JP3497285B2 - Method for producing β-alumina fiber - Google Patents
Method for producing β-alumina fiberInfo
- Publication number
- JP3497285B2 JP3497285B2 JP18057495A JP18057495A JP3497285B2 JP 3497285 B2 JP3497285 B2 JP 3497285B2 JP 18057495 A JP18057495 A JP 18057495A JP 18057495 A JP18057495 A JP 18057495A JP 3497285 B2 JP3497285 B2 JP 3497285B2
- Authority
- JP
- Japan
- Prior art keywords
- alumina
- fiber
- weight
- spinning
- alkaline earth
- 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.)
- Expired - Fee Related
Links
- 239000000835 fiber Substances 0.000 title claims description 161
- 229910000873 Beta-alumina solid electrolyte Inorganic materials 0.000 title claims description 78
- 238000004519 manufacturing process Methods 0.000 title claims description 21
- 238000009987 spinning Methods 0.000 claims description 71
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 67
- 239000002243 precursor Substances 0.000 claims description 35
- 239000000843 powder Substances 0.000 claims description 31
- 238000000034 method Methods 0.000 claims description 26
- 238000010304 firing Methods 0.000 claims description 25
- 150000001341 alkaline earth metal compounds Chemical class 0.000 claims description 22
- 150000001339 alkali metal compounds Chemical class 0.000 claims description 18
- 239000013078 crystal Substances 0.000 claims description 18
- 239000002002 slurry Substances 0.000 claims description 10
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 9
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 9
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 9
- 229910052783 alkali metal Inorganic materials 0.000 claims description 8
- 150000001340 alkali metals Chemical class 0.000 claims description 8
- 239000003125 aqueous solvent Substances 0.000 claims description 7
- 239000000243 solution Substances 0.000 claims description 7
- 150000001553 barium compounds Chemical class 0.000 claims description 3
- 229940043430 calcium compound Drugs 0.000 claims description 3
- 150000001674 calcium compounds Chemical class 0.000 claims description 3
- 150000003388 sodium compounds Chemical class 0.000 claims description 3
- 239000011550 stock solution Substances 0.000 claims description 3
- 150000003438 strontium compounds Chemical class 0.000 claims description 3
- 150000003112 potassium compounds Chemical class 0.000 claims description 2
- 239000011734 sodium Substances 0.000 description 19
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 16
- 239000000203 mixture Substances 0.000 description 14
- 239000000463 material Substances 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 10
- 230000000704 physical effect Effects 0.000 description 9
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 8
- 229910004298 SiO 2 Inorganic materials 0.000 description 8
- 239000002245 particle Substances 0.000 description 8
- 239000004317 sodium nitrate Substances 0.000 description 8
- 235000010344 sodium nitrate Nutrition 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- 239000004372 Polyvinyl alcohol Substances 0.000 description 6
- 229920002451 polyvinyl alcohol Polymers 0.000 description 6
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 6
- VXYADVIJALMOEQ-UHFFFAOYSA-K tris(lactato)aluminium Chemical compound CC(O)C(=O)O[Al](OC(=O)C(C)O)OC(=O)C(C)O VXYADVIJALMOEQ-UHFFFAOYSA-K 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 5
- 230000006866 deterioration Effects 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 239000004310 lactic acid Substances 0.000 description 5
- 235000014655 lactic acid Nutrition 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 238000006116 polymerization reaction Methods 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- BNOODXBBXFZASF-UHFFFAOYSA-N [Na].[S] Chemical compound [Na].[S] BNOODXBBXFZASF-UHFFFAOYSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000005520 cutting process Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 230000009257 reactivity Effects 0.000 description 4
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 3
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 3
- -1 aluminum compound Chemical class 0.000 description 3
- 229910001593 boehmite Inorganic materials 0.000 description 3
- 230000002542 deteriorative effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000004323 potassium nitrate Substances 0.000 description 3
- 235000010333 potassium nitrate Nutrition 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 229910001680 bayerite Inorganic materials 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 229910001648 diaspore Inorganic materials 0.000 description 2
- 229910001679 gibbsite Inorganic materials 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 description 2
- 239000012778 molding material Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000012779 reinforcing material Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- 229910052712 strontium Inorganic materials 0.000 description 2
- 238000000859 sublimation Methods 0.000 description 2
- 230000008022 sublimation Effects 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- HDYRYUINDGQKMC-UHFFFAOYSA-M acetyloxyaluminum;dihydrate Chemical compound O.O.CC(=O)O[Al] HDYRYUINDGQKMC-UHFFFAOYSA-M 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 229940009827 aluminum acetate Drugs 0.000 description 1
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- VSGNNIFQASZAOI-UHFFFAOYSA-L calcium acetate Chemical compound [Ca+2].CC([O-])=O.CC([O-])=O VSGNNIFQASZAOI-UHFFFAOYSA-L 0.000 description 1
- 239000001639 calcium acetate Substances 0.000 description 1
- 235000011092 calcium acetate Nutrition 0.000 description 1
- 229960005147 calcium acetate Drugs 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002178 crystalline material Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 150000004687 hexahydrates Chemical class 0.000 description 1
- 150000002642 lithium compounds Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 150000002681 magnesium compounds Chemical class 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000004034 viscosity adjusting agent Substances 0.000 description 1
- 239000003021 water soluble solvent Substances 0.000 description 1
Landscapes
- Inorganic Fibers (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、耐アルカリ性に優れ、
且つイオン伝導性に富むβ−アルミナ繊維及びその製造
方法に関する。The present invention is excellent in alkali resistance,
Further, the present invention relates to a β-alumina fiber rich in ion conductivity and a method for producing the same.
【0002】[0002]
【従来の技術】β−アルミナは、従来から、耐アルカリ
性構造材料として利用され、また最近では、イオン伝導
性に優れることから、ナトリウム−硫黄電池などの電池
用材料として開発が行われている。また、β−アルミナ
は、アルカリ金属酸化物及び/又はアルカリ土類金属酸
化物と、アルミナとから構成される複合酸化物である
が、その中でも、アルカリ金属成分及び/又はアルカリ
土類金属成分を5〜40モル%含有し、且つ結晶におけ
るC軸の格子定数が2.1〜3.5nmのβ−アルミナ
は、特に、イオン伝導性に優れ、電池用材料として有望
視されている。このように、β−アルミナは、各種機能
性材料として優れた性能を有しているが、このβ−アル
ミナを、成型、加工した材料として用いる場合、熱的、
機械的強度が不足するので、イオン伝導性等の特性を低
下させることなく補強できる材料として繊維状のβ−ア
ルミナの提供が強く望まれている。2. Description of the Related Art β-Alumina has been conventionally used as an alkali resistant structural material, and has recently been developed as a material for batteries such as sodium-sulfur batteries because of its excellent ionic conductivity. Further, β-alumina is a composite oxide composed of an alkali metal oxide and / or an alkaline earth metal oxide and alumina, and among them, an alkali metal component and / or an alkaline earth metal component are included. Β-alumina containing 5 to 40 mol% and having a crystallographic C-axis lattice constant of 2.1 to 3.5 nm is particularly promising as a battery material because of its excellent ionic conductivity. Thus, β-alumina has excellent performance as various functional materials, but when this β-alumina is used as a molded and processed material, thermal,
Since mechanical strength is insufficient, it is strongly desired to provide fibrous β-alumina as a material that can be reinforced without deteriorating properties such as ionic conductivity.
【0003】しかし、これまで提供されているβ−アル
ミナの形状は殆どが粉末であり、これまでβ−アルミナ
を繊維化することが極めて困難であって、その繊維状の
β−アルミナの製造方法としては、硝酸アルミニウムと
硝酸ナトリウムを主成分とした粘稠ゾルから繊維化し、
その後結晶化させる方法が、特開平3−140509に
開示されている程度に過ぎない。However, most of the β-alumina provided so far is in the form of powder, and it has been extremely difficult to form β-alumina into fibers, and the method for producing the fibrous β-alumina has been extremely difficult. As for, fibrous from a viscous sol mainly composed of aluminum nitrate and sodium nitrate,
The method of crystallization thereafter is only the level disclosed in JP-A-3-140509.
【0004】しかしながら、このようなβ−アルミナ繊
維の製造方法においても、硝酸ナトリウムようなナトリ
ウム塩を紡糸原液に多量に加えると、紡糸性を悪化させ
る上、紡糸して得られる前駆体繊維は、吸湿性が著し
く、前駆体繊維同士が融着を起し、また繊維形態の維持
が困難であるなど、最終のβ−アルミナ繊維の強度等の
物性上及び製造上に問題があった。即ち、ナトリウム成
分を5〜40モル%含有し、且つ結晶におけるC軸の格
子定数が2.1〜3.5nmのような物性を具えた従来
のβ−アルミナの製造方法においては、β−アルミナ繊
維の強度等の物性を悪化させたりして、例えば、引張強
度が60kgf/mm2 以上のβ−アルミナ繊維を得る
ことはできなかった。However, even in such a method for producing β-alumina fibers, if a large amount of sodium salt such as sodium nitrate is added to the spinning dope, the spinnability is deteriorated and the precursor fibers obtained by spinning are There is a problem in physical properties such as strength of the final β-alumina fiber and in production, such that the hygroscopicity is remarkable, the precursor fibers are fused with each other, and it is difficult to maintain the fiber form. That is, in the conventional method for producing β-alumina containing 5 to 40 mol% of sodium component and having physical properties such as a C-axis lattice constant of 2.1 to 3.5 nm in the crystal, β-alumina is used. For example, it was not possible to obtain β-alumina fibers having a tensile strength of 60 kgf / mm 2 or more, because physical properties such as the strength of the fibers were deteriorated.
【0005】また、硝酸ナトリウムの代りに硝酸カリウ
ムを用いた場合にも、このようなカリウム塩を紡糸原液
に多量に加えると、ナトリウム塩の場合と同様に、紡糸
性を悪化させる上、紡糸して得られる前駆体繊維は、吸
湿性が著しく、前駆体繊維同士が融着を起し、また繊維
形態の維持が困難であり、最終のβ−アルミナ繊維の強
度等の物性上及び製造上に問題がある。更に、硝酸ナト
リウムや硝酸カリウムの代りに又はいっしょに、カルシ
ウム化合物、ストロンチウム化合物及びバリウム化合物
などのアルカリ土類金属化合物を用いた場合には、アル
カリ金属化合物を用いた場合ほど、最終のβ−アルミナ
繊維の強度等の物性上及び製造上に問題はないが、β−
アルミナ繊維として、アルカリ土類金属成分の含有量及
び結晶におけるC軸の格子定数、並びに、繊維強度など
の物性を特定することで、β−アルミナの材料開発がな
されるようなことはなかった。そのうえ、前記のβ−ア
ルミナ繊維の製造方法においては、硝酸ナトリウム及び
硝酸アルミニウムなどの水溶性塩の水溶液をゾル化し、
そのゾル化した液体から紡糸原液を調製しているため、
この紡糸原液の調製に当っては、水溶液のゾル化処理、
ゾル化した液体の濾過処理及び濾液の濃縮処理に長時間
を要し、その生産性は極めて低いものであり、このよう
な面からも製造上問題があった。Also, when potassium nitrate is used instead of sodium nitrate, if a large amount of such a potassium salt is added to the spinning dope, the spinnability is deteriorated and spinning is performed as in the case of the sodium salt. The precursor fiber obtained has remarkable hygroscopicity, the precursor fibers are fused with each other, and it is difficult to maintain the fiber morphology, and there is a problem in physical properties such as strength of the final β-alumina fiber and in production. There is. Furthermore, when an alkaline earth metal compound such as a calcium compound, a strontium compound and a barium compound is used instead of or together with sodium nitrate and potassium nitrate, the final β-alumina fiber is as much as when the alkali metal compound is used. There is no problem in the physical properties such as the strength of and the production, but β-
As the alumina fiber, the β-alumina material was not developed by specifying the content of the alkaline earth metal component, the lattice constant of the C axis in the crystal, and the physical properties such as fiber strength. Moreover, in the method for producing the β-alumina fiber described above, an aqueous solution of a water-soluble salt such as sodium nitrate and aluminum nitrate is solized,
Since the spinning solution is prepared from the solized liquid,
In preparing the spinning dope, sol treatment of the aqueous solution,
It takes a long time to perform the filtration treatment of the sol-state liquid and the concentration treatment of the filtrate, and the productivity thereof is extremely low, which is also a problem in production.
【0006】[0006]
【発明が解決しようとする課題】本発明の目的は、前記
従来技術の問題点を解決し、アルカリ金属成分及び/又
はアルカリ土類金属成分を多量に含有するβ−アルミナ
繊維を高生産性で製造する方法を提供することにある。SUMMARY OF THE INVENTION The object of the present invention is to solve the above-mentioned problems of the prior art and to produce β-alumina fibers containing a large amount of alkali metal components and / or alkaline earth metal components with high productivity. It is to provide a manufacturing method.
【0007】[0007]
【課題を解決するための手段】本発明者らは、前記目的
を達成すべく鋭意検討の結果、紡糸原液の調製に当っ
て、アルミナ質粉末及び紡糸助剤等を特定量添加するこ
とにより、紡糸原液の紡糸性及び生産性を向上できるこ
と、並びに、高純度で高強度の種々のβ−アルミナ繊維
が得られることを見出し、本発明を完成した。Means for Solving the Problems As a result of intensive studies to achieve the above-mentioned object, the present inventors have prepared a spinning dope by adding specific amounts of an alumina powder and a spinning aid, The present invention has been completed by finding that the spinnability and productivity of the spinning dope can be improved, and that various β-alumina fibers having high purity and high strength can be obtained.
【0008】即ち、本発明は、アルカリ金属成分及び/
又はアルカリ土類金属成分を5〜40モル%含有し、結
晶におけるC軸の格子定数が2.1〜3.5nmである
β−アルミナの製造方法において、水溶性塩基性アルミ
ニウム塩、並びに、水溶性アルカリ金属化合物及び/又
は水溶性アルカリ土類金属化合物を水系溶媒中に溶解さ
せた溶液にアルミナ質粉末を添加し、更に紡糸助剤を添
加して粘度を調整して得られたスラリ−を紡糸原液と
し、この紡糸原液を紡糸して前駆体繊維とし、その前駆
体繊維を1100〜1600℃の範囲で焼成することを
特徴とするβ−アルミナ繊維の製造方法であり、また、
この好ましい態様として、アルカリ金属化合物が、ナト
リウム化合物及び/又はカリウム化合物であることを特
徴とするβ−アルミナ繊維の製造方法、並びに、アルカ
リ土類金属化合物が、カルシウム化合物、ストロンチウ
ム化合物及びバリウム化合物から選ばれる1種以上のア
ルカリ土類金属化合物であることを特徴とするβ−アル
ミナ繊維の製造方法である。That is, the present invention relates to an alkali metal component and / or
Alternatively, in the method for producing β-alumina containing an alkaline earth metal component in an amount of 5 to 40 mol% and having a C-axis lattice constant of 2.1 to 3.5 nm in the crystal, a water-soluble basic aluminum salt and a water-soluble basic aluminum salt are used. Alumina powder is added to a solution prepared by dissolving a water-soluble alkaline earth metal compound and / or a water-soluble alkaline earth metal compound in an aqueous solvent, and a spinning aid is further added to adjust the viscosity to obtain a slurry. A method for producing β-alumina fiber, characterized in that a spinning dope is spun, the spinning dope is spun into a precursor fiber, and the precursor fiber is fired in a range of 1100 to 1600 ° C.
In this preferred embodiment, the alkali metal compound is a sodium compound and / or a potassium compound, a method for producing β-alumina fiber, and an alkaline earth metal compound is a calcium compound, a strontium compound and a barium compound. A method for producing β-alumina fiber, which comprises one or more kinds of alkaline earth metal compounds selected.
【0009】本発明で使用する塩基性アルミニウム塩と
しては、塩基性乳酸アルミニウム、塩基性硝酸アルミニ
ウム、塩基性酢酸アルミニウムなどの水系溶媒に可溶で
あり、焼成後のアルミナ純度が95重量%以上で、焼成
後、SiO2 やFe2 O3 などを殆ど含まないものが好
ましい。The basic aluminum salt used in the present invention is soluble in an aqueous solvent such as basic aluminum lactate, basic aluminum nitrate and basic aluminum acetate, and has an alumina purity of 95% by weight or more after firing. After firing, it is preferable that the composition contains almost no SiO 2 , Fe 2 O 3 or the like.
【0010】アルカリ金属化合物及び/又はアルカリ土
類金属化合物としては、得られるβ−アルミナの結晶に
おけるC軸の格子定数が2.1〜3.5nmになるもの
であれば特に制限はないが、好ましい例としては、CH3C
00Na、NaNO3 、Na2CO3、NaOH、CH3C00K 、KNO3、K2C
O3 、KOH 、(CH3C00)2Mg 、Mg(NO3)2、MgCO3 、Mg(O
H)2、(CH3C00)2Ca 、Ca(NO3)2、CaCO3 、Ca(OH)2 、(CH
3C00)2Sr 、Sr(NO3)2、SrCO3 、Sr(OH)2 、(CH3C00)2Ba
、Ba(NO3)2、BaCO3 、及びBa(OH)2 などがあげられ
る。これらのアルカリ金属化合物及び/又はアルカリ土
類金属化合物は、焼成後のアルカリ金属酸化物及び/又
はアルカリ土類金属酸化物の純度が95重量%以上で、
焼成後、SiO2 やFe2 O3 などを殆ど含まないもの
が好ましい。The alkali metal compound and / or the alkaline earth metal compound is not particularly limited as long as the obtained β-alumina crystal has a C-axis lattice constant of 2.1 to 3.5 nm. As a preferable example, CH 3 C
00Na, NaNO 3 , Na 2 CO 3 , NaOH, CH 3 C 00K, KNO 3 , K 2 C
O 3 , KOH, (CH 3 C00) 2 Mg, Mg (NO 3 ) 2 , MgCO 3 , Mg (O
H) 2 , (CH 3 C00) 2 Ca, Ca (NO 3 ) 2 , CaCO 3 , Ca (OH) 2 , (CH
3 C00) 2 Sr, Sr (NO 3 ) 2 , SrCO 3 , Sr (OH) 2 , (CH 3 C00) 2 Ba
, Ba (NO 3 ) 2 , BaCO 3 , and Ba (OH) 2 . These alkali metal compounds and / or alkaline earth metal compounds have a purity of 95% by weight or more of the alkali metal oxides and / or alkaline earth metal oxides after firing,
It is preferable that the composition contains almost no SiO 2 , Fe 2 O 3 or the like after firing.
【0011】なお、溶解度の低いアルカリ金属化合物及
び/又はアルカリ土類金属化合物については、硝酸や酢
酸などを用いてpHを変化させ溶解し易くすることもで
きる。本発明の製造方法において使用する原料中のSi
O2 やFe2 O3 などの成分は、繊維強度悪化及び柔軟
性悪化並びにイオン伝導性の悪化など、β−アルミナ繊
維の物性を悪化させるので、全体として、1重量%以
下、好ましくは0.1重量%以下であることが望まし
い。焼成後のβ−アルミナ中のSiO2 及びFe2 O3
の含有量が、1重量%を超えるとβ−アルミナ繊維の強
度や柔軟性を低下させるので好ましくない。It should be noted that for alkali metal compounds and / or alkaline earth metal compounds having a low solubility, nitric acid, acetic acid or the like may be used to change the pH to facilitate dissolution. Si in the raw material used in the production method of the present invention
Components such as O 2 and Fe 2 O 3 deteriorate physical properties of the β-alumina fiber, such as deterioration of fiber strength, deterioration of flexibility, and deterioration of ionic conductivity. It is preferably 1% by weight or less. SiO 2 and Fe 2 O 3 in β-alumina after firing
Is more than 1% by weight, the strength and flexibility of the β-alumina fiber are deteriorated, which is not preferable.
【0012】また、紡糸原液の流動性及び前駆体の安定
性を向上させ且つ焼成時の揮発分を少なくし、更に繊維
強度の向上を図るために塩基性アルミニウム塩、並び
に、アルカリ金属化合物及び/又はアルカリ土類金属化
合物を水系溶媒中に溶解させた溶液に、アルミナ質粉末
を添加し、均一に混合する。なお、使用するアルミナ質
粉末の粒径は、紡糸性又はβ−アルミナ化の反応性か
ら、できるだけ小さいものが好ましく、平均粒径で1μ
m以下のものが好ましく更には0.1μm以下のものが
好ましい。添加するアルミナ質粉末としてはθ−アルミ
ナ、δ−アルミナ及びγ−アルミナなどの高純度中間ア
ルミナ並びに高純度α−アルミナの外、ギブサイト、ベ
ーマイト、バイヤライト、ダイアスポア或は擬ベーマイ
トなどの焼成により高純度アルミナとなるアルミニウム
化合物を使用することができる。Further, in order to improve the fluidity of the spinning dope and the stability of the precursor, reduce the volatile content during firing, and further improve the fiber strength, a basic aluminum salt, an alkali metal compound and / or Alternatively, the alumina powder is added to a solution in which an alkaline earth metal compound is dissolved in an aqueous solvent, and the mixture is uniformly mixed. The particle size of the alumina powder used is preferably as small as possible from the viewpoint of spinnability or β-alumination reactivity, and the average particle size is 1 μm.
It is preferably m or less, more preferably 0.1 μm or less. As the alumina powder to be added, in addition to high-purity intermediate alumina such as θ-alumina, δ-alumina and γ-alumina and high-purity α-alumina, gibbsite, boehmite, bayerite, diaspore or pseudo-boehmite can be used to increase the Aluminum compounds that provide pure alumina can be used.
【0013】ここで、「中間アルミナ」とは、前記アル
ミニウム化合物を加熱していくと、結晶水などの揮発成
分が揮散してアルミナ質に変化していき、X線回折ピ−
クがブロ−ド(非晶質)なものから、熱的に不安定な結
晶状態であるγ−アルミナ、δ−アルミナ等を経て、最
終的に結晶として最も安定型のα−アルミナになるが、
このα−アルミナになるまでの過程に存在する非晶質又
は熱的に不安定な結晶状態にあるアルミナをいう。本発
明においては、これらのアルミナ質粉末を添加し使用し
ているので、水系溶媒中に有機溶媒を添加するのが特に
効果的である。即ち、添加された有機溶媒がアルミナ質
粉末の混合分散を容易にし、アルミナ質粉末の表面及び
内部の気孔中へのアルカリ金属化合物及び/又はアルカ
リ土類金属化合物の均一な浸透を容易にし、焼成の際に
繊維の形状を保持したままアルミナ質粉末のβ−アルミ
ナ化の反応を均一に進行させることができる。なお、本
発明でいう水系溶媒とは、水、或は、水とアルコ−ル類
等の水溶性溶媒との混合溶媒を意味する。Here, the "intermediate alumina" means that when the aluminum compound is heated, volatile components such as water of crystallization are volatilized and changed to alumina, and the X-ray diffraction peak is obtained.
The crystalline form of the crystalline material is from amorphous to thermally stable γ-alumina, δ-alumina, etc., and finally becomes the most stable α-alumina as a crystal. ,
This refers to alumina in the amorphous or thermally unstable crystalline state existing in the process of becoming α-alumina. In the present invention, since these alumina powders are added and used, it is particularly effective to add the organic solvent to the aqueous solvent. That is, the added organic solvent facilitates the mixing and dispersion of the alumina powder, facilitates the uniform penetration of the alkali metal compound and / or the alkaline earth metal compound into the pores on the surface and inside the alumina powder, and calcinates In this case, the β-aluminization reaction of the alumina powder can be uniformly promoted while maintaining the fiber shape. The aqueous solvent in the present invention means water or a mixed solvent of water and a water-soluble solvent such as alcohols.
【0014】以下、本発明のβ−アルミナ繊維の製造方
法をプロセスに従って説明する。先ず、塩基性アルミニ
ウム塩と、アルカリ金属化合物及び/又はアルカリ土類
金属化合物を、水系溶媒に均一に溶解させ、この溶液
に、アルミナ質粉末を添加、混合し均一なスラリ−にす
る。アルカリ金属化合物及び/又はアルカリ土類金属化
合物の使用量は、焼成後のβ−アルミナ繊維において、
アルカリ金属成分及び/又はアルカリ土類金属成分の含
有量が5〜40モル%の範囲、好ましくは7〜20モル
%の範囲となるようにする。アルカリ金属成分及び/又
はアルカリ土類金属成分の含有量が5モル%未満では、
β−アルミナ化反応が十分進行せず、また、40モル%
を超えると、アルミン酸塩、アルカリ金属酸化物及び/
又はアルカリ土類金属酸化物などの結晶が繊維表面に多
量に析出し、良好なβ−アルミナ繊維を得ることが困難
となるので好ましくない。The method for producing the β-alumina fiber of the present invention will be described below according to the process. First, a basic aluminum salt and an alkali metal compound and / or an alkaline earth metal compound are uniformly dissolved in an aqueous solvent, and alumina powder is added to this solution and mixed to form a uniform slurry. The amount of the alkali metal compound and / or the alkaline earth metal compound used in the β-alumina fiber after firing is
The content of the alkali metal component and / or the alkaline earth metal component is in the range of 5 to 40 mol%, preferably 7 to 20 mol%. When the content of the alkali metal component and / or the alkaline earth metal component is less than 5 mol%,
The β-alumination reaction did not proceed sufficiently and was 40 mol%
If it exceeds, aluminate, alkali metal oxide and /
Alternatively, a large amount of crystals of alkaline earth metal oxides are deposited on the fiber surface, which makes it difficult to obtain a good β-alumina fiber, which is not preferable.
【0015】なお、特定の組成のβ−アルミナ繊維を高
純度で得るようにするには、スラリ−におけるアルカリ
金属成分及び/又はアルカリ土類金属成分の含有量を、
理論モル量の1〜1.1倍の範囲にすることにより達成
できる。例えば、Na2 O・11Al2 O3 の組成から
なるβ−アルミナ繊維を高純度で得るようにするには、
ナトリウム成分の含有量をNa2 O/Al2 O3 のモル
比で0.091〜0.100(モル/モル)の範囲にす
ることにより達成できる。また、スラリ−に用いたアル
カリ金属化合物及び/又はアルカリ土類金属化合物とは
別にマグネシウム化合物及び/又はリチウム化合物を更
に添加することにより、β−アルミナの1種であるβ”
−アルミナ及び/又はβ’’’−アルミナとして、β−
アルミナを安定化させることができる。In order to obtain β-alumina fiber having a specific composition with high purity, the content of alkali metal component and / or alkaline earth metal component in the slurry is
It can be achieved by adjusting the amount in the range of 1 to 1.1 times the theoretical molar amount. For example, to obtain β-alumina fiber having a composition of Na 2 O · 11Al 2 O 3 with high purity,
This can be achieved by setting the content of the sodium component in the range of 0.091 to 0.100 (mol / mol) in terms of the molar ratio of Na 2 O / Al 2 O 3 . Further, by adding a magnesium compound and / or a lithium compound in addition to the alkali metal compound and / or the alkaline earth metal compound used in the slurry, β ″ which is one kind of β-alumina.
-Alumina and / or β '''-as alumina, β-
Alumina can be stabilized.
【0016】前記溶液に添加するアルミナ質粉末として
はθ−アルミナ、δ−アルミナ及びγ−アルミナなどの
高純度中間アルミナ並びに高純度α−アルミナの外、ギ
ブサイト、ベーマイト、バイヤライト、ダイアスポア或
は擬ベーマイトなどの焼成により高純度アルミナとなる
アルミニウム化合物を使用することができるが、中でも
γ−アルミナなどの高純度中間アルミナが好適である。
これらのアルミナ質粉末の粒径は、紡糸性又はβ−アル
ミナ化の反応性から、できるだけ小さいものが好まし
く、平均粒径で1μm以下のものが好ましく更には0.
1μm以下のものが好ましい。アルミナ質粉末の添加量
は、全アルミナ成分量の10〜60重量%が好ましく、
更に好ましくは、20〜40重量%が望ましい。As the alumina powder to be added to the above solution, besides high-purity intermediate alumina such as θ-alumina, δ-alumina and γ-alumina and high-purity α-alumina, gibbsite, boehmite, bayerite, diaspore or pseudo-alumina. Although an aluminum compound which becomes high-purity alumina by firing such as boehmite can be used, high-purity intermediate alumina such as γ-alumina is preferable.
The particle size of these aluminous powders is preferably as small as possible from the viewpoint of spinnability or β-alumination reactivity, and the average particle size is preferably 1 μm or less, more preferably 0.
It is preferably 1 μm or less. The amount of the alumina powder added is preferably 10 to 60% by weight of the total amount of the alumina component,
More preferably, 20 to 40% by weight is desirable.
【0017】前記溶液にアルミナ質粉末を添加しない場
合、即ちアルミナ源としては塩基性アルミニウム塩しか
用いない場合は、紡糸工程において、吸湿性が著しいた
め繊維形態を維持し難く歩留りが低下すると共に、後工
程の焼成時において、繊維内部からの揮発ガスが繊維表
面を通過する際に、0.1〜0.5μmの大きなポアが
繊維表面にまばらで不均一に生成され易く、また揮発性
成分が多いことから、焼成時の収縮が大きいため糸切れ
が多くなると共に、得られるβ−アルミナ繊維の強度も
低くなりがちであり目的とする繊維はなかなか得られな
かった。粉末の添加量が10重量%未満では、前記の無
添加の場合と同様に、紡糸工程での吸湿及び焼成工程で
の収縮による繊維形態維持の困難性のため、更に、得ら
れるβ−アルミナ繊維の強度も低いので好ましくなく、
一方、粉末の添加量が60重量%を超える場合には、紡
糸時に糸切れを起し易く、更に得られるβ−アルミナ繊
維表面の凹凸が大きくなり、繊維強度の低下など品質の
低下をもたらすので好ましくない。When no alumina powder is added to the solution, that is, when only a basic aluminum salt is used as an alumina source, it is difficult to maintain the fiber morphology in the spinning step because the hygroscopicity is remarkable, and the yield decreases. When the volatile gas from the inside of the fiber passes through the surface of the fiber during the firing in the subsequent step, large pores of 0.1 to 0.5 μm are sparsely and unevenly generated on the surface of the fiber, and the volatile component is Since the amount of the β-alumina fiber is large, the number of yarn breakages increases due to the large shrinkage during firing, and the strength of the obtained β-alumina fiber tends to be low, so that the target fiber is difficult to obtain. If the amount of the powder added is less than 10% by weight, it is difficult to maintain the fiber morphology due to moisture absorption in the spinning step and shrinkage in the firing step, as in the case of the above-mentioned non-addition. Is not preferable because the strength of
On the other hand, when the amount of the powder added exceeds 60% by weight, yarn breakage is likely to occur during spinning, and the resulting β-alumina fiber surface has large irregularities, resulting in deterioration in fiber strength and other deterioration in quality. Not preferable.
【0018】このようにして得られたスラリ−に、酸化
物基準で1〜10重量%相当のアルミナゾル、0.1〜
10重量%相当の紡糸助剤を添加して紡糸原液を調製す
る。前記スラリ−に添加して繊維強度を更に向上させる
ためのアルミナゾルの量は、酸化物基準で1〜10重量
%相当とするのが好ましい。このアルミナゾルは、塩基
性アルミニウム塩中の揮発性成分の急激な揮散による粉
化を抑制し、生成されるβ−アルミナ結晶に対してバイ
ンダ−的効果を発揮するので、得られるβ−アルミナ繊
維は、その繊維強度が極めて高い。アルミナゾルの添加
量が1重量%未満では、このバインダ−的効果が顕著に
現れず、一方、10重量%を超えても特に効果の増大は
なく、その分、揮発性成分の量が多くなるで好ましくな
い。To the slurry thus obtained, 1 to 10% by weight of alumina sol, based on oxide, of 0.1 to
A spinning dope is prepared by adding 10% by weight of a spinning aid. The amount of alumina sol added to the slurry to further improve the fiber strength is preferably 1 to 10% by weight based on the oxide. This alumina sol suppresses pulverization due to abrupt volatilization of volatile components in the basic aluminum salt, and exerts a binder effect on the β-alumina crystals produced, so that the β-alumina fiber obtained is , Its fiber strength is extremely high. When the amount of alumina sol added is less than 1% by weight, this binder effect does not remarkably appear. On the other hand, when it exceeds 10% by weight, there is no particular increase in the effect, and the amount of volatile components increases correspondingly. Not preferable.
【0019】前記紡糸原液の曳糸性を向上させるための
紡糸助剤ついては、エチレングリコ−ル、グリセリン、
酢酸等の有機化合物、又は、ポリビニルアルコール、ポ
リエチレンオキシド、ポリプロピレンオキシド等の水溶
性有機高分子化合物、或は、これらの混合物を酸化物基
準で0.1〜10重量%添加するのが好ましい。Regarding the spinning aid for improving the spinnability of the above spinning dope, ethylene glycol, glycerin,
It is preferable to add an organic compound such as acetic acid, a water-soluble organic polymer compound such as polyvinyl alcohol, polyethylene oxide, polypropylene oxide, or a mixture thereof in an amount of 0.1 to 10% by weight based on the oxide.
【0020】このようにして得られた紡糸原液は、遠心
法、吹飛し法或は押出法などの紡糸方法のいずれかの方
法で紡糸を行ってもよいが、その紡糸装置の能力に応
じ、前記紡糸助剤など粘度調整剤としても作用する添加
物の種類及びその添加量、並びに、紡糸原液の水分量及
び粘度などは、適宜決めてもよいものである。紡糸原液
の水分量及び粘度の通常の条件については、水分量は2
0〜45重量%、25℃での粘度は300〜4000ポ
アズであるが、紡糸装置の能力により、それらの条件は
変化するものであり、これらの範囲に限定されるもので
はない。本発明の方法における紡糸原液の調製に当って
は、水溶液のゾル化処理、ゾル化した液体の濾過処理及
び濾液の濃縮処理など長時間を要する処理操作を必要と
はしないか、その処理操作を行ったとしても短時間で済
むので、紡糸原液の生産性は極めて高いものである。The spinning dope thus obtained may be spun by any spinning method such as a centrifugal method, a blow-off method, or an extrusion method, depending on the capability of the spinning apparatus. The kind and amount of additives that also act as a viscosity modifier such as the spinning aid, and the water content and viscosity of the spinning dope may be appropriately determined. For normal conditions of water content and viscosity of spinning dope, the water content is 2
The viscosity is 0 to 45% by weight and the viscosity at 25 ° C. is 300 to 4000 poise, but those conditions are changed depending on the capability of the spinning device and are not limited to these ranges. In the preparation of the spinning dope in the method of the present invention, it is not necessary to perform a treatment operation that requires a long time, such as a sol treatment of an aqueous solution, a filtration treatment of the solized liquid, and a concentration treatment of the filtrate, or the treatment operation is performed. Even if it is carried out, it takes only a short time, and therefore the productivity of the spinning dope is extremely high.
【0021】このように紡糸して得られた前駆体繊維に
ついて、その繊維径は2〜25μmとするのが好まし
い。細い繊維径の繊維を得るためには、低粘度の紡糸原
液を遠心法或は吹飛し法で紡糸する方法が主に採られる
が、繊維径2μm未満の前駆体繊維を安定的に製造する
のは困難であり実用的ではないので、繊維径を2μm未
満にするのは好ましくない。一方、太い繊維径の繊維を
得るためには、高粘度の紡糸原液を押出法で紡糸する方
法が主に採られ、本発明の方法により繊維径が25μm
を超える前駆体繊維を得、次いでβ−アルミナ繊維を製
造することはできるが、長時間の焼成が必要となり製造
上効率が悪化する上、得られたβ−アルミナ繊維は繊維
形態は維持しているものの、硬く脆くなり、柔軟性に欠
けるため、繊維としての機能に欠けるので、前駆体繊維
を25μmを超える繊維径にするのは好ましくない。ま
た、押出法で紡糸する方法においては、0.1〜0.5
mmφの孔を100個以上有する紡糸ノズルを用いるこ
とにより、更に生産性を向上させることができる。The fiber diameter of the precursor fiber thus obtained by spinning is preferably 2 to 25 μm. In order to obtain fibers having a small fiber diameter, a method of spinning a low-viscosity spinning dope by a centrifugal method or a blow-off method is mainly adopted, but a precursor fiber having a fiber diameter of less than 2 μm is stably produced. Since it is difficult and not practical, it is not preferable to make the fiber diameter less than 2 μm. On the other hand, in order to obtain a fiber having a large fiber diameter, a method of spinning a high-viscosity spinning dope by an extrusion method is mainly adopted, and a fiber diameter of 25 μm is obtained by the method of the present invention.
Although it is possible to obtain a precursor fiber exceeding the above and then to produce β-alumina fiber, long-term firing is required and the production efficiency deteriorates, and the obtained β-alumina fiber maintains the fiber morphology. However, since it becomes hard and brittle and lacks flexibility, it lacks the function as a fiber. Therefore, it is not preferable to use a precursor fiber having a fiber diameter of more than 25 μm. Further, in the method of spinning by the extrusion method, 0.1 to 0.5
By using a spinning nozzle having 100 or more mmφ holes, the productivity can be further improved.
【0022】このように紡糸して得られた前駆体繊維
は、1100〜1600℃の温度範囲で加熱し、焼成す
ることによって、アルミナ成分と、アルカリ金属化合物
及び/又はアルカリ土類金属化合物とを反応させβ−ア
ルミナ繊維とする。この前駆体繊維の焼成操作は、前駆
体繊維を適当な長さに切断した後に行ってもよいが、紡
糸された前駆体繊維を連続的に焼成炉中を通過させる方
法が効率的である。長繊維の形で前駆体繊維をそのま
ま、或は適当な長さに切断したのち焼成することによ
り、長繊維状、或は長さの揃った短繊維状のβ−アルミ
ナ繊維を得ることができる。The precursor fiber thus obtained by spinning is heated in a temperature range of 1100 to 1600 ° C. and calcined to obtain an alumina component and an alkali metal compound and / or an alkaline earth metal compound. React to give β-alumina fibers. The firing operation of this precursor fiber may be performed after cutting the precursor fiber into an appropriate length, but a method of continuously passing the spun precursor fiber through a firing furnace is efficient. Precursor fibers in the form of long fibers can be obtained as they are, or by cutting them to an appropriate length and then firing them, β-alumina fibers in the form of long fibers or short fibers of uniform length can be obtained. .
【0023】焼成温度については、1100℃未満で
は、β−アルミナ化反応が進まないか又は非常に遅く、
一方、1600℃を超えると、一旦生成したβ−アルミ
ナの再分解が起こるので好ましくない。Regarding the calcination temperature, if it is less than 1100 ° C., the β-alumination reaction does not proceed or is very slow,
On the other hand, if the temperature exceeds 1600 ° C., the β-alumina that has been once generated is redissolved, which is not preferable.
【0024】また、アルカリ金属化合物及び/又はアル
カリ土類金属化合物としてナトリウム化合物を用い、焼
成温度を1275℃以上で行う場合は、β−アルミナ化
反応が十分進まないうちに、Na2 Oの昇華が起こり易
いので、Na2 Oの昇華を防止するため密閉した匣内で
焼成することが好ましい。焼成時間は、前駆体繊維の性
状、使用するアルカリ金属化合物及び/又はアルカリ土
類金属化合物の種類や混合状態、目的とするβ−アルミ
ナ繊維中の結晶粒径等により適宜定めればよいが、最長
で24時間程度とする。When a sodium compound is used as the alkali metal compound and / or the alkaline earth metal compound and the firing temperature is 1275 ° C. or higher, the sublimation of Na 2 O occurs before the β-alumination reaction proceeds sufficiently. Therefore, it is preferable to bake in a closed box to prevent sublimation of Na 2 O. The firing time may be appropriately determined according to the properties of the precursor fiber, the type and mixed state of the alkali metal compound and / or alkaline earth metal compound used, the crystal grain size in the desired β-alumina fiber, and the like. The maximum time is about 24 hours.
【0025】本発明の方法では、紡糸原液にアルミナ質
粉末、紡糸助剤などを使用しているので、アルカリ金属
化合物及び/又はアルカリ土類金属化合物を多量含有す
るにも拘らず、紡糸性が良好で、また、アルミナ粉末の
表面及び内部気孔中へのアルカリ金属化合物及び/又は
アルカリ土類金属化合物の浸透性も良く、得られる前駆
体繊維はβ−アルミナ化の反応性も高いので、繊維の長
さの長い高強度のβ−アルミナ繊維を容易に製造するこ
とができる。アルミナ質粉末、紡糸助剤など本発明の方
法で用いられる繊維原料は、焼成後特にSiO2 やFe
2 O3 などの不純物を殆ど含まない高純度の繊維原料を
使用することができ、得られるβ−アルミナ繊維は、高
純度だけではなく、更に高強度で柔軟性のある繊維にな
る。In the method of the present invention, since the alumina powder and the spinning aid are used in the spinning dope, the spinnability is improved in spite of containing a large amount of the alkali metal compound and / or the alkaline earth metal compound. Good, and also good permeability of the alkali metal compound and / or alkaline earth metal compound into the surface and internal pores of the alumina powder, and the precursor fiber obtained has a high reactivity of β-alumination, A high-strength β-alumina fiber having a long length can be easily manufactured. The fiber raw materials used in the method of the present invention such as the alumina powder and the spinning aid are, especially, SiO 2 and Fe after firing.
A high-purity fiber raw material containing almost no impurities such as 2 O 3 can be used, and the obtained β-alumina fiber has not only high purity but also higher strength and flexibility.
【0026】本発明の方法では、前駆体繊維を5〜10
0mm程度の長さに切断し、焼成する方法で製造すれ
ば、主として3〜60mm程度のβ−アルミナ繊維が得
られる。また、前駆体繊維を長繊維のままで焼成すれば
長繊維の形のβ−アルミナ繊維を得ることができ、また
これを適当な長さに切断して長さの揃った繊維として使
用することができる。このβ−アルミナ繊維は、耐アル
カリ性構造材料、及び、ナトリウム−硫黄電池などの電
池用材料の補強材として優れた性能を有しており、β−
アルミナ粉末と混合し、成型、加工することにより、取
扱性が良好で、イオン伝導性等の物性を低下させること
なく、熱的、機械的衝撃による亀裂が生じ難い、強度の
高い成型材料を得ることができる。In the method of the present invention, the precursor fiber is added to 5 to 10
If it is manufactured by a method of cutting it to a length of about 0 mm and firing it, β-alumina fibers of about 3 to 60 mm are mainly obtained. Further, if the precursor fiber is fired as a long fiber as it is, β-alumina fiber in the form of a long fiber can be obtained, and this can be cut into an appropriate length and used as a fiber having a uniform length. You can This β-alumina fiber has excellent performance as an alkali-resistant structural material and a reinforcing material for battery materials such as sodium-sulfur batteries.
By mixing with alumina powder, molding and processing, it is possible to obtain a molding material that has good handleability, does not deteriorate physical properties such as ionic conductivity, does not easily crack due to thermal or mechanical impact, and has high strength. be able to.
【0027】[0027]
【実施例】以下実施例により本発明の方法を更に具体的
に説明する。EXAMPLES The method of the present invention will be described in more detail with reference to the following examples.
【0028】(実施例1)乳酸2.0重量部、塩基性乳
酸アルミニウム100.0重量部(Al2 O3 としての
含有率37.0重量%)及び硝酸ナトリウム9.6重量
部とを、水200重量部に溶解させたのち、平均粒径
0.02μmのγ−アルミナ微粉末24.5重量部を添
加し、30分間撹拌混合〔Na2 O/(Na2 O+Al
2 O3 )のモル比で8.6モル%〕した。このスラリー
にポリビニルアルコ−ル(平均重合度約3000)5.
0重量部を添加し十分混合し、この混合液を減圧下に8
時間濃縮して25℃での粘度が2500ポアズの紡糸原
液とした。この紡糸原液を、0.3mmφの孔を100
0個有する紡糸ノズルから乾燥用の紡糸筒内へ押出して
紡糸し、1000本のフィラメントからなる繊維径13
μmの前駆体繊維を得た。この前駆体繊維を、温度10
0℃から最高1400℃の温度勾配を持たせた焼成炉中
を滞留時間7分で連続的に通過させて焼成し、繊維径約
10μmのフィラメント1000本からなる長繊維の形
のβ−アルミナ繊維を得た。このβ−アルミナ繊維は、
柔軟性があり、引張強度105kgf/mm2 の連続長
繊維であった。また、X線回折装置による同定及び分析
の結果、純度約96重量%のNa2O・11Al2 O3
(結晶におけるC軸の格子定数:2.261nm)、並
びに、少量のNa2 O・7Al2 O3 (結晶におけるC
軸の格子定数:2.270nm)及びNa2 O・5Al
2 O3 (結晶におけるC軸の格子定数:3.395n
m)からなるβ−アルミナ繊維であった。なお、このβ
−アルミナ繊維のSiO2 含有量及びFe2 O3 含有量
を高周波プラズマ発光分析装置(ICP)により分析し
た結果、それぞれ、0.05重量%及び0.06重量%
と非常に少ない量で あった。(Example 1) 2.0 parts by weight of lactic acid, 100.0 parts by weight of basic aluminum lactate (content ratio as Al 2 O 3 of 37.0% by weight) and 9.6 parts by weight of sodium nitrate, After being dissolved in 200 parts by weight of water, 24.5 parts by weight of γ-alumina fine powder having an average particle size of 0.02 μm was added, followed by stirring and mixing for 30 minutes [Na 2 O / (Na 2 O + Al
2 O 3 ) in a molar ratio of 8.6 mol%]. Polyvinyl alcohol (average degree of polymerization: about 3000) was added to this slurry.
Add 0 parts by weight and mix well, and mix this mixture under reduced pressure for 8 hours.
It was concentrated for a period of time to obtain a spinning dope having a viscosity of 2500 poise at 25 ° C. This spinning dope is made into 100 mm holes with a diameter of 0.3 mm.
A fiber having a filament diameter of 1000 filaments is extruded from 0 spinning nozzles into a spinning cylinder for drying, and has a fiber diameter of 1000 filaments.
A precursor fiber of μm was obtained. This precursor fiber is heated at a temperature of 10
Β-alumina fiber in the form of a long fiber consisting of 1000 filaments having a fiber diameter of about 10 μm, which are continuously passed through a firing furnace having a temperature gradient from 0 ° C. to a maximum of 1400 ° C. with a residence time of 7 minutes and fired. Got This β-alumina fiber is
It was a continuous filament having flexibility and a tensile strength of 105 kgf / mm 2 . In addition, as a result of identification and analysis by an X-ray diffractometer, a purity of about 96% by weight of Na 2 O.11Al 2 O 3 was obtained.
(C-axis lattice constant in the crystal: 2.261 nm) and a small amount of Na 2 O · 7Al 2 O 3 (C in the crystal
Axial lattice constant: 2.270 nm) and Na 2 O · 5Al
2 O 3 (C-axis lattice constant in crystal: 3.395 n
m) was a β-alumina fiber. Note that this β
- Results of the SiO 2 content and Fe 2 O 3 content of the alumina fibers was analyzed by high-frequency plasma emission spectrometer (ICP), respectively, 0.05 wt% and 0.06 wt%
And it was a very small amount.
【0029】(実施例2)乳酸2.7重量部、塩基性乳
酸アルミニウム132.0重量部(Al2 O3 としての
含有率37.0重量%)、硝酸ナトリウム33.8重量
部及び硝酸マグネシウム6水塩51重量部を、水300
重量部に溶解させたのち、平均粒径0.02μmのγ−
アルミナ微粉末48.8重量部を添加し、30分間撹拌
混合〔(Na2 O+MgO)/(Na2 O+MgO+A
l2 O3 )のモル比で29モル%〕した。このスラリー
にポリビニルアルコ−ル(平均重合度約3000)6.
0重量部を添加し十分混合し、この混合液を減圧下に9
時間濃縮して25℃での粘度が2500ポアズの紡糸原
液とした。この紡糸原液を、0.3mmφの孔を100
0個有する紡糸ノズルから乾燥用の紡糸筒内へ押出して
紡糸し、1000本のフィラメントからなる繊維径13
μmの前駆体繊維を得た。この前駆体繊維を、約100
mmの長さに切断し、高純度アルミナ製の匣に入れ、毎
時100℃の昇温速度で1300℃まで昇温し、同温度
で1時間保持して焼成し、繊維径約10μm、繊維長約
60mmのβ−アルミナ繊維を得た。このβ−アルミナ
繊維は、柔軟性があり、引張強度85kgf/mm2 の
繊維であった。また、X線回折装置による同定及び分析
の結果、純度約95重量%のNa2 O・MgO・5Al
2O3 (結晶におけるC軸の格子定数:3.348n
m)のβ−アルミナ繊維であった。なお、この繊維のS
iO2 含有量及びFe2 O3 含有量は、それぞれ、0.
05重量%及び0.07重量%と非常に少ない量であっ
た。(Example 2) 2.7 parts by weight of lactic acid, 132.0 parts by weight of basic aluminum lactate (content ratio as Al 2 O 3 is 37.0% by weight), 33.8 parts by weight of sodium nitrate and magnesium nitrate. 51 parts by weight of hexahydrate, 300 parts of water
After being dissolved in parts by weight, γ-having an average particle size of 0.02 μm
48.8 parts by weight of alumina fine powder was added, and the mixture was stirred and mixed for 30 minutes [(Na 2 O + MgO) / (Na 2 O + MgO + A
The molar ratio of 1 2 O 3 ) was 29 mol%]. Polyvinyl alcohol (average degree of polymerization: about 3000) 6.
0 parts by weight was added and mixed well, and the mixture was mixed under reduced pressure to
It was concentrated for a period of time to obtain a spinning dope having a viscosity of 2500 poise at 25 ° C. This spinning dope is made into 100 mm holes with a diameter of 0.3 mm.
A fiber having a filament diameter of 1000 filaments is extruded from 0 spinning nozzles into a spinning cylinder for drying, and has a fiber diameter of 1000 filaments.
A precursor fiber of μm was obtained. About 100 of this precursor fiber
Cut into a length of mm, put in a box made of high-purity alumina, heat up to 1300 ° C. at a heating rate of 100 ° C./hour, hold at the same temperature for 1 hour and bake, fiber diameter about 10 μm, fiber length About 60 mm of β-alumina fiber was obtained. This β-alumina fiber was flexible and had a tensile strength of 85 kgf / mm 2 . In addition, as a result of identification and analysis by an X-ray diffractometer, Na 2 O.MgO.5Al with a purity of about 95% by weight was obtained.
2 O 3 (C-axis lattice constant in crystal: 3.348 n
It was the β-alumina fiber of m). In addition, S of this fiber
The iO 2 content and the Fe 2 O 3 content are respectively 0.
It was a very small amount of 05% by weight and 0.07% by weight.
【0030】(実施例3)乳酸2.0重量部、塩基性乳
酸アルミニウム100.0重量部(Al2 O3 としての
含有率37.0重量%)及び硝酸カリウム25.6重量
部とを、水200重量部に溶解させたのち、平均粒径
0.02μmのγ−アルミナ微粉末24.5重量部を添
加し、30分間撹拌混合〔K2 O/(K2 O+Al2 O
3 )のモル比で17モル%〕した。このスラリーにポリ
ビニルアルコ−ル(平均重合度約3000)5.0重量
部を添加し十分混合し、この混合液を減圧下に8時間濃
縮して25℃での粘度が2500ポアズの紡糸原液とし
た。この紡糸原液を、0.3mmφの孔を1000個有
する紡糸ノズルから乾燥用の紡糸筒内へ押出して紡糸
し、1000本のフィラメントからなる繊維径13μm
の前駆体繊維を得た。この前駆体繊維を、約100mm
の長さに切断し、高純度アルミナ製の匣に入れ、毎時1
00℃の昇温速度で1200℃まで昇温し、同温度で1
時間保持して焼成し、繊維径約10μmのフィラメント
1000本からなる繊維長約60mmのβ−アルミナ繊
維を得た。このβ−アルミナ繊維は、柔軟性があり、引
張強度100kgf/mm2 の繊維であった。また、X
線回折装置による同定及び分析の結果、純度約97重量
%のK2 O・5Al2 O3 結晶におけるC軸の格子定
数:3.423nm)のβ−アルミナ繊維であった。な
お、この繊維のSiO2 含有量及びFe2 O3 含有量
は、それぞれ、0.05重量%及び0.07重量%と非
常に少ない量であった。(Example 3) 2.0 parts by weight of lactic acid, 100.0 parts by weight of basic aluminum lactate (content of 37.0% by weight as Al 2 O 3 ) and 25.6 parts by weight of potassium nitrate were added to water. After being dissolved in 200 parts by weight, 24.5 parts by weight of γ-alumina fine powder having an average particle diameter of 0.02 μm was added, and mixed by stirring for 30 minutes [K 2 O / (K 2 O + Al 2 O
The molar ratio of 3 ) was 17 mol%]. To this slurry, 5.0 parts by weight of polyvinyl alcohol (average degree of polymerization: about 3000) was added and mixed well, and the mixture was concentrated under reduced pressure for 8 hours to give a spinning dope having a viscosity of 2500 poise at 25 ° C. did. This spinning dope is extruded from a spinning nozzle having 1000 holes of 0.3 mmφ into a spinning tube for drying to be spun, and a fiber diameter of 1000 filaments of 13 μm.
The precursor fiber of was obtained. About 100 mm of this precursor fiber
Cut to length and put in a box made of high-purity alumina, 1 hourly
At a heating rate of 00 ° C, the temperature is raised to 1200 ° C, and at the same temperature, 1
It was held for a period of time and fired to obtain β-alumina fiber having a fiber length of about 60 mm, which was composed of 1000 filaments having a fiber diameter of about 10 μm. The β-alumina fiber was flexible and had a tensile strength of 100 kgf / mm 2 . Also, X
As a result of identification and analysis by a line diffractometer, it was β-alumina fiber having a purity of about 97% by weight in a K 2 O.5Al 2 O 3 crystal and a C-axis lattice constant of 3.423 nm). The SiO 2 content and Fe 2 O 3 content of this fiber were very small amounts of 0.05% by weight and 0.07% by weight, respectively.
【0031】(実施例4)乳酸2.0重量部、塩基性乳
酸アルミニウム100.0重量部(Al2 O3 としての
含有率37.0重量%)及び酢酸カルシウム16.4重
量部とを、水200重量部に溶解させたのち、平均粒径
0.02μmのγ−アルミナ微粉末24.5重量部を添
加し、30分間撹拌混合〔CaO/(CaO+Al2 O
3 )のモル比で15モル%〕した。このスラリーにポリ
ビニルアルコ−ル(平均重合度約3000)5.0重量
部を添加し十分混合し、この混合液を減圧下に8時間濃
縮して25℃での粘度が2500ポアズの紡糸原液とし
た。この紡糸原液を、0.3mmφの孔を1000個有
する紡糸ノズルから乾燥用の紡糸筒内へ押出して紡糸
し、1000本のフィラメントからなる繊維径13μm
の前駆体繊維を得た。この前駆体繊維を、約100mm
の長さに切断し、高純度アルミナ製の匣に入れ、毎時1
00℃の昇温速度で1400℃まで昇温し、同温度で1
時間保持して焼成し、繊維径約10μmのβ−アルミナ
繊維を得た。このβ−アルミナ繊維は、柔軟性があり、
引張強度105kgf/mm2 の繊維長約60mmの繊
維であった。また、X線回折装置による同定及び分析の
結果、純度約95重量%のCaO・6Al2 O3 結晶に
おけるC軸の格子定数:2.189nm)のβ−アルミ
ナ繊維であった。なお、この繊維のSiO2 含有量及び
Fe2 O3 含有量は、それぞれ、0.06重量%及び
0.08重量%と非常に少ない量であった。(Example 4) 2.0 parts by weight of lactic acid, 100.0 parts by weight of basic aluminum lactate (content ratio as Al 2 O 3 of 37.0% by weight) and 16.4 parts by weight of calcium acetate, After being dissolved in 200 parts by weight of water, 24.5 parts by weight of γ-alumina fine powder having an average particle size of 0.02 μm was added, followed by stirring and mixing for 30 minutes [CaO / (CaO + Al 2 O
The molar ratio of 3 ) was 15 mol%]. To this slurry, 5.0 parts by weight of polyvinyl alcohol (average degree of polymerization: about 3000) was added and mixed well, and the mixture was concentrated under reduced pressure for 8 hours to give a spinning dope having a viscosity of 2500 poise at 25 ° C. did. This spinning dope is extruded from a spinning nozzle having 1000 holes of 0.3 mmφ into a spinning tube for drying to be spun, and a fiber diameter of 1000 filaments of 13 μm.
The precursor fiber of was obtained. About 100 mm of this precursor fiber
Cut to length and put in a box made of high-purity alumina, 1 hourly
The temperature is raised to 1400 ° C at a heating rate of 00 ° C, and 1
It was held for a time and fired to obtain β-alumina fiber having a fiber diameter of about 10 μm. This β-alumina fiber has flexibility,
The fiber had a tensile strength of 105 kgf / mm 2 and a fiber length of about 60 mm. As a result of identification and analysis by an X-ray diffractometer, it was β-alumina fiber having a purity of about 95% by weight in the CaO.6Al 2 O 3 crystal and having a C-axis lattice constant of 2.189 nm. The SiO 2 content and Fe 2 O 3 content of this fiber were 0.06% by weight and 0.08% by weight, respectively, which were very small amounts.
【0032】(比較例1)乳酸2.0重量部、塩基性乳
酸アルミニウム100.0重量部(Al2 O3 としての
含有率37.0重量%)及び硝酸ナトリウム5.7重量
部とを、水200重量部に溶解させたのち、ポリビニル
アルコ−ル(平均重合度約3000)5.0重量部を添
加し十分混合〔Na2 O/(Na2 O+Al2 O3 )の
モル比で8.5モル%〕し、この混合液を減圧下に濃縮
して25℃での粘度が2500ポアズの紡糸原液とし
た。この減圧下の濃縮には15時間かかり、アルミナ質
粉末を紡糸原液に添加した場合と比較すると、かなりの
時間を要し、生産性が低下した。この紡糸原液を、0.
3mmφの孔を1000個有する紡糸ノズルから乾燥用
の紡糸筒内へ押出して紡糸し、1000本のフィラメン
トからなる繊維径14μmの前駆体繊維を得た。しか
し、この前駆体繊維は部分的に融着を生じていた。この
前駆体繊維を、温度100℃から最高1400℃の温度
勾配を持たせた焼成炉中を滞留時間7分で連続的に通過
させて焼成し、繊維径約10μmのフィラメント100
0本からなる長繊維の形のβ−アルミナ繊維を得た。こ
のβ−アルミナ繊維は、引張強度42kgf/mm2 の
連続長繊維であり、アルミナ質粉末を紡糸原液に添加し
た場合と比較すると、繊維強度及び柔軟性が低かった。
また、X線回折装置による同定及び分析の結果、純度約
93重量%のNa2 O・11Al2 O3 (結晶における
C軸の格子定数:2.261nm)、並びに、少量のN
a2 O・7Al2 O3 (結晶におけるC軸の格子定数:
2.270nm)及びNa2 O・5Al2 O3 (結晶に
おけるC軸の格子定数:3.395nm)からなるβ−
アルミナ繊維であった。なお、このβ−アルミナ繊維の
SiO2 含有量及びFe2 O3 含有量を高周波プラズマ
発光分析装置(ICP)により分析した結果、それぞ
れ、0.03重量%及び0.06重量%と非常に少ない
量であった。Comparative Example 1 2.0 parts by weight of lactic acid, 100.0 parts by weight of basic aluminum lactate (content ratio as Al 2 O 3 of 37.0% by weight) and 5.7 parts by weight of sodium nitrate, After being dissolved in 200 parts by weight of water, 5.0 parts by weight of polyvinyl alcohol (average degree of polymerization of about 3000) was added and sufficiently mixed [Na 2 O / (Na 2 O + Al 2 O 3 ) at a molar ratio of 8. 5 mol%], and the mixture was concentrated under reduced pressure to give a spinning dope having a viscosity at 25 ° C. of 2500 poise. This concentration under reduced pressure took 15 hours, which required a considerable amount of time as compared with the case where the alumina powder was added to the spinning dope, and the productivity decreased. This spinning dope was mixed with 0.
A precursor nozzle having a fiber diameter of 14 μm consisting of 1000 filaments was obtained by extruding from a spinning nozzle having 1000 holes of 3 mmφ into a spinning cylinder for drying and spinning. However, this precursor fiber was partially fused. The precursor fiber is continuously passed through a firing furnace having a temperature gradient from 100 ° C. to a maximum of 1400 ° C. for a residence time of 7 minutes to be fired to obtain a filament 100 having a fiber diameter of about 10 μm.
A β-alumina fiber in the form of zero filaments was obtained. This β-alumina fiber was a continuous long fiber having a tensile strength of 42 kgf / mm 2 , and its fiber strength and flexibility were low as compared with the case where the alumina powder was added to the spinning dope.
As a result of identification and analysis by an X-ray diffractometer, a purity of about 93% by weight of Na 2 O.11Al 2 O 3 (C-axis lattice constant in the crystal: 2.261 nm) and a small amount of N
a 2 O.7Al 2 O 3 (C-axis lattice constant in the crystal:
2.270 nm) and Na 2 O.5Al 2 O 3 (C-axis lattice constant in crystal: 3.395 nm)
It was an alumina fiber. The SiO 2 content and the Fe 2 O 3 content of this β-alumina fiber were analyzed by a high-frequency plasma emission spectroscope (ICP), and as a result, they were 0.03% by weight and 0.06% by weight, respectively, which were very small. Was the amount.
【0033】[0033]
【発明の効果】本発明の方法では、紡糸原液に、アルミ
ナ質粉末、紡糸助剤などを使用しているので、アルカリ
金属化合物及び/又はアルカリ土類金属化合物を多量含
有するにも拘らず、紡糸性が良好で、また、得られる前
駆体繊維のβ−アルミナ化の反応性も高いので、繊維の
長さの長い高純度のβ−アルミナ繊維を容易に製造する
ことができる。また、本発明の方法における紡糸原液の
調製に当っては、水溶液のゾル化処理、ゾル化した液体
の濾過処理及び濾液の濃縮処理など長時間を要する処理
操作を必要とはしないか、その処理操作を行ったとして
も短時間で済むので、紡糸原液の生産性は極めて高いも
のであり、最終製品のβ−アルミナ繊維の生産性として
も極めて高いものである。アルミナ質粉末、紡糸助剤な
ど本発明の方法で用いられる繊維原料は、焼成後特にS
iO2 やFe2 O3 などの不純物を殆ど含まない高純度
の繊維原料を使用することができ、得られるβ−アルミ
ナ繊維は、高純度だけではなく、更に高強度で柔軟性の
ある繊維になる。本発明の方法では、前駆体繊維を焼成
の前又は後において5〜100mm程度の適当な長さに
切断し、焼成する方法で製造すれば、主として3〜60
mm程度のβ−アルミナ繊維が得られる。また、前駆体
繊維を長繊維のままで焼成すれば長繊維の形のβ−アル
ミナ繊維を得ることができ、またこれを適当な長さに切
断することにより長さの揃った繊維とすることもでき
る。このβ−アルミナ繊維は、耐アルカリ性構造材料、
及び、ナトリウム−硫黄電池などの電池用材料の補強材
として優れた性能を有しており、β−アルミナ粉末と混
合し、成型、加工することにより、取扱性が良好で、イ
オン伝導性等の物性を低下させることなく、熱的、機械
的衝撃による亀裂が生じ難い、強度の高い成型材料を得
ることができる。In the method of the present invention, since the spinning stock solution contains an alumina powder, a spinning aid, etc., it contains a large amount of an alkali metal compound and / or an alkaline earth metal compound. The spinnability is good, and the reactivity of the obtained precursor fibers for β-alumination is high, so that high-purity β-alumina fibers having a long fiber length can be easily produced. Further, in the preparation of the spinning dope in the method of the present invention, does not require a long-time treatment operation such as sol treatment of an aqueous solution, filtration treatment of the solized liquid and concentration treatment of the filtrate, or the treatment thereof. Since the operation can be completed in a short time, the productivity of the spinning dope is extremely high, and the productivity of the final product β-alumina fiber is also very high. The fiber raw materials used in the method of the present invention, such as the alumina powder and the spinning aid, are especially S after firing.
High-purity fiber raw material containing almost no impurities such as iO 2 and Fe 2 O 3 can be used, and the obtained β-alumina fiber is not only high in purity but also has high strength and flexibility. Become. In the method of the present invention, if the precursor fiber is cut into an appropriate length of about 5 to 100 mm before or after firing, and is produced by the method of firing, it is mainly 3 to 60.
A β-alumina fiber having a size of about mm is obtained. In addition, if the precursor fiber is fired as a long fiber as it is, a β-alumina fiber in the form of a long fiber can be obtained, and by cutting this into an appropriate length, a fiber having a uniform length can be obtained. You can also This β-alumina fiber is an alkali resistant structural material,
Also, it has excellent performance as a reinforcing material for battery materials such as sodium-sulfur batteries, and by mixing with β-alumina powder, molding and processing, the handleability is good, and the ionic conductivity, etc. It is possible to obtain a high-strength molding material in which cracks due to thermal and mechanical impact are unlikely to occur without deteriorating the physical properties.
【0034】更に、本発明の方法によって得られたβ−
アルミナ繊維は、多量のアルカリ金属成分及び/又はア
ルカリ土類金属成分を含有するにも拘らず、繊維の強度
や柔軟性を低下させることなく、高いイオン伝導性など
優れた特性を有し、耐アルカリ性構造材料の補強用とし
て、またナトリウム−硫黄電池などのイオン伝導性部材
として有用である。Further, β-obtained by the method of the present invention
Alumina fibers have excellent characteristics such as high ionic conductivity without deteriorating the strength and flexibility of the fibers, despite containing a large amount of alkali metal components and / or alkaline earth metal components, It is useful as a reinforcement for alkaline structural materials and as an ion conductive member for sodium-sulfur batteries.
フロントページの続き (56)参考文献 特開 平9−13230(JP,A) 特開 平3−140509(JP,A) (58)調査した分野(Int.Cl.7,DB名) D01F 9/08 Continuation of the front page (56) References JP-A-9-13230 (JP, A) JP-A-3-140509 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) D01F 9 / 08
Claims (3)
類金属成分を5〜40モル%含有し、結晶におけるC軸
の格子定数が2.1〜3.5nmであるβ−アルミナの
製造方法において、水溶性塩基性アルミニウム塩、並び
に、水溶性アルカリ金属化合物及び/又は水溶性アルカ
リ土類金属化合物を水系溶媒中に溶解させた溶液にアル
ミナ質粉末を添加し、更に紡糸助剤を添加して粘度を調
整して得られたスラリ−を紡糸原液とし、この紡糸原液
を紡糸して前駆体繊維とし、その前駆体繊維を1100
〜1600℃の範囲で焼成することを特徴とするβ−ア
ルミナ繊維の製造方法。1. A method for producing β-alumina containing an alkali metal component and / or an alkaline earth metal component in an amount of 5 to 40 mol% and having a C-axis lattice constant of 2.1 to 3.5 nm in the crystal, A water-soluble basic aluminum salt, and a solution of a water-soluble alkali metal compound and / or a water-soluble alkaline earth metal compound dissolved in an aqueous solvent, an alumina powder is added, and a spinning aid is further added to increase the viscosity. The slurry obtained by adjusting the above is used as a spinning stock solution, and this spinning stock solution is spun into a precursor fiber.
A method for producing β-alumina fiber, which comprises firing in the range of ˜1600 ° C.
物及び/又はカリウム化合物である請求項1に記載のβ
−アルミナ繊維の製造方法。2. The β according to claim 1, wherein the alkali metal compound is a sodium compound and / or a potassium compound.
-Alumina fiber manufacturing method.
化合物、ストロンチウム化合物及びバリウム化合物から
選ばれる1種以上のアルカリ土類金属化合物である請求
項1又は請求項2に記載のβ−アルミナ繊維の製造方
法。3. The production of β-alumina fiber according to claim 1 or 2, wherein the alkaline earth metal compound is one or more alkaline earth metal compounds selected from calcium compounds, strontium compounds and barium compounds. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18057495A JP3497285B2 (en) | 1995-06-26 | 1995-06-26 | Method for producing β-alumina fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18057495A JP3497285B2 (en) | 1995-06-26 | 1995-06-26 | Method for producing β-alumina fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0913231A JPH0913231A (en) | 1997-01-14 |
| JP3497285B2 true JP3497285B2 (en) | 2004-02-16 |
Family
ID=16085663
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18057495A Expired - Fee Related JP3497285B2 (en) | 1995-06-26 | 1995-06-26 | Method for producing β-alumina fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3497285B2 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3979494B2 (en) * | 2002-12-04 | 2007-09-19 | サンゴバン・ティーエム株式会社 | Biosoluble inorganic fiber that does not produce free silicic acid after heating and method for producing the same |
| JP7651295B2 (en) * | 2020-12-18 | 2025-03-26 | 株式会社クラレ | Method for producing polyvinyl alcohol fiber containing ferroelectric substance and fiber made of ferroelectric substance |
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1995
- 1995-06-26 JP JP18057495A patent/JP3497285B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0913231A (en) | 1997-01-14 |
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