JP3584091B2 - Copper source material for CVD and film forming method using the same - Google Patents
Copper source material for CVD and film forming method using the same Download PDFInfo
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- JP3584091B2 JP3584091B2 JP22608595A JP22608595A JP3584091B2 JP 3584091 B2 JP3584091 B2 JP 3584091B2 JP 22608595 A JP22608595 A JP 22608595A JP 22608595 A JP22608595 A JP 22608595A JP 3584091 B2 JP3584091 B2 JP 3584091B2
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- 239000010949 copper Substances 0.000 title claims description 55
- 229910052802 copper Inorganic materials 0.000 title claims description 54
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims description 53
- 239000000463 material Substances 0.000 title claims description 27
- 238000000034 method Methods 0.000 title claims description 8
- 238000005229 chemical vapour deposition Methods 0.000 claims description 25
- 150000004699 copper complex Chemical class 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 13
- 230000008018 melting Effects 0.000 claims description 12
- 238000002844 melting Methods 0.000 claims description 12
- 239000003446 ligand Substances 0.000 claims description 8
- GPOXCFJNNXDRSC-UHFFFAOYSA-N 6-ethyl-2,2-dimethyloctane-3,5-dione Chemical compound CCC(CC)C(=O)CC(=O)C(C)(C)C GPOXCFJNNXDRSC-UHFFFAOYSA-N 0.000 claims description 7
- 239000000758 substrate Substances 0.000 claims description 7
- 238000000151 deposition Methods 0.000 claims description 5
- 239000007791 liquid phase Substances 0.000 claims description 2
- 239000002994 raw material Substances 0.000 description 23
- 239000010408 film Substances 0.000 description 15
- 150000001875 compounds Chemical class 0.000 description 14
- 239000010409 thin film Substances 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 238000011068 loading method Methods 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 125000002524 organometallic group Chemical group 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 3
- 239000005751 Copper oxide Substances 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000012159 carrier gas Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229910000431 copper oxide Inorganic materials 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000010453 quartz Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000000859 sublimation Methods 0.000 description 3
- 230000008022 sublimation Effects 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- QAMFBRUWYYMMGJ-UHFFFAOYSA-N hexafluoroacetylacetone Chemical compound FC(F)(F)C(=O)CC(=O)C(F)(F)F QAMFBRUWYYMMGJ-UHFFFAOYSA-N 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 238000002230 thermal chemical vapour deposition Methods 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- YRAJNWYBUCUFBD-UHFFFAOYSA-N 2,2,6,6-tetramethylheptane-3,5-dione Chemical compound CC(C)(C)C(=O)CC(=O)C(C)(C)C YRAJNWYBUCUFBD-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- -1 copper carboxylate Chemical class 0.000 description 1
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical compound [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 description 1
- NWFNSTOSIVLCJA-UHFFFAOYSA-L copper;diacetate;hydrate Chemical compound O.[Cu+2].CC([O-])=O.CC([O-])=O NWFNSTOSIVLCJA-UHFFFAOYSA-L 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 125000005594 diketone group Chemical group 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000005268 plasma chemical vapour deposition Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Crystals, And After-Treatments Of Crystals (AREA)
- Chemical Vapour Deposition (AREA)
- Electrodes Of Semiconductors (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は,化学的気相蒸着法(CVD法)によって銅または銅含有物質を析出させるのに適したCVD用銅源物質に関する。
【0002】
【従来の技術】
【0003】
超電導材料やLSI配線材料などに有用な薄膜として,銅または銅含有物質の薄膜をCVD法で成膜することが種々提案されている。銅または銅含有物質をCVD法によって析出させる場合の原料化合物として有機銅錯体を用いることが有利である。
【0004】
従来より,或る金属またはその化合物をCVD法で成膜するさいの原料化合物としてその金属の有機錯体が使用されており,かような有機金属錯体を構成する有機部分(配位子)としては,ジピバロイルメタン或いはヘキサフルオロアセチルアセトン等のβ−ジケトンが一般に知られている。特開平4−72066号公報および特開平4−74866号公報には周期律表第IIA属金属, IIIA属金属,IVA属金属,IB属金属との錯体を構成する有機化合物として炭素数1〜5の低級アルキル基をもつ1,3ジケトン類が記載されている。
【0005】
なお,CVD法には,熱CVD法,光CVD法またはプラズマCVD法などが知られており,いずれも原料化合物の蒸気を分解させて薄膜を形成するものであるが,原料化合物の蒸気を発生させる場合には,固体状態にある原料化合物からその蒸気を昇華させるのが一般的である。
【0006】
【発明が解決しようとする課題】
従来提案されたβ−ジケトン系有機化合物を配位子とした有機銅錯体は,一般にその融点が高い(ほぼ200℃前後)。このため,CVD法の原料化合物に適用する場合,これを融点以上の高温に加熱することはせずに,固体状態からの昇華によって原料蒸気を発生させることが行われている。
【0007】
固体状態からの昇華の場合には,原料容器内の原料残量が減少するに従って,原料化合物の表面積が減少して気化速度が遅くなるという現象が起き,この蒸気量の減少により,一定した成膜速度を長時間確保することができないという問題がある。また,この気化速度が変化することにより,銅と他の元素とが複合した物質の薄膜(例えばYBa2Cu3O7 など) を作製しようとする場合には, その組成の制御が困難になるという問題もある。
【0008】
前記の特開平4−72066号公報および特開平4−74866号公報に記載された有機金属錯体も高昇華性である点を特徴とするものであり,CVD用原料化合物としては固体状態で蒸発させるものである。したがって,前記同様の問題がある。
【0009】
また,ヘキサフルオロアセチルアセトン等のように分子内にフッ素を含む配位子を用いた有機金属錯体は,融点は低いが成膜した膜中に不純物としてフッ化物が混在するおそれがあり,この場合には膜の特性を著しく損なう結果となる。
【0010】
したがって本発明は,前記のような問題を解決できるような低融点のCVD用銅源物質を得ることを課題としたものである。
【0011】
【課題を解決するための手段】
本発明者らは斯かる課題を解決するために鋭意研究したところ,6−エチル−2,2−ジメチル−3,5−オクタンジオンのβ−ジケトンを配位子とした有機銅錯体は,CVD用原料化合物として液体状態で使用可能な低融点(ほぼ69〜70℃)を有し且つ蒸発温度と分解温度がはっきり離れているというCVD法の成膜にとって極めて有利な性質を有することを見いだした。この特性により,これをCVD法の銅源物質とした場合,液体状態からの蒸発を行わせることができ,また銅の原料蒸気の基材への供給と基材上での銅の分解析出を安定して行わせることができるので,既述の課題が解決できることがわかった。
【0012】
すなわち,本発明によれば,CVD法により銅または銅含有物質を析出させるのに使用するCVD用銅源物質であって,6−エチル−2,2−ジメチル−3,5−オクタンジオンを銅の配位子とした有機銅錯体からなるCVD用同源物質を提供する。
【0013】
また本発明によれば,CVD法により銅または銅含有物質を基材上に析出させるさいに,銅源物質として6−エチル−2,2−ジメチル−3,5−オクタンジオンを銅の配位子とした有機銅錯体を使用し,この有機銅錯体を融点以上の温度に加熱し,当該錯体の液相から当該錯体を蒸発させることを特徴とするCVD法による銅または銅含有物質の成膜法を提供する。
【0014】
本発明に従う有機銅錯体は化1の一般式で表されるものであり,新規化合物であると思われる。
【0015】
【化1】
【0016】
【発明の実施の形態】
本発明に従うβ−ジケトン系有機銅錯体は,銅カルボン酸塩(例えば酢酸銅など)と,配位子の6−エチル−2,2−ジメチル−3,5−オクタンジオンを,水−エタノール溶液中で攪拌し,生じた沈澱を濾過で分取し,これを再結晶,蒸留等の精製法で精製するという方法で得ることができる。
【0017】
このようにして得られた本発明の有機銅錯体をCVD法の原料化合物として使用し,CVD法で該銅または銅含有物質を成膜するには,例えば図1に示したように,該有機銅錯体1を入れた原料容器2を恒温槽3内で所定の温度(融点より高い温度例えば80〜100℃)に保持し,不活性キャリアガス(例えばアルゴンガス)4を流量計5によって流量を調整しながら(例えば5〜500ミリリットル/分)原料容器2内に導入することよって,有機銅錯体を同伴したガス流を該容器2から発生させる。
【0018】
発生した有機銅錯体蒸気は熱分解炉6の反応管7内に導かれる。反応管(例えば石英管)7はヒータ8によって加熱され,管内に設置した基板9を所定の温度(例えば400〜800℃)に加熱保持することによって,該有機銅錯体が熱分解して基板9上に銅が析出し,成膜する。なお,原料容器2から熱分解炉6までの配管は,凝縮を防ぐために保温層10または加熱保温手段によって原料容器の加熱温度より5〜20℃高い温度に保温維持するのがよい。反応管7から出る排ガスは冷却トラップ11を経て排出される。図中の12はバルブを,また13はロータリーポンプを示している。なお,銅の酸化物を成膜するさいには,酸素容器14から流量計15およびバルブ16を経て反応雰囲気中(例えば反応間7内)に適量の気体酸素を送気する。また,他の元素との複合物質を成膜するには,図示されてはいないが,当該他の物質の原料化合物を同時に反応間7内に導くようにする。
【0019】
【実施例】
〔実施例1〕
図1のCVD設備を用いて,ステンレス鋼製の原料容器2内に,銅源としての原料化合物として化1に示したビス(6−エチル−2,2−ジメチル−3,5−オクタンジオナト)銅入れ,基板9にはシリコン基板を用いてその上に成膜する操作を行った。
【0020】
なお,化1のビス(6−エチル−2,2−ジメチル−3,5−オクタンジオナト)銅は,次のようにして製造した。まず,酢酸銅1水和物10gを水200ミリリットルに溶解させ,これに6−エチル−2,2−ジメチル−3,5−オクタンジオン20gとメタノール20ミリリットルを加えて攪拌し,生じた沈澱を濾過し,減圧乾燥したのち昇華精製によって5.4gのビス(6−エチル−2,2−ジメチル−3,5−オクタンジオナト)銅を得た。得られた錯体の融点測定を行ったところ69〜70℃であった。
【0021】
この有機銅錯体1gを容器2内に装填し,恒温槽3を100℃の恒温に設定保持した。シリコン基板9をヒータ8によって600℃に加熱保持した状態で,キャリヤーガスとしてアルゴンガスを100ミリリットル/分を通流して該化合物を石英反応管7に導いた。容器2から熱分解炉6までの配管は120℃に保持されるように保温した。
【0022】
この条件下で30分間の成膜操作を行ったところ,厚さ1700オングストロームの均一な銅の薄膜が得られた。
【0023】
容器2に装填したビス(6−エチル−2,2−ジメチル−3,5−オクタンジオナト)銅の量を2gに変更した以外は,前記と全く同じ条件で成膜操作を繰り返した。この場合にも同じく厚さが1700オングストロームの均一な銅の薄膜が得られた。すなわち,容器2に装填する原料化合物量を変えても同厚の成膜ができた。このことは,原料化合物からの蒸発量が処理時間中一定であり,且つ分解量も一定であることを示している。
【0024】
〔実施例2〕
気体酸素を酸素源14から流量計15および弁16を経て反応管7内に50ミリリットル/分の流量で追加した以外は,実施例1と同様の処理を同じく30分間行った。その結果,原料装填量が1gと2gの両方とも2400オングストロームの同じ厚さの酸化銅の薄膜が得られた。
【0025】
〔比較例1〕
ビス(6−エチル−2,2−ジメチル−3,5−オクタンジオナト)銅に代えて,融点が197〜198℃のビス(ジピバロイルメタナト)銅を使用した以外は,実施例1と同様な条件で成膜した。その結果,30分後に原料充填量1gのものは厚さが2000オングストローム,また,原料充填量2gのものは厚さが2800オングストロームの銅の薄膜が得られた。このことは,容器内原料の容積変化にともなって蒸発量も経時変化したことを示している。
【0026】
〔比較例2〕
気体酸素を酸素源14から流量計15および弁16を経て反応管7内に50ミリリットル/分の流量で追加した以外は,比較例1と同様の処理を同じく30分間行った。その結果,原料充填量1gのものは厚さが2800オングストローム,また原料充填量2gのものは厚さが3900オングストロームの酸化銅の薄膜が得られた。
【0027】
【発明の効果】
以上のように,本発明に従うβ−ジケトン系有機銅錯体は低融点で,高気化性であり,かつ蒸発温度と分解温度がはなれていることから,CVD法によって銅または銅含有物質の薄膜を製造するための銅源物質として使用する場合に,液体状態で使用できるという優れた利点があり,またこのために蒸発速度が一定となるので安定した成膜速度が得られ,しかも高速で且つ均質な成膜ができるという特徴がある。
【0028】
したがって,本発明によれば,超電導材料やLSI配線材料などに有用な銅または銅含有物質の成膜技術に多大の貢献ができる。
【図面の簡単な説明】
【図1】熱CVD法を実施する設備の機器配置例を示した略断面図である。
【符号の説明】
1 有機金属錯体
2 原料容器
3 恒温槽
4 不活性キャリヤーガス
5 流量計
6 熱分解炉
7 石英反応管
8 ヒータ
9 基板
10 保温層
11 冷却トラップ
12 バルブ
13 ロータリーポンプ
14 酸素源[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a copper source material for CVD suitable for depositing copper or a copper-containing material by a chemical vapor deposition (CVD) method.
[0002]
[Prior art]
[0003]
Various proposals have been made for forming a thin film of copper or a copper-containing substance by a CVD method as a thin film useful for a superconducting material or an LSI wiring material. It is advantageous to use an organic copper complex as a starting compound when copper or a copper-containing substance is deposited by a CVD method.
[0004]
BACKGROUND ART Conventionally, an organic complex of a metal or a compound thereof has been used as a raw material compound when a film is formed by a CVD method, and an organic portion (ligand) constituting such an organometallic complex is as follows. Β-diketones such as dipivaloylmethane and hexafluoroacetylacetone are generally known. JP-A-4-72066 and JP-A-4-74866 disclose organic compounds constituting a complex with metals belonging to Group IIA, IIIA, IVA and IB of the periodic table having 1 to 5 carbon atoms. 1,3 diketones having a lower alkyl group are described.
[0005]
As the CVD method, a thermal CVD method, an optical CVD method, a plasma CVD method, and the like are known. In each case, a thin film is formed by decomposing a vapor of a raw material compound. In this case, the vapor is generally sublimated from the raw material compound in a solid state.
[0006]
[Problems to be solved by the invention]
The conventionally proposed organocopper complex using a β-diketone organic compound as a ligand generally has a high melting point (about 200 ° C.). For this reason, when it is applied to a raw material compound of the CVD method, a raw material vapor is generated by sublimation from a solid state without heating it to a high temperature higher than its melting point.
[0007]
In the case of sublimation from the solid state, as the remaining amount of the raw material in the raw material container decreases, the surface area of the raw material compound decreases, and the vaporization rate slows down. There is a problem that the film speed cannot be secured for a long time. Further, when the vaporization rate changes, it is difficult to control the composition of a thin film of a substance in which copper and other elements are combined (for example, YBa 2 Cu 3 O 7 ). There is also a problem.
[0008]
The organometallic complexes described in the above-mentioned JP-A-4-72066 and JP-A-4-74866 are also characterized in that they have high sublimability, and as a raw material compound for CVD, they are evaporated in a solid state. Things. Therefore, there is the same problem as described above.
[0009]
An organometallic complex using a ligand containing fluorine in the molecule, such as hexafluoroacetylacetone, has a low melting point, but fluoride may be present as an impurity in the formed film. Results in significantly impairing the properties of the film.
[0010]
Accordingly, an object of the present invention is to provide a copper source material for CVD having a low melting point capable of solving the above-mentioned problems.
[0011]
[Means for Solving the Problems]
The present inventors have conducted intensive studies in order to solve such a problem. As a result, an organocopper complex having β-diketone of 6-ethyl-2,2-dimethyl-3,5-octanedione as a ligand was produced by CVD. It has a very low melting point (approximately 69-70 ° C) that can be used in a liquid state as a raw material compound, and has extremely advantageous properties for film formation by CVD, in which the evaporation temperature and the decomposition temperature are clearly separated. . Due to this characteristic, when this is used as a copper source material in the CVD method, it can be evaporated from a liquid state, and supply of a raw material vapor of copper to a base material and decomposition and deposition of copper on the base material. Can be performed stably, so that the above-mentioned problem can be solved.
[0012]
That is, according to the present invention, 6-ethyl-2,2-dimethyl-3,5-octanedione is a copper source material for CVD used for depositing copper or a copper-containing material by a CVD method. The present invention provides a source material for CVD comprising an organocopper complex as a ligand.
[0013]
According to the present invention, when copper or a copper-containing substance is deposited on a substrate by a CVD method, 6-ethyl-2,2-dimethyl-3,5-octanedione is coordinated with copper as a copper source substance. A copper or copper-containing substance formed by a CVD method, wherein the organic copper complex is heated to a temperature equal to or higher than the melting point thereof, and the complex is evaporated from a liquid phase of the complex. Provide the law.
[0014]
The organocopper complex according to the present invention is represented by the general formula of Chemical Formula 1, and is considered to be a novel compound.
[0015]
Embedded image
[0016]
BEST MODE FOR CARRYING OUT THE INVENTION
The β-diketone-based organic copper complex according to the present invention is obtained by adding a copper carboxylate (for example, copper acetate or the like) and a ligand, 6-ethyl-2,2-dimethyl-3,5-octanedione, to a water-ethanol solution. The resulting precipitate can be collected by filtration, and purified by a purification method such as recrystallization or distillation.
[0017]
In order to use the thus obtained organic copper complex of the present invention as a raw material compound for the CVD method and form a film of the copper or copper-containing material by the CVD method, for example, as shown in FIG. The raw material container 2 containing the copper complex 1 is maintained at a predetermined temperature (a temperature higher than the melting point, for example, 80 to 100 ° C.) in the thermostat 3, and the flow rate of an inert carrier gas (eg, argon gas) 4 is measured by a flow meter 5. By introducing into the raw material container 2 while adjusting (for example, 5 to 500 ml / min), a gas flow accompanied by the organic copper complex is generated from the container 2.
[0018]
The generated organic copper complex vapor is led into the reaction tube 7 of the thermal decomposition furnace 6. The reaction tube (for example, a quartz tube) 7 is heated by a heater 8, and the substrate 9 installed in the tube is heated and maintained at a predetermined temperature (for example, 400 to 800 ° C.). Copper deposits on the top and forms a film. The piping from the raw material container 2 to the thermal decomposition furnace 6 is preferably maintained at a temperature higher than the heating temperature of the raw material container by 5 to 20 ° C. by the heat insulating layer 10 or a heat insulating means in order to prevent condensation. Exhaust gas from the reaction tube 7 is discharged through a cooling trap 11. In the figure,
[0019]
【Example】
[Example 1]
The bis (6-ethyl-2,2-dimethyl-3,5-octanedionato shown in Chemical Formula 1 as a raw material compound as a copper source is placed in a raw material container 2 made of stainless steel using the CVD equipment shown in FIG. 2) An operation of depositing copper and forming a film thereon using a silicon substrate as the substrate 9 was performed.
[0020]
The bis (6-ethyl-2,2-dimethyl-3,5-octandionato) copper of Chemical Formula 1 was produced as follows. First, 10 g of copper acetate monohydrate was dissolved in 200 ml of water, 20 g of 6-ethyl-2,2-dimethyl-3,5-octanedione and 20 ml of methanol were added thereto, and the mixture was stirred. After filtration and drying under reduced pressure, 5.4 g of bis (6-ethyl-2,2-dimethyl-3,5-octanedionato) copper was obtained by sublimation purification. The melting point of the obtained complex was measured to be 69 to 70 ° C.
[0021]
1 g of this organic copper complex was charged into the container 2 and the temperature of the thermostat 3 was kept at a constant temperature of 100 ° C. With the silicon substrate 9 heated and maintained at 600 ° C. by the heater 8, argon gas as a carrier gas was passed at 100 ml / min to guide the compound to the quartz reaction tube 7. The piping from the vessel 2 to the pyrolysis furnace 6 was kept warm so as to be kept at 120 ° C.
[0022]
When a film forming operation was performed for 30 minutes under these conditions, a uniform copper thin film having a thickness of 1700 angstroms was obtained.
[0023]
The film forming operation was repeated under exactly the same conditions as above except that the amount of bis (6-ethyl-2,2-dimethyl-3,5-octanedionato) copper charged in the container 2 was changed to 2 g. In this case, a uniform copper thin film having a thickness of 1700 angstroms was obtained. That is, even when the amount of the raw material compound charged in the container 2 was changed, a film having the same thickness could be formed. This indicates that the amount of evaporation from the starting compound is constant during the treatment time and the amount of decomposition is also constant.
[0024]
[Example 2]
The same processing as in Example 1 was performed for 30 minutes, except that gaseous oxygen was added from the
[0025]
[Comparative Example 1]
Example 1 except that bis (dipivaloylmethanato) copper having a melting point of 197 to 198 ° C was used in place of bis (6-ethyl-2,2-dimethyl-3,5-octandionato) copper. A film was formed under the same conditions as described above. As a result, after 30 minutes, a copper thin film having a thickness of 2000 Å was obtained for a material having a loading of 1 g and a copper thin film having a thickness of 2800 Å for a loading having a material loading of 2 g. This indicates that the evaporation amount also changed over time with the change in the volume of the raw material in the container.
[0026]
[Comparative Example 2]
The same process as in Comparative Example 1 was performed for 30 minutes, except that gaseous oxygen was added from the
[0027]
【The invention's effect】
As described above, the β-diketone-based organocopper complex according to the present invention has a low melting point, a high vaporization property, and an evaporating temperature and a decomposition temperature separated from each other. When used as a copper source material for production, it has an excellent advantage that it can be used in a liquid state, and since it has a constant evaporation rate, a stable film formation rate can be obtained. It has the feature that it is possible to form a thin film.
[0028]
Therefore, according to the present invention, a great contribution can be made to a technique for forming copper or a copper-containing substance useful for a superconducting material or an LSI wiring material.
[Brief description of the drawings]
FIG. 1 is a schematic cross-sectional view showing an example of equipment arrangement of equipment for performing a thermal CVD method.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Organometallic complex 2 Raw material container 3 Thermostat 4 Inert carrier gas 5 Flow meter 6 Pyrolysis furnace 7 Quartz reaction tube 8 Heater 9 Substrate 10 Heat insulation layer 11
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22608595A JP3584091B2 (en) | 1995-08-11 | 1995-08-11 | Copper source material for CVD and film forming method using the same |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22608595A JP3584091B2 (en) | 1995-08-11 | 1995-08-11 | Copper source material for CVD and film forming method using the same |
Publications (2)
| Publication Number | Publication Date |
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| JPH0953177A JPH0953177A (en) | 1997-02-25 |
| JP3584091B2 true JP3584091B2 (en) | 2004-11-04 |
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| JP3680029B2 (en) | 2001-08-08 | 2005-08-10 | 三菱重工業株式会社 | Vapor growth method and vapor growth apparatus for metal thin film |
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