JPH06122533A - Silica glass containing silicon carbide and its production - Google Patents
Silica glass containing silicon carbide and its productionInfo
- Publication number
- JPH06122533A JPH06122533A JP27626092A JP27626092A JPH06122533A JP H06122533 A JPH06122533 A JP H06122533A JP 27626092 A JP27626092 A JP 27626092A JP 27626092 A JP27626092 A JP 27626092A JP H06122533 A JPH06122533 A JP H06122533A
- Authority
- JP
- Japan
- Prior art keywords
- silicon carbide
- glass
- silica glass
- organochlorosilane
- silica
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/14—Other methods of shaping glass by gas- or vapour- phase reaction processes
- C03B19/1415—Reactant delivery systems
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/14—Other methods of shaping glass by gas- or vapour- phase reaction processes
- C03B19/1453—Thermal after-treatment of the shaped article, e.g. dehydrating, consolidating, sintering
-
- 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
- C03C14/00—Glass compositions containing a non-glass component, e.g. compositions containing fibres, filaments, whiskers, platelets, or the like, dispersed in a glass matrix
- C03C14/004—Glass compositions containing a non-glass component, e.g. compositions containing fibres, filaments, whiskers, platelets, or the like, dispersed in a glass matrix the non-glass component being in the form of particles or flakes
-
- 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
- C03C3/00—Glass compositions
- C03C3/04—Glass compositions containing silica
- C03C3/06—Glass compositions containing silica with more than 90% silica by weight, e.g. quartz
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2201/00—Type of glass produced
- C03B2201/06—Doped silica-based glasses
- C03B2201/20—Doped silica-based glasses doped with non-metals other than boron or fluorine
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B2201/00—Type of glass produced
- C03B2201/06—Doped silica-based glasses
- C03B2201/30—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi
- C03B2201/58—Doped silica-based glasses doped with metals, e.g. Ga, Sn, Sb, Pb or Bi doped with metals in non-oxide form, e.g. CdSe
-
- 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
- C03C2201/00—Glass compositions
- C03C2201/06—Doped silica-based glasses
- C03C2201/20—Doped silica-based glasses containing non-metals other than boron or halide
- C03C2201/26—Doped silica-based glasses containing non-metals other than boron or halide containing carbon
-
- 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
- C03C2214/00—Nature of the non-vitreous component
- C03C2214/30—Methods of making the composites
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Manufacturing & Machinery (AREA)
- Dispersion Chemistry (AREA)
- Ceramic Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Glass Melting And Manufacturing (AREA)
- Glass Compositions (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、炭化珪素含有シリカガ
ラス、およびその製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to silicon carbide-containing silica glass and a method for producing the same.
【0002】[0002]
【従来の技術】高強度、高剛性、耐熱性に優れた材料と
して炭素含有ガラスは期待され、現在盛んに研究されて
いる。これまでに報告されている炭素含有ガラスは、C
H3Si(OC2H5)3などを用いゾル−ゲル法により得
られたゲルを、不活性ガス中で焼結して得られた炭素含
有ガラスや、炭化ケイ素粉末とシリカ粉末との混合粉末
を溶融して得られている炭素含有ガラスなどがある。し
かしながら、ゾル−ゲル法により作製された炭素含有ガ
ラスにおいては、多量のOH基と多量の遊離炭素を含有
するため、耐熱性が良好でなく、また溶融法により作製
された炭素含有ガラスにおいては、1400℃以上の温
度で炭化ケイ素とシリカの反応に伴うガス発生のため
に、炭素含有ガラスを安定的に製造することが困難であ
る。2. Description of the Related Art Carbon-containing glass is expected as a material excellent in high strength, high rigidity and heat resistance, and is currently being actively researched. The carbon-containing glass reported so far is C
Carbon-containing glass obtained by sintering a gel obtained by a sol-gel method using H 3 Si (OC 2 H 5 ) 3 or the like in an inert gas, or a mixture of silicon carbide powder and silica powder For example, carbon-containing glass obtained by melting powder. However, in the carbon-containing glass produced by the sol-gel method, since it contains a large amount of OH groups and a large amount of free carbon, the heat resistance is not good, and in the carbon-containing glass produced by the melting method, It is difficult to stably produce a carbon-containing glass because of the gas generation accompanying the reaction between silicon carbide and silica at a temperature of 1400 ° C. or higher.
【0003】[0003]
【発明が解決しようとする課題】本発明は、高強度、高
剛性、耐熱性に優れたシリカガラスとして、OH基の含
有が少なく、遊離炭素を含まず、高密度である炭化珪素
含有シリカガラスと、それを安定的に製造する製造方法
を提供することを目的とするものである。DISCLOSURE OF THE INVENTION The present invention provides a silica glass having a high density, a high rigidity, and a high heat resistance, which contains a small amount of OH groups, does not contain free carbon, and has a high density. And a manufacturing method for stably manufacturing the same.
【0004】[0004]
【課題を解決するための手段】本発明者らは、上記の課
題を解決するために鋭意検討を行った結果、本発明を完
成するに至ったものである。The present inventors have completed the present invention as a result of intensive studies to solve the above problems.
【0005】すなわち本発明は、平均粒径が20nm以
下の炭化珪素微粒子を0.5〜10重量パーセントが分
散させたシリカガラスであって、含まれるOH基が50
ppm以下、遊離炭素が200ppm以下であり、かつ
密度が2.22〜2.30g/cm3であることを特徴
とする高密度炭化珪素含有シリカガラスである。以下、
本発明を更に詳細に説明する。That is, the present invention is a silica glass in which 0.5 to 10 weight percent of silicon carbide fine particles having an average particle size of 20 nm or less are dispersed, and the silica glass contains 50 OH groups.
It is a silica glass containing high density silicon carbide, characterized in that it is below ppm, free carbon below 200 ppm, and density is 2.22 to 2.30 g / cm 3 . Less than,
The present invention will be described in more detail.
【0006】本発明の炭化珪素含有シリカガラスの炭化
珪素分は、0.5〜10重量パーセントである。0.5
パ−セント未満の炭化珪素含有量では高強度、高剛性、
耐熱性に優れたシリカガラスにならない。また炭化珪素
分を10重量パーセントをこえて含有すると、炭化珪素
とシリカとの熱収縮の差が顕著に現れて、製造が困難に
なる。含有効果を得ることと安定的に製造するために、
1〜5重量パーセントの炭化珪素分を含有していること
が好ましい。The silicon carbide-containing silica glass of the present invention has a silicon carbide content of 0.5 to 10 weight percent. 0.5
If the silicon carbide content is less than percent, high strength, high rigidity,
Does not become silica glass with excellent heat resistance. Further, if the content of silicon carbide exceeds 10% by weight, the difference in heat shrinkage between silicon carbide and silica becomes prominent and the production becomes difficult. In order to obtain the effect of inclusion and to manufacture stably,
It preferably contains 1 to 5 weight percent of silicon carbide.
【0007】また、本発明の炭化珪素含有シリカガラス
中の遊離炭素は200ppm以下で、実質上は含有され
ていない。そのためガラス体の外観は、黒色ではなく淡
緑色を呈する。また遊離炭素を含まないため、酸化性雰
囲気中での加熱に対して安定で、例えば酸水素炎による
加熱においても発泡しにくい。Further, the free carbon in the silicon carbide-containing silica glass of the present invention is 200 ppm or less, which is substantially not contained. Therefore, the appearance of the glass body is not green but light green. In addition, since it does not contain free carbon, it is stable against heating in an oxidizing atmosphere and is unlikely to foam even when heated by, for example, an oxyhydrogen flame.
【0008】ガラス中に分散している炭化珪素は、X線
回折、NMRによって同定することができる。炭化珪素
微粒子の平均粒径は20nm以下で、通常は5〜10n
mである。20nmを越える大きな粒径の炭化珪素粒子
は、高温下でシリカガラス中に安定的に存在させること
が困難である。Silicon carbide dispersed in glass can be identified by X-ray diffraction and NMR. The average particle diameter of the silicon carbide fine particles is 20 nm or less, and usually 5 to 10 n.
m. Silicon carbide particles having a large particle size exceeding 20 nm are difficult to stably exist in silica glass at high temperatures.
【0009】本発明のシリカガラスでは、炭素はすべて
SiC或いはSiOxCyの形態で存在すると推定さ
れ、密度は2.22〜2.30g/cm3の高密度シリ
カガラスになる。In the silica glass of the present invention, it is presumed that all carbon is present in the form of SiC or SiOxCy, and a high density silica glass having a density of 2.22 to 2.30 g / cm 3 is obtained.
【0010】さらにまた、本発明の炭化珪素含有シリカ
ガラス中に含まれるOH基は、50ppm以下さらに好
ましくは30ppm以下である。ガラス中のOH基は耐
熱性を著しく低下させることが知られているが、OH基
が50ppm以下であれば、十分な耐熱性を有し、30
ppm以下であればさらに好ましいものである。Furthermore, the OH groups contained in the silica glass containing silicon carbide of the present invention is 50 ppm or less, more preferably 30 ppm or less. It is known that the OH group in glass significantly lowers the heat resistance, but if the OH group is 50 ppm or less, it has sufficient heat resistance,
It is more preferable if it is ppm or less.
【0011】また本発明は、上述の炭化珪素含有シリカ
ガラスを安定的に製造する方法である。即ち、シリカ微
粉末堆積体にオルガノクロロシランを気体として700
℃以上で吸着させ、ついで水素雰囲気中で焼成してオル
ガノクロロシランを炭化珪素化させ、得られた多孔質体
を非酸化性雰囲気中、1700℃以上の温度で処理して
緻密なガラスとすることを特徴とする、炭化珪素含有シ
リカガラスの製造方法である。以下、更に詳細に説明す
る。The present invention is also a method for stably producing the above silica glass containing silicon carbide. That is, it is possible to use the organochlorosilane gas as a gas in the silica fine powder deposit 700
Adsorb at ℃ or more, then calcinate in hydrogen atmosphere to convert organochlorosilane to silicon carbide, and treat the obtained porous body at a temperature of 1700 ° C or more in a non-oxidizing atmosphere to form a dense glass. And a method for producing silica glass containing silicon carbide. The details will be described below.
【0012】公知の方法により製造されたシリカ微粉末
堆積体に、オルガノクロロシランを気体として接触さ
せ、シリカ微粉末堆積体に吸着させる。オルガノクロロ
シランとしては、低級アルキル基を含むものが用いら
れ、例えば、メチル基やエチル基を含むもの、具体的に
はCH3SiCl3や(CH3)2SiCl2などがあげら
れる。これらをシリカ微粉末体積体に接触させるときの
濃度には特に限定はなく、オルガノクロロシランだけを
接触させてもよく、またヘリウムなどの不活性ガスを混
合し接触させても良い。接触・吸着時間はオルガノクロ
ロシラン濃度とのかねあいによるものであり、特に限定
はされない。Organochlorosilane as a gas is brought into contact with the silica fine powder deposit produced by a known method to be adsorbed on the silica fine powder deposit. As the organochlorosilane, those containing a lower alkyl group are used, and examples thereof include those containing a methyl group or an ethyl group, specifically CH 3 SiCl 3 and (CH 3 ) 2 SiCl 2 . There is no particular limitation on the concentration when these are brought into contact with the silica fine powder volume body, and only organochlorosilane may be brought into contact therewith, or an inert gas such as helium may be mixed and brought into contact therewith. The contact / adsorption time depends on the balance with the organochlorosilane concentration and is not particularly limited.
【0013】これにより、元のシリカ微粉末堆積体に存
在するOH基がオルガノクロロシランに置換され、OH
基が低減する。吸着させる温度は700℃以上である。
オルガノクロロシランの吸着量と分解、OH基の低減量
の点から800〜1000℃で行うことが好ましい。接
触時間は、30分以上が好ましい。また吸着させた後、
表面に吸着した過剰のオルガノクロロシランを除去する
ために、Heなどの不活性ガスを作用させてもよい。As a result, the OH groups present in the original silica fine powder deposits are replaced with organochlorosilanes,
The group is reduced. The adsorption temperature is 700 ° C. or higher.
It is preferably carried out at 800 to 1000 ° C. from the viewpoint of the adsorption amount and decomposition of organochlorosilane and the reduction amount of OH groups. The contact time is preferably 30 minutes or longer. After absorbing again,
An inert gas such as He may be applied to remove the excess organochlorosilane adsorbed on the surface.
【0014】次いで水素雰囲気中で焼成し、吸着したオ
ルガノクロロシランのCH3,C2H5などの有機基の部
分を還元して、炭化珪素化させる。この水素処理をしな
いとオルガノクロロシランを炭化珪素化出来ず、遊離炭
素が生成しやすくなり、高密度にならず、高強度、高剛
性、耐熱性に優れたシリカガラスにならない。水素処理
の温度は、好ましくは700℃以上であるが、炭化珪素
を十分に含有させるために、800〜1700℃である
ことがさらに好ましい。水素雰囲気中の水素濃度には特
に限定はなく、水素だけからなる雰囲気でもよく、また
ヘリウムなどの拡散係数が大きく、反応性を持たないガ
スと水素とを混合した雰囲気でもよい。Then, it is fired in a hydrogen atmosphere to reduce the adsorbed organochlorosilane portion of organic groups such as CH 3 and C 2 H 5 to form silicon carbide. Without this hydrogen treatment, the organochlorosilane cannot be converted to silicon carbide, free carbon is likely to be generated, the density will not be high, and the silica glass will not be excellent in high strength, high rigidity and heat resistance. The temperature of the hydrogen treatment is preferably 700 ° C. or higher, but more preferably 800 to 1700 ° C. in order to sufficiently contain silicon carbide. The hydrogen concentration in the hydrogen atmosphere is not particularly limited, and may be an atmosphere composed of only hydrogen, or an atmosphere in which hydrogen having a large diffusion coefficient such as helium and having no reactivity is mixed with hydrogen.
【0015】700℃以上の温度で前述の水素処理を行
ったシリカ微粉末堆積体は、1700℃未満の温度では
完全には緻密化しない。したがって、炭化珪素の酸化防
止のため非酸化性雰囲気中、1700℃以上の温度で溶
融し完全緻密化させ、本発明の炭化珪素含有シリカガラ
スを得ることができる。The silica fine powder deposit which has been subjected to the above-mentioned hydrogen treatment at a temperature of 700 ° C. or higher is not completely densified at a temperature of less than 1700 ° C. Therefore, the silicon carbide-containing silica glass of the present invention can be obtained by melting and completely densifying at a temperature of 1700 ° C. or higher in a non-oxidizing atmosphere to prevent the oxidation of silicon carbide.
【0016】[0016]
【実施例】本発明を更に詳細に説明するため、以下に実
施例を挙げるが、本発明はこれらに限定されるものでは
ない。EXAMPLES In order to explain the present invention in more detail, examples will be given below, but the present invention is not limited thereto.
【0017】(実施例1)火炎加水分解法により得られ
たシリカ微粉末堆積体を電気炉に装着し、He雰囲気中
で800℃まで昇温した。ついで、CH3SiCl3に8
00ml/minの速度でHeガスをバブリングさせた
ものを炉内へ導入し、炉内にCH3SiCl3を気体とし
て作用させながら1時間半保持した。ついでバブリング
を停止しCH3SiCl3の供給を停止して、Heガスの
みを供給しながら1時間保持した。Example 1 The silica fine powder deposit obtained by the flame hydrolysis method was mounted in an electric furnace and heated to 800 ° C. in a He atmosphere. Then add 8 to CH 3 SiCl 3 .
What bubbled He gas at a rate of 00 ml / min was introduced into the furnace, and was held for one and a half hours while CH 3 SiCl 3 acting as a gas in the furnace. Then, bubbling was stopped, supply of CH 3 SiCl 3 was stopped, and only He gas was supplied and held for 1 hour.
【0018】つづいて、H2ガス550ml/min,
及びHeガス230ml/minを供給し1450℃ま
で昇温し、この温度で1時間保持させてガラス化させ
た。得られたガラス体は多孔質状態であり、窒素雰囲気
中で1800℃まで昇温し1時間保持させて完全に緻密
化させた。Subsequently, H 2 gas of 550 ml / min,
And 230 ml / min of He gas were supplied, the temperature was raised to 1450 ° C., and this temperature was maintained for 1 hour for vitrification. The obtained glass body was in a porous state and was heated to 1800 ° C. in a nitrogen atmosphere and kept for 1 hour to be completely densified.
【0019】こうして得られたガラスは淡緑色を呈し、
X線回折により炭化珪素が含有されていることが判り、
含有量は1.3重量パーセントであった。TEM写真よ
り求めた炭化珪素の平均粒径は10nmであった。遊離
炭素は見当たらず密度は2.238g/cm3 であっ
た。また、IR吸収スペクトルによると、OH基は21
ppmであった。The glass thus obtained has a light green color,
X-ray diffraction reveals that it contains silicon carbide,
The content was 1.3 weight percent. The average particle size of silicon carbide obtained from the TEM photograph was 10 nm. No free carbon was found and the density was 2.238 g / cm 3 . Further, according to the IR absorption spectrum, the OH group is 21
It was ppm.
【0020】(実施例2,3)CH3SiCl3処理、H
2処理条件を表1に記載のように変えて、同様のガラス
作製実験を行った。結果を表1に示す。いずれの実施例
においても、得られたガラスは淡緑色を呈し、X線回折
により炭化珪素が含有されていることが判り、遊離炭素
は見当たらなかった。またいずれの実施例においても、
IR吸収スペクトルによるOH基は10ppm、TEM
写真より求めた炭化珪素の平均粒径は10nmであっ
た。(Examples 2 and 3) CH 3 SiCl 3 treatment, H
2 The same glass making experiment was conducted by changing the treatment conditions as shown in Table 1. The results are shown in Table 1. In each of the examples, the obtained glass was light green, and it was found by X-ray diffraction that silicon carbide was contained, and no free carbon was found. Also, in any of the examples,
OH group is 10 ppm by IR absorption spectrum, TEM
The average particle size of silicon carbide obtained from the photograph was 10 nm.
【0021】(比較例1)火炎加水分解法により得られ
たシリカ微粉末堆積体を電気炉に装着し、He雰囲気中
で650℃まで昇温した。ついで、CH3SiCl3に8
00ml/minの速度でHeガスをバブリングさせた
ものを炉内に導入し、炉内にCH3SiCl3を気体とし
て作用させながら1時間保持した。ついで、バブリング
を停止し、CH3SiCl3の供給を停止してHeガスの
みを供給しながら1時間保持した。(Comparative Example 1) The silica fine powder deposit obtained by the flame hydrolysis method was mounted in an electric furnace and heated to 650 ° C in a He atmosphere. Then add 8 to CH 3 SiCl 3 .
A bubbling He gas at a rate of 00 ml / min was introduced into the furnace, and the furnace was kept for 1 hour while CH 3 SiCl 3 acting as a gas. Then, bubbling was stopped, supply of CH 3 SiCl 3 was stopped, and only He gas was supplied and held for 1 hour.
【0022】つづいて、H2ガス550ml/min,
およびHeガス230ml/minを供給し1450℃
まで昇温し、この温度で1時間保持し、緻密なガラスを
得た。こうして得られたガラスは黒色を呈し、0.03
重量パーセントの遊離炭素が含有されていたが、X線回
折によると炭化珪素は認められなかった。密度は2.2
02g/cm3であった。また、IR吸収スペクトルに
よると、OH基は30ppmであった。Subsequently, H 2 gas of 550 ml / min,
And He gas of 230 ml / min are supplied and 1450 ° C
The temperature was raised up to and maintained at this temperature for 1 hour to obtain a dense glass. The glass thus obtained has a black color and is 0.03
It contained weight percent free carbon but no silicon carbide was observed by X-ray diffraction. Density is 2.2
It was 02 g / cm 3 . Further, according to the IR absorption spectrum, the OH group was 30 ppm.
【0023】(比較例2)火炎加水分解法により得られ
たシリカ微粉末堆積体を電気炉に装着し、He雰囲気中
で700℃まで昇温した。ついで、CH3SiCl3に8
00ml/minの速度でHeガスをバブリングさせた
ものを炉内へ導入し、炉内にCH3SiCl3を気体とし
て作用させながら1時間保持した。ついでバブリングを
停止し、CH3SiCl3の供給を停止してHeガスのみ
を供給しながら1時間保持した。Comparative Example 2 A silica fine powder deposit obtained by the flame hydrolysis method was mounted in an electric furnace and heated to 700 ° C. in a He atmosphere. Then add 8 to CH 3 SiCl 3 .
What bubbled He gas at a rate of 00 ml / min was introduced into the furnace, and the furnace was kept for 1 hour while CH 3 SiCl 3 acting as a gas. Then, bubbling was stopped, supply of CH 3 SiCl 3 was stopped, and only He gas was supplied and maintained for 1 hour.
【0024】つづいて、Heガスのみを230ml/m
in供給し1450℃まで昇温し、この温度で1時間保
持させ、緻密なガラスを得た。Subsequently, only He gas was added at 230 ml / m.
In was supplied, the temperature was raised to 1450 ° C., and the temperature was maintained for 1 hour to obtain a dense glass.
【0025】こうして得られたガラスは黒色を呈し、
0.04重量パーセントの遊離炭素が含有されていたが
X線回折によると炭化珪素は認められなかった。密度は
2.205g/cm3であった。また、IR吸収スペク
トルによると、OH基は30ppmであった。The glass thus obtained has a black color,
It contained 0.04 weight percent free carbon but no silicon carbide was observed by X-ray diffraction. The density was 2.205 g / cm 3 . Further, according to the IR absorption spectrum, the OH group was 30 ppm.
【0026】[0026]
【表1】 [Table 1]
【0027】[0027]
【発明の効果】以上詳述したように、本発明の方法によ
り、遊離炭素を含まず、OH基の含有が少なく、高密度
であり、高強度、高剛性、耐熱性に優れた本発明の炭化
珪素含有シリカガラスを安定的に作製することができ
る。As described in detail above, according to the method of the present invention, free carbon is not contained, the content of OH groups is small, the density is high, and the strength, rigidity and heat resistance of the present invention are excellent. It is possible to stably produce silicon carbide-containing silica glass.
Claims (2)
を0.5〜10重量パーセントが分散させたシリカガラ
スであって、含まれるOH基が50ppm以下、遊離炭
素が200ppm以下であり、かつ密度が2.22〜
2.30g/cm3であることを特徴とする、高密度炭
化珪素含有シリカガラス。1. A silica glass in which 0.5 to 10% by weight of silicon carbide fine particles having an average particle diameter of 20 nm or less are dispersed, the OH groups contained in the silica glass are 50 ppm or less, and the free carbon is 200 ppm or less, and Density is 2.22
2.30 g / cm 3 of high density silicon carbide-containing silica glass.
ンを気体として700℃以上で吸着させ、ついで水素雰
囲気中で焼成してオルガノクロロシランを炭化珪素化さ
せ、得られた多孔質体を非酸化性雰囲気中、1700℃
以上の温度で処理して緻密なガラスとすることを特徴と
する、請求項1に記載の炭化珪素含有シリカガラスの製
造方法。2. A silica fine powder deposit is adsorbed with organochlorosilane as a gas at a temperature of 700 ° C. or higher, and then fired in a hydrogen atmosphere to convert the organochlorosilane into silicon carbide, and the resulting porous body is subjected to a non-oxidizing atmosphere. Medium 1700 ° C
The method for producing silicon carbide-containing silica glass according to claim 1, wherein the glass is treated at the above temperature to obtain a dense glass.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27626092A JPH06122533A (en) | 1992-10-14 | 1992-10-14 | Silica glass containing silicon carbide and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27626092A JPH06122533A (en) | 1992-10-14 | 1992-10-14 | Silica glass containing silicon carbide and its production |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06122533A true JPH06122533A (en) | 1994-05-06 |
Family
ID=17566955
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27626092A Pending JPH06122533A (en) | 1992-10-14 | 1992-10-14 | Silica glass containing silicon carbide and its production |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06122533A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004050570A1 (en) | 2002-11-29 | 2004-06-17 | Shin-Etsu Quartz Products Co., Ltd. | Method for producing synthetic quartz glass and synthetic quartz glass article |
KR100653004B1 (en) * | 2004-02-23 | 2006-12-01 | 가부시키가이샤 고베 세이코쇼 | Two-phase glass-like carbon member and method of manufacturing the same |
WO2008105191A1 (en) * | 2007-02-27 | 2008-09-04 | Shin-Etsu Quartz Products Co., Ltd. | Black synthetic quartz glass and process for producing the black synthetic quartz glass |
JP2008280247A (en) * | 2002-07-31 | 2008-11-20 | Shinetsu Quartz Prod Co Ltd | Synthetic quartz glass body |
-
1992
- 1992-10-14 JP JP27626092A patent/JPH06122533A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008280247A (en) * | 2002-07-31 | 2008-11-20 | Shinetsu Quartz Prod Co Ltd | Synthetic quartz glass body |
WO2004050570A1 (en) | 2002-11-29 | 2004-06-17 | Shin-Etsu Quartz Products Co., Ltd. | Method for producing synthetic quartz glass and synthetic quartz glass article |
EP1580170A1 (en) * | 2002-11-29 | 2005-09-28 | Shin-Etsu Quartz Products Co., Ltd. | Method for producing synthetic quartz glass and synthetic quartz glass article |
EP1580170A4 (en) * | 2002-11-29 | 2011-12-28 | Shinetsu Quartz Prod | Method for producing synthetic quartz glass and synthetic quartz glass article |
KR100653004B1 (en) * | 2004-02-23 | 2006-12-01 | 가부시키가이샤 고베 세이코쇼 | Two-phase glass-like carbon member and method of manufacturing the same |
WO2008105191A1 (en) * | 2007-02-27 | 2008-09-04 | Shin-Etsu Quartz Products Co., Ltd. | Black synthetic quartz glass and process for producing the black synthetic quartz glass |
JP5312313B2 (en) * | 2007-02-27 | 2013-10-09 | 信越石英株式会社 | Black synthetic quartz glass and manufacturing method thereof |
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