JPH0665757A - Formation of particulate film by gas deposition and forming device therefor - Google Patents

Formation of particulate film by gas deposition and forming device therefor

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Publication number
JPH0665757A
JPH0665757A JP22304692A JP22304692A JPH0665757A JP H0665757 A JPH0665757 A JP H0665757A JP 22304692 A JP22304692 A JP 22304692A JP 22304692 A JP22304692 A JP 22304692A JP H0665757 A JPH0665757 A JP H0665757A
Authority
JP
Japan
Prior art keywords
fine particle
film
substrate
fine particles
forming
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
Application number
JP22304692A
Other languages
Japanese (ja)
Other versions
JP3154213B2 (en
Inventor
Hidetsugu Fuchida
英嗣 渕田
Masaaki Oda
正明 小田
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.)
Vacuum Metallurgical Co Ltd
Original Assignee
Vacuum Metallurgical Co Ltd
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 Vacuum Metallurgical Co Ltd filed Critical Vacuum Metallurgical Co Ltd
Priority to JP22304692A priority Critical patent/JP3154213B2/en
Publication of JPH0665757A publication Critical patent/JPH0665757A/en
Application granted granted Critical
Publication of JP3154213B2 publication Critical patent/JP3154213B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To provide the method for formation of a particulate film by a gas deposition method for forming the particulate having good adhesion to a substrate and the improved density free from flocs and the forming device therefor. CONSTITUTION:This method for formation of the particulate film consists in transporting the particulates formed by an evaporating source 7 to a rectilinear state by using a rectilinear transporting pipe 3 at the time of transporting the above-mentioned particulates together with a carrier gas onto a substrate 13. This particulate film forming device by the gas deposition method consists in forming the transporting pipe 3 connecting a particulate forming chamber 1 and a film forming chamber 2 to a rectilinear state without having a bend in the middle between the part above the evaporating source 7 and the substrate 13.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ガス・デポジション法
による微粒子膜の形成法およびその形成装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for forming a fine particle film by a gas deposition method and an apparatus for forming the same.

【0002】[0002]

【従来の技術】従来、この種の形成装置としては、例え
ば図6に示すような、微粒子膜材料aを加熱蒸発させる
蒸発源bを配設した微粒子生成室cと、該微粒子生成室
cより微粒子をキャリアガスと共に搬送する搬送管d
と、該搬送管dの先端に接続せるノズルeと、該ノズル
eより微粒子とキャリアガスを噴射せしめて微粒子膜f
を形成するための移動自在の基板gを配設した膜形成室
hとからなり、微粒子生成室cと膜形成室hを同一平面
上に配置し、微粒子生成室cと膜形成室hとの間に配設
する搬送管dを、蒸発源bより生成された微粒子をキャ
リアガスと共に膜形成室h側に搬送する搬送管dの搬入
口i付近で大きく曲がった曲り部分jと、搬送管dで搬
送された微粒子をガスと共に噴射させるノズルeの基部
付近で大きく曲がった曲り部分kを有する例えば略コ字
形状の搬送管dとした形成装置が知られている。尚、図
中、mは微粒子生成室c内にキャリアガスを供給するガ
ス供給源nに連なるニードルバルブ、oは蒸発源bの加
熱装置、pは膜形成室hにバルブqを介して接続せる真
空ポンプを示す。
2. Description of the Related Art Conventionally, as a forming apparatus of this type, for example, as shown in FIG. 6, a fine particle generating chamber c provided with an evaporation source b for heating and evaporating a fine particle film material a, and a fine particle generating chamber c Conveying pipe d for conveying fine particles together with carrier gas
And a nozzle e connected to the tip of the carrier pipe d, and a fine particle film f formed by injecting fine particles and carrier gas from the nozzle e.
And a film forming chamber h in which a movable substrate g for forming a film is arranged. The particle forming chamber c and the film forming chamber h are arranged on the same plane. The transfer pipe d disposed between the transfer pipe d and the curved portion j which is largely bent near the carry-in port i of the transfer pipe d for transferring the fine particles generated from the evaporation source b to the film forming chamber h side together with the carrier gas. There is known a forming apparatus having, for example, a substantially U-shaped carrier pipe d having a bent portion k that is largely bent near the base portion of a nozzle e that injects the fine particles conveyed with the gas together with a gas. In the figure, m is a needle valve connected to a gas supply source n for supplying a carrier gas into the fine particle production chamber c, o is a heating device for the evaporation source b, and p is connected to the film forming chamber h via a valve q. A vacuum pump is shown.

【0003】そして、図6に示す装置により微粒子膜を
形成する場合には、先ず、微粒子生成室c内の蒸発源b
内に微粒子膜材料aとして例えばAuを充填する。続い
て、微粒子生成室b内にガス供給源nより例えばヘリウ
ムガスをキャリアガスとしてニードルバルブmで所定量
導入すると共に、加熱装置oで例えば430Wの電力を
投入して蒸発源bを加熱し、蒸発源b内の膜材料のAu
を加熱・溶融せしめ、蒸発させてAu微粒子を生成させ
る。次に膜形成室h内を真空ポンプpで排気し、微粒子
生成室cと膜形成室hとの差圧で微粒子生成室c内のA
u微粒子をキャリアガスと共に搬送管dで膜形成室hに
搬送し、ノズルeより一定速度で移動中(矢印x方向)
の基板g上にAu微粒子をキャリアガスと共に噴射して
該基板g上にAu微粒子膜fを形成する。
When forming a fine particle film by the apparatus shown in FIG. 6, first, the evaporation source b in the fine particle generating chamber c is formed.
For example, Au is filled as the fine particle film material a. Subsequently, a predetermined amount of helium gas as a carrier gas is introduced from the gas supply source n into the particle generation chamber b by the needle valve m, and the evaporation source b is heated by supplying electric power of 430 W by the heating device o, Au of the film material in the evaporation source b
Is heated and melted and evaporated to produce Au fine particles. Next, the inside of the film forming chamber h is evacuated by the vacuum pump p, and A in the particle forming chamber c is generated by the pressure difference between the particle forming chamber c and the film forming chamber h.
u The fine particles are carried together with the carrier gas by the carrying pipe d into the film forming chamber h, and are moving at a constant speed from the nozzle e (arrow x direction).
The Au fine particles are jetted together with the carrier gas onto the substrate g to form the Au fine particle film f on the substrate g.

【0004】[0004]

【発明が解決しようとする課題】従来のガス・デポジシ
ョン法による微粒子膜の形成装置では、微粒子生成室c
と膜形成室hを同一平面に配置されている関係上、微粒
子生成室c内の蒸発源と膜形成室h内の基板gとを結ぶ
搬送管dは、搬送管dの搬入口i付近に曲り部分jと、
ノズルeの基部付近に曲り部分kを有するため、この搬
送管dの曲り部分j,kの曲りによりキャリアガスのガ
ス流れに乱れが生じて搬送過程で微粒子同士の衝突が発
生し、単位体積当たりの搬送微粒子が多くなってくる
と、大きな凝集体が形成される。この凝集体は基板gと
の付着力等の膜質を低下させる原因となるため、微粒子
堆積膜が基板から剥離するという問題があった。
In the conventional apparatus for forming a fine particle film by the gas deposition method, the fine particle generating chamber c is used.
Since the film forming chamber h and the film forming chamber h are arranged on the same plane, the transfer pipe d connecting the evaporation source in the particle generation chamber c and the substrate g in the film forming chamber h is located near the carry-in port i of the transfer pipe d. Curved part j,
Since there is a bent portion k near the base of the nozzle e, the bending of the bent portions j and k of the carrier pipe d causes turbulence in the gas flow of the carrier gas, resulting in collision of fine particles with each other during the carrier process. Larger aggregates are formed when the number of the transported fine particles of (3) increases. Since this aggregate causes deterioration of film quality such as adhesion to the substrate g, there is a problem that the fine particle deposition film is separated from the substrate.

【0005】本発明は前記問題点を解消し、微粒子を搬
送する際、ガスの流れの乱れを防止して微粒子同士の衝
突による凝集を生じさせることなく搬送することが出来
るガス・デポジション法による微粒子膜の形成法と、そ
の膜形成に用いる形成装置を提供することを目的とす
る。
The present invention is based on the gas deposition method which solves the above-mentioned problems, and when the fine particles are conveyed, the flow of gas can be prevented from being disturbed and the fine particles can be conveyed without causing agglomeration due to collision between the fine particles. An object of the present invention is to provide a method for forming a fine particle film and a forming apparatus used for forming the film.

【0006】[0006]

【課題を解決するための手段】本発明は、前記目的を達
成するガス・デポジション法による微粒子膜の形成方法
を提案するもので、搬送管で微粒子をキャリアガスと共
に搬送し、これを搬送管の先端のノズルより噴射して基
板上に微粒子膜を形成するガス・デポジション法におい
て、微粒子とキャリアガスを蒸発源と基板との間を直線
状の搬送管で搬送することを特徴とする。
The present invention proposes a method for forming a fine particle film by a gas deposition method that achieves the above-mentioned object. A fine particle film is carried by a carrying tube together with a carrier gas, and this is carried by the carrying tube. In the gas deposition method of forming a fine particle film on a substrate by jetting from a nozzle at the tip of, the fine particles and carrier gas are conveyed by a linear conveying pipe between the evaporation source and the substrate.

【0007】また、更に本発明は、前記形成方法を実施
するためのガス・デポジション法による微粒子膜の形成
装置を提案するもので、微粒子膜材料の蒸発源と、基板
と、キャリアガスと共に微粒子膜材料の微粒子を搬送す
る搬送管と、該搬送管の先端に設けた微粒子とキャリア
ガスを基板上に噴射するノズルとから成るガス・デポジ
ション法による微粒子膜の形成装置において、前記搬送
管は蒸発源と基板間を曲げることなく直線状に形成した
搬送管であることを特徴とする。また、蒸発源と搬送管
の搬入口との相対的位置を調整する調整機構を設けても
よいし、また、搬送管の搬入口近傍に余剰微粒子を排出
する排出口を設けてもよい。
Further, the present invention proposes an apparatus for forming a fine particle film by a gas deposition method for carrying out the above-mentioned forming method, wherein the fine particle film material evaporation source, the substrate, and the fine particles together with the carrier gas. In the apparatus for forming a fine particle film by the gas deposition method, which comprises a transport pipe for transporting fine particles of a film material, and a nozzle provided at the tip of the transport pipe for injecting a fine particle and a carrier gas onto a substrate, the transport pipe is It is characterized in that it is a carrier pipe formed in a straight line without bending between the evaporation source and the substrate. Further, an adjusting mechanism for adjusting the relative position between the evaporation source and the carry-in port of the carrier pipe may be provided, or a discharge port for discharging the surplus particles may be provided near the carry-in port of the carrier pipe.

【0008】[0008]

【作用】キャリアガスと共に微粒子は搬送されてノズル
より基板上に噴射されて堆積し微粒子膜を形成する。そ
の際、微粒子はキャリアガスと共に直線状の搬送管で直
進状態に搬送されるので、搬送中にガスの流れの乱れが
生じることないから微粒子の凝集体が発生しない。
The fine particles are carried together with the carrier gas and jetted from the nozzle onto the substrate to be deposited to form a fine particle film. At that time, since the fine particles are conveyed in a straight traveling state together with the carrier gas through the linear conveying pipe, the gas flow is not disturbed during the conveyance, and therefore the fine particles do not aggregate.

【0009】[0009]

【実施例】本発明の実施例を添付図面に基づき説明す
る。図1は本発明を実施する形成装置の1例を示すもの
で、図中、1は微粒子生成室、2は膜形成室、3は微粒
子生成室1と膜形成室2の間に配設された搬送管を示
す。
Embodiments of the present invention will be described with reference to the accompanying drawings. FIG. 1 shows an example of a forming apparatus for carrying out the present invention. In the figure, 1 is a fine particle generating chamber, 2 is a film forming chamber, and 3 is a space between the fine particle generating chamber 1 and the film forming chamber 2. The carrier pipe is shown.

【0010】微粒子生成室1内に連通されたガス導入管
4から例えばヘリウムガスから成るキャリアガスをガス
供給源5よりニードルバルブ6を介して導入出来るよう
にした。また、該微粒子生成室1内に加熱蒸発させる微
粒子膜材料Mを収容する開口部径15mmのアルミナコー
トのタングステン製バスケットとから成る蒸発源7を配
設し、該蒸発源7を蒸発源加熱装置8に接続した。ま
た、該微粒子生成室1内に微粒子をキャリアガスと共に
搬送する内径0.5mmの搬送管3の一端を気密に挿入し
て接続し、該搬送管3の先端側にステンレス製の内径
0.5mmのノズル9を接続した。
A carrier gas made of, for example, helium gas can be introduced from a gas supply source 5 through a needle valve 6 from a gas introduction pipe 4 communicating with the fine particle production chamber 1. Further, an evaporation source 7 consisting of an alumina-coated tungsten basket having an opening diameter of 15 mm for accommodating the fine particle film material M to be heated and evaporated is provided in the fine particle generation chamber 1, and the evaporation source 7 is used as an evaporation source heating device. Connected to 8. Further, one end of a transfer pipe 3 having an inner diameter of 0.5 mm for transferring the fine particles together with a carrier gas is airtightly inserted and connected to the inside of the fine particle generation chamber 1, and a stainless steel inner diameter of 0.5 mm is attached to the tip side of the transfer pipe 3. Nozzle 9 of was connected.

【0011】膜形成室2内は真空ポンプ10にバルブ1
1および排気管12を介して接続し、該真空ポンプ10
によって膜形成室2内の真空度を調整自在とした。ま
た、膜形成室2内に基板13を水平方向(矢印X方向)
に移動させる基板保持装置14を配置した。また、微粒
子生成室1に接続されている搬送管3の先端部分を膜形
成室2内に気密に挿入した。
In the film forming chamber 2, a vacuum pump 10 and a valve 1 are provided.
1 and the exhaust pipe 12, and the vacuum pump 10
The degree of vacuum in the film forming chamber 2 can be adjusted freely. In addition, the substrate 13 is horizontally placed in the film forming chamber 2 (direction of arrow X).
The substrate holding device 14 to be moved to was placed. Further, the tip portion of the transfer tube 3 connected to the particle generation chamber 1 was airtightly inserted into the film forming chamber 2.

【0012】前記構成は従来のガス・デポジション法に
よる微粒子膜の形成装置と特に変わりはないが、本発明
装置は、微粒子生成室1と膜形成室2を縦列に配設する
と共に、微粒子生成室1内の蒸発源7と膜形成室2内の
基板13の間に配設せる搬送管3を途中で曲りのない直
線状とし、搬送管3の一端15を微粒子生成室1内の蒸
発源7の上方に例えば50mm間隔を存して配置して、蒸
発源7で蒸発し、生成せしめた微粒子とキャリアガスを
膜形成室2側に搬送する搬入口15とした。また、搬送
管3の先端部分のノズル9の先端を膜形成室2内の基板
13と所定間隔例えば0.5mmを存して配置して、微粒
子をキャリアガスと共に微粒子生成室1内の蒸発源7よ
り膜形成室2内の基板13に直接に直進状で搬送出来る
ようにした。
The above-mentioned structure is not particularly different from the conventional apparatus for forming a fine particle film by the gas deposition method, but in the apparatus of the present invention, the fine particle generating chambers 1 and the film forming chambers 2 are arranged in tandem and the fine particle generating chambers are formed. The transport pipe 3 disposed between the evaporation source 7 in the chamber 1 and the substrate 13 in the film forming chamber 2 is formed into a straight line without any bend in the middle, and one end 15 of the transport pipe 3 is an evaporation source in the particle generation chamber 1. For example, they are arranged at an interval of 50 mm above 7 to serve as a carry-in port 15 for carrying the fine particles and the carrier gas, which are evaporated by the evaporation source 7 and are generated, to the film forming chamber 2 side. Further, the tip of the nozzle 9 at the tip of the transfer tube 3 is arranged at a predetermined distance from the substrate 13 in the film forming chamber 2, for example, 0.5 mm, and the fine particles together with the carrier gas are evaporated in the fine particle generating chamber 1. 7 allows the film to be directly conveyed to the substrate 13 in the film forming chamber 2 in a straight line.

【0013】また、図示例では微粒子生成室1内に挿入
されている搬送管3のの外方に内径25mmの排出管16
の一端を搬送管3と同心円状態に微粒子生成室1内に気
密に配置して、これを微粒子の排出口17とすると共
に、該排出管16の他端を微粒子生成室1の外方に配置
せる油回転ポンプ等の排気系18にバルブ19を介して
接続した。
Further, in the illustrated example, a discharge pipe 16 having an inner diameter of 25 mm is provided outside the carrier pipe 3 inserted in the particle generation chamber 1.
One end of which is concentrically arranged with the transfer pipe 3 in the fine particle generation chamber 1 in an airtight manner, and which serves as a discharge port 17 for the fine particles, and the other end of the discharge pipe 16 is disposed outside the fine particle generation chamber 1. It was connected to an exhaust system 18 such as an oil rotary pump via a valve 19.

【0014】次に前記図1に示す形成装置を用いて、微
粒子膜の具体的形成例を説明する。
Next, a specific example of forming a fine particle film will be described using the forming apparatus shown in FIG.

【0015】実施例 先ず、微粒子生成室1内の蒸発源7内に微粒子膜材料M
としてAuを20g充填した後、ニードルバルブ6で流
量を調節しながらガス供給源5よりヘリウムガスを微粒
子生成室1内に圧力2atmで導入し、該圧力を維持するよ
うにした。また、膜形成室2内の基板保持装置14に長
さ70mm、幅30mmの長方形で厚さ1mmから成るアルミ
ナ製の基板13を保持し、基板13表面と、ノズル9の
先端とを0.5mmの間隔に保持した後、基板13を基板
加熱装置(図示せず)で温度200℃に加熱した。
Embodiment First, the fine particle film material M is placed in the evaporation source 7 in the fine particle generating chamber 1.
After charging 20 g of Au as described above, helium gas was introduced from the gas supply source 5 into the fine particle production chamber 1 at a pressure of 2 atm while the flow rate was adjusted by the needle valve 6 so that the pressure was maintained. In addition, a substrate 13 made of alumina having a length of 70 mm and a width of 30 mm and a thickness of 1 mm is held in the substrate holding device 14 in the film forming chamber 2, and the surface of the substrate 13 and the tip of the nozzle 9 are 0.5 mm. After being held at the interval of, the substrate 13 was heated to a temperature of 200 ° C. by a substrate heating device (not shown).

【0016】次に、バスケット状の蒸発源7に蒸発源用
加熱装置8で400Wの電力を投入して蒸発源7を加熱
して、微粒子膜材料Mを溶融させて蒸発させ、Au微粒
子(平均粒径0.1μm)を生成させた。
Next, 400 W of electric power is applied to the basket-shaped evaporation source 7 by the evaporation source heating device 8 to heat the evaporation source 7 to melt and evaporate the fine particle film material M, and Au fine particles (average Particle size 0.1 μm) was produced.

【0017】そして、真空ポンプ10を作動させて膜形
成室2の排気を行って、膜形成室2内の圧力を0.3To
rrに維持すると、微粒子生成室1と膜形成室2との差圧
で微粒子生成室1内に生成したAu微粒子は微粒子生成
室1内に導入したヘリウムガスをキャリアガスとして、
搬送管3の搬入口15より搬送管3内に圧送され、直線
状の搬送管3内を9リットル/minの流量で直進状態で
通過して膜形成室2内に搬送され、搬送管3の先端のノ
ズル9より予め前記温度(200℃)に加熱され、基板
保持装置14で移動方向(矢印X方向)に速度7.5mm
/minで移動している基板13上にAu微粒子とキャリ
アガスを噴射して膜堆積高さ速度100μm/secで膜
厚400μmのAu微粒子膜Fを形成した。
Then, the vacuum pump 10 is operated to evacuate the film forming chamber 2 so that the pressure in the film forming chamber 2 is 0.3 To.
When maintained at rr, the Au fine particles generated in the fine particle generation chamber 1 due to the differential pressure between the fine particle generation chamber 1 and the film formation chamber 2 use the helium gas introduced into the fine particle generation chamber 1 as the carrier gas.
It is pressure-fed into the transfer tube 3 through the carry-in port 15 of the transfer tube 3, passes through the linear transfer tube 3 at a flow rate of 9 liters / min in a straight line, and is transferred into the film forming chamber 2. The nozzle 9 at the tip is preheated to the above temperature (200 ° C.), and the substrate holding device 14 moves at a speed of 7.5 mm in the moving direction (arrow X direction).
Au particles and a carrier gas were jetted onto the substrate 13 moving at a speed of / min to form an Au particle film F having a film thickness of 400 μm at a film deposition height rate of 100 μm / sec.

【0018】基板13上にAu微粒子膜Fを形成後は直
ちに蒸発源7による微粒子膜材料Mの加熱と、キャリア
ガスによる微粒子の搬送とを停止すると共に、排気系1
8のバルブ19を開放して排出口17より搬送管3の搬
入口15付近に残存せるAu微粒子を微粒子生成室1の
外方に排出した。
Immediately after the Au fine particle film F is formed on the substrate 13, the heating of the fine particle film material M by the evaporation source 7 and the transport of the fine particles by the carrier gas are stopped, and the exhaust system 1
The valve 19 of No. 8 was opened, and the Au fine particles remaining in the vicinity of the carry-in port 15 of the carrier pipe 3 were discharged from the discharge port 17 to the outside of the fine particle generation chamber 1.

【0019】そして、基板13上に形成されたAu微粒
子膜Fを走査電子顕微鏡(倍率5,000倍)で観察し
たところ図2に示すような凝集体のない粒子径が0.1
μm以下のAu微粒子膜が形成されたいることが分かっ
た。また、Au微粒子膜のNi膜に対する密着力を調べ
たところ20kgf/mm2であった。
When the Au fine particle film F formed on the substrate 13 was observed with a scanning electron microscope (magnification: 5,000 times), the particle size without agglomerates as shown in FIG. 2 was 0.1.
It was found that an Au fine particle film having a thickness of μm or less was formed. The adhesion of the Au fine particle film to the Ni film was examined and found to be 20 kgf / mm 2 .

【0020】比較例 比較のために、膜形成装置の搬送管を図4に示すよう
な、その一部にらせん状(R:60mm)に1回曲げた曲
り部21を有する搬送管22とした以外は図1に示す形
成装置を用い、前記実施例と同じ条件で基板13上にA
u微粒子膜F′(図4参照)を形成した。
Comparative Example For comparison, the transfer pipe of the film forming apparatus was a transfer pipe 22 having a bent portion 21 bent once in a spiral shape (R: 60 mm), as shown in FIG. Other than the above, the forming apparatus shown in FIG.
A u fine particle film F ′ (see FIG. 4) was formed.

【0021】尚、図4に示す形成装置で前記記号(2
1,22)以外の他の符号については前記図1に示す形
成装置と同一構成のため説明を省略する。
In the forming apparatus shown in FIG. 4, the symbol (2
The other reference numerals other than 1 and 22) are the same as those of the forming apparatus shown in FIG.

【0022】そして、基板13上に形成されたAu微粒
子膜F′を走査電子顕微鏡(倍率10,000倍)で観
察したところ図5に示すような大きさが約2μmの凝集
体が認められた。また、Au微粒子膜のNi膜に対する
密着力を調べたところ8kgf/mm2であった。
When the Au fine particle film F'formed on the substrate 13 was observed with a scanning electron microscope (magnification: 10,000 times), aggregates having a size of about 2 μm were recognized as shown in FIG. . Further, when the adhesion of the Au fine particle film to the Ni film was examined, it was 8 kgf / mm 2 .

【0023】図2および図5から明らかなように、微粒
子とキャリアガスを直進状態に搬送するようにした本発
明実施例では形成されたAu微粒子膜には微粒子の凝集
がなかったのに対し、微粒子とキャリアガスを搬送途中
で曲げて搬送した比較例では形成されたAu微粒子膜に
は微粒子の凝集体が存在していた。従って、微粒子とキ
ャリアガスを直進状態で搬送することにより基板上に形
成される微粒子膜中に凝集体の生成を防止出来ることが
確認された。また、本発明実施例は比較例に比してNi
膜に対する密着力を向上した微粒子膜が形成されてお
り、微粒子とキャリアガスの搬送を直進状態とすること
により微粒子膜のNi膜への密着力が大幅に改良された
効果が表れている。
As is clear from FIGS. 2 and 5, in the embodiment of the present invention in which the fine particles and the carrier gas were conveyed straight, the Au fine particle film formed had no fine particle aggregation. In the comparative example in which the fine particles and the carrier gas were bent and conveyed during the conveyance, the formed Au fine particle film had aggregates of the fine particles. Therefore, it was confirmed that the formation of aggregates in the fine particle film formed on the substrate can be prevented by conveying the fine particles and the carrier gas in a straight line. In addition, the example of the present invention is
A fine particle film having improved adhesion to the film is formed, and the effect of greatly improving the adhesion of the fine particle film to the Ni film is exhibited by making the conveyance of the fine particles and the carrier gas straight.

【0024】図1に示す形成装置では搬送管3の搬入口
15近傍に微粒子の排出口16を設けたが、該排出口を
設ける代わりに、搬送管3の搬入口15の位置と蒸発源
7の位置とを相対的に位置調整する例えばベローズ、球
面シールポートのような位置調整装置(図示せず)を搬
送管3の搬入口15、或いは蒸発源7のいずれかに設置
して、微粒子膜の形成後は直ちに蒸発源7による微粒子
膜材料Mの加熱と、キャリアガスによる微粒子の搬送と
を停止すると共に、位置調整装置を作動させて搬送管3
の搬入口15位置を蒸発源7の蒸発口に対向する位置よ
り移動させて蒸発源7と搬送管3の搬入口15の相対的
位置を変更させて、蒸発源7の余熱により蒸発、生成し
て搬入口15近傍に残存せる微粒子の搬送管3内に搬送
されることを防止するようにしてもよい。
In the forming apparatus shown in FIG. 1, a particulate discharge port 16 is provided in the vicinity of the carry-in port 15 of the carrier pipe 3, but instead of providing the discharge port, the position of the carry-in port 15 of the carrier pipe 3 and the evaporation source 7 are provided. A position adjusting device (not shown) such as a bellows or a spherical seal port for adjusting the relative position of the particle film is installed at either the carry-in port 15 of the carrier pipe 3 or the evaporation source 7. Immediately after the formation, the heating of the fine particle film material M by the evaporation source 7 and the conveyance of the fine particles by the carrier gas are stopped, and the position adjusting device is operated to move the conveyance pipe 3
Of the evaporation source 7 is moved from the position facing the evaporation port of the evaporation source 7 to change the relative position of the evaporation source 7 and the transfer port 15 of the carrier pipe 3, and the residual heat of the evaporation source 7 evaporates and generates. Therefore, it may be possible to prevent the fine particles remaining in the vicinity of the carry-in port 15 from being carried into the carrying pipe 3.

【0025】図3は本発明の形成装置の他の実施例であ
って、前記図1に示す形成装置では微粒子生成室1と膜
形成室2を縦列に配置したが、微粒子生成室1と膜形成
室2を横列に配置した装置である。図3に示す装置につ
いて前記図1に示す装置との相違点を説明する。
FIG. 3 shows another embodiment of the forming apparatus of the present invention. In the forming apparatus shown in FIG. 1, the fine particle producing chambers 1 and the film forming chambers 2 are arranged in tandem. This is an apparatus in which the forming chambers 2 are arranged in rows. Differences between the apparatus shown in FIG. 3 and the apparatus shown in FIG. 1 will be described.

【0026】微粒子生成室1内に気密に挿入した搬送管
3の搬入口15を蒸発源7の上方に蒸発源7に対して横
向きに配設すると共に、横向きの搬送管3をそのまま直
線状に延設して搬送管3の先端部分を膜形成室2内に気
密に挿入すると共に、ノズル9の先端を微粒子生成室1
内で水平面に対して立設状態の基板13と所定間隔例え
ば0.5mmを存して配置した。また、排出管16の排出
口17を蒸発源7の上方に搬送管3の搬入口15に近接
して配置した。その他の符号については前記図1に示す
形成装置と同一構成のため説明を省略する。
The carry-in port 15 of the carrier pipe 3 which is airtightly inserted in the fine particle production chamber 1 is arranged above the evaporation source 7 in a lateral direction with respect to the evaporation source 7, and the laterally-carried carrier pipe 3 is linear as it is. The tip end of the transfer tube 3 is extended and inserted into the film forming chamber 2 in an airtight manner, and the tip of the nozzle 9 is attached to the particle forming chamber 1.
It was arranged with a predetermined distance, for example 0.5 mm, from the substrate 13 standing upright on the horizontal plane. Further, the discharge port 17 of the discharge pipe 16 is arranged above the evaporation source 7 and close to the carry-in port 15 of the carrier pipe 3. Since the other reference numerals are the same as those of the forming apparatus shown in FIG. 1, the description thereof will be omitted.

【0027】図3装置を図1装置と対照すれば、微粒子
生成室1はそのままであり、膜形成室2と搬送管3は微
粒子生成室に対し、あたかも横倒し状態である。また、
図3に示す形成装置の作動および効果は図1に示す形成
装置と同一である。
When the apparatus of FIG. 3 is contrasted with the apparatus of FIG. 1, the fine particle production chamber 1 remains as it is, and the film forming chamber 2 and the transfer tube 3 are in a state of lying sideways with respect to the fine particle production chamber. Also,
The operation and effects of the forming apparatus shown in FIG. 3 are the same as those of the forming apparatus shown in FIG.

【0028】前記図1示の形成装置では微粒子生成室1
と膜形成室2を縦列に配置したが、本発明はこれに限定
されるものではなく、微粒子生成室1内の蒸発源7と膜
形成室2内の基板13とを結ぶ搬送管3を直線状に配設
出来ればよく、微粒子生成室1と膜形成室2の配置を縦
列配置のまま横倒し状態の横並びに配置してもよい。ま
た、前記図3示の形成装置では微粒子生成室1と膜形成
室2を横列に配置したが本発明はこれに限定されるもの
ではなく、微粒子生成室1内の蒸発源7と膜形成室2内
の基板13とを結ぶ搬送管3を直線状に配設出来ればよ
く、微粒子生成室1と膜形成室2の配列を横列配置のま
ま立設状態の縦並びに配置してもよい。
In the forming apparatus shown in FIG. 1, the particle generation chamber 1
The film forming chambers 2 and the film forming chambers 2 are arranged in tandem, but the present invention is not limited to this, and the transfer pipe 3 connecting the evaporation source 7 in the particle generation chamber 1 and the substrate 13 in the film forming chamber 2 is linear. It suffices that the fine particle generation chambers 1 and the film formation chambers 2 be arranged side by side in the laid-down state as they are arranged in a column. Further, in the forming apparatus shown in FIG. 3, the particle generation chamber 1 and the film formation chamber 2 are arranged in a row, but the present invention is not limited to this, and the evaporation source 7 and the film formation chamber in the particle generation chamber 1 are not limited to this. It suffices that the transfer tube 3 connecting the substrate 13 in 2 can be linearly arranged, and the fine particle generation chambers 1 and the film formation chambers 2 may be vertically arranged in a horizontal arrangement.

【0029】[0029]

【発明の効果】本発明のガス・デポジション法による微
粒子膜の形成法によるときは、微粒子とキャリアガスの
搬送を蒸発源と基板との間を途中で曲りのない直線状の
搬送管で直進状態で行うようにしたので、搬送中にガス
の流れに乱れが生じないから、搬送過程で微粒子同士の
衝突による凝集が発生せず、基板との密着力が良好で、
凝集体のない密度の向上した微粒子膜を基板上に極めて
簡単に形成することが出来る等の効果がある。
According to the method of forming a fine particle film by the gas deposition method of the present invention, the fine particles and the carrier gas are conveyed straight between the evaporation source and the substrate by a straight conveying pipe which does not bend. Since it is performed in a state, since the gas flow is not disturbed during transportation, agglomeration due to collision of fine particles does not occur in the transportation process, and the adhesion with the substrate is good,
There is an effect that it is possible to form a fine particle film having a high density without agglomerates on a substrate very easily.

【0030】また、本発明のガス・デポジション法によ
る微粒子膜の形成装置によるときは、微粒子とキャリア
ガスとを搬送する搬送管を蒸発源と基板間を曲げること
なく直線状に形成した搬送管としたので、微粒子とキャ
リアガスを直進状態に搬送することが出来て、基板との
密着力が良好で、凝集体のない密度の向上した微粒子膜
を基板上に極めて簡単に形成することが出来る形成装置
を提供出来る効果がある。
When the apparatus for forming a fine particle film by the gas deposition method of the present invention is used, the transfer tube for transferring the fine particles and the carrier gas is formed in a straight line without bending between the evaporation source and the substrate. Therefore, it is possible to convey the fine particles and the carrier gas in a straight line state, the adhesion force with the substrate is good, and it is possible to extremely easily form the fine particle film on the substrate, which has an increased density without aggregation. There is an effect that a forming device can be provided.

【0031】また、蒸発源と搬送管の搬入口との相対的
位置を調整する調整機構を設けると、蒸発生成された粒
子濃度の多い位置に合わせられ、充分な堆積速度が確保
出来る。
Further, by providing an adjusting mechanism for adjusting the relative position between the evaporation source and the carry-in port of the carrier pipe, it can be adjusted to a position where the concentration of particles produced by evaporation is large, and a sufficient deposition rate can be secured.

【0032】また、搬送管の搬入口近傍に微粒子を排出
する排出口を設けると、膜形成に使用されない余分粒子
を除外し、微粒子生成室内での対流による凝集体の生成
を除外することが出来る。
If a discharge port for discharging fine particles is provided in the vicinity of the carry-in port of the transfer pipe, excess particles not used for film formation can be excluded, and generation of aggregates due to convection in the fine particle generation chamber can be excluded. .

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

【図1】 本発明装置の1実施例の説明線図、FIG. 1 is an explanatory diagram of one embodiment of the device of the present invention,

【図2】 本発明方法の1実施例で基板上に形成した微
粒子膜の表面状態を表している図面代用写真、
FIG. 2 is a drawing-substituting photograph showing the surface condition of a fine particle film formed on a substrate in one embodiment of the method of the present invention,

【図3】 本発明装置の他の実施例の説明線図、FIG. 3 is an explanatory diagram of another embodiment of the device of the present invention,

【図4】 本発明方法と比較するために用いた形成装置
の説明線図、
FIG. 4 is an explanatory diagram of a forming apparatus used for comparison with the method of the present invention;

【図5】 図4に示した形成装置で基板上に形成した微
粒子膜の表面状態を表している図面代用写真、
5 is a photograph as a substitute for a drawing showing a surface state of a fine particle film formed on a substrate by the forming apparatus shown in FIG.

【図6】 従来の形成装置の説明線図。FIG. 6 is an explanatory diagram of a conventional forming apparatus.

【符号の説明】[Explanation of symbols]

1 微粒子生成室、 2 膜形成室、 3 搬
送管、7 蒸発源、 9 ノズル、 1
3 基板、15 搬入口、 17 排出口、F
微粒子膜、 M 微粒子膜材料。
1 fine particle generating chamber, 2 film forming chamber, 3 carrier pipe, 7 evaporation source, 9 nozzle, 1
3 substrates, 15 carry-in port, 17 discharge port, F
Fine particle film, M Fine particle film material.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 搬送管で微粒子をキャリアガスと共に搬
送し、これを搬送管の先端のノズルより噴射して基板上
に微粒子膜を形成するガス・デポジション法において、
微粒子とキャリアガスを蒸発源と基板との間を直線状の
搬送管で搬送することを特徴とするガス・デポジション
法による微粒子膜の形成法。
1. A gas deposition method in which fine particles are transported together with a carrier gas in a transport tube and the fine particles are formed on a substrate by jetting the fine particles from a nozzle at the tip of the transport tube.
A method of forming a fine particle film by a gas deposition method, characterized in that fine particles and carrier gas are conveyed between a vaporization source and a substrate by a linear conveying pipe.
【請求項2】 微粒子膜材料の蒸発源と、基板と、キャ
リアガスと共に微粒子膜材料の微粒子を搬送する搬送管
と、該搬送管の先端に設けた微粒子とキャリアガスを基
板上に噴射するノズルとから成るガス・デポジション法
による微粒子膜の形成装置において、前記搬送管は蒸発
源と基板間を曲げることなく直線状に形成した搬送管で
あることを特徴とするガス・デポジション法による微粒
子膜の形成装置。
2. An evaporation source of the fine particle film material, a substrate, a carrier pipe for carrying the fine particles of the fine particle film material together with a carrier gas, and a nozzle provided at the tip of the carrier pipe for injecting the fine particles and the carrier gas onto the substrate. In the apparatus for forming a fine particle film by the gas deposition method, the transfer tube is a transfer tube formed in a straight line without bending between the evaporation source and the substrate. Membrane forming device.
【請求項3】 蒸発源と搬送管の微粒子とキャリアガス
の搬入口との相対的位置を調整する調整機構を設けたこ
とを特徴とする請求項第2項に記載のガス・デポジショ
ン法による微粒子膜の形成装置。
3. The gas deposition method according to claim 2, further comprising an adjusting mechanism for adjusting the relative positions of the evaporation source, the fine particles in the carrier pipe and the carrier gas inlet. Device for forming fine particle film.
【請求項4】 搬送管の微粒子とキャリアガスの搬入口
近傍に微粒子を排出する排出口を設けたことを特徴とす
る請求項第2項に記載のガス・デポジション法による微
粒子膜の形成装置。
4. An apparatus for forming a fine particle film by the gas deposition method according to claim 2, wherein an outlet for discharging the fine particles is provided in the vicinity of the inlet for the fine particles and the carrier gas of the carrier pipe. .
JP22304692A 1992-08-21 1992-08-21 Method of forming fine particle film by gas deposition method and its forming apparatus Expired - Lifetime JP3154213B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22304692A JP3154213B2 (en) 1992-08-21 1992-08-21 Method of forming fine particle film by gas deposition method and its forming apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22304692A JP3154213B2 (en) 1992-08-21 1992-08-21 Method of forming fine particle film by gas deposition method and its forming apparatus

Publications (2)

Publication Number Publication Date
JPH0665757A true JPH0665757A (en) 1994-03-08
JP3154213B2 JP3154213B2 (en) 2001-04-09

Family

ID=16791996

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22304692A Expired - Lifetime JP3154213B2 (en) 1992-08-21 1992-08-21 Method of forming fine particle film by gas deposition method and its forming apparatus

Country Status (1)

Country Link
JP (1) JP3154213B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002309383A (en) * 2001-04-12 2002-10-23 National Institute Of Advanced Industrial & Technology Brittle material composite structure and production method therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002309383A (en) * 2001-04-12 2002-10-23 National Institute Of Advanced Industrial & Technology Brittle material composite structure and production method therefor

Also Published As

Publication number Publication date
JP3154213B2 (en) 2001-04-09

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