JPH0651914B2 - Thin film etching equipment - Google Patents

Thin film etching equipment

Info

Publication number
JPH0651914B2
JPH0651914B2 JP17406889A JP17406889A JPH0651914B2 JP H0651914 B2 JPH0651914 B2 JP H0651914B2 JP 17406889 A JP17406889 A JP 17406889A JP 17406889 A JP17406889 A JP 17406889A JP H0651914 B2 JPH0651914 B2 JP H0651914B2
Authority
JP
Japan
Prior art keywords
concentration
nitric acid
phosphoric acid
thin film
etchant
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.)
Expired - Lifetime
Application number
JP17406889A
Other languages
Japanese (ja)
Other versions
JPH0339491A (en
Inventor
立身 小林
秀之 鈴木
博之 ▲吉▼川
久子 茂木
桂志 檀上
仁志 堀江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Canon Inc
Original Assignee
Canon Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Canon Inc filed Critical Canon Inc
Priority to JP17406889A priority Critical patent/JPH0651914B2/en
Publication of JPH0339491A publication Critical patent/JPH0339491A/en
Publication of JPH0651914B2 publication Critical patent/JPH0651914B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • ing And Chemical Polishing (AREA)
  • Weting (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は薄膜エッチング装置に関し、特にSiウエハ上、
ガラス基板上、セラミック基板上などに形成されるアル
ミニウム薄膜のエッチングにおいて、エッチャント中の
各成分濃度を最適に保持することのできる薄膜エッチン
グ装置に関するものである。
The present invention relates to a thin film etching apparatus, particularly on a Si wafer,
The present invention relates to a thin film etching apparatus capable of optimally maintaining the concentration of each component in an etchant when etching an aluminum thin film formed on a glass substrate, a ceramic substrate, or the like.

〔従来の技術〕[Conventional technology]

従来、硝酸、燐酸に水と添加剤を加えたエッチャントを
用いて、ガラス等からなる基板上に形成されたアルミニ
ウム薄膜をエッチングする際には、エッチャントは50℃
付近に加熱して使用される。そのために、加熱による水
の蒸発も関与して貯蔵されているエッチャントの組成が
変化する。従って、エッチャントの組成の変化は、必ず
しもアルミニウム薄膜のエッチングのために消費された
各成分の量、すなわち薄膜の加工量に比例しない。
Conventionally, when etching an aluminum thin film formed on a substrate made of glass or the like using an etchant containing nitric acid and phosphoric acid with water and an additive, the etchant is 50 ° C.
Used by heating in the vicinity. Therefore, the composition of the stored etchant changes due to the evaporation of water due to heating. Therefore, the change in the composition of the etchant is not necessarily proportional to the amount of each component consumed for etching the aluminum thin film, that is, the processing amount of the thin film.

そのために、被加工物(この場合、アルミニウム薄膜)
を一定量処理するごとに、新しい組成のエッチャントに
更新する方法では、この更新直前にしばしばアルミニウ
ム薄膜のエッチングの不良が発生する。エッチャントの
成分組成を確認しようとすれば、エッチング装置をオフ
ラインにして、しかも時間のかかる成分分析法に頼るほ
かはなく、インラインで直接に成分濃度を管理するには
適さなかった。
Therefore, the work piece (in this case, an aluminum thin film)
In the method of renewing the etchant with a new composition every time a certain amount of is treated, defective etching of the aluminum thin film often occurs immediately before the renewal. In order to confirm the composition of the etchant, the etching apparatus was set off-line, and it took a long time to analyze the composition, which was not suitable for in-line composition control.

一般には、アルミニウム薄膜の加工処理量を管理し、一
定の加工処理ごとにエッチャントを更新する方法が採用
され、この場合エッチャントは安全側に更新してゆく傾
向にあった。従って、エッチャントの使用量は理論値よ
りも多くなり、またエッチャントの交換のための工程数
が増すためコスト高となる。さらに、交換の際装置を停
止するため、歩留まりが悪く、しかも品質上好ましいも
のではなかった。
Generally, a method of managing the processing amount of the aluminum thin film and updating the etchant at every fixed processing is adopted. In this case, the etchant tends to be updated to the safe side. Therefore, the amount of the etchant used is larger than the theoretical value, and the number of steps for exchanging the etchant increases, resulting in high cost. Further, since the device is stopped at the time of replacement, the yield is poor and the quality is not favorable.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

そこで、本発明の目的は、上述した問題点を解消し、ア
ルミニウム薄膜のエッチャント成分である硝酸の濃度と
燐酸の濃度とをインラインで測定し、エッチャントを適
正な濃度に設定し、しかも工程数を削減することのでき
る薄膜エッチング装置を提供することにある。
Therefore, the object of the present invention is to eliminate the above-mentioned problems, measure the concentration of nitric acid and the concentration of phosphoric acid, which are the etchant components of the aluminum thin film, in-line, set the etchant to a proper concentration, and It is to provide a thin film etching apparatus capable of reducing the number.

〔課題を解決するための手段〕[Means for Solving the Problems]

このような目的を達成するために、本発明は、硝酸と燐
酸と水とを含むエッチャントを用いて被加工物の薄膜を
エッチングする薄膜エッチング装置において、エッチャ
ントの吸光度を測定する第1の測定手段と、エッチャン
トの比重を測定する第2の測定手段と、エッチング液貯
蔵槽に硝酸を供給する第1の供給手段と、エッチング液
貯蔵槽に燐酸を供給する第2の供給手段と、エッチング
液貯蔵槽に水を供給する第3の供給手段と、第1の測定
手段の出力結果に基づいてエッチャント中の硝酸の濃度
を算出し、算出された硝酸の濃度と第2の測定手段によ
って測定された比重とに基づいて燐酸の濃度を算出し、
算出された硝酸の濃度と燐酸の濃度とに基づいて、第1
の供給手段、第2の供給手段、および第3の供給手段を
制御する制御手段とを具えたことを特徴とする。
In order to achieve such an object, the present invention provides a first measuring means for measuring the absorbance of an etchant in a thin film etching apparatus for etching a thin film of a workpiece using an etchant containing nitric acid, phosphoric acid and water. A second measuring means for measuring the specific gravity of the etchant; a first supplying means for supplying nitric acid to the etching solution storage tank; a second supplying means for supplying phosphoric acid to the etching solution storage tank; and an etching solution storage The concentration of nitric acid in the etchant was calculated based on the output results of the third supply means for supplying water to the tank and the first measurement means, and the calculated concentration of nitric acid and the second measurement means were used for measurement. Calculate the concentration of phosphoric acid based on specific gravity,
Based on the calculated nitric acid concentration and phosphoric acid concentration, the first
And a control means for controlling the second supply means and the third supply means.

〔作用〕[Action]

本発明による硝酸の濃度と燐酸の濃度を測定する原理に
ついて述べる。硝酸は、第1図に示すように、燐酸や酢
酸が混在する溶液中においては、これらの成分の影響を
受けず、かつ200nm付近の波長における紫外線の吸光度
が著るしく大きいため、200nm付近の波長における紫外
線の吸光度を吸光光度計を用いて測定することによって
硝酸の濃度を算出する事ができる。硝酸の重量%を横軸
に取り、200nmの波長における紫外線の吸光度を縦軸に
取ると、第2図に示すように、硝酸の重量%が約5%まで
ほぼ直線が得られた。これを検量線とすれば、吸光度を
測定することにより硝酸の濃度を算出することができ
る。
The principle of measuring the concentration of nitric acid and the concentration of phosphoric acid according to the present invention will be described. As shown in FIG. 1, nitric acid is not affected by these components in a solution containing phosphoric acid and acetic acid, and the absorbance of ultraviolet rays at a wavelength of around 200 nm is extremely large. The nitric acid concentration can be calculated by measuring the absorbance of ultraviolet rays at a wavelength using an absorptiometer. When the weight% of nitric acid is plotted on the horizontal axis and the absorbance of ultraviolet rays at a wavelength of 200 nm is plotted on the vertical axis, a straight line was obtained up to a weight% of nitric acid of about 5%, as shown in FIG. By using this as a calibration curve, the concentration of nitric acid can be calculated by measuring the absorbance.

燐酸の重量%は、硝酸と燐酸が混在している場合には、
混合溶液の比重は、各濃度に応じて変化する。燐酸の重
量%を横軸に取り混合溶液の比重を縦軸に取ると、第3
図に示すようになる。硝酸の重量%が一定ならば、燐酸
の重量%と比重との関係は直線性が成立する。従って、
予め使用範囲の硝酸の重量%における燐酸の重量%と比
重との検量線を作成しておけば、混合溶液の比重を測定
することにより、燐酸の重量%を算出することができ
る。
The weight% of phosphoric acid is, when nitric acid and phosphoric acid are mixed,
The specific gravity of the mixed solution changes depending on each concentration. When the weight% of phosphoric acid is plotted on the horizontal axis and the specific gravity of the mixed solution is plotted on the vertical axis,
As shown in the figure. If the weight% of nitric acid is constant, the relationship between the weight% of phosphoric acid and the specific gravity is linear. Therefore,
If a calibration curve of the weight% of phosphoric acid and the specific gravity in the weight% of nitric acid in the usable range is prepared in advance, the weight% of phosphoric acid can be calculated by measuring the specific gravity of the mixed solution.

このようにして算出された硝酸および燐酸の濃度と、エ
ッチング方法に応じて予め設定された硝酸と燐酸の基準
濃度との差異を比較して、その差異量に応じて硝酸、燐
酸および水の供給量を制御するようにしたので、エッチ
ャントに含まれる各成分の濃度を一定の範囲内に保ちな
がら、アルミニウム薄膜の安定したエッチングが可能と
なる。
The difference between the concentrations of nitric acid and phosphoric acid calculated in this way and the reference concentrations of nitric acid and phosphoric acid preset according to the etching method are compared, and nitric acid, phosphoric acid and water are supplied according to the difference. Since the amount is controlled, it is possible to stably etch the aluminum thin film while keeping the concentration of each component contained in the etchant within a certain range.

〔実施例〕〔Example〕

以下、図面を参照して本発明の実施例を詳細に説明す
る。
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

第4図は本発明を適用した薄膜エッチング装置の実施例
を示す模式図である。
FIG. 4 is a schematic diagram showing an embodiment of a thin film etching apparatus to which the present invention is applied.

第5図は第4図に示した実施例の基本構成を示すブロッ
ク図である。
FIG. 5 is a block diagram showing the basic configuration of the embodiment shown in FIG.

まず、第4図および第5図に基づいて硝酸と燐酸の濃度
を算出するまでの装置の作動方法について説明する。装
置の全体の作動方法については後述する。
First, the operating method of the apparatus until the concentrations of nitric acid and phosphoric acid are calculated will be described based on FIGS. 4 and 5. The operation method of the entire device will be described later.

エッチング液貯蔵槽1に、硝酸、燐酸を主成分とし水を
添加したエッチング液2を入れて、ヒータ3により加温
し攪拌機4を用いて均一な濃度のエッチング液とする。
ポンプ10によりエッチング液1をエッチング槽11に送
り、エッチング液2をスプレ12により被処理アルミニウ
ム薄膜基板13へ吹き付けてエッチングを行ない、排液は
配管14を通ってエッチング液貯蔵槽1に戻る。
The etching liquid 2 containing water containing nitric acid and phosphoric acid as a main component is placed in the etching liquid storage tank 1, heated by a heater 3 and made into an etching liquid having a uniform concentration using a stirrer 4.
The pump 10 sends the etching solution 1 to the etching tank 11, the spray 12 sprays the etching solution 2 onto the aluminum thin film substrate 13 to be processed for etching, and the discharged liquid returns to the etching solution storage tank 1 through the pipe 14.

制御部17はROM17Bに格納された制御手順に従って以下の
動作を行なう。試料採取ポンプ5により採取されたエッ
チング液2は、フローセル7に送られる。重水素ランプ
とモノクロメータとの組み合わせなどによる紫外線光源
8より、波長200nm付近の紫外線をフローセル中のエッ
チング液に照射して、紫外線検知部9で透過光量を求め
る。この透過光量のデータは制御部17に送られる。一
方、ポンプ10により送られたエッチング液はエッチング
槽11に送られると同時に比重計セル16に送られる。エッ
チング液の流量は、バルブ15により自由に調整できる。
比重計セル16により得られたエッチング液の比重データ
は制御部17に送られる。
The control unit 17 performs the following operations according to the control procedure stored in the ROM 17B. The etching liquid 2 collected by the sample collection pump 5 is sent to the flow cell 7. An ultraviolet light source 8 such as a combination of a deuterium lamp and a monochromator irradiates the etching liquid in the flow cell with ultraviolet light having a wavelength of about 200 nm, and the ultraviolet light detector 9 determines the amount of transmitted light. This transmitted light amount data is sent to the control unit 17. On the other hand, the etching solution sent by the pump 10 is sent to the etching tank 11 and at the same time, sent to the hydrometer cell 16. The flow rate of the etching solution can be freely adjusted by the valve 15.
Specific gravity data of the etching solution obtained by the specific gravity cell 16 is sent to the control unit 17.

CPU17Aは透過光量より吸光度を算出し、次に吸光度と硝
酸濃度とのデータが格納されているRAM17Cのテーブルに
基づいて硝酸の濃度を算出する。
The CPU 17A calculates the absorbance from the amount of transmitted light, and then calculates the concentration of nitric acid based on the table of the RAM 17C that stores the data on the absorbance and the nitric acid concentration.

次に、硝酸の濃度と燐酸の濃度に応じて変化する比重の
データが格納されているRAM17Cのテーブルに基づいて、
CPU17Aは燐酸の濃度を算出する。
Next, based on the table of RAM17C that stores the data of specific gravity that changes according to the concentration of nitric acid and the concentration of phosphoric acid,
CPU17A calculates the concentration of phosphoric acid.

硝酸および燐酸の濃度がこのように算出されるとCPU17A
は制御部17に格納されている規準濃度との差異を照合
し、その差異量に応じて硝酸供給ポンプ19、燐酸供給ポ
ンプ21および電磁弁23の作動させ、かつ作動時間を指示
する。
When the concentrations of nitric acid and phosphoric acid are calculated in this way, CPU17A
Compares the difference with the reference concentration stored in the control unit 17, operates the nitric acid supply pump 19, the phosphoric acid supply pump 21 and the solenoid valve 23 according to the difference amount, and instructs the operation time.

ここで、基準濃度はRAM17Cまたは17Bとは異なる他のROM
に格納させることができる。
Here, the reference density is different from RAM17C or 17B
Can be stored in.

第6図は本発明の実施例の処理手順の一例を示すフロー
チャートである。ステップS1ないしステップS3におい
て、エッチング液を採取して、硝酸および燐酸の濃度を
算出する。この処理手順の詳細については、すでに説明
したのでここでは省略する。
FIG. 6 is a flow chart showing an example of the processing procedure of the embodiment of the present invention. In steps S1 to S3, the etchant is sampled and the concentrations of nitric acid and phosphoric acid are calculated. The details of this processing procedure have already been described, and will be omitted here.

ステップS4において、ステップS2で算出した硝酸の濃度
とエッチャントの基準硝酸濃度とを比較して、硝酸の濃
度が不足しているか、否かを判断する。硝酸の濃度が不
足していると判断されたならば、ステップS5に進み不足
量を計算し、その結果に基づいて硝酸供給タンク18より
硝酸供給ポンプ19を通して、エッチング液貯蔵槽1に所
定量の硝酸を所定時間かけて供給する。
In step S4, the nitric acid concentration calculated in step S2 is compared with the reference nitric acid concentration of the etchant to determine whether or not the nitric acid concentration is insufficient. If it is determined that the concentration of nitric acid is insufficient, the process proceeds to step S5 to calculate the amount of insufficiency, and based on the result, the nitric acid supply tank 18 passes the nitric acid supply pump 19 to store a predetermined amount of nitric acid in the etching solution storage tank 1. Nitric acid is supplied over a predetermined period of time.

ステップS4において、硝酸の濃度が不足していなければ
ステップS6に進み、ステップS3で算出した燐酸の濃度と
エッチャントの規準燐酸濃度とを比較して、燐酸の濃度
が不足であるか、過剰であるか、規準濃度であるかを判
断する。燐酸の濃度が過剰ならば、ステップS7に進み純
水の配管22の電磁弁23を開き、所定量の純水を供給した
ら電磁弁を閉じる。燐酸の濃度が不足していればステッ
プS8に進み、燐酸の不足量を計算し、その結果に基づい
て燐酸供給タンク20から燐酸ポンプ21を通して所定量の
燐酸をエッチング液貯蔵槽1に供給する。
If the concentration of nitric acid is not insufficient in step S4, the process proceeds to step S6, the concentration of phosphoric acid calculated in step S3 is compared with the standard phosphoric acid concentration of the etchant, and the concentration of phosphoric acid is insufficient or excessive. Or the standard concentration is determined. If the concentration of phosphoric acid is excessive, the process proceeds to step S7, the solenoid valve 23 of the pure water pipe 22 is opened, and when a predetermined amount of pure water is supplied, the solenoid valve is closed. If the concentration of phosphoric acid is insufficient, the process proceeds to step S8, the insufficient amount of phosphoric acid is calculated, and based on the result, a predetermined amount of phosphoric acid is supplied from the phosphoric acid supply tank 20 to the etching solution storage tank 1 through the phosphoric acid pump 21.

硝酸供給ポンプ19、燐酸供給ポンプ21および電磁弁23に
よる硝酸、燐酸および水の供給速度を一定とすれば、そ
れらの作動時間を制御することによって供給量を制御
し、エッチャントを所定の濃度に保つことができる。
If the supply rates of nitric acid, phosphoric acid and water by the nitric acid supply pump 19, the phosphoric acid supply pump 21 and the solenoid valve 23 are constant, the supply amount is controlled by controlling the operation time of them to keep the etchant at a predetermined concentration. be able to.

〔発明の効果〕〔The invention's effect〕

以上説明したように、本発明によれば、インラインでエ
ッチャント濃度の制御が可能であり、エッチング液中の
硝酸および燐酸の濃度が安定化して、エッチングの品質
を確保すると共にエッチング液寿命の延長により、エッ
チング液交換による装置の停止が激減し、薬品の使用量
の減少を含め大幅なコストダウンを達成することができ
る。
As described above, according to the present invention, the etchant concentration can be controlled in-line, the nitric acid and phosphoric acid concentrations in the etching solution are stabilized, and the etching quality is ensured and the etching solution life is extended. Therefore, the number of stoppages of the apparatus due to the exchange of the etching liquid is drastically reduced, and a large cost reduction including the reduction of the amount of chemicals used can be achieved.

【図面の簡単な説明】[Brief description of drawings]

第1図は紫外線波長に対する硝酸の吸光度の変化を示す
特性図、 第2図は硝酸の吸光度と硝酸の濃度との関係を変化を示
す特性図、 第3図は硝酸濃度に応じた燐酸濃度とエッチング液の比
重との関係を示す特性図、 第4図は本発明を適用した薄膜エッチング装置の模式
図、 第5図は本発明の実施例のブロック図、 第6図は本発明の実施例の処理手順の一例を示すフロー
チャートである。 1……エッチング液貯蔵槽、 2……エッチング液、 3……ヒータ、 4……攪拌機、 5……試料採取ポンプ、 6……硝酸の吸光度測定部、 7……フローセル、 8……紫外線光源、 9……紫外線検出部、 10……ポンプ、 11……エッチング槽、 12……スプレー、 13……被加工アルミニウム薄膜基板、 14……配管、 15……バルブ、 16……比重計セル、 17……制御部、 18……硝酸供給タンク、 19……硝酸供給ポンプ、 20……燐酸供給タンク、 21……燐酸供給ポンプ、 22……配管、 23……電磁弁。
Fig. 1 is a characteristic diagram showing the change of the absorbance of nitric acid with respect to the ultraviolet wavelength, Fig. 2 is a characteristic diagram showing the change of the relation between the absorbance of nitric acid and the concentration of nitric acid, and Fig. 3 is the phosphoric acid concentration according to the concentration of nitric acid. FIG. 4 is a characteristic diagram showing the relationship with the specific gravity of the etching solution, FIG. 4 is a schematic diagram of a thin film etching apparatus to which the present invention is applied, FIG. 5 is a block diagram of an embodiment of the present invention, and FIG. 6 is an embodiment of the present invention. 6 is a flowchart showing an example of the processing procedure of FIG. 1 ... Etching solution storage tank, 2 ... Etching solution, 3 ... Heater, 4 ... Stirrer, 5 ... Sampling pump, 6 ... Nitric acid absorbance measurement section, 7 ... Flow cell, 8 ... Ultraviolet light source , 9 ... UV detector, 10 ... Pump, 11 ... Etching tank, 12 ... Spray, 13 ... Aluminum thin film substrate, 14 ... Piping, 15 ... Valve, 16 ... Densitometer cell, 17 …… control part, 18 …… nitric acid supply tank, 19 …… nitric acid supply pump, 20 …… phosphoric acid supply tank, 21 …… phosphoric acid supply pump, 22 …… piping, 23 …… solenoid valve.

フロントページの続き (72)発明者 茂木 久子 埼玉県児玉郡上里町七本木3461 キヤノ ン・コンポーネンツ株式会社内 (72)発明者 檀上 桂志 東京都大田区下丸子3丁目30番2号 キヤ ノン株式会社内 (72)発明者 堀江 仁志 東京都大田区下丸子3丁目30番2号 キヤ ノン株式会社内 (56)参考文献 特開 昭62−103383(JP,A)Front page continued (72) Inventor Hisako Mogi 3461 Nanashiki, Kamisato-cho, Kodama-gun, Saitama Canon Inc. (72) Inventor Keishi Dangami 3-30-2 Shimomaruko, Ota-ku, Tokyo Canon Inc. In-house (72) Inventor Hitoshi Horie 3-30-2 Shimomaruko, Ota-ku, Tokyo Canon Inc. (56) Reference JP 62-103383 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】硝酸と燐酸と水とを含むエッチャントを用
いて被加工物の薄膜をエッチングする薄膜エッチング装
置において、 前記エッチャントの吸光度を測定する第1の測定手段
と、 前記エッチャントの比重を測定する第2の測定手段と、 エッチング液貯蔵槽に硝酸を供給する第1の供給手段
と、 エッチング液貯蔵槽に燐酸を供給する第2の供給手段
と、 エッチング液貯蔵槽に水を供給する第3の供給手段と、 前記第1の測定手段の出力結果に基づいてエッチャント
中の硝酸の濃度を算出し、算出された硝酸の濃度と第2
の測定手段によって測定された比重とに基づいて燐酸の
濃度を算出し、算出された硝酸の濃度と燐酸の濃度とに
基づいて、第1の供給手段、第2の供給手段、および第
3の供給手段を制御する制御手段と を具えたことを特徴とする薄膜エッチング装置。
1. A thin film etching apparatus for etching a thin film of a workpiece using an etchant containing nitric acid, phosphoric acid and water, wherein a first measuring means for measuring the absorbance of the etchant and a specific gravity of the etchant are measured. A second measuring unit for supplying nitric acid to the etching solution storage tank, a second supplying means for supplying phosphoric acid to the etching solution storage tank, and a second supply means for supplying water to the etching solution storage tank. No. 3 supply means, and the concentration of nitric acid in the etchant is calculated based on the output result of the first measuring means, and the calculated concentration of nitric acid and the second concentration are calculated.
The concentration of phosphoric acid is calculated on the basis of the specific gravity measured by the measuring means, and the first supply means, the second supply means, and the third supply means are calculated on the basis of the calculated nitric acid concentration and phosphoric acid concentration. A thin film etching apparatus comprising: a control unit that controls a supply unit.
JP17406889A 1989-07-07 1989-07-07 Thin film etching equipment Expired - Lifetime JPH0651914B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17406889A JPH0651914B2 (en) 1989-07-07 1989-07-07 Thin film etching equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17406889A JPH0651914B2 (en) 1989-07-07 1989-07-07 Thin film etching equipment

Publications (2)

Publication Number Publication Date
JPH0339491A JPH0339491A (en) 1991-02-20
JPH0651914B2 true JPH0651914B2 (en) 1994-07-06

Family

ID=15972071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17406889A Expired - Lifetime JPH0651914B2 (en) 1989-07-07 1989-07-07 Thin film etching equipment

Country Status (1)

Country Link
JP (1) JPH0651914B2 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100390553B1 (en) * 2000-12-30 2003-07-07 주식회사 동진쎄미켐 method of controlling metal-layer etching process and method of regenerating etchant composition using near infrared spectrometer
JP2003049285A (en) * 2001-08-08 2003-02-21 Mitsubishi Chemicals Corp Etching method, quantitative analysis method for etching solution and method for recovering phosphoric acid from etching solution
US7743783B2 (en) * 2006-04-04 2010-06-29 Air Liquide Electronics U.S. Lp Method and apparatus for recycling process fluids
JP5058560B2 (en) * 2006-10-26 2012-10-24 株式会社平間理化研究所 Etching solution management device
JP2008191159A (en) * 2008-02-08 2008-08-21 Ebara Densan Ltd Method and apparatus for analyzing and apparatus for managing concentration of component of system which makes specific gravity and concentration of component vary
JP5405042B2 (en) * 2008-04-22 2014-02-05 株式会社平間理化研究所 Etching solution preparation device and etching solution concentration measuring device
JP5522860B2 (en) * 2012-02-13 2014-06-18 株式会社平間理化研究所 Etching solution management device
JP6454605B2 (en) * 2015-06-01 2019-01-16 東芝メモリ株式会社 Substrate processing method and substrate processing apparatus
JP6751326B2 (en) 2016-09-16 2020-09-02 キオクシア株式会社 Substrate processing apparatus and semiconductor device manufacturing method
JP6850650B2 (en) * 2017-03-27 2021-03-31 株式会社Screenホールディングス Board processing method and board processing equipment

Also Published As

Publication number Publication date
JPH0339491A (en) 1991-02-20

Similar Documents

Publication Publication Date Title
KR101248213B1 (en) Etchant managing device
KR101213108B1 (en) Etching solution preparation apparatus and etching solution concentration measurement apparatus
JPH0651914B2 (en) Thin film etching equipment
US5149659A (en) Method and apparatus for analyzing fluorine containing gases
US5715173A (en) Concentration controlling method and a substate treating apparatus utilizing same
US20040218173A1 (en) Methods and systems for controlling the concentration of a component in a composition with absorption spectroscopy
JP3212958B2 (en) Chemical solution concentration control device
JPH05215703A (en) Method and device for controlling detergent concentration
JP6024936B2 (en) Method for measuring total oxidizing substance concentration, substrate cleaning method and substrate cleaning system
US6921193B2 (en) Chemical concentration control device for semiconductor processing apparatus
US3826741A (en) Method of treating waste solution containing chromate ion or cyanide ion
EP1373600B1 (en) Method of controlling solution concentration in strip cleaning line
US4710261A (en) Apparatus and method for maintaining a uniform etching solution composition
JP2747647B2 (en) Etching liquid management device
JPH11349397A (en) Feeding system and process for epitaxial deposition of silicon using continuously feeding single bubbler
JP4429189B2 (en) Substrate processing apparatus and method
JP3843224B2 (en) Method for measuring sulfuric acid concentration in plating solution
JP3078199B2 (en) Concentration control method and substrate processing apparatus using the same
JPH0634890B2 (en) Preparation method of chemicals
JPH02241591A (en) Regulating method of residual free chlorine in process water
JP2702449B2 (en) Solution sampling device in salt production process
JPH0524660B2 (en)
TWI840693B (en) Method of fluorine measurement
JP3692332B2 (en) Water quality analysis method and apparatus
JP3333237B2 (en) Galvanic cell type oxygen analyzer and method of controlling this analyzer

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 14

Free format text: PAYMENT UNTIL: 20080706

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 14

Free format text: PAYMENT UNTIL: 20080706

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090706

Year of fee payment: 15

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090706

Year of fee payment: 15

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 16

Free format text: PAYMENT UNTIL: 20100706

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100706

Year of fee payment: 16