JPH0218400A - Device for producing si-based whisker - Google Patents
Device for producing si-based whiskerInfo
- Publication number
- JPH0218400A JPH0218400A JP16927288A JP16927288A JPH0218400A JP H0218400 A JPH0218400 A JP H0218400A JP 16927288 A JP16927288 A JP 16927288A JP 16927288 A JP16927288 A JP 16927288A JP H0218400 A JPH0218400 A JP H0218400A
- Authority
- JP
- Japan
- Prior art keywords
- cylinder
- raw material
- whiskers
- reaction
- gas
- 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
- 239000002994 raw material Substances 0.000 claims abstract description 47
- 238000006243 chemical reaction Methods 0.000 claims abstract description 40
- 238000010438 heat treatment Methods 0.000 claims abstract description 16
- 239000007787 solid Substances 0.000 claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 claims description 26
- 238000004891 communication Methods 0.000 claims description 9
- 239000007789 gas Substances 0.000 abstract description 30
- 238000007790 scraping Methods 0.000 abstract description 8
- 239000012159 carrier gas Substances 0.000 abstract description 5
- 229910052581 Si3N4 Inorganic materials 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 4
- 239000003610 charcoal Substances 0.000 abstract description 3
- 229940087654 iron carbonyl Drugs 0.000 abstract description 2
- 239000000376 reactant Substances 0.000 abstract 3
- 230000003197 catalytic effect Effects 0.000 abstract 1
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 description 19
- 239000012495 reaction gas Substances 0.000 description 8
- 239000003054 catalyst Substances 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 241000209094 Oryza Species 0.000 description 3
- 235000007164 Oryza sativa Nutrition 0.000 description 3
- 239000010903 husk Substances 0.000 description 3
- 235000009566 rice Nutrition 0.000 description 3
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 3
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000005121 nitriding Methods 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 229910052990 silicon hydride Inorganic materials 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Crystals, And After-Treatments Of Crystals (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は窒化珪素(Si3N4)ウィスカー炭化珪素(
SiC)ウィスカー等のSi系ウィスカーの製造装置に
関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to silicon nitride (Si3N4) whisker silicon carbide (
The present invention relates to an apparatus for producing Si-based whiskers such as SiC whiskers.
Si系ウィスカーは原料である一酸化珪素(Si0)と
メタン(CH,)、窒素(N2)またはアンモニアガス
(NH3)等の反応ガスとの反応によって合成されるも
のである。このSi系ウィスカーの製造装置としては、
例えば特開昭61−14200号公報及び特公昭47−
18531号公報に開示されているものがある。Si-based whiskers are synthesized by reacting raw material silicon monoxide (Si0) with a reactive gas such as methane (CH, ), nitrogen (N2), or ammonia gas (NH3). The manufacturing equipment for this Si-based whisker is as follows:
For example, JP-A-61-14200 and JP-A-47-
There is one disclosed in Japanese Patent No. 18531.
前者は原料充填容器の上部に炭素反応管を連通接続し、
原料からの一酸化珪素(S i O)を反応ガスと一緒
に前記反応管内に送り込み、この反応管内の内周面にウ
ィスカーを成長させるものである。また後者は、断熱材
を内張すした加熱炉内に原料充填容器、加熱電極および
ウィスカー成長用反応部材を配設し、原料からの一酸化
珪素(SiO)と炉内へ供給された反応ガスとを反応さ
せ、前記反応部材の表面にウィスカーを成長させるもの
である。In the former, a carbon reaction tube is connected to the top of the raw material filling container,
Silicon monoxide (S i O) from a raw material is fed into the reaction tube together with a reaction gas, and whiskers are grown on the inner peripheral surface of the reaction tube. In addition, in the latter case, a raw material filling container, a heating electrode, and a reaction member for whisker growth are arranged in a heating furnace lined with a heat insulating material, and silicon monoxide (SiO) from the raw material and a reaction gas supplied to the furnace are and to grow whiskers on the surface of the reaction member.
(発明が解決しようとする課題〕
しかしながらこれら従来の製造装置によるウィスカー製
造は、容器内に所定量の原料を充填し、この原料による
ウィスカー生成が完了した時点で装置を一旦停止させ、
生成ウィスカーを取り出して新たな原料を再び容器内に
充填するというバッチ操業であるため、ウィスカー生産
効率が悪いという問題がある。(Problems to be Solved by the Invention) However, in whisker production using these conventional production devices, a predetermined amount of raw material is filled into a container, and when whisker production using this raw material is completed, the device is temporarily stopped.
Since it is a batch operation in which generated whiskers are taken out and new raw materials are filled into the container again, there is a problem of poor whisker production efficiency.
また、前者では充填容器部の内壁表面に、後者では炉の
内壁表面にウィスカーが生成し、回収効率が低下すると
いう問題がある。In addition, whiskers are generated on the inner wall surface of the filling container portion in the former case, and whiskers are generated on the inner wall surface of the furnace in the latter case, resulting in a reduction in recovery efficiency.
そこで本発明は装置を途中で一旦停止させる必要なくし
て連続的にウィスカーを生産でき、しかも生成したウィ
スカーの回収効率を従来装置におけるよりも高くするこ
とができるSi系ウィスカー製造装置を提供することを
目的とする。SUMMARY OF THE INVENTION Therefore, the present invention aims to provide a Si-based whisker manufacturing apparatus that can produce whiskers continuously without the need to temporarily stop the apparatus midway through the production process, and that can collect the generated whiskers more efficiently than in conventional apparatuses. purpose.
本発明は前記目的にしたがい、内部に固体原料受は用多
孔部材を有する反応筒とウィスカーを生成させる生成筒
とを加熱炉内に設置し、前記加熱炉内において前記両筒
を連通管にて接続して原料ガスを前記連通管を通して生
成湾内に流入させるようにするとともに、前記反応筒に
は原料供給装置を設け、前記生成筒にはウィスカー掻き
押し装置を設けてなることを特徴とするSi系ウィスカ
ー製造装置を提供するものである。In accordance with the above-mentioned object, the present invention includes a reaction tube having a porous member for solid material receiving therein and a generation tube for generating whiskers, which are installed in a heating furnace, and the two tubes are connected in the heating furnace by a communicating tube. The silicon hydride is connected to allow raw material gas to flow into the production bay through the communication pipe, and the reaction tube is provided with a raw material supply device, and the production tube is provided with a whisker pushing device. The present invention provides an apparatus for manufacturing whiskers.
〔作 用]
本発明ウィスカー製造装置によると、加熱によって気化
SiOを発生する固体原料が原料供給装置によって反応
筒内へ供給され、ここで加熱されてガス状に気化したS
iOを発生し、該SiOが雰囲気ガス供給部から供給さ
れたガスとともに連通管を通って生成筒へ入り、ここで
窒化反応、炭化反応等の反応を起こして生成筒の内壁面
にウィスカーを生成する。生成されたウィスカーはウィ
スカー掻き押し装置により生成筒内壁面から掻き落とさ
れつつウィスカー取出し部へ押しやられ、そこから取り
出される。[Function] According to the whisker manufacturing apparatus of the present invention, the solid raw material that generates vaporized SiO by heating is supplied into the reaction column by the raw material supply device, and the solid raw material that generates vaporized SiO by heating is supplied into the reaction column, where S is heated and vaporized into a gaseous state.
iO is generated, and the SiO enters the generation cylinder through a communication pipe together with the gas supplied from the atmospheric gas supply section, where reactions such as nitriding and carbonization reactions occur to generate whiskers on the inner wall surface of the generation cylinder. do. The generated whiskers are scraped off from the inner wall surface of the generation cylinder by the whisker scraping device and pushed to the whisker extraction section, where they are extracted.
前記反応筒内には、その中の原料の減少に見合った量の
新しい原料が原料供給装置によって次々と供給され、生
成筒においてはウィスカーが連続的に生成される。New raw materials are successively supplied into the reaction column by a raw material supply device in an amount commensurate with the decrease in the raw materials in the reaction column, and whiskers are continuously produced in the production column.
以下、本発明の実施例を図面を参照して説明する。 Embodiments of the present invention will be described below with reference to the drawings.
図面は一実施例ウィスカー製造装置の断面を示している
。The drawing shows a cross-section of one embodiment of the whisker manufacturing apparatus.
図において、10は加熱炉で、炉lOは断熱材11が内
張すされ、内部に電熱ヒータ12が設けられている。In the figure, 10 is a heating furnace, and the furnace IO is lined with a heat insulating material 11, and an electric heater 12 is provided inside.
また、この加熱炉10には、縦型反応筒1及び縦型生成
筒2が平行に設置されている。これら両筒はその上下端
部が加熱炉lOより外へ突き出している。反応筒1及び
生成筒2は加熱炉10の底部において連通管3により互
いに連通している。Further, in this heating furnace 10, a vertical reaction tube 1 and a vertical generation tube 2 are installed in parallel. The upper and lower ends of both cylinders protrude outside of the heating furnace IO. The reaction tube 1 and the production tube 2 communicate with each other through a communication tube 3 at the bottom of the heating furnace 10.
反応筒lは前記連通管よりやや高位置において内部に原
料を受は止める多孔板等からなる多孔部材4を備えてい
る。The reaction tube 1 is provided with a porous member 4 made of a perforated plate or the like for receiving and stopping raw materials at a position slightly higher than the communication tube.
反応筒lの上端部にはシール材5を介してキャップ6A
が取り外し可能に設けられており、このキャップに原料
供給装置20が接続されている。A cap 6A is attached to the upper end of the reaction tube l via a sealing material 5.
is removably provided, and a raw material supply device 20 is connected to this cap.
原料供給装置20はキャップ6Aを貫通する筒体21お
よびこれにシール機構を有するフィーダ、例えばロータ
リーパルプ22を介して接続された原料ホッパ23とか
らなっている。筒体21は加熱炉lO内まで延びている
。この筒体21には雰囲気ガス供給管24が接続されて
いる。The raw material supply device 20 includes a cylindrical body 21 passing through the cap 6A and a raw material hopper 23 connected to this via a feeder having a sealing mechanism, such as a rotary pulp 22. The cylindrical body 21 extends into the heating furnace IO. An atmospheric gas supply pipe 24 is connected to this cylinder 21 .
該供給管24は分岐されていて、一方は原料供給装置2
0の筒体21に、他方はキャップ6Aにそれぞれ接続さ
れており、本例では図示しないガス供給源からキャリア
ガス及び反応ガスを供給される。The supply pipe 24 is branched, and one side is connected to the raw material supply device 2.
0 and the other to the cap 6A, and in this example, a carrier gas and a reaction gas are supplied from a gas supply source (not shown).
また反応筒lの下端にはキャップ7Aが取り外し可能に
設けられており、雰囲気ガス供給管25が該キャップ7
Aを貫通して筒l内へ挿入設置されており1.そのガス
噴出口25Aは°連通管3の入口に向いている。このガ
ス供給管25には本例では図示しないガス源から反応ガ
ス及び触媒ガスが供給される。Further, a cap 7A is removably provided at the lower end of the reaction cylinder l, and an atmospheric gas supply pipe 25 is connected to the cap 7A.
It is installed by penetrating A and being inserted into the cylinder l.1. The gas outlet 25A faces the inlet of the communication pipe 3. A reaction gas and a catalyst gas are supplied to this gas supply pipe 25 from a gas source (not shown) in this example.
生成筒2の上端部にはウィスカー取出しのための開閉自
在扉8が設けられているとともに排気管9が設けられて
いる。An openable/closable door 8 for removing whiskers is provided at the upper end of the generation cylinder 2, and an exhaust pipe 9 is provided.
生成筒2の下端部にはウィスカー掻き押し装置30が設
けられている。A whisker scraping device 30 is provided at the lower end of the generating cylinder 2.
装置30は生成筒2内を摺動可能に昇降する掻き押しピ
ストン31、該ピストンに連結されたロッド32及び該
ロッド32を往復駆動させる駆動袋rt33からなって
いる。ロッド32は筒2下端の取り外し可能ボトムキャ
ップ7Bを貫通している。駆動装置33はチェーン34
を含み、該チェーン34は一部がロッド32の下端に連
結され、二つのスプロケット35.36に巻き掛けられ
、一方のスプロケットが図示しないモータにて回される
ことにより往復回動でき、これによってロッド32、従
ってピストン31が昇降する。The device 30 consists of a scraping piston 31 that slides up and down within the production cylinder 2, a rod 32 connected to the piston, and a drive bag rt33 that drives the rod 32 back and forth. The rod 32 passes through a removable bottom cap 7B at the lower end of the tube 2. The drive device 33 is a chain 34
A part of the chain 34 is connected to the lower end of the rod 32, and is wound around two sprockets 35 and 36, and can be rotated back and forth by rotating one of the sprockets by a motor (not shown). The rod 32 and therefore the piston 31 move up and down.
この実施例ウィスカー製造装置によると、原料供給装置
20のホッパ23内に加熱によって気化SiOを発生す
る固体原料Aが入れられ、該原料はロータリーバルブ2
2の開成によって筒体21から反応筒l内の多孔板4に
落下、充填される。According to the whisker manufacturing apparatus of this embodiment, a solid raw material A that generates vaporized SiO by heating is put into the hopper 23 of the raw material supply device 20, and the raw material is fed to the rotary valve 22.
2, it falls from the cylinder 21 into the perforated plate 4 inside the reaction cylinder 1 and is filled.
この例においては、固体原料として籾殻燻炭が使用され
る。In this example, rice husk charcoal is used as the solid raw material.
原料Aは反応による減少量だけ、逐次ロータリーパルプ
22を開成して、反応筒l内へ供給される。The raw material A is supplied into the reaction cylinder 1 by successively opening the rotary pulp 22 in an amount corresponding to the amount reduced by the reaction.
反応筒1は通常1300−1400°Cに加熱され、籾
殻燻炭原料A自身に含まれる炭素によって同原料に含ま
れるSingが還元され、SiOとなるとともに、該S
iOはガス供給管24からの反応ガスおよびキャリアガ
スとともに多孔部材4の下方に送り込まれ、反応筒lの
底部空間に設けられたガス供給管25から送入された触
媒ガスおよび反応ガスと一緒に連通管3を通って生成筒
2に入る。The reaction tube 1 is normally heated to 1300-1400°C, and Sing contained in the rice husk smoky coal raw material A is reduced by the carbon contained in the raw material A, becoming SiO, and the S
iO is sent below the porous member 4 together with the reaction gas and carrier gas from the gas supply pipe 24, and together with the catalyst gas and reaction gas sent from the gas supply pipe 25 provided in the bottom space of the reaction tube l. It passes through the communication pipe 3 and enters the production cylinder 2.
これ等のガスは通常1350〜1450℃に加熱された
生成筒2において窒化反応、炭化反応等を起こし、生成
筒2の内壁面にウィスカーBを生成する。These gases usually undergo nitriding reactions, carbonization reactions, etc. in the production cylinder 2 heated to 1350 to 1450°C, and generate whiskers B on the inner wall surface of the production cylinder 2.
ウィスカーBが十分に生成したところで掻き押し装置3
0のピストン31を上昇させてウィスカーBを掻き落と
しつつ上方へ押し上げ、キャップ6Bの空間部に綿状体
ウィスカーCとして蓄える。When enough whiskers B have been generated, the scraping device 3
The piston 31 of No. 0 is raised and pushed upward while scraping off the whiskers B, and is stored as flocculent whiskers C in the space of the cap 6B.
余剰のおよび/または不要なガスは排気管9から外へ放
出される。Excess and/or unnecessary gas is discharged to the outside through the exhaust pipe 9.
キャップ6Bの空間部に十分にウィスカーが蓄積すると
扉8が開かれて取り出される。When enough whiskers have accumulated in the space of the cap 6B, the door 8 is opened and the cap 6B is taken out.
前記実施例において、窒化珪素ウィスカーを得る場合に
は、ガス供給管24からは反応ガスとして例えばNtま
たはNH,を、キャリアガスとして例えばHzを供給し
、ガス供給管25からは反応ガスとして例えばNtまた
はNH,を、触媒ガスとして鉄カルボニールを供給すれ
ばよい。In the embodiment described above, when obtaining silicon nitride whiskers, the reaction gas such as Nt or NH is supplied from the gas supply pipe 24 and the carrier gas is, for example, Hz, and the reaction gas is supplied from the gas supply pipe 25 such as Nt or NH. Alternatively, iron carbonyl may be supplied as a catalyst gas.
また、炭化珪素ウィスカーを得る場合には、ガス供給管
24からは反応ガスとして例えばCHsを、キャリアガ
スとして例えばH2を供給し、ガス供給管25からは反
応ガスとして例えばCHaを、触媒ガスとして鉄カルボ
ニールを供給すればよい。In addition, when obtaining silicon carbide whiskers, from the gas supply pipe 24, for example, CHs is supplied as a reactive gas, and for example, H2 is supplied as a carrier gas, and from the gas supply pipe 25, for example, CHa is supplied as a reactive gas, and iron is supplied as a catalyst gas. Just supply carbonyl.
なお、固体原料としては、前記籾殻燻炭のほか、Sin
、とカーボン粉からなるフレーク状混合物等を採用でき
る。In addition to the above-mentioned rice husk smoked charcoal, the solid raw materials include
, and a flake-like mixture consisting of carbon powder.
前記実施例によると、次のような利点がある。According to the embodiment described above, there are the following advantages.
■ 固体原料Aの反応気化のための反応筒1とウィスカ
ー生成筒2とが分離しているので、反応筒l内への原料
供給が原料の還元反応量に対応して行なうことができ、
それだけ装置稼働効率が向上するとともに、自動化が可
能となる。前記実施例は反応筒1が縦型であるから特に
原料供給には好都合である。- Since the reaction tube 1 for reaction vaporization of the solid raw material A and the whisker generation tube 2 are separated, the raw material can be supplied into the reaction tube 1 in accordance with the amount of reduction reaction of the raw material.
This improves the operating efficiency of the equipment and enables automation. In the above embodiment, since the reaction column 1 is vertical, it is particularly convenient for supplying raw materials.
■ 生成筒2の内壁面に生成するウィスカーBを装置を
停止させることなく、しかも略その全量を取り出すこと
ができ、それだけ装置稼働効率を上げることができると
ともにウィスカー回収効率を上げることができる。(2) Almost all of the whiskers B generated on the inner wall surface of the generation cylinder 2 can be taken out without stopping the apparatus, and the operating efficiency of the apparatus can be increased accordingly, as well as the whisker recovery efficiency.
■ 筒l及び2が縦型であるとともにキャップ6A、6
B、?A、7Bが取り外し可能となっていることも手伝
って原料の残さ処理等、反応塔および生成基の清掃を容
易に行え、装置のメインテナンスがそれだけ容易となっ
ている。■ The cylinders 1 and 2 are vertical, and the caps 6A and 6
B.? The fact that A and 7B are removable also makes it easy to clean the reaction tower and production group, such as processing residual raw materials, making the maintenance of the apparatus that much easier.
■ 反応筒l内の雰囲気が原料の上部から下部へ流れる
ので、還元分解された5ill気を効率よく生成基2へ
導くことができる。(2) Since the atmosphere inside the reaction tube 1 flows from the upper part of the raw material to the lower part, the 5ill gas that has been reductively decomposed can be efficiently guided to the production group 2.
なお本発明は前記実施例に限定されるものではなく、他
にも様々の態様で実施することができる。Note that the present invention is not limited to the above-mentioned embodiments, and can be implemented in various other ways.
例えば、反応筒及び生成筒はかならずしも縦型である必
要はなく、例えば水平に横に配置されていてもよい。こ
のような場合には、原料供給装置として、例えば反応筒
内へ挿入したスクリューコンベアの一端部に原料ホッパ
を設け、該ホッパ内原料を反応筒内原料の減少に応じて
随時該コンベアにて筒内へ供給するようにしてもよい。For example, the reaction cylinder and the production cylinder do not necessarily have to be vertical, and may be arranged horizontally, for example. In such a case, as a raw material supply device, for example, a raw material hopper is provided at one end of a screw conveyor inserted into the reaction cylinder, and the raw material in the hopper is transferred to the cylinder from time to time according to the decrease in the raw material in the reaction cylinder. It may also be supplied inside.
[発明の効果]
本発明によると、装置を途中で一旦停止させる必要なく
して連続的にウィスカーを生産でき、しかも生成したウ
ィスカーの回収効率を従来装置におけるよりも高くする
ことができるSi系ウィスカー製造装置を提供すること
ができる。[Effects of the Invention] According to the present invention, Si-based whisker production is possible, in which whiskers can be produced continuously without the need to temporarily stop the device, and the recovery efficiency of generated whiskers can be made higher than in conventional devices. equipment can be provided.
図面は一実施例の断面図である。 10・・・加熱炉、 l・・・反応筒、 2・・・生成筒、 3・・・連通管、 4・・・多孔部材、 20・・・原料供給装置、 24.25・・・雰囲気ガス供給管、 30・・・ウィスカー掻き押し装置、 8・・・ウィスカー取出し用扉、 A・・・固体原料、 B、C・・・ウィスカー The drawing is a cross-sectional view of one embodiment. 10... heating furnace, l...reaction tube, 2...Generation cylinder, 3...Communication pipe, 4... Porous member, 20...raw material supply device, 24.25...atmosphere gas supply pipe, 30... whisker scraping device, 8...Whisker removal door, A...solid raw material, B, C...whisker
Claims (1)
ウィスカーを生成させる生成筒とを加熱炉内に設置し、
前記加熱炉内において前記両筒を連通管にて接続して気
化SiOを前記連通管を通して生成筒内に流入させるよ
うにするとともに、前記反応筒には原料供給装置を設け
、前記生成筒にはウィスカー掻き押し装置を設けてなる
ことを特徴とするSi系ウィスカー製造装置。(1) A reaction cylinder having a porous member for receiving solid raw material inside and a generation cylinder for generating whiskers are installed in a heating furnace,
In the heating furnace, the two cylinders are connected by a communication pipe so that vaporized SiO flows into the production cylinder through the communication pipe, and the reaction cylinder is provided with a raw material supply device, and the production cylinder is provided with a raw material supply device. 1. A Si-based whisker manufacturing device characterized by being equipped with a whisker pushing device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16927288A JPH0218400A (en) | 1988-07-07 | 1988-07-07 | Device for producing si-based whisker |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16927288A JPH0218400A (en) | 1988-07-07 | 1988-07-07 | Device for producing si-based whisker |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0218400A true JPH0218400A (en) | 1990-01-22 |
Family
ID=15883433
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16927288A Pending JPH0218400A (en) | 1988-07-07 | 1988-07-07 | Device for producing si-based whisker |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0218400A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61219800A (en) * | 1985-03-26 | 1986-09-30 | Toyota Motor Corp | Production of silicon carbide whisker |
JPS63103899A (en) * | 1986-10-22 | 1988-05-09 | Fuji Electric Co Ltd | Silicon carbide whisker manufacturing method and manufacturing device |
-
1988
- 1988-07-07 JP JP16927288A patent/JPH0218400A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61219800A (en) * | 1985-03-26 | 1986-09-30 | Toyota Motor Corp | Production of silicon carbide whisker |
JPS63103899A (en) * | 1986-10-22 | 1988-05-09 | Fuji Electric Co Ltd | Silicon carbide whisker manufacturing method and manufacturing device |
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