JPH11145107A - Surface treatment method for substrate - Google Patents

Surface treatment method for substrate

Info

Publication number
JPH11145107A
JPH11145107A JP32247797A JP32247797A JPH11145107A JP H11145107 A JPH11145107 A JP H11145107A JP 32247797 A JP32247797 A JP 32247797A JP 32247797 A JP32247797 A JP 32247797A JP H11145107 A JPH11145107 A JP H11145107A
Authority
JP
Japan
Prior art keywords
temperature
phosphoric acid
aqueous solution
acid aqueous
substrate
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
Application number
JP32247797A
Other languages
Japanese (ja)
Inventor
Katsunori Tanaka
克典 田中
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.)
Dainippon Screen Manufacturing Co Ltd
Original Assignee
Dainippon Screen Manufacturing Co Ltd
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 Dainippon Screen Manufacturing Co Ltd filed Critical Dainippon Screen Manufacturing Co Ltd
Priority to JP32247797A priority Critical patent/JPH11145107A/en
Publication of JPH11145107A publication Critical patent/JPH11145107A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method which enables selective etching of a predetermined film formed on the surface of a substrate, while maintaining a treatment solution made of an acid solution constantly in a boiling state by holding the treatment solution at a predetermined temperature and a predetermined acid concentration. SOLUTION: A treatment solution 14 in a treatment tub 10 is heated and constantly held in a boiling state by a constant-output heater 16 and 24, and the temperature of the treatment solution is detected by a temperature detector 34. On the basis of the detected temperature, the quantity of pure water 28 supplied from a pure water tub 30 to the treatment solution is controlled by a regulator 42, so that the treatment solution is held at a predetermined temperature.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【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燐酸
水溶液等の酸の水溶液からなる処理液中に浸漬させて表
面処理する方法、特に、沸騰状態に保たれた処理液中に
基板を浸漬させて、基板の表面上に形成された2種類も
しくはそれ以上の種類の被膜のうちの所定の被膜を選択
的にエッチングする基板の表面処理方法に関する。
[0001] The present invention relates to a semiconductor wafer,
A method of immersing a glass substrate for a liquid crystal display device, a substrate such as an electronic component, etc. in a treatment solution composed of an aqueous solution of an acid such as a phosphoric acid aqueous solution to perform surface treatment, particularly, immersing the substrate in a treatment solution kept in a boiling state. The present invention also relates to a substrate surface treatment method for selectively etching a predetermined coating of two or more types of coatings formed on the surface of a substrate.

【0002】[0002]

【従来の技術】基板、例えば半導体ウエハを酸の水溶液
からなる処理液、例えば燐酸水溶液中に浸漬させて、半
導体ウエハの表面上に形成された2種類もしくはそれ以
上の種類の被膜のうちの所定の被膜、例えばシリコン酸
化膜(SiO2膜)とシリコン窒化膜(Si34)との
うちのシリコン窒化膜を選択的にエッチングする場合に
は、従来、図3に概略構成を模式図で示すような表面処
理装置が使用されている。この装置は、底部に液導入口
12が形設され内部に燐酸水溶液14が貯留される処理
槽10を有し、処理槽10の内部には、投込みヒータ1
6が配設されている。そして、処理しようとする半導体
ウエハは、ウエハホルダ(図示せず)に複数枚収納され
て、処理槽10内へ投入され燐酸水溶液14中に浸漬さ
せられる。
2. Description of the Related Art A substrate, for example, a semiconductor wafer is immersed in a processing solution comprising an aqueous solution of an acid, for example, an aqueous solution of phosphoric acid, and a predetermined one of two or more kinds of coating films formed on the surface of the semiconductor wafer is obtained. Conventionally, when selectively etching a silicon nitride film out of a silicon oxide film (SiO 2 film) and a silicon nitride film (Si 3 N 4 ), a schematic configuration is schematically shown in FIG. A surface treatment device as shown is used. This apparatus has a processing tank 10 in which a liquid inlet 12 is formed at the bottom and a phosphoric acid aqueous solution 14 is stored inside. A processing heater 10 is provided inside the processing tank 10.
6 are provided. Then, a plurality of semiconductor wafers to be processed are stored in a wafer holder (not shown), put into the processing tank 10 and immersed in the phosphoric acid aqueous solution 14.

【0003】処理槽10には、溢流液受け部18が付設
されており、処理槽10の上部から溢れ出た燐酸水溶液
が溢流液受け部18内へ流入するようになっている。溢
流液受け部18の内底部には、液循環用配管20が連通
しており、液循環用配管20の先端は、処理槽10の液
導入口12に連通接続されている。液循環用配管20に
は、循環ポンプ22、インラインヒータ24およびフィ
ルタ26が介設されており、燐酸水溶液は、処理槽1
0、溢流液受け部18および液循環用配管20により構
成された循環経路を循環させられる。溢流液受け部18
には、純水28が貯留された純水槽30の内底部に一端
が連通し定量ポンプ32が介設された純水供給管50の
他端吐出口が配置されている。また、処理槽10の内部
には、温度検出器34が配置されており、温度検出器3
4は温度調節器52に接続され、温度調節器52は投込
みヒータ16に接続されている。さらに、液循環用配管
20の途中に温度検出器54が介挿され、温度検出器5
4は温度調節器56に接続され、温度調節器56はイン
ラインヒータ24に接続されている。
[0003] The processing tank 10 is provided with an overflow liquid receiving portion 18 so that the phosphoric acid aqueous solution overflowing from the upper portion of the processing tank 10 flows into the overflow liquid receiving portion 18. A liquid circulation pipe 20 communicates with the inner bottom of the overflow liquid receiving portion 18, and the tip of the liquid circulation pipe 20 is connected to the liquid inlet 12 of the processing tank 10. A circulation pump 22, an in-line heater 24, and a filter 26 are interposed in the liquid circulation pipe 20.
0, the liquid can be circulated through the circulation path formed by the overflow liquid receiving portion 18 and the liquid circulation pipe 20. Overflow liquid receiver 18
Is provided with a discharge port at the other end of a pure water supply pipe 50 having one end communicating with the inner bottom of a pure water tank 30 in which pure water 28 is stored and having a fixed amount pump 32 interposed therebetween. Further, a temperature detector 34 is disposed inside the processing tank 10, and the temperature detector 3 is provided.
4 is connected to the temperature controller 52, and the temperature controller 52 is connected to the injection heater 16. Further, a temperature detector 54 is inserted in the middle of the liquid circulation pipe 20, and the temperature detector 5
4 is connected to a temperature controller 56, and the temperature controller 56 is connected to the in-line heater 24.

【0004】図3に示した構成の装置により半導体ウエ
ハを表面処理する場合、燐酸水溶液14は、投込みヒー
タ16およびインラインヒータ24によって150℃〜
180℃程度の温度に加熱される。このため、処理槽1
0内の燐酸水溶液14から水分が蒸発し、燐酸水溶液1
4の燐酸濃度が上昇する。そこで、定量ポンプ32によ
って純水槽30内から純水28を、純水供給管50を通
して供給し、純水供給管50の吐出口から、溢流液受け
部18内に流入した燐酸水溶液に純水を連続して滴下さ
せるようにしている。この際、従来は、純水供給管50
内を通って一定流量の純水を流し、処理槽10内の燐酸
水溶液14から蒸発した水分量にほぼ相当する量の純水
を常時補充するようにしている。また、処理槽10内の
燐酸水溶液14の温度は、各温度検出器34、54から
送られる検出信号に基づいて各温度調節器52、56に
より投込みヒータ16およびインラインヒータ24をそ
れぞれ制御、通常はPID制御して、所定温度に保たれ
るように調節されている。
When a semiconductor wafer is subjected to surface treatment by the apparatus having the structure shown in FIG. 3, a phosphoric acid aqueous solution 14 is heated to 150 ° C. by an injection heater 16 and an in-line heater 24.
It is heated to a temperature of about 180 ° C. Therefore, processing tank 1
Water evaporates from the phosphoric acid aqueous solution 14 in the
The phosphoric acid concentration of 4 increases. Therefore, pure water 28 is supplied from the pure water tank 30 through the pure water supply pipe 50 by the metering pump 32, and the pure water is supplied from the discharge port of the pure water supply pipe 50 to the phosphoric acid aqueous solution flowing into the overflow liquid receiving portion 18. Is continuously dropped. At this time, conventionally, the pure water supply pipe 50
A constant flow of pure water is passed through the inside of the processing tank, and pure water is constantly replenished in an amount substantially equivalent to the amount of water evaporated from the phosphoric acid aqueous solution 14 in the treatment tank 10. The temperature of the phosphoric acid aqueous solution 14 in the processing tank 10 is controlled by the temperature controllers 52 and 56 based on the detection signals sent from the temperature detectors 34 and 54, respectively. Is controlled by PID control so as to be maintained at a predetermined temperature.

【0005】ところで、シリコン酸化膜に対してシリコ
ン窒化膜を選択的にエッチングする場合には、シリコン
酸化膜のエッチングレートに対するシリコン窒化膜のエ
ッチングレートの比、すなわち選択比が問題となる。ま
た、シリコン酸化膜やシリコン窒化膜のエッチングレー
トは、燐酸水溶液の温度によって変化し、燐酸水溶液の
温度が高くなるほど大きくなる。そして、燐酸水溶液の
或る温度における選択比は、当該温度において燐酸水溶
液が沸騰状態にあるとき、言い換えると、当該温度が燐
酸水溶液の沸点となるような燐酸濃度であるときに、最
も大きくなる。したがって、シリコン窒化膜のエッチン
グレートや選択比、燐酸水溶液の濃度などとの関係で適
宜選定された処理温度に処理槽10内の燐酸水溶液14
の温度を保持し、かつ、その温度において常に燐酸水溶
液が沸騰している状態に保たれるように、すなわち、当
該温度が燐酸水溶液の沸点となるような燐酸濃度に保た
れるようにして、半導体ウエハの表面処理を行うことが
重要である。
When the silicon nitride film is selectively etched with respect to the silicon oxide film, the ratio of the etching rate of the silicon nitride film to the etching rate of the silicon oxide film, that is, the selectivity becomes a problem. Further, the etching rate of the silicon oxide film or the silicon nitride film changes depending on the temperature of the phosphoric acid aqueous solution, and increases as the temperature of the phosphoric acid aqueous solution increases. The selectivity of the phosphoric acid aqueous solution at a certain temperature becomes maximum when the phosphoric acid aqueous solution is in a boiling state at the temperature, in other words, when the temperature is a phosphoric acid concentration at which the phosphoric acid aqueous solution has a boiling point. Therefore, the phosphoric acid aqueous solution 14 in the processing bath 10 is kept at a processing temperature appropriately selected in relation to the etching rate and the selectivity of the silicon nitride film, the concentration of the phosphoric acid aqueous solution, and the like.
So that the phosphoric acid aqueous solution is always kept at a boiling state at that temperature, that is, the phosphoric acid concentration is maintained such that the temperature becomes the boiling point of the phosphoric acid aqueous solution. It is important to perform a surface treatment on a semiconductor wafer.

【0006】[0006]

【発明が解決しようとする課題】処理槽10内の燐酸水
溶液14は、投込みヒータ16およびインラインヒータ
24で加熱されることにより水分が蒸発して、燐酸濃度
が上昇し、一方、上昇した燐酸濃度を下げるために、燐
酸水溶液の循環経路中において純水槽30から純水供給
管50を通って純水が燐酸水溶液へ補充される。したが
って、燐酸水溶液14の燐酸濃度は、燐酸水溶液14か
らの水分の蒸発量と純水の補充量とによって決まり、水
分蒸発量と純水補充量とが常に等しくなれば、燐酸水溶
液の燐酸濃度は、一定に保たれることになる。
The phosphoric acid aqueous solution 14 in the treatment tank 10 is heated by the injection heater 16 and the in-line heater 24 to evaporate water, thereby increasing the concentration of phosphoric acid. In order to lower the concentration, pure water is replenished to the phosphoric acid aqueous solution from the pure water tank 30 through the pure water supply pipe 50 in the circulation path of the phosphoric acid aqueous solution. Therefore, the phosphoric acid concentration of the phosphoric acid aqueous solution 14 is determined by the evaporation amount of water from the phosphoric acid aqueous solution 14 and the replenishing amount of pure water. If the water evaporation amount and the replenishing amount of pure water are always equal, the phosphoric acid concentration of the phosphoric acid aqueous solution becomes , Will be kept constant.

【0007】一方、燐酸水溶液への純水の補充によって
燐酸水溶液の熱量を奪うため、燐酸水溶液の温度が低下
する。燐酸水溶液の温度が低下すると、温度検出器3
4、54からの検出信号に基づいて温度調節器52、5
6によりヒータ16、24が制御されて、純水の補充に
よって燐酸水溶液から奪われた熱量に見合った熱量が燐
酸水溶液に与えられ、処理槽10内の燐酸水溶液14の
温度が所定温度に保持される。
On the other hand, the replenishment of pure water into the phosphoric acid aqueous solution removes the heat of the phosphoric acid aqueous solution, so that the temperature of the phosphoric acid aqueous solution decreases. When the temperature of the phosphoric acid aqueous solution decreases, the temperature detector 3
Temperature controllers 52, 5 based on the detection signals from 4, 54
The heaters 16 and 24 are controlled by 6 so that the amount of heat corresponding to the amount of heat removed from the aqueous phosphoric acid solution by the replenishment of pure water is given to the aqueous phosphoric acid solution, and the temperature of the aqueous phosphoric acid solution 14 in the processing tank 10 is maintained at a predetermined temperature. You.

【0008】ところが、従来のように燐酸水溶液へ一定
量の純水を連続して補充する方法では、処理槽10内の
燐酸水溶液14からの水分蒸発量と純水補充量とが等し
くなるとは限らない。このため、処理槽10内の燐酸水
溶液14の温度が所定温度に保持されても、その温度が
燐酸水溶液の沸点となるとは限らない。このように、従
来の方法では、所定温度において常に燐酸水溶液が沸騰
状態に保たれるように燐酸水溶液の燐酸濃度を制御しな
がら、半導体ウエハの表面処理を行うことは困難であっ
た。
However, in the conventional method of continuously replenishing a fixed amount of pure water to the phosphoric acid aqueous solution, the amount of water evaporated from the phosphoric acid aqueous solution 14 in the treatment tank 10 and the amount of pure water replenishment are not always equal. Absent. For this reason, even if the temperature of the phosphoric acid aqueous solution 14 in the treatment tank 10 is maintained at a predetermined temperature, the temperature does not always become the boiling point of the phosphoric acid aqueous solution. As described above, in the conventional method, it is difficult to perform the surface treatment of the semiconductor wafer while controlling the phosphoric acid concentration of the phosphoric acid aqueous solution such that the phosphoric acid aqueous solution is always kept in a boiling state at a predetermined temperature.

【0009】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、酸の水溶液からなる処理液を所定温
度に保持しかつ常に沸騰状態に保ちながら、基板の表面
上に形成された2種類もしくはそれ以上の種類の被膜の
うちの所定の被膜を選択的にエッチングすることができ
る基板の表面処理方法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 has been made on a surface of a substrate while maintaining a processing solution comprising an aqueous acid solution at a predetermined temperature and always in a boiling state. It is an object of the present invention to provide a method for treating a surface of a substrate, which can selectively etch a predetermined film among two or more types of films.

【0010】[0010]

【課題を解決するための手段】請求項1に係る発明は、
酸の水溶液からなる処理液をヒータで加熱して処理液を
沸騰状態に保ち、沸騰状態の処理液中に基板を浸漬させ
て、基板の表面上に形成された2種類もしくはそれ以上
の種類の被膜のうちの所定の被膜を選択的にエッチング
する基板の表面処理方法において、前記ヒータの出力を
一定にして処理液に対し一定の熱量を与えて処理液を常
に沸騰状態に保つとともに、処理液の温度を検出し、そ
の検出温度に基づいて処理液の温度が所定温度に保持さ
れるように処理液への純水の補充量を制御することを特
徴とする。
The invention according to claim 1 is
A processing solution comprising an aqueous solution of an acid is heated by a heater to maintain the processing solution in a boiling state, and the substrate is immersed in the processing solution in a boiling state, and two or more types formed on the surface of the substrate In a method of treating a surface of a substrate for selectively etching a predetermined film among the films, a constant amount of heat is applied to the processing solution while the output of the heater is kept constant, and the processing solution is always kept in a boiling state. And the amount of pure water replenished to the processing liquid is controlled based on the detected temperature so that the temperature of the processing liquid is maintained at a predetermined temperature.

【0011】請求項2に係る発明は、請求項1記載の方
法において、処理液中への基板の投入時点から所定時間
内だけ、および、処理液の補充時点から所定時間内だ
け、それぞれヒータの出力を最大にすることを特徴とす
る。
According to a second aspect of the present invention, in the method according to the first aspect, the heaters are provided only within a predetermined time from a point in time when the substrate is put into the processing liquid and within a predetermined time from a point in time when the processing liquid is replenished. The feature is to maximize the output.

【0012】請求項3に係る発明は、請求項1または請
求項2記載の方法において、処理液が燐酸水溶液であ
り、基板の表面上に形成された被膜がシリコン酸化膜と
シリコン窒化膜とであって、シリコン窒化膜を選択的に
エッチングすることを特徴とする。
According to a third aspect of the present invention, in the method according to the first or second aspect, the processing solution is a phosphoric acid aqueous solution, and the film formed on the surface of the substrate is a silicon oxide film and a silicon nitride film. And selectively etching the silicon nitride film.

【0013】請求項1に係る発明の基板の表面処理方法
によると、一定出力のヒータにより処理液に対し一定の
熱量が与えられて、処理液が常に沸騰状態に保たれる。
すなわち、処理液がヒータによって加熱されることによ
り、処理液から水分が蒸発して、処理液の酸濃度が上昇
し、それに伴って処理液の沸点も上昇するが、処理液
は、上昇した沸点まで処理液の温度を同時的に上昇させ
ることができる程度の一定出力のヒータにより加熱され
て、常に沸騰状態に保たれる。一方、処理液の温度が検
出され、その検出温度に基づいて処理液の温度が所定温
度に保持されるように処理液へ純水が補充される。すな
わち、上記したように処理液からの水分の蒸発に伴う処
理液の酸濃度の上昇(沸点の上昇)により処理液の温度
が上昇するので、処理液からの水分蒸発に相応する処理
液の温度上昇を検出して、その温度上昇分に対応する量
の純水を処理液へ補充することにより、処理液の温度が
降下して元の所定温度に保持される。この時も、処理液
は沸騰状態に保たれているので、所定温度が処理液の沸
点であり、処理液は、所定温度が沸点となるような元の
酸濃度に保持されることとなる。このようにして、処理
液は、所定温度に保持されかつ所定濃度に保持されて常
に沸騰状態に保たれる。
According to the substrate surface treatment method of the present invention, a constant amount of heat is given to the processing liquid by the heater having a constant output, and the processing liquid is always kept in a boiling state.
That is, when the processing liquid is heated by the heater, the water evaporates from the processing liquid, the acid concentration of the processing liquid increases, and the boiling point of the processing liquid also increases accordingly. The temperature of the processing liquid is raised by a heater having a constant output that can raise the temperature of the processing liquid simultaneously, and the processing liquid is always kept in a boiling state. On the other hand, the temperature of the processing liquid is detected, and pure water is replenished to the processing liquid based on the detected temperature so that the temperature of the processing liquid is maintained at a predetermined temperature. That is, as described above, the temperature of the processing solution rises due to the increase in the acid concentration (boiling point increase) of the processing solution accompanying the evaporation of water from the processing solution. By detecting the rise and replenishing the processing liquid with pure water in an amount corresponding to the temperature rise, the temperature of the processing liquid falls and is maintained at the original predetermined temperature. Also at this time, since the processing liquid is kept in a boiling state, the predetermined temperature is the boiling point of the processing liquid, and the processing liquid is maintained at the original acid concentration such that the predetermined temperature becomes the boiling point. In this way, the processing liquid is maintained at a predetermined temperature and a predetermined concentration, and is constantly kept in a boiling state.

【0014】請求項2に係る発明の方法では、処理液中
へ基板を投入した時や処理液を補充した時のように処理
液の温度が瞬時に大きく低下した時に、その時点から所
定時間内だけヒータの出力が最大にされるので、処理液
の温度が速やかに回復する。このため、基板の表面上に
形成された被膜のエッチングレートが低下するのを避け
ることができる。
In the method according to the second aspect of the present invention, when the temperature of the processing liquid is greatly reduced instantaneously, such as when the substrate is put into the processing liquid or when the processing liquid is replenished, the processing is performed within a predetermined time from that point. Only the output of the heater is maximized, so that the temperature of the processing liquid quickly recovers. For this reason, it is possible to avoid a decrease in the etching rate of the film formed on the surface of the substrate.

【0015】請求項3に係る発明の方法では、燐酸水溶
液が所定温度に保持されかつ所定の燐酸濃度に保持され
て常に沸騰状態に保たれ、シリコン酸化膜に対するシリ
コン窒化膜の選択比が大きくなった状態で、基板の表面
上に形成されたシリコン窒化膜が選択的にエッチングさ
れる。
In the method according to the third aspect of the present invention, the phosphoric acid aqueous solution is maintained at a predetermined temperature and a predetermined phosphoric acid concentration to be constantly kept in a boiling state, and the selectivity of the silicon nitride film to the silicon oxide film is increased. In this state, the silicon nitride film formed on the surface of the substrate is selectively etched.

【0016】[0016]

【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および図2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.

【0017】図1は、この発明に係る基板の表面処理方
法を実施するのに使用される表面処理装置の概略構成の
1例を示す模式図である。図1において、図3で使用し
た符号と同一符号を付した構成要素は、図3に示した従
来の装置と共通するものであり、それらの説明を省略す
る。
FIG. 1 is a schematic view showing an example of a schematic configuration of a surface treatment apparatus used for carrying out a substrate surface treatment method according to the present invention. In FIG. 1, components denoted by the same reference numerals as those used in FIG. 3 are the same as those in the conventional apparatus shown in FIG. 3, and the description thereof will be omitted.

【0018】この装置では、純水28が貯留された純水
槽30の内底部に一端が連通し他端吐出口が溢流液受け
部18に配置され定量ポンプ32が介設された純水供給
管36に、流量制御弁38および流量計40が介挿され
ている。また、処理槽10の内部に配置された温度検出
器34が流量調節器42に接続され、流量調節器42が
流量制御弁38に接続されている。さらに、投込みヒー
タ16およびインラインヒータ24に出力調節器44が
接続されている。これら以外の構成は、図3に示した従
来の装置と同様である。
In this apparatus, one end communicates with the inner bottom of a pure water tank 30 in which pure water 28 is stored, and the other end of the pure water tank 30 is disposed in the overflow liquid receiving portion 18 and a pure water supply system in which a metering pump 32 is provided. A flow control valve 38 and a flow meter 40 are inserted in the pipe 36. Further, the temperature detector 34 disposed inside the processing tank 10 is connected to the flow controller 42, and the flow controller 42 is connected to the flow control valve 38. Further, an output adjuster 44 is connected to the injection heater 16 and the in-line heater 24. Other configurations are the same as those of the conventional device shown in FIG.

【0019】図1に示した構成の装置より基板を表面処
理するには、例えば表面上にシリコン酸化膜とシリコン
窒化膜とが形成された半導体ウエハを燐酸水溶液によっ
て選択的エッチングするには、出力調節器44により投
込みヒータ16およびインラインヒータ24の出力が常
に一定となるように調節して、投込みヒータ16および
インラインヒータ24によって処理槽10内の燐酸水溶
液14が150℃〜180℃の所定温度に加熱されるよ
うにする。この際のヒータ16、24の出力は、燐酸水
溶液14を常に沸騰状態に保つために必要な熱量が燐酸
水溶液に対して与えられる程度に設定される。すなわ
ち、燐酸水溶液から水分が蒸発して燐酸濃度が上昇し、
それに伴って燐酸水溶液の沸点が上昇しても、その上昇
した沸点まで燐酸水溶液の温度を同時的に上昇させるこ
とができる程度に、ヒータ16、24の出力が設定され
る。また、処理槽10内の燐酸水溶液14の温度が温度
検出器34によって検出され、その検出信号が流量調節
器42へ送られ、検出信号に基づいて流量調節器42に
より流量制御弁38が制御、例えばPID制御されるよ
うにする。そして、処理槽10内の燐酸水溶液14の温
度が所定温度に保持されるように、純水槽30から純水
供給管36を通って溢流液受け部18内へ供給される純
水の流量が調節され、循環経路内を循環している燐酸水
溶液への単位時間当りの純水の補充量が調節される。
In order to perform a surface treatment on a substrate with the apparatus having the structure shown in FIG. 1, for example, in order to selectively etch a semiconductor wafer having a silicon oxide film and a silicon nitride film formed on its surface with a phosphoric acid aqueous solution, an output power is required. The output of the injection heater 16 and the in-line heater 24 is adjusted to be always constant by the controller 44, and the phosphoric acid aqueous solution 14 in the processing tank 10 is adjusted to a predetermined temperature of 150 ° C. to 180 ° C. by the injection heater 16 and the in-line heater 24. Allow to heat to temperature. The outputs of the heaters 16 and 24 at this time are set to such an extent that the amount of heat necessary to keep the phosphoric acid aqueous solution 14 in a boiling state is always given to the phosphoric acid aqueous solution. That is, the water content evaporates from the phosphoric acid aqueous solution and the phosphoric acid concentration increases,
Even if the boiling point of the phosphoric acid aqueous solution rises accordingly, the outputs of the heaters 16 and 24 are set to such an extent that the temperature of the phosphoric acid aqueous solution can be raised simultaneously to the increased boiling point. Further, the temperature of the phosphoric acid aqueous solution 14 in the processing tank 10 is detected by the temperature detector 34, and a detection signal is sent to the flow controller 42, and the flow controller 42 controls the flow control valve 38 based on the detection signal. For example, PID control is performed. Then, the flow rate of pure water supplied from the pure water tank 30 to the overflow liquid receiving portion 18 through the pure water supply pipe 36 so that the temperature of the phosphoric acid aqueous solution 14 in the treatment tank 10 is maintained at a predetermined temperature. The amount of pure water replenished per unit time to the phosphoric acid aqueous solution circulating in the circulation path is regulated.

【0020】上記したように、出力調節器44により投
込みヒータ16およびインラインヒータ24の出力を一
定にするとともに、温度検出器34によって処理槽10
内の燐酸水溶液14の温度を検出し、流量調節器42に
より流量制御弁38を制御して、燐酸水溶液14の温度
が所定温度に保持されるように単位時間当りの純水の補
充量を調節することにより、燐酸水溶液14の燐酸濃度
が一定に保持されて、燐酸水溶液14が常に沸騰状態に
保たれることとなる。すなわち、処理槽10内の燐酸水
溶液14から水分が蒸発することにより、燐酸水溶液1
4の燐酸濃度が上昇して燐酸水溶液14の沸点が上昇
し、それに伴って燐酸水溶液14の温度が上昇するの
で、燐酸水溶液14からの水分蒸発に相応する燐酸水溶
液14の温度上昇を温度検出器34により検出して、そ
の温度上昇分に対応する量の純水を燐酸水溶液へ補充す
ると、燐酸水溶液14の温度が降下して元の所定温度に
保持される。この時も、燐酸水溶液14は沸騰状態に保
たれているので、所定温度が燐酸水溶液14の沸点であ
り、燐酸水溶液14は、所定温度が沸点となるような元
の燐酸濃度に保持されることとなる。
As described above, the output of the injection heater 16 and the output of the in-line heater 24 are made constant by the output adjuster 44, and the temperature of the processing tank 10 is changed by the temperature detector 34.
The temperature of the phosphoric acid aqueous solution 14 is detected, and the flow controller 42 controls the flow control valve 38 to adjust the amount of pure water replenished per unit time so that the temperature of the phosphoric acid aqueous solution 14 is maintained at a predetermined temperature. By doing so, the phosphoric acid concentration of the phosphoric acid aqueous solution 14 is kept constant, and the phosphoric acid aqueous solution 14 is always kept in a boiling state. That is, water evaporates from the phosphoric acid aqueous solution 14 in the treatment tank 10, and the phosphoric acid aqueous solution 1
4, the boiling point of the phosphoric acid aqueous solution 14 rises, and the temperature of the phosphoric acid aqueous solution 14 rises accordingly. Therefore, the temperature rise of the phosphoric acid aqueous solution 14 corresponding to the evaporation of water from the phosphoric acid aqueous solution 14 is detected by a temperature detector. When the amount of pure water is detected in step 34 and added to the phosphoric acid aqueous solution in an amount corresponding to the temperature rise, the temperature of the phosphoric acid aqueous solution 14 is lowered and maintained at the original predetermined temperature. At this time, since the phosphoric acid aqueous solution 14 is kept in a boiling state, the predetermined temperature is the boiling point of the phosphoric acid aqueous solution 14, and the phosphoric acid aqueous solution 14 is maintained at the original phosphoric acid concentration such that the predetermined temperature becomes the boiling point. Becomes

【0021】なお、処理槽10内の燐酸水溶液14中へ
半導体ウエハを投入した時や処理槽10内へ燐酸水溶液
を補充した時などのように、外乱によって燐酸水溶液1
4の温度が瞬時に大きく低下すると、シリコン窒化膜の
エッチングレートの低下を招くこととなる。このため、
処理槽10内の燐酸水溶液14中へのウエハの投入や処
理槽10内への燐酸水溶液の補充などによって燐酸水溶
液14の温度が瞬時に低下した時には、出力調節器44
によりヒータ16、24の出力を最大値に調節して燐酸
水溶液14を加熱するようにするとよい。このようにす
ると、燐酸水溶液14の温度が瞬時に低下しても、燐酸
水溶液14の温度は速やかに回復するので、シリコン窒
化膜のエッチングレートの低下を避けることができる。
Incidentally, when the semiconductor wafer is put into the phosphoric acid aqueous solution 14 in the processing tank 10 or when the phosphoric acid aqueous solution is replenished into the processing tank 10, the phosphoric acid aqueous solution 1 is disturbed by disturbance.
If the temperature of 4 greatly decreases instantaneously, the etching rate of the silicon nitride film will decrease. For this reason,
When the temperature of the phosphoric acid aqueous solution 14 is instantaneously lowered due to the introduction of the wafer into the phosphoric acid aqueous solution 14 in the processing bath 10 or the replenishment of the phosphoric acid aqueous solution into the processing bath 10, the output controller 44.
It is preferable to adjust the output of the heaters 16 and 24 to the maximum value to heat the phosphoric acid aqueous solution 14. In this way, even if the temperature of the phosphoric acid aqueous solution 14 instantaneously decreases, the temperature of the phosphoric acid aqueous solution 14 recovers quickly, so that a decrease in the etching rate of the silicon nitride film can be avoided.

【0022】図2に、処理槽10内の燐酸水溶液14の
温度変化の状態の1例を示す。まず、処理を開始して燐
酸水溶液14の温度が設定温度に到達するまでの期間T
1は、出力調節器44によりヒータ16、24の出力を
最大値に調節して燐酸水溶液14を加熱する。そして、
燐酸水溶液14の温度が設定温度に到達した後、処理槽
10内の燐酸水溶液14中へウエハを投入したりあるい
は処理槽10内へ燐酸水溶液を補充したりする時点tま
での期間T2は、出力調節器44によりヒータ16、2
4の出力を設定値に調節して、燐酸水溶液14に対し一
定の熱量を与え続ける。処理槽10内の燐酸水溶液14
中へウエハを投入したりあるいは処理槽10内へ燐酸水
溶液を補充したりすると、その時点tから燐酸水溶液1
4の温度が降下した後上昇に転じて再び設定温度に到達
するまでの期間T3は、出力調節器44によりヒータ1
6、24の出力を最大値に調節して燐酸水溶液14に大
きな熱量を与える。そして、燐酸水溶液14の温度が設
定温度に到達した以後の期間T4は、出力調節器44に
よりヒータ16、24の出力を設定値に調節して、燐酸
水溶液14に対し一定の熱量を与え続ける。
FIG. 2 shows an example of a temperature change state of the phosphoric acid aqueous solution 14 in the processing tank 10. First, a period T until the temperature of the phosphoric acid aqueous solution 14 reaches the set temperature from the start of the treatment.
1 controls the output of the heaters 16 and 24 to the maximum value by the output adjuster 44 to heat the phosphoric acid aqueous solution 14. And
After the temperature of the phosphoric acid aqueous solution 14 reaches the set temperature, a period T2 until a time t at which a wafer is loaded into the phosphoric acid aqueous solution 14 in the processing bath 10 or the phosphoric acid aqueous solution is replenished into the processing bath 10 is output. The heaters 16 and 2 are controlled by the controller 44.
The output of 4 is adjusted to the set value, and a constant amount of heat is continuously given to the phosphoric acid aqueous solution 14. Phosphoric acid aqueous solution 14 in processing tank 10
When a wafer is put into the tank or the phosphoric acid aqueous solution is replenished into the processing tank 10, the phosphoric acid aqueous solution 1
During the period T3 from the time when the temperature of the temperature controller 4 falls to the time when the temperature rises and reaches the set temperature again, the output controller 44 controls the heater 1
The output of 6, 24 is adjusted to the maximum value to give a large amount of heat to the phosphoric acid aqueous solution 14. In the period T4 after the temperature of the phosphoric acid aqueous solution 14 reaches the set temperature, the output of the heaters 16 and 24 is adjusted to the set value by the output adjuster 44, and a constant amount of heat is continuously given to the phosphoric acid aqueous solution 14.

【0023】また、処理槽10内の燐酸水溶液14の温
度が上昇する過程で、燐酸水溶液14の温度が比例帯P
内に入ると(a時点)、純水の補充を開始して補充量を
徐々に増加させる。この後、燐酸水溶液14の温度がな
おも上昇して比例帯P内を出ると(b時点)、純水の補
充量を最大にして一定に保つ。そして、燐酸水溶液14
の温度がさらに上昇してピークに達した後降下する過程
で、燐酸水溶液14の温度が比例帯P内に入ると(c時
点)、純水の補充量を徐々に減少させる。この後、燐酸
水溶液14の温度がなおも降下して比例帯P内を出ると
(d時点)、純水の補充を停止する。純水の補充を停止
してからしばらくすると、燐酸水溶液14の温度は降下
から上昇に転じる。そして、燐酸水溶液14の温度が上
昇して比例帯P内に入ると(a時点)、再び純水の補充
を開始して補充量を徐々に増加させる。以後、このよう
な温度変化が繰り返される。そして、この場合、処理槽
10内の燐酸水溶液14は常に沸騰状態に保たれている
ので、図2に示した定常状態での燐酸水溶液14の温度
変化は、燐酸水溶液14の沸点の変化に対応するもので
あり、したがって、図2に示した燐酸水溶液14の温度
変化は、燐酸水溶液14の燐酸濃度の変化を示している
ことになる。すなわち、純水の補充によって燐酸水溶液
14の燐酸濃度が低下(燐酸水溶液14の沸点が降下)
すると、それに伴って処理槽10内の燐酸水溶液14の
温度が降下し、純水の補充を停止することによって燐酸
水溶液14からの水分蒸発により燐酸水溶液14の燐酸
濃度が上昇(燐酸水溶液14の沸点が上昇)すると、そ
れに伴って処理槽10内の燐酸水溶液14の温度が上昇
することになるからである。
During the process of increasing the temperature of the phosphoric acid aqueous solution 14 in the processing tank 10, the temperature of the phosphoric acid aqueous solution 14
When it enters (time point a), replenishment of pure water is started and the replenishment amount is gradually increased. Thereafter, when the temperature of the phosphoric acid aqueous solution 14 still rises and exits the proportional band P (time point b), the replenishing amount of pure water is maximized and kept constant. And the phosphoric acid aqueous solution 14
When the temperature of the phosphoric acid aqueous solution 14 falls within the proportional band P (time point c) in the process of further increasing the temperature, reaching the peak and then decreasing, the replenishment amount of pure water is gradually reduced. Thereafter, when the temperature of the phosphoric acid aqueous solution 14 still falls and goes out of the proportional band P (time point d), the replenishment of pure water is stopped. Some time after the replenishment of the pure water is stopped, the temperature of the phosphoric acid aqueous solution 14 starts to fall from rising to rising. Then, when the temperature of the phosphoric acid aqueous solution 14 rises and enters the proportional band P (time point a), replenishment of pure water is started again, and the replenishment amount is gradually increased. Thereafter, such a temperature change is repeated. In this case, since the phosphoric acid aqueous solution 14 in the treatment tank 10 is always kept in a boiling state, the temperature change of the phosphoric acid aqueous solution 14 in the steady state shown in FIG. Therefore, the temperature change of the phosphoric acid aqueous solution 14 shown in FIG. 2 indicates a change in the phosphoric acid concentration of the phosphoric acid aqueous solution 14. In other words, the replenishment of pure water lowers the phosphoric acid concentration of the phosphoric acid aqueous solution 14 (the boiling point of the phosphoric acid aqueous solution 14 drops).
Then, the temperature of the phosphoric acid aqueous solution 14 in the treatment tank 10 is lowered accordingly, and the replenishment of pure water is stopped. This increases the temperature of the phosphoric acid aqueous solution 14 in the treatment tank 10 accordingly.

【0024】なお、上記した実施形態では、温度検出器
34によって検出された燐酸水溶液14の温度に基づい
て流量調節器42により流量制御弁38を制御して、純
水槽30から純水供給管36を通って溢流液受け部18
内へ供給される純水の流量を調節するようにしている
が、流量制御弁38に代えて開閉制御弁を使用して、調
節器によって単位時間内に開閉制御弁を開く時間(単位
時間内における純水の補充時間)を調節することによ
り、燐酸水溶液への単位時間当りの純水の補充量を調節
するようにしてもよい。
In the above-described embodiment, the flow rate control valve 38 is controlled by the flow rate regulator 42 based on the temperature of the phosphoric acid aqueous solution 14 detected by the temperature detector 34, and the pure water supply pipe 36 Overflow liquid receiving part 18 through
Although the flow rate of the pure water supplied into the inside is adjusted, an opening / closing control valve is used instead of the flow control valve 38, and a time during which the opening / closing control valve is opened within a unit time by the controller (the unit time , The amount of pure water replenished to the phosphoric acid aqueous solution per unit time may be adjusted.

【0025】[0025]

【発明の効果】請求項1に係る発明の基板の表面処理方
法によると、酸の水溶液からなる処理液を所定温度に保
持しかつ所定の酸濃度に保持して常に沸騰状態に保ちな
がら、基板の表面処理を行うことができ、このため、基
板の表面上に形成された2種類もしくはそれ以上の種類
の被膜のうちの所定の被膜を大きな選択比でもって選択
的にエッチングすることができる。
According to the method for treating the surface of a substrate according to the first aspect of the present invention, while maintaining a treatment solution comprising an aqueous solution of an acid at a predetermined temperature and at a predetermined acid concentration and always in a boiling state, Surface treatment can be performed, so that a predetermined coating of two or more types of coatings formed on the surface of the substrate can be selectively etched with a large selection ratio.

【0026】請求項2に係る発明の方法では、処理液中
へ基板を投入した時や処理液を補充した時のように処理
液の温度が瞬時に大きく低下した時に、処理液の温度を
速やかに回復させることができるので、基板の表面上に
形成された被膜のエッチングレートの低下を防ぐことが
できる。
In the method according to the second aspect of the present invention, when the temperature of the processing liquid is greatly reduced instantaneously, such as when the substrate is put into the processing liquid or when the processing liquid is replenished, the temperature of the processing liquid is rapidly increased. Therefore, a decrease in the etching rate of the film formed on the surface of the substrate can be prevented.

【0027】請求項3に係る発明の方法では、シリコン
酸化膜に対するシリコン窒化膜の選択比を大きくして、
基板の表面上に形成されたシリコン窒化膜を選択的にエ
ッチングすることができる。
According to the method of the present invention, the selectivity of the silicon nitride film to the silicon oxide film is increased.
The silicon nitride film formed on the surface of the substrate can be selectively etched.

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

【図1】この発明に係る基板の表面処理方法を実施する
のに使用される表面処理装置の概略構成の1例を示す模
式図である。
FIG. 1 is a schematic diagram showing an example of a schematic configuration of a surface treatment apparatus used to carry out a substrate surface treatment method according to the present invention.

【図2】この発明に係る基板の表面処理方法を実施した
ときの、処理槽内の燐酸水溶液の温度変化の状態の1例
を示す図である。
FIG. 2 is a diagram illustrating an example of a state of a temperature change of a phosphoric acid aqueous solution in a processing tank when a substrate surface treatment method according to the present invention is performed.

【図3】従来の表面処理装置の概略構成の1例を示す模
式図である。
FIG. 3 is a schematic view showing an example of a schematic configuration of a conventional surface treatment apparatus.

【符号の説明】[Explanation of symbols]

10 処理槽 12 処理槽底部の液導入口 14 燐酸水溶液 16 投込みヒータ 18 溢流液受け部 20 液循環用配管 22 循環ポンプ 24 インラインヒータ 26 フィルタ 28 純水 30 純水槽 32 定量ポンプ 34 温度検出器 36 純水供給管 38 流量制御弁 40 流量計 42 流量調節器 44 出力調節器 DESCRIPTION OF SYMBOLS 10 Processing tank 12 Liquid inlet at the bottom of processing tank 14 Phosphoric acid aqueous solution 16 Injection heater 18 Overflow liquid receiving part 20 Liquid circulation pipe 22 Circulation pump 24 In-line heater 26 Filter 28 Pure water 30 Pure water tank 32 Metering pump 34 Temperature detector 36 Pure water supply pipe 38 Flow control valve 40 Flow meter 42 Flow controller 44 Output controller

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 酸の水溶液からなる処理液をヒータで加
熱して処理液を沸騰状態に保ち、沸騰状態の処理液中に
基板を浸漬させて、基板の表面上に形成された2種類も
しくはそれ以上の種類の被膜のうちの所定の被膜を選択
的にエッチングする基板の表面処理方法において、 前記ヒータの出力を一定にして処理液に対し一定の熱量
を与えて処理液を常に沸騰状態に保つとともに、処理液
の温度を検出し、その検出温度に基づいて処理液の温度
が所定温度に保持されるように処理液への純水の補充量
を制御することを特徴とする基板の表面処理方法。
1. A treatment solution comprising an aqueous solution of an acid is heated by a heater to maintain the treatment solution in a boiling state, and the substrate is immersed in the boiling treatment solution to form two or more types formed on the surface of the substrate. In a surface treatment method for a substrate, which selectively etches a predetermined coating of coatings of a higher type, a constant amount of heat is applied to the processing liquid while the output of the heater is kept constant, so that the processing liquid is always brought into a boiling state. Maintaining the temperature of the processing solution, and controlling the replenishment amount of pure water to the processing solution based on the detected temperature so that the temperature of the processing solution is maintained at a predetermined temperature. Processing method.
【請求項2】 処理液中への基板の投入時点から所定時
間内だけ、および、処理液の補充時点から所定時間内だ
け、それぞれヒータの出力が最大にされる請求項1記載
の基板の表面処理方法。
2. The substrate surface according to claim 1, wherein the output of the heater is maximized only within a predetermined time from the time when the substrate is introduced into the processing liquid, and within a predetermined time from the time when the processing liquid is replenished. Processing method.
【請求項3】 処理液が燐酸水溶液であり、基板の表面
上に形成された被膜がシリコン酸化膜とシリコン窒化膜
とであって、シリコン窒化膜が選択的にエッチングされ
る請求項1または請求項2記載の基板の表面処理方法。
3. The processing liquid is a phosphoric acid aqueous solution, the coating formed on the surface of the substrate is a silicon oxide film and a silicon nitride film, and the silicon nitride film is selectively etched. Item 3. The method for treating a surface of a substrate according to Item 2.
JP32247797A 1997-11-07 1997-11-07 Surface treatment method for substrate Pending JPH11145107A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
JP32247797A JPH11145107A (en) 1997-11-07 1997-11-07 Surface treatment method for substrate

Publications (1)

Publication Number Publication Date
JPH11145107A true JPH11145107A (en) 1999-05-28

Family

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Country Link
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Cited By (5)

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Publication number Priority date Publication date Assignee Title
US7097784B2 (en) 2002-12-27 2006-08-29 Kabushiki Kaisha Toshiba Etching method and apparatus for semiconductor wafers
JP2008252122A (en) * 2008-06-16 2008-10-16 Dainippon Screen Mfg Co Ltd Substrate processing apparatus
JP2009231527A (en) * 2008-03-24 2009-10-08 Nec Electronics Corp Substrate processing method and substrate processing apparatus
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US20190080937A1 (en) * 2017-09-11 2019-03-14 Tokyo Electron Limited Substrate liquid processing apparatus, substrate liquid processing method and recording medium

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7097784B2 (en) 2002-12-27 2006-08-29 Kabushiki Kaisha Toshiba Etching method and apparatus for semiconductor wafers
JP2009231527A (en) * 2008-03-24 2009-10-08 Nec Electronics Corp Substrate processing method and substrate processing apparatus
JP2008252122A (en) * 2008-06-16 2008-10-16 Dainippon Screen Mfg Co Ltd Substrate processing apparatus
JP4628448B2 (en) * 2008-06-16 2011-02-09 大日本スクリーン製造株式会社 Substrate processing equipment
JP2013206946A (en) * 2012-03-27 2013-10-07 Dainippon Screen Mfg Co Ltd Substrate processing apparatus
US10520416B2 (en) 2012-03-27 2019-12-31 SCREEN Holdings Co., Ltd. Substrate treating method for a substrate treating apparatus that carries out etching treatment of substrates
US20190080937A1 (en) * 2017-09-11 2019-03-14 Tokyo Electron Limited Substrate liquid processing apparatus, substrate liquid processing method and recording medium

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