Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0825729B2 - Combustion synthesis method of high-purity TiN - Google Patents
[go: Go Back, main page]

JPH0825729B2 - Combustion synthesis method of high-purity TiN - Google Patents

Combustion synthesis method of high-purity TiN

Info

Publication number
JPH0825729B2
JPH0825729B2 JP2243882A JP24388290A JPH0825729B2 JP H0825729 B2 JPH0825729 B2 JP H0825729B2 JP 2243882 A JP2243882 A JP 2243882A JP 24388290 A JP24388290 A JP 24388290A JP H0825729 B2 JPH0825729 B2 JP H0825729B2
Authority
JP
Japan
Prior art keywords
reaction
combustion
nitrogen
green compact
liquid nitrogen
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.)
Expired - Lifetime
Application number
JP2243882A
Other languages
Japanese (ja)
Other versions
JPH04124007A (en
Inventor
修 小田原
化 呉
Original Assignee
東京工業大学長
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 東京工業大学長 filed Critical 東京工業大学長
Priority to JP2243882A priority Critical patent/JPH0825729B2/en
Publication of JPH04124007A publication Critical patent/JPH04124007A/en
Publication of JPH0825729B2 publication Critical patent/JPH0825729B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Inorganic Compounds Of Heavy Metals (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はチタン粉末と窒素との燃焼を利用したTiNの
燃焼合成法に関し、液体窒素を窒素源とし、高純度窒化
チタンを高効率に燃焼合成する方法に関するものであ
る。より詳しくはチタン粉末圧粉体を液体窒素浴中に配
置し圧粉体下部表面を加熱着火し反応を誘導し、情報へ
の反応伝播に伴い気相成分および熱も上方に移動させる
ことにより高純度な窒化物を製造する方法に関する。
TECHNICAL FIELD The present invention relates to a TiN combustion synthesis method using combustion of titanium powder and nitrogen, and uses liquid nitrogen as a nitrogen source to burn highly pure titanium nitride with high efficiency. It relates to a method of synthesizing. More specifically, the titanium powder compact is placed in a liquid nitrogen bath, the lower surface of the compact is heated and ignited to induce a reaction, and the gas phase component and heat are also moved upward as the reaction propagates to information. It relates to a method for producing a pure nitride.

(従来の技術) 窒化物は、その高い強度、耐摩耗性および耐食性を特
徴とし、かつ電気工学や化学工業において広範囲な用途
を有する。かかる窒化物の製造に対する公知方法の一つ
は、窒素またはアンモニア気流中で温度1200〜2000℃に
おいて初期成分を加熱することからなる。出発成分とし
ては純元素およびその化合物、例えば、ハロゲン化物等
が用いられる。熱処理の結果得られた生成物は微粉化さ
れ、かつ出発成分に相互作用させるため熱処理を反復さ
せる。この工程は目的生成物が所要品質に達するまで数
段階で行われる。なぜなら窒素のケーキ化した層中への
拡散が阻害されるために窒化反応が完全には進行しない
ためであり、ケーキ化した団塊を排出して粉砕した上、
再び繰り返して窒化が行われる。他の方法として、例え
ば特公昭56−27441号公報に記載の発明の如く、燃焼反
応を利用する方法があるが、高圧の窒素ガスまたは液体
窒素を用いて金属粉末圧粉体の上部表面より燃焼反応を
誘導し窒化物を合成する方法であり、圧粉体の充填度を
変えることにより反応伝播速度を制御し窒化率を向上さ
せることを目的としている。
BACKGROUND OF THE INVENTION Nitride is characterized by its high strength, wear resistance and corrosion resistance, and has a wide range of applications in the electrical engineering and chemical industries. One known method for the production of such nitrides consists of heating the initial components in a nitrogen or ammonia stream at a temperature of 1200-2000 ° C. As the starting component, pure elements and their compounds such as halides are used. The product resulting from the heat treatment is finely divided and the heat treatment is repeated in order to interact with the starting components. This process is carried out in several stages until the desired product reaches the required quality. This is because the nitriding reaction does not proceed completely because nitrogen is prevented from diffusing into the caked layer, and the caked nodule is discharged and crushed.
The nitriding is repeated again. As another method, there is a method of utilizing a combustion reaction, for example, as in the invention described in Japanese Patent Publication No. 56-27441, which uses a high-pressure nitrogen gas or liquid nitrogen to burn from the upper surface of a metal powder compact. It is a method of inducing a reaction to synthesize a nitride, and its purpose is to control the reaction propagation speed and improve the nitriding rate by changing the filling degree of the green compact.

(発明が解決しようとする課題) しかし、液体窒素を用いた場合に上部表面からの着火
による下方への反応伝播では反応伝播方向と反応生成熱
や気化した窒素の移動方向が逆であり、結果的に窒化率
はあまり向上しない。すなわち、液体窒素中での金属粉
末の燃焼は、第一段階として液体窒素の気化過程があ
り、その気相と金属との反応が進行する。したがって下
方への反応伝播では反応の伝播と熱の移動方向が逆であ
るため、反応面後方での高温領域の維持時間が短く、ま
た高温領域後方で生成した窒素ガスも上方へ移動するた
め反応伝播に伴う後方の高温領域面での継続する窒化反
応に効果的ではなく、さらに窒素ガスが上方へ移動する
過程で雰囲気中に存在する不純物成分(例えば酸素ガ
ス)を下方へ取り込まれるため、得られる窒化物の高純
度化にも効果的でない。
(Problems to be solved by the invention) However, when liquid nitrogen is used, the reaction propagation direction is opposite to the reaction propagation heat and the migration direction of vaporized nitrogen in the downward reaction propagation due to ignition from the upper surface. However, the nitriding rate does not improve so much. That is, in the combustion of metal powder in liquid nitrogen, there is a vaporization process of liquid nitrogen as the first step, and the reaction between the vapor phase and the metal proceeds. Therefore, in the downward reaction propagation, the reaction propagation direction and the heat transfer direction are opposite, so the maintenance time of the high temperature region behind the reaction surface is short, and the nitrogen gas generated behind the high temperature region also moves upward, It is not effective for the continuous nitriding reaction on the surface of the high temperature region behind due to the propagation, and the impurity component (for example, oxygen gas) existing in the atmosphere is taken in downward in the process of moving nitrogen gas upward. It is not effective in purifying the obtained nitride.

(問題点を解決するための手段) 本発明は上記従来の液体窒素を用いた燃焼合成におい
て窒化率の向上が困難であるという問題点を解決し、高
純度で高転換率の窒化物合成を達成するために、液体窒
素中に配置した金属圧粉体の下部表面より着火し、上方
へ反応伝播させる窒化物の製造方法を採用したものであ
る。
(Means for Solving Problems) The present invention solves the problem that it is difficult to improve the nitriding rate in the above-described conventional combustion synthesis using liquid nitrogen, and realizes nitride synthesis with high purity and high conversion rate. In order to achieve this, a method for producing a nitride is adopted in which ignition is performed from the lower surface of a metal green compact placed in liquid nitrogen and the reaction is propagated upward.

本発明は金属チタン粉末圧粉体を液体窒素を充填した
反応容器中に配置し、前記圧粉体の下部端面にタングス
テン線等の耐熱性導体を配設し、これを外部の電源に接
続し、通電により圧粉体の下部表面の一部を1700℃以上
に加熱して該圧粉体と窒素との燃焼反応を誘導し、燃焼
反応に引き続く該圧粉体の構成粉末内部への窒素の拡散
に伴う自発的な金属チタンの窒化反応を促進し、開始さ
れた燃焼過程の結果発生する熱によって2000℃以上の高
温反応層を形成し、この反応層を層状に逐次上方へ進行
させることを特徴とする高純度TiNの燃焼合成法にあ
る。
In the present invention, a metal titanium powder green compact is placed in a reaction vessel filled with liquid nitrogen, a heat resistant conductor such as a tungsten wire is placed on the lower end face of the green compact, and this is connected to an external power source. , A part of the lower surface of the green compact is heated to 1700 ° C or more by energization to induce a combustion reaction between the green compact and nitrogen, and nitrogen in the constituent powder of the green compact following the combustion reaction The spontaneous nitridation reaction of titanium metal with diffusion is promoted, and the heat generated as a result of the initiated combustion process forms a high-temperature reaction layer of 2000 ° C or higher, and the reaction layer is successively advanced upward in layers. It is characterized by a combustion synthesis method of high-purity TiN.

(作 用) 本発明の特徴は、液体窒素を窒素源とし反応伝播方向
を上下に置いた試料の下部より着火し反応が下部より上
部に伝播するよう制御し、発熱反応で生成する熱の移動
方向と一致させることにより、更に高転換率を達成させ
ることである。
(Operation) The feature of the present invention is that the transfer of heat generated by the exothermic reaction is controlled by igniting from the lower part of the sample with liquid nitrogen as the nitrogen source and setting the reaction propagation direction up and down By matching the direction, it is possible to achieve a higher conversion rate.

液体窒素は、窒素ガスに比べ単位体積あたりの窒素密
度が高く窒化効率は高いと判断されるのであるが、窒化
反応は気相状態で進行するため気化熱相当分だけ液体窒
素が不利となり、必ずしも窒素ガスより高い転換率とは
ならない。
Liquid nitrogen has a higher nitrogen density per unit volume than nitrogen gas, and it is judged that the nitriding efficiency is high, but since the nitriding reaction proceeds in the gas phase, liquid nitrogen is disadvantageous by the amount equivalent to the heat of vaporization, The conversion rate is not higher than that of nitrogen gas.

このために本発明では反応伝播を下方より上方に順次
層状に行われるようにしたものである。すなわち、本発
明では上方への反応伝播とともに熱も上方へ拡散する
が、反応伝播速度は圧粉体中の熱の伝播速度より同等以
上が望ましく、反応が誘導できる圧粉体状態ならばその
条件を満たしている。反応の誘導は局所を加熱すること
により達成されるが、その着火温度は1700℃以上が望ま
しく、そのような温度環境を生みだす手段であるならば
いかなる方法でも良いが、一般的にタングステン(W)
線などを用いた通電加熱が利用できる。
For this reason, in the present invention, the reaction propagation is carried out in layers from the lower part to the upper part. That is, in the present invention, heat is also diffused upward as the reaction is propagated upward, but the reaction propagation speed is preferably equal to or higher than the propagation speed of heat in the powder compact, and if the powder compact state can induce the reaction Meets The induction of the reaction is achieved by locally heating, but the ignition temperature is preferably 1700 ° C or higher, and any method can be used as long as it is a means of producing such a temperature environment, but generally tungsten (W)
Electric heating using a wire can be used.

一般的な圧粉体は理論密度の40〜60%が望ましい。ま
た、反応伝播過程で生成する窒素ガスも下部より上方へ
移動するため、反応面後方での高温領域における窒素の
純度は高く、得られる窒化物は高純度となる。窒化反応
は、反応性粉末の融点以上で進行させることが好まし
く、たとえ窒化反応での生成熱が外部に一部放散したと
しても反応系の温度は2000℃以上が望ましい。反応中は
上部より液体窒素を連続的に供給し、試料圧粉体を常に
液体窒素中に維持することが望ましい。反応が上方へ伝
播する場合には、熱の移動も上方であり、さらに反応伝
播速度が反応圧粉体中の熱伝導の速度より速くなるよう
に制御するならば燃焼反応の定常的伝播ができ、後方で
の高温状態の維持時間も長くなり、結果的により効率的
な窒化を達成することができる。また、液体窒素を用い
ると含有不純物が少なく、上方への反応伝播に伴い生成
窒素ガスも上方に移動するため得られる窒化物中の不純
物も少なく高純度な生成物を得ることができる。
For general green compact, 40-60% of theoretical density is desirable. Further, since the nitrogen gas generated in the reaction propagation process also moves upward from the lower part, the purity of nitrogen in the high temperature region behind the reaction surface is high, and the obtained nitride has high purity. The nitriding reaction preferably proceeds at a temperature equal to or higher than the melting point of the reactive powder, and the temperature of the reaction system is preferably 2000 ° C. or higher even if part of the heat generated by the nitriding reaction is dissipated to the outside. During the reaction, it is desirable that liquid nitrogen is continuously supplied from the upper part so that the sample green compact is always kept in liquid nitrogen. When the reaction propagates upward, the heat transfer is also upward, and if the reaction propagation velocity is controlled to be higher than the heat conduction velocity in the reaction compact, steady combustion propagation is possible. In addition, the time for maintaining the high temperature state in the rear also becomes longer, and as a result, more efficient nitriding can be achieved. Further, when liquid nitrogen is used, the amount of impurities contained is small, and the nitrogen gas produced moves upward as the reaction propagates upward, so that the amount of impurities in the obtained nitride is small and a highly pure product can be obtained.

なお、反応を層状に順次段階的に行わせる理由は、反
応温度が急激に4000〜5000℃に上昇すると、チタン粉末
が一部溶融して団塊状の固溶体となり、液体窒素と反応
しない未反応物を生成し、転換率を下げるので好ましく
ない。このために反応は下方より上方に2000℃以上の高
温反応層を層状に形成し、この反応層を逐次上方に進行
させるのがよい。
The reason why the reaction is carried out stepwise in layers is that when the reaction temperature rapidly rises to 4000 to 5000 ° C., the titanium powder is partially melted into a nodular solid solution, which is an unreacted substance that does not react with liquid nitrogen. Is generated and the conversion rate is lowered, which is not preferable. For this reason, the reaction is preferably performed by forming a high temperature reaction layer having a temperature of 2000 ° C. or more in a layered manner from the lower side to the upper side of the reaction layer.

本発明の方法で得られる金属窒化物は、従来の電気炉
を溶いた合成方法に比べ、短時間で合成が可能であり燃
焼過程で活性な元素は除去されるため不純物の少ない高
純度な合成窒化物となる。したがって、半導体分野で拡
散阻止層として注目されている窒化チタン等の出発原料
として充分利用可能な高純度窒化物を供給することがで
きる。
The metal nitride obtained by the method of the present invention can be synthesized in a short time as compared with the conventional synthesis method in which an electric furnace is melted, and active elements are removed in the combustion process, so that high-purity synthesis with few impurities is performed. It becomes a nitride. Therefore, it is possible to supply a high-purity nitride that can be sufficiently used as a starting material such as titanium nitride, which is attracting attention as a diffusion blocking layer in the semiconductor field.

上記の如く、燃焼反応を下部より伝播させ熱およびガ
スの移動を制御することにより、高い転換率を得ること
ができることを見い出し、本発明の提起に至った。
As described above, it has been found that a high conversion can be obtained by propagating the combustion reaction from the lower part and controlling the movement of heat and gas, and has led to the present invention.

以下図面について本発明の高純度チタンの燃焼合成法
の実施の態様について詳細に説明する。
Hereinafter, embodiments of the combustion synthesis method of high-purity titanium according to the present invention will be described in detail with reference to the drawings.

第1図は実験に使用したジュワー瓶の一例を示す断面
であり、1は透明なジュワー瓶(液化ガスの容器とし
て、低温実験に用いる魔法瓶)、2はこの容器中に収納
した液体窒素、3は容器中に収納した耐火煉瓦を示し、
本発明では石英管4中に収納したチタン粉末成形体試料
5を成形体試料の下端面にタングステン線6をチタン粉
成形体試料の着火用に装置し、外部電源(図示せず)に
接続する。7はジュワー瓶の蓋である。ジュワー瓶の上
方を大気に開放するが熱の出入を遮断するものとする。
8は容器外部に設けたトランジエントレコーダーで、導
線9により内部の試料又はそれを保持する石英管4に設
けたセンサ10に接続して、反応伝播速度と温度の変化を
記録した。
FIG. 1 is a cross section showing an example of a dewar used in the experiment, 1 is a transparent dewar (a thermos bottle used for a low temperature experiment as a liquefied gas container), 2 is liquid nitrogen stored in this container, 3 Indicates a refractory brick stored in a container,
In the present invention, the titanium powder compact sample 5 housed in the quartz tube 4 is provided with a tungsten wire 6 on the lower end surface of the compact sample for igniting the titanium powder compact sample and connected to an external power source (not shown). . Reference numeral 7 is a lid for a dewar. The upper part of the dewar should be open to the atmosphere but the heat flow should be blocked.
Reference numeral 8 is a transient recorder provided outside the container, which was connected to a sensor 10 provided on the sample inside or the quartz tube 4 holding the sample by a conductor 9 to record changes in reaction propagation velocity and temperature.

第2図はジュワー瓶以外の他の反応容器の一例を示す
もので、11はアルミ容器、12はこのアルミ容器11に螺合
した蓋部、13は石英管であり、この石英管13中に試料圧
粉体14を保持する。15は試料圧粉体14の下部端面に沿い
配設した着火用タングステン等の耐熱金属線15であり、
容器11中に液体窒素16を充填する。17は電極、18は液体
窒素供給口を示す。
FIG. 2 shows an example of a reaction container other than the dewar, 11 is an aluminum container, 12 is a lid part screwed to the aluminum container 11, and 13 is a quartz tube. The sample green compact 14 is held. 15 is a refractory metal wire 15 such as tungsten for ignition disposed along the lower end surface of the sample green compact 14,
The container 11 is filled with liquid nitrogen 16. Reference numeral 17 is an electrode, and 18 is a liquid nitrogen supply port.

(実施例) 実施例1 チタン粉末25gを充填度58%になるように直径25mmの
円柱状に圧粉成形し、液体窒素を充填したジュワー瓶1
中に配置し、圧粉体試料5の下部に接触させたタングス
テン線6(直径0.5mm)に通電加熱することにより圧粉
体試料5の下部端面に着火し、反応を圧粉体試料13の下
部端面の局部を1700℃以上に加熱し、該圧粉体試料と窒
素との燃焼反応を誘導し、圧粉体試料と窒素の相互作用
を、開始された燃焼反応の結果発生する熱によって、20
0℃以上の高温反応層を形成し、この反応層を層状に逐
次上方に進行させた。
(Example) Example 1 A dewar bottle 1 filled with liquid nitrogen was formed by compacting 25 g of titanium powder into a cylinder having a diameter of 25 mm so that the filling degree was 58%.
The lower end surface of the powder compact sample 5 is ignited by electrically heating the tungsten wire 6 (diameter 0.5 mm) that is placed inside and brought into contact with the lower part of the powder compact sample 5, and the reaction is performed on the powder compact sample 13. By heating the local part of the lower end face to 1700 ° C. or higher, the combustion reaction between the green compact sample and nitrogen is induced, the interaction between the green compact sample and nitrogen, and the heat generated as a result of the initiated combustion reaction, 20
A high temperature reaction layer of 0 ° C. or higher was formed, and this reaction layer was successively advanced upward in layers.

反応は自発的に下方より上方に層状をなして順次伝播
し、その結果、試料の体積変化より推定した窒化物への
転換率は68%であった。この結果は、同様の圧粉体試料
と窒素との反応を上部より下方に伝播させた場合と比べ
約30%高い転換率であった。
The reaction spontaneously propagated in layers from the bottom to the top, and as a result, the conversion rate to nitride estimated from the volume change of the sample was 68%. The result was about 30% higher conversion rate than the case where the reaction between the same green compact sample and nitrogen was propagated downward from the upper part.

実施例2 チタン粉末と窒化チタン粉末の混合粉体25gを充填度5
0%で直径25mmの円柱状に圧粉成形し、液体窒素を充満
したジュワー瓶中に配置し、実施例1と同様な方法で着
火し反応を誘導し伝播させた。その結果、窒化チタン粉
末を20%添加した場合では90%の転換率であった。一
方、上部からの着火を試みたが着火されなかった。
Example 2 25 g of a mixed powder of titanium powder and titanium nitride powder was filled at a filling degree of 5
The powder was compacted into a cylindrical shape having a diameter of 25 mm at 0%, placed in a dewar filled with liquid nitrogen, and ignited in the same manner as in Example 1 to induce and propagate the reaction. As a result, when the titanium nitride powder was added by 20%, the conversion rate was 90%. On the other hand, an attempt was made to ignite it from above, but it did not ignite.

実施例3 I.目 的:本研究では、Ti粉末と窒素との燃焼を利用し
たTiNの燃焼合成において、窒素源を液体窒素とした場
合における高効率燃焼合成の可能性の検討を目的に、反
応伝播方向を上方あるいは下方に変えることによる反応
伝播特性および合成過程の変化を調べた。
Example 3 I. Objective: In the present study, in the combustion synthesis of TiN using combustion of Ti powder and nitrogen, the purpose was to investigate the possibility of high-efficiency combustion synthesis when the nitrogen source was liquid nitrogen. We investigated changes in reaction propagation characteristics and synthesis process by changing the reaction propagation direction upward or downward.

II.実験方法:市販のTi粉末(40μm以下)50gを、種々
の充填度(ρ:40%〜60%)で直径25mmの円柱状に加圧
成形し試料とした。石英管中に保持した試料をジュワー
瓶に満たした液体窒素中に配置し、試料上端あるいは下
端に接触させたタングステン線(0.5mmφ)を通電加熱
することにより着火し、下方あるいは上方への反応を伝
播させた。反応伝播方向に25mm間隔で挿入した熱電対に
より反応過程での温度上昇の時間間隔を測定し、伝播速
度(V)を求めた。得られた合成物の転換率(η)と性
状を調べ、合成過程に及ぼす反応伝播特性の影響を調べ
た。
II. Experimental method: A commercially available Ti powder (40 μm or less) (50 g) was pressure-molded into a cylinder having a diameter of 25 mm at various packing degrees (ρ: 40% to 60%) to obtain a sample. A sample held in a quartz tube is placed in liquid nitrogen filled in a dewar, and a tungsten wire (0.5 mmφ) in contact with the upper or lower end of the sample is energized and ignited to cause a downward or upward reaction. Propagated. The time interval of temperature rise in the reaction process was measured by a thermocouple inserted at 25 mm intervals in the reaction propagation direction, and the propagation velocity (V) was obtained. The conversion (η) and properties of the obtained compound were investigated, and the influence of reaction propagation characteristics on the synthesis process was investigated.

III.結 果:Tiの窒化反応 (Ti+1/2N2→TiN) において約340kJ/molの生成熱が開放されるので、液体
窒素がガス化する過程で必要とする熱量(約12kJ/mol)
を充分補うことができ、着火さえすれば反応は自発的に
伝播する。しかし、TiNの燃焼合成では伝播面後方の高
温状態が転換率を左右すると考えられ、液体窒素の気化
とその気相面を通しての試料と周囲との温度勾配を考慮
すると、必ずしも液体窒素で高い転換率は期待できな
い。特に上方からの反応伝播では、高温部での熱および
気化した窒素の移動が反応伝播との逆方向であるため、
高い転換率は得られないと予想される。上方および下方
からの伝播における伝播速度と転換率の充填度に対する
関係を調べた結果、充填度の増加とともに伝播速度が減
少し転換率が上昇する傾向はいずれも同様であるが、伝
播速度については下方からの伝播が10%程度小さくな
る。(充填度ρ:40%、下方より燃焼時の伝播速度V
(下方):7mm/s、充填度ρ:60%、下方より燃焼時の伝
播速度V(下方):1mm/sとなる)また転換率は特に高充
填度で下方から燃焼時の伝播が大きくなっており(充填
度ρ:55%;下方より燃焼時の転換率η(下方):60%以
上、上方より燃焼時の転換率η(上方):50%以下とな
る)、下方から燃焼時の伝播ではより高い転換率が期待
されることを確認した。
III. Result: The heat of formation of about 340 kJ / mol is released in the nitriding reaction of Ti (Ti + 1 / 2N 2 → TiN), so the amount of heat required in the process of gasification of liquid nitrogen (about 12 kJ / mol)
Can be fully compensated for, and the reaction will spontaneously propagate as long as it is ignited. However, in the combustion synthesis of TiN, it is considered that the high temperature state behind the propagating surface influences the conversion rate, and in consideration of the vaporization of liquid nitrogen and the temperature gradient between the sample and the surroundings through the vapor phase surface, the high conversion of liquid nitrogen is not always necessary. You can't expect a rate. Especially in reaction propagation from above, heat and vaporized nitrogen transfer at high temperature are in the opposite direction to reaction propagation,
High conversion rates are not expected. As a result of investigating the relationship between the propagation velocity and the conversion rate in the propagation from above and below and the filling rate, the tendency that the propagation rate decreases and the conversion rate increases with the increase of the filling degree is the same, but Propagation from below is reduced by about 10%. (Filling degree ρ: 40%, propagation velocity V during combustion from below
(Lower): 7 mm / s, filling degree ρ: 60%, propagation velocity V from lower side during combustion becomes V (lower side): 1 mm / s) Moreover, the conversion rate is particularly high at high filling degree and large propagation from lower side to combustion. (Filling degree ρ: 55%; Conversion rate η (downward): 60% or more from below, combustion conversion rate η (upper): 50% or less from above), combustion from below It was confirmed that a higher conversion rate is expected in the transmission of.

(発明の効果) 本発明によれば、液体窒素を用いての窒化物の高速、
高純度、高効率合成を達成させるために反応の伝播方向
を上方とするようにしたので、燃焼での生成熱を有効に
活用し高い転換率を達成している。本発明による製造方
法は、従来の燃焼による方法の伝播方向を変換すること
に特徴を有しているので、その方法実施のための装置も
簡単なものとすることができ、直ちに実施可能なものと
して工業的に価値がある。
(Effects of the Invention) According to the present invention, high-speed nitride using liquid nitrogen,
In order to achieve high-purity and high-efficiency synthesis, the propagation direction of the reaction is set to the upper direction, so the heat of formation of combustion is effectively utilized and a high conversion rate is achieved. Since the manufacturing method according to the present invention is characterized in that the propagation direction of the conventional combustion method is changed, the apparatus for carrying out the method can be simplified and can be immediately implemented. As industrially valuable.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明方法の実験に使用したジュワー瓶の断面
図、 第2図は本発明方法の実施に使用した反応容器の概略構
成を示す断面図である。 1……ジュワー瓶 2……液体窒素 3……耐火煉瓦 4……石英管 5……圧粉体試料 6……着火用タングステン線 7……蓋 8……トランジエントレコーダー 9……導線 10……熱電堆 11……アルミニウム製反応容器 12……蓋 13……石英管 14……圧粉体試料 15……着火用タングステン線 16……液体窒素 17……電極 18……液体窒素供給口 19……電極挿入口 20……液体窒素供給用ロート
FIG. 1 is a cross-sectional view of a dewar used for an experiment of the method of the present invention, and FIG. 2 is a cross-sectional view showing a schematic configuration of a reaction container used for carrying out the method of the present invention. 1 …… Dewar bottle 2 …… Liquid nitrogen 3 …… Refractory brick 4 …… Quartz tube 5 …… Powder compact sample 6 …… Ignition tungsten wire 7 …… Lid 8 …… Transient recorder 9 …… Conductor 10… … Thermoelectric stack 11 …… Aluminum reaction vessel 12 …… Lid 13 …… Quartz tube 14 …… Powder compact sample 15 …… Ignition tungsten wire 16 …… Liquid nitrogen 17 …… Electrode 18 …… Liquid nitrogen supply port 19 ...... Electrode insertion port 20 ...... Fluid for supplying liquid nitrogen

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】金属チタン粉末圧粉体を液体窒素を充填し
た反応容器中に配置し、前記圧粉体の下部端面にタング
ステン線等の耐熱性導体を配設し、これを外部の電源に
接続し、通電により圧粉体の下部表面の一部を1700℃以
上に加熱して該圧粉体と窒素との燃焼反応を誘導し、燃
焼反応に引き続く該圧粉体の構成粉末内部への窒素の拡
散に伴う自発的な金属チタンの窒化反応を促進し、開始
された燃焼過程の結果発生する熱によって2000℃以上の
高温反応層を形成し、この反応層を層状に逐次上方へ進
行させることを特徴とする高純度TiNの燃焼合成法。
1. A metal titanium powder green compact is placed in a reaction vessel filled with liquid nitrogen, and a heat resistant conductor such as a tungsten wire is placed on the lower end face of the green compact, which is used as an external power source. By connecting and energizing, a part of the lower surface of the green compact is heated to 1700 ° C. or more to induce a combustion reaction between the green compact and nitrogen, and the internal combustion of the powder inside the constituent powder of the green compact following the combustion reaction. It promotes the spontaneous nitriding reaction of titanium metal with the diffusion of nitrogen, and the heat generated as a result of the initiated combustion process forms a high temperature reaction layer of 2000 ° C or higher, and the reaction layer is successively advanced upward in layers. Combustion synthesis method of high-purity TiN characterized by the following.
JP2243882A 1990-09-17 1990-09-17 Combustion synthesis method of high-purity TiN Expired - Lifetime JPH0825729B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2243882A JPH0825729B2 (en) 1990-09-17 1990-09-17 Combustion synthesis method of high-purity TiN

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2243882A JPH0825729B2 (en) 1990-09-17 1990-09-17 Combustion synthesis method of high-purity TiN

Publications (2)

Publication Number Publication Date
JPH04124007A JPH04124007A (en) 1992-04-24
JPH0825729B2 true JPH0825729B2 (en) 1996-03-13

Family

ID=17110389

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2243882A Expired - Lifetime JPH0825729B2 (en) 1990-09-17 1990-09-17 Combustion synthesis method of high-purity TiN

Country Status (1)

Country Link
JP (1) JPH0825729B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10293418A (en) * 1997-04-21 1998-11-04 Toyo Ink Mfg Co Ltd Electrostatic image developing toner and image forming method using the toner
CN114728787A (en) * 2019-12-05 2022-07-08 株式会社德山 Method for producing metal nitride

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6276906A (en) * 1985-09-30 1987-04-09 Toshiba Corp Noise generator

Also Published As

Publication number Publication date
JPH04124007A (en) 1992-04-24

Similar Documents

Publication Publication Date Title
KR870011062A (en) Molded ceramic hybrids and its manufacturing method
US4632849A (en) Method for making a fine powder of a metal compound having ceramic coatings thereon
JPS6330062B2 (en)
US4145224A (en) Method for enhancing the crystallization rate of high purity amorphous Si3 N4 powder, powders produced thereby and products therefrom
US6168752B1 (en) Process for producing metal powders and apparatus for producing the same
JPH0155201B2 (en)
TW201127747A (en) Manufacturing method for AlN
JPS5913442B2 (en) Manufacturing method of high purity type silicon nitride
JPH0825729B2 (en) Combustion synthesis method of high-purity TiN
Costantino et al. High pressure combustion synthesis of aluminum nitride
CN102531611B (en) Method for preparing aluminum nitride
TWI253437B (en) Method and apparatus for preparing aluminum nitride
US4656021A (en) Method for the production of silicon
US3862020A (en) Production method for polycrystalline semiconductor bodies
KR100386510B1 (en) Method for Preparing Aluminum Nitride Powder by Self-propagating High-temperature Synthesis
KR100461962B1 (en) Process for producing composite powders of metallic oxides/nitride compounds
Puszynski Thermochemistry and kinetics
JPH0649640B2 (en) Method for manufacturing aluminum nitride Isca
JPH059009A (en) Production of intermetallic compound and ceramics
Wang Chemical vapor deposition and its applications in inorganic synthesis
JPH01197309A (en) Production of granular silicon
KR950005295B1 (en) Method for preparing titanium compound
CN100398432C (en) Synthetic method of aluminum nitride
EP0140625A1 (en) Tellurides
RU2207979C1 (en) Method and apparatus for producing silicon monoxide

Legal Events

Date Code Title Description
S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term