet face of the spinneret is removed and the amorphous Ta 2 O 5 film on the micropore inner wall of the spinneret is retained, that is because if there is an amorphous Ta 2 O 5 film on the fiber outlet face of the spinneret and then step (c) electrochemical coating is performed, the hardness of the surface of the obtained coating is much lower than that of the surface of the coating obtained by electrochemical coating after removing the amorphous Ta 2 O 5 film by polishing, as shown in Table 4.
- step (b) is not employed before step (c), i.e., step (c) is directly performed without removing the amorphous Ta 2 O 5 film, and the surface hardness of the obtained spinneret is adjusted to be close to the surface hardness of the noble metal spinneret, for example, both around HV220, which can also be adapted to some specific spinning conditions, such as chemical fiber with low spinning speed and low spinning pressure, to simplify the operation process and reduce the cost.
- Table 4 4.
- step (c) In the case when the coating temperature in step (c) was lowered to 350°C, an anode voltage of 10V or 39V is applied, and the reaction time is 20 hours, 30 hours, or 40 hours, the roughness of the film layer of lithium-containing compound is lower, and the spinnability is better.
- the measured roughness and hardness are shown in Table 5.
- 1 indicates a fiber outlet face of a tantalum spinneret
- 2 indicates a spinneret body
- 3 indicates a Ta 2 O 5 film
- 6 indicates a film layer of lithium-containing compound
- 7 indicates a modified layer
- the modified layer is the film layer of lithium-containing compound plus a transition layer
- 8 indicates a transition layer.
- Example 1 the surface treatment method for wet spinning of the present invention is illustrated.
- the steps of Example 1 are as follows:
- Table 7 shows the results of a combined spinneret formed by a combination of 45 of single spinnerets of ⁇ 16*2600 holes*0.05.
- the conditions for forming the three coated tantalum spinnerets listed in Table 7 are shown in the notes of Table 1.
- Example 2 the surface treatment method of spinneret for wet spinning of the present invention is illustrated.
- the steps of Example 2 are as follows:
- the above-mentioned 27 anodized and coated tantalum spinneret were mounted on a base plate of a viscose short-staple stainless-steel combined spinneret, and were subjected to a viscose short-staple flame-retardant fiber spinning test in comparison with a coated tantalum spinneret which was not anodized before coating of the prior art.
- the results showed that the spinneret change period of the coated tantalum spinneret of the present invention was 16 hours, and the best second-generation coated tantalum spinneret (i.e., patent ZL2101015.8 ) in the prior art had a spinneret change period of 8 hours, therefore, the time had been doubled.
- the method is also applicable to the tantalum-niobium spinneret made of tantalum-niobium alloy which is cheaper, but the corrosion resistance and processing performance of tantalum-niobium are inferior to those of pure tantalum.
- the tantalum-niobium alloy spinneret is superior to the pure niobium spinneret, thus can be considered for some wet spinning without strong acid and alkali requirements.
- Example 3 the surface treatment method for wet spinning of the present invention is illustrated.
- the steps of Example 3 are as follows:
- Example 4 the surface treatment method for wet spinning of the present invention is illustrated.
- the steps of Example 4 are as follows:
- Example 5 the surface treatment method for wet spinning of the present invention is illustrated.
- the steps of Example 5 are as follows:
- Example 6 the surface treatment method for wet spinning of the present invention is illustrated.
- the steps of Example 6 are as follows:
- the four coated tantalum spinnerets prepared in Examples 3 to 6 were subjected to aramid III spinning test in comparison with the coated tantalum spinneret manufactured by the prior art patent ZL02106915.8 .
- the spinning cycle of the coated tantalum spinneret of the prior patent ZL02106915.8 was about 5-7 days on average, and the spinning cycle of the coated tantalum spinneret of the present invention was more than 20 days on average.
- the experimental results are shown in Table 9, and thus an unexpected technical effect was obtained. Table 9.
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Abstract
Description
- The present invention relates to a surface treatment method of tantalum spinneret. More specifically, the present invention relates to a surface treatment method of tantalum spinneret for wet spinning or dry-wet spinning, and more particularly to a surface treatment method of tantalum spinneret.
- Chemical fiber production has developed vigorously at the end of the 20th century. With the vigorous development of China's economy, China has become the world's largest producer of chemical fiber. The chemical fiber industry has become an important part of the national economy, and the spinneret (plate) is the most precise and critical component in the production of chemical fiber. The quality of the spinneret (plate) directly affects the quality of the chemical fiber production and labor productivity, cost and so on. The spinneret has been continuously improved to meet the development needs of chemical fiber production.
- The process for producing chemical fiber is different, and the requirements for the spinneret (plate) are also different. In the industry, chemical fiber production usually employs three processes, namely, melt spinning, dry spinning (also called dry-wet spinning), and wet spinning. Among them, in melt spinning, the spinneret used needs to withstand a pressure of up to several hundred atmospheric pressures. Therefore, the material for manufacturing the spinneret is required to have good physical and mechanical properties, and the thickness of the spinneret reaches 10 mm to 30 mm. In wet spinning, the spinneret used is subjected to much less pressure and its thickness is generally between 0.2 and 0.75 mm. In dry spinning, the pressure that the spinneret needs to withstand and the thickness required for the spinneret are between those for the spinneret used for melt spinning and the spinneret used for the wet spinning. Since wet spinning is carried out in a strong acid and alkali environment, the spinneret used needs to have strong corrosion resistance. Therefore, in the early stage of chemical fiber production, in most wet spinning processes, for example, in the production process of viscose fiber, acrylic yarn, etc., the spinneret is made of a noble metal such as an alloy of gold, platinum, rhodium or palladium. In the past three decades, the applicant of the present invention has developed a spinneret made of tantalum instead of gold-platinum, and such a spinneret is gradually being widely used, in which a coated tantalum spinneret made by electrochemical reaction (see Chinese patents
ZL85101505 ZL86102269 ZL02106915.8 - For the quality of the spinneret, the most critical criterion is the spinnability of the spinneret. The spinnability of the spinneret is judged based on various aspects such as the unplanned spinneret change rate of the spinneret, the spinning cycle of a single spinneret, the quality of the chemical fiber spun using the spinneret, and the broken filament ratio of the filament (broken filament ratio = the number of bobbins in which the filament grade is decreased within one working day / the total amount of bobbins producing filament), the defects, strength and uniformity of the spun yarn. Spinneret with good spinnability will result in low unplanned spinneret change rate, long spinning cycle, good quality of spun chemical fiber, low broken filament ratio, few defects, high strength and good uniformity. In the art, the broken filament ratio is detected for the filament and the defect ratio is detected for the staple fiber. These directly affect the quality of the chemical fiber produced and the labor productivity and cost in the production of chemical fiber, as well as the labor intensity of the spinning workers.
- For a spinneret in wet spinning, its spinnability depends to a large extent on the material used and the finish of the work surface. Therefore, it is desirable to improve the surface finish of the inner walls and surfaces of the micropores of the spinneret by surface treatment. In addition to affecting the surface hardness, surface treatment is important to affect the surface characteristics of the spinneret. The surface-treated tantalum spinneret can reduce the adsorption of charged waste around the micropores of the spinneret, or affect the deposition speed, and thus affect the plugging of the spinneret, thereby improving the spinnability index (such as broken filament, spinneret change rate, etc.). In addition, the surface treatment also has an effect on the surface roughness, and if the roughness is lowered, the spinnability is better. For the initially processed spinneret, it is desirable to further reduce the roughness of the micropore wall and the surface of the spinneret after micropore punching. At present, the processed tantalum spinneret has been tried to reduce the roughness of the micropore wall by the surface treatment process, thereby improving the spinnability of the spinneret, but there has been no effective method.
- At the same time, the surface treatment after the spinneret processing needs to balance the surface properties, surface finish and surface hardness to obtain a suitable comprehensive and optimal effect, but the most critical aspects related to the spinnability of the spinneret are the surface properties and finish to meet the different requirements of different chemical fiber varieties. For example, a nitriding only tantalum spinneret can be used for wet spinning of acrylic fibers, but for wet spinning of viscose fibers, the spinnability is poor.
- Patents
ZL 85101505 ZL 86102269 ZL 02106915.8 - Accordingly, there is still a need to provide a spinneret for wet spinning that further reduces the roughness of the micropore wall and surface of the spinneret while maintaining a certain strength of the spinneret.
- It is an object of the present invention to provide a surface treatment method of tantalum spinneret, and more particularly to a surface treatment method of tantalum spinneret for wet spinning to provide a spinneret having a film having significantly reduced micropore wall roughness and better surface characteristics to ensure that the surface finish of the micropores is improved for the tantalum spinneret while satisfying the required surface characteristics and surface hardness for spinning fiber, so that the obtained spinneret has excellent spinnability, improves fiber quality and economic efficiency, and reduces cost, thereby widely replaces the noble metal spinneret.
- The present invention relates to a surface treatment method of tantalum spinneret, in particular to a surface treatment method of tantalum spinneret for wet spinning, wherein the method comprises the following steps:
- (a) forming a layer of Ta2O5 film on the tantalum spinneret;
- (b) optionally polishing: polishing a fiber outlet face of the tantalum spinneret treated in step (a) to remove the Ta2O5 film on a surface of the fiber outlet face; and
- (c) coating: subjecting the tantalum spinneret treated in step (b) to a coating treatment by a molten salt electrochemical method to form a film layer containing lithium-containing compound.
- The method of the present invention further comprises a polishing step (d): subjecting the fiber outlet face of the tantalum spinneret treated in step (c) to a polishing treatment to remove the film layer containing lithium-containing compound on the surface of the fiber outlet face.
- In step (a), the Ta2O5 film formed on the tantalum spinneret is an amorphous Ta2O5 film.
- In an embodiment of the present invention, a layer of amorphous Ta2O5 film is formed on the tantalum spinneret by anodization in step (a). Specifically, in step (a), the tantalum spinneret is placed in an oxygen-containing electrolyte solution at room temperature to 380°C, preferably room temperature to 300°C, and an anode voltage of 3 to 800V is applied constantly for 0.01 to 2 hours, with a voltage-increasing current density of 1 to 200 mA/cm2 to form a layer of amorphous Ta2O5 film.
- In step (a), if the solution temperature is high, the applied voltage should be low, and vice versa. For example, for a 0.01% H3PO4 solution at room temperature, a voltage of up to 600V can be applied. Regardless of the solution, the applied voltage should be below the flashover voltage of the solution.
- In step (a), the oxygen-containing electrolyte solution may be an aqueous solution, a non-aqueous solution, or a mixture of an aqueous electrolyte and an organic compound.
- The aqueous oxygen-containing electrolyte may be, for example, an aqueous solution of an acid, a base, or a salt. The solution temperature is from room temperature (about 25°C) to 95°C, the anode voltage is 5 to 600V, and the constant voltage time is within 60 to 90 minutes. When the temperature is too high, the water volatilizes too quickly. When the solution temperature is high, the anode voltage should be low. A high solution temperature, a high anode voltage, and a long constant voltage time tend to result in crystallization of the amorphous anodic oxide film, which should be prevented because the roughness is increased after crystallization or partial crystallization of the amorphous Ta2O5 film.
- The non-aqueous oxygen-containing electrolyte may be anhydrous concentrated sulfuric acid or a molten salt or a mixture of a molten salt and a base, such as potassium nitrate, sodium nitrate, lithium nitrate, or a mixture thereof with a base such as lithium, sodium or potassium-containing base. The melting temperature should be controlled to the melting point of the molten salt to below 380°C, because tantalum will be significantly oxidized above 400°C. A voltage of 3 to 66V is applied.
- Another kind of oxygen-containing electrolyte solution may be a mixture of an aqueous electrolyte and an organic compound such as ethanol, ethylene glycol, n-butanol or the like. The temperature of the aqueous solution should be below 95°C, otherwise the water volatilizes quickly, and it is difficult to control.
- When the coating temperature in step (c) is from 250°C to 430°C, preferably from 300°C to 400°C, more preferably from 300°C to 350°C, step (a) of forming a layer of Ta2O5 film before coating on the tantalum spinneret may be omitted.
- In an embodiment of the present invention, in step (c), the spinneret is placed in an oxygen-containing inorganic lithium salt (such as LiNO3) or a mixed melt of oxygen-containing inorganic lithium salt and lithium hydroxide, or a mixed melt liquid of a salt and lithium hydroxide or a mixed melt liquid of a lithium salt and an oxygen-containing salt at a temperature of 250°C to 650°C, preferably 250°C to 430°C, and an anode voltage of 1 to 66V is applied constantly for 0.01 to 200 hours, with a voltage-increasing current density of 1 to 1000 mA/cm2 to form a film layer of lithium-containing compound.
- Preferably, in step (c), the mixed melt or the mixed melt liquid has a temperature of 300°C to 520°C, the applied anode voltage is 5 to 25V, and the voltage-increasing current density is 5 to 20 mA/cm2. In a preferred embodiment, an ultrasonic generator can be placed in the mixed melt or the mixed melt liquid in step (c).
- Preferably, the molten salt electrochemical method in step (c) is a molten lithium salt electrochemical method.
- In an embodiment of the present invention, the surface treatment method of the present invention comprises subjecting the tantalum spinneret to a nitriding treatment prior to step (a), as in accordance with the method of step (b) of the specification of
ZL02106915.8 -
- Table 1 shows that the film roughness of the coated tantalum spinneret of the present invention is nearly four times lower than those of the coated tantalum spinnerets of the prior art patents
ZL 85101505 ZL86102269 ZL02106915.8 - Although the roughness of the micropore wall of the spinneret is not technically detectable at present, due to the automatic balancing effect of the electrochemical coating, it is considered that the film layer of the micropore wall of the spinneret has the same roughness as the film layer on the surface of the spinneret, or has a corresponding relationship.
- The roughness of the film layer of lithium-containing compound formed after subjecting the amorphous Ta2O5 film which is obtained by using different anodization voltages in step (a) of the present invention to the treatment of step (c) is shown in Table 2.
Table 2. Effect of different anodization voltages in step (a) on the roughness of film layer of lithium-containing compound Anodizing voltage 130V 240V 420V 30V (molten salt) Roughness 0.027 0.051 0.061 0.053 Note: 1. For the anodizing solutions, except for that the molten salt was subjected to a constant anode voltage of 30V for 1 hour at 300°C in LiNO3 salt, the other three were all kept at a constant voltage of 90°C in an aqueous solution of phosphoric acid ethylene glycol for 1 hour. The solution volume ratio was 0.01% H3PO4 solution: ethylene glycol = 1:2.
2. The coating of step (c) in Table 2 was applied with an anode voltage of 10V constantly for 1.5 hours. - It can be seen from Table 2 that the voltage of the oxidation is increased, and the roughness of the film layer of lithium-containing compound after the coating is increased, so that the voltage of the anodization is not too high. Anodizing forms an amorphous Ta2O5 film. As the amorphous Ta2O5 film thickens, its roughness increases or its molecular aggregate volume increases, resulting in an increase in the crystal nuclei of the formed lithium-containing compound, thereby an increase in the roughness of the film layer of lithium-containing compound. The voltage for anodization in step (a) is preferably between 5 and 240V, wherein the treatment of the molten salt is to apply an anode voltage of 30V constantly for 1.5 hours at 300°C. If a higher anodization voltage such as 480V is used, the constant voltage time is shorter.
- After the amorphous Ta2O5 film is electrochemically reacted to form a film layer of lithium-containing compound, the roughness of the obtained film layer of lithium-containing compound is affected by the solution temperature, the applied anode voltage, and the constant voltage time of step (c). That is, as the temperature rises, the anode voltage increases, and the time extension increases the roughness of the film layer of lithium-containing compound. Wherein, the change with voltage is shown in Table 3:
Table 3. Changes of roughness of the film layer of lithium-containing compound in step (c) with anode voltage Anode voltage 10V 25V 30V Film layer roughness 0.027 0.096 0.127 Hardness (HV) 346.8 406.7 433.3 Note: 1. The anodization of step (a) was carried out in an aqueous solution of phosphoric acid ethylene glycol, and a voltage of 60V was applied thereto constantly for 1.0 hour.
2. The solution used in step (c) was pure LiNO3 at 488°C and a constant voltage for 1.5 hours. - In the polishing step (b) of the present invention, the amorphous Ta2O5 film on the fiber outlet face of the spinneret is removed and the amorphous Ta2O5 film on the micropore inner wall of the spinneret is retained, that is because if there is an amorphous Ta2O5 film on the fiber outlet face of the spinneret and then step (c) electrochemical coating is performed, the hardness of the surface of the obtained coating is much lower than that of the surface of the coating obtained by electrochemical coating after removing the amorphous Ta2O5 film by polishing, as shown in Table 4. Through such a polishing operation, it can maintain the low roughness of the micropore wall of the spinneret and ensure high hardness of the surface, thereby increasing the scratch resistance of the spinneret having the film layer of lithium-containing compound. If step (b) is not employed before step (c), i.e., step (c) is directly performed without removing the amorphous Ta2O5 film, and the surface hardness of the obtained spinneret is adjusted to be close to the surface hardness of the noble metal spinneret, for example, both around HV220, which can also be adapted to some specific spinning conditions, such as chemical fiber with low spinning speed and low spinning pressure, to simplify the operation process and reduce the cost.
Table 4. Effect of removing the amorphous Ta2O5 film on the fiber outlet face of the spinneret by polishing before electrochemical coating on the surface hardness (HV) Anode voltage of step (a) 130V 240V 480V Anodizing (a) + coating (c) 238 162.7 150.9 Anodizing (a) + coating (c) + polishing (d) 236.6 157 132 Anodizing (a) + polishing (b) + coating (c) + polishing (d) 376 377 395.2 Note: 1. 012 spinneret, anodized at 90°C for 1.5 hours in aqueous solution of phosphoric acid ethylene glycol.
2. The weight for hardness measurement was 100 g.
3. The coating step (c) is to apply an anode voltage of 10V at 488°C in a molten salt of LiNO3 constantly for 1.5 hours. - In the case when the coating temperature in step (c) was lowered to 350°C, an anode voltage of 10V or 39V is applied, and the reaction time is 20 hours, 30 hours, or 40 hours, the roughness of the film layer of lithium-containing compound is lower, and the spinnability is better. The measured roughness and hardness are shown in Table 5.
- As can be seen from Table 5:
- 1. For the non-nitriding tantalum spinneret (first generation), the anodizing is applied before the coating, and within the electrochemical reaction for 20 to 40 hours, the roughness of the tantalum spinneret is 2 to 3 times lower than the roughness of the tantalum spinneret to which no anodization is applied.
- 2. For the nitriding tantalum spinneret (second generation), the anodizing applied before the coating has no obvious influence on the roughness of the tantalum spinneret after coating, and even the roughness is increased.
-
-
FIG. 1 is a schematic view showing overall appearance of a tantalum spinneret of the present invention. -
FIG. 2 is a flow chart showing a surface treatment method of tantalum spinneret for wet spinning of the present invention. -
FIG. 3 is a partially enlarged cross-sectional view showing micropores of a tantalum spinneret of the present invention after forming an amorphous Ta2O5 film. -
FIG. 4 is a partially enlarged cross-sectional view showing micropores of a tantalum spinneret of the present invention after polishing the fiber outlet face. -
FIG. 5 is a cross-sectional view showing a tantalum spinneret coated with a film layer of lithium-containing compound. -
FIG. 6 is a cross-sectional view showing a tantalum spinneret coated with a film layer of lithium-containing compound after polishing the fiber outlet face. -
FIG. 7 is a schematic view of an entire tantalum spinneret. -
FIGs. 8-14 show the results of XRD comparison of samples before and after annealing under different surface treatment conditions. - In the
figure: 1 indicates a fiber outlet face of a tantalum spinneret; 2 indicates a spinneret body; 3 indicates a Ta2O5 film; 6 indicates a film layer of lithium-containing compound; 7 indicates a modified layer; and the modified layer is the film layer of lithium-containing compound plus a transition layer; 8 indicates a transition layer. - Referring to
FIG. 2 , the surface treatment method for wet spinning of the present invention is illustrated. The steps of Example 1 are as follows: -
Step 1. A tantalum metal plate was processed into 45 tantalum spinnerets. Each tantalum spinneret is shown inFIG. 1 . The tantalum spinneret comprised abody 2, the outer diameter of the spinneretfiber outlet face 1 was 16 mm, the number ofmicropores 12 was 2600, and the inner diameter of the micropores was 0.052 ± 0.001 mm. -
Step 2. At room temperature of 25°C, using 0.01% H3PO4, with an anode voltage of 150V applied constantly for 1 hour and then washed, a layer of amorphous Ta2O5 film 3 was formed on the surface of the tantalum spinneret, as shown inFIG. 4 . -
Step 3. The amorphous Ta2O5 film 3 of thefiber outlet face 1 was removed by polishing. -
Step 4. Coating: A film layer of lithium-containingcompound 6 was obtained by applying an anode voltage of 10V constantly for 1.5 hours in a molten lithium nitrate solution at 482°C. The inner diameter of the micropores after coating was 0.050 ± 0.001 mm. -
Step 5. Polishing thefiber outlet face 1 of the tantalum spinneret, the film layer of lithium-containingcompound 6 on thefiber outlet face 1 of the tantalum spinneret was ground away, leaving thetransition layer 8, as shown inFIG. 6 . The hardness of the transition layer was HV229. - The above-mentioned 45 coated tantalum spinneret having a film layer of lithium-containing compound after anodization were mounted on a base plate of a viscose short-staple stainless-steel combined spinneret, and were subjected to a viscose short-staple spinning test in comparison with a coated tantalum spinneret of the prior art (which was not anodized before coating), and the results are shown in Table 7.
- The results showed that the broken filament and fiber strand of the tantalum spinneret obtained by the method of the present invention were significantly lower than those of the prior art and the results are shown in Table 7 below:
Table 7. Comparison results of spinning with coated tantalum spinnerets after anodization according to the present invention and the prior art Broken filament Fiber strand Average value Standard deviation Average value Standard deviation First generation coated tantalum spinneret in prior art 1.89 2.4 0.56 0.58 Second generation coated tantalum spinneret in prior art 0.77 1.84 0.34 0.36 coated tantalum spinneret of the present invention 0.17 0.14 0.12 0.07 - From Table 7, it can be seen that the coated tantalum spinneret having a film layer of lithium-containing compound which is subjected to anodization and then coating treatment of the present invention can significantly reduce the fiber strand and the broken filament. Table 7 shows the results of a combined spinneret formed by a combination of 45 of single spinnerets of Ø16*2600 holes*0.05. The conditions for forming the three coated tantalum spinnerets listed in Table 7 are shown in the notes of Table 1.
- Referring to
FIG. 2 , the surface treatment method of spinneret for wet spinning of the present invention is illustrated. The steps of Example 2 are as follows: -
Step 1. A tantalum metal plate was processed into 27 tantalum spinnerets, each of which is shown inFIG. 1 . The tantalum spinneret comprised abody 2, the outer diameter of the spinneretfiber outlet face 1 was 16 mm, the number ofmicropores 12 was 1400, and the inner diameter of the micropores was 0.083 ± 0.001 mm. -
Step 2. At room temperature of 25°C, using 0.01% H3PO4, with an anode voltage of 150V applied constantly for 1 hour and then washed, a layer of amorphous Ta2O5 film 3 was formed on the surface of the tantalum spinneret. -
Step 3. The amorphous Ta2O5 film 3 of thefiber outlet face 1 was removed by polishing. -
Step 4. Coating: A film layer of lithium-containingcompound 6 was obtained by applying an anode voltage of 10V constantly for 2 hours in a molten lithium nitrate solution at 488°C. The inner diameter of the micropores after coating was 0.08 ± 0.001 mm, as shown inFIG. 5 . -
Step 5. Polishing thefiber outlet face 1 of the tantalum spinneret, the film layer of lithium-containingcompound 6 on thefiber outlet face 1 of the tantalum spinneret was ground away, leaving thetransition layer 8, as shown inFIG. 6 . The hardness of the transition layer was HV426. - The above-mentioned 27 anodized and coated tantalum spinneret were mounted on a base plate of a viscose short-staple stainless-steel combined spinneret, and were subjected to a viscose short-staple flame-retardant fiber spinning test in comparison with a coated tantalum spinneret which was not anodized before coating of the prior art. The results showed that the spinneret change period of the coated tantalum spinneret of the present invention was 16 hours, and the best second-generation coated tantalum spinneret (i.e., patent
ZL2101015.8 - The method is also applicable to the tantalum-niobium spinneret made of tantalum-niobium alloy which is cheaper, but the corrosion resistance and processing performance of tantalum-niobium are inferior to those of pure tantalum. However, the tantalum-niobium alloy spinneret is superior to the pure niobium spinneret, thus can be considered for some wet spinning without strong acid and alkali requirements.
- Referring to
FIG. 2 , the surface treatment method for wet spinning of the present invention is illustrated. The steps of Example 3 are as follows: -
Step 1. A tantalum metal plate was processed into one tantalum spinneret, as shown inFIG. 1 . The tantalum spinneret comprised abody 2, the outer diameter of the spinneretfiber outlet face 1 was 22 mm, the number of micropores was 330, and the inner diameter of the micropores was 0.082 ± 0.001 mm. -
Step 2. The tantalum spinneret obtained in step (1) was subjected to nitriding treatment, and the obtained spinneret had a hardness of HV385. -
Step 3. Using a solution having a volume ratio of ethylene glycol: 0.01% H3PO4 = 2:1 at a solution temperature of 90°C, with an anode voltage of 60V applied constantly for 1.5 hours and then washed, a layer of amorphous Ta2O5 film 3 was formed on the surface of the spinneret. -
Step 4. The amorphous Ta2O5 film 3 of the fiber outlet face was removed by polishing. -
Step 5. Coating: A film layer of lithium-containingcompound 6 was obtained by applying an anode voltage of 10V constantly for 20 hours in a molten lithium nitrate solution at 350°C. The inner diameter of the micropores after coating was 0.08 ± 0.001 mm, as shown inFIG. 5 . -
Step 6. Polishing thefiber outlet face 1 of the tantalum spinneret: the insulatingcoating layer 6 of thefiber outlet face 1 of the tantalum spinneret was ground away, leaving thetransition layer 8, as shown inFIG. 6 . The hardness of the transition layer was HV455. - Referring to
FIG. 2 , the surface treatment method for wet spinning of the present invention is illustrated. The steps of Example 4 are as follows: -
Step 1. A tantalum metal plate was processed into one tantalum spinneret, as shown inFIG. 1 . The tantalum spinneret comprised abody 2, the outer diameter of the spinneretfiber outlet face 1 was 22 mm, the number of micropores was 330, and the inner diameter of the micropores was 0.082 ± 0.001 mm. The tantalum spinneret was not subjected to nitriding treatment, and the obtained spinneret had a hardness of HV98. -
Step 2. Using a solution having a volume ratio of ethylene glycol: 0.01% H3PO4 = 2:1 at a solution temperature of 90°C, with an anode voltage of 140V applied constantly for 1.5 hours and then washed, a layer of amorphous Ta2O5 film 3 was formed on the surface of the spinneret. -
Step 3. The amorphous Ta2O5 film 3 of the fiber outlet face was removed by polishing. -
Step 4. Coating: A film layer containing lithium-containingcompound 6 was obtained by applying an anode voltage of 39V constantly for 20 hours in a molten lithium nitrate solution at 350°C. The inner diameter of the micropores after coating was 0.08 ± 0.001 mm, as shown inFIG. 5 . -
Step 5. Polishing thefiber outlet face 1 of the tantalum spinneret: the insulatingcoating layer 6 of thefiber outlet face 1 of the tantalum spinneret was ground away, leaving thetransition layer 8, as shown inFIG. 6 . The hardness of the transition layer was HV287. - Referring to
FIG. 2 , the surface treatment method for wet spinning of the present invention is illustrated. The steps of Example 5 are as follows: -
Step 1. A tantalum metal plate was processed into one tantalum spinneret, as shown inFIG. 1 . The tantalum spinneret comprised abody 2, the outer diameter of the spinneretfiber outlet face 1 was 22 mm, the number of micropores was 330, and the inner diameter of the micropores was 0.082 ± 0.001 mm. -
Step 2. The tantalum spinneret obtained in step (1) was subjected to nitriding treatment, and the obtained spinneret had a hardness of HV283. -
Step 3. Using a solution having a volume ratio of ethylene glycol: 0.01% H3PO4 = 2:1 at a solution temperature of 90°C, with an anode voltage of 140V applied constantly for 1.5 hours and then washed, a layer of amorphous Ta2O5 film 3 was formed on the surface of the spinneret. -
Step 4. The amorphous Ta2O5 film 3 of the fiber outlet face was removed by polishing. -
Step 5. Coating: A film layer containing lithium-containingcompound 6 was obtained by applying an anode voltage of 10V constantly for 12 hours in a molten lithium nitrate solution at 400°C. The inner diameter of the micropores after coating was 0.08 ± 0.001 mm, as shown inFIG. 5 . -
Step 6. Polishing thefiber outlet face 1 of the tantalum spinneret: the insulatingcoating layer 6 of thefiber outlet face 1 of the tantalum spinneret was ground away, leaving thetransition layer 8, as shown inFIG. 6 . The hardness of the transition layer was HV536. - Referring to
FIG. 2 , the surface treatment method for wet spinning of the present invention is illustrated. The steps of Example 6 are as follows: -
Step 1. A tantalum metal plate was processed into one tantalum spinneret, as shown inFIG. 1 . The tantalum spinneret comprised abody 2, the outer diameter of the spinneretfiber outlet face 1 was 22 mm, the number of micropores was 330, and the inner diameter of the micropores was 0.081 ± 0.001 mm. The tantalum spinneret was not subjected to nitriding treatment, and the obtained spinneret had a hardness of HV387. -
Step 2. Using a solution having a volume ratio of ethylene glycol: 0.01% H3PO4 = 2:1 at a solution temperature of 90°C, with an anode voltage of 140V applied constantly for 1.5 hours and then washed, a layer of amorphous Ta2O5 film 3 was formed on the surface of the spinneret. -
Step 3. The amorphous Ta2O5 film 3 of the fiber outlet face was removed by polishing. -
Step 4. Coating: A film layer containing lithium-containingcompound 6 was obtained by applying an anode voltage of 39V constantly for 6 hours in a molten lithium nitrate solution at 350°C. The inner diameter of the micropores after coating was 0.08 ± 0.001 mm, as shown inFIG. 5 . -
Step 5. Polishing thefiber outlet face 1 of the tantalum spinneret: the insulatingcoating layer 6 of thefiber outlet face 1 of the tantalum spinneret was ground away, leaving thetransition layer 8, as shown inFIG. 6 . The hardness of the transition layer was HV374. - The four coated tantalum spinnerets prepared in Examples 3 to 6 were subjected to aramid III spinning test in comparison with the coated tantalum spinneret manufactured by the prior art patent
ZL02106915.8 ZL02106915.8 Table 9. Effect of surface treatment conditions of tantalum spinneret on aramid III spinning Coating process Anodizing voltage before coating (V) Fiber mechanical properties Fineness Spinning cycle Average strength Maximum strength Minimum strength CV% average value CV% 350°C/10V/20h (first generation) 0 30.59 31.73 29.85 1.539 149.04 0.57 More than 20 days 350°C/10V/20h Example 3 (first generation) 60 31.91 33.13 30.19 2.379 146.4 0.513 350°C/39V/20h Example 4 (first generation) 140 30.66 31.35 29.46 1.631 147.05 0.52 350°C/39V/20h (second generation) 0 30.39 31.54 29.36 1.66 350°C/39V/20h Example 6 60 32.44 33.7 31.26 1.518 149.19 0.414 482°C/10V/3h (second generation) 0 31.74 32.81 30.45 1.88 147.02 0.7 482°C/10V/3h (second generation) 60 30.46 31.95 29.58 1.94 482°C/10V/3h (second generation) 140 Comparison group Second generation, i.e., nitriding + coating 31.89 32.95 30.56 2.04 146.83 0.704 5-7 days 32.31 33.81 29.37 3.241 148.19 1.303 - The spinning results of viscose filaments are shown in Table 10.
Table 10. Comparison results of anodization and non-anodization before coating at low temperature on the spinning of viscose filaments Coating oxidation process Spinning data of two months Coating process Anodizing voltage before coating (V) Fineness CV value% Blocking head rate Unplanned spinneret change rate Monofilament insufficient Broken filament rate 350°C/10V/30h (first generation) 0 0.68 0 0 0 0 350°C/10V/30h (first generation) 140 0.97 0 0 0 1.72 350°C/10V/30h (second generation) 0 0.73 0.27 0.26 0 2.59 350°C/10V/30h (second generation) 60 0.8 1.08 0 0 3.45 350°C/39V20h (second generation) 0 0.26 0 0 0 0.86 Prior art Comparison group 1.07 1.23 0.89 0.02 1.87 Note: The coating process and anodization in the table were obtained by reference to the methods of the previous examples. - The results in Table 10 show that unexpected results were obtained when no anodization was applied before coating, however, XRD analysis of the sample at a low temperature of 350°C showed no obvious LiTaO3 diffraction peak, but XRD (X-ray phase analysis) carried out after vacuum treatment at 660°C for 2 hours showed LiTaO3 diffraction peak (see
FIGs. 8-14 ), indicating that the film layer of LiTaO3 obtained by coating at a low temperature such as 350°C was an amorphous LiTaO3 film, and good results were related thereto.
* The definitions of CV values and standard deviations in the examples are as follows: - The meaning of the CV value: The CV value of a set of data, i.e., the "variation coefficient" or "discrete coefficient", is an indicator used to measure the "consistency" or "discreteness" of the set of data.
- Definition and calculation of CV value:
- µ: The average of the set of data. That is: assuming a set of data is {x 1 , x 2, ......, xi , ......, x n}, then the average of the set of data is:
- σ: The standard deviation or standard deviation of the set of data. That is: assuming a set of data is {x 1 , x 2, ......, xi , ......, x n}, then the standard deviation of the set of data is:
- µ: The average of the set of data. That is: assuming a set of data is {x 1 , x 2, ......, xi , ......, x n}, then the average of the set of data is:
Formation condition/corre sponding parameter | Oxidation solution temperature (°C) | Anodizing voltage (V) | Coating solution temperature (°C) | Coating voltage (V) | Coating constant voltage time (V) | Roughness of the finished product (µm) | Hardness of the finished product (HV) |
Example 3 | 90 | 60 | 350 | 10 | 20 | (0.030) 0.036 | (118) 229 |
Example 4 | 90 | 140 | 350 | 39 | 20 | (0.038) 0.064 | (99) 287 |
Example 5 | 90 | 140 | 400 | 10 | 12 | (0.034) 0.052 | (283) 536 |
Example 6 | 90 | 60 | 350 | 39 | 20 | (0.028) 0.074 | (387) 632 |
Note: The values of roughness and hardness in parentheses were the values before anodization and were detected using an unperforated tantalum spinneret. |
Claims (25)
- A surface treatment method of tantalum spinneret, characterized in that the method comprises the following steps:(a) forming a layer of Ta2O5 film on the tantalum spinneret;(b) optionally polishing: polishing a fiber outlet face of the tantalum spinneret treated in step (a) to remove the Ta2O5 film on a surface of the fiber outlet face; and(c) coating: subjecting the tantalum spinneret treated in step (b) to a coating treatment by a molten salt electrochemical method to form a film layer containing lithium-containing compound.
- The method according to claim 1, further comprises a polishing step (d): subjecting the fiber outlet face of the tantalum spinneret treated in step (c) to a polishing treatment to remove the film layer containing lithium-containing compound on the surface of the fiber outlet face.
- The method according to claim 1, wherein in step (a), the Ta2O5 film formed on the tantalum spinneret is an amorphous Ta2O5 film.
- The method according to claim 3, wherein a layer of amorphous Ta2O5 film is formed on the tantalum spinneret by anodization in step (a).
- The method according to claim 1, wherein in step (a), the tantalum spinneret is placed in an oxygen-containing electrolyte solution at room temperature to 380°C, preferably room temperature to 300°C, and an anode voltage of 3 to 800V is applied constantly for 0.01 to 2 hours, with a voltage-increasing current density of 1 to 200 mA/cm2 to form a layer of amorphous Ta2O5 film.
- The method according to claim 5, wherein the oxygen-containing electrolyte solution is an aqueous solution, a non-aqueous solution, or a mixture of an aqueous electrolyte and an organic compound.
- The method according to claim 1, wherein in step (c), the molten salt electrochemical method is a molten lithium salt electrochemical method.
- The method according to claim 1, wherein in step (c), the spinneret is placed in an oxygen-containing inorganic lithium salt or a mixed melt of oxygen-containing inorganic lithium salt and lithium hydroxide, or a mixed melt liquid of a salt and lithium hydroxide or a mixed melt liquid of a lithium salt and an oxygen-containing salt at a temperature of 250°C to 650°C, and an anode voltage of 1 to 66V is applied constantly for 0.01 to 200 hours, with a voltage-increasing current density of 1 to 1000 mA/cm2 to form a film layer containing lithium-containing compound.
- The method according to claim 8, wherein the mixed melt or the mixed melt liquid has a temperature of 300°C to 520°C, the applied anode voltage is 5 to 25V, and the voltage-increasing current density is 5 to 20 mA/cm2.
- The method according to claim 8, wherein the oxygen-containing inorganic lithium salt is LiNO3.
- The method according to claim 8, wherein an ultrasonic generator is disposed in the mixed melt or the mixed melt liquid in step (c).
- The method according to claim 1, wherein the tantalum spinneret is nitrided or not nitrided prior to step (a).
- The method according to claim 1, wherein the tantalum spinneret comprises a pure tantalum spinneret and a tantalum alloy spinneret, preferably a tantalum-niobium alloy spinneret.
- The method according to claim 1, wherein the method is a surface treatment method of tantalum spinneret for wet spinning.
- A surface treatment method of tantalum spinneret, wherein the method comprises the steps of:
subjecting the tantalum spinneret to a coating treatment by a molten salt electrochemical method to form a film layer containing lithium-containing compound, wherein the coating temperature is from 250°C to 430°C. - The method according to claim 15, wherein the coating temperature is from 300°C to 400°C, preferably from 300°C to 350°C.
- The method according to claim 15, wherein the molten salt electrochemical method is a molten lithium salt electrochemical method.
- The method according to claim 15, wherein in step (c), the spinneret is placed in an oxygen-containing inorganic lithium salt or a mixed melt of oxygen-containing inorganic lithium salt and lithium hydroxide, or a mixed melt liquid of a salt and lithium hydroxide or a mixed melt liquid of a lithium salt and an oxygen-containing salt at a temperature of 250°C to 430°C, and an anode voltage of 1 to 66V is applied constantly for 0.01 to 200 hours, with a voltage-increasing current density of 1 to 1000 mA/cm2 to form a film layer containing lithium-containing compound.
- The method according to claim 18, wherein the mixed melt or the mixed melt liquid has a temperature of 300°C to 350°C, the applied anode voltage is 5 to 25V, and the voltage-increasing current density is 5 to 20 mA/cm2.
- The method according to claim 18, wherein the oxygen-containing inorganic lithium salt is LiNO3.
- The method according to claim 18, wherein an ultrasonic generator is disposed in the mixed melt or the mixed melt liquid.
- The method according to claim 15, wherein the tantalum spinneret is nitrided or not nitrided before coating.
- The method according to claim 15, wherein the tantalum spinneret comprises a pure tantalum spinneret and a tantalum alloy spinneret, preferably a tantalum-niobium alloy spinneret.
- The method according to claim 15, wherein the method is a surface treatment method of tantalum spinneret for wet spinning.
- A tantalum spinneret obtained by the surface treatment of the method of any one of claims 1 to 24.
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PCT/CN2018/077938 WO2018157867A1 (en) | 2017-03-03 | 2018-03-02 | Surface processing method for tantalum spinning head |
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CN111005050A (en) * | 2020-02-19 | 2020-04-14 | 南昌航空大学 | Preparation method of double coating for improving corrosion resistance of sintered neodymium-iron-boron magnet |
CN113913953A (en) * | 2019-11-19 | 2022-01-11 | 中国石油化工股份有限公司 | Preparation method of flat acrylic fiber |
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US4678546A (en) * | 1985-03-27 | 1987-07-07 | North China Research Institute Of Electro-Optics | Process for providing lithium tantalum oxide coated tantalum articles with improved wear resistance |
CN85101505B (en) * | 1985-04-01 | 1988-03-30 | 华北光电技术研究所 | Method of making lithium tantalate film on tantalum apparatus and its products |
JPH0660436B2 (en) * | 1986-03-28 | 1994-08-10 | ユ ツオン リユ | Protective film for tantalum, niobium or its alloy articles and method for producing the same |
CN86102269B (en) * | 1986-04-09 | 1988-11-23 | 华北光电技术研究所 | Tanfalum-made spinning jet (plate) with lithium tantalate film for wet and dry and wet spinning |
CN2151155Y (en) * | 1992-11-15 | 1993-12-29 | 李士华 | Ion electrolytically coating on tantalum products |
CN1279224C (en) * | 2001-04-09 | 2006-10-11 | 北京华宇创新科贸有限责任公司 | Surface treatment method of tantalum sprayer for wet spinning |
CN1428465A (en) * | 2001-12-27 | 2003-07-09 | 北京华宇创新科贸有限责任公司 | Surface treatment method of tantalum spinneret for wet spinning |
CN100443629C (en) * | 2006-06-22 | 2008-12-17 | 上海交通大学 | Diamond thin-film reinforcement on tantalum spinning head surface by chemical gas phase deposition |
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CN113913953B (en) * | 2019-11-19 | 2022-07-01 | 中国石油化工股份有限公司 | Preparation method of flat acrylic fiber |
CN111005050A (en) * | 2020-02-19 | 2020-04-14 | 南昌航空大学 | Preparation method of double coating for improving corrosion resistance of sintered neodymium-iron-boron magnet |
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