JP2000290693A - Cleaning of electronic parts and members - Google Patents
Cleaning of electronic parts and membersInfo
- Publication number
- JP2000290693A JP2000290693A JP10353599A JP10353599A JP2000290693A JP 2000290693 A JP2000290693 A JP 2000290693A JP 10353599 A JP10353599 A JP 10353599A JP 10353599 A JP10353599 A JP 10353599A JP 2000290693 A JP2000290693 A JP 2000290693A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- ozone
- water
- hydrogen peroxide
- members
- 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
- 238000004140 cleaning Methods 0.000 title claims abstract description 110
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 64
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 40
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000007789 gas Substances 0.000 claims abstract description 30
- 239000011259 mixed solution Substances 0.000 claims abstract description 26
- 239000000243 solution Substances 0.000 claims abstract description 13
- 150000001450 anions Chemical class 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 claims description 46
- 229910021642 ultra pure water Inorganic materials 0.000 claims description 46
- 239000012498 ultrapure water Substances 0.000 claims description 46
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims description 34
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 22
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract description 23
- 229910052710 silicon Inorganic materials 0.000 abstract description 23
- 239000010703 silicon Substances 0.000 abstract description 23
- 239000000126 substance Substances 0.000 abstract description 12
- 239000000758 substrate Substances 0.000 abstract description 11
- 239000004065 semiconductor Substances 0.000 abstract description 5
- 239000011521 glass Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- 239000004973 liquid crystal related substance Substances 0.000 abstract description 2
- 238000005406 washing Methods 0.000 description 33
- 239000007788 liquid Substances 0.000 description 22
- 235000012431 wafers Nutrition 0.000 description 20
- 238000004519 manufacturing process Methods 0.000 description 17
- 229910052751 metal Inorganic materials 0.000 description 12
- 239000002184 metal Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 9
- 238000007872 degassing Methods 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- 239000010419 fine particle Substances 0.000 description 6
- 239000012528 membrane Substances 0.000 description 6
- -1 nitrate ions Chemical class 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052736 halogen Inorganic materials 0.000 description 2
- QOSATHPSBFQAML-UHFFFAOYSA-N hydrogen peroxide;hydrate Chemical compound O.OO QOSATHPSBFQAML-UHFFFAOYSA-N 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000011265 semifinished product Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000009281 ultraviolet germicidal irradiation Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
Landscapes
- Cleaning By Liquid Or Steam (AREA)
- Detergent Compositions (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、半導体基板、ガラ
ス基板、電子部品又はこれらの製造装置部品等のような
電子部品部材類の洗浄方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning electronic parts such as a semiconductor substrate, a glass substrate, an electronic part, or a part for manufacturing the same.
【0002】[0002]
【従来の技術】LSI等の電子部品部材類の製造工程等
においては、表面を極めて清浄にすることが求められる
ことがある。例えばLSIは、シリコンウエハ上に酸化
ケイ素の絶縁被膜を形成し、次いでこの被膜上に所定の
パターンにレジスト層を設け、レジスト層を設けていな
い部分の絶縁被膜をエッチング等によって除去して金属
シリコンを露出させ、この表面を洗浄した後、目的に応
じてp型あるいはn型の元素を導入し、アルミニウム等
の金属配線を埋め込む工程を繰り返して素子が製造され
るが、p型、n型の元素を導入する際や金属配線を埋め
込む際に、金属シリコン表面に微粒子等の異物や、金
属、有機物、自然酸化膜等が付着していると、金属シリ
コンと金属配線との接触不良や接触抵抗増大により、素
子の特性が不良となることがある。このためLSI製造
工程において、シリコンウエハ表面の洗浄工程は高性能
な素子を得る上で、非常に重要な工程であり、シリコン
ウエハ上の付着不純物は可能な限り取り除くことが必要
である。2. Description of the Related Art In the process of manufacturing electronic parts such as LSIs, it is sometimes required to make the surface extremely clean. For example, in LSI, a silicon oxide insulating film is formed on a silicon wafer, a resist layer is provided in a predetermined pattern on the silicon film, and the insulating film in a portion where the resist layer is not provided is removed by etching or the like to remove metal silicon. After the surface is cleaned and the surface is washed, a step of introducing a p-type or n-type element according to the purpose and embedding a metal wiring such as aluminum is repeated to manufacture an element. When introducing elements or embedding metal wiring, if foreign matter such as fine particles, metal, organic matter, natural oxide film, etc. adhere to the metal silicon surface, poor contact or contact resistance between the metal silicon and the metal wiring will occur. Due to the increase, the characteristics of the element may be poor. Therefore, in the LSI manufacturing process, the step of cleaning the surface of the silicon wafer is a very important step in obtaining a high-performance device, and it is necessary to remove impurities adhering to the silicon wafer as much as possible.
【0003】従来、シリコンウエハの洗浄は、硫酸・過
酸化水素水混合溶液、塩酸・過酸化水素水混合溶液、フ
ッ酸溶液等による洗浄と、超純水による洗浄とを組み合
わせて行い、シリコンウエハ表面の原子レベルでの平坦
性を損なうことなく、シリコンウエハ表面に付着してい
る有機物、微粒子、金属、自然酸化膜等を除去してい
る。このうち、硫酸・過酸化水素水混合溶液は、シリコ
ンウエハ表面に付着している有機物や金属不純物を除去
するためのものであり、塩酸・過酸化水素水混合溶液
は、シリコンウエハ表面の金属不純物を除去するもので
あり、フッ酸溶液は、シリコンウエハ表面の自然酸化膜
を除去するためのものである。Conventionally, silicon wafer cleaning is performed by combining cleaning with a mixed solution of sulfuric acid and hydrogen peroxide, a mixed solution of hydrochloric acid and hydrogen peroxide, a hydrofluoric acid solution, and cleaning with ultrapure water. Organic substances, fine particles, metals, natural oxide films and the like adhering to the silicon wafer surface are removed without deteriorating the surface flatness at the atomic level. Of these, the sulfuric acid / hydrogen peroxide mixed solution is for removing organic substances and metal impurities adhering to the surface of the silicon wafer, and the hydrochloric acid / hydrogen peroxide mixed solution is used for removing the metal impurities on the silicon wafer surface. The hydrofluoric acid solution is for removing a natural oxide film on the surface of the silicon wafer.
【0004】そして、この硫酸・過酸化水素水混合溶液
等の薬品による付着物除去工程後に実施されるすすぎ処
理は、ウエハ表面に残留する薬品のすすぎを行うもので
あって、当該すすぎ用の水には、通常超純水製造装置に
よって製造される超純水が使用される。また、硫酸・過
酸化水素水混合溶液による洗浄後に行われる超純水洗浄
工程では、硫酸イオンの粘性が高いためにシリコンウエ
ハ上から当該イオンの除去が容易ではなく、また、当該
イオンの残存に伴う後工程での金属及び微粒子による汚
染を受けやすくなるなどの点から、該すすぎ用の水は、
通常80℃以上に加温された温超純水が使用されてい
る。A rinsing process carried out after the step of removing deposits with a chemical such as a mixed solution of sulfuric acid and hydrogen peroxide is for rinsing chemicals remaining on the wafer surface. , Ultrapure water usually produced by an ultrapure water production apparatus is used. In addition, in the ultrapure water cleaning step performed after the cleaning with the sulfuric acid / hydrogen peroxide mixed solution, it is not easy to remove the ions from the silicon wafer due to the high viscosity of the sulfate ions. In terms of being susceptible to contamination by metal and fine particles in the accompanying post-process, the water for rinsing is
Normally, warm ultrapure water heated to 80 ° C. or higher is used.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、このよ
うな温超純水を使用することは熱エネルギーの負担を増
大する。例えば、洗浄機の前段に加温装置を設ける場
合、加温装置は加熱源や温度制御系などの付帯設備を備
えるためコスト高となる。また、設置スペースを予想外
に採るため、省スペース化が図れない。更に、加温装置
を設けることでより高度な安全管理基準が必要となる。
一方、超純水を加温せずに使用する場合、洗浄力が温超
純水と比べて低下するため大量の超純水が洗浄に必要と
なる。このため、超純水使用量増加によるコスト上昇に
つながるという問題がある。However, the use of such warm ultrapure water increases the burden of thermal energy. For example, when a heating device is provided in a stage preceding the washing machine, the cost of the heating device is increased because the heating device includes auxiliary equipment such as a heating source and a temperature control system. In addition, since the installation space is unexpectedly taken, space saving cannot be achieved. Further, by providing a heating device, a higher safety management standard is required.
On the other hand, when using ultrapure water without heating, a large amount of ultrapure water is required for cleaning because the cleaning power is lower than that of warm ultrapure water. For this reason, there is a problem that the cost increases due to an increase in the amount of ultrapure water used.
【0006】したがって、本発明の目的は、電子部品部
材類を、硫酸・過酸化水素水混合溶液等の薬品で洗浄す
る工程の後、残留する陰イオンをすすぐ(リンス)工程
において、洗浄に要する洗浄液の加温設備を設けること
なく、超純水の使用量を低減することができ、しかも低
温でも確実な洗浄を行うことができる電子部品部材類の
洗浄方法を提供することにある。Therefore, an object of the present invention is to clean the electronic component members in the step of rinsing (rinsing) the remaining anions after the step of cleaning the components with a chemical such as a mixed solution of sulfuric acid and hydrogen peroxide. It is an object of the present invention to provide a method for cleaning electronic parts and members that can reduce the amount of ultrapure water used without providing a cleaning liquid heating facility and that can perform reliable cleaning even at a low temperature.
【0007】[0007]
【課題を解決するための手段】かかる実情において、本
発明者は鋭意検討を行った結果、電子部品部材類を、硫
酸・過酸化水素水混合溶液、塩酸・過酸化水素水混合溶
液又はフッ酸溶液で洗浄する工程の後、残留する洗浄液
をすすぐ(リンス)工程において、従来使用されていた
超純水や温超純水に代えて、オゾン溶解水を使用すれ
ば、洗浄液の加温設備を特に設けることなく、純水の使
用量を低減することができ、しかも低温でも確実な洗浄
を行うことができることを見出し、本発明を完成するに
至った。Under such circumstances, the present inventors have conducted intensive studies and as a result, have found that electronic component members can be mixed with a sulfuric acid / hydrogen peroxide mixed solution, hydrochloric acid / hydrogen peroxide mixed solution or hydrofluoric acid. After the step of washing with the solution, in the rinsing step of the remaining washing liquid, if ozone-dissolved water is used instead of conventionally used ultrapure water or warm ultrapure water, a heating apparatus for the washing liquid is particularly provided. The present inventors have found that the amount of pure water used can be reduced, and that cleaning can be performed reliably even at a low temperature, and the present invention has been completed.
【0008】すなわち、本発明は、電子部品部材類の洗
浄面に残留する陰イオンをオゾン溶解水により洗浄する
ことを特徴とする電子部品部材類の洗浄方法を提供する
ものである。また、本発明は、電子部品部材類を、硫酸
・過酸化水素水混合溶液、塩酸・過酸化水素水混合溶液
又はフッ酸溶液で洗浄する工程の後に、該洗浄面をオゾ
ン溶解水により洗浄する工程を設けることを特徴とする
電子部品部材類の洗浄方法を提供するものである。[0008] That is, the present invention provides a method for cleaning electronic component members, characterized in that anions remaining on the cleaning surface of the electronic component members are cleaned with ozone-dissolved water. Further, according to the present invention, after the step of cleaning the electronic component members with a sulfuric acid / hydrogen peroxide solution, a hydrochloric acid / hydrogen peroxide solution or a hydrofluoric acid solution, the cleaning surface is cleaned with ozone-dissolved water. An object of the present invention is to provide a method for cleaning electronic component members, which comprises a step.
【0009】[0009]
【発明の実施の形態】本発明において、洗浄の対象とな
る電子部品部材類(「被洗浄物」ともいう)としては、
電子部品製造分野等において使用される種々の部品、材
料等が挙げられ、例えばシリコン基板、III −V族半導
体ウエハ等の半導体基板、液晶用ガラス基板等の基板材
料、メモリ素子、CPU、センサー素子等の電子部品等
の完成品やその半製品、石英反応管、洗浄槽、基板キャ
リヤ等の電子部品製造装置用部品等が例示される。DESCRIPTION OF THE PREFERRED EMBODIMENTS In the present invention, electronic parts and members to be cleaned (also referred to as "objects to be cleaned") include:
Examples of various components and materials used in the electronic component manufacturing field and the like include, for example, silicon substrates, semiconductor substrates such as III-V semiconductor wafers, substrate materials such as glass substrates for liquid crystals, memory devices, CPUs, and sensor devices. And finished products such as electronic parts and semi-finished products thereof, parts for electronic parts manufacturing equipment such as quartz reaction tubes, cleaning tanks, substrate carriers, and the like.
【0010】本発明は、電子部品部材類を、例えば硫酸
・過酸化水素水混合溶液、塩酸・過酸化水素水混合溶液
又はフッ酸溶液で洗浄した後、洗浄面に残留する陰イオ
ンをオゾン溶解水により洗浄するものである。洗浄面に
残留する陰イオンとしては、硫酸イオン、硝酸イオン、
塩素イオン及びフッ素イオン等のハロゲンイオンなどが
挙げられる。このような電子部品部材類を洗浄する洗浄
工程の一例を次に示す。 (1)硫酸・過酸化水素水洗浄工程;硫酸:過酸化水素
水=4:1(体積比)の混合溶液により、130℃で1
0分間洗浄する。 (2)オゾン溶解水洗浄工程;オゾン溶解水で5〜10
分間洗浄する。 (3)フッ酸洗浄工程;0.5%のフッ酸により1分間
洗浄する。 (4)オゾン溶解水洗浄工程;オゾン溶解水で5〜10
分間洗浄する。 (5)アンモニア・過酸化水素水洗浄工程;アンモニ
ア:過酸化水素水:超純水=0.05:1:5(体積
比)の混合溶液により、80℃で10分間洗浄する。 (6)超純水洗浄工程;超純水で10分間洗浄する。 (7)フッ酸洗浄工程;0.5%のフッ酸により1分間
洗浄する。 (8)オゾン溶解水洗浄工程;オゾン溶解水で5〜10
分間洗浄する。 (9)塩酸・過酸化水素水洗浄工程;塩酸:過酸化水素
水:超純水=1:1:6(体積比)の混合溶液により8
0℃で10分間洗浄する。 (10)オゾン溶解水洗浄工程;オゾン溶解水で5〜1
0分間洗浄する。 (11)フッ酸洗浄工程;0.5%のフッ酸により1分
間洗浄する。 (12)オゾン溶解水洗浄工程;オゾン溶解水で5〜1
0分間洗浄する。 (13)スピン乾燥又はIPA蒸気乾燥According to the present invention, after cleaning electronic component members with, for example, a mixed solution of sulfuric acid and hydrogen peroxide, a mixed solution of hydrochloric acid and hydrogen peroxide or a hydrofluoric acid solution, anions remaining on the cleaning surface are dissolved in ozone. It is to be washed with water. Anions remaining on the cleaning surface include sulfate ions, nitrate ions,
Halogen ions such as chlorine ions and fluorine ions are exemplified. An example of a cleaning process for cleaning such electronic component members will be described below. (1) Sulfuric acid / hydrogen peroxide solution washing step; a mixed solution of sulfuric acid: hydrogen peroxide solution = 4: 1 (volume ratio) at 130 ° C.
Wash for 0 minutes. (2) Ozone-dissolved water washing step;
Wash for minutes. (3) Hydrofluoric acid washing step: washing with 0.5% hydrofluoric acid for 1 minute. (4) Ozone-dissolved water washing step;
Wash for minutes. (5) Ammonia / hydrogen peroxide water washing step: Washing is performed at 80 ° C. for 10 minutes with a mixed solution of ammonia: hydrogen peroxide: ultra pure water = 0.05: 1: 5 (volume ratio). (6) Ultrapure water washing step: Washing with ultrapure water for 10 minutes. (7) Hydrofluoric acid washing step: washing with 0.5% hydrofluoric acid for 1 minute. (8) Ozone-dissolved water washing step;
Wash for minutes. (9) Hydrochloric acid / hydrogen peroxide water washing step;
Wash at 0 ° C. for 10 minutes. (10) Ozone-dissolved water washing step;
Wash for 0 minutes. (11) Hydrofluoric acid washing step: washing with 0.5% hydrofluoric acid for 1 minute. (12) Ozone-dissolved water washing step;
Wash for 0 minutes. (13) Spin drying or IPA vapor drying
【0011】前記工程において、電子部品部材類を、硫
酸・過酸化水素水混合溶液、塩酸・過酸化水素水混合溶
液又はフッ酸溶液で洗浄する工程は、(1)、(3)、
(7)、(9)及び(11)の工程である。前記工程に
おける洗浄方法としては、特に制限されず、例えば洗浄
液中に被洗浄物を浸漬して洗浄するバッチ洗浄法、洗浄
液を循環させながら被洗浄液と接触させて洗浄する循環
洗浄法、洗浄槽の底部側から洗浄液を供給し、洗浄槽の
上部からオーバーフローさせながら洗浄するフロー洗浄
法、被洗浄物に洗浄液をシャワー状に吹き掛けて洗浄す
る方法、高速回転させた被洗浄物に洗浄液を吹き掛けて
洗浄する方法等が挙げられる。In the above step, the step of cleaning the electronic component members with a mixed solution of sulfuric acid / hydrogen peroxide solution, a mixed solution of hydrochloric acid / hydrogen peroxide solution or a hydrofluoric acid solution includes the steps (1), (3),
These are the steps (7), (9) and (11). The cleaning method in the step is not particularly limited, for example, a batch cleaning method in which an object to be cleaned is immersed in a cleaning liquid for cleaning, a circulating cleaning method in which the cleaning liquid is contacted with the cleaning liquid while being circulated, and a cleaning tank. Flow cleaning method in which the cleaning liquid is supplied from the bottom side and the cleaning is performed while overflowing from the top of the cleaning tank, cleaning liquid is sprayed on the object to be cleaned in a shower shape, and the cleaning liquid is sprayed on the object rotated at high speed. Washing method.
【0012】前記硫酸・過酸化水素水混合溶液、塩酸・
過酸化水素水混合溶液又はフッ酸溶液により被洗浄物が
洗浄された後、該洗浄液が残存する洗浄面をオゾン溶解
水により洗浄する。該工程は、前記洗浄工程において
は、(2)、(4)、(8)、(10)及び(12)で
ある。この工程における洗浄方法を図1を参照して説明
する。図1は電子部品部材類をオゾン溶解水により洗浄
する方法を実施する洗浄装置の一例を示し、図中、1は
超純水製造装置、2はオゾンガス溶解槽、3は洗浄槽、
4はオゾン発生器を示す。この洗浄装置10には更に必
要に応じ、超純水製造装置1で製造された超純水中に溶
解しているガスを除去するための脱ガス装置5が設けら
れる。The sulfuric acid / hydrogen peroxide mixed solution, hydrochloric acid
After the object to be cleaned is cleaned with a mixed solution of hydrogen peroxide or a hydrofluoric acid, the cleaning surface where the cleaning liquid remains is cleaned with ozone-dissolved water. The steps are (2), (4), (8), (10) and (12) in the washing step. The cleaning method in this step will be described with reference to FIG. FIG. 1 shows an example of a cleaning apparatus for performing a method of cleaning electronic component members with ozone-dissolved water. In the figure, 1 is an ultrapure water production apparatus, 2 is an ozone gas dissolving tank, 3 is a cleaning tank,
Reference numeral 4 denotes an ozone generator. The cleaning device 10 is further provided with a degassing device 5 for removing gas dissolved in the ultrapure water produced by the ultrapure water production device 1 as necessary.
【0013】超純水製造装置1には、例えば、図では省
略する原水を凝集沈殿装置、砂濾過装置、活性炭濾過装
置で処理する前処理装置と、この前処理水を逆浸透膜装
置、2床3塔イオン交換装置、混床式イオン交換装置、
精密フィルターで処理して一次純水を得る一次純水製造
装置と、一次純水に紫外線照射、混床式ポリッシャー、
限外濾過膜処理を施して、一次純水中に残留する微粒
子、コロイド物質、有機物、金属イオン、陰イオン等を
除去する二次純水製造装置とを備えている。The ultrapure water production apparatus 1 includes, for example, a pretreatment apparatus for treating raw water, which is not shown in the figure, with a coagulation settling apparatus, a sand filtration apparatus, and an activated carbon filtration apparatus, and a reverse osmosis membrane apparatus, Bed 3 tower ion exchanger, mixed bed ion exchanger,
Primary pure water production equipment that obtains primary pure water by processing with a precision filter, UV irradiation on the primary pure water, mixed bed polisher,
The apparatus is provided with a secondary pure water production device that performs an ultrafiltration membrane treatment to remove fine particles, colloidal substances, organic substances, metal ions, anions and the like remaining in the primary pure water.
【0014】上記超純水製造装置1で製造される超純水
は、例えば次のような水質を有しているものが好まし
い。すなわち、電気抵抗率18.0M Ω・cm以上、全有
機炭素10μgC/L以下、粒径0.07μm 以上の微粒子
数10個/ml 以下、生菌数10個/L以下、シリカ1μgS
iO2/L 以下、ナトリウム0.01μgNa/L 以下、鉄0.
01μgFe/L 以下、銅0.01μgCu/L 以下、塩化物イ
オン0.01μgCl/L 以下、水素イオン濃度(pH)
7、過酸化水素濃度15μg/l 以下のものである。この
うち、過酸化水素濃度は、その値を15μg/l 以下とす
ることにより、超純水にオゾンを溶解させたオゾン水は
自己分解が抑制され、その寿命が著しく延びる点で好ま
しい。超純水中の過酸化水素濃度を15μg/l 以下とす
る方法としては、超純水が超純水製造過程において紫外
線照射処理を受けない方法、紫外線照射処理を受けて
も、その後吸着材により過酸化水素を吸着もしくは分解
処理する方法、パラジウム担持担体イオン交換樹脂ある
いは金属イオン型陽イオン交換樹脂により分解処理する
方法などが挙げられる。The ultrapure water produced by the ultrapure water production apparatus 1 preferably has, for example, the following water quality. That is, the electric resistivity is 18.0 MΩ · cm or more, the total organic carbon is 10 μgC / L or less, the number of fine particles having a particle size of 0.07 μm or more is 10 / ml or less, the number of viable bacteria is 10 / L or less, and the silica is 1 μgS
iO 2 / L or less, sodium 0.01 μg Na / L or less, iron 0.
01 μg Fe / L or less, copper 0.01 μg Cu / L or less, chloride ion 0.01 μg Cl / L or less, hydrogen ion concentration (pH)
7. It has a hydrogen peroxide concentration of 15 μg / l or less. Among them, the concentration of hydrogen peroxide is preferably set to 15 μg / l or less, because ozone water obtained by dissolving ozone in ultrapure water is suppressed from self-decomposition and its life is significantly extended. As a method for reducing the concentration of hydrogen peroxide in ultrapure water to 15 μg / l or less, a method in which ultrapure water is not subjected to ultraviolet irradiation in the process of producing ultrapure water, even if it is subjected to ultraviolet irradiation, A method of adsorbing or decomposing hydrogen peroxide, a method of decomposing with a palladium-supported carrier ion exchange resin or a metal ion type cation exchange resin, and the like can be given.
【0015】上記超純水製造装置1で製造された超純水
は、オゾンガス溶解槽2においてオゾンガスが溶解され
るが、その前に超純水中に溶解しているガスを脱ガス装
置5により除去しておくことが好ましい。脱ガス装置5
においては、特に超純水中に溶存している酸素ガス、窒
素ガス、炭酸ガスを除去することが好ましく、これらの
1種又は2種以上を組み合わせた溶存ガス濃度が10p
pm未満、好ましくは2ppm以下となるように脱ガス
しておくことが好ましい。なお、溶存ガス濃度が10p
pm以上となると洗浄時に気泡が発生して被洗浄物に気
泡が付着し、気泡が付着した部分の洗浄効果が低下する
傾向となる。脱ガス装置5において、超純水中の溶存ガ
スの脱ガスを行う方法としては、ガス透過膜を介して真
空脱ガスする方法が好ましい。The ultrapure water produced by the ultrapure water producing apparatus 1 is dissolved in the ozone gas dissolving tank 2 in the ozone gas dissolving tank 2. It is preferable to remove them. Degassing device 5
In particular, it is preferable to remove oxygen gas, nitrogen gas, and carbon dioxide gas dissolved in ultrapure water, and the dissolved gas concentration of one or a combination of two or more thereof is 10 p.
It is preferable to degas so as to be less than pm, preferably 2 ppm or less. The dissolved gas concentration is 10p
When the pressure is equal to or more than pm, air bubbles are generated at the time of cleaning, the air bubbles adhere to the object to be cleaned, and the cleaning effect on the portion where the air bubbles are adhered tends to decrease. In the degassing device 5, as a method for degassing the dissolved gas in the ultrapure water, a method of vacuum degassing via a gas permeable membrane is preferable.
【0016】脱ガス装置5で溶解している溶存ガスを脱
ガスした超純水は、オゾンガス溶解槽2においてオゾン
ガスが溶解される。オゾンガス溶解槽2で超純水にオゾ
ンガスが溶解して得られた洗浄液は、電子部品部材類の
表面に残留した、例えば硫酸・過酸化水素水混合溶液の
硫酸イオンの除去に好適な正の酸化還元電位を有する洗
浄液とすることができ、通常、溶存オゾン濃度が、25
℃、1気圧下で0.05〜20ppm 、特に3〜10ppm
となるようにオゾンガスを溶解させることが好ましい。
オゾン溶解濃度が20ppm を越えると、配管等の接液部
部材の劣化を引き起こすため適切ではない。The ozone gas is dissolved in the ozone gas dissolving tank 2 in the ultrapure water from which the dissolved gas dissolved in the degassing device 5 is degassed. The cleaning liquid obtained by dissolving ozone gas in ultrapure water in the ozone gas dissolving tank 2 is a positive oxidation suitable for removing sulfate ions, for example, of a mixed solution of sulfuric acid and hydrogen peroxide, remaining on the surface of electronic component members. A cleaning solution having a reduction potential can be used.
° C, 1-20 atm, 0.05-20ppm, especially 3-10ppm
Preferably, the ozone gas is dissolved so that
If the ozone dissolution concentration exceeds 20 ppm, it is not appropriate because it causes deterioration of liquid contact parts such as piping.
【0017】超純水にオゾンガスを溶解させる方法とし
ては、特に制限されず、超純水にガス透過膜を介してオ
ゾンガスを注入して溶解させる膜溶解方法、超純水中に
オゾンガスをバブリングして溶解させる方法、超純水中
にエジェクターを介してオゾンガスを溶解させる方法、
ガス溶解槽に超純水を供給するポンプの上流側にオゾン
ガスを供給し、ポンプ内の攪拌によって溶解させる方法
等が挙げられる。上記膜溶解に用いられるガス透過性膜
としては、オゾンの強い酸化力に耐え得る、フッ素樹脂
系の疎水性多孔質膜が好適であるが、これに限定される
ものではない。また、オゾン発生器としては、無声放電
及び電解法等によるオゾン発生器が挙げられる。The method for dissolving ozone gas in ultrapure water is not particularly limited. A film dissolving method in which ozone gas is injected into ultrapure water through a gas permeable membrane to dissolve the ozone gas, and ozone gas is bubbled into ultrapure water. Dissolving ozone gas in ultrapure water via an ejector,
A method of supplying ozone gas to the upstream side of a pump for supplying ultrapure water to the gas dissolving tank and dissolving the ozone gas by stirring in the pump may be used. As the gas permeable film used for the film dissolution, a fluororesin-based hydrophobic porous film that can withstand the strong oxidizing power of ozone is suitable, but is not limited to this. Examples of the ozone generator include an ozone generator using a silent discharge, an electrolytic method, or the like.
【0018】オゾンガス溶解槽2においてオゾンガスが
溶解されたオゾン溶解水は、洗浄槽3に送られる。洗浄
槽3において被洗浄物を前記オゾン溶解水によって洗浄
する方法としては、前記硫酸・過酸化水素水混合溶液等
の薬品洗浄の場合と同様の方法が挙げられ、例えばオゾ
ン溶解水中に被洗浄物を浸漬して洗浄するバッチ洗浄
法、オゾン溶解水を循環させながら被洗浄液と接触させ
て洗浄する循環洗浄法、洗浄槽の底部側からオゾン溶解
水を供給し、洗浄槽の上部からオーバーフローさせなが
ら洗浄するフロー洗浄法、被洗浄物にオゾン溶解水をシ
ャワー状に吹き掛けて洗浄する方法、高速回転させた被
洗浄物にオゾン溶解水を吹き掛けて洗浄する方法等が挙
げられる。The ozone-dissolved water in which the ozone gas is dissolved in the ozone gas dissolving tank 2 is sent to the cleaning tank 3. As a method of cleaning the object to be cleaned in the cleaning tank 3 with the ozone-dissolved water, the same method as in the case of the chemical cleaning of the sulfuric acid / hydrogen peroxide mixed solution or the like can be used. A washing method by immersing the ozone-dissolved water in the washing tank, a circulating washing method in which the ozone-dissolved water is circulated and brought into contact with the liquid to be washed, and the ozone-dissolved water is supplied from the bottom side of the washing tank and overflowed from the top of the washing tank. A flow cleaning method for washing, a method of spraying ozone-dissolved water on an object to be washed in a shower shape, and a method of spraying ozone-dissolved water on an object to be washed rotated at a high speed for washing are exemplified.
【0019】洗浄槽3にはヒーターを設け、必要に応じ
てオゾン溶解水の温度を調節するようにしてもよく、オ
ゾン溶解水を20〜80℃に温度調整して洗浄すること
がより優れた洗浄効果を得ることができる点で好まし
い。このように、被洗浄物をオゾン溶解水で洗浄する洗
浄時間は、特に制限されないが、例えば3〜20分間、
好ましくは5〜10分間である。A heater may be provided in the cleaning tank 3 to adjust the temperature of the ozone-dissolved water as required. It is more preferable to adjust the temperature of the ozone-dissolved water to 20 to 80 ° C. for cleaning. This is preferable in that a cleaning effect can be obtained. As described above, the cleaning time for cleaning the object to be cleaned with ozone-dissolved water is not particularly limited, but is, for example, 3 to 20 minutes.
Preferably, it is 5 to 10 minutes.
【0020】本発明においては、電子部品部材類を、例
えば硫酸・過酸化水素水混合溶液、塩酸・過酸化水素水
混合溶液又はフッ酸溶液等の薬品で洗浄した後、オゾン
溶解水によりすすぐ(リンス)ことにより、洗浄面に残
留する硫酸イオン、塩化物イオン及びフッ化物イオン等
のハロゲンイオン等の陰イオンをオゾン溶解水への拡散
とオゾン溶解水の酸化力により、例えば残留陰イオン濃
度1×1011atoms/cm 2 程度まで確実に除去できる。ま
た、洗浄液の加温設備を特に設けることがなく、且つ純
水の使用量を低減することができる。In the present invention, electronic parts and members are described as examples.
For example, sulfuric acid / hydrogen peroxide mixed solution, hydrochloric acid / hydrogen peroxide
After washing with a chemical such as a mixed solution or hydrofluoric acid solution, ozone
Rinse with dissolved water to leave on the cleaning surface
Sulfate ion, chloride ion and fluoride ion etc.
Of anions such as halogen ions from water into ozone-dissolved water
And the oxidizing power of ozone-dissolved water, for example,
Degree 1 × 1011atoms / cm TwoIt can be reliably removed to the extent. Ma
In addition, there is no special need
The amount of water used can be reduced.
【0021】[0021]
【実施例】次に、実施例を挙げて本発明を更に具体的に
説明する。 (洗浄装置)図2は、本発明の洗浄方法を実施する洗浄
装置の構成を示す概略フロー図である。図2中、図1と
同一構成要素については同一符号を付してその説明を省
略し、異なる点についてのみ説明する。すなわち、図2
において、符号12〜23はバッチ式シリコンウエハ用
洗浄装置を構成する各洗浄槽及びすすぎ槽を示し、これ
らの各槽のうち、12は硫酸・過酸化水素水混合洗浄液
を用いる洗浄槽、14、18及び22はフッ酸溶液を洗
浄液として用いる洗浄槽、20は塩酸・過酸化水素水混
合洗浄液を用いる洗浄槽、16はアンモニア・過酸化水
素水混合洗浄液を用いる洗浄槽であり、これらの各洗浄
槽のそれぞれの後段には、オゾン溶解水を用いるすすぎ
槽13、15、19、21、23及び超純水を用いるす
すぎ槽17がそれぞれ設けられている。そして、すすぎ
槽13、15、19、21、23にはオゾン溶解水製造
装置10aからのオゾン溶解水が配水され、すすぎ槽1
7には超純水を脱ガス装置5により脱ガスした水が配水
される。Next, the present invention will be described more specifically with reference to examples. (Cleaning Apparatus) FIG. 2 is a schematic flow chart showing the configuration of a cleaning apparatus for performing the cleaning method of the present invention. 2, the same components as those of FIG. 1 are denoted by the same reference numerals, and the description thereof will be omitted. Only different points will be described. That is, FIG.
, Reference numerals 12 to 23 denote respective cleaning tanks and rinsing tanks constituting the batch-type silicon wafer cleaning apparatus, and among these tanks, 12 is a cleaning tank using a sulfuric acid / hydrogen peroxide mixed cleaning liquid; Reference numerals 18 and 22 denote cleaning tanks using a hydrofluoric acid solution as a cleaning liquid, reference numeral 20 denotes a cleaning tank using a hydrochloric acid / hydrogen peroxide mixed cleaning liquid, and reference numeral 16 denotes a cleaning tank using an ammonia / hydrogen peroxide mixed cleaning liquid. At the subsequent stage of each of the tanks, a rinsing tank 13, 15, 19, 21, 23 using ozone-dissolved water and a rinsing tank 17 using ultrapure water are provided, respectively. The ozone-dissolved water from the ozone-dissolved water producing apparatus 10a is distributed to the rinsing tanks 13, 15, 19, 21, and 23, and the rinsing tanks 1
To 7 is supplied water degassed from ultrapure water by a degassing device 5.
【0022】シリコンウエハ11は以上のように配置さ
れた各槽12〜23を図中の矢印で示したように移送さ
れながら、順次に有機物除去、微粒子除去、付着金属除
去と、各洗浄工程後段でのフッ酸溶液による酸化膜除去
の洗浄処理が行われ、最終的にスピン乾燥器24に移送
されて乾燥が行われる。The silicon wafer 11 is sequentially transported through the tanks 12 to 23 arranged as described above as indicated by arrows in the figure, and sequentially removes organic substances, removes fine particles, removes adhered metals, and performs the subsequent steps of each cleaning step. The cleaning process for removing the oxide film using a hydrofluoric acid solution is performed, and finally, the wafer is transferred to the spin dryer 24 to be dried.
【0023】実施例1及び実施例2 (超純水)本実施例において、超純水は原水を凝集沈澱
処理装置、逆浸透膜処理装置、2床3塔式イオン交換処
理装置、混床式イオン交換処理装置、精密フィルタによ
る膜処理装置に通して一次純水を製造する一次純水製造
装置と、次いでこの一次純水を更に混床式ポリッシャ
ー、限外濾過装置に通して超純水を製造する2次純水製
造装置(いずれも図では省略)とを備える超純水製造装
置1から製造され、その水質は前記に示したとおりであ
った。Embodiments 1 and 2 (Ultra pure water) In this embodiment, ultra pure water is obtained by coagulating and separating raw water from a coagulated sedimentation treatment apparatus, a reverse osmosis membrane treatment apparatus, a two-bed three-column ion exchange treatment apparatus, and a mixed-bed type. An ion exchange treatment device, a primary pure water production device that produces primary pure water by passing through a membrane treatment device using a precision filter, and then the primary pure water is further passed through a mixed-bed polisher and an ultrafiltration device to remove ultrapure water. It was manufactured from the ultrapure water production apparatus 1 including the secondary pure water production apparatus to be produced (both are not shown in the drawings), and the water quality was as described above.
【0024】6インチの大きさのシリコンウエハ11を
130℃で10分間、洗浄槽12においてオーバーフロ
ー法により洗浄した。オーバーフロー洗浄は洗浄液をオ
ーバーフローさせることが可能な洗浄槽を用い、該槽内
でシリコンウエハを静止させて、洗浄液を線流速5m/
hでオーバーフローさせながら洗浄処理を行った。洗浄
槽12で使用する洗浄液には硫酸:過酸化水素水=4:
1(体積比)の混合溶液を使用した。次いで、洗浄され
たシリコンウエハ11をすすぎ槽13に移送し、常温又
は80℃の温度条件下ですすぎ処理した。すすぎ槽13
で使用したオゾン溶解水は電解法オゾン発生器を使用
し、前記超純水に膜溶解方法により、オゾンガス5ppm
を溶解させて製造した。すすぎ処理はオゾン溶解水を用
いて、前記同様のオーバーフロー法により行った。すな
わち、オーバーフローさせることが可能なすすぎ槽を用
い、該槽内でシリコンウエハを静止させて、オゾン溶解
水量を線流速5m/hで、5分間又は10分間オーバー
フローさせながらすすぎ処理を行った。そして、すすぎ
処理後、シリコンウエハの洗浄表面について、残留イオ
ン濃度を測定した。測定は熱水抽出イオンクロマトグラ
フィ法により行った。結果を表1に示す。A silicon wafer 11 having a size of 6 inches was washed by an overflow method in a washing tank 12 at 130 ° C. for 10 minutes. In the overflow cleaning, a cleaning tank capable of overflowing the cleaning liquid is used. The silicon wafer is stopped in the cleaning tank, and the cleaning liquid is supplied at a linear flow rate of 5 m /.
The washing process was performed while overflowing at h. The cleaning liquid used in the cleaning tank 12 includes sulfuric acid: hydrogen peroxide solution = 4:
A mixed solution of 1 (volume ratio) was used. Next, the washed silicon wafer 11 was transferred to a rinsing tank 13 and subjected to a rinsing process at room temperature or at a temperature of 80 ° C. Rinse tank 13
The ozone-dissolved water used in (5) was obtained by using an electrolytic ozone generator.
Was dissolved and produced. The rinsing treatment was performed by the same overflow method as described above using ozone-dissolved water. That is, a rinsing tank capable of overflowing was used, the silicon wafer was kept stationary in the tank, and the rinsing treatment was performed while the amount of the ozone dissolved water overflowed at a linear flow rate of 5 m / h for 5 minutes or 10 minutes. After the rinsing process, the residual ion concentration was measured on the cleaned surface of the silicon wafer. The measurement was performed by hot water extraction ion chromatography. Table 1 shows the results.
【0025】比較例1 オゾン溶解水の代わりに超純水を使用する以外は、実施
例1と同様の方法により行った。結果を表1に示す。Comparative Example 1 The same procedure as in Example 1 was carried out except that ultrapure water was used instead of the ozone-dissolved water. Table 1 shows the results.
【0026】[0026]
【表1】 [Table 1]
【0027】[0027]
【発明の効果】本発明によれば、電子部品部材類を、硫
酸・過酸化水素水混合溶液等の薬品で洗浄する工程の
後、残留する陰イオンを含む洗浄液を低温のオゾン溶解
水で充分に洗浄できる。このため、従来のように、洗浄
液の加温設備を設けることなく、電気使用量や付帯設備
コストを低減できる。また、洗浄効率が向上するためリ
ンス時間を短縮できると共に、純水の使用量を低減する
ことが可能である。また、洗浄工程の時間短縮により生
産性が向上する。According to the present invention, after the step of cleaning the electronic component members with a chemical such as a sulfuric acid / hydrogen peroxide mixed solution, the cleaning liquid containing the remaining anions is sufficiently washed with low-temperature ozone-dissolved water. Can be washed. For this reason, the amount of electricity used and the cost of auxiliary facilities can be reduced without providing a cleaning liquid heating facility as in the related art. Further, since the cleaning efficiency is improved, the rinsing time can be shortened, and the amount of pure water used can be reduced. Further, productivity is improved by shortening the time of the cleaning step.
【図1】本発明の電子部品部材類をオゾン溶解水により
洗浄する洗浄装置の構成を示す概略フロー図である。FIG. 1 is a schematic flow chart showing the configuration of a cleaning apparatus for cleaning electronic component members of the present invention with ozone-dissolved water.
【図2】本発明の洗浄方法を実施する洗浄装置の構成を
示す概略フロー図である。FIG. 2 is a schematic flow chart showing a configuration of a cleaning apparatus for performing the cleaning method of the present invention.
1 超純水製造装置 2 オゾンガス溶解槽 3 洗浄槽 4 オゾン発生器 5 脱ガス装置 10 電子部品部材類洗浄装置 11 シリコンウエハ 12〜23 洗浄槽又はすすぎ槽 24 スピン乾燥器 DESCRIPTION OF SYMBOLS 1 Ultrapure water production apparatus 2 Ozone gas dissolving tank 3 Cleaning tank 4 Ozone generator 5 Degassing apparatus 10 Electronic component member cleaning apparatus 11 Silicon wafer 12-23 Cleaning tank or rinsing tank 24 Spin dryer
Claims (4)
オンをオゾン溶解水により洗浄することを特徴とする電
子部品部材類の洗浄方法。1. A method for cleaning electronic component members, wherein anions remaining on the cleaning surface of the electronic component members are cleaned with ozone-dissolved water.
混合溶液、塩酸・過酸化水素水混合溶液又はフッ酸溶液
で洗浄する工程の後に、該洗浄面をオゾン溶解水により
洗浄する工程を設けることを特徴とする電子部品部材類
の洗浄方法。2. A process of cleaning electronic component members with a mixed solution of sulfuric acid and hydrogen peroxide, a mixed solution of hydrochloric acid and hydrogen peroxide or a hydrofluoric acid solution, and then cleaning the cleaning surface with ozone-dissolved water. And a method for cleaning electronic component members.
5μg/L 以下の水質を有する超純水にオゾンを溶解した
ものであることを特徴とする請求項1又は2記載の電子
部品部材類の洗浄方法。3. The ozone-dissolved water has a hydrogen peroxide concentration of 1
3. The method according to claim 1, wherein ozone is dissolved in ultrapure water having a water quality of 5 μg / L or less.
0.05〜20ppmであることを特徴とする請求項1〜
3のいずれか1項記載の電子部品部材類の洗浄方法。4. The ozone-dissolved water has a dissolved ozone gas concentration of 0.05 to 20 ppm.
4. The method for cleaning electronic component members according to claim 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10353599A JP2000290693A (en) | 1999-04-12 | 1999-04-12 | Cleaning of electronic parts and members |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10353599A JP2000290693A (en) | 1999-04-12 | 1999-04-12 | Cleaning of electronic parts and members |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000290693A true JP2000290693A (en) | 2000-10-17 |
Family
ID=14356565
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10353599A Pending JP2000290693A (en) | 1999-04-12 | 1999-04-12 | Cleaning of electronic parts and members |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000290693A (en) |
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|---|---|---|---|---|
| JP2002231677A (en) * | 2001-01-31 | 2002-08-16 | Kurita Water Ind Ltd | How to clean electronic materials |
| JP2007251127A (en) * | 2006-02-14 | 2007-09-27 | Elpida Memory Inc | Pure water supply system, cleaning system and method using pure water |
| JP2008053392A (en) * | 2006-08-24 | 2008-03-06 | Dainippon Printing Co Ltd | Cleaning the storage case |
| JP2010027853A (en) * | 2008-07-18 | 2010-02-04 | Sumitomo Electric Ind Ltd | Method for manufacturing group iii-v compound semiconductor substrate, method for manufacturing epitaxial wafer, group iii-v compound semiconductor substrate, and epitaxial wafer |
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1999
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002231677A (en) * | 2001-01-31 | 2002-08-16 | Kurita Water Ind Ltd | How to clean electronic materials |
| JP2007251127A (en) * | 2006-02-14 | 2007-09-27 | Elpida Memory Inc | Pure water supply system, cleaning system and method using pure water |
| JP2008053392A (en) * | 2006-08-24 | 2008-03-06 | Dainippon Printing Co Ltd | Cleaning the storage case |
| JP2010027853A (en) * | 2008-07-18 | 2010-02-04 | Sumitomo Electric Ind Ltd | Method for manufacturing group iii-v compound semiconductor substrate, method for manufacturing epitaxial wafer, group iii-v compound semiconductor substrate, and epitaxial wafer |
| WO2012048534A1 (en) * | 2010-10-15 | 2012-04-19 | 北京通美晶体技术有限公司 | Process for cleaning compound semiconductor wafer |
| US8691019B2 (en) | 2010-10-15 | 2014-04-08 | Beijing Tongmei Xtal Technology Co., Ltd. | Process for cleaning a compound semiconductor wafer |
| JP2015106647A (en) * | 2013-11-29 | 2015-06-08 | 株式会社Sumco | Method of manufacturing silicon wafer |
| WO2016203681A1 (en) * | 2015-06-18 | 2016-12-22 | 信越半導体株式会社 | Silicon wafer washing method |
| JP2017011005A (en) * | 2015-06-18 | 2017-01-12 | 信越半導体株式会社 | Cleaning method of silicon wafer |
| CN107639070A (en) * | 2017-08-24 | 2018-01-30 | 天津市环欧半导体材料技术有限公司 | A kind of Wafer Cleaning equipment and cleaning |
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| CN112652518B (en) * | 2019-10-11 | 2023-04-28 | 中芯国际集成电路制造(天津)有限公司 | Method for forming semiconductor device |
| CN115274409A (en) * | 2022-09-26 | 2022-11-01 | 广州粤芯半导体技术有限公司 | Method for cleaning semiconductor structure and method for manufacturing semiconductor structure |
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