JP2015021175A - Film production method of metallic thin film - Google Patents
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- 239000010408 film Substances 0.000 title claims abstract description 109
- 239000010409 thin film Substances 0.000 title claims abstract description 91
- 238000004519 manufacturing process Methods 0.000 title abstract 4
- 229910052751 metal Inorganic materials 0.000 claims abstract description 99
- 239000002184 metal Substances 0.000 claims abstract description 99
- 239000007789 gas Substances 0.000 claims abstract description 78
- 239000000758 substrate Substances 0.000 claims abstract description 73
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 42
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims abstract description 34
- 150000004767 nitrides Chemical class 0.000 claims abstract description 29
- 239000012495 reaction gas Substances 0.000 claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- 125000004433 nitrogen atom Chemical group N* 0.000 claims abstract description 8
- 238000007736 thin film deposition technique Methods 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims description 95
- 229910052721 tungsten Inorganic materials 0.000 claims description 35
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 31
- 125000004429 atom Chemical group 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 8
- 239000000126 substance Substances 0.000 claims description 7
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 claims description 6
- 229930195733 hydrocarbon Natural products 0.000 claims description 6
- 150000002430 hydrocarbons Chemical class 0.000 claims description 6
- 229910021529 ammonia Inorganic materials 0.000 claims description 5
- 229910052750 molybdenum Inorganic materials 0.000 claims description 5
- HDZGCSFEDULWCS-UHFFFAOYSA-N monomethylhydrazine Chemical compound CNN HDZGCSFEDULWCS-UHFFFAOYSA-N 0.000 claims description 5
- DIIIISSCIXVANO-UHFFFAOYSA-N 1,2-Dimethylhydrazine Chemical compound CNNC DIIIISSCIXVANO-UHFFFAOYSA-N 0.000 claims description 3
- YBQZXXMEJHZYMB-UHFFFAOYSA-N 1,2-diphenylhydrazine Chemical compound C=1C=CC=CC=1NNC1=CC=CC=C1 YBQZXXMEJHZYMB-UHFFFAOYSA-N 0.000 claims description 3
- 239000002994 raw material Substances 0.000 abstract description 84
- 239000011737 fluorine Substances 0.000 abstract description 5
- 229910052731 fluorine Inorganic materials 0.000 abstract description 5
- 239000013626 chemical specie Substances 0.000 abstract description 3
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 42
- 125000002524 organometallic group Chemical group 0.000 description 42
- -1 butylimino Chemical group 0.000 description 39
- 238000010926 purge Methods 0.000 description 35
- 239000010937 tungsten Substances 0.000 description 33
- 239000001307 helium Substances 0.000 description 31
- 229910052734 helium Inorganic materials 0.000 description 31
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 31
- 239000000203 mixture Substances 0.000 description 24
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 22
- 229910052757 nitrogen Inorganic materials 0.000 description 20
- 230000005587 bubbling Effects 0.000 description 14
- 238000001179 sorption measurement Methods 0.000 description 12
- 229910001220 stainless steel Inorganic materials 0.000 description 9
- 239000010935 stainless steel Substances 0.000 description 9
- FFBHFFJDDLITSX-UHFFFAOYSA-N benzyl N-[2-hydroxy-4-(3-oxomorpholin-4-yl)phenyl]carbamate Chemical compound OC1=C(NC(=O)OCC2=CC=CC=C2)C=CC(=C1)N1CCOCC1=O FFBHFFJDDLITSX-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- 229910052715 tantalum Inorganic materials 0.000 description 6
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 6
- 239000012298 atmosphere Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 4
- 238000000231 atomic layer deposition Methods 0.000 description 4
- MZLGASXMSKOWSE-UHFFFAOYSA-N tantalum nitride Chemical compound [Ta]#N MZLGASXMSKOWSE-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 3
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 3
- GPBUGPUPKAGMDK-UHFFFAOYSA-N azanylidynemolybdenum Chemical compound [Mo]#N GPBUGPUPKAGMDK-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000011733 molybdenum Substances 0.000 description 3
- JVCWKXBYGCJHDF-UHFFFAOYSA-N CC(C)(C)N=[W](N(C)C)(=NC(C)(C)C)N(C)C Chemical compound CC(C)(C)N=[W](N(C)C)(=NC(C)(C)C)N(C)C JVCWKXBYGCJHDF-UHFFFAOYSA-N 0.000 description 2
- VGROASXKXRYOQN-UHFFFAOYSA-N CCCCN=[Ta](N(CC)CC)(N(CC)CC)N(CC)CC Chemical group CCCCN=[Ta](N(CC)CC)(N(CC)CC)N(CC)CC VGROASXKXRYOQN-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- KUMGWCYRXZGGGP-UHFFFAOYSA-N bis(tert-butylimino)molybdenum(2+) dimethylazanide Chemical compound C(C)(C)(C)N=[Mo](N(C)C)(N(C)C)=NC(C)(C)C KUMGWCYRXZGGGP-UHFFFAOYSA-N 0.000 description 2
- 239000012159 carrier gas Substances 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000004544 sputter deposition Methods 0.000 description 2
- NXHILIPIEUBEPD-UHFFFAOYSA-H tungsten hexafluoride Chemical compound F[W](F)(F)(F)(F)F NXHILIPIEUBEPD-UHFFFAOYSA-H 0.000 description 2
- KRTHAZICNMQWPF-UHFFFAOYSA-N C(C)(C)(C)N=[Mo](N(CC)C)(N(C)CC)=NC(C)(C)C Chemical compound C(C)(C)(C)N=[Mo](N(CC)C)(N(C)CC)=NC(C)(C)C KRTHAZICNMQWPF-UHFFFAOYSA-N 0.000 description 1
- JKBNASDITMQHMZ-UHFFFAOYSA-N C(C)N(CC)[Mo]N(CC)CC Chemical compound C(C)N(CC)[Mo]N(CC)CC JKBNASDITMQHMZ-UHFFFAOYSA-N 0.000 description 1
- KJJLGQQSUUSUOI-UHFFFAOYSA-N CCCCN=[Ta](N(C)CC)(N(C)CC)N(C)CC Chemical group CCCCN=[Ta](N(C)CC)(N(C)CC)N(C)CC KJJLGQQSUUSUOI-UHFFFAOYSA-N 0.000 description 1
- KKSXSQXELVXONV-UHFFFAOYSA-N CCN(C)[W](=NC(C)(C)C)(=NC(C)(C)C)N(C)CC Chemical compound CCN(C)[W](=NC(C)(C)C)(=NC(C)(C)C)N(C)CC KKSXSQXELVXONV-UHFFFAOYSA-N 0.000 description 1
- IVBDGJZEAHBGFJ-UHFFFAOYSA-N CCN(CC)[W](=NC(C)(C)C)(=NC(C)(C)C)N(CC)CC Chemical compound CCN(CC)[W](=NC(C)(C)C)(=NC(C)(C)C)N(CC)CC IVBDGJZEAHBGFJ-UHFFFAOYSA-N 0.000 description 1
- PTDGQDJPIFTKJL-UHFFFAOYSA-N CN(C)[W] Chemical compound CN(C)[W] PTDGQDJPIFTKJL-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- CATZWJHMMLOSEK-UHFFFAOYSA-N bis(tert-butylimino)molybdenum(2+) tert-butylazanide Chemical compound C(C)(C)(C)N=[Mo](NC(C)(C)C)(NC(C)(C)C)=NC(C)(C)C CATZWJHMMLOSEK-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 125000002147 dimethylamino group Chemical group [H]C([H])([H])N(*)C([H])([H])[H] 0.000 description 1
- 125000001153 fluoro group Chemical group F* 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 238000005289 physical deposition Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 230000003595 spectral effect Effects 0.000 description 1
- 238000000391 spectroscopic ellipsometry Methods 0.000 description 1
- KNHNEFGWIAXKRC-UHFFFAOYSA-N tungsten dihydride Chemical compound [WH2] KNHNEFGWIAXKRC-UHFFFAOYSA-N 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
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Abstract
Description
本発明は、金属薄膜の製膜方法に関するものである。 The present invention relates to a method for forming a metal thin film.
半導体デバイスは、微細化・高集積化に伴って、高いアスペクト比の溝や孔に様々な金属膜を形成することが求められている。これまではスパッタリングを用いた物理的製膜手法によって金属膜が形成されてきた。しかしながら、従来のスパッタリングを用いた物理的製膜手法は段差被覆性に劣っているため、基板上に形成された高アスペクト比のパターンを被覆する目的でこれらの薄膜を形成すると、ボイド形成やバリア膜破れなどが生じて信頼性劣化に繋がるという問題が顕在化してきた。 With miniaturization and high integration, semiconductor devices are required to form various metal films in grooves and holes having a high aspect ratio. Until now, a metal film has been formed by a physical film forming technique using sputtering. However, since the conventional physical deposition method using sputtering is inferior in step coverage, when these thin films are formed for the purpose of covering a high aspect ratio pattern formed on a substrate, void formation and barrier The problem that film breakage and the like lead to deterioration of reliability has become apparent.
上記問題を解決するために、段差被覆性に優れたＣＶＤ法またはＡＬＤ法による金属膜の導入が検討されている（例えば、特許文献１を参照）。具体的には、例えば、メモリデバイスの形成において製膜されるタングステン薄膜については、従来から六フッ化タングステン（ＷＦ６）を原料として用いたＣＶＤプロセスが適用されていた。しかしながら、原料である六フッ化タングステンに含まれているフッ素により、周囲の絶縁膜やタングステン（Ｗ）膜そのものの信頼性が損なわれるおそれが懸念されている。 In order to solve the above problem, introduction of a metal film by a CVD method or an ALD method having excellent step coverage has been studied (for example, see Patent Document 1). Specifically, for example, for a tungsten thin film formed in the formation of a memory device, conventionally, a CVD process using tungsten hexafluoride (WF 6 ) as a raw material has been applied. However, there is a concern that the reliability of the surrounding insulating film and the tungsten (W) film itself may be impaired by the fluorine contained in the raw material tungsten hexafluoride.
ところで、フッ素フリーのタングステン膜形成用の原料としては、下記式（Ａ）に示したビスシクロペンタジエニルタングステン二水素化物や、下記式（Ｂ）に示したビス（ターシャリーブチルイミノ）ビス（ジメチルアミノ）タングステン、あるいは、これらの類似体が提案されてきた。 By the way, as a raw material for forming a fluorine-free tungsten film, biscyclopentadienyl tungsten dihydride represented by the following formula (A) or bis (tertiary butylimino) bis ( (Dimethylamino) tungsten or analogs thereof have been proposed.
しかしながら、上記式（Ａ）に示した原料は、製膜温度が５００℃以上と高く、基板や装置を損傷するおそれがあるため、実用のプロセスには適さないという課題があった。一方、上記式（Ｂ）に示した原料は、３５０℃以上の温度で製膜できるものの、タングステン膜ではなく窒化タングステン膜が得られるため、抵抗率を低減させることが困難であるという課題があった。 However, the raw material represented by the above formula (A) has a problem that it is not suitable for a practical process because the film forming temperature is as high as 500 ° C. or higher and there is a risk of damaging the substrate or the apparatus. On the other hand, although the raw material shown in the above formula (B) can be formed at a temperature of 350 ° C. or higher, a tungsten nitride film is obtained instead of a tungsten film, so that it is difficult to reduce the resistivity. It was.
本発明は、上記事情に鑑みてなされたものであって、フッ素によって基板に損傷を与えることなく、高純度の金属薄膜を得ることが可能な金属薄膜の製膜方法を提供することを目的とする。 The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a method for forming a metal thin film capable of obtaining a high-purity metal thin film without damaging the substrate with fluorine. To do.
かかる課題を解決するため、本願発明者は鋭意検討した結果、所定のフッ素フリーのタングステン膜の原料を用いて形成した金属窒化膜について、水素雰囲気下で加熱することにより窒素原子を除去することができることを見出した。また、膜中の窒素組成が原子組成で１ａｔ％（原子組成百分率）以下になるまでの時間と膜厚との関係は、およそ比例関係にあることを見出して、本願発明を完成させた。 In order to solve this problem, the present inventor has intensively studied, and as a result, it is possible to remove nitrogen atoms by heating a metal nitride film formed using a raw material of a predetermined fluorine-free tungsten film in a hydrogen atmosphere. I found out that I can do it. Further, the present invention was completed by finding that the relationship between the time until the nitrogen composition in the film became 1 at% (atomic composition percentage) or less in atomic composition and the film thickness was approximately proportional.
すなわち、本発明は、以下の構成を有する。
請求項１にかかる発明は、化学反応を用いた薄膜堆積法によって基板の表面に金属薄膜を製膜する方法であって、
基板の表面に、下記式（１）で示される有機金属化学種を含む原料ガスと含窒素反応ガスとを供給して、金属窒化膜を形成する第１工程と、
前記基板の表面に水素ガスを供給して、前記金属窒化膜中の窒素原子を除去する第２工程と、を含むことを特徴とする金属薄膜の製膜方法である。
また、Ｍ１は、第５族又は第６族の金属原子であり、Ｍ１が第５族である場合にｐ＋２ｑ＝５であり、Ｍ１が第６族である場合にｐ＋２ｑ＝６である。
That is, the present invention has the following configuration.
The invention according to claim 1 is a method of forming a metal thin film on the surface of a substrate by a thin film deposition method using a chemical reaction,
A first step of forming a metal nitride film by supplying a source gas containing a metalorganic species represented by the following formula (1) and a nitrogen-containing reaction gas to the surface of the substrate;
And a second step of removing nitrogen atoms in the metal nitride film by supplying hydrogen gas to the surface of the substrate.
Further, M 1 is a Group 5 or Group 6 metal atoms are p + 2q = 5 when M 1 is a Group 5 is the p + 2q = 6 when M 1 is a Group 6 .
請求項２にかかる発明は、前記第１工程において、前記原料ガスを供給した後に、前記含窒素反応ガスを供給することを特徴とする請求項１に記載の金属薄膜の製膜方法である。 The invention according to claim 2 is the metal thin film forming method according to claim 1, wherein in the first step, the nitrogen-containing reaction gas is supplied after the source gas is supplied.
請求項３にかかる発明は、前記第１工程において、前記原料ガスと前記含窒素反応ガスとを同時に供給することを特徴とする請求項１に記載の金属薄膜の製膜方法である。 The invention according to claim 3 is the metal thin film forming method according to claim 1, wherein in the first step, the source gas and the nitrogen-containing reaction gas are supplied simultaneously.
請求項４にかかる発明は、上記式（１）中に示すＭ１は、Ｔａであることを特徴とする請求項１乃至３のいずれか一項に記載の金属薄膜の製膜方法である。 The invention according to claim 4 is the method for forming a metal thin film according to any one of claims 1 to 3, wherein M 1 shown in the formula (1) is Ta.
請求項５にかかる発明は、上記式（１）中に示すＭ１は、Ｗ又はＭｏであることを特徴とする請求項１乃至３のいずれか一項に記載の金属薄膜の製膜方法である。 The invention according to claim 5, M 1 shown in the above formula (1) is a film forming method of the metal thin film according to any one of claims 1 to 3, characterized in that the W or Mo is there.
請求項６にかかる発明は、前記含窒素反応ガスが、アンモニア、ヒドラジン、モノメチルヒドラジン、ジメチルヒドラジン及びジフェニルヒドラジンのうち、少なくともいずれか一つを含むことを特徴とする請求項１乃至５のいずれか一項に記載の金属薄膜の製膜方法である。 The invention according to claim 6 is characterized in that the nitrogen-containing reaction gas contains at least one of ammonia, hydrazine, monomethylhydrazine, dimethylhydrazine and diphenylhydrazine. A method for forming a metal thin film according to one item.
請求項７にかかる発明は、前記第１工程で形成する金属窒化膜の厚さを１０ｎｍ以下とすることを特徴とする請求項１乃至６のいずれか一項に記載の金属薄膜の製膜方法である。 The invention according to claim 7 is characterized in that the thickness of the metal nitride film formed in the first step is 10 nm or less, and the method for forming a metal thin film according to any one of claims 1 to 6 is provided. It is.
請求項８にかかる発明は、前記第１及び第２工程を２回以上繰り返すことを特徴する請求項１乃至７のいずれか一項に記載の金属薄膜の製膜方法である。 The invention according to claim 8 is the metal thin film forming method according to any one of claims 1 to 7, wherein the first and second steps are repeated twice or more.
本発明の金属薄膜の製膜方法によれば、フッ素によって基板に損傷を与えることなく、高純度の金属薄膜を得ることができる。 According to the metal thin film forming method of the present invention, a high-purity metal thin film can be obtained without damaging the substrate with fluorine.
以下、本発明を適用した実施の形態である金属薄膜の製膜方法について、図面を用いて詳細に説明する。なお、以下の説明で用いる図面は、特徴をわかりやすくするために、便宜上特徴となる部分を拡大して示している場合があり、各構成要素の寸法比率などが実際と同じであるとは限らない。 Hereinafter, a metal thin film forming method according to an embodiment to which the present invention is applied will be described in detail with reference to the drawings. In addition, in the drawings used in the following description, in order to make the features easy to understand, there are cases where the portions that become the features are enlarged for the sake of convenience, and the dimensional ratios of the respective components are not always the same as the actual ones. Absent.
＜第１の実施形態＞
本実施形態の金属薄膜の製膜方法は、化学反応を用いた薄膜堆積法（例えば、ＣＶＤ法、ＡＬＤ法）によって、例えばシリコン基板等の基板の表面に金属薄膜を製膜する方法であって、製膜対象となる基板の表面に、下記式（１）で示される有機金属化学種を含む原料ガスと含窒素反応ガスとを供給して、金属窒化膜を形成する第１工程と、基板の表面に水素ガスを供給して、金属窒化膜中の窒素原子を除去する第２工程と、を含んで概略構成されている。
<First Embodiment>
The metal thin film forming method of the present embodiment is a method of forming a metal thin film on the surface of a substrate such as a silicon substrate by a thin film deposition method (for example, a CVD method or an ALD method) using a chemical reaction. A first step of forming a metal nitride film by supplying a raw material gas containing an organometallic chemical species represented by the following formula (1) and a nitrogen-containing reaction gas to the surface of a substrate to be formed; And a second step of removing nitrogen atoms in the metal nitride film by supplying hydrogen gas to the surface.
なお、上記式（１）において、Ｒ１及びＲ２は、ＣｎＨ２ｎ＋１（ｎ＝１〜４）の化学式で表される直鎖状又は分岐された炭化水素であり、Ｒ３は、水素又はＣｎＨ２ｎ＋１（ｎ＝１〜４）の化学式で表される直鎖状又は分岐された炭化水素である。
また、Ｍ１は、第５族又は第６族の金属原子であり、Ｍ１が第５族である場合にｐ＋２ｑ＝５であり、Ｍ１が第６族である場合にｐ＋２ｑ＝６である。
In the above formula (1), R 1 and R 2 are linear or branched hydrocarbons represented by the chemical formula of C n H 2n + 1 (n = 1 to 4), and R 3 is hydrogen. or C n H 2n + 1 (n = 1~4) linear or branched hydrocarbons represented by the chemical formula.
Further, M 1 is a Group 5 or Group 6 metal atoms are p + 2q = 5 when M 1 is a Group 5 is the p + 2q = 6 when M 1 is a Group 6 .
上記式（１）で示される有機金属化学種（以下、アミノイミノ原料という）としては、当該式（１）中に示される金属原子Ｍ１が第５族である場合には、ｐ＋２ｑ＝５を満たす物質を原料として用いる。具体的には、例えば、金属原子Ｍ１が、タンタル（Ｔａ）である場合には、ターシャリーブチルイミノトリス（ジエチルアミノ）タンタル、ターシャリーブチルイミノトリス（エチルメチルアミノ）タンタル、ペンタキス（ジメチルアミノ）タンタル等が挙げられる。 The organometallic chemical species represented by the above formula (1) (hereinafter referred to as aminoimino raw material) satisfies p + 2q = 5 when the metal atom M 1 represented by the formula (1) is Group 5. The substance is used as a raw material. Specifically, for example, when the metal atom M 1 is tantalum (Ta), tertiary butyl imino tris (diethylamino) tantalum, tertiary butyl imino tris (ethylmethylamino) tantalum, pentakis (dimethylamino) Examples include tantalum.
また、上記式（１）で示されるアミノイミノ原料としては、当該式（１）中に示される金属原子Ｍ１が第６族である場合には、ｐ＋２ｑ＝６を満たす物質を原料として用いる。具体的には、例えば、金属原子Ｍ１が、タングステン（Ｗ）である場合には、ビス（ターシャリーブチルイミノ）ビス（ジメチルアミノ）タングステン、ビス（ターシャリーブチルイミノ）ビス（ターシャリーブチルアミノ）タングステン、ビス（ターシャリーブチルイミノ）ビス（ジエチルアミノ）タングステン、ビス（ターシャリーブチルイミノ）ビス（エチルメチルアミノ）タングステン等が挙げられる。また、金属原子Ｍ１が、モリブデン（Ｍｏ）である場合には、ビス（ターシャリーブチルイミノ）ビス（ジメチルアミノ）モリブデン、ビス（ターシャリーブチルイミノ）ビス（ターシャリーブチルアミノ）モリブデン、ビス（ターシャリーブチルイミノ）ビス（ジエチルアミノ）モリブデン、ビス（ターシャリーブチルイミノ）ビス（エチルメチルアミノ）モリブデン等が挙げられる。 In addition, as the aminoimino raw material represented by the above formula (1), when the metal atom M 1 represented in the formula (1) is a Group 6, a material satisfying p + 2q = 6 is used as the raw material. Specifically, for example, when the metal atom M 1 is tungsten (W), bis (tertiarybutylimino) bis (dimethylamino) tungsten, bis (tertiarybutylimino) bis (tertiarybutylamino) ) Tungsten, bis (tertiary butyl imino) bis (diethylamino) tungsten, bis (tertiary butyl imino) bis (ethylmethylamino) tungsten, and the like. When the metal atom M 1 is molybdenum (Mo), bis (tertiary butyl imino) bis (dimethylamino) molybdenum, bis (tertiary butyl imino) bis (tertiary butyl amino) molybdenum, bis ( And tertiary butylimino) bis (diethylamino) molybdenum and bis (tertiarybutylimino) bis (ethylmethylamino) molybdenum.
含窒素反応ガスの成分は、上記式（１）で示されるアミノイミノ原料と反応して金属窒化膜を形成可能な成分であれば、特に限定されるものではない。このような含窒素反応ガスの含窒素成分としては、具体的には、例えば、アンモニア、ヒドラジン、モノメチルヒドラジン、ジメチルヒドラジン及びジフェニルヒドラジン等が挙げられる。なお、含窒素反応ガスは、上記含窒素成分のうち、いずれか一種を選択して用いても良いし、２種以上の混合ガスとして用いても良い。 The component of the nitrogen-containing reactive gas is not particularly limited as long as it can react with the aminoimino raw material represented by the above formula (1) to form a metal nitride film. Specific examples of the nitrogen-containing component of such a nitrogen-containing reaction gas include ammonia, hydrazine, monomethyl hydrazine, dimethyl hydrazine, and diphenyl hydrazine. The nitrogen-containing reaction gas may be used by selecting any one of the nitrogen-containing components, or may be used as a mixed gas of two or more.
次に、図１を参照して、本実施形態の金属薄膜の製膜方法について、具体的に説明する。
先ず、図１中に示すステップＳ１１に示すように、ＣＶＤ装置あるいはＡＬＤ装置等のプロセス装置のチャンバ内に製膜対象となる基板を搬入する。
Next, with reference to FIG. 1, the metal thin film forming method of the present embodiment will be specifically described.
First, as shown in step S11 shown in FIG. 1, a substrate to be formed is carried into a chamber of a process apparatus such as a CVD apparatus or an ALD apparatus.
ここで、チャンバ内の真空度は、５０Ｔｏｒｒ（６．６ｋＰａ）以上、０．１Ｔｏｒｒ（１３Ｐａ）以下とすることが好ましく、０．３Ｔｏｒｒ（４０Ｐａ）以下とすることがより好ましい。上記真空度が５０Ｔｏｒｒ未満であると、原料ガスの分圧が低くなり、金属窒化膜の膜厚が得られないために好ましくない。一方、上記真空度が０．１Ｔｏｒｒを超えると、供給ガスの切り替え間のパージ処理時間が長くなってしまうために好ましくない。これに対して、チャンバ内の真空度が上記範囲内であると、充分な膜厚の金属窒化膜が短時間で得られるために好ましい。 Here, the degree of vacuum in the chamber is preferably 50 Torr (6.6 kPa) or more and 0.1 Torr (13 Pa) or less, and more preferably 0.3 Torr (40 Pa) or less. When the degree of vacuum is less than 50 Torr, the partial pressure of the source gas is lowered, and the thickness of the metal nitride film cannot be obtained, which is not preferable. On the other hand, when the degree of vacuum exceeds 0.1 Torr, it is not preferable because the purge processing time between supply gas changes becomes long. On the other hand, it is preferable that the degree of vacuum in the chamber is within the above range because a sufficiently thick metal nitride film can be obtained in a short time.
（第１工程）
次に、ステップＳ１２に示すように、チャンバ内をヘリウム（Ｈｅ）ガスを流通させながら基板を加熱する。ここで、基板の加熱温度は、３５０〜４００℃の範囲とすることが好ましい。上記加熱温度が３５０℃未満であると、金属窒化膜の製膜速度が遅くなるために好ましくない。一方、上記加熱温度が４００℃を超えると、熱によって基板やプロセス装置が損傷をうけるおそれがあるために好ましくない。これに対して、基板の加熱温度が上記範囲内であれば、基板やプロセス装置に損傷を与えるおそれがなく、金属窒化膜の製膜速度を高めることができるために好ましい。
(First step)
Next, as shown in step S12, the substrate is heated while flowing helium (He) gas through the chamber. Here, the heating temperature of the substrate is preferably in the range of 350 to 400 ° C. If the heating temperature is less than 350 ° C., the film forming speed of the metal nitride film is slow, which is not preferable. On the other hand, if the heating temperature exceeds 400 ° C., the substrate and the process apparatus may be damaged by heat, which is not preferable. On the other hand, it is preferable that the heating temperature of the substrate is within the above range because there is no possibility of damaging the substrate and the process apparatus, and the deposition rate of the metal nitride film can be increased.
次に、ステップＳ１３に示すように、ヘリウムガスの供給を停止した後、上記式（１）で示されるアミノイミノ原料をキャリアガスに同伴させてチャンバ内に供給する。換言すると、チャンバ内の加熱された基板表面にアミノイミノ原料を供給する。これにより、基板の表面にアミノイミノ原料を吸着させる。なお、キャリアガスは、上記アミノイミノ原料と反応しない不活性ガスであれば、特に限定されるものではなく、例えば、窒素ガス、ヘリウムガス、アルゴンガス等を用いることができる。 Next, as shown in step S13, after the supply of helium gas is stopped, the aminoimino raw material represented by the above formula (1) is supplied into the chamber along with the carrier gas. In other words, the aminoimino raw material is supplied to the heated substrate surface in the chamber. Thereby, the aminoimino raw material is adsorbed on the surface of the substrate. The carrier gas is not particularly limited as long as it is an inert gas that does not react with the aminoimino raw material. For example, nitrogen gas, helium gas, argon gas, or the like can be used.
次に、ステップＳ１４に示すように、アミノイミノ原料ガスの供給を停止した後、チャンバ内にパージガスを供給する。なお、パージガスは、上記アミノイミノ原料と反応しない不活性ガスであれば、特に限定されるものではなく、例えば、窒素ガス、ヘリウムガス、アルゴンガス等を用いることができる。 Next, as shown in step S14, after the supply of the aminoimino source gas is stopped, the purge gas is supplied into the chamber. The purge gas is not particularly limited as long as it is an inert gas that does not react with the aminoimino raw material. For example, nitrogen gas, helium gas, argon gas, or the like can be used.
次に、ステップＳ１５に示すように、パージガスの供給を停止した後、チャンバ内に含窒素反応ガスを供給する。換言すると、チャンバ内の加熱された基板表面に含窒素反応ガスを供給する。これにより、基板表面に吸着させたアミノイミノ原料と含窒素反応ガスとを反応させて、当該基板の表面に金属窒化膜を製膜することができる。 Next, as shown in step S15, after supply of the purge gas is stopped, a nitrogen-containing reactive gas is supplied into the chamber. In other words, a nitrogen-containing reactive gas is supplied to the heated substrate surface in the chamber. Thus, a metal nitride film can be formed on the surface of the substrate by reacting the aminoimino raw material adsorbed on the substrate surface with the nitrogen-containing reactive gas.
なお、ステップＳ１３に示すアミノイミノ原料の供給量およびステップＳ１５に示す含窒素反応ガスの供給量は、基板表面に製膜される金属窒化膜の膜厚が、１０ｎｍ以下となるように調整することが好ましい。ここで、金属窒化膜の上記膜厚が１０ｎｍを超えると、ガスの供給量の増加や製膜時間の増加を招くとともに、後述する第２工程において金属窒化膜中の窒素原子の除去に時間を要する、あるいは除去が不十分となるために好ましくない。しかしながら、理想的な原子層堆積工程においては、ステップＳ１３に示すアミノイミノ原料の供給量を増やしても、基板全体にアミノイミノ原料が１層吸着した時点で飽和する。また引き続くステップＳ１５の含窒素反応ガスの供給量を増やしても、上記吸着したアミノイミノ原料がすべて反応した時点でそれ以上反応が進まなくなる。そのため、ステップ１３〜１５による第１工程によって製膜された金属窒化膜の膜厚は１ｎｍ以下にとどまり、上述の膜厚１０ｎｍ以下という必要条件を満たす。 The supply amount of the aminoimino raw material shown in step S13 and the supply amount of the nitrogen-containing reactive gas shown in step S15 can be adjusted so that the thickness of the metal nitride film formed on the substrate surface is 10 nm or less. preferable. Here, when the thickness of the metal nitride film exceeds 10 nm, an increase in gas supply amount and an increase in film formation time are caused, and a time is required for removing nitrogen atoms in the metal nitride film in the second step described later. This is not preferable because it requires or is insufficiently removed. However, in an ideal atomic layer deposition process, even if the supply amount of the aminoimino raw material shown in step S13 is increased, the aminoimino raw material is saturated when one layer is adsorbed on the entire substrate. Further, even if the supply amount of the nitrogen-containing reactive gas in the subsequent step S15 is increased, the reaction does not proceed any more when all the adsorbed aminoimino raw materials have reacted. Therefore, the thickness of the metal nitride film formed by the first process in steps 13 to 15 is 1 nm or less, and satisfies the above requirement of the film thickness of 10 nm or less.
（第２工程）
次に、図１中のステップＳ１６に示すように、含窒素反応ガスの供給を停止した後、チャンバ内にパージガスを供給する。
(Second step)
Next, as shown in step S16 in FIG. 1, after the supply of the nitrogen-containing reaction gas is stopped, the purge gas is supplied into the chamber.
次に、ステップＳ１７に示すように、パージガスの供給を停止した後、チャンバ内に水素ガスを供給する。換言すると、チャンバ内の基板表面に製膜された金属窒化膜に水素ガスを供給する。これにより、金属窒化膜中の窒素原子が除去されて、低不純物の（すなわち、高純度の）金属薄膜を製膜することができる。 Next, as shown in step S17, after the supply of the purge gas is stopped, hydrogen gas is supplied into the chamber. In other words, hydrogen gas is supplied to the metal nitride film formed on the substrate surface in the chamber. Thereby, nitrogen atoms in the metal nitride film are removed, and a low impurity (that is, high purity) metal thin film can be formed.
なお、ステップＳ１７において、水素ガスの供給量（あるいは供給時間）は、上記第１工程で基板表面に製膜した金属窒化膜の膜厚に応じて適宜選択することが好ましい。 In step S17, the supply amount (or supply time) of hydrogen gas is preferably selected as appropriate according to the thickness of the metal nitride film formed on the substrate surface in the first step.
次に、ステップＳ１８に示すように、水素ガスの供給を停止した後、チャンバ内にパージガスを供給する。
以上のステップＳ１３〜Ｓ１８を１サイクルとして、基板表面に、膜厚が１ｎｍ以下の金属薄膜を製膜することができる。
Next, as shown in step S18, after the supply of hydrogen gas is stopped, purge gas is supplied into the chamber.
With the above steps S13 to S18 as one cycle, a metal thin film having a thickness of 1 nm or less can be formed on the substrate surface.
ここで、金属薄膜の膜厚が目標の膜厚に達していない場合には、ステップＳ１３〜Ｓ１８のサイクル（すなわち、第１工程及び第２工程）を２以上繰りかえすことが好ましい。これにより、金属薄膜の膜厚を目標の膜厚とすることができる。 Here, when the film thickness of the metal thin film does not reach the target film thickness, it is preferable to repeat two or more cycles of steps S13 to S18 (that is, the first step and the second step). Thereby, the film thickness of a metal thin film can be made into a target film thickness.
一方、金属薄膜の膜厚が目標の膜厚に達した場合には、ステップＳ１９に示すように、チャンバ内を大気圧に戻した後、プロセス装置から金属薄膜を製膜した基板を取り出す。 On the other hand, when the film thickness of the metal thin film reaches the target film thickness, as shown in step S19, the chamber is returned to atmospheric pressure, and then the substrate on which the metal thin film is formed is taken out from the process apparatus.
以上説明したように、本実施形態の金属薄膜の製膜方法によれば、元素組成で１ａｔ％以下の高純度の金属薄膜を製膜することができる。また、本実施形態の金属薄膜の製膜方法によって製膜された金属薄膜によれば、抵抗率を３．０×１０−７Ω・ｍ以下に抑えることができる。 As described above, according to the metal thin film forming method of the present embodiment, a high-purity metal thin film having an element composition of 1 at% or less can be formed. Moreover, according to the metal thin film formed by the metal thin film forming method of the present embodiment, the resistivity can be suppressed to 3.0 × 10 −7 Ω · m or less.
また、本実施形態の金属薄膜の製膜方法によれば、フッ素原子を含まないアミノイミノ原料を用いるため、製膜中にフッ素が生成するおそれがなく、基板に損傷を与えることがない。 Further, according to the metal thin film forming method of the present embodiment, since an aminoimino raw material not containing fluorine atoms is used, there is no possibility that fluorine is generated during film formation, and the substrate is not damaged.
＜第２の実施形態＞
次に、本発明を適用した第２の実施形態について説明する。本実施形態では、第１の実施形態の金属薄膜の製膜方法とは一部異なる構成となっている。このため、図２を用いて本実施形態の金属薄膜の製膜方法について説明する。
<Second Embodiment>
Next, a second embodiment to which the present invention is applied will be described. In this embodiment, the metal thin film forming method of the first embodiment is partially different. For this reason, the metal thin film forming method of the present embodiment will be described with reference to FIG.
図２中に示すステップＳ２１〜Ｓ２７は、それぞれ下記に示す内容となっている。
Ｓ２１：基板搬送ステップ（図１中のＳ１１に対応）
Ｓ２２：基板加熱ステップ（図１中のＳ１２に対応）
Ｓ２３：アミノイミノ原料及び含窒素反応ガスの同時供給ステップ
Ｓ２４：パージガスの供給ステップ（図１中のＳ１６に対応）
Ｓ２５：水素ガスの供給ステップ（図１中のＳ１７に対応）
Ｓ２６：パージガスの供給ステップ（図１中のＳ１８に対応）
Ｓ２７：基板取り出しステップ（図１中のＳ１９に対応）
Steps S21 to S27 shown in FIG. 2 have the following contents, respectively.
S21: Substrate transport step (corresponding to S11 in FIG. 1)
S22: Substrate heating step (corresponding to S12 in FIG. 1)
S23: Aminoimino raw material and nitrogen-containing reaction gas simultaneous supply step S24: Purge gas supply step (corresponding to S16 in FIG. 1)
S25: Hydrogen gas supply step (corresponding to S17 in FIG. 1)
S26: Purge gas supply step (corresponding to S18 in FIG. 1)
S27: Substrate removal step (corresponding to S19 in FIG. 1)
本実施形態の金属薄膜の製膜方法は、図２中に示すステップＳ２３に示すように、基板の加熱後、チャンバ内にアミノイミノ原料と含窒素反応ガスと同時に供給する点で上述した第１実施形態と異なっている。換言すると、金属窒化膜を形成する第１工程において、上述した第１実施形態ではアミノイミノ原料（原料ガス）を供給した後に含窒素反応ガスを供給する（すなわち、ステップＳ１３〜Ｓ１５の３ステップで行う）のに対して、本実施形態ではアミノイミノ原料と含窒素反応ガスとを同時に供給する（すなわち、ステップＳ２３の１ステップで行う）点で異なる構成となっている。 As shown in step S23 in FIG. 2, the metal thin film forming method of the present embodiment is the first implementation described above in that after the substrate is heated, the aminoimino raw material and the nitrogen-containing reactive gas are supplied into the chamber at the same time. It is different from the form. In other words, in the first step of forming the metal nitride film, in the first embodiment described above, the nitrogen-containing reactive gas is supplied after supplying the aminoimino raw material (raw material gas) (that is, performed in three steps S13 to S15). On the other hand, the present embodiment is different in that the aminoimino raw material and the nitrogen-containing reactive gas are supplied simultaneously (that is, performed in one step of step S23).
しかしながら、本実施形態の金属薄膜の製膜方法によれば、第１実施形態と同様に、チャンバ内の基板にアミノイミノ原料と含窒素反応ガスと同時に供給する（ステップＳ２３）ことにより、加熱された基板表面でアミノイミノ原料と含窒素反応ガスとを反応させて金属窒化膜を形成することができる。 However, according to the metal thin film forming method of the present embodiment, as in the first embodiment, the substrate is heated by supplying the aminoimino raw material and the nitrogen-containing reactive gas simultaneously to the substrate in the chamber (step S23). A metal nitride film can be formed by reacting an aminoimino raw material with a nitrogen-containing reactive gas on the substrate surface.
また、本実施形態の金属薄膜の製膜方法によれば、チャンバ内の基板にアミノイミノ原料と含窒素反応ガスと同時に供給する（ステップＳ２３）ため、第１実施形態における第１工程よりも金属窒化膜の膜厚を厚く製膜することができる。しかしながら、窒素原子を除去する第２工程を考慮して、第１工程で製膜する金属窒化膜の膜厚は、１０ｎｍ未満とすることが好ましい。 Further, according to the metal thin film forming method of the present embodiment, since the aminoimino raw material and the nitrogen-containing reactive gas are supplied simultaneously to the substrate in the chamber (step S23), the metal nitridation is performed more than the first step in the first embodiment. The film can be formed thick. However, considering the second step of removing nitrogen atoms, the thickness of the metal nitride film formed in the first step is preferably less than 10 nm.
ところで、プロセス装置のチャンバ内に、アミノイミノ原料、含窒素反応ガス及び水素ガスを供給する順番の組合せとしては、図３〜図６に示すフローチャートを例示することができる。ここで、図３に示すフローチャートでは、ステップＳ３７の含窒素反応ガスの供給の前に、ステップＳ３５において水素ガスを供給する構成となっている。また、図４に示すフローチャートでは、ステップＳ４５において含窒素反応ガスと水素ガスとを同時に供給する構成となっている。また、図５に示すフローチャートでは、ステップＳ５５窒素反応ガスの供給の前に、ステップＳ５３においてアミノイミノ原料と同時に水素ガスを供給する構成となっている。また、図６に示すフローチャートでは、ステップＳ６３においてアミノイミノ原料、含窒素反応ガス及び水素ガスを同時に供給する構成となっている。 By the way, as a combination of the order of supplying the aminoimino raw material, the nitrogen-containing reaction gas, and the hydrogen gas into the chamber of the process apparatus, the flowcharts shown in FIGS. 3 to 6 can be exemplified. Here, in the flowchart shown in FIG. 3, the hydrogen gas is supplied in step S <b> 35 before the supply of the nitrogen-containing reaction gas in step S <b> 37. Moreover, in the flowchart shown in FIG. 4, it has the structure which supplies a nitrogen-containing reaction gas and hydrogen gas simultaneously in step S45. In the flowchart shown in FIG. 5, hydrogen gas is supplied simultaneously with the aminoimino raw material in step S53 before supplying the nitrogen reactive gas in step S55. In the flowchart shown in FIG. 6, the aminoimino raw material, the nitrogen-containing reaction gas, and the hydrogen gas are simultaneously supplied in step S63.
しかしながら、図３〜図６に示すフローチャートでは、いずれも含窒素反応ガスの供給の後に水素ガスを供給する構成（すなわち、金属窒化膜を形成した後に、水素ガスを供給する構成）とはなっていないため、当該図３〜図６に示すフローチャートによって製膜された金属薄膜は、いずれも上述した第１及び第２実施形態で得られるような高純度の金属薄膜とはならない。例えば、図３及び図４に示すフローチャートによって製膜された金属薄膜は、膜中に炭素原子（Ｃ）が取り残されてしまうため、タングステン炭窒化膜（ＷＣＮ膜）となる。 However, the flowcharts shown in FIGS. 3 to 6 are all configured to supply hydrogen gas after supplying the nitrogen-containing reaction gas (that is, to supply hydrogen gas after forming the metal nitride film). Therefore, none of the metal thin films formed by the flowcharts shown in FIGS. 3 to 6 is a high-purity metal thin film as obtained in the first and second embodiments described above. For example, the metal thin film formed by the flowcharts shown in FIGS. 3 and 4 becomes a tungsten carbonitride film (WCN film) because carbon atoms (C) are left behind in the film.
これに対して、上述した第１及び第２実施形態の金属薄膜の製膜方法では、いずれも含窒素反応ガスの供給の後に水素ガスを供給する構成（すなわち、金属窒化膜を形成した後に、水素ガスを供給する構成）となっているため、元素組成で１ａｔ％以下の高純度の金属薄膜を製膜することができる。 On the other hand, in the metal thin film forming methods of the first and second embodiments described above, the configuration in which hydrogen gas is supplied after the supply of the nitrogen-containing reaction gas (that is, after forming the metal nitride film, Therefore, a high-purity metal thin film having an elemental composition of 1 at% or less can be formed.
以下、具体例を示す。
なお、以下に示す実施例及び比較例における製膜は、コールドウォールの基板加熱式ステンレスチャンバを用いて実施した。また、元素組成は、Ｘ線光電子分光法（アルバックファイ社製、以下ＸＰＳと略す）によってスペクトル強度から測定した。このＸＰＳによる元素組成の検出下限は１ａｔ％である。また、膜厚は、分光エリプソメトリー（Ｓｏｐｒａ社製）用いた観察によって評価した。
Specific examples are shown below.
The film formation in the following examples and comparative examples was performed using a cold wall substrate heating type stainless steel chamber. The elemental composition was measured from the spectral intensity by X-ray photoelectron spectroscopy (manufactured by ULVAC-PHI, hereinafter abbreviated as XPS). The lower limit of detection of the element composition by XPS is 1 at%. The film thickness was evaluated by observation using spectroscopic ellipsometry (manufactured by Sopra).
（実施例１）
有機金属原料として、下記式（２）に示したビス（ターシャリーブチルイミノ）ビス（ジメチルアミノ）タングステンを用いて、タングステン膜の製膜を実施した。
先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムを、３０ｓｃｃｍのアンモニアと同時に基板表面に搬送した。このとき、ステンレスチャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。次に、原料ガスおよびアンモニアガスの供給を約５分間続け、これにより、基板表面上にタングステン窒化膜２ｎｍを製膜した。得られたタングステン窒化膜をステンレスチャンバより取り出し、組成を調べた結果を下記の表１に示す。
Example 1
A tungsten film was formed using bis (tertiarybutylimino) bis (dimethylamino) tungsten represented by the following formula (2) as the organometallic raw material.
First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 30 sccm of ammonia by bubbling. At this time, the total pressure of the stainless steel chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. Next, the supply of the source gas and the ammonia gas was continued for about 5 minutes, thereby forming a tungsten nitride film of 2 nm on the substrate surface. The obtained tungsten nitride film was taken out from the stainless steel chamber and the composition was examined. The results are shown in Table 1 below.
次に、一度取り出したタングステン窒化膜を、５０Ｔｏｒｒ（約６．６ｋＰａ）の水素雰囲気で約４００℃に加熱して１５分間保持した。処理後の薄膜を取り出して、組成を調べたところ、下記の表１に示した結果となり、窒素が除去されていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ、３．０×１０−７Ω・ｍであった。 Next, the tungsten nitride film once taken out was heated to about 400 ° C. in a hydrogen atmosphere of 50 Torr (about 6.6 kPa) and held for 15 minutes. The treated thin film was taken out and the composition was examined. The results shown in Table 1 below were obtained, and it was confirmed that nitrogen was removed. Moreover, when the resistivity of the thin film after a process was investigated by the 4-terminal method, it was 3.0 * 10 <-7> ohm * m.
（実施例２）
有機金属原料として、上記式（２）に示した原料を用いてタングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムを、３０ｓｃｃｍのアンモニアと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。次に、原料ガスおよびアンモニアガスの供給を約５分間続け、これにより、基板表面上にタングステン窒化膜２ｎｍを製膜した。
(Example 2)
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 30 sccm of ammonia by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. Next, the supply of the source gas and the ammonia gas was continued for about 5 minutes, thereby forming a tungsten nitride film of 2 nm on the substrate surface.
次いで、チャンバから取り出すことなく、引き続き５０Ｔｏｒｒ（約６．６ｋＰａ）の水素雰囲気で４００℃に加熱して１５分間保持した。得られた薄膜をチャンバより取り出して組成を調べたところ、下記の表１に示した結果となり、タングステン膜が得られていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ、３．０×１０−７Ω・ｍであった。 Next, without removing from the chamber, it was continuously heated to 400 ° C. in a hydrogen atmosphere of 50 Torr (about 6.6 kPa) and held for 15 minutes. The obtained thin film was taken out of the chamber and the composition was examined. The results shown in Table 1 below were obtained, and it was confirmed that a tungsten film was obtained. Moreover, when the resistivity of the thin film after a process was investigated by the 4-terminal method, it was 3.0 * 10 <-7> ohm * m.
（実施例３）
有機金属原料として、上記式（２）に示した原料を用いてタングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、３０ｓｃｃｍのアンモニアガスと同時に約３５０℃に加熱した基板表面に６秒間供給した（製膜工程）。引き続いて、ヘリウムガス６０ｓｃｃｍを３秒間流通させて、チャンバ内に残った原料ガスを排気（パージ工程１）した後、水素ガス６０ｓｃｃｍを同じく約３５０℃に加熱した基板に３秒間供給した（窒素除去工程）。この後、ヘリウムガス６０ｓｃｃｍを３秒間流通させて、チャンバ内に残った水素ガスを排気した（パージ工程２）。
Example 3
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was supplied by bubbling to the substrate surface heated to about 350 ° C. simultaneously with 30 sccm of ammonia gas (film forming step). Subsequently, 60 sccm of helium gas was circulated for 3 seconds to exhaust the raw material gas remaining in the chamber (purge process 1), and then hydrogen gas 60 sccm was supplied to the substrate heated to about 350 ° C. for 3 seconds (nitrogen removal). Process). Thereafter, 60 sccm of helium gas was circulated for 3 seconds to exhaust the hydrogen gas remaining in the chamber (purge process 2).
このとき、チャンバの全圧を０．３Ｔｏｒｒ（約４０Ｐａ）に保ち、製膜工程、パージ工程１、窒素除去工程及びパージ工程２を、３００回繰り返した。これにより、タングステン窒化膜２７ｎｍを製膜した。得られた薄膜をチャンバより取り出して組成を調べたところ、下記の表１に示した結果となり、タングステン膜が得られていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ、３．０×１０−７Ω・ｍであった。 At this time, the total pressure in the chamber was maintained at 0.3 Torr (about 40 Pa), and the film forming process, the purge process 1, the nitrogen removing process, and the purge process 2 were repeated 300 times. As a result, a tungsten nitride film of 27 nm was formed. The obtained thin film was taken out of the chamber and the composition was examined. The results shown in Table 1 below were obtained, and it was confirmed that a tungsten film was obtained. Moreover, when the resistivity of the thin film after a process was investigated by the 4-terminal method, it was 3.0 * 10 <-7> ohm * m.
（実施例４）
有機金属原料として、上記式（２）に示した原料を用いてタングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、約３５０℃に加熱した基板表面に６秒間供給した（Ｗ吸着工程）。引き続いて、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバに残った原料を排気（パージ工程１）した後、３０ｓｃｃｍのアンモニアガスを３秒間供給して、上記Ｗ吸着工程で吸着した原料を分解した（反応工程）。引き続いて、ヘリウム３０ｓｃｃｍを３秒間流通させて、チャンバ内に残ったアンモニアガスを排気（パージ工程２）した後、水素ガス３０ｓｃｃｍを同じく約３５０℃に加熱した基板に３秒間供給した（窒素除去工程）。この後、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバ内に残った水素ガスを排気した（パージ工程３）。
Example 4
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material by bubbling was supplied to the substrate surface heated to about 350 ° C. for 6 seconds (W adsorption process). Subsequently, 30 sccm of helium gas was circulated for 3 seconds to exhaust the raw material remaining in the chamber (purge process 1), and then 30 sccm of ammonia gas was supplied for 3 seconds to decompose the raw material adsorbed in the W adsorption process. (Reaction process). Subsequently, 30 sccm of helium was circulated for 3 seconds to exhaust the ammonia gas remaining in the chamber (purge process 2), and then 30 sccm of hydrogen gas was supplied to the substrate heated to about 350 ° C. for 3 seconds (nitrogen removal process) ). Thereafter, 30 sccm of helium gas was circulated for 3 seconds to exhaust the hydrogen gas remaining in the chamber (purge process 3).
このとき、チャンバの全圧を０．３Ｔｏｒｒ（約４０Ｐａ）に保ち、Ｗ吸着工程、パージ工程１、反応工程、パージ工程２、窒素除去工程及びパージ工程３を３００回繰り返した。これにより、タングステン窒化膜１３ｎｍを製膜した。得られた薄膜をチャンバより取り出して組成を調べたところ、下記の表１に示した結果となり、タングステン膜が得られていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ３．０×１０−７Ω・ｍであった。 At this time, the total pressure in the chamber was maintained at 0.3 Torr (about 40 Pa), and the W adsorption step, purge step 1, reaction step, purge step 2, nitrogen removal step and purge step 3 were repeated 300 times. As a result, a tungsten nitride film of 13 nm was formed. The obtained thin film was taken out of the chamber and the composition was examined. The results shown in Table 1 below were obtained, and it was confirmed that a tungsten film was obtained. Further, when the resistivity of the thin film after the treatment by the four-terminal method was examined, it was 3.0 × 10 −7 Ω · m.
（比較例１）
有機金属原料として、上記式（２）に示した原料を用いてタングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、１５ｓｃｃｍのアンモニアガス、１５ｓｃｃｍの水素ガスと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。原料ガス、アンモニアガス及び水素ガスの供給を５分間続け、得られた薄膜をステンレスチャンバより取り出し、組成を調べた結果を下記の表１に示した。また、４端子法で処理後の薄膜の抵抗率を調べたところ１．０×１０−４Ω・ｍであった。
(Comparative Example 1)
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 15 sccm of ammonia gas and 15 sccm of hydrogen gas by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. The supply of the source gas, ammonia gas and hydrogen gas was continued for 5 minutes, the obtained thin film was taken out from the stainless steel chamber, and the composition was examined. The results are shown in Table 1 below. Further, when the resistivity of the thin film after the treatment was examined by the four-terminal method, it was 1.0 × 10 −4 Ω · m.
（比較例２）
有機金属原料として、上記式（２）に示した原料を用いてタングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、３０ｓｃｃｍの水素ガスと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。原料ガスおよび水素ガスの供給を５分間続け、得られた薄膜をステンレスチャンバより取り出し、組成を調べた結果を下記の表１に示した。また、４端子法で処理後の薄膜の抵抗率を調べたところ、３．０×１０−４Ω・ｍであった。
(Comparative Example 2)
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 30 sccm of hydrogen gas by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. The supply of the source gas and the hydrogen gas was continued for 5 minutes, the obtained thin film was taken out from the stainless steel chamber, and the composition was examined. The results are shown in Table 1 below. Moreover, when the resistivity of the processed thin film was investigated by the 4-terminal method, it was 3.0 × 10 −4 Ω · m.
（比較例３）
有機金属原料として、上記式（２）に示した原料を用いてタングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、３０ｓｃｃｍのアンモニアガスと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。原料ガスおよびアンモニアガスの供給を５分間続け、これにより、タングステン窒化膜２ｎｍを製膜した。
(Comparative Example 3)
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 30 sccm of ammonia gas by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. The supply of the source gas and ammonia gas was continued for 5 minutes, thereby forming a tungsten nitride film of 2 nm.
次に、一度取り出したタングステン窒化膜を、５０Ｔｏｒｒ（約６．６ｋＰａ）の窒素雰囲気で４００℃に加熱し、１５分間保持した。処理後の薄膜を取り出して、組成を調べたところ、下記の表１に示した結果となり、窒素が除去されていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ１．０×１０−４Ω・ｍであった。 Next, the tungsten nitride film once taken out was heated to 400 ° C. in a nitrogen atmosphere of 50 Torr (about 6.6 kPa) and held for 15 minutes. The treated thin film was taken out and the composition was examined. The results shown in Table 1 below were obtained, and it was confirmed that nitrogen was removed. Further, when the resistivity of the thin film after the treatment was examined by the four-terminal method, it was 1.0 × 10 −4 Ω · m.
（比較例４）
有機金属原料として、上記式（２）に示した原料を用いてタングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、約３５０℃に加熱した基板表面に６秒間供給した（Ｗ吸着工程）。引き続いて、ヘリウムガス６０ｓｃｃｍを３秒間流通させて、チャンバ内に残った原料ガスを排気（パージ工程１）した後、３０ｓｃｃｍのアンモニアガスと３０ｓｃｃｍの水素ガスとを同時に３秒間供給して上記Ｗ吸着工程で吸着した原料を分解した（反応工程）。引き続いて、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバ内に残ったアンモニアガスを排気（パージ工程２）した。このとき、チャンバの全圧を０．３Ｔｏｒｒ（約４０Ｐａ）に保ち、Ｗ吸着工程、パージ工程１、反応工程及びパージ工程２を３００回繰り返した。これにより、タングステン窒化膜１５ｎｍを製膜した。得られた薄膜をチャンバより取り出して組成を調べたところ、下記の表１に示した結果となり、タングステン膜が得られていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ２．０×１０−４Ω・ｍであった。
(Comparative Example 4)
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material by bubbling was supplied to the substrate surface heated to about 350 ° C. for 6 seconds (W adsorption process). Subsequently, 60 sccm of helium gas was circulated for 3 seconds to exhaust the raw material gas remaining in the chamber (purging process 1), and then 30 sccm of ammonia gas and 30 sccm of hydrogen gas were simultaneously supplied for 3 seconds to perform the W adsorption. The raw material adsorbed in the process was decomposed (reaction process). Subsequently, 30 sccm of helium gas was circulated for 3 seconds to exhaust the ammonia gas remaining in the chamber (purge process 2). At this time, the total pressure in the chamber was maintained at 0.3 Torr (about 40 Pa), and the W adsorption process, the purge process 1, the reaction process, and the purge process 2 were repeated 300 times. Thereby, a tungsten nitride film of 15 nm was formed. The obtained thin film was taken out of the chamber and the composition was examined. The results shown in Table 1 below were obtained, and it was confirmed that a tungsten film was obtained. Moreover, it was 2.0 * 10 <-4> ( omega | ohm) * m when the resistivity of the thin film after processing by the 4 terminal method was investigated.
（実施例５）
有機金属原料として、下記式（３）に示したビス（ターシャリーブチルイミノ）ビス（ジメチルアミノ）モリブデンを用いて、モリブデン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、３０ｓｃｃｍのアンモニアガスと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。原料ガスおよびアンモニアガスの供給を５分間続け、これにより、モリブデン窒化膜２ｎｍを製膜した。得られたモリブデン窒化膜をステンレスチャンバより取り出し、組成を調べた結果、Ｍｏ：４５ａｔ％、窒素：５５ａｔ％であった。
(Example 5)
A molybdenum film was formed using bis (tertiarybutylimino) bis (dimethylamino) molybdenum represented by the following formula (3) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 30 sccm of ammonia gas by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. The supply of source gas and ammonia gas was continued for 5 minutes, thereby forming a molybdenum nitride film of 2 nm. The obtained molybdenum nitride film was taken out from the stainless steel chamber and the composition was examined. As a result, Mo was 45 at% and nitrogen was 55 at%.
次に、一度取り出したモリブデン窒化膜を、５０Ｔｏｒｒ（約６．６ｋＰａ）の水素雰囲気で４００℃に加熱し、１５分間保持した。処理後の薄膜を取り出して、組成を調べた結果、Ｍｏ：１００ａｔ％となり、窒素が除去されていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ、４．０×１０−７Ω・ｍであった。 Next, the molybdenum nitride film once taken out was heated to 400 ° C. in a hydrogen atmosphere of 50 Torr (about 6.6 kPa) and held for 15 minutes. The processed thin film was taken out and the composition was examined. As a result, it was confirmed that Mo was 100 at% and nitrogen was removed. Further, when the resistivity of the thin film after the treatment by the four-terminal method was examined, it was 4.0 × 10 −7 Ω · m.
（比較例５）
有機金属原料として、下記式（３）に示した原料を用いて、モリブデン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、１５ｓｃｃｍのアンモニアガス、１５ｓｃｃｍの水素ガスと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。原料ガス、アンモニアガス及び水素ガスの供給を５分間続け、得られた薄膜をステンレスチャンバより取り出し、組成を調べた結果、Ｍｏ：４０ａｔ％、窒素：３０ａｔ％、炭素：３０ａｔ％であった。また、４端子法で処理後の薄膜の抵抗率を調べたところ１．３×１０−４Ω・ｍであった。
(Comparative Example 5)
A molybdenum film was formed using the raw material represented by the following formula (3) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 15 sccm of ammonia gas and 15 sccm of hydrogen gas by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. The supply of the raw material gas, ammonia gas and hydrogen gas was continued for 5 minutes. The obtained thin film was taken out from the stainless steel chamber and examined for the composition. As a result, Mo: 40 at%, nitrogen: 30 at%, and carbon: 30 at%. Further, when the resistivity of the thin film after the treatment was examined by the four-terminal method, it was 1.3 × 10 −4 Ω · m.
（実施例６）
有機金属原料として、下記式（４）に示したターシャリーブチルイミノトリス（ジエチルアミノ）タンタルを用いて、タンタル膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、３０ｓｃｃｍのアンモニアガスと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。原料ガスおよびアンモニアガスの供給を５分間続け、これにより、タンタル窒化膜２ｎｍを製膜した。得られたタンタル窒化膜をステンレスチャンバより取り出し、組成を調べた結果、Ｔａ：４５ａｔ％、窒素：５５ａｔ％であった。
(Example 6)
A tantalum film was formed using tertiary butyliminotris (diethylamino) tantalum represented by the following formula (4) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 30 sccm of ammonia gas by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. The supply of source gas and ammonia gas was continued for 5 minutes, thereby forming a tantalum nitride film of 2 nm. As a result of taking out the obtained tantalum nitride film from the stainless steel chamber and examining the composition, Ta: 45 at% and nitrogen: 55 at%.
次に、取り出したタンタル窒化膜を、５０Ｔｏｒｒ（約６．６ｋＰａ）の水素雰囲気で約４００℃に加熱し、１５分間保持した。処理後の薄膜を取り出して、組成を調べた結果、Ｔａ：８０ａｔ％、窒素：２０ａｔ％となり、窒素が部分的に除去されていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ９．０×１０−７Ω・ｍであった。 Next, the extracted tantalum nitride film was heated to about 400 ° C. in a hydrogen atmosphere of 50 Torr (about 6.6 kPa) and held for 15 minutes. The processed thin film was taken out and the composition was examined. As a result, Ta: 80 at% and nitrogen: 20 at% were obtained, and it was confirmed that nitrogen was partially removed. Further, when the resistivity of the thin film after the treatment by the four-terminal method was examined, it was 9.0 × 10 −7 Ω · m.
（実施例７）
有機金属原料として、下記式（４）に示した原料を用いて、タンタル膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、約３５０℃に加熱した基板表面に６秒間供給した（Ｔａ吸着工程）。引き続いて、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバに残った原料ガスを排気（パージ工程１）した後、３０ｓｃｃｍのアンモニアガスを３秒間供給して上記Ｔａ吸着工程で吸着した原料を分解した（反応工程）。引き続いて、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバ内に残ったアンモニアガスを排気（パージ工程２）した後、水素ガス３０ｓｃｃｍを同じく約３５０℃に加熱した基板に３秒間供給した（窒素除去工程）。この後、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバ内に残った水素ガスを排気した（パージ工程３）。このとき、チャンバの全圧を０．３Ｔｏｒｒ（約４０Ｐａ）に保ち、Ｔａ吸着工程、パージ工程１、反応工程、パージ工程２、窒素除去工程及びパージ工程３を３００回繰り返した。これにより、タンタル窒化膜１３ｎｍを製膜した。得られた薄膜をチャンバより取り出して組成を調べたところ、タンタル膜が得られていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ３．５×１０−７Ω・ｍであった。
(Example 7)
A tantalum film was formed using the raw material represented by the following formula (4) as the organic metal raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material by bubbling was supplied to the substrate surface heated to about 350 ° C. for 6 seconds (Ta adsorption step). Subsequently, 30 sccm of helium gas was circulated for 3 seconds to exhaust the raw material gas remaining in the chamber (purge process 1), and then 30 sccm of ammonia gas was supplied for 3 seconds to decompose the raw material adsorbed in the Ta adsorption process. (Reaction process). Subsequently, 30 sccm of helium gas was allowed to flow for 3 seconds to exhaust the ammonia gas remaining in the chamber (purging process 2), and then 30 sccm of hydrogen gas was supplied to the substrate that was also heated to about 350 ° C. for 3 seconds (removal of nitrogen) Process). Thereafter, 30 sccm of helium gas was circulated for 3 seconds to exhaust the hydrogen gas remaining in the chamber (purge process 3). At this time, the total pressure in the chamber was maintained at 0.3 Torr (about 40 Pa), and the Ta adsorption process, purge process 1, reaction process, purge process 2, nitrogen removal process, and purge process 3 were repeated 300 times. Thereby, a tantalum nitride film of 13 nm was formed. When the obtained thin film was taken out from the chamber and the composition was examined, it was confirmed that a tantalum film was obtained. Further, when the resistivity of the thin film after the treatment by the four-terminal method was examined, it was 3.5 × 10 −7 Ω · m.
（比較例６）
有機金属原料として、下記式（４）に示した原料を用いて、タンタル膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを、１５ｓｃｃｍのアンモニアガス、１５ｓｃｃｍの水素ガスと同時に基板表面に搬送した。このとき、チャンバの全圧を３Ｔｏｒｒ（約４００Ｐａ）に保ち、基板温度を約３５０℃に加熱した。原料ガス、アンモニアガス、水素ガスの供給を５分間続け、得られた薄膜をステンレスチャンバより取り出し、組成を調べたところ、Ｔａ：３５ａｔ％、窒素：２５ａｔ％、炭素：３０ａｔ％であった。また、４端子法で処理後の薄膜の抵抗率を調べたところ４．０×１０−４Ω・ｍであった。
(Comparative Example 6)
A tantalum film was formed using the raw material represented by the following formula (4) as the organic metal raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was transferred to the substrate surface simultaneously with 15 sccm of ammonia gas and 15 sccm of hydrogen gas by bubbling. At this time, the total pressure in the chamber was maintained at 3 Torr (about 400 Pa), and the substrate temperature was heated to about 350 ° C. The supply of the source gas, ammonia gas, and hydrogen gas was continued for 5 minutes, and the obtained thin film was taken out from the stainless steel chamber and examined for the composition. Ta: 35 at%, nitrogen: 25 at%, carbon: 30 at%. Further, when the resistivity of the thin film after the treatment was examined by the four-terminal method, it was 4.0 × 10 −4 Ω · m.
（実施例８）
有機金属原料として、上記式（２）に示した原料を用いて、タングステン膜の製膜を実施した。先ず、有機金属ボトルを４０℃に加熱し、バブリングによって有機金属原料を同伴した３０ｓｃｃｍヘリウムガスを約３５０℃に加熱した基板表面に６秒間供給した（Ｗ吸着工程）。引き続いて、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバに残った原料ガスを排気（パージ工程１）した後、３０ｓｃｃｍのモノメチルヒドラジンを３秒間供給して上記Ｗ吸着工程で吸着した原料を分解した（反応工程）。引き続いて、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバ内に残ったモノメチルヒドラジンを排気（パージ工程２）した後、水素ガス３０ｓｃｃｍを同じく約３５０℃に加熱した基板に３秒間供給した（窒素除去工程）。この後、ヘリウムガス３０ｓｃｃｍを３秒間流通させて、チャンバ内に残った水素ガスを排気した（パージ工程３）。このとき、チャンバの全圧を０．３Ｔｏｒｒ（約４０Ｐａ）に保ち、Ｗ吸着工程、パージ工程１、反応工程、パージ工程２、窒素除去工程及びパージ工程３を３００回繰り返した。これにより、タングステン窒化膜１５ｎｍを製膜した。得られた薄膜をチャンバより取り出して組成を調べたところ、Ｗ：１００％（炭素および窒素は検出下限以下）であり、タングステン膜が得られていることを確認した。また、４端子法で処理後の薄膜の抵抗率を調べたところ、３．２×１０−７Ω・ｍであった。
(Example 8)
A tungsten film was formed using the raw material represented by the above formula (2) as the organometallic raw material. First, the organometallic bottle was heated to 40 ° C., and 30 sccm helium gas accompanied by the organometallic raw material was supplied by bubbling to the substrate surface heated to about 350 ° C. for 6 seconds (W adsorption process). Subsequently, 30 sccm of helium gas was circulated for 3 seconds to exhaust the raw material gas remaining in the chamber (purging process 1), and then 30 sccm of monomethylhydrazine was supplied for 3 seconds to decompose the raw material adsorbed in the W adsorption process. (Reaction process). Subsequently, 30 sccm of helium gas was allowed to flow for 3 seconds to exhaust the monomethylhydrazine remaining in the chamber (purging process 2), and then 30 sccm of hydrogen gas was supplied to the substrate that was also heated to about 350 ° C. for 3 seconds (removal of nitrogen) Process). Thereafter, 30 sccm of helium gas was circulated for 3 seconds to exhaust the hydrogen gas remaining in the chamber (purge process 3). At this time, the total pressure in the chamber was maintained at 0.3 Torr (about 40 Pa), and the W adsorption step, purge step 1, reaction step, purge step 2, nitrogen removal step and purge step 3 were repeated 300 times. Thereby, a tungsten nitride film of 15 nm was formed. When the obtained thin film was taken out from the chamber and the composition was examined, it was confirmed that W was 100% (carbon and nitrogen were below the detection lower limit), and a tungsten film was obtained. Further, when the resistivity of the thin film after the treatment by the four-terminal method was examined, it was 3.2 × 10 −7 Ω · m.
Claims (8)
基板の表面に、下記式（１）で示される有機金属化学種を含む原料ガスと含窒素反応ガスとを供給して、金属窒化膜を形成する第１工程と、
前記基板の表面に水素ガスを供給して、前記金属窒化膜中の窒素原子を除去する第２工程と、を含むことを特徴とする金属薄膜の製膜方法。
また、Ｍ１は、第５族又は第６族の金属原子であり、Ｍ１が第５族である場合にｐ＋２ｑ＝５であり、Ｍ１が第６族である場合にｐ＋２ｑ＝６である。 A method of forming a metal thin film on the surface of a substrate by a thin film deposition method using a chemical reaction,
A first step of forming a metal nitride film by supplying a source gas containing a metalorganic species represented by the following formula (1) and a nitrogen-containing reaction gas to the surface of the substrate;
And a second step of removing nitrogen atoms in the metal nitride film by supplying hydrogen gas to the surface of the substrate.
Further, M 1 is a Group 5 or Group 6 metal atoms are p + 2q = 5 when M 1 is a Group 5 is the p + 2q = 6 when M 1 is a Group 6 .
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