JPH0634276A - Device for pressurized self-combustion synthesis oxidizing atmosphere - Google Patents
Device for pressurized self-combustion synthesis oxidizing atmosphereInfo
- Publication number
- JPH0634276A JPH0634276A JP4186946A JP18694692A JPH0634276A JP H0634276 A JPH0634276 A JP H0634276A JP 4186946 A JP4186946 A JP 4186946A JP 18694692 A JP18694692 A JP 18694692A JP H0634276 A JPH0634276 A JP H0634276A
- Authority
- JP
- Japan
- Prior art keywords
- heater
- self
- combustion
- insulating
- ignition
- 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.)
- Granted
Links
Landscapes
- Furnace Housings, Linings, Walls, And Ceilings (AREA)
- Furnace Details (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、加圧自己燃焼合成法に
よるセラミックスの合成装置の改良に関し、特に酸化雰
囲気中での加圧自己燃焼合成法により酸化物セラミック
スを合成する装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to improvement of a ceramics synthesizing apparatus by a pressure self-combustion synthesis method, and more particularly to an apparatus for synthesizing oxide ceramics by a pressure self-combustion synthesis method in an oxidizing atmosphere. .
【0002】[0002]
【従来の技術】材料粉末を自己燃焼させてセラミックス
を合成する自己燃焼合成法が、セラミックスの有力な製
造方法として注目されてきた。特に、圧力ガス媒体中で
材料粉末を加圧しながら自己燃焼させる加圧自己燃焼合
成法は、さらに優れた緻密性を持つセラミックスを製造
することが出来るという利点を有する。2. Description of the Related Art The self-combustion synthesis method, in which material powder is self-combusted to synthesize ceramics, has attracted attention as a promising method for producing ceramics. In particular, the pressurized self-combustion synthesis method, in which the material powder is self-combusted while being pressurized in a pressure gas medium, has the advantage of being able to produce ceramics with even higher density.
【0003】この加圧自己燃焼合成法において、アルゴ
ン、窒素、酸素など各種圧力ガス媒体を使用することに
よつて、セラミックス材料の安定性および生成セラミッ
クスの特性を制御することが可能であり、高圧下での雰
囲気制御が重要な技術的課題になつている。In this pressurized self-combustion synthesis method, it is possible to control the stability of the ceramic material and the characteristics of the produced ceramic by using various pressure gas media such as argon, nitrogen and oxygen. Atmosphere control below has become an important technical issue.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、この加
圧自己燃焼合成法を実施する装置は、主として熱間等方
圧プレスを改造したものが使われてきた。反応容器には
窒化ホウ素などを使用し、ヒーターにはグラファイトな
どを使用するため、圧力ガス媒体はアルゴン、窒素など
の不活性ガスが使用される。したがつて、炉室内は還元
雰囲気であり、非酸化物系セラミックス等の製造に使用
されてきた。However, as the apparatus for carrying out the pressurized self-combustion synthesis method, a hot hot isostatic press modified is mainly used. Since boron nitride or the like is used for the reaction vessel and graphite or the like is used for the heater, an inert gas such as argon or nitrogen is used as the pressure gas medium. Therefore, the furnace chamber has a reducing atmosphere and has been used for manufacturing non-oxide ceramics and the like.
【0005】このような加圧自己燃焼合成装置では、酸
化雰囲気で焼結を行う酸化物セラミックスなどを製造す
ることが出来なかつた。With such a pressurized self-combustion synthesizer, it has been impossible to manufacture oxide ceramics or the like that are sintered in an oxidizing atmosphere.
【0006】本発明の目的は、酸化雰囲気中で加圧自己
燃焼合成法により酸化物セラミックスを合成する装置を
提供することにある。An object of the present invention is to provide an apparatus for synthesizing oxide ceramics by a pressure self-combustion synthesis method in an oxidizing atmosphere.
【0007】[0007]
【課題を解決するための手段】本発明は、耐圧容器中に
断熱炉筒および断熱炉床を設けて炉室を画設し、かつ炉
室中にヒーターを備えた加圧自己燃焼合成装置におい
て、断熱炉筒および断熱炉床を耐酸化性の多孔質セラミ
ックスで構成し、かつ着火ヒーターおよび加熱ヒーター
を耐酸化性の白金−ロジウム合金とすることを特徴とす
る酸化雰囲気加圧自己燃焼合成装置を提供する。DISCLOSURE OF THE INVENTION The present invention provides a pressurized self-combustion synthesis apparatus in which a pressure-resistant container is provided with an insulating furnace tube and an insulating hearth to define a furnace chamber, and a heater is provided in the furnace chamber. An oxidizing atmosphere pressurized self-combustion synthesizer characterized in that the adiabatic furnace barrel and adiabatic hearth are made of oxidation-resistant porous ceramics, and the ignition heater and the heating heater are made of an oxidation-resistant platinum-rhodium alloy I will provide a.
【0008】[0008]
【作用】本発明の装置は、断熱炉筒および断熱炉床を耐
酸化性の多孔質酸化物セラミックスで構成し、かつ着火
ヒーターおよび加熱ヒーターを耐酸化性の白金−ロジウ
ム合金とすることにより、圧力ガス媒体として酸素混合
ガスを使用できる構造となり、炉室内を酸化雰囲気にす
ることにより、酸化物セラミックスの加圧自己燃焼合成
が可能となつた。In the apparatus of the present invention, the heat insulating furnace tube and the heat insulating hearth are made of oxidation resistant porous oxide ceramics, and the ignition heater and the heating heater are made of the oxidation resistant platinum-rhodium alloy. Oxygen mixed gas can be used as a pressure gas medium, and pressurized self-combustion synthesis of oxide ceramics is possible by making the furnace chamber an oxidizing atmosphere.
【0009】使用し得る圧力ガス媒体の酸素濃度は、好
適には0−20%である。The oxygen concentration of the pressurized gas medium which can be used is preferably 0-20%.
【0010】また、断熱筒および炉床断熱材は、耐熱性
と耐熱衝撃性を有する多孔質酸化物セラミックス材を使
用することにより、自己燃焼時の高熱が圧力容器側に放
散することを防止し、かつ自己燃焼時の急激な温度上昇
による高熱襲撃に対応する。Further, the heat insulating cylinder and the hearth heat insulating material use a porous oxide ceramic material having heat resistance and thermal shock resistance to prevent the high heat during self-combustion from radiating to the pressure vessel side. In addition, it responds to a high heat attack due to a rapid temperature rise during self-combustion.
【0011】加熱ヒーターにより、炉室を高温まで加熱
することができる。使用し得る炉室温度は、好適には0
−1600℃である。The heater can heat the furnace chamber to a high temperature. The furnace chamber temperature that can be used is preferably 0.
-1600 ° C.
【0012】本発明の装置は、その構造および材質か
ら、当然に圧力媒体としてアルゴン、窒素などの不活性
ガスを使用することが可能であり、従来通りの炭化物、
ホウ化物、窒化物セラミックスなどの加圧自己燃焼合成
にも利用することが出来る。The apparatus of the present invention can naturally use an inert gas such as argon or nitrogen as a pressure medium due to its structure and material, and it is possible to use a conventional carbide,
It can also be used for pressurized self-combustion synthesis of borides and nitride ceramics.
【0013】本発明の装置は、通常の酸化雰囲気熱間等
方圧プレスとして、1600℃、2000kg/cm2
にて試料を加圧焼結することも可能である。The apparatus of the present invention is used as a normal hot isostatic press in an oxidizing atmosphere at 1600 ° C. and 2000 kg / cm 2.
It is also possible to pressure sinter the sample.
【0014】[0014]
【実施例】本発明に係る酸化雰囲気加圧自己燃焼合成装
置について、図1を参照しながら以下詳細に説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An oxidizing atmosphere pressurized self-combustion synthesizer according to the present invention will be described in detail below with reference to FIG.
【0015】圧力容器(1)中の炉台(9)上に断熱筒
(6)および断熱炉床(8)を設けて燃焼炉を画設す
る。炉床に試料台(10)を設け、その上に被処理物を
置く。試料台には加熱ヒーター(12)を装着し、被処
理物の上方には着火ヒーター(11)を装着する。加熱
ヒーターおよび着火ヒーターは、炉台および下蓋(4)
を貫通する配線により各々加熱ヒーター電極(14)お
よび着火ヒーター電極(13)に接続する。被処理物に
接して試料温度測定用熱電対(15)を設け、炉室中央
に加熱ヒーター制御用熱電対(16)を設け、各々熱電
対取出線(17)を介して温度表示制御器(図に示して
いない)に配線する。A heat insulation cylinder (6) and a heat insulation hearth (8) are provided on a furnace table (9) in the pressure vessel (1) to define a combustion furnace. A sample table (10) is provided on the hearth, and an object to be processed is placed thereon. A heating heater (12) is attached to the sample stage, and an ignition heater (11) is attached above the object to be processed. Heaters and ignition heaters include furnace base and lower lid (4)
Are connected to the heating heater electrode (14) and the ignition heater electrode (13) respectively. A thermocouple (15) for measuring the sample temperature is provided in contact with the object to be treated, a thermocouple (16) for controlling the heater is provided in the center of the furnace chamber, and a temperature display controller ( (Not shown).
【0016】被処理物が位置する炉室中に、下蓋および
炉台を貫通する加圧ガス導入管を介して、酸素濃度最高
20%の混合アルゴンガス又は混合窒素ガスを2000
kg/cm2まで圧入する。着火ヒーター電極から着火
ヒーターに通電して、被処理物を加熱することにより、
自己燃焼の着火を行う。着火しにくい試料の場合は(ま
たは標準生成熱、断熱温度が共に低い場合など)、加熱
ヒーター電極から加熱ヒーターに通電し、試料を予熱す
ることにより、自己燃焼の開始を促進する。この間、試
料温度測定用熱電対で試料温度を測定することにより、
前述の予熱時の試料温度を制御する。さらに、自己燃焼
が開始した時は試料温度が急激に上昇することから、合
成反応の開始を確認する。In the furnace chamber in which the object to be treated is located, a mixed argon gas or a mixed nitrogen gas having an oxygen concentration of up to 20% is added through a pressurized gas introduction pipe penetrating the lower lid and the furnace base.
Press up to kg / cm 2 . By energizing the ignition heater from the ignition heater electrode to heat the object to be processed,
Performs self-combustion ignition. In the case of a sample that is difficult to ignite (or when the standard heat of formation and the adiabatic temperature are both low), the heater is energized from the heating heater electrode to preheat the sample to accelerate the start of self-combustion. During this time, by measuring the sample temperature with a thermocouple for measuring the sample temperature,
The sample temperature during the preheating is controlled. Furthermore, when self-combustion starts, the sample temperature rises sharply, confirming the start of the synthesis reaction.
【0017】[0017]
【発明の効果】本発明の装置は、加圧自己燃焼セラミッ
クス合成装置の炉室中を酸化雰囲気にすることにより、
従来の装置では合成が出来なかつた酸化物セラミックス
の酸化雰囲気加圧自己燃焼合成が可能となり、高品質の
酸化物セラミックスを製造し得る利点を有する。EFFECT OF THE INVENTION The apparatus according to the present invention is provided with an oxidizing atmosphere in the furnace chamber of the pressurized self-combusting ceramics synthesis apparatus,
The conventional apparatus has the advantage that it is possible to perform self-combustion under pressure in an oxidizing atmosphere while being unable to synthesize oxide ceramics, and to manufacture high-quality oxide ceramics.
【0018】また、炉室中を酸化雰囲気にすることによ
り、加圧ガス中の酸素と被処理物との反応による酸化雰
囲気加圧自己燃焼合成も可能となつた。合成反応の範囲
も拡大して、より多種類の製品を得ることが出来る。Further, by making the inside of the furnace chamber in an oxidizing atmosphere, it is possible to perform the self-combustion synthesis under the oxidizing atmosphere by the reaction between oxygen in the pressurized gas and the object to be treated. The range of synthetic reactions can also be expanded to obtain a wider variety of products.
【0019】本発明の装置は、その構造および材質か
ら、当然に圧力ガス媒体としてアルゴン、窒素などの不
活性ガスを使用することが可能であり、従来通りの炭化
物、ホウ化物、窒化物セラミックスなどの加圧自己燃焼
合成にも利用することが出来る。The apparatus of the present invention can naturally use an inert gas such as argon or nitrogen as a pressure gas medium due to its structure and material, and it is possible to use conventional carbides, borides, nitride ceramics, etc. It can also be used for pressurized self-combustion synthesis of.
【0020】また、通常の酸化雰囲気熱間等方圧プレス
として、最高1600℃、2000kg/cm2で試料
を加圧焼結することも可能である。It is also possible to press-sinter the sample at a maximum temperature of 1600 ° C. and 2000 kg / cm 2 as a normal hot isostatic press in an oxidizing atmosphere.
【図1】本発明に係る実施例を示す酸化雰囲気加圧自己
燃焼合成装置の要部断面図である。FIG. 1 is a sectional view of an essential part of an oxidizing atmosphere pressurized self-combustion synthesizer showing an embodiment according to the present invention.
1 圧力容器 2 ヨークフレーム 3 上蓋 4 下蓋 5 ガスシール 6 断熱筒 7 断熱筒支持ケーシング 8 断熱炉床 9 炉台 10 試料台 11 着火ヒーター 12 加熱ヒーター 13 着火ヒーター電極 14 加熱ヒーター電極 15 試料温度測定用熱電対 16 加熱ヒーター制御用熱電対 17 熱電対取出線 1 Pressure Vessel 2 Yoke Frame 3 Upper Lid 4 Lower Lid 5 Gas Seal 6 Heat Insulation Cylinder 7 Heat Insulation Cylinder Support Casing 8 Heat Insulation Hearth 9 Heat Sink 10 Sample Stage 11 Ignition Heater 12 Heating Heater 13 Ignition Heater Electrode 14 Heating Heater Electrode 15 For Measuring Sample Temperature Thermocouple 16 Thermocouple for heating heater control 17 Thermocouple lead wire
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 F27D 11/02 A 8222−4K ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI technical display location F27D 11/02 A 8222-4K
Claims (1)
設けて炉室を画設し、かつ炉室中にヒーターを備えた加
圧自己燃焼合成装置において、断熱炉筒および断熱炉床
を耐酸化性の多孔質セラミックスで構成し、かつ着火ヒ
ーターおよび加熱ヒーターを耐酸化性の白金−ロジウム
合金とすることを特徴とする酸化雰囲気加圧自己燃焼合
成装置。1. A pressurized self-combustion synthesizer in which a pressure-resistant container is provided with an adiabatic furnace barrel and an adiabatic hearth to define a furnace chamber, and a heater is provided in the furnace chamber. Is composed of an oxidation-resistant porous ceramics, and the ignition heater and the heating heater are made of an oxidation-resistant platinum-rhodium alloy.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4186946A JPH07117344B2 (en) | 1992-07-14 | 1992-07-14 | Oxidizing atmosphere pressurized self-combustion synthesizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4186946A JPH07117344B2 (en) | 1992-07-14 | 1992-07-14 | Oxidizing atmosphere pressurized self-combustion synthesizer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0634276A true JPH0634276A (en) | 1994-02-08 |
JPH07117344B2 JPH07117344B2 (en) | 1995-12-18 |
Family
ID=16197497
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4186946A Expired - Fee Related JPH07117344B2 (en) | 1992-07-14 | 1992-07-14 | Oxidizing atmosphere pressurized self-combustion synthesizer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07117344B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113390100A (en) * | 2021-05-13 | 2021-09-14 | 张明玉 | Candle seedling type burner |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02126093A (en) * | 1988-07-30 | 1990-05-15 | Kobe Steel Ltd | Oxidizing atmosphere hot isotropic pressurizer |
-
1992
- 1992-07-14 JP JP4186946A patent/JPH07117344B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02126093A (en) * | 1988-07-30 | 1990-05-15 | Kobe Steel Ltd | Oxidizing atmosphere hot isotropic pressurizer |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113390100A (en) * | 2021-05-13 | 2021-09-14 | 张明玉 | Candle seedling type burner |
CN113390100B (en) * | 2021-05-13 | 2022-07-08 | 张明玉 | Candle seedling type burner |
Also Published As
Publication number | Publication date |
---|---|
JPH07117344B2 (en) | 1995-12-18 |
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