EP3536827A1 - Surface processing method for tantalum spinning head - Google Patents

Surface processing method for tantalum spinning head Download PDF

Info

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
Application number
EP18761041.5A
Other languages
German (de)
French (fr)
Other versions
EP3536827B9 (en
EP3536827A4 (en
EP3536827B1 (en
Inventor
Yuzhong Liu
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Huayu Chuangxin Science & Trade Co Ltd
Beijing Huayu Chuangxin Ta-Nb Science & Technology Co Ltd
Original Assignee
Beijing Huayu Chuangxin Science & Trade Co Ltd
Beijing Huayu Chuangxin Ta-Nb Science & Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing Huayu Chuangxin Science & Trade Co Ltd, Beijing Huayu Chuangxin Ta-Nb Science & Technology Co Ltd filed Critical Beijing Huayu Chuangxin Science & Trade Co Ltd
Priority claimed from PCT/CN2018/077938 external-priority patent/WO2018157867A1/en
Publication of EP3536827A1 publication Critical patent/EP3536827A1/en
Publication of EP3536827A4 publication Critical patent/EP3536827A4/en
Application granted granted Critical
Publication of EP3536827B1 publication Critical patent/EP3536827B1/en
Publication of EP3536827B9 publication Critical patent/EP3536827B9/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C28/00Coating 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
    • C23C28/04Coating 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
    • C23C28/042Coating 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
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C28/00Coating 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
    • C23C28/04Coating 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
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/02Anodisation
    • C25D11/26Anodisation of refractory metals or alloys based thereon
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D9/00Electrolytic coating other than with metals
    • C25D9/04Electrolytic coating other than with metals with inorganic materials
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00Spinnerette packs; Cleaning thereof
    • D01D4/02Spinnerettes
    • D01D4/022Processes 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.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Metallurgy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Electrochemistry (AREA)
  • Ceramic Engineering (AREA)
  • Textile Engineering (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Other Surface Treatments For Metallic Materials (AREA)

Abstract

The present invention relates to a surface treatment method of tantalum spinneret, 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.

Description

    Field of the Invention
  • 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.
  • Background of the Invention
  • 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 and ZL02106915.8 for details) has good effect and wide application in place of gold-platinum spinneret in wet spinning because of its good spinnability.
  • 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 (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. When the spinning process is unstable, for example, when the spinning dope of the viscose fiber is not well filtered or the coarse particles of the raw solution are increased, the spinnability of the gold-platinum spinneret and the coated tantalum spinneret decreased, but the coated tantalum spinneret decreased more. The more prominent problem appears when 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. At this time, the spinnability of the coated tantalum spinneret is significantly inferior to that of the gold-platinum spinneret. For example, in the case of spunbonded staple fiber flame retardant fiber, 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.
  • 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.
  • Summary of The Invention
  • 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:
    1. (a) forming a layer of Ta2O5 film on the tantalum spinneret;
    2. (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
    3. (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 . That is, an ion nitriding furnace is used, with a tantalum spinneret as a cathode, a furnace temperature of 500 to 1000°C, a furnace pressure of 20 to 2000 Pa, a filled gas such as nitrogen and hydrogen with nitrogen : hydrogen = 2:1 to 1:10, and a nitriding time of 0.5 to 6 hours, thus forming a nitriding layer on the surface of the tantalum spinneret, and controlling the hardness of the tantalum spinneret after nitriding to be between HV180 and 480. However, 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. For example, a fiber type having a low spinning speed and a low-pressure requirement may not be nitrided in advance, which can save costs. However, if the electrochemical coating treatment is carried out in step (c), 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.
    Figure imgb0001
    Figure imgb0002
  • 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 .
  • 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.
    Figure imgb0003
    Figure imgb0004
    Figure imgb0005
  • As can be seen from Table 5:
    1. 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. 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.
    Brief Description of the Drawings
    • 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.
  • Detailed Description of The Invention Example 1.
  • 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 in FIG. 1. The tantalum spinneret comprised a body 2, the outer diameter of the spinneret fiber outlet face 1 was 16 mm, the number of micropores 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 in FIG. 4.
    • Step 3. The amorphous Ta2O5 film 3 of the fiber outlet face 1 was removed by polishing.
    • Step 4. Coating: A film layer of lithium-containing compound 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 the fiber outlet face 1 of the tantalum spinneret, the film layer of lithium-containing compound 6 on the fiber outlet face 1 of the tantalum spinneret was ground away, leaving the transition layer 8, as shown in FIG. 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.
  • Example 2
  • 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 in FIG. 1. The tantalum spinneret comprised a body 2, the outer diameter of the spinneret fiber outlet face 1 was 16 mm, the number of micropores 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 the fiber outlet face 1 was removed by polishing.
    • Step 4. Coating: A film layer of lithium-containing compound 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 in FIG. 5.
    • Step 5. Polishing the fiber outlet face 1 of the tantalum spinneret, the film layer of lithium-containing compound 6 on the fiber outlet face 1 of the tantalum spinneret was ground away, leaving the transition layer 8, as shown in FIG. 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 ) 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. 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.
  • Example 3
  • 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 in FIG. 1. The tantalum spinneret comprised a body 2, the outer diameter of the spinneret fiber 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-containing compound 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 in FIG. 5.
    • Step 6. Polishing the fiber outlet face 1 of the tantalum spinneret: the insulating coating layer 6 of the fiber outlet face 1 of the tantalum spinneret was ground away, leaving the transition layer 8, as shown in FIG. 6. The hardness of the transition layer was HV455.
    Example 4
  • 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 in FIG. 1. The tantalum spinneret comprised a body 2, the outer diameter of the spinneret fiber 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-containing compound 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 in FIG. 5.
    • Step 5. Polishing the fiber outlet face 1 of the tantalum spinneret: the insulating coating layer 6 of the fiber outlet face 1 of the tantalum spinneret was ground away, leaving the transition layer 8, as shown in FIG. 6. The hardness of the transition layer was HV287.
    Example 5
  • 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 in FIG. 1. The tantalum spinneret comprised a body 2, the outer diameter of the spinneret fiber 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-containing compound 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 in FIG. 5.
    • Step 6. Polishing the fiber outlet face 1 of the tantalum spinneret: the insulating coating layer 6 of the fiber outlet face 1 of the tantalum spinneret was ground away, leaving the transition layer 8, as shown in FIG. 6. The hardness of the transition layer was HV536.
    Example 6
  • 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 in FIG. 1. The tantalum spinneret comprised a body 2, the outer diameter of the spinneret fiber 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-containing compound 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 in FIG. 5.
    • Step 5. Polishing the fiber outlet face 1 of the tantalum spinneret: the insulating coating layer 6 of the fiber outlet face 1 of the tantalum spinneret was ground away, leaving the transition layer 8, as shown in FIG. 6. The hardness of the transition layer was HV374.
    Table 8. Process conditions and parameters for treating the tantalum spinneret in Examples 3-6
    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.
  • 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. 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: CV = σ μ × 100 % ,
      Figure imgb0006
      wherein:
      • 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: μ = i = 1 n x i n = x 1 + x 2 + + x n n
        Figure imgb0007
      • 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: σ = i = 1 n x i μ 2 n = x 1 μ 2 x 2 μ 2 + + x n μ 2 n
        Figure imgb0008

Claims (25)

  1. 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.
  2. 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.
  3. The method according to claim 1, wherein in step (a), the Ta2O5 film formed on the tantalum spinneret is an amorphous Ta2O5 film.
  4. The method according to claim 3, wherein a layer of amorphous Ta2O5 film is formed on the tantalum spinneret by anodization in step (a).
  5. 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.
  6. 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.
  7. The method according to claim 1, wherein in step (c), the molten salt electrochemical method is a molten lithium salt electrochemical method.
  8. 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.
  9. 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.
  10. The method according to claim 8, wherein the oxygen-containing inorganic lithium salt is LiNO3.
  11. The method according to claim 8, wherein an ultrasonic generator is disposed in the mixed melt or the mixed melt liquid in step (c).
  12. The method according to claim 1, wherein the tantalum spinneret is nitrided or not nitrided prior to step (a).
  13. 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.
  14. The method according to claim 1, wherein the method is a surface treatment method of tantalum spinneret for wet spinning.
  15. 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.
  16. The method according to claim 15, wherein the coating temperature is from 300°C to 400°C, preferably from 300°C to 350°C.
  17. The method according to claim 15, wherein the molten salt electrochemical method is a molten lithium salt electrochemical method.
  18. 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.
  19. 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.
  20. The method according to claim 18, wherein the oxygen-containing inorganic lithium salt is LiNO3.
  21. The method according to claim 18, wherein an ultrasonic generator is disposed in the mixed melt or the mixed melt liquid.
  22. The method according to claim 15, wherein the tantalum spinneret is nitrided or not nitrided before coating.
  23. 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.
  24. The method according to claim 15, wherein the method is a surface treatment method of tantalum spinneret for wet spinning.
  25. A tantalum spinneret obtained by the surface treatment of the method of any one of claims 1 to 24.
EP18761041.5A 2017-03-03 2018-03-02 Surface processing method for tantalum spinning head Active EP3536827B9 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN201710124797 2017-03-03
CN201710587999.8A CN108531906B (en) 2017-03-03 2017-07-19 Surface treatment method of tantalum spinneret
PCT/CN2018/077938 WO2018157867A1 (en) 2017-03-03 2018-03-02 Surface processing method for tantalum spinning head

Publications (4)

Publication Number Publication Date
EP3536827A1 true EP3536827A1 (en) 2019-09-11
EP3536827A4 EP3536827A4 (en) 2020-04-29
EP3536827B1 EP3536827B1 (en) 2022-01-26
EP3536827B9 EP3536827B9 (en) 2022-05-18

Family

ID=63489542

Family Applications (1)

Application Number Title Priority Date Filing Date
EP18761041.5A Active EP3536827B9 (en) 2017-03-03 2018-03-02 Surface processing method for tantalum spinning head

Country Status (4)

Country Link
EP (1) EP3536827B9 (en)
JP (1) JP6808848B2 (en)
CN (1) CN108531906B (en)
ES (1) ES2908746T3 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
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

Also Published As

Publication number Publication date
EP3536827B9 (en) 2022-05-18
CN108531906B (en) 2020-05-29
CN108531906A (en) 2018-09-14
ES2908746T9 (en) 2022-06-13
EP3536827A4 (en) 2020-04-29
ES2908746T3 (en) 2022-05-03
EP3536827B1 (en) 2022-01-26
JP2020509250A (en) 2020-03-26
JP6808848B2 (en) 2021-01-06

Similar Documents

Publication Publication Date Title
EP1409767B1 (en) Electrochemical production of peroxopyrosulphuric acid using diamond coated electrodes
EP3536827B1 (en) Surface processing method for tantalum spinning head
DE102006036084A1 (en) Electrode for electrolysis and process for its preparation
JP6930527B2 (en) High-performance PPS fiber structure and its manufacturing method and application
CN109554746B (en) Method for manufacturing high-pressure high-specific-volume corrosion foil
KR20080111243A (en) Implant having high quality surface and method for surface treatment of implant
US4678546A (en) Process for providing lithium tantalum oxide coated tantalum articles with improved wear resistance
CN1279224C (en) Surface treatment method of tantalum sprayer for wet spinning
JP4721448B2 (en) Method for producing aluminum foil for electrolytic capacitor
WO2018157867A1 (en) Surface processing method for tantalum spinning head
EP0224444A1 (en) Process for manufacturing a partially permeable membrane
Shmychkova et al. Lead dioxide electrocrystallization from nitrate and methanesulfonate electrolytes: the influence of various dopants on initial stages
CN108906974B (en) Film lubrication method in tantalum spinning jet micropore punching process
CN110085429B (en) Method for pulse deposition of nano tin dots on medium-high voltage anode aluminum foil for aluminum electrolytic capacitor
US4810584A (en) Lithium tantalum oxide coated tantalum articles with improved wear resistance and process for providing the same
KR102065215B1 (en) A method for preparing electroformed fe-ni alloy foil and a plating solution for preparing electroformed fe-ni alloy foil
CN1428465A (en) Surface treatment method of tantalum spinneret for wet spinning
CN114686960B (en) Pretreatment method for preparing medium-high pressure corrosion foil and application thereof
CH633321A5 (en) METHOD FOR PRODUCING ELECTRODES.
JPS62230997A (en) Protective film of article made of tantalum,niobium or allowthereof and its production
DE1592395C3 (en) Process for the production of manganese dioxide by electrolysis
CN108672706B (en) Preparation process of stainless steel fiber micro powder
EP3502325B1 (en) Ring for fine spinning machine
CN116607103A (en) Preparation method of high-hardness tantalum spinneret
JPH04119109A (en) Production of spinneret

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

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

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20190607

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

A4 Supplementary search report drawn up and despatched

Effective date: 20200401

RIC1 Information provided on ipc code assigned before grant

Ipc: D01D 4/02 20060101ALI20200326BHEP

Ipc: C25D 11/26 20060101AFI20200326BHEP

DAV Request for validation of the european patent (deleted)
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

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTG Intention to grant announced

Effective date: 20210812

INTG Intention to grant announced

Effective date: 20210819

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

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: AT

Ref legal event code: REF

Ref document number: 1465372

Country of ref document: AT

Kind code of ref document: T

Effective date: 20220215

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602018030106

Country of ref document: DE

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20220303

Year of fee payment: 5

REG Reference to a national code

Ref country code: CH

Ref legal event code: PK

Free format text: BERICHTIGUNG B9

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2908746

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20220503

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG9D

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20220308

Year of fee payment: 5

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20220126

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

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: 20220126

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: 20220126

Ref country code: RS

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: 20220126

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: 20220526

Ref country code: NO

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: 20220426

Ref country code: LT

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: 20220126

Ref country code: HR

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: 20220126

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20220406

Year of fee payment: 5

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PL

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: 20220126

Ref country code: LV

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: 20220126

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: 20220427

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: 20220126

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IS

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: 20220526

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602018030106

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SM

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: 20220126

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: 20220126

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: 20220126

Ref country code: MC

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: 20220126

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: 20220126

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: 20220126

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: 20220126

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AL

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: 20220126

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20220331

26N No opposition filed

Effective date: 20221027

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: 20220302

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220331

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220302

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220331

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: 20220126

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20220331

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20230302

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: 20230302

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: 20230302

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20230331

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20240226

Year of fee payment: 7

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 NON-PAYMENT OF DUE FEES

Effective date: 20230303

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20240426

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

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: 20220126

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20230303

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: 20220126

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20240227

Year of fee payment: 7

Ref country code: BG

Payment date: 20240228

Year of fee payment: 7

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

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; INVALID AB INITIO

Effective date: 20180302

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: TR

Payment date: 20240227

Year of fee payment: 7

Ref country code: IT

Payment date: 20240227

Year of fee payment: 7