JPS60174866A - Method and apparatus for oxidizing metal consisting essentially of iron - Google Patents
Method and apparatus for oxidizing metal consisting essentially of ironInfo
- Publication number
- JPS60174866A JPS60174866A JP3090784A JP3090784A JPS60174866A JP S60174866 A JPS60174866 A JP S60174866A JP 3090784 A JP3090784 A JP 3090784A JP 3090784 A JP3090784 A JP 3090784A JP S60174866 A JPS60174866 A JP S60174866A
- Authority
- JP
- Japan
- Prior art keywords
- iron
- gas
- nitrogen gas
- oxidizing atmosphere
- dry
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
- C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
- C23C8/10—Oxidising
- C23C8/12—Oxidising using elemental oxygen or ozone
- C23C8/14—Oxidising of ferrous surfaces
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Furnace Details (AREA)
- Powder Metallurgy (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は良質な酸化皮膜を効率よく得ることのできる鉄
(Fe)を主成分とする金属の酸化方法およびその装置
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for oxidizing metals containing iron (Fe) as a main component, which can efficiently obtain a high-quality oxide film.
整合封止型気密端子の製造においては、優れた気密特性
を得るために金属外環およびリード線に酸化処理を行っ
て、表面に金属素地との密着性に優れ、かつガラスとの
濡れ性がよいスピネル型Fe104等の酸化皮膜を生成
させた後、ガラスと組合わせて封止する製造方法が一般
的に採用されている。この場合に生成される酸化皮膜の
質が気密特性等の製品の最終的な品質を支配するため、
良質な酸化皮膜を安定して、かつ効率よく生成させる方
法および装置が要望される。In manufacturing matched sealed hermetic terminals, the metal outer ring and lead wire are oxidized to obtain excellent airtightness, and the surface has excellent adhesion to the metal base and good wettability with glass. Generally, a manufacturing method is adopted in which a good spinel-type Fe104 oxide film is formed and then combined with glass and sealed. The quality of the oxide film produced in this case controls the final quality of the product, such as airtightness, so
There is a need for a method and apparatus that can stably and efficiently generate a high-quality oxide film.
従来この種の酸化方法としては、コンベア式連続酸化処
理炉を用いて、大気雰囲気中で部品を600〜1000
℃に加熱して表面に皮膜を生成させる方法が知られてい
る。この方法によるときは、処理能力においては優れる
が、大気雰囲気中で得られる酸化皮膜が金属素地との密
着性において劣るために、金属外環とガラスとの組立時
の振動等によってしばしば酸化皮膜に亀裂や剥離が生じ
、気密性が阻害され信頼性に劣るという難点がある。Conventionally, this type of oxidation method uses a conveyor-type continuous oxidation treatment furnace to oxidize parts in an atmosphere of 600 to 1000
A method of forming a film on the surface by heating to ℃ is known. Although this method has excellent processing ability, the oxide film obtained in the atmosphere has poor adhesion to the metal substrate, so vibrations during assembly of the metal outer ring and glass often cause the oxide film to deteriorate. It has the disadvantage that cracks and peeling occur, impeding airtightness and lowering reliability.
他の方法としてはバッチ式酸化処理炉を用いる方法があ
る。この方法によるときは、例えば鉄−ニッケルーコバ
ル) (Fe−Ni−Co)合金を酸化処理する場合、
バッチ式酸化処理炉内に所定量の部品を入れ、まずドラ
イ窒素(NQ)ガス雰囲気中で、温度が転移点以上に達
するまで非酸化性雰囲気の状態で昇温した後、炉内をウ
ェット窒素(N2)ガスまたはウェットN2ガスとウェ
ット酸素(08)ガスの混合ガスの酸化性雰囲気に切替
えて、所定量の蔀品毎に酸化処理するものである。この
バッチ式においては、非酸化性雰囲気と、スピネル型の
密着性に優れた酸化皮膜を生成させる高温状態の酸化性
雰囲気とを確実に得ることができるので、良質の酸化皮
膜を生成させることができる利点がある。しかしながら
1つの処理炉を非酸化性雰囲気と酸化性雰囲気とに交互
に切替える必要があるため、作業能率に著しく劣り、生
産性が極めて悪いという難点がある。Another method is to use a batch type oxidation treatment furnace. When using this method, for example, when oxidizing an iron-nickel-cobal (Fe-Ni-Co) alloy,
A predetermined amount of parts is placed in a batch-type oxidation treatment furnace, and the temperature is first raised in a non-oxidizing atmosphere in a dry nitrogen (NQ) gas atmosphere until the temperature reaches the transition point or higher, and then the inside of the furnace is heated with wet nitrogen. The atmosphere is switched to an oxidizing atmosphere of (N2) gas or a mixed gas of wet N2 gas and wet oxygen (08) gas to oxidize each predetermined amount of shingles. In this batch method, it is possible to reliably obtain a non-oxidizing atmosphere and a high-temperature oxidizing atmosphere that produces a spinel-type oxide film with excellent adhesion, so it is possible to produce a high-quality oxide film. There are advantages that can be achieved. However, since it is necessary to alternately switch one processing furnace between a non-oxidizing atmosphere and an oxidizing atmosphere, there is a drawback that work efficiency is extremely poor and productivity is extremely low.
本発明は上記難点に鑑みてなされたものであり、その目
的とするところは、良質な酸化皮膜を生産性良く得るこ
とのできる鉄を′主成分とする金属の酸化方法およびそ
の装置を提供するにあり、その特徴は、鉄、鉄−ニソケ
ル合金、鉄−ニッケルーコバルト合金等の鉄を主成分と
する金属を、入口側にドライ窒素ガスによる非酸化性雰
囲気の低温ゾーンが、中間にウェット窒素ガスまたはウ
ェット窒素ガスとウェット酸素ガスとの混合ガスによる
酸化性雰囲気の高温ゾーンが、出口側にドライ窒素ガス
による非酸化性雰囲気の低温ゾーンがそれぞれ配された
炉中を連続的に通過させて、前記金属を次々連続的に酸
化するところにある。The present invention has been made in view of the above-mentioned difficulties, and its purpose is to provide a method and apparatus for oxidizing metals containing iron as a main component, which can produce a high-quality oxide film with high productivity. It is characterized by a low-temperature zone with a non-oxidizing atmosphere of dry nitrogen gas on the inlet side, and a wet zone in the middle where metals mainly composed of iron, such as iron, iron-Nisokel alloy, and iron-nickel-cobalt alloy, are heated. A high-temperature zone with an oxidizing atmosphere made of nitrogen gas or a mixture of wet nitrogen gas and wet oxygen gas is continuously passed through a furnace, which has a low-temperature zone with a non-oxidizing atmosphere made of dry nitrogen gas on the outlet side. Then, the metals are successively oxidized one after another.
以下本発明の好適な実施例を添付図面に基づき詳細に説
明する。Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.
図は本発明に係る酸化装置10の概要を示す。The figure schematically shows an oxidation device 10 according to the invention.
12は入口開口部、14は出口開口部である。16は入
口開口部12から出口開口部14に向かって連続的に移
動する無端コンベヤである。*他装置10は、入口開口
部12側が非酸化性雰囲気の低温ゾーンAに、中央が酸
化性雰囲気の高温ゾーンBに、出口開口部14側が非酸
化性雰囲気の低温ゾーンCに形成されている。12 is an inlet opening, and 14 is an outlet opening. 16 is an endless conveyor that moves continuously from the inlet opening 12 towards the outlet opening 14. *The other device 10 is formed in a low temperature zone A with a non-oxidizing atmosphere on the inlet opening 12 side, a high temperature zone B with an oxidizing atmosphere in the center, and a low temperature zone C with a non-oxidizing atmosphere on the outlet opening 14 side. .
18は低温ゾーンAにドライN2ガスを導入するドライ
N2ガス吹込口であり、酸化装置10の入口開口部12
近傍上部に設けられている。20は高温ゾーンBにウェ
ットN2ガス、またはウェットNxガスとウェット0.
ガスとの混合ガスを吹込む吹込口であり、高温ゾーンB
の中央上部に設けられている。22はN、ガス源、24
はojPガス源であり、パイプ26に接続されてガス源
からの両ガスが混合されるとともに、該パイプ26先端
が、密閉水槽28の水中に開口されることによって水中
でバブリングされ混合ガスに湿り気が与えられる。密閉
水槽28には温度調節装置(図示せず)が設けられてお
り、種々の温度“設定がしうるようになっている。した
がって該密閉水槽28において、上 □記設定温度で決
定される飽和水蒸気を含んだウェットN2ガスとウェッ
トN2ガスとの混合ガスが得られる。該混合ガスは密閉
水槽28と吹込口2oとを接続する導入パイプ3oによ
って吹込口2oに導かれ、吹込口20から高温ゾーンB
内に吹込まれる。32.34はN2ガス源22と02ガ
ス源24とにそれぞれ設けたパルプである。該バルブ3
2゜34を操作することに、よって、N2ガスまたは0
2ガスの単独ガスも得られ、また両ガスの混合比率の異
なる任意の混合ガスが得られる。18 is a dry N2 gas inlet for introducing dry N2 gas into the low temperature zone A, and is connected to the inlet opening 12 of the oxidizer 10.
It is located near the top. 20 is wet N2 gas or wet Nx gas and wet 0.20 in high temperature zone B.
This is an inlet for blowing mixed gas with gas, and is located in high temperature zone B.
is located at the top center of the 22 is N, gas source, 24
is an OJP gas source, which is connected to a pipe 26 so that both gases from the gas source are mixed, and the tip of the pipe 26 is opened into the water of a sealed water tank 28 to bubble in the water and add moisture to the mixed gas. is given. The sealed water tank 28 is equipped with a temperature control device (not shown), so that various temperature settings can be made. A mixed gas of wet N2 gas containing water vapor and wet N2 gas is obtained.The mixed gas is guided to the air inlet 2o by an introduction pipe 3o connecting the airtight water tank 28 and the air inlet 2o, and from the air inlet 20 at a high temperature. Zone B
blown inside. Numerals 32 and 34 are pulps provided in the N2 gas source 22 and the 02 gas source 24, respectively. The valve 3
By operating 2°34, N2 gas or 0
Single gases of two gases can also be obtained, and arbitrary mixed gases with different mixing ratios of both gases can be obtained.
36は低温ゾーンCにドライN2ガスを導入するドライ
N2ガス吹込口であり、酸化装置1oの出口開口部14
近傍上部に設けられている。36 is a dry N2 gas inlet for introducing dry N2 gas into the low temperature zone C, and is connected to the outlet opening 14 of the oxidizer 1o.
It is located near the top.
38は酸化装置1oの低温ゾーンAと高温ゾーンBとの
境界上部に設けられたドライN2ガス吹込口であり、下
方に向けてドライN2ガスを吹込み、低温ゾーンAと高
温ゾーンBを仕切るドライN2ガスカーテンを形成する
。38 is a dry N2 gas blowing port provided at the upper part of the boundary between the low temperature zone A and the high temperature zone B of the oxidizer 1o, which blows dry N2 gas downward to separate the low temperature zone A and the high temperature zone B. Form a N2 gas curtain.
40は上記境界部に、上記ドライN2ガス吹込口38と
反対側に位置して設けたガス強制排気口であり、上記の
ドライN2ガス吹込口38がらのドライN2ガスを引き
込んで前記のドライN2ガスカーテンを形成させると同
時に、低温ゾーンAおよび高温ゾーンB内のガスを引き
込んで排気する。Reference numeral 40 denotes a gas forced exhaust port provided at the boundary, opposite to the dry N2 gas inlet 38, which draws in the dry N2 gas from the dry N2 gas inlet 38 and discharges the dry N2 gas from the dry N2 gas inlet 38. At the same time as forming a gas curtain, the gas in the low temperature zone A and the high temperature zone B is drawn in and exhausted.
42は高温ゾーンBと低温ゾーンCとの境界部に設けた
ドライN2ガス吹込口、44は該ドライN2ガス吹込口
42と対向して設けたガス強制排気口であり、前記と同
様に境界部にドライN2ガスカーテンを形成する。42 is a dry N2 gas inlet provided at the boundary between the high temperature zone B and the low temperature zone C, and 44 is a forced gas exhaust port provided opposite to the dry N2 gas inlet 42; A dry N2 gas curtain is formed.
なお前記の無端コンベヤ16は例えば網目状に形成され
、被酸化物は落下させないが、ガスを通過させうるよう
になっている。Note that the endless conveyor 16 is formed, for example, in a mesh shape, and is configured to prevent the material to be oxidized from falling, but to allow gas to pass therethrough.
また酸化装置IOの各低温ゾーンA、Cおよび高温ゾー
ンBには適宜な加熱源(図示せず)が設けられ、加熱し
うるようになっている。In addition, appropriate heating sources (not shown) are provided in each of the low temperature zones A, C and high temperature zone B of the oxidizer IO so that they can be heated.
酸化処理工程について説明すると、例えばFe −Ni
−Co合金を酸化するには、まず、高温ゾーンB内の温
度を、前記各ガス流通時においてスピネル型の良質の酸
化皮膜が得られる転移温度430℃以上とし、最高温度
が高温ゾーンB内にあるように酸化装置の温度プロフィ
ルを設定しておく。この場合の温度プロフィルは、例え
ば第2図に示すごとくなる。そして被酸化物を無端コン
ベヤ16上に載せて酸化装置lO内を連続的に通過させ
れば、被酸化物表面上に良質な酸化膜を形成させること
ができる。すなわち、被酸化物は低温ゾーンA内を通過
する際に徐々に加温され、高温ゾーンB内に入る際には
430℃以上に昇温しでいるから、高温ゾーンB内でス
ピネル型酸化皮膜が形成される。To explain the oxidation treatment step, for example, Fe-Ni
- To oxidize the Co alloy, first, set the temperature in high temperature zone B to 430°C or higher, the transition temperature at which a spinel type oxide film of good quality is obtained during each of the above gas flows, and then set the maximum temperature in high temperature zone B to Set the temperature profile of the oxidizer as follows. The temperature profile in this case is, for example, as shown in FIG. If the object to be oxidized is placed on the endless conveyor 16 and passed through the oxidizer 10 continuously, a high-quality oxide film can be formed on the surface of the object to be oxidized. In other words, the material to be oxidized is gradually heated as it passes through the low temperature zone A, and the temperature rises to 430°C or higher when it enters the high temperature zone B. is formed.
低温ゾーンA内はドライN2ガスによって非酸化性雰囲
気に保たれているから、低温における密着性に劣る酸化
皮膜は形成されることはない。Since the inside of the low temperature zone A is maintained in a non-oxidizing atmosphere by dry N2 gas, an oxide film with poor adhesion at low temperatures is not formed.
また低温ゾーンA、高温ゾーンB、低温ゾーンC間はド
ライN2ガスカーテンによって有効に仕切られ、各ゾー
ン間のガスが混合することがなく、各々の非酸化性雰囲
気、酸化性雰囲気が融絶して保持されるものである。In addition, low temperature zone A, high temperature zone B, and low temperature zone C are effectively partitioned by a dry N2 gas curtain, so that the gases between each zone do not mix, and the non-oxidizing atmosphere and oxidizing atmosphere of each zone are dissolved. It is maintained as follows.
また非酸化物の材質によって、前記の温度プロフィルを
材質に合わせて最適に設定するとともに、高温ゾーンB
内へ吹込む酸化性ガスを、混合比、湿り気等において材
質に合わせて最適に設定する。In addition, depending on the non-oxide material, the temperature profile described above can be set optimally according to the material, and the high temperature zone B
The oxidizing gas that is blown into the interior is optimally set in terms of mixing ratio, moisture, etc., depending on the material.
本発明は鉄および鉄を主成分とする金属であれば広く採
用しうる。例えば焼結金属の水蒸気黒化処理においても
良質な酸化皮膜を形成することができる。The present invention can be applied to a wide variety of metals including iron and iron-based metals. For example, a high-quality oxide film can be formed even in steam blackening treatment of sintered metal.
以上のように本発明方法によれば、被酸化物表面上に良
質な酸化皮膜を形成することができるとともに、酸化処
理を連続的に行うことができ生産性を向上させることが
できる。また本発明装置によれば、非酸化性雰囲気と酸
化性雰囲気とを、温度は伝達するが、ガスの流通は阻止
するガスカーテンで仕切ったことによって、良質な酸化
皮膜を形成することのできる酸化装置を提供し得たもの
である。As described above, according to the method of the present invention, a high-quality oxide film can be formed on the surface of the object to be oxidized, and the oxidation treatment can be performed continuously, thereby improving productivity. Furthermore, according to the device of the present invention, a non-oxidizing atmosphere and an oxidizing atmosphere are separated by a gas curtain that transmits temperature but blocks gas flow, thereby forming a high-quality oxide film. We were able to provide the equipment.
以上本発明につき好適な実施例を挙げて種々説明したが
、本発明はこの実施例に限定されるものではなく、発明
の精神を逸脱しない範囲内で多くの改変を施し得るのは
もぢ−ろんのことである。Although the present invention has been variously explained above using preferred embodiments, the present invention is not limited to these embodiments, and many modifications can be made without departing from the spirit of the invention. I mean Ron.
第1図は本発明装置の概要を示す説明図、第2図はFe
−Ni−Co合金の酸化処理における酸化装置内の温度
プロフィルの例を示す温度曲呻である。
10・・・酸化装置、12・・・入ロ開ロ音ド14・・
・出口開口部、16・・・無端コンベヤ、18・・・ド
ライN2ガス吹込口、20・・・吹込口、22・・・N
xガス源、24・・・Ozガス源、26・・・パイプ、
28・・・密閉水槽、30・・・導入パイプ、 32.
34・・・バルブ、 36.38・・・ドライN2ガス
吹込口、40・・・ガス強制排気口、42・・・ドライ
N2ガス吹込口、44・・・ガス強制排気口。
特許出願人
新光電気工業株式会社
代表者光延丈喜夫
第2図
八
手続補正書
昭和59年3月16日
・特許庁長官若杉和夫 殿
1、事件の表示
昭和59年特許 願第30907 号
3、 補正をする者
事件との関係 特許出願人
4、代理人
8、補正の内容
1)明細書第9頁第7行目の「非酸化物」を「被酸化物
」と補正する。
2)図面は第2図を別紙のごとく補正する。FIG. 1 is an explanatory diagram showing the outline of the device of the present invention, and FIG.
- Figure 2 is a temperature curve showing an example of a temperature profile in an oxidizer during oxidation treatment of a -Ni-Co alloy. 10...Oxidizer, 12...Inlet opening sound 14...
・Outlet opening, 16... Endless conveyor, 18... Dry N2 gas inlet, 20... Inlet, 22... N
x gas source, 24...Oz gas source, 26...pipe,
28... Sealed water tank, 30... Introduction pipe, 32.
34...Valve, 36.38...Dry N2 gas inlet, 40...Gas forced exhaust port, 42...Dry N2 gas inlet, 44...Gas forced exhaust port. Patent Applicant Shinko Electric Industry Co., Ltd. Representative Takekio Mitsunobu Figure 2 8 Procedural Amendments March 16, 1980 Kazuo Wakasugi, Commissioner of the Japan Patent Office 1, Indication of Case 1982 Patent Application No. 30907 3, Amendment Patent applicant 4, agent 8, content of amendment 1) Amend "non-oxidized material" in line 7 of page 9 of the specification to "oxidized material". 2) For drawings, please correct Figure 2 as shown in the attached sheet.
Claims (1)
金等の鉄を主成分とする金属を、入口側にドライ窒素ガ
スによる非酸化性雰囲気の低温ゾーンが、中間にウェッ
ト窒素ガスまたはウェット窒素ガスとウェット酸素ガス
との混合ガスによる酸化性雰囲気の高温ゾーンが、出口
側にドライ窒素ガスによる非酸化性雰囲気の低温ゾーン
がそれぞれ配された炉中を連続的に通過させて、前記金
属を次々連続的に酸化することを特徴とする鉄を主成分
とする金属の酸化方法。 2、a、e−ニッケル合金、鉄−ニッケルーコバルト合
金等の鉄を主成分とする金属を連続的に酸化する酸化装
置において、入口側がドライ窒素ガス吹込口を備えた非
酸化性雰囲気の低温ゾーンに、中間がウェット窒素ガス
またはウェット窒素ガスとウェット酸素ガスとの混合ガ
スを吹込む吹込口を備えた酸化性雰囲気の高温ゾーンに
、出口側がドライ窒素ガス吹込口を備えた非酸化性雰囲
気の低温ゾーンにそれぞれ形成されると共に、前記各ゾ
ーンの境界部にドライ窒素ガスカーテンを形成すべく、
前記各ゾーンの境界部にドライ窒素ガス吹込口と該ドラ
イ窒素ガス吹込口に対向してガス強制排気口とが設けら
れていることを特徴とする鉄を主成分とする金属の酸化
装置。[Claims] 1. Metals mainly composed of iron, such as iron, iron-nickel alloys, iron-nickel-cobalt alloys, etc., are placed in a low temperature zone with a non-oxidizing atmosphere using dry nitrogen gas on the inlet side, and A high-temperature zone with an oxidizing atmosphere made of wet nitrogen gas or a mixture of wet nitrogen gas and wet oxygen gas passes continuously through a furnace, each of which has a low-temperature zone with a non-oxidizing atmosphere made of dry nitrogen gas on the outlet side. A method for oxidizing a metal containing iron as a main component, characterized in that the metal is oxidized one after another. 2, a, e - In an oxidizing device that continuously oxidizes metals whose main component is iron such as nickel alloys and iron-nickel-cobalt alloys, the inlet side is equipped with a dry nitrogen gas inlet at a low temperature in a non-oxidizing atmosphere. The high temperature zone has an oxidizing atmosphere with an inlet in the middle for blowing wet nitrogen gas or a mixture of wet nitrogen gas and wet oxygen gas into the zone, and a non-oxidizing atmosphere with a dry nitrogen gas inlet at the outlet side. and to form a dry nitrogen gas curtain at the boundary between the zones,
An apparatus for oxidizing metals containing iron as a main component, characterized in that a dry nitrogen gas inlet is provided at the boundary between the zones, and a forced gas exhaust port is provided opposite the dry nitrogen gas inlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3090784A JPS60174866A (en) | 1984-02-20 | 1984-02-20 | Method and apparatus for oxidizing metal consisting essentially of iron |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3090784A JPS60174866A (en) | 1984-02-20 | 1984-02-20 | Method and apparatus for oxidizing metal consisting essentially of iron |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60174866A true JPS60174866A (en) | 1985-09-09 |
JPS622624B2 JPS622624B2 (en) | 1987-01-21 |
Family
ID=12316782
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3090784A Granted JPS60174866A (en) | 1984-02-20 | 1984-02-20 | Method and apparatus for oxidizing metal consisting essentially of iron |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60174866A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63161152A (en) * | 1986-12-24 | 1988-07-04 | Daido Steel Co Ltd | Blackening furnace |
US4943164A (en) * | 1988-08-26 | 1990-07-24 | Hitachi, Ltd. | Mixing apparatus for mixing reagent for use in automatic chemistry analyzer |
JPH0378052U (en) * | 1989-11-28 | 1991-08-07 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2020001176A (en) | 2018-06-25 | 2020-01-09 | 株式会社神戸製鋼所 | Screw-type extruder |
-
1984
- 1984-02-20 JP JP3090784A patent/JPS60174866A/en active Granted
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63161152A (en) * | 1986-12-24 | 1988-07-04 | Daido Steel Co Ltd | Blackening furnace |
US4943164A (en) * | 1988-08-26 | 1990-07-24 | Hitachi, Ltd. | Mixing apparatus for mixing reagent for use in automatic chemistry analyzer |
JPH0378052U (en) * | 1989-11-28 | 1991-08-07 |
Also Published As
Publication number | Publication date |
---|---|
JPS622624B2 (en) | 1987-01-21 |
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