JPH03112828A - Production of silica fiber - Google Patents
Production of silica fiberInfo
- Publication number
- JPH03112828A JPH03112828A JP24813789A JP24813789A JPH03112828A JP H03112828 A JPH03112828 A JP H03112828A JP 24813789 A JP24813789 A JP 24813789A JP 24813789 A JP24813789 A JP 24813789A JP H03112828 A JPH03112828 A JP H03112828A
- Authority
- JP
- Japan
- Prior art keywords
- water glass
- carbonate
- silica fiber
- dealkalization
- amount
- 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.)
- Pending
Links
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 239000000835 fiber Substances 0.000 title claims abstract description 26
- 239000000377 silicon dioxide Substances 0.000 title claims abstract description 23
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 235000019353 potassium silicate Nutrition 0.000 claims abstract description 16
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 12
- ZZXUZKXVROWEIF-UHFFFAOYSA-N 1,2-butylene carbonate Chemical compound CCC1COC(=O)O1 ZZXUZKXVROWEIF-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000009987 spinning Methods 0.000 claims abstract description 7
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000010306 acid treatment Methods 0.000 claims abstract description 4
- 238000010304 firing Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 2
- 239000003513 alkali Substances 0.000 abstract description 6
- 239000002253 acid Substances 0.000 abstract description 5
- -1 alkylene carbonate Chemical compound 0.000 abstract description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 abstract description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 abstract description 3
- 229910017604 nitric acid Inorganic materials 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 229910052681 coesite Inorganic materials 0.000 abstract 2
- 229910052906 cristobalite Inorganic materials 0.000 abstract 2
- 235000012239 silicon dioxide Nutrition 0.000 abstract 2
- 229910052682 stishovite Inorganic materials 0.000 abstract 2
- 229910052905 tridymite Inorganic materials 0.000 abstract 2
- 229910004742 Na2 O Inorganic materials 0.000 abstract 1
- 238000000034 method Methods 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 150000004703 alkoxides Chemical class 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 101100348017 Drosophila melanogaster Nazo gene Proteins 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 1
- BDAGIHXWWSANSR-UHFFFAOYSA-N Formic acid Chemical compound OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- ANTVXUWVWRKHPP-UHFFFAOYSA-N carbonic acid;pent-1-ene Chemical compound OC(O)=O.CCCC=C ANTVXUWVWRKHPP-UHFFFAOYSA-N 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 125000000896 monocarboxylic acid group Chemical group 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B37/00—Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
- C03B37/01—Manufacture of glass fibres or filaments
- C03B37/011—Manufacture of glass fibres or filaments starting from a liquid phase reaction process, e.g. through a gel phase
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2201/00—Type of glass produced
- C03B2201/02—Pure silica glass, e.g. pure fused quartz
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Fibers (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はシリカ繊維の製造方法、特に安価な水ガラスを
主原料としてアルカリ含有量の少ない高強度のシリカ繊
維を得る方法に係るものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for producing silica fibers, particularly a method for obtaining high-strength silica fibers with low alkali content using inexpensive water glass as a main raw material. .
[従来の技術]
従来、シリカ繊維の製造方法としては例えば02000
℃以上の高温で熔融成形したシリカロッドを火炎中で軟
化延伸して曳糸する方法、■テトラエトキシシランの様
なアルコキシドを出発原料とし、これらのアルコール溶
液に加水分解に必要な酸又はアルカリを加えてゲル化し
、得られた粘性溶液から曳糸し、次いで400〜120
0℃で焼成せしめる所謂ゾル−ゲル法、■出発原料とし
て安価な水ガラスを用い、これに苛性ソーダ等のアルカ
リを加え、且水分を蒸発させることにより濃縮して得ら
れた粘稠液から曳糸する方法(特公昭59−47043
号公報参照)等が知られている。[Prior Art] Conventionally, as a method for producing silica fiber, for example, 02000
A method in which a silica rod is melt-molded at a high temperature above ℃ and then softened and stretched in a flame and then threaded.■ Using an alkoxide such as tetraethoxysilane as a starting material, adding the acid or alkali necessary for hydrolysis to an alcohol solution of the silica rod. The resulting viscous solution is then gelled, and the resulting viscous solution is then threaded, and then 400 to 120
The so-called sol-gel method, which involves firing at 0°C, uses inexpensive water glass as a starting material, adds an alkali such as caustic soda to it, and evaporates the water to concentrate the resulting viscous liquid. How to
(see Publication No. 2003), etc. are known.
[発明が解決しようとする課題]
しかしながら、上記■の方法にあっては、熔融温度がか
なり高く、エネルギーコストがかかり又熔融曳糸の条件
コントロールが難しく、生産性が低いと云う欠点を有し
ている。[Problems to be Solved by the Invention] However, the method (2) above has the disadvantages that the melting temperature is quite high, energy costs are high, and it is difficult to control the conditions of the melted string, resulting in low productivity. ing.
又、■の方法においては、一般に曳糸性を示す時間が比
較的短(、作業性が悪い欠点の他、出発原料となるアル
コキシドのコストが高い為、得られるシリカ繊維のコス
トも高くなる欠点を有している。In addition, in method (2), the time required to exhibit spinnability is generally relatively short (in addition to the disadvantage of poor workability, the disadvantage is that the cost of the alkoxide used as the starting material is high, so the cost of the silica fiber obtained is also high). have.
更に、■の方法にあっては、曳糸液中のアルカリ成分が
多(、曳糸後焼成する際にシリカが結晶化し、一部が繊
維状態を保持し得ず、ボロボロになったり、高温強度の
著しい低下をもたらす等の欠点を有している。Furthermore, in method (2), there is a large amount of alkaline component in the spinning solution (silica crystallizes during firing after spinning, some of the yarn cannot maintain its fiber state, becomes crumbly, or is exposed to high temperatures). It has drawbacks such as a significant decrease in strength.
[課題を解決する為の手段]
本発明者は、前記従来法が有する諸欠点を排除し、安価
な水ガラスを用いながらもアルカリによる障害を排除し
、安価且高強度のシリカ繊維を得ることを目的として種
々研究、検討した結果、特定のアルキレンカーボネート
を併用することにより、前記目的を達成し得ることを見
出した。[Means for Solving the Problems] The present inventor aims to eliminate the various drawbacks of the above-mentioned conventional methods, eliminate troubles caused by alkali while using inexpensive water glass, and obtain inexpensive and high-strength silica fibers. As a result of various studies and examinations aimed at this purpose, it has been found that the above object can be achieved by using a specific alkylene carbonate in combination.
かくして本発明は、水ガラスにプロピレンカーボネート
及び/又はブチレンカーボネートを添加混合し、得られ
た粘稠液から曳糸し、酸処理により脱アルカリ後焼成せ
しめることを特徴とするシリカ繊維の製造方法を提供す
るにある。Thus, the present invention provides a method for producing silica fibers, which comprises adding and mixing propylene carbonate and/or butylene carbonate to water glass, spinning the resulting viscous liquid, dealkalizing it by acid treatment, and then firing it. It is on offer.
本発明において、用いられる水ガラスとじてはNa2O
:5iOz= 1:1.9〜3.3のものを用い得るが
、脱アルカリが容易で且プロピレンやブチレンのカーボ
ネートの使用量が少なくて済む点でSiO□成分の多い
方が好ましく、Na2O:SiO□=l:3〜3.3の
組成を採用するのが好ましい。In the present invention, the water glass used is Na2O
:5iOz=1:1.9 to 3.3 can be used, but it is preferable to have a large SiO□ component because dealkalization is easy and the amount of propylene or butylene carbonate used is small, and Na2O: It is preferable to adopt a composition of SiO□=l: 3 to 3.3.
次に本発明にあってはプロピレンカーボネートやブチレ
ンカーボネートが用いられる。これらより低位のアルキ
レンカーボネート、例えばエチレンカーボネートを用い
ると瞬時にゲル化が進行し、曳糸することが出来ず、逆
にこれらより高位のカーボネート、例えばペンテンカー
ボネートを用いると曳糸し得る程度の粘稠液となるのに
長時間を要するので何れも不適当である。Next, in the present invention, propylene carbonate and butylene carbonate are used. If an alkylene carbonate lower than these, such as ethylene carbonate, is used, gelation will proceed instantaneously and threading will not be possible.On the other hand, if a carbonate higher than these, such as pentene carbonate, is used, the viscosity will be high enough to be threadable. Both are unsuitable because it takes a long time to form a thick liquid.
プロピレンカーボネートやブチレンカーボネートは何れ
もほぼ同様に用いることが出来、両者を任意の割合で併
用することも出来る。Both propylene carbonate and butylene carbonate can be used in substantially the same way, and both can also be used together in any ratio.
これらカーボネートの使用量は、用いられる水ガラスの
珪曹比や紡糸条件により適宜決定されるが、SiO□成
分が多(なる程用いられるカーボネートの量は少な(て
済む傾向にある。The amount of these carbonates to be used is appropriately determined depending on the silica ratio of the water glass used and the spinning conditions, but there is a tendency for the SiO□ component to be large (as it is true, the amount of carbonate used is small).
一般にNatO:SiO*= l:3〜3.3の範囲で
は水ガラス100重量部に対しカーボネートを1.0〜
1.6重量部の割合で用いるのが曳糸性の面から最適で
ある。Generally, when NatO:SiO*=l:3 to 3.3, carbonate is added to 1.0 to 100 parts by weight of water glass.
It is optimal to use it at a ratio of 1.6 parts by weight from the viewpoint of stringability.
これらの好適な組成を採用する場合には、曳糸性を示す
粘稠液となった後10〜14日間の長期にわたり常温に
おいて初期と同様に曳糸性を保持し続けることが出来る
。When these suitable compositions are employed, after the liquid becomes a viscous liquid that exhibits stringiness, it can continue to maintain its stringiness at room temperature for a long period of 10 to 14 days as at the initial stage.
かくして得られた粘稠液からは常法に従って曳糸が行な
われる。The viscous liquid thus obtained is threaded according to a conventional method.
得られた糸はアルカリ性を呈し、これをそのまま焼成せ
しめると、結晶化が進み、糸がボロボロになったり、強
度が著しく低下する。この為本発明においては、脱アル
カリ即ち酸による中和を行なう。The obtained thread exhibits alkalinity, and if it is fired as it is, crystallization progresses, causing the thread to become crumbly and significantly reduced in strength. Therefore, in the present invention, dealkalization, that is, neutralization with an acid is performed.
用いられる酸としては例えばHNO3,HCI。Examples of acids that can be used include HNO3 and HCI.
H,SO,等の鉱酸類やHCOOH,CH,C0OH等
の有機酸類を適宜用い得るが、とりわけHNO3,HC
Iを用いると最終的に得られるシリカ繊維中に好ましか
らざる不純物が残留しないので特に好ましい。Mineral acids such as H, SO, etc. and organic acids such as HCOOH, CH, COOH can be used as appropriate, but especially HNO3, HC
The use of I is particularly preferred since no undesirable impurities remain in the silica fibers finally obtained.
かくして脱アルカリ後の繊維は次いで400〜1200
℃の温度範囲で焼成されるが、800〜1000℃の温
度を採用することによりシリカ繊維の緻密性や強度向上
を期待し得るので好ましい。Thus, the fiber after dealkalization is then 400-1200
It is preferable to use a temperature in the range of 800 to 1000 degrees Celsius because it is expected that the denseness and strength of the silica fibers will be improved.
本発明方法を採用すると、曳糸期間がlO日間以上と長
(、作業性や原料の有効利用の面で優れており、安価な
水ガラスを原料とし、アルカリ含有量の少ない高純度の
シリカ繊維を1000℃程度の比較的低温で容易に得る
ことが出来る利点を有している
[実施例]
実施例I
JIS 3号水ガラス(NazO:SxO,= 1:3
.2モル比) longにブチレンカーボネート 1.
4gを加え、室温下に約1時間撹拌して均一な粘稠液を
得た。該液を約1時間静置して脱泡後、常法に従い連続
曳糸し、直径15〜20μのゲル状繊維を得た。この繊
維を100℃で12時間乾燥後、5NHNOa中に30
分間浸漬して脱アルカリし、イオン交換水中に30分浸
漬して洗浄後100℃にて1時間乾燥せしめた。得られ
た繊維は次いで電気炉中で10℃/分の速度で1000
℃迄昇温し、1000°Cに1時間保持後、常温迄放冷
してシリカ繊維を得た。When the method of the present invention is adopted, the spinning period is longer than 10 days (it is superior in terms of workability and effective use of raw materials, and is made from high-purity silica fibers made from inexpensive water glass and with low alkali content. [Example] Example I JIS No. 3 water glass (NazO:SxO, = 1:3)
.. 2 molar ratio) long butylene carbonate 1.
4 g was added and stirred at room temperature for about 1 hour to obtain a uniform viscous liquid. The solution was allowed to stand for about 1 hour to defoam, and then continuously threaded according to a conventional method to obtain gel-like fibers with a diameter of 15 to 20 μm. After drying this fiber at 100°C for 12 hours,
It was immersed for 1 minute to dealkalize it, immersed in ion-exchanged water for 30 minutes, washed, and then dried at 100° C. for 1 hour. The obtained fibers were then heated in an electric furnace at a rate of 10°C/min.
The temperature was raised to 1000°C, held at 1000°C for 1 hour, and then allowed to cool to room temperature to obtain silica fibers.
この繊維は、繊維径lO〜15μ、比重2.ONa含有
量15ppm 、引張り強度55〜60 k g /
m m 2であった。This fiber has a fiber diameter of lO~15μ and a specific gravity of 2. ONa content 15 ppm, tensile strength 55-60 kg/
It was mm2.
尚、前記粘I11液を密閉容器中にIO日間常温下に保
存後、その曳糸性を試験した処、保存前と同条件で曳糸
出来、同性状、同物性のシリカ繊維が得られた。In addition, after storing the above-mentioned viscous I11 liquid in a sealed container at room temperature for 10 days, its spinnability was tested, and silica fibers with the same properties and physical properties were obtained under the same conditions as before storage. .
実施例2
実施例1と同一の水ガラス100gにプロピレンカーボ
ネート1.5gを加えて得た粘稠液を用いた以外実施例
1と同様にしてシリカ繊維を得た。Example 2 Silica fibers were obtained in the same manner as in Example 1, except that a viscous liquid obtained by adding 1.5 g of propylene carbonate to 100 g of the same water glass as in Example 1 was used.
この繊維の繊維径は10〜15μ、比重2,1、Na含
有量18ppm 、引張り強度5’j〜64kg/mm
2であった。The fiber diameter of this fiber is 10~15μ, specific gravity 2.1, Na content 18ppm, tensile strength 5'j~64kg/mm.
It was 2.
尚、前記粘稠液を密閉容器中に12日間常温下に保存後
、その曳糸性を試験した処、保存前と同条件で曳糸出来
、同性状、同物性のシリカ繊維が得られた。The viscous liquid was stored in a sealed container at room temperature for 12 days, and then its spinnability was tested, and silica fibers with the same properties and physical properties were obtained under the same conditions as before storage. .
Claims (1)
レンカーボネートを添加混合し、得られた粘稠液から曳
糸し、酸処理により脱アルカリ後焼成せしめることを特
徴とするシリカ繊維の製造方法。1. A method for producing silica fibers, which comprises adding and mixing propylene carbonate and/or butylene carbonate to water glass, spinning the resulting viscous liquid, dealkalizing it by acid treatment, and then firing it.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24813789A JPH03112828A (en) | 1989-09-26 | 1989-09-26 | Production of silica fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24813789A JPH03112828A (en) | 1989-09-26 | 1989-09-26 | Production of silica fiber |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03112828A true JPH03112828A (en) | 1991-05-14 |
Family
ID=17173778
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24813789A Pending JPH03112828A (en) | 1989-09-26 | 1989-09-26 | Production of silica fiber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03112828A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20180050947A1 (en) * | 2015-02-26 | 2018-02-22 | Corning Incorporated | Glass manufacturing apparatus and methods |
JP2018090926A (en) * | 2016-12-02 | 2018-06-14 | 日立化成株式会社 | Method for producing fibrous material |
-
1989
- 1989-09-26 JP JP24813789A patent/JPH03112828A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20180050947A1 (en) * | 2015-02-26 | 2018-02-22 | Corning Incorporated | Glass manufacturing apparatus and methods |
JP2018090926A (en) * | 2016-12-02 | 2018-06-14 | 日立化成株式会社 | Method for producing fibrous material |
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