JPH0620975A - Carbon film manufacturing method - Google Patents
Carbon film manufacturing methodInfo
- Publication number
- JPH0620975A JPH0620975A JP26927092A JP26927092A JPH0620975A JP H0620975 A JPH0620975 A JP H0620975A JP 26927092 A JP26927092 A JP 26927092A JP 26927092 A JP26927092 A JP 26927092A JP H0620975 A JPH0620975 A JP H0620975A
- Authority
- JP
- Japan
- Prior art keywords
- substrate
- carbon
- film
- reaction
- plasma
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 45
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 238000004519 manufacturing process Methods 0.000 title claims description 23
- 238000006243 chemical reaction Methods 0.000 claims abstract description 54
- 239000000758 substrate Substances 0.000 claims abstract description 53
- 238000000034 method Methods 0.000 claims abstract description 33
- 239000001301 oxygen Substances 0.000 claims abstract description 13
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 13
- 239000012808 vapor phase Substances 0.000 claims abstract description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 31
- 239000001257 hydrogen Substances 0.000 claims description 11
- 229910052739 hydrogen Inorganic materials 0.000 claims description 11
- 238000004140 cleaning Methods 0.000 claims description 4
- 150000002222 fluorine compounds Chemical class 0.000 claims description 4
- 238000000151 deposition Methods 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 239000012535 impurity Substances 0.000 abstract description 20
- 229910010271 silicon carbide Inorganic materials 0.000 abstract description 15
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 abstract description 14
- CZDYPVPMEAXLPK-UHFFFAOYSA-N tetramethylsilane Chemical compound C[Si](C)(C)C CZDYPVPMEAXLPK-UHFFFAOYSA-N 0.000 abstract description 7
- 239000007795 chemical reaction product Substances 0.000 abstract description 6
- 238000005530 etching Methods 0.000 abstract description 2
- HMDDXIMCDZRSNE-UHFFFAOYSA-N [C].[Si] Chemical compound [C].[Si] HMDDXIMCDZRSNE-UHFFFAOYSA-N 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- 230000008878 coupling Effects 0.000 abstract 1
- 238000010168 coupling process Methods 0.000 abstract 1
- 238000005859 coupling reaction Methods 0.000 abstract 1
- 239000004065 semiconductor Substances 0.000 description 35
- 229910052698 phosphorus Inorganic materials 0.000 description 12
- 229910052757 nitrogen Inorganic materials 0.000 description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 7
- 238000000576 coating method Methods 0.000 description 7
- 238000005268 plasma chemical vapour deposition Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 150000001340 alkali metals Chemical group 0.000 description 5
- 239000001307 helium Substances 0.000 description 5
- 229910052734 helium Inorganic materials 0.000 description 5
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910052796 boron Inorganic materials 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 230000005672 electromagnetic field Effects 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 238000001020 plasma etching Methods 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 2
- 239000012159 carrier gas Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 150000004820 halides Chemical class 0.000 description 2
- 150000004678 hydrides Chemical class 0.000 description 2
- 229910052740 iodine Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000009832 plasma treatment Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 229910000077 silane Inorganic materials 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910001868 water Inorganic materials 0.000 description 2
- -1 By (51) Substances 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910018540 Si C Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910000410 antimony oxide Inorganic materials 0.000 description 1
- 238000003491 array Methods 0.000 description 1
- RBFQJDQYXXHULB-UHFFFAOYSA-N arsane Chemical compound [AsH3] RBFQJDQYXXHULB-UHFFFAOYSA-N 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000001804 chlorine Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- ZOCHARZZJNPSEU-UHFFFAOYSA-N diboron Chemical compound B#B ZOCHARZZJNPSEU-UHFFFAOYSA-N 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 230000005669 field effect Effects 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052733 gallium Inorganic materials 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- VTRUBDSFZJNXHI-UHFFFAOYSA-N oxoantimony Chemical compound [Sb]=O VTRUBDSFZJNXHI-UHFFFAOYSA-N 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 229910021332 silicide Inorganic materials 0.000 description 1
- FVBUAEGBCNSCDD-UHFFFAOYSA-N silicide(4-) Chemical compound [Si-4] FVBUAEGBCNSCDD-UHFFFAOYSA-N 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- VCZQFJFZMMALHB-UHFFFAOYSA-N tetraethylsilane Chemical compound CC[Si](CC)(CC)CC VCZQFJFZMMALHB-UHFFFAOYSA-N 0.000 description 1
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 description 1
- 229910001887 tin oxide Inorganic materials 0.000 description 1
- 238000001771 vacuum deposition Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/50—Photovoltaic [PV] energy
Landscapes
- Photovoltaic Devices (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明はプラズマ気相法により、
再現性、特性のよい炭素または炭素を主成分とする膜を
作製する方法に関する。BACKGROUND OF THE INVENTION The present invention is based on the plasma vapor phase method.
The present invention relates to a method for producing carbon or a film containing carbon as a main component, which has good reproducibility and characteristics.
【0002】本発明はプラズマ気相法により反応炉内に
設けられた基板上にP型およびN型の層を形成した後、
このNまたはP型不純物が次に作られるPまたはN型の
半導体層中に反応装置の内壁または基板のホルダにより
再放出され、これが1015〜1018cm-3の濃度で混入
されてしまうことを防止するため、この各工程の間に前
の回に作られた層上に真性または実質的に真性(以下I
層という)のコ−ティング用の膜を形成する工程(この
場合は次の工程の最初に作られる膜をコ−ティングして
もよい)により実質的に過去の履歴を除去してしまうこ
とを目的とする。According to the present invention, after P-type and N-type layers are formed on a substrate provided in a reaction furnace by a plasma vapor phase method,
This N or P type impurity is re-emitted by the inner wall of the reactor or the holder of the substrate into the P or N type semiconductor layer to be produced next, and this is mixed in at a concentration of 10 15 to 10 18 cm -3. In order to prevent the intrinsic or substantially intrinsic (hereinafter I
The process of forming a coating film (referred to as a layer) (in this case, the film formed at the beginning of the next process may be coated) substantially removes the past history. To aim.
【0003】さらにまたは前回作られた層のうち、反応
装置の内壁、基板のホルダ等の表面に付着したものを水
素、CF4 等の弗素化合物反応性気体をプラズマ化する
ことにより除去してしまう工程を設けることを目的にし
ている。In addition, or in the previously formed layers, those adhering to the inner wall of the reactor, the surface of the holder of the substrate and the like are removed by converting hydrogen and a fluorine compound reactive gas such as CF 4 into plasma. The purpose is to provide a process.
【0004】かくすることにより再現性よくRUN−T
O−RUNの特性バラツキを少なくするとともに、その
得られた特性もきわめて優れたものとすることができる
という特徴を有する。By doing so, the RUN-T can be reproduced with good reproducibility.
The O-RUN has a characteristic that variations in characteristics can be reduced and the obtained characteristics can be made extremely excellent.
【0005】また本発明は反応炉内に設けられた基板上
に少なくともひとつの接合特にPIN、PI、NIまた
はPN接合を有する半導体装置において、反応炉の内壁
特にプラズマ原子または反応性気体が衝突する内壁より
不純物特に酸素、アルカリ金属原子が放出されることを
防ぐため、これらの表面に予め炭素または炭素を主成分
とする膜を形成することを目的としている。Further, according to the present invention, in a semiconductor device having at least one junction, particularly PIN, PI, NI or PN junction on a substrate provided in the reaction furnace, the inner wall of the reaction furnace, particularly plasma atoms or reactive gas, collides. In order to prevent impurities, particularly oxygen and alkali metal atoms, from being released from the inner wall, it is intended to form carbon or a film containing carbon as a main component in advance on the surface thereof.
【0006】[0006]
【従来の技術】従来プラズマCVD法に関しては、ひと
つの反応炉にてPIN接合等を有する半導体装置の作製
が行われていた。しかしこの接合を繰り返し行うと、全
くわけのわからない劣化、バラツキに悩まされてしま
い、半導体装置としての信頼性に不適当なものしかでき
なかった。2. Description of the Related Art Conventionally, with respect to the plasma CVD method, a semiconductor device having a PIN junction or the like has been manufactured in one reaction furnace. However, if this bonding is repeated, it suffers from completely indefinite deterioration and variation, and only the reliability as a semiconductor device is unsuitable.
【0007】この原因を調べた結果、この最大の原因
は、反応炉内に付着している酸素、アルカリ金属が半導
体層中に混入して、電気伝導度の低下をもたらすもので
あり、酸素にあっては1PPMの混入であっても、暗伝
導度10-6( Ωcm)-1を10-8(Ωcm)-1と1/1
00にまで下げてしまっていた。またアルカリ金属にあ
っても、5PPMの混入において、P型、I型の伝導度
の低下または透明導電膜の伝導度の低下をもたらしてし
まった。As a result of investigating the cause, the most probable cause is that oxygen and alkali metals adhering to the inside of the reaction furnace are mixed in the semiconductor layer to cause a decrease in electric conductivity. Even if 1PPM is mixed, the dark conductivity of 10 -6 (Ωcm) -1 is 10 -8 (Ωcm) -1 and 1/1
It had been lowered to 00. Further, even in the case of an alkali metal, when 5PPM is mixed, the conductivity of P-type and I-type is lowered or the conductivity of the transparent conductive film is lowered.
【0008】これらの混入を防ぐため、反応炉の内壁ま
た基板のホルダ(ボ−トともいう)の特にプラズマによ
る反応性気体にスパッタされる部分に対して、予め半導
体層を0.2〜2μの厚さに形成させ、コ−ティングし
てしまうことがきわめて重要であった。さらに再現性特
性劣化に対しては、ひとつの半導体装置の作製に対し、
その最後の工程がNまたはP型半導体層を作りまた次の
最初の工程にPまたはN型の半導体層を作ろうとした
時、1015〜1018cm-3の濃度に最初の不純物例えば
リンがP型半導体層中に混入してしまう。このためP型
半導体層は例えば1018〜1021cm-3の濃度にホウ素
を添加してP型層としてもその電気伝導度はリンの混入
により再結合中心が増加するためきわめて特性が悪く、
混入がない場合10-2〜10+1(Ωcm)-1に対し、1
0-6〜10-4(Ωcm)-1と1/100〜1/1000
しか得られなかった。In order to prevent these from being mixed, the semiconductor layer is preliminarily 0.2 to 2 .mu.m on the inner wall of the reaction furnace or the portion of the holder (also called "boat") of the substrate, which is sputtered by the reactive gas due to the plasma. It was extremely important that the film be formed to a thickness of 10 mm and coated. Furthermore, for the deterioration of reproducibility characteristics, for the fabrication of one semiconductor device,
When the last step is to make an N or P type semiconductor layer and the next first step is to make a P or N type semiconductor layer, the first impurity such as phosphorus is added at a concentration of 10 15 -10 18 cm -3. It is mixed in the P-type semiconductor layer. For this reason, even if boron is added to the P-type semiconductor layer at a concentration of, for example, 10 18 to 10 21 cm −3 , its electrical conductivity is extremely poor because the recombination centers increase due to the incorporation of phosphorus.
When there is no mixture: 10 -2 to 10 +1 (Ωcm) -1 against 1
0 -6 to 10 -4 (Ωcm) -1 and 1/100 to 1/1000
I only got it.
【0009】このためPIN型光電変換装置においては
2〜4%の効率を各ランごとのバラツキを±200%も
有して得られたにすぎず好ましくなかった。Therefore, in the PIN photoelectric conversion device, an efficiency of 2 to 4% was obtained only with a variation of ± 200% for each run, which was not preferable.
【0010】しかし本発明方法にあっては、8〜10%
の約3〜5倍の高い変換効率を得ることができるように
なった。However, in the method of the present invention, 8-10%
It has become possible to obtain a conversion efficiency as high as about 3 to 5 times that of.
【0011】またこの不純物酸素ド−ピングの効果を少
なくするため、本発明人の出願になる特許願 半導体装
置作製方法 特許願56−55608(原表示53−1
52887 昭和53年12月10日出願)が知られて
いる。これは例えばPIN半導体装置を作ろうとする
時、各P層、I層、N層をそれぞれ独立の反応炉を作
り、基板をその層間を移動せしめることにより行わんと
するものである。この方法にあっては、本発明と同じ対
策を持つことができ、きわめて好ましい電気的特性を得
ることができる。しかしその場合、装置はひとつの室の
方法の3倍であり、製造コストが2.5〜3倍も高価に
なってしまう。さらに多量生産向きでない等の欠点を有
していた。Further, in order to reduce the effect of the impurity oxygen doping, a patent application filed by the present inventor, a semiconductor device manufacturing method, patent application 56-55608 (original display 53-1).
52887, filed on Dec. 10, 1978) is known. For example, when a PIN semiconductor device is to be manufactured, each P layer, I layer, and N layer is made into an independent reaction furnace, and the substrate is moved between the layers. This method can have the same measures as those of the present invention, and can obtain extremely preferable electric characteristics. However, in that case, the apparatus is three times as expensive as the one-chamber method, and the manufacturing cost is 2.5 to 3 times more expensive. Further, it has a defect that it is not suitable for mass production.
【0012】[0012]
【発明が解決しようとする課題】本発明はかかる反応炉
において、特に横型の反応炉において特に有効である。
また多量に基板上に半導体装置を作ろうとする時特に有
効であり、半導体装置ひとつあたりの装置の減価償却を
含めて、製造コストを縦型反応炉の1/100にできる
という大きな特徴を有している。The present invention is particularly effective in such a reactor, particularly in a horizontal reactor.
In addition, it is particularly effective when trying to make a large number of semiconductor devices on a substrate, and has a major feature that the manufacturing cost including depreciation of each semiconductor device can be reduced to 1/100 of that of a vertical reactor. ing.
【0013】[0013]
【課題を解決するための手段】本発明は、プラズマ気相
法により反応容器内に設けられた基板上に炭素膜を形成
するに際し、プラズマ化させた水素、酸素、弗素化合物
またはその混合物気体により前記反応容器の内壁または
基板ホルダに形成された炭素膜または炭素を主成分とす
る膜をプラズマクリ−ニングし、この後、前記反応容器
内に基板を配設し、プラズマ気相法により炭素または炭
素を主成分とする膜を形成することを特徴とする炭素膜
作製方法、を第1の発明とし、さらにプラズマ気相法に
より反応炉内に配設された基板上に炭素膜または炭素を
主成分とする膜を形成するに際し、前記炭素膜を形成す
る前に前記反応炉内壁または基板ホルダの表面に真性ま
たは実質的に真性の炭素膜を形成するとともに、この後
前記反応炉内に基板を配設して炭素または炭素を主成分
とする膜を形成することを特徴とする炭素膜作製方法、
を第2の発明とするものである。According to the present invention, when a carbon film is formed on a substrate provided in a reaction vessel by a plasma vapor phase method, hydrogen, oxygen, a fluorine compound or a mixture gas thereof made into plasma is used. Plasma cleaning a carbon film or a film containing carbon as a main component formed on the inner wall of the reaction container or the substrate holder, and thereafter, disposing the substrate in the reaction container, the carbon or A method for producing a carbon film, characterized in that a film containing carbon as a main component is formed, and the carbon film or the carbon is mainly formed on a substrate arranged in a reaction furnace by a plasma vapor phase method. When forming a film as a component, an intrinsic or substantially intrinsic carbon film is formed on the inner wall of the reaction furnace or the surface of the substrate holder before forming the carbon film, and thereafter, a base film is formed in the reaction furnace. Carbon film manufacturing method characterized by forming a film mainly containing carbon or carbon and arranged,
Is a second invention.
【0014】本発明はかかる多量生産用に横型に配置さ
れた反応炉または反応筒(10〜30cmφ、長さ1〜
5m)を用いる方法を中心として記す。かかる反応筒の
外側に一対の反応性気体をプラズマ化する電磁エネルギ
供給用の電極と該電極の外側にこの反応筒および電極を
囲んで加熱装置とを具備し、この反応炉内を炉方向に反
応性気体を流し、この気体の流れにそって基板を配置せ
しめたものである。According to the present invention, a reactor or a reaction cylinder (10 to 30 cmφ, length 1 to 1) arranged horizontally for such mass production is used.
The method using 5 m) will be mainly described. An electrode for supplying electromagnetic energy for converting a pair of reactive gases into plasma is provided outside the reaction tube, and a heating device is provided outside the electrode to surround the reaction tube and the electrode, and the inside of the reaction furnace is directed toward the furnace. A reactive gas is caused to flow, and the substrate is arranged along the flow of this gas.
【0015】さらにかかる装置内に一対の電極により発
生する電磁界に垂直または平行に基板を配置し、これを
複数段または複数列配置して2〜20cm平方の基板例
えば10cm平方の基板を20段20列計400枚の被
形成面上に一度に膜特に炭素、炭化珪素膜を形成せしめ
ることを中心として記す。Further, substrates are arranged in the apparatus in a direction perpendicular or parallel to the electromagnetic field generated by a pair of electrodes, and the substrates are arranged in a plurality of stages or a plurality of rows to form a substrate of 2 to 20 cm square, for example, 20 stages of 10 cm square substrate. The description will focus on forming a film, particularly a carbon or silicon carbide film, on one surface of 400 sheets of 20 columns in total.
【0016】本発明は炭素−珪素結合を有する水素化物
またはハロゲン化物(炭化珪化物気体)よりなる反応性
気体、アセチレン等の炭化水素を用いて被形成面上に非
単結晶の炭素、または炭素を主成分とする膜を0.05
〜1torrの反応圧力で100〜400℃の温度で形
成せしめるプラズマ気相法に関する。The present invention uses non-single-crystal carbon or carbon on the surface to be formed by using a reactive gas composed of a hydride or a halide (carbide silicide gas) having a carbon-silicon bond, or a hydrocarbon such as acetylene. A film whose main component is 0.05
The present invention relates to a plasma vapor phase method in which a reaction pressure of ˜1 torr and a temperature of 100 to 400 ° C. are formed.
【0017】本発明はさらにかかる反応性気体に3価の
不純物であるB、Al、Ga、Inを含む不純物気体例
えばジボラン(B2 H6 )、5価の不純物を含む不純物
気体例えばフォスヒン(PH3 )またはアルシン(As
H3 )を漸次添加して被形成面を有する基板上に密接し
てP型層、さらにI型層およびN型層をPINの順序に
て積層形成せしめ、これを繰り返し、安定して作製する
ことを目的としている。さらに本発明はプラズマ化する
電磁エネルギのパワ−により、アモルファス構造の半導
体(ASという)、5〜100Åの大きさの微結晶性を
有するセミアモルファス(半非晶質、以下SASとい
う)または5〜200Åの大きさのポリクリスタル(多
結晶、以下PCという)の構造を有する膜を作製せんと
するものである。さらにプラズマ反応に200〜500
Wという高いエネルギが必要な場合であっても、被形成
面上にはこのスピ−シスの実質的なプラズマエネルギを
得る距離を基板間の距離で制御したことを特徴とする。The present invention further provides that the reactive gas contains an impurity gas containing trivalent impurities such as B, Al, Ga and In, such as diborane (B 2 H 6 ), and an impurity gas containing pentavalent impurities such as Phoshin (PH). 3 ) or arsine (As
H 3 ) is gradually added to closely form a P-type layer, an I-type layer and an N-type layer in the order of PIN on a substrate having a surface to be formed, and these steps are repeated to stably produce the layer. Is intended. Further, according to the power of the electromagnetic energy to be turned into plasma, the present invention is a semiconductor having an amorphous structure (referred to as AS), a semi-amorphous (semi-amorphous, hereinafter referred to as SAS) having a crystallinity of 5 to 100Å, or 5 to It is intended to produce a film having a structure of a polycrystal (polycrystal, hereinafter referred to as PC) having a size of 200Å. 200 to 500 for plasma reaction
Even when a high energy of W is required, the distance for obtaining the substantial plasma energy of the spine on the formation surface is controlled by the distance between the substrates.
【0018】このため本発明においては、その出発物質
である反応性気体に炭素を主成分とした炭化珪素を作ろ
うとした場合、炭素−珪素結合を有する材料を用いた。
すなわち炭素−珪素結合を有する水素化物またはハロゲ
ン化物例えばテトラメチルシラン(Si(CH3 )4 )
(単にTMSという)、テトラエチルシラン(Si(C
2 H5 )4 )、Si(CH3 )xCl4-x(1≦x≦
3)、Si(CH3 )xH4-x(1≦x≦3)等の反応
性気体を用いて反応生成物中にSi−C結合を得やすく
している。Therefore, in the present invention, when an attempt is made to produce silicon carbide containing carbon as a main component in the reactive gas as the starting material, a material having a carbon-silicon bond is used.
That is, a hydride or a halide having a carbon-silicon bond, such as tetramethylsilane (Si (CH 3 ) 4 )
(Simply called TMS), tetraethylsilane (Si (C
2 H 5 ) 4 ), Si (CH 3 ) xCl 4- x (1 ≦ x ≦
3), Si (CH 3 ) xH 4 -x (1 ≦ x ≦ 3) and other reactive gases are used to facilitate obtaining Si—C bonds in the reaction product.
【0019】炭素を得ようとする時は、アセチレン(C
2 H2 )またはエチレン(C2 H4)を主として用い
た。こうすることにより、炭化珪素( SixC1-x)
(0≦x<0.5)または炭素(C)(これらを合わせ
るとSixC1-x(0≦x<0.5)と示すことができ
るため、以下炭化珪素という時はSixC1-x(0≦x
<0.5)を意味するものとする)を作製する。When trying to obtain carbon, acetylene (C
2 H 2 ) or ethylene (C 2 H 4 ) were mainly used. By doing so, silicon carbide (SixC 1- x)
(0 ≦ x <0.5) or carbon (C) (when these are combined, it can be shown as SixC 1− x (0 ≦ x <0.5). Therefore, hereinafter, when silicon carbide is referred to, SixC 1− x ( 0 ≦ x
<0.5) shall be produced).
【0020】さらにここに3価または5価の不純物を添
加して被形成面よりP型、I型(真性またはオ−トド−
ピング等を含む人為的に不純物を添加しない実質的に真
性)さらにN型の半導体または半絶縁体を作製した。Further, a trivalent or pentavalent impurity is added here to obtain P-type or I-type (intrinsic or auto-doped) from the surface to be formed.
Further, an N-type semiconductor or a semi-insulator was manufactured by substantially artificially adding impurities such as ping).
【0021】さらにかかる反応性気体を用いると、反応
炉を1気圧以下特に0.01〜10torr、代表的に
は0.3〜0.6torrの圧力下にて50W以下の電
磁エネルギにおいても、例えば0.01〜100MHz
特に500KHzまたは13.56MHzにおいて被膜
を形成することが可能である。即ち低エネルギプラズマ
CVD装置とすることができた。Further, when such a reactive gas is used, the electromagnetic energy of 50 W or less at a pressure of 1 atm or less, particularly 0.01 to 10 torr, typically 0.3 to 0.6 torr, is applied to the reactor, for example. 0.01-100MHz
In particular, it is possible to form a coating at 500 KHz or 13.56 MHz. That is, a low energy plasma CVD apparatus could be obtained.
【0022】さらに50〜500Wという高エネルギプ
ラズマ雰囲気とすると、形成された炭化珪素は微結晶化
し、その結果P型またはN型において、ホウ素またはリ
ンを0.1〜5%(ここでは(B2 H6 またはPH3 )
/(炭化物気体または炭化珪化物気体の比をパ−セント
で示す)添加した場合、低エネルギでは電気伝導度は1
0-9〜10-3(Ωcm)-1であったものが10-6〜10
+2(Ωcm)-1と約千倍にまで高めることができた。When a high energy plasma atmosphere of 50 to 500 W is further applied, the formed silicon carbide is crystallized, and as a result, 0.1 to 5% of boron or phosphorus is added in the P or N type (here, (B 2 H 6 or PH 3 )
In the case of the addition of / (the ratio of the carbide gas or the silicon carbide gas is expressed as a percentage), the electrical conductivity is 1 at low energy.
What was 0 -9 to 10 -3 (Ωcm) -1 was 10 -6 to 10
We were able to increase it to +2 (Ωcm) -1 , approximately 1000 times.
【0023】さらにこの高エネルギ法を用いて得られた
炭化珪素は5〜200Åの大きさの微結晶構造を有せし
めることができた。かかる構造において、そのPまたは
N型の不純物のアクセプタまたはドナ−となるイオン化
率は97〜100%を有し、添加した不純物のすべてを
活性化することができた。Furthermore, the silicon carbide obtained by using this high energy method was able to have a microcrystalline structure with a size of 5 to 200 Å. In such a structure, the ionization rate of the P or N type impurity as an acceptor or a donor was 97 to 100%, and all the added impurities could be activated.
【0024】〔実施例〕以下に図面に従って本発明の実
施例を説明する。図1は本発明を用いたプラズマCVD
装置の概要を示す。図1において被形成面を有する基板
(1)は角型の石英ホルダにて保持され、図面では7段
2列計14枚の構成をさせている。基板およびホルダは
反応炉の前方の別室(29)に入口(30)より予め配
置され、バルブ(32)ロ−タリ−ポンプ(33)によ
り真空引きがなされる。さらに開閉扉(34)を開け
て、反応炉内に自動送り装置により導入され、さらにミ
キサ−用混合板(35)も同時配置される。これらは反
応炉、別室ともに真空状態においてなされ、反応炉内に
酸素(空気)が少しでも混入しないように努めた。さら
に開閉扉(34)を閉じたことにより、図面の如く電極
(9)、(10)の間に基板が配置された。[Embodiment] An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows plasma CVD using the present invention.
An outline of the device is shown. In FIG. 1, a substrate (1) having a surface to be formed is held by a square quartz holder, and in the drawing, a total of 14 sheets of 7 rows and 2 columns is used. The substrate and the holder are placed in advance in a separate chamber (29) in front of the reactor through an inlet (30), and a vacuum is drawn by a valve (32) and a rotary pump (33). Further, the opening / closing door (34) is opened and introduced into the reaction furnace by an automatic feeder, and further, the mixer mixing plate (35) is also arranged at the same time. These were performed in a vacuum state in both the reaction furnace and the separate room, and efforts were made to prevent oxygen (air) from entering the reaction furnace at all. Further, by closing the opening / closing door (34), the substrate was placed between the electrodes (9) and (10) as shown in the drawing.
【0025】また図面は反応系を上方より眺めた構造を
示したものであり、基板(1)は互いに裏面を合わせて
垂直に配置させている。かくの如く重力を利用してフレ
イクを下部に除去することは、量産歩留まりを考慮する
時きわめて重要である。さらにこの基板(1)を折入さ
せた反応炉(25)には、この基板に垂直または平行
(特に平行にすると膜の均一性が得やすい)に電磁エネ
ルギの電界が図2(A)または(B)特に(B)の如く
に加わるように一対の電極(9)、(10)を上下また
は左右に配置して設けた。この電極の外側に電気炉
(5)が設けられており、基板(1)が100〜400
℃代表的には300℃に加熱されている。The drawing shows the structure of the reaction system viewed from above, and the substrates (1) are arranged vertically with their back surfaces aligned with each other. As described above, it is very important to remove the flakes to the lower part by utilizing gravity when considering the mass production yield. Further, in the reaction furnace (25) in which the substrate (1) is inserted, an electric field of electromagnetic energy is perpendicular to or parallel to the substrate (especially if it is parallel, it is easy to obtain film uniformity). (B) In particular, a pair of electrodes (9) and (10) are arranged vertically or horizontally so as to be added as shown in (B). An electric furnace (5) is provided outside this electrode, and the substrate (1) is 100 to 400.
C. Typically, it is heated to 300.degree.
【0026】反応性気体は水素またはヘリウムのキャリ
アガス例えばヘリウムを(13)より、3価の不純物で
あるジボランを(14)より、5価の不純物であるフォ
スヒンを(15)より、4価の添加物である珪化物気体
のシランを(16)より導入した。Reactive gases are hydrogen or helium carrier gas such as helium (13), trivalent impurity diborane (14), pentavalent impurity foshin (15), and tetravalent. Silica gas silane, which is an additive, was introduced from (16).
【0027】また炭素−珪素結合を有する反応性気体T
MS(20)を用いると、初期状態で液体であるためス
テンレス容器(21)に保存される。この容器は電子恒
温槽(22)により所定の温度に制御されている。Further, a reactive gas T having a carbon-silicon bond.
When MS (20) is used, it is stored in the stainless steel container (21) because it is a liquid in the initial state. This container is controlled at a predetermined temperature by an electronic thermostat (22).
【0028】このTMSは沸点が25℃であり、ロ−タ
リ−ポンプ(12)をバルブ(11)をへて排気させ、
反応炉内を0.01〜10torr特に0.02〜0.
4torrに保持させた。こうすることにより、1気圧
より低い圧力により結果として特に加熱しなくともTM
Sを気化させることができる。この気化したTMSを1
00%の濃度で流量計を介して反応炉に導入すること
は、従来の如く容器(21)をバブルして反応性気体を
放出するやり方に比較して、その流量制御が精度よく可
能であり、技術上重要である。実用上流量計が詰まった
場合、図面において(24)よりヘリウムを導入した。This TMS has a boiling point of 25 ° C., the rotary pump (12) is evacuated through the valve (11),
0.01 to 10 torr, especially 0.02 to 0.
It was kept at 4 torr. By doing this, the pressure lower than 1 atm results in no TM
S can be vaporized. This vaporized TMS is 1
Introducing into the reaction furnace at a concentration of 00% via a flow meter enables the flow rate to be controlled more accurately than in the conventional method in which the container (21) is bubbled to release the reactive gas. , Technically important. When the flow meter was clogged for practical use, helium was introduced from (24) in the drawing.
【0029】また反応筒(25)またはホルダ(2)の
内壁または表面に付着した反応生成物を除去する場合は
(17)より弗素化合物気体CF4 または酸素との混合
気体CF4 +O2 (2〜5%)を導入し、電磁エネルギ
を加えてフッ素ラジカル、酸素ラジカルを発生させて気
相エッチングをして除去した。When the reaction product attached to the inner wall or surface of the reaction tube (25) or the holder (2) is to be removed, the fluorine compound gas CF 4 or the mixed gas CF 4 + O 2 (2) with oxygen is obtained from (17). ˜5%) was introduced, and by applying electromagnetic energy, fluorine radicals and oxygen radicals were generated and removed by vapor phase etching.
【0030】さらにこのプラズマ放電においては、反応
性気体が混合室(8)をへて混合された後、励起室(2
6)において分解または反応をおこさしめ、反応生成物
を基板上に形成する空間反応を主として用いた。電磁エ
ネルギは電源(4)より直流または高周波を主として用
いた。Further, in this plasma discharge, after the reactive gas is mixed into the mixing chamber (8), the excitation chamber (2
In 6), a spatial reaction in which decomposition or reaction was caused and a reaction product was formed on the substrate was mainly used. As the electromagnetic energy, DC or high frequency was mainly used from the power source (4).
【0031】このようにして被形成面上に炭化珪素膜を
形成した。例えば基板温度300℃、高周波エネルギの
出力25W、シランまたはTMS 50cc/分、キャ
リアガスとしてのHe 250cc/分とした。(反応
性気体/He)5において160Å/分の膜成長速度を
得ることができた。In this way, a silicon carbide film was formed on the formation surface. For example, the substrate temperature was 300 ° C., the high-frequency energy output was 25 W, silane or TMS was 50 cc / min, and He as a carrier gas was 250 cc / min. With (reactive gas / He) 5, a film growth rate of 160Å / min could be obtained.
【0032】さらにこの膜形成には、PIN接合、PN
接合、PI、NI接合、PINPIN接合等をその必要
な厚さに必要な反応生成物を基板上に漸次積層して形成
させた。Further, for this film formation, a PIN junction, a PN
Bonding, PI, NI bonding, PINPIN bonding, etc. were formed by gradually laminating reaction products required to have the required thickness on the substrate.
【0033】このようにして被形成面上に膜を形成させ
てしまった後、反応性気体を反応筒より十分にパ−ジし
た後、開閉扉(34)を開け、ミキサ用混合板(3
5)、ジグ(3)上の基板を別室(29)に自動引き出
し管により反応筒および別室をともに真空(0.01t
orr以下)にして移動させた。さらに開閉扉(34)
を閉じた後、別室に(31)よりバルブを開けて空気を
充填し大気圧とした後、外部にジグおよび膜の形成され
た基板を取り出した。After the film has been formed on the surface to be formed in this manner, the reactive gas is sufficiently purged from the reaction tube, and then the opening / closing door (34) is opened and the mixer mixing plate (3).
5), the substrate on the jig (3) is evacuated (0.01 t) to the separate chamber (29) by an automatic drawing tube for both the reaction cylinder and the separate chamber.
or or below) and moved. Further open / close door (34)
After closing (1), the valve was opened from (31) in another room to fill it with air to bring it to atmospheric pressure, and then the substrate on which the jig and the film were formed was taken out.
【0034】以上の実施例より明らかな如く、本発明は
反応性気体をミキサ(8)にて混合した後、排気口
(6)に層状(ミクロにはプラズマ化された状態ではラ
ンダム運動をしていた)に流し、この流れに平行に基板
を配置して被形成面上にその膜厚が±5%以内のバラツ
キで0.1〜3μの厚さに膜を形成せしめたことを特徴
としている。As is clear from the above examples, according to the present invention, after the reactive gas is mixed in the mixer (8), the exhaust gas (6) is randomly moved in a layered state (microscopically in a plasmaized state). The film was formed on the surface to be formed to a thickness of 0.1 to 3 μ with a variation of ± 5% or less on the surface to be formed. There is.
【0035】図2は図1の図面における排気口(6)方
向よりみた基板(1)の配置と電極(9)、(10)と
の関係を示す。図面において(A)は基板を水平、電極
(9)、(10)による電磁界を水平方向に配置したも
ので、この場合一度に導入できる基板の枚数を増やすこ
とができる。FIG. 2 shows the relationship between the arrangement of the substrate (1) and the electrodes (9) and (10) as seen from the direction of the exhaust port (6) in the drawing of FIG. In the drawing, (A) shows the substrates arranged horizontally and the electromagnetic fields of the electrodes (9) and (10) arranged horizontally. In this case, the number of substrates that can be introduced at one time can be increased.
【0036】図2(B)は電極(9)、(10)による
電磁界、基板(1)ともに垂直にしたもので、基板の配
置数が(A)の2倍になる。図3は本発明の半導体装置
作製方法の操作手順チャ−トを示したものである。In FIG. 2B, the electromagnetic fields by the electrodes (9) and (10) and the substrate (1) are vertically arranged, and the number of substrates arranged is twice that of (A). FIG. 3 shows an operation procedure chart of the semiconductor device manufacturing method of the present invention.
【0037】図面において“0”である(49)は反応
炉の真空引きによる0.01torr以下の保持を示
す。さらに“1”の(40)は本発明による反応炉また
は反応筒およびホルダに炭素または炭化珪素のコ−ティ
ングを示す。In the drawing, "49", which is "0", indicates the retention of 0.01 torr or less by evacuation of the reaction furnace. Further, the "1" (40) indicates the coating of carbon or silicon carbide on the reactor or reactor and the holder according to the present invention.
【0038】このコ−ティングはその詳細を示すと図3
(B)、(C)である。図3(B)は真空引き(49)
により0.01torr以下にし、10〜30分保持し
た後、水素を電磁エネルギにより0〜30分、30〜5
0Wの出力によりプラズマクリ−ニングを行い、吸着、
水分、酸素を除去した。さらにその水素を除去した後、
(51)によりヘリウムを同時に30〜50Wの出力に
より10〜30分プラズマ化し、さらに表面の水素を除
去した。この水素プラズマ発生(50)に対しては、水
素中に1〜5%の濃度でHClまたはClを添加して行
うと、塩素ラジカルが同時に発生し、このラジカルが石
英等ホルダの内側に存在しているナトリウムの如きアル
カリ金属を吸いだす効果を有する。このためバックグラ
ウンドレベルでのナトリウム、水分、酸素の濃度を形成
された膜中にて1014cm-3以下にすることができ、き
わめて重要な前処理工程であった。The details of this coating are shown in FIG.
(B) and (C). FIG. 3 (B) shows vacuum evacuation (49)
To 0.01 torr or less and hold for 10 to 30 minutes, and then hydrogen for 0 to 30 minutes, 30 to 5 by electromagnetic energy.
Plasma cleaning by the output of 0 W, adsorption,
Water and oxygen were removed. After further removing the hydrogen,
By (51), helium was simultaneously turned into plasma by the output of 30 to 50 W for 10 to 30 minutes to further remove hydrogen on the surface. The hydrogen plasma generation (50) is performed by adding HCl or Cl at a concentration of 1 to 5% in hydrogen, chlorine radicals are simultaneously generated, and the radicals exist inside the holder such as quartz. It has the effect of sucking out alkali metals such as sodium. Therefore, the concentration of sodium, water, and oxygen at the background level can be reduced to 10 14 cm -3 or less in the formed film, which was a very important pretreatment step.
【0039】この塩素を添加した場合、さらにこの壁面
に残留吸着した塩素を除去するため(51)の不活性気
体によるスパッタリングによる除去も有効であった。か
かる石英等の反応容器は内壁を十分プラズマクリ−ニン
グすることによりこの容器内壁に不純物のプラズマで放
出しやすい状態をおさえる膜を十分密着させることがで
きる。かくすると、この膜を数十μの厚さまで形成して
も残留応力等により壁面からこの保護膜が剥がれフレ−
ク(粉)となり被膜中に注入することを防ぐことができ
る。When this chlorine was added, it was also effective to remove chlorine adsorbed on the wall surface by sputtering with an inert gas (51). By sufficiently plasma-cleaning the inner wall of such a reaction container such as quartz, a film which can easily release the impurity plasma by plasma can be closely adhered to the inner wall of the container. Thus, even if this film is formed to a thickness of several tens of μm, the protective film is peeled off from the wall surface due to residual stress or the like.
It can be prevented from becoming a powder (powder) and injecting into the coating.
【0040】この後これらの系を真空引きした後、炭化
物気体であるエチレンまたは炭化珪素化物であるTMS
を導入し、プラズマエネルギにより分解して、0.1〜
2μ代表的には0.2〜0.5μの厚さに形成させた。
これらの膜形成をさせる際、高い電磁エネルギが加わる
領域即ち不純物が再放出されやすい領域に特に厚くつき
やすく、二重に好ましい結果をもたらした。Then, after vacuuming these systems, ethylene which is a carbide gas or TMS which is a silicon carbide.
Is introduced and decomposed by plasma energy,
The thickness of 2 μm is typically 0.2 to 0.5 μm.
When these films are formed, the region where high electromagnetic energy is applied, that is, the region where impurities are likely to be re-emitted, is particularly thick and easy to stick, which gives doubly preferable results.
【0041】かかる本発明の複雑な前処理工程を行わな
い場合であっても、図3(C)に示す如く真空引きの
後、炭素または炭化珪素を(52)において同様に0.
1〜2μ形成し、反応炉壁からの酸素、アルカリ金属の
再放出を防ぐことが有効であった。Even when the complicated pretreatment step of the present invention is not carried out, after vacuuming as shown in FIG.
It was effective to form 1-2 μm and prevent the re-release of oxygen and alkali metal from the reactor wall.
【0042】また図3(A)においては、半導体装置の
作製のため、基板のコ−ティング、系の真空引き(4
1)さらにPまたはN型半導体の作製(42)、I型半
導体層の作製(43)、N型層の作製(44)を行い、
第1の装置を作製(48)した。この装置は前記したP
I、NI、PIN、PN等の接合を少なくとも1つ有す
るディバイス設計仕様によって作られなければならない
ことはいうまでもない。Further, in FIG. 3A, in order to manufacture a semiconductor device, substrate coating and system vacuuming (4
1) Further, a P or N type semiconductor is produced (42), an I type semiconductor layer is produced (43), and an N type layer is produced (44),
A first device was made (48). This device is P
It goes without saying that it must be made according to a device design specification having at least one junction such as I, NI, PIN, PN.
【0043】さらにこの後、この系に対し、反応炉のみ
またはこの反応炉とホルダとを挿入設置された反応系に
対し(46)に示すI型半導体層または(42)に示す
層と同じ層のコ−ティングにより前の装置作製の際用い
られた工程(44)の履歴が次のランに対して影響を与
えないようにした。その詳細は図3(B)、(C)、
(D)、(E)に示す。After this, the same layer as the I-type semiconductor layer shown in (46) or the layer shown in (42) for the reaction system in which only the reaction furnace or the reaction furnace and the holder are inserted and installed in this system. The coating was used to prevent the history of the step (44) used in manufacturing the previous device from affecting the next run. The details are shown in FIGS.
Shown in (D) and (E).
【0044】即ち図3(B)は前記した前処理と同じく
真空引き(49)水素プラズマ放電(50)、ヘリウム
プラズマ処理(51)、半導体装置のランの最初の工程
の半導体層を形成する工程(52)を有する。しかしこ
の(50)(51)がすでに(A)での(46)で行わ
れているため、一般には(C)の(52)での0.1〜
2μの厚さの半導体層の作製で十分であった。That is, FIG. 3 (B) shows a process of forming a semiconductor layer in the first step of vacuuming (49), hydrogen plasma discharge (50), helium plasma treatment (51), and the first run of the semiconductor device, as in the above-mentioned pretreatment. It has (52). However, since (50) and (51) have already been performed in (46) of (A), 0.1 to (52) of (C) is generally used.
It was sufficient to produce a semiconductor layer with a thickness of 2μ.
【0045】またこの前の装置の作製(40)すなわち
前のランでの履歴をなくすため、(D)、(E)に示す
プラズマエッチング工程を行ってもよい。すなわち図3
(B)は真空引き(49)CF4 またはCF4 +O(約
5%)を図1での(17)より導入し、20分〜1時間
プラズマエッチング(53)を行った。さらに真空引き
をしてその後C、Fの残留物を除去するため水素プラズ
マ処理(50)を10〜30分、さらにこのI層に0.
05〜0.5μのI型または次の工程の最初のランの半
導体層(42)と同様の導電型、成分の半導体層の作製
を行った。この方法が最も徹底して再現性を保証するこ
とができた。The plasma etching step shown in (D) and (E) may be carried out in order to eliminate the history of the previous production of the apparatus (40), that is, the previous run. That is, FIG.
In (B), vacuum evacuation (49) CF 4 or CF 4 + O (about 5%) was introduced from (17) in FIG. 1, and plasma etching (53) was performed for 20 minutes to 1 hour. Further evacuation is performed, and then hydrogen plasma treatment (50) is performed for 10 to 30 minutes to remove the C and F residues.
A semiconductor layer having a conductivity type and components similar to those of the semiconductor layer (42) of I-type of 0.5 to 0.5 μm or the first run of the next step was manufactured. This method was the most thorough and guaranteed reproducibility.
【0046】簡単な方法としては(E)に示す(49)
の真空引き、プラズマエッチング(53)残部吸着ガス
の除去(50)の工程を行った。A simple method is shown in (E) (49).
The steps of evacuation and plasma etching (53) and removal of residual adsorption gas (50) were performed.
【0047】かくすることにより第1の半導体装置の作
製(48)の最後工程(44)と次の工程(48)の最
初の工程(42)との間でPまたはN型の不純物が互い
に(42)にて混入する可能性を除去することができ
た。As a result, P or N type impurities are separated from each other between the last step (44) of the fabrication (48) of the first semiconductor device and the first step (42) of the next step (48). It was possible to eliminate the possibility of contamination in 42).
【0048】かかる本発明の方法によりその効果を評価
した結果を図4に示す。図4は本発明方法を用いて作ら
れた光電変換装置の結果である。この場合基板として金
属例えばステンレス基板または透光性基板であるガラス
上にITOを500〜2000Å、さらにこの上に酸化
スズまたは酸化アンチモンを100〜500Åの厚さに
形成させた多重膜の電極を有する基板を用いた。この上
にP型炭素を主成分とする炭化珪素(SixC1-X 0
≦X<1)(例えばX=0.3〜0.5)を100〜3
00Åの厚さにまたこの上面に真性または実質的に真性
のASまたはSASの珪素を0.4〜0.7μの厚さ
に、さらにこの上面にN型炭素を主成分とする炭化珪素
(SixC1-X 0≦X<1)(例えばX=0.3〜
0.5)を100〜300Åの厚さに形成させたPIN
構造を有せしめた。このP、I、N型半導体の仕様は図
3(A)のチャ−トにおける(42)、(43)、(4
4)、(42)・・・・に対応させた。FIG. 4 shows the result of evaluation of the effect by the method of the present invention. FIG. 4 shows the result of a photoelectric conversion device manufactured using the method of the present invention. In this case, as a substrate, ITO having a thickness of 500 to 2000 Å on a metal such as a stainless steel substrate or a glass which is a translucent substrate, and a multi-layer electrode having tin oxide or antimony oxide formed thereon to a thickness of 100 to 500 Å are provided. A substrate was used. On top of this, silicon carbide (SixC 1-X 0
≦ X <1) (for example, X = 0.3 to 0.5) is 100 to 3
To a thickness of 00Å and to the upper surface thereof an intrinsic or substantially intrinsic silicon of AS or SAS to a thickness of 0.4 to 0.7 μm, and on this upper surface, a silicon carbide (SixC) containing N-type carbon as a main component. 1−X 0 ≦ X <1 (for example, X = 0.3 to
0.5) PIN with a thickness of 100-300Å
It has a structure. The specifications of the P, I, and N type semiconductors are (42), (43), and (4) in the chart of FIG.
4), (42) ...
【0049】さらにこの後この工程にITOを600〜
800Åの厚さにまたはアルミニウム金属膜を真空蒸着
法で形成して光電変換装置を作った。その変換効率を図
4(A)に示す。Further, after that, 600 to ITO is added in this step.
A photoelectric conversion device was made to a thickness of 800 Å or an aluminum metal film was formed by vacuum deposition. The conversion efficiency is shown in FIG.
【0050】1cm2 のセルの大きさでAM1(100
mW/cm2 )の条件にて前処理(40)をいれない場
合(71)の3%が、また前処理を行うと(70)の値
が得られた。さらに中間の(46)の工程を加えること
によるラン(製造日毎)の効率の変化(60)になりま
ったく加えないと(61)が得られた。With a cell size of 1 cm 2 , AM1 (100
Under the condition of mW / cm 2 ), 3% of the case (71) without the pretreatment (40) and the value (70) with the pretreatment were obtained. Furthermore, the change in the efficiency of the run (every production date) due to the addition of the intermediate step (46) (60) resulted in (61) without any addition.
【0051】(60)はその効率が11〜9%を得るこ
とができるのに対し、本発明方法を用いない場合1〜4
%しかなかった。The efficiency of (60) can be 11 to 9%, while the efficiency of (60) is 1 to 4 when the method of the present invention is not used.
There was only%.
【0052】さらにこのセル面積を100cm2 にする
と、本発明方法を用いると7〜9%の効率を得ることが
できるのに際し、本発明方法を用いないと0〜3%であ
った。特にダイオ−ド特性がないものが30%以上を有
し、製造不可能であった。Further, when the cell area was set to 100 cm 2 , the efficiency of 7 to 9% could be obtained using the method of the present invention, while it was 0 to 3% without the method of the present invention. In particular, those having no diode characteristics had 30% or more and could not be manufactured.
【0053】図4(B)は特に表面程にてP型の半導体
を作る工程でI型の珪素半導体を作った場合の電気伝導
度の値を示す。FIG. 4B shows the electric conductivity value when an I-type silicon semiconductor is formed in the process of forming a P-type semiconductor particularly near the surface.
【0054】前工程でP型半導体を作り、本発明方法の
中間処理法の前処理を行わない時、AM1の光照射によ
る電気伝導度が(65)である。暗伝導度(64)と逆
の場合もみられ、またその値も10-6〜10-4で大きな
バラツキがあった。他方本発明の前処理をおこなわた場
合、光伝導度(70)、暗伝導度(70’)が得られ
た。また中間処理を行った時は光伝導度(62)、暗伝
導度(63)が得られた。これらは本発明におけるド−
ピング効果防止がいかに重要であるかを明確に示したも
のである。When a P-type semiconductor is produced in the previous step and the pretreatment of the intermediate treatment method of the method of the present invention is not carried out, the electrical conductivity by light irradiation of AM1 is (65). The case opposite to the dark conductivity (64) was also observed, and the value was 10 −6 to 10 −4 , which was a large variation. On the other hand, when the pretreatment of the present invention was performed, photoconductivity (70) and dark conductivity (70 ') were obtained. Further, when the intermediate treatment was performed, photoconductivity (62) and dark conductivity (63) were obtained. These are the
It clearly shows how important it is to prevent the ping effect.
【0055】以上の説明より明らかな如く、本発明は同
一反応筒を用いて光電変換装置または発光素子のみなら
ず、電界効果半導体装置、フォトセンサアレ−等の各種
の半導体装置を作製する上にきわめて重要な製造装置お
よび製造方法を提供したものであり、これにより従来縦
型のプラズマCVD装置にて10cm平方を4枚作ると
同じ時間で、100〜500枚の基板上に非単結晶半導
体膜を作ることができ、きわめて多量生産向きである。
さらに本発明の如き電極構造または基板の配置をするこ
とにより、PIN構造を有する光電変換装置において1
0%以上の変換効率を繰り返し安定して得ることがで
き、その膜質においてもきわめて優れたものであった。As is apparent from the above description, the present invention is applicable to the production of not only photoelectric conversion devices or light emitting elements but also various semiconductor devices such as field effect semiconductor devices and photosensor arrays using the same reaction tube. The present invention provides an extremely important manufacturing apparatus and manufacturing method, which allows a non-single crystal semiconductor film to be formed on 100 to 500 substrates in the same time as when four 10 cm squares are formed by a conventional vertical plasma CVD apparatus. Can be made and is very suitable for mass production.
Further, by arranging the electrode structure or the substrate as in the present invention, the photoelectric conversion device having the PIN structure is
A conversion efficiency of 0% or more could be repeatedly and stably obtained, and the film quality was extremely excellent.
【0056】本発明においては炭化珪素(SixC1-X
0≦X<0.5)を中心として記した。本発明は図1
に示す横型のプラズマCVD装置を中心として示した。
しかしその電極の作り方を誘電型としたり、またア−ク
放電を利用するプラズマCVD装置であっても本発明は
有効である。また縦型、縦横型のベルジャ−型のプラズ
マCVD装置であっても同様に本発明方法を適用するこ
とができる。In the present invention, silicon carbide (SixC 1-X
The description is centered on 0 ≦ X <0.5). The present invention is shown in FIG.
The horizontal plasma CVD apparatus shown in FIG.
However, the present invention is effective even if the electrode is made in a dielectric type or a plasma CVD apparatus utilizing arc discharge. Further, the method of the present invention can be similarly applied to a vertical or horizontal bell jar type plasma CVD apparatus.
【0057】[0057]
【効果】本発明の構成をとることにより、不要な不純物
の混入を防ぐ作用をゆうせしめる炭素膜を効率よく得る
ことができた。[Effect] By adopting the constitution of the present invention, it is possible to efficiently obtain a carbon film having a function of preventing the mixing of unnecessary impurities.
【図1】 実施例において用いたプラズマ気相装置であ
る。FIG. 1 is a plasma vapor phase apparatus used in Examples.
【図2】 図1の一部を示す。FIG. 2 shows a part of FIG.
【図3】 図1の装置を用い、本発明方法のプラズマ気
相法を用いるチャ−トである。3 is a chart using the apparatus of FIG. 1 and using the plasma vapor phase method of the method of the present invention.
【図4】 図3のチャ−トに従って得られた光電変換装
置の効率および本発明方法のド−ピング防止効果を示す
他の資料である。4 is another material showing the efficiency of the photoelectric conversion device obtained according to the chart of FIG. 3 and the anti-doping effect of the method of the present invention.
Claims (2)
れた基板上に炭素膜を形成するに際し、プラズマ化させ
た水素、酸素、弗素化合物またはその混合物気体により
前記反応容器の内壁または基板ホルダに形成された炭素
膜または炭素を主成分とする膜をプラズマクリ−ニング
し、この後、前記反応容器内に基板を配設し、プラズマ
気相法により炭素または炭素を主成分とする膜を形成す
ることを特徴とする炭素膜作製方法。1. When forming a carbon film on a substrate provided in a reaction vessel by a plasma vapor phase method, an inner wall of the reaction vessel or a substrate holder is formed by plasmatizing hydrogen, oxygen, a fluorine compound or a mixture gas thereof. Plasma cleaning the carbon film or the film containing carbon as the main component formed in the above step, and thereafter disposing the substrate in the reaction vessel, and depositing the carbon or the film containing carbon as the main component by the plasma vapor phase method. A method for producing a carbon film, which comprises forming the carbon film.
た基板上に炭素膜または炭素を主成分とする膜を形成す
るに際し、前記炭素膜を形成する前に前記反応炉内壁ま
たは基板ホルダの表面に真性または実質的に真性の炭素
膜を形成するとともに、この後前記反応炉内に基板を配
設して炭素または炭素を主成分とする膜を形成すること
を特徴とする炭素膜作製方法。2. When forming a carbon film or a film containing carbon as a main component on a substrate arranged in a reaction furnace by a plasma vapor phase method, the inner wall of the reaction furnace or the substrate is formed before forming the carbon film. A carbon film characterized in that an intrinsic or substantially intrinsic carbon film is formed on the surface of the holder, and thereafter a substrate is placed in the reaction furnace to form carbon or a film containing carbon as a main component. Manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4269270A JPH0732141B2 (en) | 1992-09-11 | 1992-09-11 | Carbon film production method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4269270A JPH0732141B2 (en) | 1992-09-11 | 1992-09-11 | Carbon film production method |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8159121A Division JP2805611B2 (en) | 1996-05-31 | 1996-05-31 | Coating method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0620975A true JPH0620975A (en) | 1994-01-28 |
| JPH0732141B2 JPH0732141B2 (en) | 1995-04-10 |
Family
ID=17470018
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4269270A Expired - Lifetime JPH0732141B2 (en) | 1992-09-11 | 1992-09-11 | Carbon film production method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0732141B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6267075B1 (en) * | 1998-07-09 | 2001-07-31 | Yield Engineering Systems, Inc. | Apparatus for cleaning items using gas plasma |
| WO2008035678A1 (en) * | 2006-09-19 | 2008-03-27 | Tokyo Electron Limited | Plasma cleaning process and plasma cvd method |
| WO2024166678A1 (en) * | 2023-02-07 | 2024-08-15 | 東京エレクトロン株式会社 | Film forming method and substrate processing apparatus |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5329065A (en) * | 1976-08-31 | 1978-03-17 | Toshiba Corp | Vapour phase reaction unit of semiconductor |
| JPS5892218A (en) * | 1981-11-28 | 1983-06-01 | Semiconductor Energy Lab Co Ltd | Manufacture of semiconductor device |
| JPS63267430A (en) * | 1987-04-27 | 1988-11-04 | Toshiba Corp | Cleaning method for inside of reaction chamber |
| JPH02119126A (en) * | 1989-08-25 | 1990-05-07 | Semiconductor Energy Lab Co Ltd | Manufacture of semiconductor device |
| JPH056877A (en) * | 1991-06-14 | 1993-01-14 | Semiconductor Energy Lab Co Ltd | Etching method of carbon film |
-
1992
- 1992-09-11 JP JP4269270A patent/JPH0732141B2/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5329065A (en) * | 1976-08-31 | 1978-03-17 | Toshiba Corp | Vapour phase reaction unit of semiconductor |
| JPS5892218A (en) * | 1981-11-28 | 1983-06-01 | Semiconductor Energy Lab Co Ltd | Manufacture of semiconductor device |
| JPS63267430A (en) * | 1987-04-27 | 1988-11-04 | Toshiba Corp | Cleaning method for inside of reaction chamber |
| JPH02119126A (en) * | 1989-08-25 | 1990-05-07 | Semiconductor Energy Lab Co Ltd | Manufacture of semiconductor device |
| JPH056877A (en) * | 1991-06-14 | 1993-01-14 | Semiconductor Energy Lab Co Ltd | Etching method of carbon film |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6267075B1 (en) * | 1998-07-09 | 2001-07-31 | Yield Engineering Systems, Inc. | Apparatus for cleaning items using gas plasma |
| WO2008035678A1 (en) * | 2006-09-19 | 2008-03-27 | Tokyo Electron Limited | Plasma cleaning process and plasma cvd method |
| US8366953B2 (en) | 2006-09-19 | 2013-02-05 | Tokyo Electron Limited | Plasma cleaning method and plasma CVD method |
| JP5241499B2 (en) * | 2006-09-19 | 2013-07-17 | 東京エレクトロン株式会社 | Plasma cleaning method, plasma CVD method, and plasma processing apparatus |
| WO2024166678A1 (en) * | 2023-02-07 | 2024-08-15 | 東京エレクトロン株式会社 | Film forming method and substrate processing apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0732141B2 (en) | 1995-04-10 |
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