JP2001269634A - Treatment method for semiconductor material or the like - Google Patents
Treatment method for semiconductor material or the likeInfo
- Publication number
- JP2001269634A JP2001269634A JP2000086567A JP2000086567A JP2001269634A JP 2001269634 A JP2001269634 A JP 2001269634A JP 2000086567 A JP2000086567 A JP 2000086567A JP 2000086567 A JP2000086567 A JP 2000086567A JP 2001269634 A JP2001269634 A JP 2001269634A
- Authority
- JP
- Japan
- Prior art keywords
- processing
- chamber
- medium
- impurities
- reduced pressure
- 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.)
- Pending
Links
- 239000000463 material Substances 0.000 title claims abstract description 14
- 239000004065 semiconductor Substances 0.000 title claims abstract description 14
- 238000000034 method Methods 0.000 title claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 238000005406 washing Methods 0.000 claims abstract description 37
- 238000009835 boiling Methods 0.000 claims description 10
- 239000012535 impurity Substances 0.000 abstract description 31
- 230000008569 process Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 12
- 230000000630 rising effect Effects 0.000 description 9
- 238000003672 processing method Methods 0.000 description 7
- 239000000428 dust Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- 230000006837 decompression Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Landscapes
- Cleaning By Liquid Or Steam (AREA)
- Chemical Vapour Deposition (AREA)
- Weting (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、半導体材料等の処
理方法に係り、詳しくはシリコンウエハ、液晶基板及び
マスク用基板、そしてIC及びトランジスタの電子部品
関連の製作プロセスにおいて、エッチング処理等が行わ
れた後に被処理媒体に付着しているゴミ、有機残留物或
いは無機残留物等の不純物を洗い落として除去する処理
方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for processing semiconductor materials and the like. The present invention relates to a processing method for washing and removing impurities such as dust, organic residues, and inorganic residues attached to a medium to be processed after being washed.
【0002】[0002]
【従来の技術】従来から、ゴミ、有機残留物或いは無機
残留物等の不純物を半導体材料から洗い落す水洗い処理
として、半導体材料を収納する処理チャンバーの底部か
ら処理液を継続的に送り込みながら行う処理方法が、こ
の種の半導体材料の作製プロセスにおいて良く知られて
いる(例えば、特開平6-326073号等において知
られている)。2. Description of the Related Art Conventionally, as a water washing process for washing impurities such as dust, organic residues or inorganic residues from a semiconductor material, a process in which a processing solution is continuously fed from the bottom of a processing chamber for storing a semiconductor material. A method is well known in this kind of semiconductor material manufacturing process (for example, it is known in Japanese Patent Application Laid-Open No. 6-326073).
【0003】ところで、半導体材料の表面にはトレンチ
と称される小さな表面溝等が多数存在しており、この表
面溝等に不純物が入り込み、そして空気が内在している
ことが多い。By the way, a large number of small surface grooves called trenches exist on the surface of a semiconductor material, and impurities often enter these surface grooves and the like, and air is often contained therein.
【0004】[0004]
【発明が解決しようとする課題】しかし乍ら、水を処理
チャンバーの底部から送り込んで不純物を洗い落とす従
来の処理方法では、被処理媒体の表面に付着している不
純物を洗い落として除去することはできるが、表面溝等
に内在している空気を取り除くはできい。つまり、空気
によって表面溝等に閉じ込められている不純物を当該溝
から洗い落とすことができない等から、生産歩留まりが
非常に悪く、その改善が求められていた。However, in the conventional processing method in which water is fed from the bottom of the processing chamber to wash away impurities, impurities adhering to the surface of the medium to be processed can be removed by washing. However, it is not possible to remove air present in the surface groove or the like. In other words, since impurities trapped in the surface grooves and the like by air cannot be washed out from the grooves, the production yield is extremely poor, and an improvement has been required.
【0005】そこで、この様な従来事情に鑑み、数々の
研究を重ねた結果、被処理媒体が没入状に浸漬する密閉
された処理チャンバー内を吸引減圧せしめて処理液を減
圧沸騰させることで、不純物が付着する被処理媒体の表
面部分や表面溝等からも泡が発生し、この泡の発生が被
処理媒体から不純物を洗い落とす洗浄に優れた効果があ
ることに着目し、本発明に至ったものであり、その目的
とする処は、表面に付着しているゴミ、有機残留物或い
は無機残留物等の不純物は更に効果的に、そして、表面
溝等に入り込んで空気により閉じ込められている不純物
をも完全に除去し得るように開発した半導体材料等の処
理方法を提供することにある。In view of such circumstances, as a result of numerous studies, the inside of a closed processing chamber in which the medium to be processed is immersed is evacuated to a reduced pressure, and the processing liquid is boiled under reduced pressure. Focusing on the fact that bubbles are also generated from the surface portion or surface groove of the medium to which the impurities are attached, and that the generation of the bubbles has an excellent effect of washing off the impurities from the medium to be processed, the present invention has been achieved. The purpose is to remove impurities such as dust, organic residues or inorganic residues adhering to the surface more effectively, and impurities entering the surface grooves and the like and trapped by air. It is an object of the present invention to provide a method for treating a semiconductor material or the like which has been developed so as to completely remove the same.
【0006】[0006]
【課題を達成するための手段】課題を達成するために本
発明は、処理液中に被処理媒体を没入状に浸漬する密閉
された処理チャンバー内の純水又は処理液等からなる処
理液を減圧沸騰させながら被処理媒体の水洗い処理を行
うようにしたことである。又、上記処理液の減圧沸騰
が、処理チャンバーの底部から処理液が継続的に送り込
まれる水洗い処理中に行なわれることである。又、上記
処理チャンバー内の減圧圧力が−720〜−30mmHgの範囲
内に設定されてなることである。尚、この減圧度範囲の
設定は使用する処理液の水温(例えば10〜95℃)によっ
て適宜選択されるものである。又、本発明では、被処理
媒体の水洗い処理の初期段階では水温が低い処理液を用
い、該処理液を減圧沸騰させながら水洗い処理を行う。
そして、低い処理液を用いた水洗い処理開始から適宜の
時間をおいて徐々に水温が高い処理液に切換えながら且
つ同処理液を減圧沸騰させながら水洗い処理を行うこと
で、トレンチと称される表面溝等を効果的に水洗い処理
するものである。斯かる構成によれば、処理チャンバー
内の処理液が減圧沸騰する減圧圧力(mmHg)範囲までチ
ャンバー内を吸引減圧する。すると、不純物が付着する
被処理媒体の表面部分、そして表面に存在するトレンチ
と称される小さな表面溝等から泡が発生する。この泡の
発生とチャンバーの底部から上部へと上昇水流を形成す
る処理液の流れとにより被処理媒体の最終水洗い(リン
ス処理)が行なわれる。それにより、被処理媒体の表面
から不純物を洗い落とす洗浄はより効果的に、そして、
表面溝等からも当該溝からの泡の発生による物理的な力
により不純物が確実に洗い落とされる。In order to achieve the object, the present invention provides a processing solution comprising pure water or a processing solution in a sealed processing chamber in which a medium to be processed is immersed in the processing solution. That is, the medium to be treated is washed with water while boiling under reduced pressure. Further, the boiling of the processing solution under reduced pressure is performed during the water washing process in which the processing solution is continuously fed from the bottom of the processing chamber. Further, the reduced pressure in the processing chamber is set within a range of -720 to -30 mmHg. The setting of the degree of pressure reduction is appropriately selected depending on the water temperature (for example, 10 to 95 ° C.) of the processing liquid to be used. In the present invention, a treatment liquid having a low water temperature is used in the initial stage of the water treatment of the medium to be treated, and the water is washed while the treatment liquid is boiled under reduced pressure.
Then, after an appropriate time has elapsed from the start of the water washing process using the low processing solution, the water washing process is performed while gradually switching the processing solution to a high water temperature and boiling the processing solution under reduced pressure to obtain a surface called a trench. The grooves and the like are effectively washed with water. According to such a configuration, the pressure in the chamber is reduced by suction to a reduced pressure (mmHg) range in which the processing liquid in the processing chamber is boiled under reduced pressure. Then, bubbles are generated from the surface portion of the medium to which the impurities are attached, and small surface grooves called trenches existing on the surface. The final washing (rinsing treatment) of the medium to be treated is performed by the generation of the bubbles and the flow of the treatment liquid forming a rising water flow from the bottom to the top of the chamber. As a result, cleaning for removing impurities from the surface of the medium to be processed is more effective, and
Impurities are reliably washed away from the surface grooves and the like by physical force due to the generation of bubbles from the grooves.
【0007】[0007]
【発明の実施の形態】本発明の実施の具体例を図面に基
づいて説明する。図1は、本発明処理方法を実施する処
理装置の一例を示した概略図で、1は処理チャンバー、
2は処理液発生ユニット、3は排水・真空吸引ユニッ
ト、4は蒸気発生ユニット、5はガス供給ユニットであ
り、被処理媒体Wを没入状に浸漬する密閉された処理チ
ャンバー1内の処理液を減圧沸騰させながら被乾燥媒体
Wの最終水洗い処理を行うように構成してなる。然る
に、排水・真空吸引ユニット3により処理チャンバー1
内の処理液が減圧沸騰する減圧圧力(mmHg)範囲までチ
ャンバー内を吸引減圧する。すると、不純物が付着する
被処理媒体の表面部分、そして表面に存在するトレンチ
と称される小さな表面溝6等から泡が発生する(図2
(ロ)の拡大断面図参照)。この泡の発生とチャンバー
1の底部から上部へと上昇水流を形成する処理液の流れ
とにより被処理媒体の最終水洗い(リンス処理)が行な
われるように構成してなる。Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a schematic diagram showing an example of a processing apparatus for performing the processing method of the present invention.
2 is a processing liquid generating unit, 3 is a drainage / vacuum suction unit, 4 is a steam generating unit, 5 is a gas supply unit, and a processing liquid in a closed processing chamber 1 in which the medium to be processed W is immersed. The structure is such that the final washing process of the medium to be dried W is performed while boiling under reduced pressure. However, the processing chamber 1 is provided by the drainage / vacuum suction unit 3.
The inside of the chamber is suctioned and depressurized to a reduced pressure (mmHg) range in which the processing liquid in the inside boils under reduced pressure. Then, bubbles are generated from the surface portion of the medium to which the impurities adhere and the small surface grooves 6 called trenches existing on the surface (FIG. 2).
(See the enlarged cross-sectional view of (b).) The final washing (rinsing treatment) of the medium to be treated is performed by the generation of the bubbles and the flow of the treatment liquid forming a rising water flow from the bottom to the top of the chamber 1.
【0008】そして、本発明においては用いる処理液の
水温によって異なるが、水温が10〜95℃の処理液を用い
る場合、処理チャンバー1内の減圧圧力を、−720〜−3
0mmHgの範囲に設定することが本発明を成立させる上で
重要である。例えば、水温が15〜20℃の処理液の場合
で、処理チャンバー1内の減圧圧力を−700 mmHg位に設
定することが好ましい。In the present invention, depending on the temperature of the processing solution to be used, when a processing solution having a water temperature of 10 to 95 ° C. is used, the reduced pressure in the processing chamber 1 is reduced to −720 to −3.
It is important to set the range to 0 mmHg in order to realize the present invention. For example, in the case of a processing solution having a water temperature of 15 to 20 ° C., it is preferable to set the reduced pressure in the processing chamber 1 to about −700 mmHg.
【0009】処理チャンバー1は、内チャンバー1-1と
密閉蓋7を開閉可能に装備する外チャンバー1-2とから
二重構造に構成してなる。The processing chamber 1 has a double structure comprising an inner chamber 1-1 and an outer chamber 1-2 provided with an openable / closable lid 7.
【0010】内チャンバー1-1は、多数枚の被処理媒体
Wを並列収納し得る大きさで、処理液中に没入状に浸漬
し得る深さを有する上面開口の有底箱形に形成され、傾
斜する底部中央に処理液の給・排水口8を形成し、給水
流路9を介して処理液発生ユニット2を接続して、最終
水洗い時に内チャンバー1-1の底部から同チャンバー1-1
内に処理液を継続的に送り込むようにしてある(図2
(イ)、(ロ)の状態)。そして、給水流路9の途中か
ら分岐させた排水流路10と、この排水流路10の一端に接
続したヘッダ11とを介して排水・真空吸引ユニット3を
接続して、最終水洗いが終了した後に内チャンバー1-1
内の処理液を底部から強制排水するようにしてなる(図
2(ハ)の状態)。The inner chamber 1-1 has a size capable of accommodating a large number of media W to be processed in parallel, and is formed in a bottomed box shape having an upper surface opening having a depth capable of being immersed in the processing liquid. A processing liquid supply / drain port 8 is formed in the center of the inclined bottom, and the processing liquid generating unit 2 is connected through a water supply flow path 9 so that the chamber 1 is removed from the bottom of the inner chamber 1-1 at the time of final washing. 1
The processing liquid is continuously fed into the chamber (FIG. 2).
(B), (b)). Then, the drainage / vacuum suction unit 3 is connected via the drainage channel 10 branched from the middle of the water supply channel 9 and the header 11 connected to one end of the drainage channel 10, and the final washing is completed. Later inside chamber 1-1
The treatment liquid in the inside is forcibly drained from the bottom (the state shown in FIG. 2C).
【0011】外チャンバー1-2は、内チャンバー1-1を図
示の如く遊嵌状に内設し得る大きさを有する上面開口の
有底箱形に形成され、上部開口に密閉蓋8を開閉可能に
装備してなる。そして、傾斜する底部にはオーバーフロ
ー口12を形成し、前述のヘッダ11に亘りオーバーフロー
流路13を介して排水・真空吸引ユニット5に接続して、
最終水洗い処理中に内チャンバー1-1の上面開口から溢
れ出た処理液(所謂オーバーフロー水)を外部に強制排
水するようにしてなる(図2(イ)、(ハ)の状態)。
又、内チャンバー1-1の上面開口より上部側に位置する
壁部には蒸気導入口14とガス供給口15とを夫々形成し、
蒸気流路16の一端を蒸気導入口14に接続して、最終水洗
いが終了した後に内チャンバー1-1内の処理液が底部か
ら強制排水されることにより真空化される密閉チャンバ
ー1内に有機溶剤が吸い込まれ導入されるようにしてな
る(図2(ハ)の状態)。又、ガス供給口15にガス流路
17を介してガス供給ユニット5を接続し、有機溶剤によ
る被処理媒体Wの蒸気置換による蒸気乾燥が終了した後
に、内外両チャンバー1-1,1-2内に残る有機蒸気や湿気
等をチャンバー1-1,1-2外に強制排気せしめた後に、真
空化された同チャンバー1-1,1-2内にクリーンガス(例
えばN2)を送り込んで(図2(ニ)の状態)、同チャ
ンバー1-1,1-2内を常圧(大気圧)に戻し、その後、密
閉蓋8を開けて被処理媒体を外部に取り出せるようにし
てなる(図5(ホ)の状態)。The outer chamber 1-2 is formed in the shape of a box with a bottom and an upper opening having a size that allows the inner chamber 1-1 to be freely inserted inside as shown in the figure, and a closed lid 8 is opened and closed at the upper opening. It will be equipped as possible. Then, an overflow port 12 is formed in the inclined bottom, and the overflow port 12 is connected to the drain / vacuum suction unit 5 through the overflow channel 13 over the above-mentioned header 11,
During the final washing process, the processing liquid (so-called overflow water) overflowing from the upper opening of the inner chamber 1-1 is forcibly drained to the outside (the state shown in FIGS. 2A and 2C).
In addition, a steam inlet 14 and a gas supply port 15 are formed on a wall located above the upper opening of the inner chamber 1-1, respectively,
One end of the steam flow path 16 is connected to the steam inlet 14, and after the final washing is completed, the processing liquid in the inner chamber 1-1 is forcibly drained from the bottom, and the organic liquid is placed in the closed chamber 1 which is evacuated. The solvent is sucked and introduced (the state shown in FIG. 2C). In addition, the gas supply port 15
The gas supply unit 5 is connected to the processing chamber 17 through a gas supply unit 17, and after vapor drying of the medium W to be treated with the organic solvent is completed, the organic vapor or moisture remaining in the inner and outer chambers 1-1 and 1-2 is removed. After forcibly evacuating the chambers 1-1 and 1-2, a clean gas (eg, N 2 ) is fed into the evacuated chambers 1-1 and 1-2 (the state shown in FIG. 2 (d)). The inside of the chambers 1-1 and 1-2 is returned to normal pressure (atmospheric pressure), and thereafter, the closed lid 8 is opened so that the medium to be processed can be taken out (state of FIG. 5 (e)).
【0012】又、蒸気導入口14を開口した外チャンバー
1-2の上部側壁部には吸引口18を形成し、前述のヘッダ1
1に亘り吸引流路19を接続して、最終水洗い処理中に排
水・真空吸引ユニット3により処理チャンバー1内を吸
引減圧し、被処理媒体Wを没入状に浸漬する内チャンバ
ー1-1内の処理液を減圧沸騰せしめて同処理液中に泡を
発生させ(図2(ロ)の状態)、尚且つ、不純物が付着
する表面部分、そして、表面に存在する表面溝6等から
も泡を発生させ(図2(ロ)の拡大断面図)、この泡の
発生により被処理媒体Wの表面や表面溝6等に付着して
いる不純物を泡発生による物理的な力な利用して被処理
媒体Wの最終水洗い時の洗浄効果(リンス作用)を促進
させて効率的且つ短時間で最終水洗い処理を行うように
してなる。An outer chamber having a steam inlet 14 opened.
A suction port 18 is formed in the upper side wall portion of 1-2, and the header 1 described above is formed.
1, the suction chamber 19 is connected, and the drainage / vacuum suction unit 3 suctions and depressurizes the inside of the processing chamber 1 during the final rinsing process, so that the processing target medium W is immersed in the inner chamber 1-1. The processing liquid is boiled under reduced pressure to generate bubbles in the processing liquid (the state shown in FIG. 2B). In addition, bubbles are also generated from the surface portion to which impurities adhere and the surface grooves 6 existing on the surface. 2 (b), and the bubbles adhere to the surface of the medium W to be processed and the surface grooves 6 to be processed by utilizing the physical force generated by the bubbles. The washing effect (rinsing action) at the time of the final washing of the medium W is promoted, so that the final washing process can be performed efficiently and in a short time.
【0013】図中20は処理液の給水流路9に配備された
給水バルブ、21は同排水流路10に配備された排水バル
ブ、22はオーバーフロー流路13に配備されたオーバーフ
ローバルブ、23は蒸気流路16に配備された蒸気バルブ、
24はガス流路17に配備されたガスバルブ、25は吸引流路
19に配備された減圧バルブである。In the drawing, reference numeral 20 denotes a water supply valve provided in the water supply flow path 9 for the treatment liquid, 21 denotes a drain valve provided in the drainage flow path 10, 22 denotes an overflow valve provided in the overflow flow path 13, and 23 denotes an overflow valve. A steam valve arranged in the steam passage 16,
24 is a gas valve provided in the gas flow path 17, 25 is a suction flow path
This is a pressure reducing valve provided at 19.
【0014】次に、以上の構成した処理装置を用いた本
発明の処理方法を簡単に述べると、被処理媒体Wが内チ
ャンバー1-1内に並列収納され、外チャンバー1-2の上面
開口が密閉蓋8により閉蓋されと、処理液発生ユニット
4が作動し、給水バルブ19が開いて例えば10℃位の処理
液が内チャンバー1-1内に所定の流速(m/s)にて送り込
まれる。すると、内チャンバー1-1内には各被処理媒体
Wの表面に接触する処理液の上昇水流が形成され、各被
処理媒体Wの最終水洗い(リンス処理)が開始する(図
2(イ)の状態)。この最終水洗い処理開始と同時か、
所定のタイミングにて減圧バルブ25が開いて継続して作
動している排水・真空吸引ユニット3による処理チャン
バー1内の吸引減圧が開始し、上昇水流を形成しながら
内チャンバー1-1の底部から上部へと流れる処理液が減
圧沸騰する(図2(ロ)の状態)。すると、処理液中に
は泡が発生し、この泡が被処理媒体Wの表面に物理的に
接触(衝突)しながら浮上すると共に、不純物が付着す
る表面部分、そして、トレンチと称される小さな表面溝
6等からも泡が発生する。そして、10℃位の処理液によ
る処理開始から適宜の時間をおいて水温が例えば30℃位
の処理液を送り込みながら尚且つ当該処理液を減圧沸騰
させながら水洗い処理を行う。それにより、被処理媒体
Wの表面に付着する不純物は泡と処理液の上昇水流とに
より効果的に洗い落とされると共に、表面溝6等にも泡
による物理的な力が効果的に作用して表面溝6等からも
泡による物理的な力により不純物が剥がされて洗い落と
される(図2(ロ)の拡大断面図参照)。尚、最終水洗
い中における処理液の減圧沸騰は、間欠的又は最終水洗
い処理が終了まで継続的に行う等、任意である。Next, the processing method of the present invention using the processing apparatus constructed as described above will be briefly described. The medium W to be processed is housed in parallel in the inner chamber 1-1, and the upper surface opening of the outer chamber 1-2 is opened. Is closed by the closed lid 8, the processing liquid generating unit 4 is operated, the water supply valve 19 is opened, and the processing liquid of, for example, about 10 ° C. is supplied into the inner chamber 1-1 at a predetermined flow rate (m / s). Sent in. Then, a rising water flow of the processing liquid that contacts the surface of each processing target medium W is formed in the inner chamber 1-1, and the final rinsing (rinsing processing) of each processing target medium W starts (FIG. 2A). State). At the same time as the start of this final washing process,
At a predetermined timing, the decompression valve 25 is opened and the suction / decompression inside the processing chamber 1 is started by the drain / vacuum suction unit 3 which is continuously operated, and a rising water flow is formed from the bottom of the inner chamber 1-1. The processing liquid flowing to the upper portion is boiled under reduced pressure (the state shown in FIG. 2B). Then, bubbles are generated in the processing liquid, and the bubbles float while physically contacting (colliding) with the surface of the processing target medium W, and a surface portion to which impurities adhere and a small portion called a trench. Bubbles are also generated from the surface grooves 6 and the like. Then, after an appropriate time from the start of the treatment with the treatment liquid at about 10 ° C., the water washing process is performed while the treatment liquid having a water temperature of, for example, about 30 ° C. is fed and the treatment liquid is boiled under reduced pressure. Thereby, impurities adhering to the surface of the processing target medium W are effectively washed away by the bubbles and the rising water flow of the processing solution, and the physical force of the bubbles effectively acts on the surface grooves 6 and the like. The impurities are also peeled off from the surface grooves 6 and the like by the physical force of the bubbles and washed away (see an enlarged sectional view of FIG. 2B). The boiling under reduced pressure of the treatment liquid during the final washing is optional, such as intermittently or continuously performed until the final washing treatment is completed.
【0015】処理液の上昇水流と処理液の減圧沸騰によ
り発生する泡とによる被処理媒体Wの最終水洗い(リン
ス処理)が終了し、給水バルブ20と減圧バルブ25とが閉
じられて内チャンバー1-1への処理液の供給が停止、そ
して、処理チャンバー1内の吸引減圧が停止すると、排
水バルブ21が開いて継続運転する排水・真空吸引ユニッ
ト3により内チャンバー1-1内の処理液が底部の給・排
水口8からチャンバー1-1外に強制排水されると共に、
この強制排水に伴い内チャンバー1-1内を含めた外チャ
ンバー1-2内が徐々に真空化される。そして、この真空
化と共に蒸気バルブ23が開き、内外チャンバー1-1,1-2
内の真空化による負圧により外チャンバー1-2の蒸気導
入口14から内外チャンバー1-1,1-2内に有機蒸気が吸い
込まれるように導入される(図2(ハ)の状態)。The final washing (rinsing treatment) of the medium W to be treated with the rising water flow of the treatment liquid and bubbles generated by the boiling of the treatment liquid under reduced pressure is completed, the water supply valve 20 and the pressure reduction valve 25 are closed, and the inner chamber 1 is closed. When the supply of the processing liquid to the processing chamber 1 is stopped and the suction and pressure in the processing chamber 1 are stopped, the drain valve 21 is opened and the processing liquid in the inner chamber 1-1 is discharged by the drain / vacuum suction unit 3 which is continuously operated. The water is forcibly drained out of the chamber 1-1 from the water supply / drain opening 8 at the bottom,
With this forced drainage, the inside of the outer chamber 1-2 including the inside of the inner chamber 1-1 is gradually evacuated. Then, with the evacuation, the steam valve 23 is opened, and the inner and outer chambers 1-1 and 1-2 are opened.
Organic vapor is introduced into the inner and outer chambers 1-1 and 1-2 from the vapor inlet 14 of the outer chamber 1-2 by the negative pressure due to the internal vacuum so as to be sucked into the inner and outer chambers 1-1 and 1-2 (state of FIG. 2C).
【0016】内チャンバー1-1内に導入された有機溶剤
は処理液の水面Lが降下するに連れて露出する被処理媒
体Wの表面に接触し、当該表面の水滴との蒸気置換が成
される。然る後、内チャンバー1-1内の処理液が完全に
強制排水され、有機蒸気による被処理媒体Wの蒸気乾燥
が終了し、蒸気バルブ23が閉じられると、継続運転する
排水・真空吸引ユニット3により内外チャンバー1-1,1
-2内に残る有機蒸気や湿気等が内チャンバー1-1の給・
排水口8、そして外チャンバー1-2のオーバーフロー口1
2から強制排気される。The organic solvent introduced into the inner chamber 1-1 comes into contact with the surface of the processing target medium W which is exposed as the water level L of the processing liquid is lowered, and vapor replacement with water droplets on the surface is performed. You. Thereafter, when the processing liquid in the inner chamber 1-1 is completely forcibly drained, the steam drying of the processing target medium W by the organic vapor is completed, and when the steam valve 23 is closed, the drain / vacuum suction unit that is continuously operated is operated. 3, inner and outer chambers 1-1, 1
-2 The organic vapor and moisture remaining in the
Drain port 8 and overflow port 1 of outer chamber 1-2
It is forcibly exhausted from 2.
【0017】処理液による最終水洗いから有機蒸気によ
る蒸気乾燥が行なわれて内外チャンバー1-1,1-2内から
有機蒸気や湿気等が完全に強制排気され、排水バルブ2
1、オーバーフローバルブ22が閉じられると、ガスバル
ブ24が開いて外チャンバー1-2のガス導入口15から内外
チャンバー1-1,1-2内にクリーンガスが送り込まれて真
空状態(負圧下)の同チャンバー1-1,1-2内は大気圧
(常圧)に戻される(図2(ニ)の状態)。それによ
り、外チャンバー1-2の上部開口を密閉する密閉蓋7を
開くことで、被処理媒体Wを内チャンバー1-内から取り
出すことができる(図2(ホ)の状態)。After the final washing with the treatment liquid, steam drying with organic vapor is performed, and the organic vapor and moisture are completely forcibly exhausted from the inside and outside chambers 1-1 and 1-2.
1. When the overflow valve 22 is closed, the gas valve 24 is opened and clean gas is sent from the gas inlet port 15 of the outer chamber 1-2 into the inner and outer chambers 1-1 and 1-2, and the vacuum state (under negative pressure) is established. The inside of the chambers 1-1 and 1-2 is returned to the atmospheric pressure (normal pressure) (the state of FIG. 2 (d)). Thereby, the processing target medium W can be taken out from the inner chamber 1 by opening the sealing lid 7 for closing the upper opening of the outer chamber 1-2 (the state of FIG. 2 (e)).
【0018】従って、本発明の処理方法によれば、内チ
ャンバー1-1の底部から上部へと上昇水流を形成する処
理液による被処理媒体Wの最終水洗い中に、処理液の減
圧沸騰により泡が発生し、不純物が付着する被処理媒体
Wの表面部分、表面の表面溝6等からも泡が発生する。
この泡の発生とチャンバーの底部から上部へと上昇水流
を形成する処理液の流れとにより被処理媒体の最終水洗
い(リンス処理)が行なわれる。それにより、被処理媒
体Wの表面から不純物を洗い落とす洗浄はより効果的
に、そして、表面溝6等からも当該溝6からの泡の発生
による物理的な力により不純物が剥がされて確実に洗い
落とされる。Therefore, according to the processing method of the present invention, during the final washing of the processing target medium W with the processing liquid forming the rising water flow from the bottom to the upper part of the inner chamber 1-1, bubbles are generated by the reduced pressure boiling of the processing liquid. Is generated, and bubbles are also generated from the surface portion of the processing target medium W to which impurities adhere, the surface groove 6 on the surface, and the like.
The final washing (rinsing treatment) of the medium to be treated is performed by the generation of the bubbles and the flow of the treatment liquid forming a rising water flow from the bottom to the top of the chamber. Thereby, the cleaning for removing impurities from the surface of the medium to be processed W is more effective, and the impurities are also peeled off from the surface grooves 6 and the like by the physical force due to the generation of bubbles from the grooves 6 so as to be surely washed. Dropped.
【0019】尚、前述した実施例詳述においては処理チ
ャンバー1を内外チャンバー1-1,1-2からなる二重構造
のチャンバー形態として説明したが、例えば外チャンバ
ーのみからなる単体のチャンバー形態でも良く、任意で
ある。この場合、最終水洗い時に被処理媒体Wが没入状
に浸漬するその上部側から余分な処理液が強制排水され
るようにチャンバーの壁部にオーバーフロー口を設け、
このオーバーフロー口にオーバーフロー流路を接続す
る。In the above embodiment, the processing chamber 1 is described as having a double-chamber configuration including the inner and outer chambers 1-1 and 1-2. Good and optional. In this case, an overflow port is provided in the chamber wall so that excess processing liquid is forcibly drained from the upper side where the medium to be processed W is immersed in the final washing,
An overflow channel is connected to the overflow port.
【0020】又、最終水洗い処理後の被処理媒体Wの完
全乾燥処理としては、温風や遠心力(スピンドルドライ
ヤ)を利用した乾燥でも良いことは言うまでもないであ
ろう。It goes without saying that the medium W to be treated after the final washing treatment may be completely dried using hot air or centrifugal force (spindle dryer).
【0021】[0021]
【発明の効果】本発明の半導体材料等の処理方法は叙上
の如く構成してなることから、下記の作用効果を秦す
る。被処理媒体が没入状に浸漬する密閉された処理チャ
ンバー内の処理液を減圧沸騰させることで、不純物が付
着する被処理媒体の表面部分やトレンチと称される小さ
な表面溝等からも泡を発生させ、この泡の発生による物
理的な力を利用して被処理媒体の水洗い処理を行うこと
ができる。それにより、被処理媒体の表面から不純物を
洗い落とす洗浄はより効果的に、そして、表面溝等から
も当該溝からの泡の発生による物理的な力により不純物
が剥がされて確実に洗い落とされる。Since the method for treating a semiconductor material or the like according to the present invention is constituted as described above, the following functions and effects are obtained. By boiling the processing solution in a closed processing chamber in which the medium to be processed is immersed in a immersive manner under reduced pressure, bubbles are also generated from the surface portion of the medium to which impurities adhere and small surface grooves called trenches. Then, the medium to be treated can be washed with water using the physical force caused by the generation of the bubbles. As a result, the washing for removing impurities from the surface of the medium to be treated is more effective, and the impurities are peeled off from the surface grooves and the like by the physical force due to the generation of bubbles from the grooves, so that the impurities are surely washed off.
【0022】又、前述したように処理液の減圧沸騰によ
り発生する泡の物理的な力と処理チャンバーの底部から
上部へと上昇水流を形成する処理液の流れとの相乗効果
(洗浄促進力の向上)により被処理媒体をより一層効果
的に水洗い処理することができる。それにより、従来に
比べて処理能率が圧倒的に速くなり、半導体材料等の製
作歩留まりの向上が期待でき、有益である。Further, as described above, the synergistic effect of the physical force of the bubbles generated by the boiling under reduced pressure of the processing solution and the flow of the processing solution forming a rising water flow from the bottom to the top of the processing chamber (the cleaning promoting power). Improvement) allows the medium to be treated to be more effectively washed with water. As a result, the processing efficiency is overwhelmingly faster than in the past, and the production yield of semiconductor materials and the like can be expected to be improved, which is beneficial.
【0023】従って、本発明によれば、被処理媒体の表
面に付着しているゴミ、有機残留物或いは無機残留物等
の不純物は更に効果的に除去し得る。そして、トレンチ
と称される小さな表面溝等に入り込んで空気により閉じ
込められている不純物をも完全に除去し得る画期的な処
理方法を提供することができる。Therefore, according to the present invention, impurities such as dust, organic residues and inorganic residues adhering to the surface of the medium to be treated can be more effectively removed. In addition, it is possible to provide an epoch-making treatment method capable of completely removing impurities trapped by air by entering small surface grooves called trenches.
【図1】 本発明処理方法を実施する処理装置の一例を
示した概略図FIG. 1 is a schematic diagram illustrating an example of a processing apparatus that performs a processing method of the present invention.
【図2】 本発明処理方法による半導体材料等の製作プ
ロセスの一例を示した工程概略図で、(イ)は底部から
処理チャンバー内に処理液を送り込んで最終水洗いをし
ている状態、(ロ)は最終水洗い処理中に処理チャンバ
ー内を減圧せしめて処理液を減圧沸騰させることで、当
該処理液中に泡を発生させ、尚且つ、表面の溝等からも
泡を発生させながら最終水洗いをしている状態、(ハ)
は最終水洗いが終了した後に底部から処理液を強制排水
し、処理チャンバー内の真空化により有機溶剤が蒸気導
入管を通ってチャンバー内の導入されている状態、
(ニ)は処理チャンバー内に残る有機蒸気や湿気等を強
制排気せしめた後に処理チャンバーに不活性ガスを導入
させて同チャンバー内を常圧(大気圧)に戻している状
態、(ホ)は密閉蓋を開けて完全乾燥された被処理媒体
を処理チャンバー内から取り出している状態FIGS. 2A and 2B are schematic views showing an example of a manufacturing process of a semiconductor material or the like according to the processing method of the present invention. FIG. 2A shows a state in which a processing liquid is fed into a processing chamber from the bottom to perform a final washing. ) Is to reduce the pressure inside the processing chamber and boil the processing solution under reduced pressure during the final washing process, thereby generating bubbles in the processing solution and performing final washing while generating bubbles also from the grooves on the surface. (C)
After the final washing is completed, the processing liquid is forcibly drained from the bottom after the final washing, and the organic solvent is introduced into the chamber through the vapor introduction pipe by evacuation of the processing chamber,
(D) is a state in which organic vapor or moisture remaining in the processing chamber is forcibly exhausted, and then an inert gas is introduced into the processing chamber to return the inside of the chamber to normal pressure (atmospheric pressure). Opening the sealing lid and removing the completely dried medium from the processing chamber
1:処理チャンバー 2:処理液発生ユニッ
ト 3:排水・真空吸引ユニット 4:蒸気発生ユニット 5:ガスユニット 6:表面溝 7:密閉蓋 W:被処理媒体1: processing chamber 2: processing liquid generation unit 3: drainage / vacuum suction unit 4: steam generation unit 5: gas unit 6: surface groove 7: closed lid W: medium to be processed
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3B201 AA03 AB45 BB02 BB13 BB82 BB92 CB12 4K030 DA08 5F043 DD05 DD30 EE03 EE27 GG10 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 3B201 AA03 AB45 BB02 BB13 BB82 BB92 CB12 4K030 DA08 5F043 DD05 DD30 EE03 EE27 GG10
Claims (3)
た処理チャンバー内の処理液を減圧沸騰させながら被処
理媒体の水洗い処理を行うことを特徴とする半導体材料
等の処理方法。1. A method for processing a semiconductor material or the like, wherein the processing medium is washed with water while the processing liquid in a closed processing chamber in which the medium to be processed is immersed is immersed under reduced pressure.
理チャンバーの底部から処理液が継続的に送り込まれる
水洗い処理中に行なわれることを特徴とする半導体材料
等の処理方法。2. A method for treating semiconductor material or the like, wherein the reduced pressure boiling of the treatment liquid according to claim 1 is performed during a water washing treatment in which the treatment liquid is continuously fed from the bottom of the treatment chamber.
の減圧圧力が、−720〜―30mmHgの範囲であることを特
徴とする半導体材料等の処理方法。3. A method for processing a semiconductor material or the like, wherein the reduced pressure in the processing chamber according to claim 1 or 2 is in a range of -720 to -30 mmHg.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000086567A JP2001269634A (en) | 2000-03-27 | 2000-03-27 | Treatment method for semiconductor material or the like |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000086567A JP2001269634A (en) | 2000-03-27 | 2000-03-27 | Treatment method for semiconductor material or the like |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2001269634A true JP2001269634A (en) | 2001-10-02 |
Family
ID=18602711
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000086567A Pending JP2001269634A (en) | 2000-03-27 | 2000-03-27 | Treatment method for semiconductor material or the like |
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| Country | Link |
|---|---|
| JP (1) | JP2001269634A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008545272A (en) * | 2005-06-30 | 2008-12-11 | ラム リサーチ コーポレーション | Method and apparatus for removing substances from semiconductor wafer |
| JP2010284616A (en) * | 2009-06-15 | 2010-12-24 | Jmc:Kk | Electronic device recovery method and apparatus |
| JP2019091848A (en) * | 2017-11-16 | 2019-06-13 | 大陽日酸株式会社 | Method for cleaning component in furnace of vapor phase growth device |
-
2000
- 2000-03-27 JP JP2000086567A patent/JP2001269634A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008545272A (en) * | 2005-06-30 | 2008-12-11 | ラム リサーチ コーポレーション | Method and apparatus for removing substances from semiconductor wafer |
| KR101269783B1 (en) * | 2005-06-30 | 2013-05-30 | 램 리써치 코포레이션 | Method for removing material from semiconductor wafer and apparatus for performing the same |
| JP2010284616A (en) * | 2009-06-15 | 2010-12-24 | Jmc:Kk | Electronic device recovery method and apparatus |
| JP2019091848A (en) * | 2017-11-16 | 2019-06-13 | 大陽日酸株式会社 | Method for cleaning component in furnace of vapor phase growth device |
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