JPS6065735A - Production of quartz glass - Google Patents
Production of quartz glassInfo
- Publication number
- JPS6065735A JPS6065735A JP17501983A JP17501983A JPS6065735A JP S6065735 A JPS6065735 A JP S6065735A JP 17501983 A JP17501983 A JP 17501983A JP 17501983 A JP17501983 A JP 17501983A JP S6065735 A JPS6065735 A JP S6065735A
- Authority
- JP
- Japan
- Prior art keywords
- quartz glass
- silica
- sol
- gel
- fine powdery
- 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 78
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 24
- 239000002245 particle Substances 0.000 claims abstract description 15
- 239000002994 raw material Substances 0.000 claims abstract description 12
- -1 alkyl silicate Chemical compound 0.000 claims abstract description 9
- 238000003980 solgel method Methods 0.000 claims abstract description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract description 8
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 abstract description 2
- 238000013019 agitation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 10
- 238000005245 sintering Methods 0.000 description 10
- 239000000499 gel Substances 0.000 description 9
- 239000000843 powder Substances 0.000 description 9
- 238000001035 drying Methods 0.000 description 5
- 230000003287 optical effect Effects 0.000 description 5
- 238000005187 foaming Methods 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 description 3
- 238000004031 devitrification Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 239000000741 silica gel Substances 0.000 description 3
- 229910002027 silica gel Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 238000000862 absorption spectrum Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000001879 gelation Methods 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000001132 ultrasonic dispersion Methods 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241000237858 Gastropoda Species 0.000 description 1
- 102000011782 Keratins Human genes 0.000 description 1
- 108010076876 Keratins Proteins 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 150000004703 alkoxides Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000005350 fused silica glass Substances 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/006—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels to produce glass through wet route
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Melting And Manufacturing (AREA)
- Silicon Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、石英ガラスの製造法に関シ、さらに詳しくは
、アルキルシリケートおよび微粉末シリカを主原料とす
るゾル−ゲル法による低温での石英ガラスの製造法にお
いて、原料として平均粒子径が30OA以上の比較的大
きな微粉末シリカを用い、これとアルキルシリケート、
水、および塩酸を混合し、シリカゲルを作製、さらに仁
れを焼結する透明均質な石英ガラスの製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing quartz glass, and more particularly, a method for producing quartz glass at low temperatures by a sol-gel method using alkyl silicate and finely powdered silica as main raw materials. A relatively large finely powdered silica with an average particle size of 30OA or more is used as a raw material, and this and alkyl silicate,
This invention relates to a method for producing transparent homogeneous quartz glass by mixing water and hydrochloric acid to produce silica gel and then sintering the keratin.
まず石英ガラスの有用性について触れることにする。近
年、石英ガラスは、銅、ホウ素等の不純物濃度が0.l
ppm以下の高純度のものが製造されるようになったた
め、ゲルマニウム、シリコン、その他の半導体の製造工
程におけるルツボやボード、拡散炉の炉心管などに幅広
く用いられるようになル、また理化学用ビーカー、光学
測定用のセルとしてもよく使用され、さらに水酸基含有
量の少ないものおよび光学的均一性に優れた高品質なも
のが開発され、各種の光学的用途に使用され、特に光通
信用の石英ガラスファイバーは、注目されている。この
ように使用範囲の広い石英ガラスは、現在、一般に次に
示す3通りの方法で製造されている。First, I will touch on the usefulness of quartz glass. In recent years, quartz glass has been developed with a concentration of impurities such as copper and boron of 0. l
As high-purity products of less than ppm can now be manufactured, they are now widely used in crucibles and boards in the manufacturing process of germanium, silicon, and other semiconductors, as well as in the core tubes of diffusion furnaces, as well as in beakers for physical and chemical use. , which are often used as cells for optical measurements, and high-quality cells with low hydroxyl content and excellent optical uniformity have been developed and are used for various optical applications, especially quartz for optical communication. Glass fiber is attracting attention. Quartz glass, which has such a wide range of uses, is currently manufactured generally by the following three methods.
Ill 天然水晶を洗浄し、ξれを溶融する方法【2)
高純度EiCi4またはsgr4を原料としてsho
冨を作る方法
131 天然珪砂を溶融する方法、(泡を含む石英ガラ
スが得られる〕
しかし、以上のいずれの製造方法を用いても、原料費が
高価であることおよび高温での処理が必要であることな
どのために、石英ガラスは非常に高価なものになってい
る。Ill How to clean natural crystal and melt ξ [2]
SHO using high purity EiCi4 or sgr4 as raw material
Method for making wealth 131 Method of melting natural silica sand (Produces quartz glass containing bubbles) However, with any of the above manufacturing methods, raw materials are expensive and processing at high temperatures is required. For a number of reasons, quartz glass is extremely expensive.
そこで石英ガラスの安価な製造法として、最近、特に注
目をあびているのが、ゾル−ゲル法による低温での石英
ガラスの製造法である。この方法は簡単に説明すると、
目的ガラス成分を含む金属アルコヲート等を原料として
、ゾルを作製、これに熱処理等の操作を加えゲル化させ
、乾燥(収縮を伴う)、焼結しガラス化させるというも
のであるこのゾル−ゲル法による石英ガラス製造法の特
徴としては
+11 水晶を原料として高温溶融法で製造する場合に
比べ低温で製造可能なため省エネルギー的である。Therefore, as an inexpensive method for producing quartz glass, a method for producing quartz glass at low temperatures using a sol-gel method has recently been attracting particular attention. This method is briefly explained as follows:
PurposeThis sol-gel method involves preparing a sol using a metal alkoxide containing a glass component as a raw material, gelling it by heat treatment, drying (accompanied by shrinkage), sintering, and vitrifying it. The characteristics of the quartz glass manufacturing method according to the method are as follows:+11 It is energy saving because it can be manufactured at a lower temperature than when manufacturing by a high temperature melting method using quartz as a raw material.
(2)原料が精製容易なため高純度のガラスが得られる
。(2) High purity glass can be obtained because the raw materials are easy to purify.
(31粘性の低い溶液t−i料として用いるために、均
質なガラスが得られる。(31 A homogeneous glass is obtained for use as a low viscosity solution ti material.
などがあげられる、このように利点が多いため、この方
法を利用する石英ガラスの製造法に関する研究は、さま
ざまな所で幅広く行なわれている。Because of these many advantages, research into the production of silica glass using this method is being widely conducted in various places.
しかしながら、これまでに発表されている資料等による
と未解決の問題点が数多く実用化にまで至っていないの
が現状である。However, according to the materials published so far, there are many unresolved problems and the technology has not yet been put into practical use.
このようなゾル−ゲル法の一手法として次の方法が考案
されている。すなわち、適当なアルキルシリケー) 5
j(oR)4(Rは炭素数1〜10のアルキル基)、適
当なアルコール溶液(含水)、塩酸、および微粉末シリ
カを混合、分散させシリカゾルとし、アンそニア水等に
よるpH値の調整、熱処理等を加えることによりシリカ
ゲルとする。ここで得られた塊状のシリカゲルを炉に入
れ所定のプログラムで焼結を行ない石英ガラスとするも
のである。The following method has been devised as one of such sol-gel methods. i.e., a suitable alkyl silicate) 5
j(oR)4 (R is an alkyl group having 1 to 10 carbon atoms), a suitable alcohol solution (containing water), hydrochloric acid, and finely powdered silica are mixed and dispersed to form a silica sol, and the pH value is adjusted with aqueous ammonia, etc. , heat treatment, etc. to form silica gel. The obtained bulk silica gel is placed in a furnace and sintered according to a predetermined program to form quartz glass.
この方法での最大の利点は、微粉末シリカを添加するこ
とによp1大きな板状の石英ガラスが容易に得られるこ
とである。ところが、微粉末シリカわ添加しても乾燥ゲ
ル作製時に割れたシ、焼結の際、発泡、失透が起と力、
また、焼結後の熱処理(1250℃程度)で発泡する場
合が、平均粒子径300A未満の微粉末シリカを使用す
ると見られ、目的とする板状の大きな石英ガラスが得ら
れない、そこで本発明の目的は、原料微粉末シリカの平
均粒子径を限定することにより、上記の問題点を解消す
る仲とである、すなわち、原料の微粉末シリカとして、
平均粒子径がaoo X以上のものを使用するものであ
ル、後で実施例にて示すが、最適なものは、平均粒子径
400スのAEiRO8工ho x 50 (商品名、
Diguaaa社)である。りま9、エチルシリケー
ト、水、アルコール(有無どちらでも可)および塩酸を
混合し加水分解溶液を調製、これに平均粒子径300八
以上の微粉末シリカ(例えばく商品名) AFiRo8
ILo x 50 (Dig1bsaα社) @ *
−40OA、 N1psil E、150K 、 Ei
1505 、 JI1200 、 Fi200A 、
3220 、 B220A (日本シリカニ業に、K)
、・・1000〜4500Xなど)を混合攪拌し、分
散性を高めるために超音波による分散、遠心分離、濾過
などの操作を加える、この後、アンモニア水等によフル
H値を高く調整することによりゲル化時間の短縮が可能
である。これを容器に移し、ゲル化させ、乾燥し得られ
た乾燥ゲルを炉に入れ焼結するというものである。この
方法を用騒ると、乾燥途中で割れることが極力少なく、
歩留ルが著しく向上する、また焼結後の熱処理(130
0℃、3時間)の際にも、発泡、失透等の現象は生じな
かった。しかし、粒子径がzoooX t−超えると焼
結温度が非常に高くな9、ゾル−ゲル法の利点である低
温でのガラス作製においては好まし7〈なく、300〜
500八程度の粒子径の微粉末シリカ、すなわち(商品
名)Anas工LOX so (Dirtα88α社)
を用いるのが最適である。The greatest advantage of this method is that plate-shaped quartz glass with a large p1 can be easily obtained by adding finely powdered silica. However, even when finely powdered silica is added, cracks occur during dry gel preparation, foaming, and devitrification occur during sintering.
In addition, foaming may occur during post-sintering heat treatment (approximately 1250°C) when fine powder silica with an average particle diameter of less than 300A is used, making it impossible to obtain the desired large plate-shaped silica glass. The purpose of this is to solve the above problems by limiting the average particle diameter of the raw material fine powder silica, that is, as the raw material fine powder silica,
A material with an average particle size of aoo
Diguaaa Inc.). Prepare a hydrolyzed solution by mixing Rima 9, ethyl silicate, water, alcohol (with or without), and hydrochloric acid, and add fine powder silica (eg, trade name) with an average particle size of 3008 or more to this solution.
ILo x 50 (Dig1bsaα) @ *
-40OA, N1psi E, 150K, Ei
1505, JI1200, Fi200A,
3220, B220A (K to Nippon Silkani Industry)
, 1000-4500X, etc.), and add operations such as ultrasonic dispersion, centrifugation, and filtration to improve dispersibility. After this, adjust the full H value to a high value with aqueous ammonia, etc. This makes it possible to shorten the gelation time. This is transferred to a container, gelled, and dried, and the resulting dry gel is placed in a furnace and sintered. If you use this method, there will be as little chance of cracking as possible during drying.
The yield rate is significantly improved, and post-sintering heat treatment (130
0° C. for 3 hours), no phenomena such as foaming or devitrification occurred. However, if the particle size exceeds zooooX t, the sintering temperature will be very high9, but it is preferable to prepare glass at low temperatures, which is an advantage of the sol-gel method.
Finely powdered silica with a particle size of about 5008, i.e. (trade name) Anasko LOX so (Dirtα88α)
It is best to use
以下、実施例に従い本発明の内容をさらに詳細に説明す
る。Hereinafter, the content of the present invention will be explained in more detail according to Examples.
実施例
市販ノエチルシリケート(8i(OBt )4)264
??Jと0.0IN HCA 21677L#1!:
混合、激しく攪拌し加水分解反応を行なった。加水分解
終了後、攪拌を継続しこの溶液に、微杓末シリカ90g
を徐々に添加した。Example Commercially available noethyl silicate (8i (OBt)4) 264
? ? J and 0.0IN HCA 21677L#1! :
The mixture was mixed and stirred vigorously to carry out a hydrolysis reaction. After hydrolysis is complete, continue stirring and add 90 g of silica powder to this solution.
was added gradually.
添加後、分散性を高めるために、攪拌′t−2時間、超
音波による分散t−3時間、更に遠心分離(3000r
、prn、 10分間)シ、この後アンモニア水を滴下
しpH値を4.5〜5.OK調整し、濾過(400mg
5h (Dポリプロピレン製シート)後、27 X 2
2 cmのポリプロピレン製容器に移し、蓋をして密閉
状態にて、室温でゲル化させた。上記が容器1枚分の操
作方法であるが本実験にお込ては、微粉末シリカとして
、■AEROS工LOX 50 (400” ) *■
Hipail E220A(1000裏)、■N1ps
il R200(2500X ) 、、■Cob−a−
ai1M−5(100A) の4種類について、それぞ
れ容器40枚ずつ行ない、以下に記すが、乾燥条件を4
鍾類に変えて乾燥を行なった。ゲル化後、収縮が始まっ
た時点で蓋を乾燥速度の調節可能な穴あきの蓋に取り替
えた。ここでこの蓋の開孔率は+1)1.0係、 12
12.0 % 、 1315.0%、(4)1000%
の4種類〔各10枚ずつ〕を用い、乾燥機に入れ、(資
)℃から昇温速度3Vnrでω℃まで温度を上昇させ、
以後ω℃に保持し5、乾燥を行なった。この結果を表I
K示す、このように乾燥条件によって歩留ルは、大きく
左右されるが、上記の■〜■を用いた場合、開孔率を1
〜2%にするとはとんど割れずに乾燥ゲルが作製可能な
ことが明らかになった。しかし■についてはほとんどで
きなし状態であった。ここで得られた乾燥ゲルの大きさ
は、微粉末シリカの種類とは、はとんど関係なく、18
゜5 X 14.OX O,6副の板状であp1開孔率
の大きな容器のゲルは、反りが見られた。この乾燥ゲル
を昇温速度180Vnrで加熱焼結を行なった。また焼
結後1300℃で3時間の熱処理を行なった。これらの
結果を表2に示す。これより加えた微粉末シリカの粒子
径が大きb程、焼結温度が高くなシ、熱処理においては
■〜■については、問題なかったが、■は発泡しふくれ
あがり白色となってしまった。また、それぞれの焼結体
の焼結時の大きさはi4.OX9.8X0.4crnで
あり諸物性分析の結果は、ビッカース硬度800Kl/
−u−” −比重2.2であル、赤外吸収スペクトル、
近赤外吸収スペクトル、および屈折率など溶融石英ガラ
スと全く一致していた。但し■については、多少OH量
が多かった。これが、熱処理の際の発泡、失透の原因で
あると考える。After addition, in order to improve dispersibility, stirring was carried out for 2 hours, ultrasonic dispersion was carried out for 3 hours, and centrifugation was performed at 3000 rpm.
, prn, for 10 minutes) After that, ammonia water was added dropwise to adjust the pH value to 4.5-5. Adjust OK and filter (400mg
After 5 hours (D polypropylene sheet), 27 x 2
The mixture was transferred to a 2 cm polypropylene container, covered with a lid, and allowed to gel at room temperature. The above is the operation method for one container, but in this experiment, we used ■AEROS Engineering LOX 50 (400”) *■ as fine powder silica.
Hipail E220A (1000 back), ■N1ps
il R200 (2500X),, ■Cob-a-
For each of the four types of ai1M-5 (100A), 40 containers were tested, and the drying conditions were set to 4 as described below.
I changed it to snails and dried it. After gelation, when shrinkage began, the lid was replaced with a perforated lid with adjustable drying rate. Here, the open area ratio of this lid is +1) 1.0 factor, 12
12.0%, 1315.0%, (4) 1000%
Using 4 types [10 sheets each], put them in a dryer and raise the temperature from (capital) °C to ω °C at a heating rate of 3Vnr.
Thereafter, the temperature was maintained at ω°C (5) and dried. This result is shown in Table I
In this way, the yield rate is greatly affected by the drying conditions, but when using the above ■~■, the open area ratio is 1
It has become clear that when the content is set at ~2%, a dry gel can be produced without cracking. However, regarding ■, there was almost no improvement. The size of the dried gel obtained here has almost no relation to the type of finely powdered silica;
゜5×14. The gel in the plate-shaped container with a large p1 porosity with OX O,6 side was warped. This dried gel was heated and sintered at a heating rate of 180 Vnr. Further, after sintering, heat treatment was performed at 1300° C. for 3 hours. These results are shown in Table 2. The larger the particle size of the finely powdered silica added, the higher the sintering temperature.There was no problem in heat treatment for items 1 to 2, but item 2 foamed and swelled to a white color. Moreover, the size of each sintered body when sintered is i4. OX9.8X0.4crn, and the results of physical property analysis are Vickers hardness 800Kl/
-u-" - specific gravity 2.2, infrared absorption spectrum,
The near-infrared absorption spectrum and refractive index completely matched those of fused silica glass. However, regarding ■, the amount of OH was somewhat large. This is thought to be the cause of foaming and devitrification during heat treatment.
前実施例の他にも、少し小さい容器あるいは円形の容器
(シャーレ)等を用いて同様の実験を行なったが、はぼ
同様の結果が得られた。また粒子径に関しても上記以外
に、50A 、 200 A 、 600 A、 40
00Hの微粉末シリカを使用したが、50Aと2ooX
は■、 600 Xは■、 4000久は■■の結果と
同様というように、はぼ3種類に大別できた。In addition to the previous example, similar experiments were conducted using a slightly smaller container or a circular container (Petri dish), and similar results were obtained. In addition to the above, particle diameters include 50A, 200A, 600A, and 40A.
00H fine powder silica was used, but 50A and 2ooX
The results could be roughly divided into three types: ■, 600X, and ■■, 4000K.
以上、実施例にて示したように、添加する微粉末シリカ
の粒子径により、石英ガラスの歩留pbよび、焼結温度
、耐熱性は大きく影1#を受ける。このため、より低コ
ストでしかも耐熱性に優れた石英ガラスを製造するのに
は、平均粒子径が30OA以上の微粉末シリカを用いる
のが好ましく、コスト面などから、平均粒子径400A
のARROSよりox 50(商品名)が最適である。As shown in the examples above, the yield pb, sintering temperature, and heat resistance of quartz glass are greatly affected by the particle size of the finely powdered silica to be added. Therefore, in order to manufacture quartz glass with excellent heat resistance at a lower cost, it is preferable to use fine powder silica with an average particle size of 30 OA or more.
OX 50 (product name) is the best choice from ARROS.
このようにして本発明によル製造される石英ガラスは、
従来の方法(溶融法)によるよりも、低コストでできる
等の大きな利点により、これまで石英ガラスを使用して
いた分野では、もちろんのこと、耐熱性にも良好な石英
ガラスが容易に製造できるため、光学的用途など、さら
に広範囲にその応用が広がってゆ〈本のと考える。The quartz glass thus produced according to the present invention is
Due to its major advantages such as lower cost than conventional methods (melting method), silica glass with good heat resistance can be manufactured easily in fields where quartz glass has been used up until now. Therefore, it is thought that its application will expand to a wider range of applications, such as optical applications.
表1は、実施例にて行なったゲル化後の乾燥ゲルの歩留
りを示したものであり、表2は得られた乾燥ゲルの焼結
および熱処理(1300℃、3時間)の結果を示したも
のであり、それぞれ使用した微粉末シリカ(粒子径の異
なる)ごとにまとめた。Table 1 shows the yield of dried gel after gelling performed in the example, and Table 2 shows the results of sintering and heat treatment (1300°C, 3 hours) of the obtained dry gel. The results are summarized for each type of fine powder silica (with different particle sizes) used.
Claims (1)
用騒るゾル−ゲル法において、原料として、平均粒子径
が300X以上の微粉末シリカを用いることを特徴とす
る石英ガラスの製造法。A method for producing quartz glass, characterized in that a sol-gel method using alkyl silicate and finely powdered silica as main raw materials uses finely powdered silica having an average particle size of 300X or more as a raw material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17501983A JPS6065735A (en) | 1983-09-21 | 1983-09-21 | Production of quartz glass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17501983A JPS6065735A (en) | 1983-09-21 | 1983-09-21 | Production of quartz glass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6065735A true JPS6065735A (en) | 1985-04-15 |
Family
ID=15988793
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17501983A Pending JPS6065735A (en) | 1983-09-21 | 1983-09-21 | Production of quartz glass |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6065735A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5114881A (en) * | 1988-03-04 | 1992-05-19 | Mitsubishi Kasei Corporation | Process for producing a ceramic preform |
| WO2005040053A1 (en) * | 2003-10-01 | 2005-05-06 | Novara Technology S.R.L. | An improved sol-gel process, the product obtained thereby and method for storing nuclear material employing the same |
| JP2016127924A (en) * | 2008-10-16 | 2016-07-14 | オリオン テック アクチェンゲゼルシャフト | Treatment of liquid waste containing heavy metals |
| CN112758973A (en) * | 2021-01-21 | 2021-05-07 | 成都信息工程大学 | Method for recycling iron-making and steel-making manganese slag |
-
1983
- 1983-09-21 JP JP17501983A patent/JPS6065735A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5114881A (en) * | 1988-03-04 | 1992-05-19 | Mitsubishi Kasei Corporation | Process for producing a ceramic preform |
| WO2005040053A1 (en) * | 2003-10-01 | 2005-05-06 | Novara Technology S.R.L. | An improved sol-gel process, the product obtained thereby and method for storing nuclear material employing the same |
| JP2016127924A (en) * | 2008-10-16 | 2016-07-14 | オリオン テック アクチェンゲゼルシャフト | Treatment of liquid waste containing heavy metals |
| CN112758973A (en) * | 2021-01-21 | 2021-05-07 | 成都信息工程大学 | Method for recycling iron-making and steel-making manganese slag |
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