JP2000031109A - Method of drying - Google Patents
Method of dryingInfo
- Publication number
- JP2000031109A JP2000031109A JP10193483A JP19348398A JP2000031109A JP 2000031109 A JP2000031109 A JP 2000031109A JP 10193483 A JP10193483 A JP 10193483A JP 19348398 A JP19348398 A JP 19348398A JP 2000031109 A JP2000031109 A JP 2000031109A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- drying
- gas
- wafer
- catalyzer
- 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
Landscapes
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、半導体製造プロセ
スの乾燥方法に係り、より詳細には気体中に発生させた
水素ラジカルを使用しウエハの乾燥を行う方法に関す
る。The present invention relates to a method for drying a semiconductor manufacturing process, and more particularly to a method for drying a wafer using hydrogen radicals generated in a gas.
【0002】[0002]
【従来の技術】半導体製造プロセスのウェットプロセス
において、最終工程にはそれ以前のプロセスでウエハ上
に付着した水分を除去する工程が行われている。乾燥プ
ロセスには、スピンドライ乾燥、IPA(2−プロパノ
ール)蒸気乾燥、マランゴニードライ乾燥などの手法が
あるがいずれも水分を除去する効果のみであった。2. Description of the Related Art In a wet process of a semiconductor manufacturing process, a step of removing moisture adhering to a wafer in an earlier process is performed as a final step. The drying process includes methods such as spin drying, IPA (2-propanol) vapor drying, and Marangoni drying, all of which have only the effect of removing water.
【0003】シリコン基板のウエット洗浄工程において
フッ酸を含有した洗浄液での洗浄後の基板表面は最表面
のシリコン原子は水素原子と結びつき、最表面が水素原
子で終端した構造を取っている。この水素終端したシリ
コン表面は、化学的に非常に安定な表面といわれてい
る。しかし、全てのシリコン原子が水素原子と結合して
いるわけではなく、中にはシリコン原子がそのまま表面
に現れている未結合状態やフッ素原子が結合したシリコ
ン原子も存在が確認されている。このようなシリコン原
子は、化学的に非常に不安定であり酸化を受けやすいサ
イトとなっている。[0003] In a wet cleaning step of a silicon substrate, the substrate surface after cleaning with a cleaning solution containing hydrofluoric acid has a structure in which silicon atoms on the outermost surface are linked to hydrogen atoms and the outermost surface is terminated by hydrogen atoms. This hydrogen-terminated silicon surface is said to be a chemically very stable surface. However, not all silicon atoms are bonded to hydrogen atoms, and it has been confirmed that silicon atoms are present in the unbonded state as they are on the surface as well as silicon atoms to which fluorine atoms are bonded. Such a silicon atom is a site that is extremely unstable chemically and is susceptible to oxidation.
【0004】シリコン基板のウエット洗浄工程において
フッ酸を含有した洗浄液での洗浄後の基板は表面に酸化
膜のない状態である。しかし、この状態の基板は各種パ
ーティクルの付着を引き起こしやすい。そのため、フッ
酸にオゾンを添加した洗浄液が開発されているが、従来
のフッ酸のみの洗浄工程に比べ水素終端量が弱いことが
わかっている。In a wet cleaning process for a silicon substrate, the substrate after cleaning with a cleaning solution containing hydrofluoric acid has no oxide film on the surface. However, the substrate in this state tends to cause adhesion of various particles. Therefore, although a cleaning solution in which ozone is added to hydrofluoric acid has been developed, it has been found that the amount of hydrogen termination is weaker than the conventional cleaning process using only hydrofluoric acid.
【0005】[0005]
【発明が解決しようとする課題】本発明は、半導体の乾
燥工程において、水分を乾燥するとともにシリコン原子
の水素終端化を助長する乾燥方法の提供を目的とする。SUMMARY OF THE INVENTION An object of the present invention is to provide a drying method for drying moisture and promoting hydrogen termination of silicon atoms in a semiconductor drying step.
【0006】[0006]
【課題を解決するための手段】本発明の乾燥方法は、半
導体製造プロセスのウエハ乾燥工程において、水素ラジ
カルを含有する不活性ガスにより乾燥を行うことを特徴
とする。水素ラジカルを含むガスを乾燥に使用すること
により、酸化膜のないシリコン表面から水分子を脱離さ
せ、同時に水素終端化を促進する。A drying method according to the present invention is characterized in that in a wafer drying step of a semiconductor manufacturing process, drying is performed with an inert gas containing hydrogen radicals. By using a gas containing hydrogen radicals for drying, water molecules are eliminated from the silicon surface without an oxide film, and at the same time, hydrogen termination is promoted.
【0007】[0007]
【作用】本発明においては、まず不活性ガス中に水素を
添加し、加熱した金属触媒を使用することによって水素
ラジカルを発生させ、乾燥後の水素終端化を促進させる
ことが可能となる。ここで使用する触媒は、ラジカル発
生のための触媒効果があれば使用が可能である。例とし
てニッケル、プラチナ等があげられるが、触媒能として
より好ましいのはプラチナの方である。According to the present invention, hydrogen is first added to an inert gas, and hydrogen radicals are generated by using a heated metal catalyst to promote the termination of hydrogen after drying. The catalyst used here can be used as long as it has a catalytic effect for generating radicals. Examples include nickel, platinum and the like, but platinum is more preferred as the catalytic ability.
【0008】金属触媒として使用する場合の形状は、出
来るだけ表面積の大きい形状が好ましい。例えば、チュ
ーブ状のものより、フィルター状のものを使用し金属触
媒と水素の有効接触面積を大きくした方がよい。[0008] When used as a metal catalyst, the shape is preferably as large as possible in surface area. For example, it is better to use a filter-shaped material than a tube-shaped material and increase the effective contact area between the metal catalyst and hydrogen.
【0009】ガスは、ウエハに吹き付ける近傍まで昇温
しておく必要がある。また、ウエハを乾燥させる位置は
ガスが金属触媒をでて出来るだけ近い位置においた方が
よい。これは、ウエハに照射するラジカルの寿命が短い
ためである。特に、ガス出口から30mm離してしまう
と、効果はほとんどない。It is necessary to raise the temperature of the gas up to the vicinity of blowing the gas onto the wafer. Further, it is preferable that the position where the wafer is dried be as close as possible to the gas coming out of the metal catalyst. This is because the lifetime of the radical irradiated on the wafer is short. In particular, there is almost no effect if it is 30 mm away from the gas outlet.
【0010】ウエハに吹き付けるガスの温度は、150
℃以上より効果が見られるが、より好ましくは、200
℃以上350℃以下である。特に、高温部ではラジカル
の効果による水素終端化より水素終端が破壊され、酸化
膜形成の方に反応が進む。[0010] The temperature of the gas blown to the wafer is 150
Although the effect is seen more than ℃, more preferably 200
It is higher than or equal to 350 ° C. In particular, in the high temperature part, the hydrogen termination is destroyed by the hydrogen termination due to the effect of the radical, and the reaction proceeds toward the formation of the oxide film.
【0011】水素濃度は、0.05%より効果があるこ
とがわかった。また、水素濃度の上限は、水素の爆発限
界4.1%以下である事が望ましい。It has been found that the hydrogen concentration is more effective than 0.05%. Further, the upper limit of the hydrogen concentration is desirably not more than a hydrogen explosion limit of 4.1%.
【0012】ここで使用する不活性ガスおよび水素中に
は、出来るだけ水分および酸素がないこと、特に1pp
b以下であることが好ましい。The inert gas and hydrogen used here are as free from moisture and oxygen as possible, especially 1 pp.
b or less is preferable.
【0013】[0013]
【実施例】以下に実施例を挙げて本発明を具体的に説明
するが、本発明がこれら実施例に限定されることがない
ことは言うまでもない。EXAMPLES The present invention will be specifically described below with reference to examples, but it goes without saying that the present invention is not limited to these examples.
【0014】(実施例1)抵抗率3〜7Ω/cmを有す
るn型(100)シリコン基板を97%硫酸と30%過
酸化水素を体積比4:1に混合した薬液で10分間洗浄
を行い、流量1L/分の超純水でリンスを行った後、
0.5wt%フッ酸にて1分間処理し、再び流量1L/
分の超純水でリンスを行った。(Example 1) An n-type (100) silicon substrate having a resistivity of 3 to 7 Ω / cm was washed with a chemical solution in which 97% sulfuric acid and 30% hydrogen peroxide were mixed at a volume ratio of 4: 1 for 10 minutes. After rinsing with ultrapure water at a flow rate of 1 L / min,
Treated with 0.5wt% hydrofluoric acid for 1 minute, and flow rate 1L /
Rinsing with ultrapure water for one minute.
【0015】リンス後、ガス流量10L/分の窒素乾燥
および金属触媒としてニッケルフィルター(有効ろ過面
積13.5cm2)を使用した水素ラジカル乾燥(ガス
組成比:水素:窒素=0.1%:99.9%)を20秒
間行った。After rinsing, dry with nitrogen at a gas flow rate of 10 L / min and dry with hydrogen radicals using a nickel filter (effective filtration area: 13.5 cm 2 ) as a metal catalyst (gas composition ratio: hydrogen: nitrogen = 0.1%: 99). .9%) for 20 seconds.
【0016】この基板を直ちに、大きさ50mm×20
mm(厚さ2mm)断面の角度が60度の平行四辺形型
ゲルマニウムクリスタルをプリズムとして、フーリエ変
換赤外分光装置の多重反射法によりSi−Hピークを観
察した。その結果を表1、表2に示す。Immediately, the substrate is sized 50 mm × 20 mm.
Si-H peaks were observed by a multiple reflection method using a Fourier transform infrared spectrometer using a parallelogram type germanium crystal having a 60 mm angle (thickness: 2 mm) cross section as a prism. The results are shown in Tables 1 and 2.
【0017】[0017]
【表1】 [Table 1]
【0018】[0018]
【表2】 [Table 2]
【0019】(実施例2)抵抗率3〜7Ω/cmを有す
るn型(100)シリコン基板を97%硫酸と30%過
酸化水素を体積比4:1に混合した薬液で10分間洗浄
を行い、流量1L/分の超純水でリンスを行った後、
0.5wt%フッ酸にて1分間処理し、再び流量1L/
分の超純水でリンスを行った。Example 2 An n-type (100) silicon substrate having a resistivity of 3 to 7 Ω / cm was washed for 10 minutes with a chemical solution in which 97% sulfuric acid and 30% hydrogen peroxide were mixed at a volume ratio of 4: 1. After rinsing with ultrapure water at a flow rate of 1 L / min,
Treated with 0.5wt% hydrofluoric acid for 1 minute, and flow rate 1L /
Rinsing with ultrapure water for one minute.
【0020】リンス後、ガス流量10L/分、金属触媒
としてニッケルフィルター(有効ろ過面積13.5cm
2)の水素ラジカル乾燥をガス組成比を変化させ300
℃で20秒間行った。After rinsing, use a nickel filter (effective filtration area 13.5 cm) as a metal catalyst at a gas flow rate of 10 L / min.
2 ) The hydrogen radical drying of 300 was performed by changing the gas composition ratio.
C. for 20 seconds.
【0021】この基板を直ちに、大きさ50mm×20
mm(厚さ2mm)断面の角度が60度の平行四辺形型
ゲルマニウムクリスタルをプリズムとして、フーリエ変
換赤外分光装置の多重反射法によりSi−Hピークを観
察した。その結果を表3に示す。Immediately, this substrate is sized 50 mm × 20 mm.
Si-H peaks were observed by a multiple reflection method using a Fourier transform infrared spectrometer using a parallelogram type germanium crystal having a 60 mm angle (thickness: 2 mm) cross section as a prism. Table 3 shows the results.
【0022】[0022]
【表3】 [Table 3]
【0023】(実施例3)抵抗率3〜7Ω/cmを有す
るn型(100)シリコン基板を97%硫酸と30%過
酸化水素を体積比4:1に混合した薬液で10分間洗浄
を行い、流量1L/分の超純水でリンスを行った後、5
ppmオゾン、0.5wt%フッ酸混合溶液にて1分間
処理し、再び流量1L/分の超純水でリンスを行った。Example 3 An n-type (100) silicon substrate having a resistivity of 3 to 7 Ω / cm was washed for 10 minutes with a chemical solution in which 97% sulfuric acid and 30% hydrogen peroxide were mixed at a volume ratio of 4: 1. After rinsing with ultrapure water at a flow rate of 1 L / min,
The mixture was treated with a mixed solution of ppm ozone and 0.5 wt% hydrofluoric acid for 1 minute, and rinsed again with ultrapure water at a flow rate of 1 L / min.
【0024】リンス後、ガス流量10L/分、金属触媒
としてニッケルフィルター(有効ろ過面積13.5cm
2)の水素ラジカル乾燥(ガス組成比:水素:窒素=
0.1%:99.9%)を300℃で20秒間行った。After rinsing, use a nickel filter (effective filtration area: 13.5 cm) as a metal catalyst at a gas flow rate of 10 L / min.
2 ) Hydrogen radical drying (gas composition ratio: hydrogen: nitrogen =
0.1%: 99.9%) at 300 ° C. for 20 seconds.
【0025】この基板を直ちに、大きさ50mm×20
mm(厚さ2mm)断面の角度が60度の平行四辺形型
ゲルマニウムクリスタルをプリズムとして、フーリエ変
換赤外分光装置の多重反射法によりSi−Hピークを観
察した。その結果を表4に示す。Immediately, this substrate is sized 50 mm × 20 mm.
Si-H peaks were observed by a multiple reflection method using a Fourier transform infrared spectrometer using a parallelogram type germanium crystal having a 60 mm angle (thickness: 2 mm) cross section as a prism. Table 4 shows the results.
【0026】[0026]
【表4】 [Table 4]
【0027】[0027]
【発明の効果】本発明によれば以下の効果が得られる。
従来の乾燥工程に加えて、乾燥後のシリコン表面を化学
的に安定化する機能を付与することができる。According to the present invention, the following effects can be obtained.
In addition to the conventional drying step, a function of chemically stabilizing the dried silicon surface can be provided.
フロントページの続き (72)発明者 大見 忠弘 宮城県仙台市青葉区米ヶ袋2の1の17の 301 (72)発明者 新田 雄久 東京都文京区本郷4丁目1−7 株式会社 ウルトラクリーンテクノロジー開発研究所 内Continued on the front page. (72) Inventor Tadahiro Omi, 1-17-1, Yonegabukuro, Aoba-ku, Sendai-shi, Miyagi 301 (72) Inventor Yuhisa Nitta 4- 1-7 Hongo, Bungo-ku, Tokyo Ultra Clean Co., Ltd. Technology Development Laboratory
Claims (1)
おいて、水素ラジカルを含有する不活性ガスにより乾燥
を行うことを特徴とする乾燥方法。1. A method of drying a wafer in a semiconductor manufacturing process, wherein drying is performed with an inert gas containing hydrogen radicals.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19348398A JP4375584B2 (en) | 1998-07-08 | 1998-07-08 | Drying method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19348398A JP4375584B2 (en) | 1998-07-08 | 1998-07-08 | Drying method |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2000031109A true JP2000031109A (en) | 2000-01-28 |
JP4375584B2 JP4375584B2 (en) | 2009-12-02 |
Family
ID=16308792
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19348398A Expired - Fee Related JP4375584B2 (en) | 1998-07-08 | 1998-07-08 | Drying method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP4375584B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003005435A1 (en) * | 2001-07-05 | 2003-01-16 | Tokyo Electron Limited | Substrate treating device and substrate treating method, substrate flattening method |
WO2004036637A1 (en) * | 2002-09-24 | 2004-04-29 | Fujikin Incorporated | Rotary silicon wafer cleaning apparatus |
-
1998
- 1998-07-08 JP JP19348398A patent/JP4375584B2/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003005435A1 (en) * | 2001-07-05 | 2003-01-16 | Tokyo Electron Limited | Substrate treating device and substrate treating method, substrate flattening method |
EP1403913A1 (en) * | 2001-07-05 | 2004-03-31 | OHMI, Tadahiro | Substrate treating device and substrate treating method, substrate flattening method |
JPWO2003005435A1 (en) * | 2001-07-05 | 2004-10-28 | 大見 忠弘 | Substrate processing apparatus, substrate processing method, and substrate flattening method |
EP1403913A4 (en) * | 2001-07-05 | 2006-02-08 | Tadahiro Ohmi | Substrate treating device and substrate treating method, substrate flattening method |
WO2004036637A1 (en) * | 2002-09-24 | 2004-04-29 | Fujikin Incorporated | Rotary silicon wafer cleaning apparatus |
US7103990B2 (en) | 2002-09-24 | 2006-09-12 | Fujikin Incorporated | Rotary silicon wafer cleaning apparatus |
KR100705344B1 (en) * | 2002-09-24 | 2007-04-10 | 가부시키가이샤 후지킨 | Rotary silicon wafer cleaning apparatus |
CN100359641C (en) * | 2002-09-24 | 2008-01-02 | 株式会社富士金 | Rotary silicon wafer cleaning apparatus |
Also Published As
Publication number | Publication date |
---|---|
JP4375584B2 (en) | 2009-12-02 |
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