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JPS6011104B2 - Gas phase plating method - Google Patents
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JPS6011104B2 - Gas phase plating method - Google Patents

Gas phase plating method

Info

Publication number
JPS6011104B2
JPS6011104B2 JP8791377A JP8791377A JPS6011104B2 JP S6011104 B2 JPS6011104 B2 JP S6011104B2 JP 8791377 A JP8791377 A JP 8791377A JP 8791377 A JP8791377 A JP 8791377A JP S6011104 B2 JPS6011104 B2 JP S6011104B2
Authority
JP
Japan
Prior art keywords
reaction
plated
plating
paper
heating element
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
Application number
JP8791377A
Other languages
Japanese (ja)
Other versions
JPS5423039A (en
Inventor
重威 岡本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP8791377A priority Critical patent/JPS6011104B2/en
Publication of JPS5423039A publication Critical patent/JPS5423039A/en
Publication of JPS6011104B2 publication Critical patent/JPS6011104B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/458Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for supporting substrates in the reaction chamber

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Vapour Deposition (AREA)

Description

【発明の詳細な説明】 本発明は、気相メッキ法の改良に関するものである。[Detailed description of the invention] The present invention relates to improvements in vapor phase plating methods.

従来、気相メッキにおいては第1図に示すように管状炉
1により反応管2の外部から被メッキ物3を加熱するの
が普通であるが、この場合、ペーパーソースは反応管2
の内壁付近で反応してペーパー密度が低下し、被メッキ
物3への葵着速度が低下する。
Conventionally, in gas phase plating, it is common to heat the object 3 to be plated from the outside of the reaction tube 2 using a tube furnace 1 as shown in FIG.
The reaction occurs near the inner wall of the paper, the density of the paper decreases, and the rate of adhesion of the paper to the object 3 to be plated decreases.

例えば四塩化チタンの場合について説明すると、気相メ
ッキに最適な温度は1気圧(76皿orr)において9
00〜1200℃であって、キャリャガスの水素との還
元反応により、Tic14十2日2900〜1200。
For example, in the case of titanium tetrachloride, the optimal temperature for vapor phase plating is 9
00-1200°C, Tic 14 12 days 2900-1200 due to the reduction reaction with hydrogen of the carrier gas.

〇Ti十虹HCIなる反応でチタンを析出し、反応が進
むに従って四塩化チタンペーパーの分圧が低下し、塩化
水素の分圧が上昇する。そして、上述したように反応管
2の外部から管状炉1によって加熱すると、反応管の内
壁付近の領域a,の温度が管中央の被メッ,キ物の付近
の領域a2よりも気相メッキに適した温度に加熱される
ことになり、従ってペーパーソ−スが領域a,で反応し
、被メッキ物に対する効率的なメッキを行うことができ
ない。加えるに、流動方式の反応管では、第2図に示す
ように多数の被メッキ物3,,32,38・・・・・・
・・・・・・・・・3nを反応管2の軸方向に配列させ
、矢印で示す方向にペーパーを流した場合、第3図に模
式的に示すように、ペーパー入口4付近から漸次ペーパ
ー密度が低下し、蒸着膜の厚さは被メッキ物3,から3
nと出口5に近づくに従って薄くなる。
Titanium is precipitated by a reaction called 〇Ti-HCl HCI, and as the reaction progresses, the partial pressure of the titanium tetrachloride paper decreases and the partial pressure of hydrogen chloride increases. As described above, when the reaction tube 2 is heated from the outside by the tube furnace 1, the temperature of the region a near the inner wall of the reaction tube becomes higher than that of the region a2 near the object to be plated in the center of the tube. Therefore, the paper source reacts in area a, and the object to be plated cannot be plated efficiently. In addition, in the flow type reaction tube, a large number of objects to be plated 3, 32, 38... as shown in FIG.
......3n are arranged in the axial direction of the reaction tube 2 and the paper is flowed in the direction shown by the arrow, as shown schematically in Fig. 3, the paper gradually flows from the vicinity of the paper inlet 4. The density decreases, and the thickness of the deposited film decreases from 3 to 3.
It becomes thinner as it approaches n and exit 5.

そして、その膜厚の誤差は、諸条件によって異るが、通
常40〜60%と言われている。従って、正確な膜厚を
必要とする製品については、第2図に示すような反応管
による量産工程の流れの中では許容誤蔓葦範囲におさま
る製品が少なく歩留りが非常に悪くなる。例えば、スロ
ーアウエーチツプへのTICコーテイングにおいては、
5仏の厚さが適当とされるが、その許容誤差が±10%
であるため、上述の量産工程によりメッキを行うことは
不適当である。本発明は、上述した問題を解決するため
、反応容器の中央に配直した発熱体によりペーパーソー
スが気相メッキに最適な温度に加熱される領域に被メッ
キ物を配遣して、効率的な気相メッキを行い、しかも量
産的な気相メッキにおける膜厚誤差を僅少にとどめ、膜
厚が略均等なメッキを能率的に行う方法を提供しようと
するものである。
The error in film thickness varies depending on various conditions, but is usually said to be 40 to 60%. Therefore, for products that require accurate film thickness, in the mass production process using reaction tubes as shown in FIG. 2, there are few products that fall within the allowable error range, and the yield is extremely poor. For example, in TIC coating on throwaway chips,
5 The thickness of the Buddha is considered to be appropriate, but the tolerance is ±10%.
Therefore, it is inappropriate to perform plating using the above-mentioned mass production process. In order to solve the above-mentioned problems, the present invention efficiently distributes the object to be plated in an area where the paper source is heated to the optimum temperature for vapor phase plating by a heating element arranged in the center of the reaction vessel. The purpose of the present invention is to provide a method for efficiently performing plating with a substantially uniform film thickness by performing vapor phase plating with minimal film thickness errors in mass-produced vapor phase plating.

また、上記反応容器の中央に配置した発熱体によって得
られる温度分布と略同等のものは、高周波加熱によって
も得ることができる。事実、高周波加熱によって反応管
の中央に配置した被メッキ物を加熱した場合、葵着速度
は管状炉により反応管の外側から加熱した場合よりもは
るかに速くなり、このことは本発明において反応容器の
中央に発熱体を配置することが効率的な気相メッキを行
うために有効であることを裏付けている。しかし、高周
波加熱を利用した場合、18一8ステンレス、モリブデ
ン、磁器等の非磁性材料に対しては気相メッキを行うこ
とができない。
Further, a temperature distribution substantially equivalent to that obtained by the heating element placed in the center of the reaction vessel can also be obtained by high frequency heating. In fact, when the object to be plated placed in the center of the reaction tube is heated by high-frequency heating, the deposition rate is much faster than when the object is heated from the outside of the reaction tube using a tube furnace. This proves that placing the heating element in the center of the plate is effective for efficient vapor phase plating. However, when high frequency heating is used, vapor phase plating cannot be performed on non-magnetic materials such as 18-8 stainless steel, molybdenum, and porcelain.

また、形状が多少複雑なものは温度が不均一になること
から場合によってメッキすることが不可能となる。本発
明は、このような高周波加熱による場合の欠点をも解決
し、簡単な装置により、被メッキ物の材料、形状、大き
さ等による制約を受けずに気相メッキを行い得る方法を
提供しようとするものである。
Furthermore, if the shape is somewhat complex, the temperature will be uneven, making it impossible to plate it in some cases. The present invention solves the drawbacks of using high-frequency heating, and provides a method that allows vapor phase plating to be performed using a simple device without being constrained by the material, shape, size, etc. of the object to be plated. That is.

即ち、本発明は、反応容器の中央に発熱体を配設し、上
記発熱体による加熱により反応容器内に形成される気相
メッキに通した反応温度領域に被メッキ物を配置すると
共に、その周囲に形成されるペーパーソースの気化温度
領域にべーパ−ソー「スを供給し、上記反応温度領域に
おいて被メッキ物上にメッキ膜を析出させた後の反応生
成物を反応温度領域の内側から排出させることを特徴と
するものである。
That is, in the present invention, a heating element is disposed in the center of a reaction vessel, and an object to be plated is placed in a reaction temperature region through which vapor phase plating is formed in the reaction vessel by heating with the heating element, and A vapor source is supplied to the vaporization temperature region of the paper source that is formed around the paper source, and a plating film is deposited on the object to be plated in the above reaction temperature region.The reaction product is then deposited inside the reaction temperature region. It is characterized by being discharged from.

さらに具体的に説明すると、本発明においては、第4図
に示すように、発熱体11を反応容器10の中央に配設
するため、反応容器10内の温度分布は、外側をペーパ
ーソースの気化に適する程度の温度に、内側をペーパー
ソースの反応に適する程度に高い温度にすることができ
、そこでこの反応容器10内の周囲からペーパーソース
を供給すると共に、その内側に被メッキ物を配置してメ
ッキを行う場合には、‘1ー ベーパーソースが気化す
る最外層の気化温度領域へ【2’ペーパーソースの反応
によるメッキに適した中間層の反応温度領域ん{3’
メッキには寄与しない反応生成物の密度が高く、ペーパ
ーソースの分圧が低下した最内層の排出成分領域んが生
じ、そのため排出成分領域A3から反応生成物を排出さ
せれば、簡単な装置により極めて効率的で膜厚が略均一
なメッキを行うことができる。
To explain more specifically, in the present invention, as shown in FIG. The inside temperature can be raised to a temperature suitable for the reaction of the paper source, and the paper source is supplied from the surroundings of this reaction vessel 10, and the object to be plated is placed inside the reaction vessel 10. When plating is performed using plating, it is necessary to change the temperature range from 1 to the vaporization temperature range of the outermost layer where the vapor source evaporates;
There is a discharged component region in the innermost layer where the density of reaction products that do not contribute to plating is high and the partial pressure of the paper source is reduced. Plating can be performed extremely efficiently and with a substantially uniform film thickness.

このような本発明の気相メッキ法は、バレル方式または
バッチ方式のメッキに適用することができ、また縦型及
び横型のいずれでも差支えない。さらに、ペーパーソー
スの気化室を別個に設けることなく、直接反応容器内の
気化温度領域にそれを供給して気化させることもできる
。第5図は本発明の方法を実施するバレル方式の気相メ
ッキ装置の一例を示すものである。
The vapor phase plating method of the present invention can be applied to barrel-type or batch-type plating, and may be either vertical or horizontal plating. Furthermore, without providing a separate vaporization chamber for the paper source, it is also possible to directly supply the paper source to the vaporization temperature region within the reaction vessel and vaporize it. FIG. 5 shows an example of a barrel type vapor phase plating apparatus for carrying out the method of the present invention.

この気相メッキ装置においては、円筒状の反応容器10
を支柱12によって支持させ、この反応容器10の中央
に発熱体11を収容した保護管13を固定すると共に、
周囲にペーパーソースをキャリャガスと共に供給する供
V給管1 4を接続し、発熱体11のまわりに被メッキ
物15を収容するための多孔の回転バレル16を回転可
能に支持させている。
In this vapor phase plating apparatus, a cylindrical reaction vessel 10
is supported by struts 12, and a protective tube 13 containing a heating element 11 is fixed in the center of this reaction vessel 10,
A supply pipe 14 for supplying a paper source together with a carrier gas is connected to the periphery, and a rotary barrel 16 with holes for accommodating an object to be plated 15 is rotatably supported around the heating element 11.

この回転バレル16は、その駆動軸17を反応容器から
気密に導出して回転駆動のためのプーリ18を固定し、
また他端の支持軸19を中空筒状に形成して、その支持
軸内部を、回転バレル16の中央部から高密度の反応生
成物を含む排出成分を外部に排出するための排出管20
‘こ接続したものであり、回転バレル16内には、必要
に応じて被メッキ物15を縄拝するための櫨梓翼板21
を設けることができる。上記発熱体1 1に接続した電
源22は、回転バレル16に近接した位置の温度を熱電
対23で検出して温度調節器24によりその温度が適正
な温度になるように制御されるものであり、これによっ
て反応容器10の周壁と回転バレル16との間に前記気
化温度領域A,が形成され、また回転バレル16内にお
ける被メッキ物15の付近に反応温度領域んが形成され
る。
The rotating barrel 16 has its drive shaft 17 airtightly led out from the reaction vessel, and a pulley 18 for rotational driving is fixed thereon.
Further, the support shaft 19 at the other end is formed into a hollow cylindrical shape, and the inside of the support shaft is connected to a discharge pipe 20 for discharging discharge components including high-density reaction products from the center of the rotating barrel 16 to the outside.
Inside the rotating barrel 16, there is a cylindrical blade plate 21 for holding the object 15 to be plated as required.
can be provided. The power source 22 connected to the heating element 11 detects the temperature near the rotating barrel 16 with a thermocouple 23 and is controlled by a temperature regulator 24 so that the temperature is at an appropriate temperature. As a result, the vaporization temperature region A is formed between the peripheral wall of the reaction vessel 10 and the rotating barrel 16, and a reaction temperature region A is also formed in the vicinity of the object to be plated 15 within the rotating barrel 16.

なお、図中25はラバーシール、26は断熱材、27は
真空ポンプに接続してメッキに際し反応容器内の空気を
排出する排気管、28はペーパ一気化領域温度測定用温
度計を示している。
In the figure, 25 is a rubber seal, 26 is a heat insulating material, 27 is an exhaust pipe connected to a vacuum pump to exhaust air from the reaction vessel during plating, and 28 is a thermometer for measuring the temperature of the paper vaporization area. .

また、第6図は本発明の方法を実施するバッチ方式の気
相メッキ装置の一例を示すもので、反応容器30の中央
に図示しない電源に接続した発熱体31を配設し、反応
容器30の一端にはペーパーソースをキャリャガスと共
に供給する供給管32を設け、この供給管32から、反
応容器30の周囲の気化温度領域A,を形成する通路3
3にペーパーソースを導びくように構成し、またその気
化温度領域公,の内側の反応温度領域んに被メッキ物3
4を戦層する教導台35を列設し、この戦層台35と発
熱体31との間の空間から高密度の反応生成物を含む排
出成分を排出するように、反応容器30の端部に排出管
36を接続している。なお、第5図の装置と同様に熱電
対及び温度調節器を設けて、反応容器30内の温度を適
正に保つように電源を制御することができる。以上に詳
述した本発明の方法によれば、極めて簡単な装置により
、気相メッキに適した反応温度領域に被メッキ物を配贋
して、高周波加熱手段を用いた場合と同様の蒸着速度を
もって効率的に気相メッキを行うことができ、また被メ
ッキ材料の材質や形状、大きさに関係なく、膜厚が略均
一な気相メッキを行なうことができる。
Further, FIG. 6 shows an example of a batch type vapor phase plating apparatus for carrying out the method of the present invention, in which a heating element 31 connected to a power source (not shown) is disposed in the center of the reaction vessel 30. A supply pipe 32 for supplying the paper source together with a carrier gas is provided at one end, and from this supply pipe 32 a passage 3 forming a vaporization temperature region A around the reaction vessel 30 is provided.
3, and the material to be plated 3 is connected to the reaction temperature region inside the vaporization temperature region.
The end of the reaction vessel 30 is arranged such that a teaching table 35 having a heating element 4 is disposed in a row, and an exhaust component containing a high-density reaction product is discharged from a space between the training table 35 and the heating element 31. A discharge pipe 36 is connected to. Note that, similarly to the apparatus shown in FIG. 5, a thermocouple and a temperature regulator can be provided to control the power supply so as to maintain the temperature inside the reaction vessel 30 appropriately. According to the method of the present invention detailed above, the object to be plated is placed in a reaction temperature range suitable for vapor phase plating using an extremely simple device, and the deposition rate is the same as when using high frequency heating means. This makes it possible to perform vapor phase plating efficiently, and it is also possible to perform vapor phase plating with a substantially uniform film thickness regardless of the material, shape, and size of the material to be plated.

本発明に基づいて気相メッキを行う場合の膜厚の均一性
に関し、次のような実験結果を得た。
Regarding the uniformity of film thickness when performing vapor phase plating based on the present invention, the following experimental results were obtained.

なお、本発明の実施においては、反応容器の中央に発熱
体を配設してその周辺に被メッキ物を配置する必要があ
るが、この場合には反応容器として太蓬管等を備えた実
用機相当の大型装置を用いる必要があり、そのため実験
室規模において実施することは、例えば大出力の電源を
必要とするなど、現実的に種々の困難な問題がある。従
って、ここでは、膜厚の均一性の良否を確認するうえで
支障がないと考えられる範囲内において実験装置の小型
化を考慮した。実験装置は、第7図に示すような構造を
有するものである。
In carrying out the present invention, it is necessary to arrange a heating element in the center of the reaction vessel and place the object to be plated around it. It is necessary to use a large device equivalent to a machine, and therefore implementing it on a laboratory scale poses various practical problems, such as the need for a high-output power source. Therefore, here, miniaturization of the experimental apparatus was considered within a range that would not pose a problem in confirming the quality of film thickness uniformity. The experimental apparatus had a structure as shown in FIG.

即ち、内径4仇吻で約1肌の長さを有するガラス製反応
管40の両端を封止部材41,42によって閉鎖し、両
封止部材41,42に設けた電極43,44間に1側め
で長さ90比舷のモリブデン線45を張設して、これを
被メッキ物とした。この場合、管40の径が小さいため
に排出管48の径はさらに小さくなりその中に所定容量
の加熱体を別個に設けることは困難であり、そのため電
源を安定させるスタビライザーを用いて被メッキ物のモ
リブデン線自体に電源43,44を通して通電すること
により、それを所定の温度に加熱制御できるようにした
。これにより赤熱したモリブデン線は、後述するように
、排出管48内に設けた発熱体からの熱によって加熱さ
れたもと等価であると考えられる。46はメッキペーパ
ーを供v給するペーパー入口管、47はペーパー出口管
で、このペーパー出口管47には、反応管40内をその
軸線方向にモリブデン線45と近接平行しながら伸びて
入口管46の近傍まで達する反応ガス排出管48を蓮設
した。
That is, both ends of a glass reaction tube 40 having an inner diameter of 4 mm and a length of approximately 1 skin are closed by sealing members 41 and 42, and a 1. A molybdenum wire 45 having a length of 90 mm was stretched on the side, and this was used as the object to be plated. In this case, since the diameter of the pipe 40 is small, the diameter of the discharge pipe 48 is even smaller, and it is difficult to separately install a heating element of a predetermined capacity therein. By energizing the molybdenum wire itself through power sources 43 and 44, it is possible to control heating to a predetermined temperature. The red-hot molybdenum wire is considered to be equivalent to the molybdenum wire heated by the heat from the heating element provided in the discharge pipe 48, as will be described later. Reference numeral 46 indicates a paper inlet pipe for supplying plating paper, and reference numeral 47 indicates a paper outlet pipe.The paper outlet pipe 47 has an inlet pipe 46 extending in the axial direction of the reaction tube 40 in close proximity to and parallel to the molybdenum wire 45. A reaction gas discharge pipe 48 was installed to reach the vicinity of the reactor.

この反応ガス排出管48は、2側めの反応ガス流入孔4
9を2仇岬間隔で穿設したものである。上記装置におい
て、発熱体としてのモリブデン線45を通電により発熱
させると、そのまわりに反応温度領域が形成されると共
に、さらにその領域の外側に気化温度領域が形成される
This reaction gas discharge pipe 48 is connected to the reaction gas inflow hole 4 on the second side.
9 were drilled at intervals of two capes. In the above device, when the molybdenum wire 45 as a heating element is energized to generate heat, a reaction temperature region is formed around the molybdenum wire 45, and a vaporization temperature region is further formed outside the region.

このことは、反応温度領域の中央にモリブデン線45則
ち被メッキ物が配置されていることを意味する。そして
、ペーパー入口管46からメッキペーパーを気化温度領
域に供給すると赤熱したモリブデン線45の周辺の反応
温度領域に達し、その領域で気化したメッキペーパーが
モリブデン線45の表面′で気相メッキ反応した後、反
応生成物が被メッキ物の表面から拡散し、その反応生成
物は反応ガス排出管48内に流入し、やがてペーパ一出
口管47から流出する。従って、上記装置は、発熱体と
被メッキ物とを同じ物とした′点及び反応生成物を被メ
ッキ物の周囲から排出するようにした点において、第5
図及び第6図の装置と異なるものの、それらの装置は、
所要の温度領域の形成という点に関しては共に原理的に
等価な装置ということができる。
This means that the molybdenum wire 45, ie, the object to be plated, is placed in the center of the reaction temperature region. When the plating paper is supplied to the vaporization temperature region from the paper inlet pipe 46, it reaches the reaction temperature region around the red-hot molybdenum wire 45, and the plating paper vaporized in that region undergoes a vapor phase plating reaction on the surface of the molybdenum wire 45. Thereafter, the reaction product diffuses from the surface of the object to be plated, flows into the reaction gas discharge pipe 48, and eventually flows out from the paper outlet pipe 47. Therefore, the above-mentioned apparatus has the fifth feature in that the heating element and the object to be plated are the same, and the reaction products are discharged from around the object to be plated.
Although different from the devices shown in FIGS.
In terms of forming the required temperature range, both devices can be said to be equivalent in principle.

即ち、発熱体及び被メッキ物として同一の物を用いても
、その違いは加熱方式の違いに過ぎず、いずれにしても
被メッキ物の近辺に反応温度領域が、その外側に気化温
度領域がそれぞれ形成され、その意味において技術的に
等価なものである。従って、第7図に示す装置による気
相メッキ法の実施は、本発明の予備的な実験として有効
なものである。一方、比較例として上記第7図に示す装
置において反応ガス排出管48を備えない場合について
も同条件で実験を行った。
In other words, even if the same heating element and the object to be plated are used, the difference is only in the heating method, and in any case, the reaction temperature region is near the object to be plated, and the vaporization temperature region is outside it. and are technically equivalent in that sense. Therefore, the implementation of the vapor phase plating method using the apparatus shown in FIG. 7 is effective as a preliminary experiment of the present invention. On the other hand, as a comparative example, an experiment was also conducted under the same conditions for the apparatus shown in FIG.

この実験も、本発明によらない通常のCVD法と等価で
あることはいうまでもない。この2つの実験におけるメ
ッキ条件は、共にメッキ温度(被メッキ物温度)115
ぴ0、メッキ時間地r、メッキペーパー流量150ノm
inとし、上記モリブデン線に窒化チタンメッキを行っ
た。
It goes without saying that this experiment is also equivalent to a normal CVD method that is not based on the present invention. The plating conditions in these two experiments were both plating temperature (temperature of the plated object) 115
Pi 0, plating time r, plating paper flow rate 150 nm
The molybdenum wire was plated with titanium nitride.

上記条件により気相メッキを行った結果、同様な装置に
よって反応管の外周から加熱する場合に比して、平均的
に40%増程度の膜厚を得ることができ、特に本発明の
ように反応容器内に発熱体を設ける内熱式は装置の設計
、メッキ原料の節約の点で有効であることが確認された
As a result of performing vapor phase plating under the above conditions, it was possible to obtain a film thickness that was approximately 40% larger on average than when heating from the outer periphery of the reaction tube using a similar device. The internal heating method, in which a heating element is installed inside the reaction vessel, has been confirmed to be effective in terms of equipment design and saving of plating raw materials.

また、第8図は上記実験によって得られたメッキ膜の厚
さの分布を示すものである。
Moreover, FIG. 8 shows the distribution of the thickness of the plating film obtained by the above experiment.

ここに示す膜厚は、メッキを行ったモリ‐プデン線の入
口管46側から出口管47側に至る45肋毎の各区分内
における平均膜厚である。なお、メッキに際して電極4
3,44を冷却したため、その電極43,44に取付け
た被メッキ物のモリブデン線の両端側が冷却され、従っ
て濃厚の測定はモリブデン線が均熱化している中央部分
のみについて行った。第8図からわかるように、第T図
の実験袋直では膜厚の変動が極めて少ないのに対し、反
応ガス排出管48を取付けない場合には著しい変動を示
し、これによって本発明では反応ガス排出管が極めて有
効に作用し、腰厚を均一化できることがわかる。
The film thickness shown here is the average film thickness within each section of every 45 ribs from the inlet pipe 46 side to the outlet pipe 47 side of the plated molybdenum wire. In addition, when plating, the electrode 4
3 and 44, both ends of the molybdenum wire of the object to be plated attached to the electrodes 43 and 44 were cooled. Therefore, the concentration measurement was performed only on the central portion where the molybdenum wire was uniformly heated. As can be seen from FIG. 8, while there is very little variation in the film thickness directly from the experimental bag in FIG. It can be seen that the discharge pipe works extremely effectively and can even out the waist thickness.

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

第1図は従来の気相メッキ装置の温度分布について説明
するための断面図、第2図は従来の装置における膜厚誤
差について説明するための縦断面図、第3図は第2図の
装置におけるペーパーソ−スの分圧に関する説明図、第
4図は本発明についての原理説明図、第5図及び第6図
は本発明の方法を実施するバレル方式及びバッチ方式の
メッキ装置の断面図、第7図は本発明に関する実験に使
用した装置の断面図、第8図は実験結果を示す線図であ
る。 10,30・・・・・・反応溶器、1 1,31・・・
・・・発熱体、15,34……被メッキ物、ん……気化
温度領域、ん・・・・・・反応温度領域。 筋1図 繁2麹 繁8髄 第4隣 第5図 繁8図 繁7函 鰭8翼
Figure 1 is a cross-sectional view to explain the temperature distribution of a conventional vapor phase plating apparatus, Figure 2 is a longitudinal cross-sectional view to explain film thickness errors in the conventional apparatus, and Figure 3 is the apparatus of Figure 2. FIG. 4 is an explanatory diagram of the principle of the present invention; FIGS. 5 and 6 are cross-sectional views of barrel-type and batch-type plating equipment for carrying out the method of the present invention; FIG. 7 is a sectional view of the apparatus used in experiments related to the present invention, and FIG. 8 is a diagram showing the experimental results. 10,30... Reaction vessel, 1 1,31...
... Heating element, 15, 34 ... Object to be plated, N... Vaporization temperature range, N... Reaction temperature range. Line 1 diagram Shigeru 2 Koji Shigeru 8 pith 4th neighbor Figure 5 Shigeru 8 diagram Shigeru 7 box fin 8 wings

Claims (1)

【特許請求の範囲】[Claims] 1 反応容器の中央に発熱体を配設し、上記発熱体によ
る加熱により反応容器内に形成される気相メツキに適し
た反応温度領域に被メツキ物を配置すると共に、その周
囲に形成されるベーパーソースの気化温度領域にベーパ
ーソースを供給し、上記反応温度領域において被メツキ
物上にメツキ膜を析出させた後の反応生成物を反応温度
領域の内側から排出させることを特徴とする気相メツキ
法。
1. A heating element is disposed in the center of the reaction vessel, and the object to be plated is placed in a reaction temperature range suitable for gas phase plating formed in the reaction vessel by heating by the heating element, and the object to be plated is placed in a reaction temperature range suitable for gas phase plating, which is formed around it. A vapor phase characterized by supplying a vapor source to a vaporization temperature region of the vapor source, depositing a plating film on the object to be plated in the reaction temperature region, and discharging the reaction product from inside the reaction temperature region. Metsuki method.
JP8791377A 1977-07-22 1977-07-22 Gas phase plating method Expired JPS6011104B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8791377A JPS6011104B2 (en) 1977-07-22 1977-07-22 Gas phase plating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8791377A JPS6011104B2 (en) 1977-07-22 1977-07-22 Gas phase plating method

Publications (2)

Publication Number Publication Date
JPS5423039A JPS5423039A (en) 1979-02-21
JPS6011104B2 true JPS6011104B2 (en) 1985-03-23

Family

ID=13928149

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8791377A Expired JPS6011104B2 (en) 1977-07-22 1977-07-22 Gas phase plating method

Country Status (1)

Country Link
JP (1) JPS6011104B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2733254B1 (en) * 1995-04-18 1997-07-18 Europ Propulsion CHEMICAL VAPOR INFILTRATION PROCESS FOR THE DENSIFICATION OF POROUS SUBSTRATES DISPOSED IN RING STACKS

Also Published As

Publication number Publication date
JPS5423039A (en) 1979-02-21

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