JPH0691112B2 - Deposited film formation method - Google Patents

Deposited film formation method

Info

Publication number
JPH0691112B2
JPH0691112B2 JP60029813A JP2981385A JPH0691112B2 JP H0691112 B2 JPH0691112 B2 JP H0691112B2 JP 60029813 A JP60029813 A JP 60029813A JP 2981385 A JP2981385 A JP 2981385A JP H0691112 B2 JPH0691112 B2 JP H0691112B2
Authority
JP
Japan
Prior art keywords
film
compound
space
group
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.)
Expired - Lifetime
Application number
JP60029813A
Other languages
Japanese (ja)
Other versions
JPS61189650A (en
Inventor
俊一 石原
茂 大野
正博 金井
俊理 小田
勇 清水
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.)
Canon Inc
Original Assignee
Canon Inc
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 Canon Inc filed Critical Canon Inc
Priority to JP60029813A priority Critical patent/JPH0691112B2/en
Publication of JPS61189650A publication Critical patent/JPS61189650A/en
Priority to US07/113,414 priority patent/US4772486A/en
Publication of JPH0691112B2 publication Critical patent/JPH0691112B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • C23C16/22Chemical 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 deposition of inorganic material, other than metallic material
    • C23C16/30Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
    • C23C16/301AIII BV compounds, where A is Al, Ga, In or Tl and B is N, P, As, Sb or Bi
    • 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
    • C23C16/22Chemical 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 deposition of inorganic material, other than metallic material
    • C23C16/30Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
    • C23C16/305Sulfides, selenides, or tellurides
    • C23C16/306AII BVI compounds, where A is Zn, Cd or Hg and B is S, Se or Te
    • 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
    • C23C16/448Chemical 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 generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials
    • C23C16/452Chemical 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 generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials by activating reactive gas streams before their introduction into the reaction chamber, e.g. by ionisation or addition of reactive species

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  • 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)
  • Inorganic Chemistry (AREA)
  • Chemical Vapour Deposition (AREA)
  • Photovoltaic Devices (AREA)
  • Photoreceptors In Electrophotography (AREA)

Description

【発明の詳細な説明】 〔従来の技術〕 本発明は、半導体膜、絶縁体膜、導体膜等の非晶性の或
いは結晶性の機能性薄膜、殊に能動性或いは受動性の半
導体デバイス、光半導体デバイス或いは太陽電池や電子
写真用の感光デバイスなどの用途に有用な堆積膜の形成
法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an amorphous or crystalline functional thin film such as a semiconductor film, an insulator film, or a conductor film, particularly an active or passive semiconductor device, or an optical device. The present invention relates to a method for forming a deposited film that is useful for applications such as semiconductor devices, solar cells, and photosensitive devices for electrophotography.

堆積膜の形成には、真空蒸着法,プラズマCVD法,熱CVD
法,光CVD法,反応性スパツタリング法,イオンプレー
テイング法などが試みられており、一般的には、プラズ
マCVD法が広く用いられ、企業化されている。
Vacuum deposition method, plasma CVD method, thermal CVD method
Method, photo CVD method, reactive sputtering method, ion plating method and the like have been tried, and in general, plasma CVD method is widely used and commercialized.

而乍ら、これ等堆積膜形成法によって得られる堆積膜は
より高度の機能が求められる電子デバイスや光電子デバ
イスへの適用が求められていることから電気的,光学的
特性及び、繰返し使用での疲労特性あるいは使用環境特
性、更には均一性,再現性を含めて生産性,量産性の点
において更に総合的な特性の向上を図る余地がある。
However, since the deposited films obtained by these deposited film forming methods are required to be applied to electronic devices and optoelectronic devices that require higher functions, electrical and optical characteristics and repeated use There is room to improve the overall characteristics in terms of fatigue characteristics, usage environment characteristics, and productivity and mass productivity including uniformity and reproducibility.

従来から一般化されているプラズマCVD法による堆積膜
の形成においての反応プロセスは、従来の所謂、熱CVD
法に比較してかなり複雑であり、その反応機構も不明な
点が少なくなかった。又、その堆積膜の形成パラメータ
ーも多く(例えば、基体温度,導入ガスの流量と比,形
成時の圧力、高周波電力,電極構造,反応容器の構造,
排気速度,プラズマ発生方式など)、これらの多くのパ
ラメータの組み合せによるため、時にはプラズマが不安
定な状態になり、形成された堆積膜に著しい悪影響を与
えることが少なくなかった。そのうえ、装置特有のパラ
メーターを装置ごとに選定しなければならず、したがっ
て製造条件を一般化することがむずかしいというのが実
状であった。
The reaction process in forming a deposited film by the plasma CVD method that has been generalized in the past is the conventional so-called thermal CVD.
It was much more complicated than the method, and its reaction mechanism was not clear. In addition, there are many formation parameters of the deposited film (for example, substrate temperature, introduced gas flow rate and ratio, formation pressure, high frequency power, electrode structure, reaction vessel structure,
(Exhaust speed, plasma generation method, etc.) and the combination of many of these parameters often cause the plasma to be in an unstable state and have a significant adverse effect on the formed deposited film. In addition, it was difficult to generalize the manufacturing conditions because the parameters peculiar to the device had to be selected for each device.

堆積膜の応用用途によっては、大面積化,膜厚の均一
性,膜品質の均一性を十分に満足させて、再現性のある
量産化を図らねばならないため、プラズマCVD法による
堆積膜の形成においては、量産装置に多大な設備投資が
必要となり、またその量産の為の管理項目も複雑にな
り、管理許容幅も狭くなり、装置の調整も微妙であるこ
とから、これらのことが、今後改善すべき問題点として
指摘されている。
Depending on the application of the deposited film, it may be necessary to achieve a large area, film thickness uniformity, and film quality uniformity for mass production with reproducibility. In this case, since a large amount of capital investment is required for mass production equipment, the management items for its mass production are complicated, the management allowable width is narrowed, and the adjustment of equipment is delicate, It is pointed out as a problem to be improved.

他方、通常のCVD法による従来の技術では、高温を必要
とすると共に、企業的なレベルでは必ずしも満足する様
な特性を有する堆積膜が得られていなかった。
On the other hand, in the conventional technique by the ordinary CVD method, a high temperature is required, and a deposited film having satisfactory characteristics at a company level has not been obtained.

これ等のことは、殊にII-VI族化合物の薄膜を形成する
場合においては、より大きな問題として残されている。
These problems remain as a larger problem especially when forming a thin film of a II-VI group compound.

上述の如く、機能性膜の形成において、その実用可能な
特性の確保と、均一性を維持させながら低コストな装置
で量産化できる堆積膜の形成方法を開発することが切望
されている。
As described above, in forming a functional film, it is earnestly desired to develop a method for forming a deposited film, which can ensure practical properties and can be mass-produced by a low-cost apparatus while maintaining uniformity.

〔目的〕〔Purpose〕

本発明は、上述した従来の堆積膜形成法の欠点を除去す
ると同時に、従来の形成方法によらない新規な堆積膜形
成法を提供するものである。
The present invention eliminates the above-mentioned drawbacks of the conventional deposited film forming method, and at the same time provides a novel deposited film forming method which does not depend on the conventional forming method.

本発明の目的は、機能性膜の特性を容易に管理化出来、
少なくとも従来法で得た良質の膜の特性を保持すると共
に、堆積速度の向上を図りながら、膜形成条件の管理の
簡素化,膜の量産化を容易に達成させることの出来る堆
積膜の形成法を提供することである。
The object of the present invention is to easily manage the characteristics of the functional film,
A method for forming a deposited film, which maintains at least the characteristics of a high-quality film obtained by the conventional method and simplifies the control of film forming conditions and facilitates mass production of the film while improving the deposition rate. Is to provide.

〔構成〕〔Constitution〕

本発明の別の目的は、炭素などの不要な不純物の含有が
ほとんど見られない良質のII-VI族化合物堆積膜を容易
に形成することの出来る堆積膜形成法を提供することで
ある。
Another object of the present invention is to provide a deposited film forming method capable of easily forming a good quality II-VI group compound deposited film in which unnecessary impurities such as carbon are hardly found.

本発明の目的は、成膜空間に配された基体上に堆積膜を
形成する堆積膜形成法において、mをRの価数に等しい
か又はその整数倍の正整数、nのMの価数に等しいか又
はその整数倍の正整数、Mを周期律表の第IIB族に属す
る元素、Rを炭化水素基としたときに、一般式RnMmで表
わされる活性化されていない化合物(A)と、aをBの
価数に等しいか又はその整数倍の正整数、bをAの価数
に等しいか又はその整数倍の正整数、Aを周期律表の第
VI族に属するO,S,Se,Teから選択される元素、Bを水
素、ハロゲン、炭化水素基としたときに、一般式AaBbで
表わされる活性化されていない化合物(B)と、前記成
膜空間とは異なる活性化空間において生成した活性種と
しての活性化ハロゲンと、を前記成膜空間に導入し、化
学反応させることにより前記基体上にII-VI族化合物の
堆積膜を形成することを特徴とする堆積膜形成法により
達成される。
An object of the present invention is, in a deposited film forming method for forming a deposited film on a substrate arranged in a film forming space, m is a positive integer which is equal to or a multiple of the valence of R, and the valence of M of n. A non-activated compound (A) represented by the general formula RnMm, where M is an element belonging to Group IIB of the periodic table and R is a hydrocarbon group. , A is a positive integer that is equal to or an integer multiple of B, b is a positive integer that is equal to or an integer multiple of A, and A is a positive integer in the periodic table.
When B, which is an element selected from O, S, Se and Te belonging to Group VI, is hydrogen, halogen or a hydrocarbon group, the compound (B) represented by the general formula AaBb and the above compound Forming a deposited film of a II-VI group compound on the substrate by introducing into the film formation space an activated halogen as an active species generated in an activation space different from the film space and causing a chemical reaction. Is achieved by the method for forming a deposited film.

[作用] 本発明の方法では、所望の機能性の堆積膜を形成するに
際して、堆積膜の形成パラメーターが、導入する前記一
般式(A)及び(B)で示される化合物(A)と化合物
(B)及びこれらのうち少なくともいずれか一方と化学
反応する活性種の導入量、基体及び成膜空間内の温度、
成膜空間内の内圧となり、従って、堆積膜形成のコント
ロールが容易になり、再現性、量産性のある機能性の堆
積膜を形成させることができる。
[Operation] In the method of the present invention, the compound (A) represented by the general formulas (A) and (B) and the compound ( B) and the introduced amount of active species that chemically reacts with at least one of these, the temperature in the substrate and the film formation space,
It becomes the internal pressure in the film forming space, so that the control of the formation of the deposited film is facilitated, and the functional deposited film having reproducibility and mass productivity can be formed.

本発明によれば、活性化ハロゲンが、化合物(A)及び
(B)よりII族元素及びVI族元素を残しての炭化水素基
等の離脱を容易にし、炭素等の不要な不純物の含有がほ
とんど見られない良質のII-VI族化合物堆積膜を容易に
形成することができる。
According to the present invention, the activated halogen facilitates the elimination of the hydrocarbon group and the like from the compounds (A) and (B) leaving the group II element and the group VI element, and the inclusion of unnecessary impurities such as carbon. It is possible to easily form a high-quality II-VI group compound deposited film that is rarely seen.

[好適な実施態様の説明] 本発明で云う「活性種」とは、前記化合物(A)又は/
及び化合物(B)と化学的相互作用を起して例えば前記
化合物(A)又は/及び(B)にエネルギーを与えた
り、化合物(A)又は/及び(B)と化学的に反応した
りして、化合物(A)又は/及び(B)を堆積膜を形成
することが出来る状態にする役目を荷うものを云う。従
って、「活性種」としては、形成される堆積膜を構成す
る構成要素に成る構成要素を含んでいても良く、或いは
その様な構成要素を含んでいなくとも良い。
[Explanation of Preferred Embodiments] The “active species” in the present invention means the compound (A) or /
And causing a chemical interaction with the compound (B) to give energy to the compound (A) or / and (B), or chemically react with the compound (A) or / and (B). Then, the compound (A) and / or (B) has a function of bringing the compound (A) and / or (B) into a state capable of forming a deposited film. Therefore, the “active species” may or may not include a component that constitutes a deposited film to be formed.

本発明において使用される前記一般式(A)及び(B)
の夫々で示される化合物(A)及び(B)としては、成
膜される基体が存在する空間において、前記の活性種と
分子的衝突を起して化学反応を起し、基体上に形成され
る堆積膜の形成に寄与する化学種を自発的に発生するも
のを選択するのがより望ましいものであるが、通常の存
在状態では、前記の活性種とは不活性であったり、或
は、それ程の活性々がない場合には、化合物(A)及び
(B)に該化合物(A)及び(B)が前記一般式(A)
及び(B)中のM及びAを完全解離しない程度の強さの
励起エネルギーを成膜前又は成膜時に与えて、化合物
(A)及び(B)を活性種と化学反応し得る励起状態に
することが必要であり、又、その様な励起状態にし得る
化合物を、本発明の方法に使用される化合物(A)及び
(B)の1種として採用するものである。
The general formulas (A) and (B) used in the present invention
Compounds (A) and (B) represented by each of the above are formed on the substrate by causing a chemical reaction by causing a molecular collision with the active species in the space where the substrate to be formed is present. It is more desirable to select one that spontaneously generates a chemical species that contributes to the formation of a deposited film, but in a normal existence state, it is inactive with the above active species, or When the compounds (A) and (B) have no such activity, the compounds (A) and (B) are replaced by the compounds represented by the general formula (A).
And (B) in which M and A in M are not completely dissociated from each other, and excitation energy having a strength that does not completely dissociate is applied to the compound (A) and (B) to an excited state capable of chemically reacting with the active species. In addition, a compound capable of producing such an excited state is employed as one of the compounds (A) and (B) used in the method of the present invention.

尚、本発明においては、化合物が前記の励起状態になっ
ているものを以後「励起種」と呼称することにする。
In the present invention, the compound in the excited state will be referred to as “excited species” hereinafter.

本発明において、前記一般式(A)及び(B)で夫々示
される化合物(A)RnMm及び化合物(B)AaBbとして、
有効に使用されるものとしては以下の化合物を挙げるこ
とが出来る。
In the present invention, as the compound (A) RnMm and the compound (B) AaBb represented by the general formulas (A) and (B), respectively,
The following compounds can be mentioned as those effectively used.

即ち「M」としては周期律表第IIB族に属する元素、具
体的にはZn,Cd,Hgを、「A」としては周期律表第VI族に
属する元素でO,S,Se,Teから選択される元素を挙げるこ
とが出来る。
That is, “M” is an element belonging to Group IIB of the periodic table, specifically Zn, Cd, Hg, and “A” is an element belonging to Group VI of the periodic table from O, S, Se, Te. The elements selected can be mentioned.

「R」及び「B」としては、直鎖状及び側鎖状の飽和炭
化水素や不飽和炭化水素から誘導される一価,二価及び
三価の炭化水素基、或いは、飽和又は不飽和の単環状の
及び多環状の炭化水素より誘導される一価,二価及び三
価の炭化水素基を挙げることが出来る。
“R” and “B” include monovalent, divalent and trivalent hydrocarbon groups derived from linear and side chain saturated hydrocarbons and unsaturated hydrocarbons, or saturated or unsaturated hydrocarbon groups. Mention may be made of monovalent, divalent and trivalent hydrocarbon radicals derived from monocyclic and polycyclic hydrocarbons.

不飽和の炭化水素基としては、炭素・炭素の結合は単一
種の結合だけでなく、一重結合,二重結合,及び三重結
合の中の少なくとも2種の結合を有しているものも本発
明の目的の達成に違うものであれば有効に採用され得
る。
As the unsaturated hydrocarbon group, not only a single type of carbon-carbon bond but also a single type bond, a double bond, and a triple bond have at least two types of bonds. Can be effectively adopted if they are different in achieving the purpose of.

又、二重結合を複数有する不飽和炭化水素基の場合、非
集積二重結合であっても集積二重結合であっても差支え
ない。
Further, in the case of an unsaturated hydrocarbon group having a plurality of double bonds, it may be a non-integrated double bond or an integrated double bond.

非環状炭化水素基としてはアルキル基,アルケニル基,
アルキニル基,アルキリデン基,アルケニリデン基,ア
ルキニリデン基,アルキリジン基,アルケニリジン基,
アルキニリジン基等を好ましいものとして挙げることが
出来、殊に、炭素数としては、好ましくは1〜10、より
好ましくは炭素数1〜7、最適には炭素数1〜5のもの
が望ましい。
As the acyclic hydrocarbon group, an alkyl group, an alkenyl group,
Alkynyl group, Alkylidene group, Alkenylidene group, Alkynylidene group, Alkyridine group, Alkenyridine group,
Alkynilidine groups and the like can be mentioned as preferable ones, and in particular, those having 1 to 10 carbon atoms, more preferably 1 to 7 carbon atoms, and most preferably 1 to 5 carbon atoms are desirable.

本発明においては、有効に使用される化合物(A)及び
(B)として、標準状態で気体状であるか或いは使用環
境下において容易に気化し得るものが選択される様に、
上記に列挙した「R」と「M」及び「A」と「B」との
選択において、適宜所望に従って、「R」と「M」及び
「A」と「B」との組合せの選択がなされる。
In the present invention, compounds (A) and (B) that are effectively used are selected such that they are gaseous in the standard state or can be easily vaporized under the use environment,
In the selection of "R" and "M" and "A" and "B" listed above, a combination of "R" and "M" and "A" and "B" is selected as desired. It

本発明において、化合物(A)として、有効に使用され
る具体的なものとしては、ZnMe3,CdMe3,ZnEt3,CdEt3
を、化合物(B)として、有効に使用される具体的なも
のとしては、Me2O,Me2S,Me2Se,Me2Te,Et2O,Et2S,Et2Se,
Et2Te,X2O,SX2,SX4,SX6,SeX2,SeX4,SeX6,TeX6H2O,H2S,H
2Se,H2Te等を挙げることが出来る。
In the present invention, specific examples that are effectively used as the compound (A) include ZnMe 3 , CdMe 3 , ZnEt 3 and CdEt 3 that are effectively used as the compound (B). Me 2 O, Me 2 S, Me 2 Se, Me 2 Te, Et 2 O, Et 2 S, Et 2 Se,
Et 2 Te, X 2 O, SX 2 , SX 4 , SX 6 , SeX 2 , SeX 4 , SeX 6 , TeX 6 H 2 O, H 2 S, H
2 Se, H 2 Te, etc. can be mentioned.

上記において、Xはハロゲン(F,Cl,Br,I)、Meはメチ
ル基、Etはエチル基を示す。
In the above, X represents halogen (F, Cl, Br, I), Me represents a methyl group, and Et represents an ethyl group.

本発明で使用される活性種の寿命は、化合物(A)又は
/及び(B)との反応性を考慮すれば短い方が良く、成
膜時の取扱い易さ及び成膜空間への輸送等を考慮すれば
長い方が良い。又、活性種の寿命は、成膜空間の内圧に
も依存する。
The life of the active species used in the present invention is preferably short in consideration of the reactivity with the compound (A) and / or (B), and it is easy to handle during film formation and transportation to the film formation space. Considering the above, the longer the better. Further, the life of the active species depends on the internal pressure of the film forming space.

従って使用される活性種は、所望する特性を有する機能
性膜が生産効率も加味して効果的に得られる様に選択さ
れて決定される他の成膜条件との関連性において、適当
な寿命を有する活性種が適宜選択されて使用される。
Therefore, the active species used are selected so that the functional film having the desired properties can be effectively obtained in consideration of the production efficiency, and the active species used have an appropriate life in relation to other film forming conditions. The active species having is selected appropriately and used.

本発明において使用される活性種は、その寿命として、
上記の点を鑑みて適宜選択された寿命を有する活性種が
具体的に使用される化合物(A)又は/及び(B)との
化学的親和性の適合範囲内の中より所望に従って適宜選
択されるが、好ましくは、その寿命としては、本発明の
適合範囲の環境下において1×10-4秒以上、より好まし
くは1×10-3秒以上、最適には1×1012秒以上であるの
が望ましい。
The active species used in the present invention has, as its life span,
In view of the above points, the active species having a properly selected life span is appropriately selected as desired from within the range of compatible chemical affinity with the compound (A) or / and (B) specifically used. However, the life is preferably 1 × 10 −4 seconds or more, more preferably 1 × 10 −3 seconds or more, most preferably 1 × 10 12 seconds or more under the environment of the conforming range of the present invention. Is desirable.

本発明において使用される活性種は、化合物(A)又は
/及び(B)との化学反応が連鎖的に起こる場合には所
謂開始剤(initiater)としての働きを最小限にすれば
良いことから、成膜空間に導入される導入量としては、
化学反応が連鎖的に効率良く起こる程度の量が確保され
れば良い。
The active species used in the present invention has a function as a so-called initiator (initiater) to be minimized when the chemical reaction with the compound (A) or / and (B) occurs in a chain. As the amount of introduction to the film formation space,
It suffices to secure an amount such that chemical reactions occur efficiently in a chain.

本発明において使用される活性種は成膜空間(A)で堆
積膜を形成する際、同時に成膜空間(A)に導入され、
形成される堆積膜の主構成成分となる構成要素を含む前
記化合物(A)及び(B)又は/及び該化合物(A)G
の励起種(A)又は/及び化合物(B)の励起種(B)
と化学的に相互作用する。その結果所望の基体上に所望
の機能成を有するII−VI族化合物堆積膜が容易に形成さ
れる。
The active species used in the present invention are introduced into the film formation space (A) at the same time when the deposited film is formed in the film formation space (A),
The compounds (A) and (B) or / and the compound (A) G containing a constituent element which is a main constituent of the deposited film to be formed.
Excited species (A) and / or compound (B) excited species (B)
Chemically interact with. As a result, a II-VI group compound deposited film having a desired functional composition is easily formed on a desired substrate.

本発明によれば成膜空間(A)の雰囲気温度、基体温度
を所望に従って任意に制御する事により、より安定した
CVD法とする事ができる。
According to the present invention, the ambient temperature of the film formation space (A) and the substrate temperature are controlled arbitrarily as desired to make it more stable.
It can be a CVD method.

本発明の方法が従来のCVD法と違う点の1つは、あらか
じめ、成膜空間(A)とは異なる〔活性化空間(C)〕
において活性化された活性種を使うことである。この事
により、従来のCVD法より堆積速度を飛躍的に伸ばす事
ができ、加えて堆積膜形成の際の基体温度も一層の低温
化を図ることが可能になり、膜品質の安定した、管理化
された膜特性を有する堆積膜を工業的に大量に、しかも
低コストで提供出来る。
One of the points that the method of the present invention is different from the conventional CVD method is that it is different from the film formation space (A) in advance [activation space (C)].
Is to use the activated species activated in. As a result, the deposition rate can be dramatically increased compared to the conventional CVD method, and in addition, the substrate temperature during deposition film formation can be further lowered, and stable film quality control can be achieved. It is possible to industrially provide a large amount of deposited film having improved film characteristics at low cost.

本発明において活性化空間(C)で生成される活性種は
放電、光、熱等のエネルギーで或いはそれ等の併用によ
って励起されて活性化されるばかりではなく、触媒など
との接触、あるいは添加により生成されてもよい。
In the present invention, the active species generated in the activation space (C) are not only activated by being excited by energy of discharge, light, heat or the like or by combination thereof, but also contact with a catalyst or addition thereof. May be generated by

本発明において、活性化空間(C)に導入され、活性種
を生成させる原料としては、好ましくは気体状の又は容
易に気化し得る物質で、ハロゲンラジカルを生成する物
質を挙げることが出来、具体的にはF2,Cl2,Br2,I2のハ
ロゲンガスやBrF,ClF,ClF3,ClF5,BrF5,BrF3,IF7,IF5,IC
l,IBr等のハロゲン間化合物等が挙げられ、その他、こ
れ等に加えて使用されるものとしてHe,Ar等の稀ガスも
挙げることが出来る。
In the present invention, the raw material that is introduced into the activation space (C) to generate the active species is preferably a substance that is in the form of a gas or easily vaporizable and that generates a halogen radical. thereof include F 2, Cl 2, Br 2 , I 2 of halogen gas or BrF, ClF, ClF 3, ClF 5, BrF 5, BrF 3, IF 7, IF 5, IC
Examples thereof include interhalogen compounds such as l and IBr, and rare gases such as He and Ar that can be used in addition to these.

上述したものに、活性化空間(C)で熱,光,放電など
の活性化エネルギーを加えることにより、活性種が生成
される。この活性種を成膜空間(A)へ導入する。この
際、活性種の寿命が望ましくは1×10-4秒以上であるこ
とが必要で、その様な寿命を有することで堆積効率及び
堆積速度の上昇を促進させ、成膜空間(A)に導入され
る化合物(A)との化学反応の効率を増す。
Activated species are generated by adding activation energy such as heat, light, or discharge in the activation space (C) to the above. This active species is introduced into the film forming space (A). At this time, it is necessary that the life of the active species is desirably 1 × 10 −4 seconds or more. By having such a life, the deposition efficiency and the deposition rate are accelerated, and the film formation space (A) is formed. Increase the efficiency of the chemical reaction with the introduced compound (A).

活性化空間(C)において活性種生成物質に活性化作用
を起す活性化エネルギーとしては、具体的には抵抗加
熱,赤外線加熱等による熱エネルギー,レーザー光,水
銀ランプ光,ハロゲンランプ光等の光エネルギー,マイ
クロ波,RF,低周波,DC等の放電を利用する電気エネルギ
ー等々を挙げることが出来、これ等の活性化エネルギー
は活性化空間(C)において単独で活性種生成物質に作
用させても良く、又、2種以上を併用して作用させても
良い。成膜空間(A)に導入される化合物(A),化合
物(B)及び活性種としては、そのままでも分子レベル
的相互衝突によって化学反応を生起し、所望の気体上に
機能成膜を堆積させることが出来るものを前記に列挙し
たものの中より夫々選択することが出来るが、化合物
(A),化合物(B)及び活性種の夫々の選択の仕方に
よって、前記の化学反応性に乏しい場合、或いは一層効
果的に化学反応を行わせて、効率良く堆積膜を気体上に
生成する場合には、成膜空間(A)において、化合物
(A),化合物(B)又は/及び活性種に作用する反応
促進エネルギー、例えば前述の活性化空間(C)におい
て使用される活性化エネルギーを使用しても差支えない
ものである。又は成膜空間(A)に導入する前に化合物
(A)及び化合物(B)を他の活性化空間(B)におい
て、化合物(A)及び化合物(B)を前述した励起状態
にする為に励起エネルギーを作用させても良い。
The activation energy that causes an activation action on the active species generating substance in the activation space (C) is specifically heat energy such as resistance heating or infrared heating, laser light, mercury lamp light, halogen lamp light, or the like. Energy, microwave, RF, low frequency, electric energy using discharge such as DC, etc. can be mentioned. These activation energies act on the active species generating substance alone in the activation space (C). Also, two or more kinds may be used in combination to act. The compound (A), the compound (B), and the active species introduced into the film formation space (A) cause a chemical reaction due to mutual collision at a molecular level even as they are to deposit a functional film on a desired gas. The compounds that can be selected from those listed above can be selected depending on the selection method of each of the compound (A), the compound (B) and the active species, or In the case where the chemical reaction is performed more effectively and the deposited film is efficiently generated on the gas, it acts on the compound (A), the compound (B), and / or the active species in the film formation space (A). The reaction accelerating energy, for example, the activation energy used in the above-mentioned activation space (C) can be used. Alternatively, in order to bring the compound (A) and the compound (B) into the above-mentioned excited state in the other activation space (B) before being introduced into the film formation space (A). Excitation energy may be applied.

本発明において成膜空間(A)に導入される化合物
(A)と化合物(B)の総量と活性化空間(C)から導
入される活性種の量の割合は、堆積条件,化合物
(A),化合物(B)及び活性種の種類、所望される機
能性膜の特性などで適宜所望に従って決められるが好ま
しくは1000:1〜1:10(導入流量比)が適当であり、より
好ましくは500:1〜1:5とされるのが望ましい。
In the present invention, the ratio of the total amount of the compound (A) and the compound (B) introduced into the film forming space (A) and the amount of the active species introduced from the activation space (C) is determined by the deposition conditions, the compound (A). , The type of compound (B) and active species, the desired characteristics of the functional membrane, etc., and may be appropriately determined according to the desire, but 1000: 1 to 1:10 (introduction flow ratio) is suitable, and more preferably 500. -1 to 1: 5 is preferable.

活性種が化合物(A)又は/及び化合物(B)と連鎖的
化学反応を起さない場合には、上記の導入量の割合は、
好ましくは10:1〜1:10、より好ましくは4:1〜2:3とされ
るのが望ましい。成膜時における成膜空間(A)の内圧
としては、化合物(A),化合物(B)及び活性種の選
択される種類及び堆積条件等に従って適宜決定される
が、好ましくは1×10-2〜5×103Pa、より好ましくは
5×10-2〜1×103Pa、最適には1×10-1〜5×102Paと
されるのが望ましい。又、成膜時に基体を加熱する必要
がある場合には基体温度としては好ましくは、50〜1000
℃、より好ましくは100〜900℃、最適には100〜750℃と
されるのが望ましい。
When the active species does not cause a chain chemical reaction with the compound (A) or / and the compound (B), the above introduction ratio is
It is preferably 10: 1 to 1:10, more preferably 4: 1 to 2: 3. The internal pressure of the film formation space (A) during film formation is appropriately determined according to the selected type of compound (A), compound (B) and active species, deposition conditions, etc., but is preferably 1 × 10 -2. ˜5 × 10 3 Pa, more preferably 5 × 10 −2 to 1 × 10 3 Pa, most preferably 1 × 10 −1 to 5 × 10 2 Pa. Further, when it is necessary to heat the substrate during film formation, the substrate temperature is preferably 50 to 1000.
C., more preferably 100 to 900.degree. C., optimally 100 to 750.degree.

成膜空間(A)に化合物(A),化合物(B)及び活性
種を導入する際の導入の仕方は、成膜空間(A)に連結
されている輸送管を通じて導入しても良いし、或いは成
膜空間(A)に設置してある基体の成膜表面近くまで前
記の輸送管を延在させて、先端をノズル状となして導入
しても良とし、輸送管を二重にして円側の管で一方を、
外側の管で他方を、例えば内側の管で活性種を、外側の
管で化合物(A)及び化合物(B)を夫々輸送して成膜
空間(A)中に導入しても良い。
When introducing the compound (A), the compound (B) and the active species into the film forming space (A), the introduction method may be through a transport pipe connected to the film forming space (A). Alternatively, the transport pipe may be extended to near the deposition surface of the substrate installed in the deposition space (A), and the tip may be introduced in the form of a nozzle, and the transport pipe may be doubled. With the tube on the circle side,
The other may be transported by the outer tube, for example, the active species may be transported by the inner tube, and the compound (A) and the compound (B) may be transported by the outer tube and introduced into the film formation space (A).

又、輸送管に連結されている3本のノズルを用意し、該
3本のノズルの先端を成膜空間(A)に既に設置されて
いる基体の表面近傍に配して、基体の表面近くにおいて
夫々のノズルより吐出される化合物(A)と化合物
(B)と活性種とが混合される様にして導入しても良
い。この場合には、基体上に選択的に機能性膜を形成す
ることが可能なので成膜と同時にパターン化が出来る為
に好都合である。
Further, three nozzles connected to the transport pipe are prepared, and the tips of the three nozzles are arranged in the vicinity of the surface of the substrate already installed in the film forming space (A) so that the surface of the substrate is close to the nozzle. In, the compound (A) and the compound (B) discharged from the respective nozzles and the active species may be mixed and introduced. In this case, the functional film can be selectively formed on the substrate, which is convenient because it can be patterned simultaneously with the film formation.

以下、本発明を実施例によって具体的に説明する。Hereinafter, the present invention will be specifically described with reference to examples.

実施例1 第1図のガス導入管102より、F2ガス200SCCMを石英ガラ
ス管によりできている活性化室103に導入し、活性化源
5としての活性化室103上におかれた導波管より300Wの
マイクロ波を活性化室103に作用させ、活性化室103中に
Fラジカルを発生させた。発生したFラジカルは石英ガ
ラス管より出来ている輸送管102-2を介して、ノズル100
-3より成膜室104に導入された。
Example 1 F 2 gas 200SCCM was introduced into the activation chamber 103 made of a quartz glass tube through the gas introduction pipe 102 of FIG. 1, and the waveguide placed on the activation chamber 103 as the activation source 5 was introduced. A microwave of 300 W was made to act on the activation chamber 103 from the tube to generate F radicals in the activation chamber 103. The generated F radicals are transferred to the nozzle 100 via a transport pipe 102-2 made of a quartz glass pipe.
-3 was introduced into the film forming chamber 104.

これと同時にガス導入管101-2を通じてHeガスによりバ
ブリングされた(CH3)2Znが10mmol/minの割合でノズル10
0-2より成膜室104に導入された。他方、ガス導入管101-
1を通じてH2Sガスを10mmol/minの割合でノズル100-10よ
り成膜室104に導入された。この場合(C2H5)2Zn及びH2S
はHラジカルの作用によって活性化されてZn,Sを分解
し、基体ヒーター109により約230℃に加熱されたAl2O3
の基体上108に1.5時間で30cm×30cmの面積に約2.2μm
の膜厚のZnS膜が形成された。
At the same time, the (CH 3 ) 2 Zn bubbled by He gas through the gas inlet pipe 101-2 was supplied at a rate of 10 mmol / min to the nozzle 10.
It was introduced into the film forming chamber 104 from 0-2. On the other hand, gas inlet pipe 101-
H 2 S gas was introduced into the film forming chamber 104 from the nozzle 100-10 at a rate of 10 mmol / min through 1. In this case (C 2 H 5 ) 2 Zn and H 2 S
Is activated by the action of H radicals to decompose Zn and S, and Al 2 O 3 heated to about 230 ° C. by the substrate heater 109.
Approximately 2.2 μm on a substrate of 108 in an area of 30 cm × 30 cm in 1.5 hours
A ZnS film having the film thickness of was formed.

このZnS膜の膜特性を評価したところ、膜厚の斑がな
く、又、半導体特性も場所による依存性が殆どない良質
な膜であることが確認された。
When the film characteristics of this ZnS film were evaluated, it was confirmed that there was no unevenness in the film thickness and that the semiconductor characteristics were of good quality with little dependence on location.

実施例2 実施例1において(C2H5)2Zn,及びH2Sの代りに第1表に
示す原料ガスを化合物(A)及び化合物(B)として夫
々使用し、化合物(A)と化合物(B)の導入量を夫々
1mmol/minとし、第1表に記載した条件以外は、実施例
1と略々同様にして成膜したところ第1表に示す薄膜が
形成された。
In Example 2 Example 1 (C 2 H 5) 2 Zn, and a raw material gas shown in Table 1 respectively used to as the compound (A) and the compound (B) in place of H 2 S, a compound (A) The amount of compound (B) introduced is
The film was formed in substantially the same manner as in Example 1 except that the conditions were 1 mmol / min and the conditions shown in Table 1 were obtained. As a result, the thin film shown in Table 1 was formed.

これ等の薄膜に就いて膜特性の評価を行ったところ均一
膜厚で、均一で良品質の特性に優れた膜であることが確
認された。
When the film characteristics of these thin films were evaluated, it was confirmed that the films had a uniform film thickness and were uniform and of excellent quality.

実施例3 実施例1において、成膜室104の周囲に設置されたRF放
電装置106で13.56MHzの高周波で3Wの電力を成膜室104に
投入して反応室104内にプラズマ雰囲気を形成した。こ
の場合、基体106はプラズマ雰囲気には直接触れない様
にプラズマ雰囲気の下流側約1cmの位置においた。成膜
開始後1時間で約2μm厚のZnS膜が形成できた。この
際の基体温度は200℃に保った。上記以外は実施例1と
同様にして行った。
Example 3 In Example 1, an RF discharge device 106 installed around the film forming chamber 104 supplied 3 W of power at a high frequency of 13.56 MHz to the film forming chamber 104 to form a plasma atmosphere in the reaction chamber 104. . In this case, the substrate 106 was placed at a position of about 1 cm on the downstream side of the plasma atmosphere so as not to directly touch the plasma atmosphere. A ZnS film having a thickness of about 2 μm could be formed within 1 hour after starting the film formation. At this time, the substrate temperature was kept at 200 ° C. Except for the above, the same procedure as in Example 1 was carried out.

このGaAs膜を実施例1と同様に膜特性の評価を行ったと
ころ、良品質の膜であることが確認された。
When the film characteristics of this GaAs film were evaluated in the same manner as in Example 1, it was confirmed that the film was of good quality.

又、基体からの剥離もなく機械的にも優れた膜であっ
た。
The film was also mechanically excellent without peeling from the substrate.

実施例4 実施例1においてF2ガスの代りにCl2ガスを使用した以
外は実施例1と同様の方法によってGaAs膜を作成した。
このGaAs膜の膜特性も良好なものであることが確認され
た。
Example 4 A GaAs film was formed by the same method as in Example 1 except that Cl 2 gas was used instead of F 2 gas in Example 1.
It was confirmed that the film characteristics of this GaAs film were also good.

〔発明の効果〕〔The invention's effect〕

本発明の堆積膜形成法によれば、形成される膜に所望さ
れる電気的、光学的、光導電的及び機械的特性が向上
し、又、成膜における再現性が向上する。しかも、炭素
等の不要な不純物の含有がほとんど見られない程の膜品
質の向上と膜質の均一化が可能になると共に、膜の大面
積化に有利であり、膜の生産性の向上並びに量産化を容
易に達成することができる。
According to the deposited film forming method of the present invention, desired electrical, optical, photoconductive and mechanical properties of the formed film are improved, and reproducibility in film formation is improved. Moreover, it is possible to improve the film quality and make the film quality uniform so that the inclusion of unnecessary impurities such as carbon is hardly seen, and it is advantageous for increasing the area of the film, improving the film productivity and mass production. Can be easily achieved.

更に、低温での成膜も可能であるために、耐熱性に乏し
い基体上にも成膜できる、低温処理によって工程の短縮
化を図れる活性種の導入量を制御して形成される堆積膜
の組成比及び特性を管理することが出来るといった効果
が発揮される。
Further, since the film can be formed at a low temperature, the film can be formed even on a substrate having poor heat resistance. The process can be shortened by the low temperature treatment. The effect that the composition ratio and characteristics can be managed is exhibited.

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

第1図は本発明方法を具現化する製造装置の模式図であ
る。 101……導入管、 102……輸送管、 103……活性化室、 104……成膜室。
FIG. 1 is a schematic diagram of a manufacturing apparatus embodying the method of the present invention. 101 …… Introduction pipe, 102 …… Transport pipe, 103 …… Activation chamber, 104 …… Film forming chamber.

フロントページの続き (72)発明者 金井 正博 東京都大田区下丸子3丁目30番2号 キヤ ノン株式会社内 (72)発明者 小田 俊理 東京都世田谷区深沢8―11―14―503 (72)発明者 清水 勇 神奈川県横浜市緑区藤が丘2―41―21 (56)参考文献 特開 昭54−158190(JP,A) 「IBM T.D.B」,22[8A], (1980−1),P.3391〜2 第45回「応物学会予稿集」(’84−10− 12),P.628〜630Front page continuation (72) Inventor Masahiro Kanai 3-30-2 Shimomaruko, Ota-ku, Tokyo Canon Inc. (72) Inventor Shunri Oda 8-11-14-503 Fukasawa, Setagaya-ku, Tokyo (72) Invention Satoru Shimizu 2-41-21 Fujigaoka, Midori-ku, Yokohama-shi, Kanagawa (56) Reference JP 54-158190 (JP, A) "IBM TDB", 22 [8A], (1980-1) , P .; 3391-2 The 45th "The Society of Biological Society Proceedings" ('84 -10-12), p. 628 ~ 630

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】成膜空間に配された基体上に堆積膜を形成
する堆積膜形成法において、 mをRの価数に等しいか又はその整数倍の正整数、nを
Mの価数に等しいか又はその整数倍の正整数、Mを周期
律表の第IIB族に属する元素、Rを炭化水素基としたと
きに、一般式RnMmで表わされる活性化されていない化合
物(A)と、 aをBの価数に等しいか又はその整数倍の正整数、bを
Aの価数に等しいか又はその整数倍の正整数、Aを周期
律表の第VI族に属するO,S,Se,Teから選択される元素、
Bを水素、ハロゲン、炭化水素基としたときに、一般式
AaBbで表わされる活性化されていない化合物(B)と、 前記成膜空間とは異なる活性化空間において生成した活
性種としての活性化ハロゲンと、 を前記成膜空間に導入し、化学反応させることにより前
記基体上にII-VI族化合物の堆積膜を形成することを特
徴とする堆積膜形成法。
1. A deposition film forming method for forming a deposition film on a substrate arranged in a film forming space, wherein m is a positive integer equal to or an integer multiple of R, and n is a valence of M. A non-activated compound (A) represented by the general formula RnMm, where M is an integer that is equal to or an integer multiple thereof, M is an element belonging to Group IIB of the periodic table, and R is a hydrocarbon group; a is a positive integer that is equal to or an integer multiple of B, b is a positive integer that is equal to or an integer multiple of A, and A is O, S, Se belonging to Group VI of the periodic table. , An element selected from Te,
When B is hydrogen, halogen or a hydrocarbon group, the general formula
A non-activated compound (B) represented by AaBb and an activated halogen as an active species generated in an activation space different from the film formation space are introduced into the film formation space and chemically reacted. A method for forming a deposited film, comprising forming a deposited film of a II-VI group compound on the substrate by:
JP60029813A 1985-02-18 1985-02-18 Deposited film formation method Expired - Lifetime JPH0691112B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP60029813A JPH0691112B2 (en) 1985-02-18 1985-02-18 Deposited film formation method
US07/113,414 US4772486A (en) 1985-02-18 1987-10-27 Process for forming a deposited film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60029813A JPH0691112B2 (en) 1985-02-18 1985-02-18 Deposited film formation method

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JPS61189650A JPS61189650A (en) 1986-08-23
JPH0691112B2 true JPH0691112B2 (en) 1994-11-14

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Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1303194C (en) 1987-07-21 1992-06-09 Katsumi Nakagawa Photovoltaic element with a semiconductor layer comprising non-single crystal material containing at least zn, se and h in an amount of 1 to40 atomic %
JPS6436086A (en) * 1987-07-31 1989-02-07 Canon Kk Functional deposition film
EP0301903A3 (en) 1987-07-31 1990-07-11 Canon Kabushiki Kaisha Functional znse1-xtex: h deposited film
EP0317350B1 (en) 1987-11-20 1995-06-21 Canon Kabushiki Kaisha A pin function photovoltaic element, tandem und triple cells
JP2717583B2 (en) * 1988-11-04 1998-02-18 キヤノン株式会社 Stacked photovoltaic element

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54158190A (en) * 1978-06-05 1979-12-13 Yamazaki Shunpei Semiconductor device and method of fabricating same

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
「IBMT.D.B」,22[8A,(1980−1),P.3391〜2
第45回「応物学会予稿集」(’84−10−12),P.628〜630

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