Method and device for producing straight ceramic fibres

• US 20060061018A1
• Filed: 09/16/2002
• Published: 03/23/2006
• Est. Priority Date: 09/15/2001
• Status: Abandoned Application

• Current Assignee: Thueringisches Institut Fuer Textil-Und Kunsiston-Forschung E.V., Thuringisches Institut fur Textil- und Kunststoff-Forschung e.V.
• Original Assignee: Thueringisches Institut Fuer Textil-Und Kunsiston-Forschung E.V.
• Inventors: Vorbach, Dieter, Frank-Guenter, Niemez
• Application Number:
  US10/489,243
• Publication Number:
  US 20060061018A1
• Time in Patent Office: Days
• US Class Current: 264/639
• CPC Class Codes: C04B 2235/3249 containing also titanium oxide or titanates, e.g. lead zirconate titanate (PZT)
• CPC Class Codes: C04B 2235/3296 Lead oxides, plumbates or oxide forming salts thereof, e.g. silver plumbate
• CPC Class Codes: C04B 2235/3463 Alumino-silicates other than clay, e.g. mullite
• CPC Class Codes: C04B 2235/3869 Aluminium oxynitrides, e.g. AlON, sialon
• CPC Class Codes: C04B 2235/3873 Silicon nitrides, e.g. silicon carbonitride, silicon oxynitride
• CPC Class Codes: C04B 35/62245 rich in aluminium oxide
• CPC Class Codes: C04B 35/6225 Fibres based on zirconium oxide, e.g. zirconates such as PZT
• CPC Class Codes: C04B 35/62286 Fibres based on nitrides
• CPC Class Codes: C04B 35/62625 Wet mixtures
• CPC Class Codes: C04B 35/6365 Cellulose or derivatives thereof
• CPC Class Codes: C08L 1/02 Cellulose; Modified cellulose
• CPC Class Codes: D01F 1/10 Other agents for modifying properties
• CPC Class Codes: D01F 2/00 Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
• CPC Class Codes: D01F 9/08 of inorganic material working or processing of metal wire B21F; from softened glass, minerals or slags C03B37/00

Abstract

The invention relates to an installation and method for producing straight ceramic fibres. Said installation essentially comprises a mixing device for producing a suspension of ceramic powder, aqueous amine oxide and cellulose. The suspension production occurs batch-wise or continuously and can take place in one or several steps with the addition of all or individual components. Said installation also comprises a device for concentrating the produced suspension of ceramic powder, aqueous amine oxide and cellulose, whereby said device intensively mixes with heating, shears and transports the suspension with water evaporation, until a precisely determined amount of water evaporates and a suspension of ceramic powder is formed in a mouldable solution of the cellulose in aqueous amine oxide. Said concentrating device also comprises a device linked to the above mentioned device, whereby the mouldable ceramic cellulose solution suspension is processed into ceramic raw fibres in a rope shape. Said concentrating device permits straight ceramic raw fibres to be formed and can be integrated with an installation, in which the raw fibre bundles are pyrolyzed and sintered.

Claims

1. A process for producing straight ceramic fibers, comprising:

a) mixing ceramic powder, aqueous amine oxide and cellulose to form a suspension;

b) concentrating the suspension from a), which while undergoing heating is mixed, sheared and transported while undergoing evaporative removal of water until a suspension of the ceramic powder in a formable solution of cellulose in aqueous amine oxide has formed;

c) pressing the suspension obtained as per b) through a shaping tool to form continuous filament fibers, winding up the continuous filament fibers to form strands and washing off the strands;

d) drying the strands obtained as per c) under a pre-tension and with defined overall shrinkage to form straight green fibers;

e) processing the dried green fibers under their own weight or under a defined tension by pyrolyzing and sintering to form straight ceramic fibers.

2. A process according to claim 1, wherein a) utilizes a ceramic powder composed of oxides, carbides, borides, nitrides, oxynitrides, sialons and/or of aluminum silicates or their mixtures and/or of ceramic-forming low or high molecular weight compounds and/or sinterable inorganic compounds and/or lead zirconium titanates.

3. A process according to claim 1, wherein a) utilizes the cellulose in the form of dissolving or paper grade pulp or cotton linters.

4. A process according to claim 1, wherein the amine oxide used is N-methylmorpholine N-oxide.

5. A process according to claim 1, wherein the fraction of cellulose in the suspension generated in b) is 0.5% to 12% by weight based on the weight of the aqueous amine oxide.

6. A process according to claim 1, wherein the fraction of ceramic powder in b) is 10% to 5000% by weight based on the weight of the cellulose.

7. A process according to claim 1, wherein a) utilizes an ultrasound treatment as well as mixing.

8. A process according to claim 1, wherein c) produces the fibers by a wet-spinning process, a dry-jet wet-spinning process, a trough spinning process or a funnel spinning process.

9. A process according to claim 1, wherein the extrusion technique is chosen so that round and/or profiled and/or multilayered and/or hollow fibers are obtained.

10. A process according to claim 1, wherein the endless filament fibers emerging from the shaping tool are wound up to form strands of defined running length.

11. A process according to claim 1, characterized wherein the amine oxide in the fibers is washed off immediately after extrusion and optionally the continuous filament fibers are wound up to form strands of defined running length.

12. A process according to claim 1, wherein the strands are washed off under their own weight or under a pulling tension due to weights or spring forces.

13. A process according to claim 1, wherein the fiber strands are dried under tension to a defined shrinkage between 0.5 and 20%.

14. A process according to claim 1, wherein the green fiber strands obtained are immediately after drying strand pyrolyzed and sintered.

15. A process according claim 1, the green fiber strands after drying are cut to defined fiber lengths and thereafter bundle pyrolyzed and sintered.

16. A process according to claims 1, wherein the fibers are dried continuously under tension to a defined shrinkage between 0.5 and 20%.

17. A process according to claim 1, wherein the dried green fibers are cut into pieces and subsequently pyrolyzed and sintered.

18. A process according to claim 1, wherein the fiber diameter is adjusted result in to values between 10 and 2000 μ

m after the sintering operation.

19. A process according to claims 1, wherein the ceramic powder is chosen such that the ceramic fibers have piezoelectric properties.

20. Straight ceramic fibers obtainable according to a process of claim 1.

26. A process according to claim 2, wherein the amine oxide used is N-methylmorpholine N-oxide.

27. A process according to claim 3, wherein the amine oxide used is N-methylmorpholine N-oxide.

21. A device for producing straight ceramic fibers, comprising:

a) a mixing device for producing a suspension of ceramic powder, aqueous amine oxide and cellulose;

b) a device for concentrating, in which the suspension produced in a) while undergoing heating is intensively mixed, sheared and transported while undergoing evaporative removal of water until a precisely defined amount of water has evaporated off and a suspension of ceramic powder in a formable solution of cellulose in aqueous amine oxide has formed,

c) a device which is downstream to that mentioned under b) or can be connected to it and wherein the suspension of ceramic powder in a formable solution of the cellulose in aqueous amine oxide is pressed through a shaping tool to form continuous filament fibers, wound up to form strands and washed off,

d) a drying device in which the strands obtained in c) are dried under a pre-tension and with defined overall shrinkage to form straight green fibers, and

e) a pyrolysis and sintering means in which the dried green fibers are processed under their own weight or under a defined tension to form straight ceramic fibers.

22. A device according to claim 21, wherein the mixing device is a continuous assembly having two or more shafts and a mixing, transporting and shearing action.

23. A device according to claim 21, wherein the mixing device and/or the device for concentrating comprises at least one stirred vessel in batch operation.

24. A device according to claim 21, wherein the device for concentrating comprises a thin film evaporator.

25. A device according to claim 21, charaterized in that the device for concentrating comprises a thick film evaporator.