JP2002110605A - Substrate treating method and device - Google Patents
Substrate treating method and deviceInfo
- Publication number
- JP2002110605A JP2002110605A JP2000296342A JP2000296342A JP2002110605A JP 2002110605 A JP2002110605 A JP 2002110605A JP 2000296342 A JP2000296342 A JP 2000296342A JP 2000296342 A JP2000296342 A JP 2000296342A JP 2002110605 A JP2002110605 A JP 2002110605A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- substrate
- processing
- wafer
- ozone water
- 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
- 239000000758 substrate Substances 0.000 title claims abstract description 234
- 238000000034 method Methods 0.000 title description 10
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 373
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 329
- 238000010438 heat treatment Methods 0.000 claims description 103
- 239000007788 liquid Substances 0.000 claims description 83
- 238000003672 processing method Methods 0.000 claims description 14
- 238000007599 discharging Methods 0.000 claims description 2
- 239000008213 purified water Substances 0.000 abstract description 4
- 238000006385 ozonation reaction Methods 0.000 abstract 2
- 235000012431 wafers Nutrition 0.000 description 176
- 239000000126 substance Substances 0.000 description 23
- 238000007664 blowing Methods 0.000 description 15
- 230000007423 decrease Effects 0.000 description 15
- 230000007246 mechanism Effects 0.000 description 15
- 239000005416 organic matter Substances 0.000 description 11
- 230000008569 process Effects 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 230000036632 reaction speed Effects 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- 101000777301 Homo sapiens Uteroglobin Proteins 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 102100031083 Uteroglobin Human genes 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002516 radical scavenger Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 230000007723 transport mechanism Effects 0.000 description 1
Landscapes
- Liquid Crystal (AREA)
- Weting (AREA)
- Exposure Of Semiconductors, Excluding Electron Or Ion Beam Exposure (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、半導体ウエハ、
液晶表示装置用ガラス基板、電子部品などの基板を、オ
ゾンが溶解したオゾン水中に浸漬させて処理する基板処
理方法、ならびに、その方法を実施するために使用され
る基板処理装置に関する。[0001] The present invention relates to a semiconductor wafer,
The present invention relates to a substrate processing method for immersing a substrate such as a glass substrate for a liquid crystal display device and an electronic component in ozone water in which ozone is dissolved, and a substrate processing apparatus used for performing the method.
【0002】[0002]
【従来の技術】例えば半導体デバイスの製造プロセスに
おいて、基板、例えばシリコンウエハの表面に付着した
レジスト等の有機物を分解して除去する目的などで、純
水中にオゾンを溶解させたオゾン水を使用し、そのオゾ
ン水中にウエハを浸漬させて処理することが行われてい
る。2. Description of the Related Art In a semiconductor device manufacturing process, for example, ozone water obtained by dissolving ozone in pure water is used for the purpose of decomposing and removing organic substances such as a resist attached to the surface of a substrate, for example, a silicon wafer. Then, the wafer is immersed in the ozone water for processing.
【0003】図6は、オゾン水を用いる従来の基板処理
装置の構成の1例を示す概略図である。この基板処理装
置は、内部にオゾン水を収容しそのオゾン水中にウエハ
Wがウエハホルダ14に保持されて浸漬させられる処理
槽12を備えている。FIG. 6 is a schematic diagram showing an example of the configuration of a conventional substrate processing apparatus using ozone water. This substrate processing apparatus is provided with a processing tank 12 in which ozone water is contained and a wafer W is held by a wafer holder 14 and immersed in the ozone water.
【0004】処理槽12は、下部に液体供給口16を有
するとともに、上部に液体が溢れ出す溢流部18を有す
る。また、処理槽12には、溢流液受け部20が付設さ
れており、処理槽12上部の溢流部18から溢れ出た液
体が溢流液受け部20内へ流入するようになっている。
溢流液受け部20の底部には、溢流液排出管22が連通
して接続されており、溢流液排出管22は、ドレイン排
出管24に接続されている。また、処理槽12の底部に
は、排液口26が形設されており、その排液口26に、
排液バルブ30が介挿された排液管28が連通して接続
され、排液管28は、ドレイン排出管24に接続されて
いる。The processing tank 12 has a liquid supply port 16 at a lower part and an overflow part 18 from which liquid overflows at an upper part. Further, the processing tank 12 is provided with an overflow liquid receiving section 20, and the liquid overflowing from the overflow section 18 above the processing tank 12 flows into the overflow liquid receiving section 20. .
An overflow liquid discharge pipe 22 is connected to the bottom of the overflow liquid receiving section 20 so as to communicate therewith, and the overflow liquid discharge pipe 22 is connected to a drain discharge pipe 24. A drain port 26 is formed at the bottom of the processing tank 12.
A drain pipe 28 in which a drain valve 30 is inserted is connected and connected, and the drain pipe 28 is connected to the drain drain pipe 24.
【0005】また、処理槽12の下部の液体供給口16
には、開閉制御弁34が介挿された液体供給管32が連
通して接続されており、その液体供給管32に、純水供
給源に接続され開閉制御弁38および流量調整弁40が
それぞれ介挿された純水供給管36、ならびに、オゾン
水発生器などのオゾン水供給源に接続され開閉制御弁4
4が介挿されたオゾン水供給管42がそれぞれ接続され
ている。なお、図6に示したような、いわゆるワンバス
方式の基板処理装置では、通常、液体供給管32にミキ
シングバルブが介在して設けられ、そのミキシングバル
ブに、それぞれ種類の異なる薬液の供給タンクに接続さ
れた複数本の薬液供給管が接続されていて、純水供給管
36を通して送られる純水と各薬液とを混合して処理槽
12内へ供給することができるように構成されている
が、その図示および説明は、本書では省略する。Further, a liquid supply port 16 at a lower portion of the processing tank 12 is provided.
Is connected to a liquid supply pipe 32 in which an open / close control valve 34 is interposed. The liquid supply pipe 32 has an open / close control valve 38 and a flow control valve 40 connected to a pure water supply source. The open / close control valve 4 is connected to an inserted pure water supply pipe 36 and an ozone water supply source such as an ozone water generator.
The ozone water supply pipes 42 each having the interposed 4 are connected to each other. In a so-called one-bus type substrate processing apparatus as shown in FIG. 6, a mixing valve is usually provided in the liquid supply pipe 32, and the mixing valve is connected to supply tanks of different types of chemical liquids. A plurality of chemical solution supply pipes are connected, and it is configured such that pure water sent through the pure water supply pipe 36 and each chemical solution can be mixed and supplied into the processing tank 12. Its illustration and description are omitted in this document.
【0006】図6に示したような構成の基板処理装置に
おいて、オゾン水によりウエハWの表面に付着したレジ
スト等の有機物を分解して除去するときは、オゾン水供
給管42から液体供給管32を通して処理槽12の液体
供給口16へオゾン水を供給し、処理槽12内へオゾン
水を流入させてその内部にオゾン水を満たし、処理槽1
2の上部の溢流部18からオゾン水が溢れ出て溢流受け
部20内へ流入する状態にする。あるいは、純水で満た
された処理槽12内へオゾン水供給管42から液体供給
管32を通して処理槽12の液体供給口16へオゾン水
を供給し、処理槽12内へオゾン水を流入させて、オゾ
ン水により処理槽12の上部の溢流部18から純水を押
し出し、処理槽12の内部をオゾン水で置換し、処理槽
12の内部にオゾン水を満たし処理槽12の上部の溢流
部18からオゾン水が溢れ出て溢流受け部20内へ流入
する状態にする。この状態において、ウエハWがオゾン
水中に浸漬させられ、あるいは、処理槽12内へのオゾ
ン水の供給前から処理槽12内に収容されていたウエハ
Wがオゾン水中に浸漬させられて、オゾンの酸化作用に
よりウエハWの表面上の有機物が分解して除去される。In the substrate processing apparatus having the structure shown in FIG. 6, when decomposing and removing organic substances such as resist adhered to the surface of the wafer W with ozone water, the ozone water supply pipe 42 is connected to the liquid supply pipe 32. The ozone water is supplied to the liquid supply port 16 of the processing tank 12 through the through-hole, the ozone water flows into the processing tank 12, and the inside thereof is filled with the ozone water.
The ozone water overflows from the overflow portion 18 at the upper part of 2 and flows into the overflow receiving portion 20. Alternatively, ozone water is supplied from the ozone water supply pipe 42 to the liquid supply port 16 of the processing tank 12 through the liquid supply pipe 32 into the processing tank 12 filled with pure water, and the ozone water flows into the processing tank 12. Then, pure water is pushed out from the overflow portion 18 on the upper portion of the processing tank 12 with ozone water, the inside of the processing tank 12 is replaced with ozone water, and the inside of the processing tank 12 is filled with ozone water and overflows on the upper portion of the processing tank 12. The state is such that ozone water overflows from the section 18 and flows into the overflow receiving section 20. In this state, the wafer W is immersed in the ozone water, or the wafer W stored in the processing tank 12 before the supply of the ozone water into the processing tank 12 is immersed in the ozone water, and Organic substances on the surface of the wafer W are decomposed and removed by the oxidizing action.
【0007】オゾン水によるウエハWの処理が終わる
と、オゾン水の供給を停止させるとともに、純水供給管
36から液体供給管32を通して処理槽12の液体供給
口16へ純水を供給し、処理槽12内へ純水を流入させ
て、純水により処理槽12の上部の溢流部18からオゾ
ン水を押し出し、処理槽12の内部を純水で置換し、処
理槽12の内部に純水を満たし処理槽12の上部の溢流
部18から純水が溢れ出て溢流受け部20内へ流入する
状態にする。あるいは、排液バルブ30を開いて処理槽
12内のオゾン水を排液口26から流出させ、排液管2
8を通ってオゾン水を急速に排出させた後、処理槽12
内へ純水を供給して、処理槽12の内部に純水を満たし
処理槽12の上部の溢流部18から純水が溢れ出て溢流
受け部20内へ流入する状態にする。この状態におい
て、ウエハWが純水中に浸漬させられて水洗される。水
洗が終了すると、ウエハWは処理槽12から搬出され
る。When the processing of the wafer W with the ozone water is completed, the supply of the ozone water is stopped, and pure water is supplied from the pure water supply pipe 36 to the liquid supply port 16 of the processing tank 12 through the liquid supply pipe 32 to process the wafer W. Pure water is allowed to flow into the tank 12, and the ozone water is pushed out from the overflow portion 18 on the upper part of the processing tank 12 with the pure water, and the inside of the processing tank 12 is replaced with pure water. So that the pure water overflows from the overflow portion 18 at the upper part of the treatment tank 12 and flows into the overflow receiving portion 20. Alternatively, the drainage valve 30 is opened to allow the ozone water in the processing tank 12 to flow out from the drainage port 26, and the drainage pipe 2
8 to quickly discharge the ozone water,
Pure water is supplied to the inside, so that the inside of the processing tank 12 is filled with the pure water, and the pure water overflows from the overflow section 18 on the upper part of the processing tank 12 and flows into the overflow receiving section 20. In this state, the wafer W is immersed in pure water and washed. When the washing is completed, the wafer W is carried out of the processing tank 12.
【0008】[0008]
【発明が解決しようとする課題】上記したようにオゾン
水を用いて基板の表面から有機物を分解除去する処理に
おいて、オゾン水中のオゾンと有機物との反応速度R
は、R=k×C×T(k:反応定数、C:溶存オゾン濃
度、T:処理温度)で表される。したがって、溶存オゾ
ン濃度Cが高いほど、また処理濃度Tが高くなるほど反
応速度Rは大きくなる。As described above, in the process of decomposing and removing organic substances from the surface of a substrate using ozone water, the reaction rate R between ozone and the organic substances in ozone water is determined as follows.
Is represented by R = k × C × T (k: reaction constant, C: dissolved ozone concentration, T: processing temperature). Therefore, the reaction rate R increases as the dissolved ozone concentration C increases and the treatment concentration T increases.
【0009】ところが、溶存オゾン濃度Cと処理温度T
とは相反する関係にある。すなわち、反応速度Rを大き
くしようとして処理温度T(オゾン水の液温)を高くす
ると、オゾンの溶解度が小さくなり、溶存オゾン濃度C
が小さくなって、反応速度Rが低下することになる。一
方、溶存オゾン濃度Cを高くして反応速度Rを大きくし
ようとして、オゾン水の液温を下げると、処理温度Tが
低下して、反応速度Rが低下することになる。また、処
理槽内へオゾン水発生器から常温のオゾン水を供給して
基板の処理を行う場合には、溶存オゾン濃度が低くなる
ため、反応速度Rは変わらない。このように、溶存オゾ
ン濃度Cと処理温度Tとを共に高くして反応速度Rを大
きくする、といったことは不可能である。However, the dissolved ozone concentration C and the processing temperature T
Is in an opposite relationship. That is, if the processing temperature T (liquid temperature of ozone water) is increased in order to increase the reaction rate R, the solubility of ozone decreases, and the dissolved ozone concentration C
Becomes small, and the reaction rate R decreases. On the other hand, if the liquid temperature of the ozone water is lowered in order to increase the dissolved ozone concentration C to increase the reaction rate R, the processing temperature T decreases, and the reaction rate R decreases. When the substrate is processed by supplying ozone water at normal temperature from the ozone water generator into the processing tank, the reaction rate R does not change because the dissolved ozone concentration decreases. As described above, it is impossible to increase the reaction rate R by increasing both the dissolved ozone concentration C and the processing temperature T.
【0010】したがって、従来は、オゾン水中のオゾン
と有機物との反応速度をある限度以上に大きくすること
ができず、このため、オゾン水による基板の処理時間が
長くなって、スループットが低くなるという問題点があ
った。Therefore, conventionally, the reaction rate between the ozone and the organic matter in the ozone water cannot be increased beyond a certain limit, so that the processing time of the substrate with the ozone water becomes longer and the throughput becomes lower. There was a problem.
【0011】この発明は、以上のような事情に鑑みてな
されたものであり、オゾン水による基板の処理時間を短
くして、スループットを高くすることができる基板処理
方法を提供すること、ならびに、その方法を好適に実施
することができる基板処理装置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 provides a substrate processing method capable of shortening the processing time of a substrate with ozone water and increasing throughput. It is an object of the present invention to provide a substrate processing apparatus capable of suitably performing the method.
【0012】[0012]
【課題を解決するための手段】請求項1に係る発明は、
オゾンが溶解したオゾン水中に基板を浸漬させて処理す
る基板処理方法において、基板を加熱する基板加熱工程
と、加熱された基板をオゾン水中に浸漬させて処理する
基板処理工程と、を含むことを特徴とする。The invention according to claim 1 is
In a substrate processing method of immersing a substrate in ozone water in which ozone is dissolved, the substrate processing method includes a substrate heating step of heating the substrate, and a substrate processing step of immersing the heated substrate in ozone water to perform processing. Features.
【0013】請求項2に係る発明は、オゾンが溶解した
オゾン水を収容しそのオゾン水中に基板が浸漬させられ
て処理されるオゾン処理槽と、このオゾン処理槽内へオ
ゾン水を供給するオゾン水供給手段と、を備えた基板処
理装置において、高温に加熱された液体を収容しその液
体中に基板が浸漬させられて加熱される加熱処理槽と、
この加熱処理槽と前記オゾン処理槽との相互間で基板を
搬送する基板搬送手段と、をさらに備えたことを特徴と
する。According to a second aspect of the present invention, there is provided an ozone treatment tank in which ozone water in which ozone is dissolved is accommodated, and a substrate is immersed in the ozone water for treatment, and ozone is supplied to the ozone treatment tank. In a substrate processing apparatus provided with a water supply unit, a heat treatment tank containing a liquid heated to a high temperature and being heated by immersing the substrate in the liquid,
A substrate transfer means for transferring a substrate between the heat treatment tank and the ozone treatment tank is further provided.
【0014】請求項3に係る発明は、オゾンが溶解した
オゾン水を収容しそのオゾン水中に基板が浸漬させられ
て処理されるオゾン処理槽と、このオゾン処理槽内へオ
ゾン水を供給するオゾン水供給手段と、を備えた基板処
理装置において、前記オゾン処理槽を複数設けるととも
に、高温に加熱された液体を収容しその液体中に基板が
浸漬させられて加熱される加熱処理槽を備え、1つのオ
ゾン処理槽から前記加熱処理槽へ、その加熱処理槽から
次のオゾン処理槽へと順次基板を搬送する基板搬送手段
をさらに備えたことを特徴とする。According to a third aspect of the present invention, there is provided an ozone treatment tank for storing ozone water in which ozone is dissolved and treating the substrate by immersing the substrate in the ozone water, and supplying ozone water to the ozone treatment tank. And a water supply means, the substrate processing apparatus provided with a plurality of the ozone treatment tank, a heat treatment tank containing a liquid heated to a high temperature, the substrate is immersed in the liquid and heated. A substrate transfer means for sequentially transferring a substrate from one ozone treatment tank to the heat treatment tank and from the heat treatment tank to the next ozone treatment tank is further provided.
【0015】請求項4に係る発明は、オゾンが溶解した
オゾン水を収容しそのオゾン水中に基板が浸漬させられ
て処理される処理槽と、この処理槽内へオゾン水を供給
するオゾン水供給手段と、を備えた基板処理装置におい
て、前記処理槽の外側に配設されて基板を加熱する加熱
手段と、この加熱手段の配設位置と前記処理槽との相互
間で基板を搬送する基板搬送手段と、をさらに備えたこ
とを特徴とする。According to a fourth aspect of the present invention, there is provided a processing tank in which ozone water in which ozone is dissolved is accommodated and a substrate is immersed in the ozone water for processing, and an ozone water supply for supplying the ozone water into the processing tank. Means for heating a substrate disposed outside the processing tank and heating the substrate, and a substrate for transferring the substrate between the position where the heating means is disposed and the processing tank. And transport means.
【0016】請求項5に係る発明は、オゾンが溶解した
オゾン水を収容しそのオゾン水中に基板が浸漬させられ
て処理される処理槽と、この処理槽内へオゾン水を供給
する第1オゾン水供給手段と、前記処理槽内から液体を
排出する排液手段と、を備えた基板処理装置において、
前記処理槽内へ高温に加熱された液体を供給する第1液
体供給手段と、前記処理槽内に収容された基板の表面に
対し処理槽の上部から高温に加熱された液体を供給する
第2液体供給手段と、前記処理槽内に収容された基板の
表面に対し処理槽の上部からオゾンが溶解したオゾン水
を供給する第2オゾン水供給手段と、をさらに備えたこ
とを特徴とする。According to a fifth aspect of the present invention, there is provided a processing tank in which ozone water in which ozone is dissolved is stored and a substrate is immersed in the ozone water for processing, and a first ozone for supplying ozone water into the processing tank. In a substrate processing apparatus comprising: a water supply unit; and a drainage unit that discharges a liquid from the processing tank.
A first liquid supply unit configured to supply a liquid heated to a high temperature into the processing tank; and a second liquid supply unit configured to supply a liquid heated to a high temperature from an upper portion of the processing tank to a surface of a substrate housed in the processing tank. Liquid supply means and second ozone water supply means for supplying ozone water in which ozone is dissolved from the upper part of the processing tank to the surface of the substrate accommodated in the processing tank are further provided.
【0017】請求項1に係る発明の基板処理方法による
と、加熱された基板を低温のオゾン水中に浸漬させて
も、基板の温度は直ぐには低下しないので、基板の表面
では、高い温度条件の下でオゾン水中のオゾンと基板表
面上の有機物とが反応することになる。したがって、低
温で高溶存オゾン濃度のオゾン水を調製して、そのオゾ
ン水中に高温の基板を浸漬させて処理することにより、
溶存オゾン濃度と処理温度とを共に高くして、オゾンと
有機物との反応速度を大きくすることができる。このた
め、オゾン水による基板の処理時間を短くすることがで
きる。According to the substrate processing method of the first aspect of the present invention, even if the heated substrate is immersed in low-temperature ozone water, the temperature of the substrate does not immediately decrease. Below, the ozone in the ozone water reacts with the organic matter on the substrate surface. Therefore, by preparing ozone water with a high dissolved ozone concentration at a low temperature, and immersing a high-temperature substrate in the ozone water and treating,
By increasing both the dissolved ozone concentration and the processing temperature, the reaction rate between ozone and organic substances can be increased. Therefore, the processing time of the substrate with ozone water can be shortened.
【0018】請求項2に係る発明の基板処理装置におい
ては、高温に加熱されて加熱処理槽内に収容された液体
中に基板を浸漬させて加熱し、その加熱された基板を基
板搬送手段によりオゾン処理槽へ搬送して、オゾン処理
槽内に収容されたオゾン水中に浸漬させて処理すると、
基板が低温のオゾン水中に浸漬させられても、基板の温
度は直ぐには低下しない。このため、基板の表面では、
高い温度条件の下でオゾン水中のオゾンと基板表面上の
有機物とが反応することになる。したがって、オゾン水
供給手段により、低温で高溶存オゾン濃度のオゾン水を
調製してオゾン処理槽内へ供給し、そのオゾン水中に加
熱処理槽で加熱された基板を浸漬させて処理すると、溶
存オゾン濃度と処理温度とが共に高い状態でオゾンと有
機物との反応が行われ、その反応速度が大きくなる。こ
のため、オゾン水による基板の処理時間が短くなる。そ
して、基板の表面から有機物が完全に除去されるまで、
基板搬送手段によって基板を加熱処理槽とオゾン処理槽
との相互間で搬送しつつ、例えば、オゾン処理槽→加熱
処理槽→オゾン処理槽、加熱処理槽→オゾン処理槽→加
熱処理槽→オゾン処理槽、あるいはオゾン処理槽→加熱
処理槽→オゾン処理槽→加熱処理槽→オゾン処理槽とい
ったように基板を搬送しつつ、加熱処理槽での基板の加
熱とオゾン処理槽でのオゾン水による基板の処理とを繰
り返すようにすればよい。In the substrate processing apparatus according to the second aspect of the present invention, the substrate is immersed and heated in a liquid heated in a high temperature and contained in a heat treatment tank, and the heated substrate is transferred by the substrate transfer means. When transported to the ozone treatment tank and immersed in ozone water contained in the ozone treatment tank for processing,
Even if the substrate is immersed in low-temperature ozone water, the temperature of the substrate does not decrease immediately. Therefore, on the surface of the substrate,
Under high temperature conditions, the ozone in the ozone water reacts with the organic matter on the substrate surface. Therefore, ozone water having a high dissolved ozone concentration at a low temperature is prepared and supplied into an ozone treatment tank by an ozone water supply means, and a substrate heated in a heat treatment tank is immersed in the ozone water for treatment. The reaction between the ozone and the organic substance is performed in a state where both the concentration and the processing temperature are high, and the reaction speed increases. Therefore, the processing time of the substrate with ozone water is shortened. Then, until the organic matter is completely removed from the surface of the substrate,
While the substrate is transferred between the heat treatment tank and the ozone treatment tank by the substrate transfer means, for example, an ozone treatment tank → a heat treatment tank → an ozone treatment tank, a heat treatment tank → an ozone treatment tank → a heat treatment tank → ozone treatment Heating the substrate in the heat treatment tank and the ozone water in the ozone treatment tank while transporting the substrate in a tank or ozone treatment tank → heat treatment tank → ozone treatment tank → heat treatment tank → ozone treatment tank. The processing may be repeated.
【0019】請求項3に係る発明の基板処理装置におい
ては、高温に加熱されて加熱処理槽内に収容された液体
中に基板を浸漬させて加熱し、その加熱された基板を基
板搬送手段によりオゾン処理槽へ搬送して、オゾン処理
槽内に収容されたオゾン水中に浸漬させて処理すると、
基板が低温のオゾン水中に浸漬させられても、基板の温
度は直ぐには低下しない。このため、基板の表面では、
高い温度条件の下でオゾン水中のオゾンと基板表面上の
有機物とが反応することになる。したがって、オゾン水
供給手段により、低温で高溶存オゾン濃度のオゾン水を
調製してオゾン処理槽内へ供給し、そのオゾン水中に加
熱処理槽で加熱された基板を浸漬させて処理すると、溶
存オゾン濃度と処理温度とが共に高い状態でオゾンと有
機物との反応が行われ、その反応速度が大きくなる。こ
のため、オゾン水による基板の処理時間が短くなる。そ
して、基板の表面から有機物が完全に除去されるまで、
基板搬送手段によって基板を1つのオゾン処理槽から加
熱処理槽へ、その加熱処理槽から次のオゾン処理槽へと
順次搬送しつつ、例えば、第1のオゾン処理槽→加熱処
理槽→第2のオゾン処理槽、第1の加熱処理槽→第1の
オゾン処理槽→第2の加熱処理槽→第2のオゾン処理
槽、あるいは第1のオゾン処理槽→第1の加熱処理槽→
第2のオゾン処理槽→第2の加熱処理槽→第3のオゾン
処理槽といったように基板を搬送しつつ、加熱処理槽で
の基板の加熱とオゾン処理槽でのオゾン水による基板の
処理とを繰り返すようにすればよい。In the substrate processing apparatus according to the third aspect of the present invention, the substrate is immersed in a liquid which is heated to a high temperature and accommodated in a heat treatment tank and heated, and the heated substrate is transferred by the substrate transfer means. When transported to the ozone treatment tank and immersed in ozone water contained in the ozone treatment tank for processing,
Even if the substrate is immersed in low-temperature ozone water, the temperature of the substrate does not decrease immediately. Therefore, on the surface of the substrate,
Under high temperature conditions, the ozone in the ozone water reacts with the organic matter on the substrate surface. Therefore, ozone water having a high dissolved ozone concentration at a low temperature is prepared and supplied into an ozone treatment tank by an ozone water supply means, and a substrate heated in a heat treatment tank is immersed in the ozone water for treatment. The reaction between the ozone and the organic substance is performed in a state where both the concentration and the processing temperature are high, and the reaction speed increases. Therefore, the processing time of the substrate with ozone water is shortened. Then, until the organic matter is completely removed from the surface of the substrate,
While sequentially transferring the substrate from one ozone treatment tank to the heat treatment tank and from the heat treatment tank to the next ozone treatment tank by the substrate transfer means, for example, the first ozone treatment tank → the heat treatment tank → the second Ozone treatment tank, first heat treatment tank → first ozone treatment tank → second heat treatment tank → second ozone treatment tank, or first ozone treatment tank → first heat treatment tank →
Heating the substrate in the heat treatment tank and treating the substrate with ozone water in the ozone treatment tank while transporting the substrate in the order of the second ozone treatment tank → the second heat treatment tank → the third ozone treatment tank. May be repeated.
【0020】請求項4に係る発明の基板処理装置におい
ては、処理槽の外側に配設された加熱手段により基板を
加熱し、その加熱された基板を基板搬送手段により処理
槽へ搬送して、処理槽内に収容されたオゾン水中に浸漬
させて処理すると、基板が低温のオゾン水中に浸漬させ
られても、基板の温度は直ぐには低下しない。このた
め、基板の表面では、高い温度条件の下でオゾン水中の
オゾンと基板表面上の有機物とが反応することになる。
したがって、オゾン水供給手段により、低温で高溶存オ
ゾン濃度のオゾン水を調製して処理槽内へ供給し、その
オゾン水中に加熱手段で加熱された基板を浸漬させて処
理すると、溶存オゾン濃度と処理温度とが共に高い状態
でオゾンと有機物との反応が行われ、その反応速度が大
きくなる。このため、オゾン水による基板の処理時間が
短くなる。そして、基板の表面から有機物が完全に除去
されるまで、基板搬送手段によって基板を加熱手段の配
設位置と処理槽との相互間で搬送しつつ、例えば、処理
槽→加熱手段→処理槽、加熱手段→処理槽→加熱手段→
処理槽、あるいは処理槽→加熱手段→処理槽→加熱手段
→処理槽といったように基板を搬送しつつ、加熱手段で
の基板の加熱と処理槽でのオゾン水による基板の処理と
を繰り返すようにすればよい。In the substrate processing apparatus according to the present invention, the substrate is heated by the heating means provided outside the processing tank, and the heated substrate is transferred to the processing tank by the substrate transferring means. When the substrate is immersed in the ozone water contained in the processing tank for processing, the temperature of the substrate does not immediately decrease even if the substrate is immersed in the low-temperature ozone water. Therefore, on the surface of the substrate, the ozone in the ozone water reacts with the organic matter on the substrate surface under high temperature conditions.
Therefore, when the ozone water having a high dissolved ozone concentration is prepared at a low temperature by the ozone water supply means and supplied into the processing tank, and the substrate heated by the heating means is immersed in the ozone water for processing, the dissolved ozone concentration is reduced. The reaction between the ozone and the organic substance is performed in a state where both the processing temperature is high, and the reaction speed increases. Therefore, the processing time of the substrate with ozone water is shortened. Until the organic matter is completely removed from the surface of the substrate, the substrate is transported by the substrate transport means between the arrangement position of the heating means and the processing tank, for example, processing tank → heating means → processing tank, Heating means → treatment tank → heating means →
While transporting the substrate such as a processing tank or a processing tank → a heating means → a processing tank → a heating means → a processing tank, the heating of the substrate by the heating means and the processing of the substrate by the ozone water in the processing tank are repeated. do it.
【0021】請求項5に係る発明の基板処理装置におい
ては、処理槽内に収容された基板が、第2液体供給手段
から供給される高温に加熱された液体と接触しもしくは
第2液体供給手段により高温に加熱されて処理槽内へ供
給され処理槽内に収容された液体中に浸漬させられるこ
とにより加熱され、あるいは、第1液体供給手段により
高温に加熱されて処理槽内へ供給された液体中に浸漬さ
れることにより加熱される。このようにして加熱された
処理槽内の基板は、第1オゾン水供給手段により処理槽
内へ供給され処理槽内に収容されたオゾン水中に浸漬さ
せられて処理され、あるいは、第2オゾン水供給手段か
ら供給されるオゾン水と接触しもしくは第2オゾン水供
給手段により処理槽内へ供給され処理槽内に収容された
オゾン水中に浸漬させられて処理される。このとき、基
板が低温のオゾン水中に浸漬させられあるいは低温のオ
ゾン水と接触しても、基板の温度は直ぐには低下しな
い。このため、基板の表面では、高い温度条件の下でオ
ゾン水中のオゾンと基板表面上の有機物とが反応するこ
とになる。したがって、第1オゾン水供給手段により、
低温で高溶存オゾン濃度のオゾン水を調製して処理槽内
へ供給し、そのオゾン水中に加熱された基板を浸漬させ
て処理すると、あるいは、第2オゾン水供給手段によ
り、低温で高溶存オゾン濃度のオゾン水を調製して処理
槽内へ供給し、そのオゾン水と加熱された基板を接触さ
せもしくはそのオゾン水中に加熱された基板を浸漬させ
て処理すると、溶存オゾン濃度と処理温度とが共に高い
状態でオゾンと有機物との反応が行われ、その反応速度
が大きくなる。このため、オゾン水による基板の処理時
間が短くなる。そして、基板の表面から有機物が完全に
除去されるまで、排液手段により処理槽内から適宜液体
を排出しつつ、第2液体供給手段による液体の供給、第
1オゾン水供給手段によるオゾン水の供給、第1液体供
給手段による液体の供給および第2オゾン水供給手段に
よるオゾン水の供給を順番に行い、基板の加熱とオゾン
水による基板の処理とを繰り返すようにすればよい。In the substrate processing apparatus according to the fifth aspect of the present invention, the substrate accommodated in the processing tank is brought into contact with the liquid heated to a high temperature supplied from the second liquid supply means or the second liquid supply means. Heated to a high temperature and supplied to the processing tank and immersed in the liquid contained in the processing tank, or heated by the first liquid supply means and supplied to the processing tank. It is heated by being immersed in a liquid. The substrate in the processing tank heated as described above is supplied into the processing tank by the first ozone water supply means and immersed in the ozone water contained in the processing tank to be processed, or the second ozone water is supplied. The treatment is performed by contacting with the ozone water supplied from the supply means or by being supplied into the treatment tank by the second ozone water supply means and immersed in the ozone water contained in the treatment tank. At this time, even if the substrate is immersed in low-temperature ozone water or comes into contact with low-temperature ozone water, the temperature of the substrate does not decrease immediately. Therefore, on the surface of the substrate, the ozone in the ozone water reacts with the organic matter on the substrate surface under high temperature conditions. Therefore, by the first ozone water supply means,
Ozone water having a high dissolved ozone concentration is prepared at a low temperature and supplied into a processing tank, and a heated substrate is immersed in the ozone water for processing. Concentration ozone water is prepared and supplied into the processing tank, and the ozone water is brought into contact with the heated substrate or the heated substrate is immersed in the ozone water for processing. The reaction between the ozone and the organic substance is performed in a high state, and the reaction speed increases. Therefore, the processing time of the substrate with ozone water is shortened. Until the organic matter is completely removed from the surface of the substrate, the liquid is supplied from the processing tank by the liquid discharging means, the liquid is supplied from the second liquid supplying means, and the ozone water is supplied from the first ozone water supplying means. The supply, the supply of the liquid by the first liquid supply unit, and the supply of the ozone water by the second ozone water supply unit may be sequentially performed, and the heating of the substrate and the treatment of the substrate with the ozone water may be repeated.
【0022】なお、請求項2、請求項3および請求項5
に記載の「液体」としては、40℃〜150℃に加熱し
た液体が考えられる。具体的には、純水と塩酸の混合
液、純水と酢酸の混合液、純水と硫酸の混合液、純水と
過酸化水素水の混合液、純水とリン酸の混合液、あるい
は純水のみが挙げられる。純水のみである場合、すなわ
ち温純水である場合、加熱処理槽の水洗は不要となり、
安価で済む。It should be noted that claims 2, 3, and 5
As the “liquid” described in (1), a liquid heated to 40 ° C. to 150 ° C. is considered. Specifically, a mixture of pure water and hydrochloric acid, a mixture of pure water and acetic acid, a mixture of pure water and sulfuric acid, a mixture of pure water and hydrogen peroxide, a mixture of pure water and phosphoric acid, or Only pure water is mentioned. In the case of pure water only, that is, in the case of warm pure water, washing of the heat treatment tank becomes unnecessary,
Inexpensive.
【0023】[0023]
【発明の実施の形態】以下、この発明の好適な実施形態
について図1ないし図5を参照しながら説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred embodiment of the present invention will be described below with reference to FIGS.
【0024】図1は、この発明に係る基板処理方法を実
施するために使用される基板処理装置の構成の1例を示
す概略図である。この装置は、基板処理部10と基板加
熱部46とを備えて構成されている。これらのうち、基
板処理部10の構成は、図6に示した上述の、オゾン水
を用いる従来の基板処理装置と同じであるので、その説
明を省略する。また、図示していないが、この装置に
は、基板処理部10と基板加熱部46との相互間でウエ
ハWを搬送するためのウエハ搬送機構が設けられてい
る。FIG. 1 is a schematic diagram showing an example of the configuration of a substrate processing apparatus used to carry out the substrate processing method according to the present invention. This apparatus includes a substrate processing unit 10 and a substrate heating unit 46. Among these, the configuration of the substrate processing unit 10 is the same as the above-described conventional substrate processing apparatus using ozone water shown in FIG. Although not shown, the apparatus is provided with a wafer transfer mechanism for transferring the wafer W between the substrate processing unit 10 and the substrate heating unit 46.
【0025】基板加熱部46は、高温、例えば沸点近く
の温度に加熱された温純水を内部に収容しその温純水中
にウエハWがウエハホルダ14に保持されて浸漬させら
れる温純水槽48を備えている。温純水槽48は、本発
明の加熱処理槽に相当し、下部に温純水給排口50を有
するとともに、上部に温純水が溢れ出す溢流部52を有
する。また、温純水槽48には、溢流水受け部54が付
設されており、温純水槽48上部の溢流部52から溢れ
出た温純水が溢流水受け部54内へ流入するようになっ
ている。溢流水受け部54の底部には、温純水循環用配
管56の一端が連通して接続されており、温純水循環用
配管56の他端が、温純水槽48の温純水給排口50に
連通して接続されている。The substrate heating section 46 includes a hot pure water tank 48 in which hot pure water heated to a high temperature, for example, near the boiling point is accommodated, and the wafer W is held by the wafer holder 14 and immersed in the hot pure water. . The hot pure water tank 48 corresponds to the heat treatment tank of the present invention, and has a hot pure water supply / discharge port 50 at a lower part and an overflow part 52 from which hot pure water overflows at an upper part. Further, the hot pure water tank 48 is provided with an overflow water receiving portion 54, and the hot pure water overflowing from the overflow portion 52 above the hot pure water tank 48 flows into the overflow water receiving portion 54. . One end of a hot pure water circulation pipe 56 is connected to and connected to the bottom of the overflow water receiving portion 54, and the other end of the hot pure water circulation pipe 56 communicates with the hot pure water supply / discharge port 50 of the hot pure water tank 48. It is connected.
【0026】温純水循環用配管56には、ポンプ58、
ヒーター60およびフィルタ62がそれぞれ介在して設
けられている。また、温純水循環用配管56は、途中で
分岐しており、その分岐管64に、純水供給源に接続さ
れ開閉制御弁68が介挿された純水供給管66、およ
び、開閉制御弁72が介挿されたドレイン排出管70が
それぞれ接続されている。A pump 58, a hot pure water circulation pipe 56,
A heater 60 and a filter 62 are provided therebetween. The hot-purified water circulation pipe 56 is branched in the middle, and a pure water supply pipe 66 connected to a pure water supply source and having an open / close control valve 68 interposed therein, and a switch valve 72. Are connected to each other.
【0027】この基板加熱部46では、常時、温純水槽
48の内部と温純水循環用配管56との間で所定温度に
加熱された温純水が循環している。そして、温純水槽4
6内の温純水中にウエハWが所定時間だけ浸漬させられ
ることにより、ウエハWが加熱されるようになってい
る。In the substrate heating section 46, hot pure water heated to a predetermined temperature is constantly circulated between the inside of the hot pure water tank 48 and the hot pure water circulation pipe 56. And hot pure water tank 4
The wafer W is heated by being immersed in the hot pure water in the wafer 6 for a predetermined time.
【0028】次に、上記した構成の基板処理装置を使用
し、ウエハWの表面に付着したレジスト等の有機物を分
解除去する処理動作の1例を説明する。Next, an example of a processing operation for decomposing and removing an organic substance such as a resist attached to the surface of the wafer W using the substrate processing apparatus having the above-described configuration will be described.
【0029】まず、基板処理部10において、上述した
ような操作により、オゾン処理槽12の内部にオゾン水
を満たしオゾン処理槽12の上部の溢流部18からオゾ
ン水が溢れ出て溢流受け部20内へ流入する状態にし、
ウエハWをオゾン処理槽12内のオゾン水中に浸漬させ
て、1回目のウエハWの処理を行う。この際、オゾン水
供給源では、低温で高溶存オゾン濃度のオゾン水を調製
し、そのオゾン水を、オゾン水供給管42から液体供給
管32を通してオゾン処理槽12の液体供給口16へ供
給し、オゾン処理槽12内を高溶存オゾン濃度のオゾン
水で満たしておくようにする。First, in the substrate processing section 10, the inside of the ozone treatment tank 12 is filled with ozone water by the above-described operation, and the ozone water overflows from the overflow section 18 on the upper part of the ozone treatment tank 12 and overflows. In the state of flowing into the part 20,
The first processing of the wafer W is performed by immersing the wafer W in ozone water in the ozone processing tank 12. At this time, the ozone water supply source prepares ozone water having a high dissolved ozone concentration at a low temperature, and supplies the ozone water from the ozone water supply pipe 42 to the liquid supply port 16 of the ozone treatment tank 12 through the liquid supply pipe 32. The ozone treatment tank 12 is filled with ozone water having a high dissolved ozone concentration.
【0030】1回目のウエハWの処理が終わると、ウエ
ハWをオゾン処理槽12内のオゾン水中から引き上げ、
そのウエハWをウエハ搬送機構により基板加熱部46へ
搬送する。そして、基板加熱部46において、温純水槽
48内に収容された高温の温純水中にウエハWを所定時
間だけ浸漬させて加熱する。When the first processing of the wafer W is completed, the wafer W is lifted from the ozone water in the ozone processing tank 12 and
The wafer W is transferred to the substrate heating section 46 by the wafer transfer mechanism. Then, in the substrate heating unit 46, the wafer W is immersed in the high-temperature hot pure water accommodated in the hot pure water tank 48 for a predetermined time and heated.
【0031】続いて、ウエハWを温純水槽48内の温純
水中から引き上げ、その加熱されたウエハWをウエハ搬
送機構により再び基板処理部10へ搬送する。そして、
基板処理部10において、加熱されたウエハWを再びオ
ゾン処理槽12内の高溶存オゾン濃度のオゾン水中に浸
漬させて、2回目のウエハWの処理を行う。このとき、
加熱されたウエハWが低温のオゾン水中に浸漬させられ
ても、ウエハWの温度は直ぐには低下しない。このた
め、ウエハWの表面では、高い温度条件の下で高溶存濃
度のオゾンと有機物とが反応することになり、その反応
速度が大きくなる。したがって、オゾン水によるウエハ
Wの処理が速やかに進行することになる。Subsequently, the wafer W is lifted out of the hot pure water in the hot pure water tank 48, and the heated wafer W is transferred to the substrate processing unit 10 again by the wafer transfer mechanism. And
In the substrate processing section 10, the heated wafer W is immersed again in ozone water having a high dissolved ozone concentration in the ozone processing tank 12, and the second processing of the wafer W is performed. At this time,
Even if the heated wafer W is immersed in low-temperature ozone water, the temperature of the wafer W does not decrease immediately. Therefore, on the surface of the wafer W, the ozone having a high dissolved concentration reacts with the organic substance under a high temperature condition, and the reaction speed increases. Therefore, the processing of the wafer W with the ozone water proceeds promptly.
【0032】ウエハWがオゾン処理槽12内の低温のオ
ゾン水中に浸漬させられている間に、ウエハWの温度
が、例えば常温付近まで低下してくると、ウエハWをオ
ゾン処理槽12内のオゾン水中から引き上げ、そのウエ
ハWをウエハ搬送機構により再び基板加熱部46へ搬送
する。そして、基板加熱部46において、ウエハWを再
び温純水槽48内の高温の温純水中に浸漬させて加熱す
る。ウエハWが加熱されて高温になると、ウエハWを温
純水槽48内の温純水中から引き上げ、加熱されたウエ
ハWをウエハ搬送機構により再び基板処理部10へ搬送
し、加熱されたウエハWを再びオゾン処理槽12内の高
溶存オゾン濃度のオゾン水中に浸漬させて、3回目のウ
エハWの処理を行う。以上のようなウエハWの加熱とウ
エハWの処理とを、ウエハWの表面から有機物が完全に
除去されるまで繰り返す。When the temperature of the wafer W decreases to, for example, near normal temperature while the wafer W is immersed in the low-temperature ozone water in the ozone processing tank 12, the wafer W is moved into the ozone processing tank 12. The wafer W is lifted out of the ozone water, and is transferred to the substrate heating unit 46 again by the wafer transfer mechanism. Then, in the substrate heating section 46, the wafer W is immersed again in high-temperature hot pure water in the hot pure water tank 48 and heated. When the wafer W is heated to a high temperature, the wafer W is lifted out of the hot pure water in the hot pure water tank 48, the heated wafer W is transported again to the substrate processing unit 10 by the wafer transport mechanism, and the heated wafer W is again transported. The third processing of the wafer W is performed by immersing the wafer W in ozone water having a high dissolved ozone concentration in the ozone processing tank 12. The heating of the wafer W and the processing of the wafer W as described above are repeated until organic substances are completely removed from the surface of the wafer W.
【0033】オゾン水によるウエハWの処理が終わる
と、上述したように、オゾン処理槽12内へのオゾン水
の供給を停止させるとともに、オゾン処理槽12内へ純
水を供給して、オゾン処理槽12の内部に純水を満たし
オゾン処理槽12の上部の溢流部18から純水が溢れ出
て溢流受け部20内へ流入する状態にし、ウエハWをオ
ゾン処理槽12内の純水中に浸漬させてウエハWを水洗
する。水洗が終了すると、ウエハWは、オゾン処理槽1
2内から引き上げられ、乾燥処理された後、装置外へ搬
出される。When the processing of the wafer W with the ozone water is completed, the supply of the ozone water into the ozone processing tank 12 is stopped, and the pure water is supplied into the ozone processing tank 12 as described above. The inside of the tank 12 is filled with pure water, and the pure water overflows from the overflow part 18 at the upper part of the ozone treatment tank 12 and flows into the overflow receiving part 20. The wafer W is rinsed with water by immersing the wafer W therein. When the washing is completed, the wafer W is removed from the ozone treatment tank 1.
After being lifted from the inside and dried, it is carried out of the apparatus.
【0034】温純水槽48に90℃の温純水を収容さ
せ、上記した一連の処理を行って評価した結果では、従
来の処理に比べて反応速度が5倍程度も向上した。The results of a series of processes described above in which hot pure water at 90 ° C. was stored in the hot pure water tank 48 and evaluated were as follows: the reaction rate was improved about 5 times as compared with the conventional process.
【0035】なお、上記した説明では、最初に、低温の
高溶存オゾン濃度のオゾン水でウエハWを一度処理し、
その後に、ウエハWを基板処理部10から基板加熱部4
6へ搬送して、ウエハWを温純水で加熱するようにして
いるが、最初に、ウエハWを基板加熱部46へ搬送して
基板加熱部46で加熱し、その後に、ウエハWを基板加
熱部46から基板処理部46へ搬送して、低温の高溶存
オゾン濃度のオゾン水による1回目のウエハWの処理を
行うようにしてもよい。In the above description, first, the wafer W is once treated with ozone water having a low dissolved ozone concentration at a low temperature.
Thereafter, the wafer W is transferred from the substrate processing unit 10 to the substrate heating unit 4.
6, the wafer W is heated with hot pure water. First, the wafer W is transferred to the substrate heating unit 46 and heated by the substrate heating unit 46, and then the wafer W is heated by the substrate heating unit. The wafer W may be transported from the substrate processing unit 46 to the substrate processing unit 46, and the first processing of the wafer W with ozone water having a low temperature and a high dissolved ozone concentration may be performed.
【0036】また、上記した一連の処理を加圧下で行う
と、オゾン水の溶存オゾン濃度をより高くすることが可
能になり、また、純水等の溶液の沸点が高くなって処理
温度をより高くすることが可能になるので、好ましい。
さらに、有機物との反応速度の大きいOHラジカルをオ
ゾン水中で発生させる目的で、メガソニック照射、過酸
化水素水の添加、紫外線照射、放射線照射等をオゾン水
による処理に併用してもよい。また、オゾン水の半減期
を長くするために、pHの小さい酸(塩酸、フッ酸等)
の添加や、炭酸イオンや重炭酸イオンとなる炭酸やカル
ボン酸等をOHラジカルのスカベンジャー(消費物質)
として添加してもよい。When the above-described series of processes is performed under pressure, the dissolved ozone concentration of ozone water can be further increased, and the boiling point of a solution such as pure water can be increased to increase the process temperature. It is preferable because the height can be increased.
Further, for the purpose of generating OH radicals having a high reaction rate with organic substances in ozone water, megasonic irradiation, addition of hydrogen peroxide solution, ultraviolet irradiation, radiation irradiation and the like may be used in combination with the treatment with ozone water. Also, in order to prolong the half-life of ozone water, acid with low pH (hydrochloric acid, hydrofluoric acid, etc.)
Addition of carbonic acid and bicarbonate ions to carbonic acid and carboxylic acid to scavenger OH radicals (consumable substance)
May be added.
【0037】図2は、基板処理装置の別の構成例を示す
概略図である。この装置は、図1に示した装置の基板処
理部10および基板加熱部46と同じ構成の基板処理部
10a、10bおよび基板加熱部46a、46bをそれ
ぞれ複数、交互に連続して設置し、図示していないが、
第1の基板処理部10aから第1の基板加熱部46a
へ、第1の基板加熱部46aから第2の基板処理部10
bへ、第2の基板処理部10bから第2の基板加熱部4
6bへと順次ウエハWを搬送するウエハ搬送機構を備え
て構成されている。FIG. 2 is a schematic diagram showing another configuration example of the substrate processing apparatus. In this apparatus, a plurality of substrate processing units 10a and 10b and substrate heating units 46a and 46b each having the same configuration as the substrate processing unit 10 and the substrate heating unit 46 of the apparatus shown in FIG. Not shown,
From the first substrate processing unit 10a to the first substrate heating unit 46a
From the first substrate heating section 46a to the second substrate processing section 10
b, from the second substrate processing unit 10b to the second substrate heating unit 4
6b is provided with a wafer transfer mechanism for sequentially transferring wafers W to 6b.
【0038】図2に示した構成の基板処理装置を使用し
たウエハWの処理動作の1例について簡単に説明する
と、まず、第1の基板処理部10aにおいて、図1に示
した装置の基板処理部10における場合と同様の操作に
より、低温で高溶存オゾン濃度のオゾン水による1回目
のウエハWの処理を行う。1回目のウエハWの処理が終
わると、ウエハWをオゾン処理槽12内のオゾン水中か
ら引き上げ、そのウエハWをウエハ搬送機構により第1
の基板加熱部46aへ搬送する。そして、第1の基板加
熱部46aにおいて、図1に示した装置の基板加熱部4
6における場合と同様の操作により、高温の温純水によ
りウエハWを加熱する。An example of the processing operation of the wafer W using the substrate processing apparatus having the configuration shown in FIG. 2 will be briefly described. First, in the first substrate processing section 10a, the substrate processing of the apparatus shown in FIG. By the same operation as in the unit 10, the first processing of the wafer W with ozone water having a low dissolved ozone concentration at a low temperature is performed. When the first processing of the wafer W is completed, the wafer W is lifted out of the ozone water in the ozone processing tank 12, and the wafer W is moved to the first position by the wafer transfer mechanism.
To the substrate heating unit 46a. Then, in the first substrate heating section 46a, the substrate heating section 4 of the apparatus shown in FIG.
6, the wafer W is heated with high-temperature hot pure water.
【0039】続いて、ウエハWを温純水槽48内の温純
水中から引き上げ、その加熱されたウエハWをウエハ搬
送機構により第2の基板処理部10bへ搬送する。そし
て、第2の基板処理部10bにおいて、加熱されたウエ
ハWをオゾン処理槽12内の高溶存オゾン濃度のオゾン
水中に浸漬させて、2回目のウエハWの処理を行う。こ
のとき、ウエハWの表面では、高い温度条件の下で高溶
存濃度のオゾンと有機物とが反応することになり、オゾ
ン水によるウエハWの処理が速やかに進行することにな
る。Subsequently, the wafer W is lifted out of the hot pure water in the hot pure water tank 48, and the heated wafer W is transferred to the second substrate processing section 10b by the wafer transfer mechanism. Then, in the second substrate processing unit 10b, the heated wafer W is immersed in ozone water having a high dissolved ozone concentration in the ozone processing tank 12, and the second processing of the wafer W is performed. At this time, on the surface of the wafer W, a high dissolved concentration of ozone reacts with an organic substance under a high temperature condition, and the processing of the wafer W with ozone water proceeds promptly.
【0040】ウエハWがオゾン処理槽12内の低温のオ
ゾン水中に浸漬させられている間に、ウエハWの温度が
低下してくると、ウエハWをオゾン処理槽12内のオゾ
ン水中から引き上げ、そのウエハWをウエハ搬送機構に
より第2の基板加熱部46bへ搬送する。そして、第2
の基板加熱部46において、ウエハWを再び温純水槽4
8内の高温の温純水中に浸漬させて加熱する。ウエハW
が加熱されて高温になると、ウエハWを温純水槽48内
の温純水中から引き上げ、加熱されたウエハWをウエハ
搬送機構により次の基板処理部(図示せず)へ搬送し、
加熱されたウエハWを再びオゾン処理槽12内の高溶存
オゾン濃度のオゾン水中に浸漬させて、3回目のウエハ
Wの処理を行う。When the temperature of the wafer W decreases while the wafer W is immersed in the low-temperature ozone water in the ozone processing tank 12, the wafer W is pulled up from the ozone water in the ozone processing tank 12, The wafer W is transferred to the second substrate heating section 46b by the wafer transfer mechanism. And the second
In the substrate heating section 46 of FIG.
8 and immersed in high-temperature hot pure water and heated. Wafer W
Is heated to a high temperature, the wafer W is pulled up from the hot pure water in the hot pure water tank 48, and the heated wafer W is transferred to the next substrate processing unit (not shown) by the wafer transfer mechanism.
The heated wafer W is immersed again in ozone water having a high dissolved ozone concentration in the ozone treatment tank 12, and the third processing of the wafer W is performed.
【0041】以上のように、ウエハWを基板処理部と基
板加熱部へ交互に搬送しつつ、ウエハWの加熱とウエハ
Wの処理とを繰り返す。そして、ウエハWの表面から有
機物が完全に除去されると、処理の終わったウエハWが
収容されている最後のオゾン処理槽12内へ純水を供給
してウエハWを水洗する。水洗が終了すると、ウエハW
は、オゾン処理槽12内から引き上げられ、乾燥処理さ
れた後、装置外へ搬出される。As described above, the heating of the wafer W and the processing of the wafer W are repeated while the wafer W is alternately transported to the substrate processing section and the substrate heating section. When the organic matter is completely removed from the surface of the wafer W, pure water is supplied into the last ozone treatment tank 12 in which the processed wafer W is stored, and the wafer W is washed with water. When the washing is completed, the wafer W
Is taken out of the ozone treatment tank 12, dried, and then carried out of the apparatus.
【0042】なお、図2に示した装置では、先頭の位置
に基板処理部10aが設けられており、低温の高溶存オ
ゾン濃度のオゾン水でウエハWを一度処理した後に、ウ
エハWを基板加熱部46aへ搬送して、ウエハWを温純
水で加熱するようにしているが、先頭の位置に基板加熱
部を設けておき、ウエハWを基板加熱部で加熱した後
に、ウエハWを基板処理部へ搬送して、低温の高溶存オ
ゾン濃度のオゾン水による1回目のウエハWの処理を行
うようにしてもよい。In the apparatus shown in FIG. 2, a substrate processing section 10a is provided at the head position, and after processing the wafer W once with low-temperature ozone water having a high dissolved ozone concentration, the wafer W is heated. The wafer W is transported to the section 46a and heated with hot pure water. However, a substrate heating section is provided at the top position, and after the wafer W is heated by the substrate heating section, the wafer W is transferred to the substrate processing section. The wafer W may be transported to perform the first processing of the wafer W with ozone water having a low temperature and a high dissolved ozone concentration.
【0043】次に、図3は、基板処理装置のさらに別の
構成例を示す概略図である。この装置は、図1に示した
装置の基板処理部10と同じ構成の基板処理部74を備
え、そのオゾン処理槽12の直上位置に、ハロゲンラン
プ等のランプや(遠)赤外線ヒーターなどの加熱器78
を有する加熱部76が設けられ、図示していないが、基
板処理部74と加熱部76との相互間でウエハWを搬送
するウエハ搬送機構を備えて構成されている。Next, FIG. 3 is a schematic view showing another example of the configuration of the substrate processing apparatus. This apparatus includes a substrate processing section 74 having the same configuration as the substrate processing section 10 of the apparatus shown in FIG. 1, and a heater such as a halogen lamp or a (far) infrared heater is provided immediately above the ozone processing tank 12. Container 78
Is provided, and includes a wafer transfer mechanism (not shown) for transferring the wafer W between the substrate processing unit 74 and the heating unit 76.
【0044】図3に示した構成の基板処理装置を使用し
たウエハWの処理動作の1例について簡単に説明する
と、まず、基板処理部74において、図1に示した装置
の基板処理部10における場合と同様の操作により、低
温で高溶存オゾン濃度のオゾン水による1回目のウエハ
Wの処理を行う。1回目のウエハWの処理が終わると、
ウエハWをオゾン処理槽12内のオゾン水中から引き上
げ、そのウエハWをウエハ搬送機構により加熱部76へ
移動させ、加熱部76において、加熱器78によってウ
エハWを加熱する。ウエハWの加熱が終わると、その加
熱されたウエハWをウエハ搬送機構により基板処理部7
4へ移動させ、加熱されたウエハWを再びオゾン処理槽
12内の高溶存オゾン濃度のオゾン水中に浸漬させて、
2回目のウエハWの処理を行う。このとき、ウエハWの
表面では、高い温度条件の下で高溶存濃度のオゾンと有
機物とが反応することになり、オゾン水によるウエハW
の処理が速やかに進行することになる。An example of the processing operation of the wafer W using the substrate processing apparatus having the configuration shown in FIG. 3 will be briefly described. First, in the substrate processing section 74, the processing in the substrate processing section 10 of the apparatus shown in FIG. By the same operation as in the case, the first processing of the wafer W with ozone water having a low dissolved ozone concentration at a low temperature is performed. After the first processing of the wafer W,
The wafer W is pulled up from the ozone water in the ozone processing tank 12, the wafer W is moved to the heating section 76 by the wafer transfer mechanism, and the wafer W is heated by the heater 78 in the heating section 76. When the heating of the wafer W is completed, the heated wafer W is transferred to the substrate processing unit 7 by the wafer transfer mechanism.
4, the heated wafer W is immersed again in ozone water having a high dissolved ozone concentration in the ozone treatment tank 12,
The second processing of the wafer W is performed. At this time, on the surface of the wafer W, a high dissolved concentration of ozone and an organic substance react under high temperature conditions, and the wafer W
Will proceed promptly.
【0045】ウエハWがオゾン処理槽12内の低温のオ
ゾン水中に浸漬させられている間に、ウエハWの温度が
低下してくると、ウエハWをオゾン処理槽12内のオゾ
ン水中から引き上げ、そのウエハWをウエハ搬送機構に
より再び加熱部76へ移動させて、加熱器78によって
ウエハWを加熱する。ウエハWが加熱されて再び高温に
なると、加熱されたウエハWをウエハ搬送機構により再
び基板処理部74へ移動させ、加熱されたウエハWを再
びオゾン処理槽12内の高溶存オゾン濃度のオゾン水中
に浸漬させて、3回目のウエハWの処理を行う。以上の
ようなウエハWの加熱とウエハWの処理とを、ウエハW
の表面から有機物が完全に除去されるまで繰り返す。When the temperature of the wafer W decreases while the wafer W is immersed in the low-temperature ozone water in the ozone processing tank 12, the wafer W is lifted from the ozone water in the ozone processing tank 12, The wafer W is moved again to the heating section 76 by the wafer transfer mechanism, and the wafer W is heated by the heater 78. When the wafer W is heated and becomes high temperature again, the heated wafer W is moved again to the substrate processing unit 74 by the wafer transfer mechanism, and the heated wafer W is again returned to the ozone water having a high dissolved ozone concentration in the ozone processing tank 12. And the third processing of the wafer W is performed. The heating of the wafer W and the processing of the wafer W as described above
Repeat until organics are completely removed from the surface of the.
【0046】オゾン水によるウエハWの処理が終わる
と、オゾン処理槽12内へのオゾン水の供給を停止させ
るとともに、オゾン処理槽12内へ純水を供給し、ウエ
ハWをオゾン処理槽12内の純水中に浸漬させてウエハ
Wを水洗する。水洗が終了すると、ウエハWは、オゾン
処理槽12内から引き上げられ、乾燥処理された後、装
置外へ搬出される。When the processing of the wafer W with the ozone water is completed, the supply of the ozone water into the ozone processing tank 12 is stopped, and pure water is supplied into the ozone processing tank 12 so that the wafer W is removed from the ozone processing tank 12. Is immersed in pure water to wash the wafer W with water. When the washing is completed, the wafer W is lifted out of the ozone treatment tank 12, dried, and carried out of the apparatus.
【0047】なお、上記した説明では、最初に、低温の
高溶存オゾン濃度のオゾン水でウエハWを一度処理し、
その後に、ウエハWを加熱部76へ移動させて、ウエハ
Wを加熱器78で加熱するようにしているが、最初に、
ウエハWを加熱部76で加熱し、その後に、ウエハWを
基板処理部74へ移動させて、低温の高溶存オゾン濃度
のオゾン水による1回目のウエハWの処理を行うように
してもよい。In the above description, first, the wafer W is first treated with ozone water having a low dissolved ozone concentration at a low temperature.
After that, the wafer W is moved to the heating unit 76, and the wafer W is heated by the heater 78.
The wafer W may be heated by the heating unit 76, and thereafter, the wafer W may be moved to the substrate processing unit 74 to perform the first processing of the wafer W with low-temperature ozone water having a high dissolved ozone concentration.
【0048】図3に示した基板処理装置において、基板
処理部74のオゾン処理槽12の直上位置に設けられる
加熱部を、図4に示すような構成とすることもできる。
図4に示した装置では、オゾン処理槽12の上方に加熱
流体の吹出しノズル82を複数個配設し、各吹出しノズ
ル82を、高温に加熱された温純水あるいは加熱蒸気や
高温に加熱された窒素ガス等の不活性ガスなどの加熱流
体の供給源に接続され開閉制御弁86が介挿された加熱
流体供給管84に接続して、加熱部80が構成されてい
る。In the substrate processing apparatus shown in FIG. 3, the heating section provided directly above the ozone processing tank 12 in the substrate processing section 74 may have a configuration as shown in FIG.
In the apparatus shown in FIG. 4, a plurality of heating fluid blowing nozzles 82 are disposed above the ozone treatment tank 12, and each of the blowing nozzles 82 is connected to hot pure water or heated steam or nitrogen heated to a high temperature. A heating unit 80 is configured by being connected to a heating fluid supply pipe 84 connected to a supply source of a heating fluid such as an inert gas such as a gas and having an opening / closing control valve 86 interposed therebetween.
【0049】また、図4に示した装置では、加熱部80
の吹出しノズル82および基板処理部74のオゾン処理
槽12が、カバー90を開閉させることによりウエハW
の搬入および搬出を行うことができるとともに密閉する
ことが可能である処理チャンバ88内に収容されてい
る。処理チャンバ88の内部には、図示していないが、
基板処理部74のオゾン処理槽12の内方位置と加熱部
80の吹出しノズル82の配設位置との相互間でウエハ
Wを搬送するウエハ搬送機構が配設されている。また、
処理チャンバ88の底部には、気液排出口92が形設さ
れており、気液排出口92に気液排出管94が連通して
接続されている。気液排出管94には、開閉制御弁98
が介挿された排液管96、および、開閉制御弁102が
介挿され真空ポンプ104に接続された排気管100が
それぞれ連通している。Further, in the apparatus shown in FIG.
When the cover 90 is opened and closed, the wafer W
Is housed in a processing chamber 88 which can carry in and carry out the wafer and can be sealed. Although not shown, inside the processing chamber 88,
A wafer transfer mechanism for transferring the wafer W between the inside of the ozone processing tank 12 of the substrate processing unit 74 and the position of the blowing nozzle 82 of the heating unit 80 is provided. Also,
A gas-liquid discharge port 92 is formed at the bottom of the processing chamber 88, and a gas-liquid discharge pipe 94 is connected to the gas-liquid discharge port 92 so as to communicate therewith. The gas-liquid discharge pipe 94 has an open / close control valve 98.
A drain pipe 96 having a through hole and an exhaust pipe 100 having an opening / closing control valve 102 and connected to a vacuum pump 104 communicate with each other.
【0050】図4に示した装置では、加熱部80の吹出
しノズル82から高温に加熱された温純水や加熱蒸気な
どがウエハWの表面に対し吹き付けられることにより、
ウエハWが加熱される。そして、吹出しノズル82から
吹き出されて処理チャンバ88の内底部に流下した温純
水は、排液管96を通って処理チャンバ88から排出さ
れる。また、蒸気は、処理チャンバ88内から排気管1
00を通って排気される。この図4に示した装置は、図
3に示した装置と加熱部の構成が相違しているだけで、
処理動作自体は同じである。In the apparatus shown in FIG. 4, hot pure water or heated steam heated to a high temperature is blown from the blowing nozzle 82 of the heating unit 80 to the surface of the wafer W,
The wafer W is heated. Then, the hot pure water blown out from the blowing nozzle 82 and flowing down to the inner bottom of the processing chamber 88 is discharged from the processing chamber 88 through the drain pipe 96. Further, the steam is discharged from the processing chamber 88 to the exhaust pipe 1.
Exhausted through 00. The device shown in FIG. 4 differs from the device shown in FIG. 3 only in the configuration of the heating unit.
The processing operation itself is the same.
【0051】次に、図5は、基板処理装置のさらに別の
構成例を示す概略図である。この図5において、図1な
いし図4および図6で使用した符号と同一符号を付した
各構成要素は、これまでに説明した装置の各構成要素と
それぞれ同一作用をなすものであり、その説明を省略す
る。FIG. 5 is a schematic view showing still another example of the configuration of the substrate processing apparatus. In FIG. 5, the components denoted by the same reference numerals as those used in FIGS. 1 to 4 and 6 have the same functions as the respective components of the device described so far. Is omitted.
【0052】図5に示した装置には、純水供給管36か
ら分岐した後に再び純水供給管36に合流して液体供給
管32に連通する純水加熱用バイパス管106が設けら
れており、このバイパス管106に開閉制御弁108お
よびヒーター110がそれぞれ介在して設けられてい
る。そして、純水供給管36に介挿された開閉制御弁3
8を閉じ、バイパス管106に介挿された開閉制御弁1
08を開くことにより、純水供給源から供給される純水
は、バイパス管106内に流入し、ヒーター110を通
過する間に高温に加熱され、その加熱された温純水がバ
イパス管106から液体供給管32を通してオゾン処理
槽12の液体供給口16へ供給され、オゾン処理槽12
の内部を温純水で満たすことができる。The apparatus shown in FIG. 5 is provided with a pure water heating bypass pipe 106 which branches off from the pure water supply pipe 36, joins the pure water supply pipe 36 again, and communicates with the liquid supply pipe 32. An opening / closing control valve 108 and a heater 110 are provided in the bypass pipe 106, respectively. The open / close control valve 3 inserted in the pure water supply pipe 36
8 is closed, and the on-off control valve 1 inserted in the bypass pipe 106 is closed.
08, the pure water supplied from the pure water supply source flows into the bypass pipe 106 and is heated to a high temperature while passing through the heater 110, and the heated hot pure water is supplied from the bypass pipe 106 The liquid is supplied to the liquid supply port 16 of the ozone treatment tank 12 through a pipe 32,
Can be filled with warm pure water.
【0053】また、オゾン処理槽12の上部に、液体を
オゾン処理槽12の内部に向かって吹き出す吹出しノズ
ル112が複数個配設されている。各吹出しノズル11
2には、上部液体供給管114が連通して接続されてお
り、その上部液体供給管114に、高温に加熱された温
純水の供給源に接続され開閉制御弁118が介挿された
温純水供給管116、および、低温で高溶存オゾン濃度
のオゾン水を調製して供給するオゾン水供給源に接続さ
れ開閉制御弁122が介挿されたオゾン水供給管120
がそれぞれ接続されている。Further, a plurality of blowing nozzles 112 for blowing the liquid toward the inside of the ozone treatment tank 12 are provided above the ozone treatment tank 12. Each blowing nozzle 11
2 is connected to an upper liquid supply pipe 114 in communication therewith. The upper liquid supply pipe 114 is connected to a supply source of hot pure water heated to a high temperature, and is provided with an open / close control valve 118 interposed therebetween. 116, and an ozone water supply pipe 120 connected to an ozone water supply source for preparing and supplying ozone water having a high dissolved ozone concentration at a low temperature and having an opening / closing control valve 122 interposed therebetween.
Are connected respectively.
【0054】図5に示した構成の基板処理装置を使用
し、ウエハWの表面に付着した有機物を分解除去する処
理動作の1例を説明する。An example of a processing operation for decomposing and removing organic substances attached to the surface of the wafer W using the substrate processing apparatus having the configuration shown in FIG. 5 will be described.
【0055】オゾン処理槽12内にウエハWが収容され
た状態において、まず、温純水供給管116に介挿され
た開閉制御弁118を開いて、温純水供給管116から
上部液体供給管114を通して吹出しノズル112へ高
温に加熱された温純水を供給する。そして、吹出しノズ
ル112からオゾン処理槽12内のウエハWに向けて温
純水を吹き付け、さらにオゾン処理槽12内に温純水を
溜めて(この時、排液管28に介挿された排液バルブ3
0は閉じられている)、その温純水中にウエハWを浸漬
させることにより、ウエハWを加熱する。なお、この
際、排液バルブ30を開いたままの状態で、吹出しノズ
ル112からオゾン処理槽12内のウエハWに向けて温
純水を吹き付けて、ウエハWを加熱するようにしてもよ
い。In a state where the wafer W is stored in the ozone treatment tank 12, first, the opening / closing control valve 118 inserted in the hot pure water supply pipe 116 is opened, and the blowing nozzle is passed from the hot pure water supply pipe 116 through the upper liquid supply pipe 114. The hot pure water heated to a high temperature is supplied to 112. Then, hot pure water is blown from the blowing nozzle 112 toward the wafer W in the ozone processing tank 12, and the hot pure water is further stored in the ozone processing tank 12 (at this time, the drain valve 3 inserted into the drain pipe 28).
0 is closed), and the wafer W is heated by immersing the wafer W in the hot pure water. At this time, the wafer W may be heated by blowing hot pure water from the blowing nozzle 112 toward the wafer W in the ozone treatment tank 12 with the drain valve 30 kept open.
【0056】ウエハWが温純水によって加熱されると、
温純水供給管116に介挿された開閉制御弁118を閉
じて温純水の供給を停止させ、排液バルブ30を開いて
オゾン処理槽12内の温純水を急速排水する。オゾン処
理槽12内から温純水が排出されると、排液バルブ30
を閉じ、オゾン水供給管42に介挿された開閉制御弁4
4を開いて、オゾン水供給管42から液体供給管32を
通してオゾン処理槽12の液体供給口16へ低温で高溶
存オゾン濃度のオゾン水を供給し、オゾン処理槽12内
へオゾン水を流入させてその内部にオゾン水を満たし、
オゾン処理槽12の上部の溢流部18からオゾン水が溢
れ出て溢流受け部20内へ流入する状態にする。これに
より、ウエハWはオゾン水中に浸漬させられて、1回目
のウエハWの処理が行われる。このとき、ウエハWの表
面では、高い温度条件の下で高溶存濃度のオゾンと有機
物とが反応することになり、オゾン水によるウエハWの
処理が速やかに進行することになる。When the wafer W is heated by the hot pure water,
The open / close control valve 118 inserted into the hot pure water supply pipe 116 is closed to stop the supply of the hot pure water, and the drain valve 30 is opened to quickly drain the hot pure water in the ozone treatment tank 12. When the hot pure water is discharged from the ozone treatment tank 12, the drain valve 30
Is closed, and the open / close control valve 4 inserted in the ozone water supply pipe 42 is closed.
4, the ozone water having a low dissolved ozone concentration is supplied from the ozone water supply pipe 42 to the liquid supply port 16 of the ozone treatment tank 12 through the liquid supply pipe 32, and the ozone water flows into the ozone treatment tank 12. And fill it with ozone water,
The ozone water overflows from the overflow portion 18 at the top of the ozone treatment tank 12 and flows into the overflow receiving portion 20. Thus, the wafer W is immersed in the ozone water, and the first processing of the wafer W is performed. At this time, on the surface of the wafer W, a high dissolved concentration of ozone reacts with an organic substance under a high temperature condition, and the processing of the wafer W with ozone water proceeds promptly.
【0057】ウエハWがオゾン処理槽12内の低温のオ
ゾン水中に浸漬させられている間に、ウエハWの温度が
低下してくると、オゾン水供給管42に介挿された開閉
制御弁44を閉じてオゾン処理槽12内へのオゾン水の
供給を停止させ、排液管28に介挿された排液バルブ3
0を開いて、オゾン処理槽12内のオゾン水を急速排水
する。オゾン処理槽12内からオゾン水が排出される
と、排液バルブ30を閉じる。そして、ウエハWの上・
下での反応速度差を改善するために、次は、純水供給管
36に介挿された開閉制御弁38を閉じた状態で、バイ
パス管106に介挿された開閉制御弁108を開くこと
により、加熱された温純水をバイパス管106から液体
供給管32を通してオゾン処理槽12の液体供給口16
へ供給し、オゾン処理槽12の内部を温純水で満たす。
そして、オゾン処理槽12内の温純水中にウエハWが浸
漬させられることにより、ウエハWが加熱される。When the temperature of the wafer W decreases while the wafer W is immersed in the low-temperature ozone water in the ozone processing tank 12, the opening / closing control valve 44 inserted in the ozone water supply pipe 42. Is closed to stop the supply of the ozone water into the ozone treatment tank 12, and the drain valve 3 inserted into the drain pipe 28 is closed.
0 is opened, and the ozone water in the ozone treatment tank 12 is rapidly drained. When the ozone water is discharged from the ozone treatment tank 12, the drain valve 30 is closed. Then, on the wafer W
Next, in order to improve the reaction rate difference below, it is necessary to open the on-off control valve 108 inserted in the bypass pipe 106 while closing the on-off control valve 38 inserted in the pure water supply pipe 36. As a result, heated pure water is supplied from the bypass pipe 106 to the liquid supply port 16 of the ozone treatment tank 12 through the liquid supply pipe 32.
And the inside of the ozone treatment tank 12 is filled with warm pure water.
Then, the wafer W is heated by being immersed in the hot pure water in the ozone treatment tank 12.
【0058】ウエハWが温純水によって加熱されると、
純水加熱用バイパス管106に介挿された開閉制御弁1
08を閉じてオゾン処理槽12内への温純水の供給を停
止させ、排液バルブ30を開いてオゾン処理槽12内の
温純水を急速排水する。オゾン処理槽12内から温純水
が排出されると、排液バルブ30を閉じ、オゾン水供給
管120に介挿された開閉制御弁122を開いて、低温
で高溶存オゾン濃度のオゾン水を、オゾン水供給管12
0から上部液体供給管114を通して吹出しノズル11
2へ供給する。そして、吹出しノズル112からオゾン
処理槽12内のウエハWに向けてオゾン水を吹き付け、
オゾン処理槽12内にオゾン水を溜める。そして、オゾ
ン処理槽12内のオゾン水中にウエハWを浸漬させるこ
とにより、2回目のウエハWの処理を行う。When the wafer W is heated by hot pure water,
Open / close control valve 1 inserted into pure water heating bypass pipe 106
08 is closed, the supply of hot pure water into the ozone treatment tank 12 is stopped, and the drain valve 30 is opened to quickly drain the hot pure water from the ozone treatment tank 12. When the hot pure water is discharged from the ozone treatment tank 12, the drain valve 30 is closed, and the open / close control valve 122 inserted in the ozone water supply pipe 120 is opened to remove the ozone water having a high dissolved ozone concentration at a low temperature. Water supply pipe 12
0 to the blowing nozzle 11 through the upper liquid supply pipe 114
Supply to 2. Then, ozone water is blown from the blowing nozzle 112 toward the wafer W in the ozone processing tank 12,
Ozone water is stored in the ozone treatment tank 12. Then, the wafer W is processed for the second time by immersing the wafer W in ozone water in the ozone processing tank 12.
【0059】2回目のウエハWの処理が終わると、オゾ
ン水供給管120に介挿された開閉制御弁122を閉じ
て吹出しノズル112へのオゾン水の供給を停止させ、
排液管28に介挿された排液バルブ30を開いて、オゾ
ン処理槽12内のオゾン水を急速排水する。オゾン処理
槽12内からオゾン水が排出されると、排液バルブ30
を閉じる。When the second processing of the wafer W is completed, the opening / closing control valve 122 inserted in the ozone water supply pipe 120 is closed to stop the supply of the ozone water to the blowing nozzle 112.
The drainage valve 30 inserted in the drainage pipe 28 is opened to quickly drain the ozone water in the ozone treatment tank 12. When ozone water is discharged from the ozone treatment tank 12, the drain valve 30
Close.
【0060】以後、必要により、上記した各動作を繰り
返して、ウエハWの表面から有機物が完全に除去する。
オゾン水によるウエハWの処理が終わると、オゾン処理
槽12内へ純水を供給してウエハWを水洗し、水洗が終
了すると、ウエハWは、オゾン処理槽12内から引き上
げられ、乾燥処理された後、装置外へ搬出される。Thereafter, if necessary, the above-mentioned operations are repeated to completely remove organic substances from the surface of the wafer W.
When the processing of the wafer W with the ozone water is completed, pure water is supplied into the ozone processing tank 12 to wash the wafer W, and when the washing is completed, the wafer W is pulled up from the ozone processing tank 12 and dried. After that, it is carried out of the device.
【0061】図5に示した装置を使用して、上記したよ
うにオゾン処理槽12の上部および下部からそれぞれ温
純水およびオゾン水を交互に供給することにより、ウエ
ハWの上下での反応速度差を改善することができる。ま
た、その処理の際には、ウエハWの揺動動作を付加する
ことが好ましい。By using the apparatus shown in FIG. 5 to supply hot pure water and ozone water alternately from the upper and lower parts of the ozone treatment tank 12 as described above, the reaction rate difference between the upper and lower parts of the wafer W can be reduced. Can be improved. In addition, it is preferable to add a swing operation of the wafer W during the processing.
【0062】[0062]
【発明の効果】請求項1に係る発明の基板処理方法によ
ると、オゾン水による基板の処理時間を短くして、スル
ープットを向上させることができる。According to the substrate processing method of the present invention, the processing time of the substrate with ozone water can be shortened and the throughput can be improved.
【0063】請求項2ないし請求項5に係る各発明の基
板処理装置を使用すると、請求項1に係る発明の方法を
好適に実施することができ、オゾン水による基板の処理
時間を短くして、スループットを向上させることができ
る。By using the substrate processing apparatus of each of the inventions according to claims 2 to 5, the method of the invention according to claim 1 can be suitably performed, and the processing time of the substrate with ozone water can be shortened. Thus, the throughput can be improved.
【図1】この発明に係る基板処理方法を実施するために
使用される基板処理装置の構成の1例を示す概略図であ
る。FIG. 1 is a schematic view showing an example of a configuration of a substrate processing apparatus used to carry out a substrate processing method according to the present invention.
【図2】この発明に係る基板処理方法を実施するために
使用される基板処理装置の別の構成例を示す概略図であ
る。FIG. 2 is a schematic view showing another example of the configuration of the substrate processing apparatus used to carry out the substrate processing method according to the present invention.
【図3】この発明に係る基板処理方法を実施するために
使用される基板処理装置のさらに別の構成例を示す概略
図である。FIG. 3 is a schematic diagram showing still another configuration example of the substrate processing apparatus used to carry out the substrate processing method according to the present invention.
【図4】この発明に係る基板処理方法を実施するために
使用される基板処理装置のさらに別の構成例を示す概略
図である。FIG. 4 is a schematic diagram showing still another configuration example of the substrate processing apparatus used for performing the substrate processing method according to the present invention.
【図5】この発明に係る基板処理方法を実施するために
使用される基板処理装置のさらに別の構成例を示す概略
図である。FIG. 5 is a schematic view showing still another configuration example of the substrate processing apparatus used to carry out the substrate processing method according to the present invention.
【図6】オゾン水を用いる従来の基板処理装置の構成の
1例を示す概略図である。FIG. 6 is a schematic view showing an example of a configuration of a conventional substrate processing apparatus using ozone water.
10、10a、10b、74 基板処理部 12 オゾン処理槽 14 ウエハホルダ 16 液体供給口 18、52 溢流部 20 溢流液受け部 22 溢流液排出管 24 ドレイン排出管 26 排液口 28、96 排液管 30 排液バルブ 32 液体供給管 34、38、44、68、72、86、98、102、
108、118、122 開閉制御弁 36 純水供給管 40 流量調整弁 42、120 オゾン水供給管 46、46a、46b 基板加熱部 48 温純水槽 50 温純水給排口 54 溢流水受け部 56 温純水循環用配管 58 ポンプ 60、110 ヒーター 62 フィルタ 64 分岐管 66 純水供給管 70 ドレイン排出管 76、80 加熱部 78 加熱器 82、112 吹出しノズル 84 加熱流体供給管 88 処理チャンバ 90 カバー 92 気液排出口 94 気液排出管 100 排気管 104 真空ポンプ 106 純水加熱用バイパス管 114 上部液体供給管 116 温純水供給管 W ウエハ10, 10a, 10b, 74 Substrate processing section 12 Ozone treatment tank 14 Wafer holder 16 Liquid supply port 18, 52 Overflow section 20 Overflow liquid receiving section 22 Overflow liquid discharge pipe 24 Drain discharge pipe 26 Drain ports 28, 96 Drain Liquid pipe 30 drain valve 32 liquid supply pipe 34, 38, 44, 68, 72, 86, 98, 102,
108, 118, 122 Open / close control valve 36 Pure water supply pipe 40 Flow rate regulating valve 42, 120 Ozone water supply pipe 46, 46a, 46b Substrate heating section 48 Hot pure water tank 50 Hot pure water supply / discharge port 54 Overflow water receiving section 56 For hot pure water circulation Pipe 58 Pump 60, 110 Heater 62 Filter 64 Branch pipe 66 Pure water supply pipe 70 Drain discharge pipe 76, 80 Heating unit 78 Heater 82, 112 Blow-out nozzle 84 Heating fluid supply pipe 88 Processing chamber 90 Cover 92 Gas-liquid discharge port 94 Gas-liquid discharge pipe 100 Exhaust pipe 104 Vacuum pump 106 Bypass pipe for heating pure water 114 Upper liquid supply pipe 116 Hot pure water supply pipe W Wafer
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) G02F 1/1333 500 G02F 1/1333 500 H01L 21/027 H01L 21/30 572B 21/306 21/306 A (72)発明者 金本 和己 京都市上京区堀川通寺之内上る4丁目天神 北町1番地の1 大日本スクリーン製造株 式会社内 Fターム(参考) 2H088 FA21 FA24 FA30 HA01 2H090 JC06 JC08 JC19 5F043 AA37 BB25 CC16 DD07 DD30 5F046 MA02 MA03 MA10 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) G02F 1/1333 500 G02F 1/1333 500 H01L 21/027 H01L 21/30 572B 21/306 21/306 A ( 72) Inventor Kazumi Kanemoto 4-chome Tenjin Kitamachi 1-chome, Horikawa-dori-Terauchi, Kamigyo-ku, Kyoto F-term (reference) 2H088 FA21 FA24 FA30 HA01 2H090 JC06 JC08 JC19 5F043 AA37 BB25 CC16 DD07 DD30 5F046 MA02 MA03 MA10
Claims (5)
漬させて処理する基板処理方法において、 基板を加熱する基板加熱工程と、 加熱された基板をオゾン水中に浸漬させて処理する基板
処理工程と、を含むことを特徴とする基板処理方法。1. A substrate processing method in which a substrate is immersed in ozone water in which ozone is dissolved for processing, wherein a substrate heating step of heating the substrate, and a substrate processing step of immersing the heated substrate in ozone water for processing. And a substrate processing method.
オゾン水中に基板が浸漬させられて処理されるオゾン処
理槽と、 このオゾン処理槽内へオゾン水を供給するオゾン水供給
手段と、を備えた基板処理装置において、 高温に加熱された液体を収容しその液体中に基板が浸漬
させられて加熱される加熱処理槽と、 この加熱処理槽と前記オゾン処理槽との相互間で基板を
搬送する基板搬送手段と、をさらに備えたことを特徴と
する基板処理装置。2. An ozone treatment tank for containing ozone water in which ozone is dissolved and treating the substrate by immersing the substrate in the ozone water, and an ozone water supply means for supplying the ozone water into the ozone treatment tank. In a substrate processing apparatus provided with: a heat treatment tank that contains a liquid heated to a high temperature and is heated by being immersed in the liquid, and the substrate is interposed between the heat treatment tank and the ozone treatment tank. A substrate processing apparatus, further comprising: a substrate transport unit configured to transport the substrate.
オゾン水中に基板が浸漬させられて処理されるオゾン処
理槽と、 このオゾン処理槽内へオゾン水を供給するオゾン水供給
手段と、を備えた基板処理装置において、 前記オゾン処理槽を複数設けるとともに、高温に加熱さ
れた液体を収容しその液体中に基板が浸漬させられて加
熱される加熱処理槽を備え、 1つのオゾン処理槽から前記加熱処理槽へ、その加熱処
理槽から次のオゾン処理槽へと順次基板を搬送する基板
搬送手段をさらに備えたことを特徴とする基板処理装
置。3. An ozone treatment tank for containing ozone water in which ozone is dissolved and treating the substrate by immersing the substrate in the ozone water, and an ozone water supply means for supplying the ozone water into the ozone treatment tank. In the substrate processing apparatus provided, a plurality of the ozone treatment tanks are provided, and a heat treatment tank that accommodates a liquid heated to a high temperature, is immersed in the liquid, and heated by heating the substrate, is provided. A substrate processing apparatus, further comprising a substrate transfer means for sequentially transferring a substrate to the heat treatment tank from the heat treatment tank to the next ozone treatment tank.
オゾン水中に基板が浸漬させられて処理される処理槽
と、 この処理槽内へオゾン水を供給するオゾン水供給手段
と、を備えた基板処理装置において、 前記オゾン処理槽の外側に配設されて基板を加熱する加
熱手段と、 この加熱手段の配設位置と前記処理槽との相互間で基板
を搬送する基板搬送手段と、をさらに備えたことを特徴
とする基板処理装置。4. A processing tank for storing ozone water in which ozone is dissolved and for processing a substrate by immersing the substrate in the ozone water, and an ozone water supply means for supplying ozone water into the processing tank. In the substrate processing apparatus, a heating unit disposed outside the ozone processing tank to heat the substrate, and a substrate transfer unit configured to transfer the substrate between the position where the heating unit is disposed and the processing tank, A substrate processing apparatus further provided.
オゾン水中に基板が浸漬させられて処理される処理槽
と、 この処理槽内へオゾン水を供給する第1オゾン水供給手
段と、 前記処理槽内から液体を排出する排液手段と、を備えた
基板処理装置において、 前記処理槽内へ高温に加熱された液体を供給する第1液
体供給手段と、 前記処理槽内に収容された基板の表面に対し処理槽の上
部から高温に加熱された液体を供給する第2液体供給手
段と、 前記処理槽内に収容された基板の表面に対し処理槽の上
部からオゾンが溶解したオゾン水を供給する第2オゾン
水供給手段と、をさらに備えたことを特徴とする基板処
理装置。5. A processing tank for storing ozone water in which ozone is dissolved, wherein the substrate is immersed in the ozone water for processing, a first ozone water supply means for supplying ozone water into the processing tank, A substrate processing apparatus comprising: a liquid discharging unit configured to discharge a liquid from a processing tank; a first liquid supply unit configured to supply a liquid heated to a high temperature into the processing tank; Second liquid supply means for supplying a liquid heated to a high temperature from the upper part of the processing tank to the surface of the substrate; ozone water in which ozone is dissolved from the upper part of the processing tank to the surface of the substrate housed in the processing tank And a second ozone water supply means for supplying the water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000296342A JP4236073B2 (en) | 2000-09-28 | 2000-09-28 | Substrate processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000296342A JP4236073B2 (en) | 2000-09-28 | 2000-09-28 | Substrate processing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002110605A true JP2002110605A (en) | 2002-04-12 |
| JP4236073B2 JP4236073B2 (en) | 2009-03-11 |
Family
ID=18778634
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000296342A Expired - Fee Related JP4236073B2 (en) | 2000-09-28 | 2000-09-28 | Substrate processing equipment |
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| Country | Link |
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| JP (1) | JP4236073B2 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007128958A (en) * | 2005-11-01 | 2007-05-24 | Toshiba Corp | Substrate cleaning apparatus and substrate cleaning method |
| WO2008059799A1 (en) * | 2006-11-15 | 2008-05-22 | Tokyo Electron Limited | Processing system, processing method and recording medium |
| JP2011001569A (en) * | 2009-06-16 | 2011-01-06 | Toyota Motor Corp | Ozone water treatment apparatus and ozone water treatment method |
| JP2011075449A (en) * | 2009-09-30 | 2011-04-14 | Kurabo Ind Ltd | Hydroxyl radical-containing water supply system |
| US8298346B2 (en) | 2008-05-15 | 2012-10-30 | Renesas Electronics Corporation | Substrate processing method and substrate processing apparatus |
| JP2014130153A (en) * | 2014-02-14 | 2014-07-10 | Kurabo Ind Ltd | Hydroxyl radical-containing water supply apparatus |
| JP2017011005A (en) * | 2015-06-18 | 2017-01-12 | 信越半導体株式会社 | Cleaning method of silicon wafer |
-
2000
- 2000-09-28 JP JP2000296342A patent/JP4236073B2/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007128958A (en) * | 2005-11-01 | 2007-05-24 | Toshiba Corp | Substrate cleaning apparatus and substrate cleaning method |
| US8066020B2 (en) | 2005-11-01 | 2011-11-29 | Kabushiki Kaisha Toshiba | Substrate cleaning apparatus and substrate cleaning method |
| WO2008059799A1 (en) * | 2006-11-15 | 2008-05-22 | Tokyo Electron Limited | Processing system, processing method and recording medium |
| US8136538B2 (en) | 2006-11-15 | 2012-03-20 | Tokyo Electron Limited | Processing system, processing method, and storage medium |
| US8298346B2 (en) | 2008-05-15 | 2012-10-30 | Renesas Electronics Corporation | Substrate processing method and substrate processing apparatus |
| JP2011001569A (en) * | 2009-06-16 | 2011-01-06 | Toyota Motor Corp | Ozone water treatment apparatus and ozone water treatment method |
| JP2011075449A (en) * | 2009-09-30 | 2011-04-14 | Kurabo Ind Ltd | Hydroxyl radical-containing water supply system |
| JP2014130153A (en) * | 2014-02-14 | 2014-07-10 | Kurabo Ind Ltd | Hydroxyl radical-containing water supply apparatus |
| JP2017011005A (en) * | 2015-06-18 | 2017-01-12 | 信越半導体株式会社 | Cleaning method of silicon wafer |
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| Publication number | Publication date |
|---|---|
| JP4236073B2 (en) | 2009-03-11 |
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