JP4708167B2 - Film forming apparatus and film forming method - Google Patents
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- JP4708167B2 JP4708167B2 JP2005333346A JP2005333346A JP4708167B2 JP 4708167 B2 JP4708167 B2 JP 4708167B2 JP 2005333346 A JP2005333346 A JP 2005333346A JP 2005333346 A JP2005333346 A JP 2005333346A JP 4708167 B2 JP4708167 B2 JP 4708167B2
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この発明は、成膜装置及び成膜方法に関し、特に金属酸化膜又は金属窒化膜を成膜する成膜装置及び成膜方法に関するものである。 The present invention relates to a film forming apparatus and a film forming method, and more particularly to a film forming apparatus and a film forming method for forming a metal oxide film or a metal nitride film.
近時、CVD(化学気相成長法、CVD法:Chemical Vapor Deposition)において、特許文献1に示すように、成膜室の内部に載置した基板に向かって、その上部に設けた噴射弁から成膜材料を液体状態のまま霧状にして射出するという新たな成膜方式(以下噴霧方式という)が開発されつつある。かかる噴霧方式よれば、気化器や配管等を加熱する必要がないため、装置の小型化や低コスト化を図ることができる。 Recently, in CVD (Chemical Vapor Deposition), as shown in Patent Document 1, from an injection valve provided on the top of a substrate placed inside a film forming chamber, A new film forming method (hereinafter referred to as a spraying method) is being developed in which a film forming material is sprayed in a liquid state in the form of a mist. According to such a spraying method, it is not necessary to heat a vaporizer, piping, etc., so that the size and cost of the apparatus can be reduced.
ところで、この噴霧方式おいては、膜品質を担保するために、噴射弁から噴出した霧状の液体成膜材料を、基板に到達するまでに確実に、かつできるだけ均一な状態で気化(ガス化)させる必要がある。 By the way, in this spraying method, in order to ensure film quality, the mist-like liquid film-forming material ejected from the injection valve is vaporized (gasified) reliably and as uniformly as possible before reaching the substrate. )
この要求に対し、単純には、エンジンなどに用いられている燃料噴射弁のように、噴射弁から液体成膜材料を均一な霧状にして広く噴出させればよいと考えがちであるが、実際には、そのような構成であると気化が不十分になり、膜品質が悪化する場合がある。エンジン用の燃料噴射弁の構造や考え方をそのまま採用することはできないのである。
そこで本発明者は、かかる不具合に鑑み、種々の実験を重ねて鋭意検討した結果、どのような噴霧形態がこの種の成膜装置に適しているのかを解明して初めて本発明に想到したものであり、その主たる所期課題とするところは、膜品質を担保でき、しかも装置の小型化や低コスト化を図ることができる噴霧式のCVD成膜装置等を提供することにある。 In view of such problems, the present inventor has conducted various experiments and intensively studied. As a result, the inventors have devised what type of spraying is suitable for this type of film forming apparatus and arrived at the present invention for the first time. The main intended problem is to provide a spray-type CVD film forming apparatus and the like that can guarantee film quality, and can reduce the size and cost of the apparatus.
すなわち本発明に係る成膜装置は、基板を内部に収容する成膜室と、その基板から所定距離離間させて配置され、成膜原料を前記成膜室内に液体状態で噴射する噴射弁と、を備えてなり、前記噴射弁に設けられた噴射孔の横断面形状が、短手方向にはほぼ一定寸法であるとともに、長手方向には入口から出口に近づくほど徐々に拡開し、出口近傍において少なくとも細長い帯状をなすように構成されていることを特徴とする。帯状とは、先端と終端とがあって閉じていない形状であれば良く、直線的に延びるものの他、部分円弧状に湾曲していたり、波状であったり、三角波状であったりするものも含む。 That is, a film forming apparatus according to the present invention includes a film forming chamber that houses a substrate therein, an injection valve that is disposed at a predetermined distance from the substrate, and injects a film forming material into the film forming chamber in a liquid state, The cross-sectional shape of the injection hole provided in the injection valve is substantially constant in the lateral direction, and gradually expands in the longitudinal direction from the inlet toward the outlet, and in the vicinity of the outlet It is comprised so that it may make at least an elongate strip shape. The band shape may be any shape that has a front end and a terminal end and is not closed, and includes a shape that extends linearly, a portion that is curved in a partial arc shape, a wave shape, or a triangular wave shape. .
このようなものであれば、成膜原料の、噴射弁から射出された直後の噴霧形状が、概略扇形の薄い膜状となるため、気化効率が可及的に向上し、気化のためのその他の特別な工夫(例えば成膜室を大きくして噴射弁と基板との離間距離を大きく設定するとか、成膜室内の圧力を特別に低く設定するとかいった工夫)をすることなく、基板に成膜原料が液体のまま到達することを無理なく防止でき、膜の品質を担保できる。 If it is such, since the spray shape of the film-forming raw material immediately after being injected from the injection valve becomes a substantially fan-shaped thin film shape, the vaporization efficiency is improved as much as possible, and other for vaporization Without special measures (such as making the film formation chamber larger and setting the separation distance between the injection valve and the substrate large, or setting the pressure in the film formation chamber to be particularly low). It is possible to easily prevent the film-forming raw material from reaching the liquid state, and to ensure the quality of the film.
また、本発明者が鋭意検討の結果見出した好ましい噴射孔に関するパラメータは以下の通りである。 Moreover, the parameter regarding the preferable injection hole which this inventor discovered as a result of earnest examination is as follows.
すなわち、前記噴射孔の横断面形状における短手方向の寸法は、約0.15mmから約0.20mmの間が好ましい。前記噴射孔の奥行き寸法は、約0.45mmから約1.4mmの間が好ましい。前記噴射孔の拡開角度は、約50°から約130°の間の角度が好ましい。前記噴射孔の仮想拡開中心点から、噴射孔の入口までの距離は、約0.4mmから約1mmの間が好ましい。前記噴射孔における奥行方向の寸法は、短手方向の寸法に対して約3倍から約7倍が好ましい。 That is, it is preferable that the dimension in the short direction in the cross-sectional shape of the injection hole is between about 0.15 mm and about 0.20 mm. The depth dimension of the injection hole is preferably between about 0.45 mm and about 1.4 mm. The expansion angle of the injection hole is preferably an angle between about 50 ° and about 130 °. The distance from the virtual expansion center point of the injection hole to the inlet of the injection hole is preferably between about 0.4 mm and about 1 mm. The dimension in the depth direction of the injection hole is preferably about 3 to about 7 times the dimension in the short direction.
噴射弁はピボットタイプのものが望ましく、その具体的態様としては、液体成膜原料が内部空間に充填され、先端部に前記噴射孔を貫通させてなるボディと、そのボディ内に進退可能に配置された弁体とを備えてなり、その弁体が、前記ボディにおける前記噴射孔より基端側内面に設けた弁座に着座又は当該弁座から離れることで、前記噴射孔とボディの内部空間とを開閉するものを挙げることができる。 The injection valve is preferably of a pivot type. As a specific aspect thereof, a liquid film forming raw material is filled in the internal space and the injection hole is penetrated through the tip, and the body is disposed so as to be able to advance and retreat in the body. The valve body is seated on or separated from the valve seat provided on the inner surface on the base end side from the injection hole in the body, so that the internal space of the injection hole and the body Can be mentioned.
このように本発明によれば、噴射弁から射出される成膜原料の噴霧形状が、概略扇形の薄い膜状となるため、気化効率が可及的に向上する。そしてその結果、基板に成膜原料が液体のまま到達することを、装置の大型化や複雑化を招来することなく防止でき、高品質な成膜が可能になる。 As described above, according to the present invention, the spraying shape of the film forming raw material injected from the injection valve becomes a substantially fan-shaped thin film shape, so that the vaporization efficiency is improved as much as possible. As a result, it is possible to prevent the film-forming raw material from reaching the substrate in a liquid state without causing an increase in size and complexity of the apparatus, and high-quality film formation is possible.
次に、本発明に係る成膜装置の一実施形態ついて図面を参照して説明する。
本実施形態に係る成膜装置1は、図1に示すように、基板2を内部に保持する成膜室3と、成膜原料を前記成膜室3内に液体のまま直接噴射する噴射弁4と、噴射弁4に液体成膜原料を供給する原料供給管5と、前記噴射弁4等を制御する制御装置11等を備えており、前記噴射弁4から噴霧射出された前記成膜原料が、途中で気化して加工対象である基板2上に堆積し、薄膜が形成されるように構成したものである。
Next, an embodiment of a film forming apparatus according to the present invention will be described with reference to the drawings.
As shown in FIG. 1, a film forming apparatus 1 according to this embodiment includes a film forming chamber 3 that holds a substrate 2 therein, and an injection valve that directly injects a film forming material into the film forming chamber 3 in a liquid state. 4, a raw material supply pipe 5 for supplying a liquid film forming raw material to the injection valve 4, a control device 11 for controlling the injection valve 4, and the like, and the film forming raw material sprayed from the injection valve 4 However, it is configured to vaporize in the middle and deposit on the substrate 2 to be processed to form a thin film.
本実施形態においては、基板2上にNb2O5膜を成膜すべく、その成膜原料として、有機ニオブ化合物であるペンタエトキシニオブ(PENb、Nb(OC2H5)5)を用いているが、このペンタエトキシニオブが単体では非常に蒸気圧が低く気化しにくいことから、これに低沸点有機化合物であるエタノールを所定比(ここでは例えば6:4、ただしmol比)で混合し、その混合溶液を噴射弁4に供給するようにしている。より具体的に説明すると、この混合溶液は、例えばステンレス製の容器6に保存されており、当該容器6に圧入された加圧ガス(N2あるいはArガス)により原料供給管5を通り噴射弁4を介して成膜室3の内部に供給されるように構成している。なお、成膜原料や低沸点有機化合物は上述したものに限られず、例えばペンタエトキシタンタル(Ta(OC2H5)5)とn−ペンタン(n-C5H12)との組み合わせなどでも構わない。 In the present embodiment, in order to form an Nb 2 O 5 film on the substrate 2, pentaethoxyniobium (PENb, Nb (OC 2 H 5 ) 5 ), which is an organic niobium compound, is used as the film forming raw material. However, since this pentaethoxyniobium alone has a very low vapor pressure and is difficult to vaporize, ethanol, which is a low-boiling organic compound, is mixed with this at a predetermined ratio (for example, 6: 4, however, mol ratio). The mixed solution is supplied to the injection valve 4. More specifically, this mixed solution is stored in, for example, a stainless steel container 6, and the injection valve passes through the raw material supply pipe 5 with the pressurized gas (N 2 or Ar gas) press-fitted into the container 6. 4 is configured to be supplied to the inside of the film forming chamber 3 via 4. Note that the raw materials for film formation and the low-boiling organic compounds are not limited to those described above, and for example, a combination of pentaethoxytantalum (Ta (OC 2 H 5 ) 5 ) and n-pentane (nC 5 H 12 ) may be used.
成膜室3は、図1に示すように、保持機構(図示しない)によって、加工対象となる基板2を保持収容するものであり、その内部収容空間は、成膜室3に噴射された混合溶液中のペンタエトキシニオブが気化するように内部圧力調節されている。つまり、その成膜室3内の圧力が、前記エタノールと混合する前のペンタエトキシニオブの飽和蒸気圧よりも大きく、かつエタノールとペンタエトキシニオブとの混合溶液の飽和蒸気圧よりも小さくなるように、例えば17〜100Pa程度に設定されている。この成膜室3には、さらに、基板2を加熱するための基板ヒータ7や、Nb2O5膜を充分に酸化させるための酸素(O2)ガスを供給する酸素供給管9が配設されている。この酸素供給管9は、マスフローコントローラ(MFC)10により酸素(O2)ガスの供給流量を制御されている。 As shown in FIG. 1, the film forming chamber 3 holds and accommodates the substrate 2 to be processed by a holding mechanism (not shown), and the internal accommodating space is a mixture injected into the film forming chamber 3. The internal pressure is adjusted so that pentaethoxyniobium in the solution is vaporized. That is, the pressure in the film forming chamber 3 is larger than the saturated vapor pressure of pentaethoxyniobium before mixing with ethanol and smaller than the saturated vapor pressure of the mixed solution of ethanol and pentaethoxyniobium. For example, it is set to about 17 to 100 Pa. The film forming chamber 3 is further provided with a substrate heater 7 for heating the substrate 2 and an oxygen supply pipe 9 for supplying oxygen (O 2 ) gas for sufficiently oxidizing the Nb 2 O 5 film. Has been. The oxygen supply pipe 9 is controlled by an oxygen (O 2 ) gas supply flow rate by a mass flow controller (MFC) 10.
噴射弁4は、図1に示すように、成膜原料を含んだ前記混合溶液を成膜室3内に液体状態(霧状)で直接噴射するものであり、成膜室3の上部に、基板2の堆積面と対向するように設けられている。 As shown in FIG. 1, the injection valve 4 directly injects the mixed solution containing the film forming raw material into the film forming chamber 3 in a liquid state (mist form). It is provided so as to face the deposition surface of the substrate 2.
詳述すれば、この噴射弁4は、図2〜図4に示すように、前記混合溶液が内部空間に充填されるものであって、先端部に前記噴射孔Hを貫通させてなるボディ41、そのボディ41内に進退可能に配置された弁体43、弁体43に互いに逆向きの軸方向に沿った進退力を付与する電磁コイル42及びバネ44を備えてなるピボットタイプのものである。 More specifically, as shown in FIGS. 2 to 4, the injection valve 4 is a body 41 in which the mixed solution is filled in an internal space, and the injection hole H is passed through the tip portion. The valve body 43 is disposed in the body 41 so as to be able to advance and retract, and is a pivot type that includes an electromagnetic coil 42 and a spring 44 that apply advancing and retracting forces along opposite axial directions to the valve body 43. .
ボディ41は、筒状のボディ本体41Aと、そのボディ本体41Aの先端に連続して設けられた噴射孔形成部41Bとからなり、ボディ本体41Aの先端部には内面が逆円錐形状に構成された弁座411が形成してある。噴射孔形成部41Bは、前記弁座411からさらに先端側に設けられた中空部分球状のものであり、その壁体に前記噴射孔Hが貫通させてある。 The body 41 includes a cylindrical body main body 41A and an injection hole forming portion 41B provided continuously at the tip of the body main body 41A. The inner surface of the tip of the body main body 41A is formed in an inverted conical shape. A valve seat 411 is formed. The injection hole forming portion 41B is a hollow spherical portion provided further on the distal end side from the valve seat 411, and the injection hole H is passed through the wall body.
前記弁体43は、前記弁座411に着座する閉止位置と、弁座411から離間する開成位置との間で、電磁コイル力とバネ力との大小関係によって、この噴射弁4の軸方向に進退移動するものである。より具体的には、前記制御装置11から閉止信号が出力されたときには、電磁コイル42が励磁されず、前記弁体43がバネ力で閉止位置に保持されて、前記噴射孔Hは、ボディ41の内部空間から遮断される。この状態では液体混合溶液(成膜原料)は噴出しない。また、前記制御装置11から開成信号が出力されると、電磁コイル42に電流が流れ、前記弁体43が開成位置に保持されて、前記噴射孔Hがボディ41の内部空間と連通する。この状態になって、当該噴射孔Hから液体混合溶液(成膜原料)が、成膜室3内に霧状に噴出し、減圧沸騰噴霧作用によって気化する。なお噴出圧は、0.1〜1MPa程度の範囲で可能であるが、ここでは例えば約0.4〜0.5MPaに設定している。 The valve body 43 is arranged in the axial direction of the injection valve 4 between the closed position where the valve body 411 is seated and the open position which is separated from the valve seat 411 due to the magnitude relationship between the electromagnetic coil force and the spring force. It moves forward and backward. More specifically, when a closing signal is output from the control device 11, the electromagnetic coil 42 is not excited, the valve element 43 is held in the closing position by a spring force, and the injection hole H is formed in the body 41. Is cut off from the interior space. In this state, the liquid mixed solution (film forming raw material) is not ejected. When the opening signal is output from the control device 11, a current flows through the electromagnetic coil 42, the valve body 43 is held in the opening position, and the injection hole H communicates with the internal space of the body 41. In this state, the liquid mixed solution (film forming raw material) is sprayed into the film forming chamber 3 in the form of a mist from the injection hole H, and is vaporized by the reduced-pressure boiling spray action. The ejection pressure can be in the range of about 0.1 to 1 MPa, but here it is set to about 0.4 to 0.5 MPa, for example.
制御装置11は、噴射弁4を周期的に開閉させて、前記液体混合溶液を前記成膜室3内に間欠的に供給するものであり、圧力計12を用いて原料供給管5内の液体混合溶液の圧力を観測しながら、所定量の液体混合溶液が噴出するよう、前記噴射弁4を制御する。 The control device 11 periodically opens and closes the injection valve 4 to intermittently supply the liquid mixed solution into the film forming chamber 3, and the liquid in the raw material supply pipe 5 using the pressure gauge 12. While observing the pressure of the mixed solution, the injection valve 4 is controlled so that a predetermined amount of the liquid mixed solution is ejected.
具体的な制御方法は、図6に示すように、液体混合溶液を成膜室3内に供給する時間である供給時間と液体混合溶液を前記成膜室3内に供給しない時間である供給停止時間とを周期的に繰り返すように噴射弁4を制御する。そして、この供給停止時間が、供給時間の約50倍以上となるようにし、本実施形態では、例えば供給時間を10[ms]、供給停止時間を990[ms]としている。供給時間は、例えば基板2の成膜対象面積、成膜室3の圧力、体積あるいは成膜原料(液体混合溶液)などに基づいて設定するようにしている。供給停止時間は、供給時間中に成膜室3内に供給され、基板2上に堆積した成膜原料の原子又は分子が泳動し、基板2上で生成された反応副生成物が蒸発するために必要な泳動・蒸発時間と同じかあるいはそれよりも長くなるように設定する。なお、供給時間中にさらに細かくON/OFFを繰り返す場合もある。 As shown in FIG. 6, the specific control method includes a supply time that is a time for supplying the liquid mixed solution into the film forming chamber 3 and a supply stop that is a time for not supplying the liquid mixed solution into the film forming chamber 3. The injection valve 4 is controlled so as to periodically repeat the time. The supply stop time is set to be about 50 times or more of the supply time. In this embodiment, for example, the supply time is 10 [ms] and the supply stop time is 990 [ms]. The supply time is set based on, for example, the film formation target area of the substrate 2, the pressure in the film formation chamber 3, the volume, the film formation raw material (liquid mixed solution), or the like. The supply stop time is supplied to the film formation chamber 3 during the supply time, and atoms or molecules of the film forming raw material deposited on the substrate 2 migrate and the reaction by-product generated on the substrate 2 evaporates. Set to be the same as or longer than the electrophoresis / evaporation time required for Note that ON / OFF may be repeated more finely during the supply time.
しかして、この実施形態では、図3、図4、図5に示すように、前記噴射孔Hの横断面形状について、短手方向寸法Bをほぼ一定にするとともに(図3参照、長手方向からみた噴射孔Hの縦断面図である)、長手方向には奥(入口)から出口に近づくほど徐々に拡開するようにし(図4参照、短手方向からみた噴射孔Hの縦断面図である)、出口近傍において少なくとも細長い直線帯状(図5参照、出口方向から見た噴射孔Hの形状である)となるように構成している。言い換えれば、この噴射孔Hが、スリット形状をなし、かつ側方から見て、出口に向かって広がる概略扇形(図4参照)をなすようにしている。 Thus, in this embodiment, as shown in FIGS. 3, 4, and 5, the transverse dimension B of the injection hole H is made substantially constant (see FIG. 3, from the longitudinal direction). It is a longitudinal sectional view of the injection hole H as viewed from the back, and gradually expands from the back (inlet) toward the outlet in the longitudinal direction (see FIG. 4, in the longitudinal sectional view of the injection hole H viewed from the short direction) In the vicinity of the outlet, it is configured to have at least an elongated straight belt shape (see FIG. 5, the shape of the injection hole H as seen from the outlet direction). In other words, the injection hole H is formed in a slit shape and has a general sector shape (see FIG. 4) that extends toward the outlet when viewed from the side.
噴射孔Hの各部の詳細寸法は以下の通りである。
すなわち、前記噴射孔Hの横断面形状における短手方向の寸法Bは、約0.15mmから約0.20mm、前記噴射孔Hの奥行き寸法Lは、約0.45mmから約1.4mm、前記噴射孔Hの拡開角度θは、約50°から約130°、前記噴射孔Hの仮想拡開中心点Cから噴射孔Hの入口までの距離Rが、約0.4mmから約1mm、前記噴射孔Hにおける奥行方向の寸法Lは、短手方向の寸法Bに対して約3倍から約7倍の間にそれぞれ設定している。
Detailed dimensions of each part of the injection hole H are as follows.
That is, the transverse dimension B of the cross-sectional shape of the injection hole H is about 0.15 mm to about 0.20 mm, and the depth dimension L of the injection hole H is about 0.45 mm to about 1.4 mm. The expansion angle θ of the injection hole H is about 50 ° to about 130 °, and the distance R from the virtual expansion center point C of the injection hole H to the inlet of the injection hole H is about 0.4 mm to about 1 mm. The depth direction dimension L in the injection hole H is set between about 3 times and about 7 times the dimension B in the short direction.
このように構成した噴射弁4による液体成膜材料の噴霧態様を、他の形態の噴射弁との等条件での比較において、図7、図8、図9に例示する。スワール式噴射弁であると、噴霧がスカートのように中空円錐状に液膜を形成し、かつ渦を巻きながら射出される(図8参照)。また等断面の細孔を多数設けてなる多孔式噴射弁であると、噴霧が広がりながらも柱状(中実円錐状)に射出される(図9参照)。一方、この実施形態にかかる噴射弁4であれば、噴霧が扇形の薄い液膜状に射出されている(図7参照)。 The spraying mode of the liquid film-forming material by the injection valve 4 configured in this way is illustrated in FIGS. 7, 8, and 9 in comparison with other types of injection valves under the same conditions. In the case of the swirl type injection valve, the spray forms a liquid film in a hollow conical shape like a skirt and is injected while swirling (see FIG. 8). Further, in the case of a porous injection valve provided with a large number of fine pores of equal cross section, the spray is injected in a columnar shape (solid conical shape) while spreading (see FIG. 9). On the other hand, in the case of the injection valve 4 according to this embodiment, the spray is injected into a fan-shaped thin liquid film (see FIG. 7).
そして、図7においては、噴霧が短い距離で気化しているのに対し、図8、図9では、気化するまでに長い距離を必要としているのが明らかにわかる。この原因は、噴霧が、中空、中実に拘わらず柱状となると、その柱状噴霧内部の局所的な圧力増大によって、噴霧内側での気化が阻害され、気化効率が落ちるからであると考えられる。 FIG. 7 clearly shows that the spray is vaporized at a short distance, whereas FIGS. 8 and 9 clearly require a long distance to vaporize. This is thought to be because if the spray is columnar regardless of whether it is hollow or solid, vaporization inside the spray is hindered due to a local increase in pressure inside the columnar spray, and the vaporization efficiency decreases.
これに対し、本実施形態による噴射弁4であれば、当該噴射弁4から射出された直後の成膜原料(混合溶液)の噴霧形状が、概略扇形の薄い膜状となるため、気化効率が可及的に向上する。そしてその結果、基板2に成膜原料が液体のまま到達することを無理なく防止でき、膜の品質を担保できる。 On the other hand, in the case of the injection valve 4 according to the present embodiment, the spraying shape of the film-forming raw material (mixed solution) immediately after being injected from the injection valve 4 becomes a substantially fan-shaped thin film shape. Improve as much as possible. As a result, it is possible to easily prevent the film forming raw material from reaching the substrate 2 in a liquid state, thereby ensuring the quality of the film.
なお、本発明は前記実施形態に限られるものではない。 The present invention is not limited to the above embodiment.
前述したように、噴霧が液柱状(中空も含む)にさえならなければよいのであるから、噴射孔の少なくとも出口形状は、先端と終端とがあって閉じていない帯状であれば良く、前記実施形態のように直線的に延びるものの他、部分円弧状に湾曲していたり、波状であったり、三角波状であったりしても構わない。また、ひとつの噴射弁に噴射孔を、例えば並列させるなどして複数設けてもよい。 As described above, since it is sufficient that the spray does not have to be in the form of a liquid column (including a hollow), at least the outlet shape of the injection hole may be a strip shape that has a front end and a terminal end and is not closed. In addition to the linearly extending shape as in the form, it may be curved in a partial arc shape, a wave shape, or a triangular wave shape. A plurality of injection holes may be provided in one injection valve, for example, in parallel.
また、前記実施形態では噴射孔を噴射弁の軸方向に対し、若干斜めに設定していた(図3参照)が、これを軸と平行にしてもよい。さらに、噴射孔形成部41Bは、中空部分球状に限られず、図10に示すように、内外面ともに角型形状でもよい。その場合は同図に示すように各寸法を規定する。その他に、外面が丸型で内面が角型、あるいはその逆などでもよく、噴射孔形成部41Bの形状に特に制限があるものではない。 Moreover, in the said embodiment, although the injection hole was set slightly diagonally with respect to the axial direction of an injection valve (refer FIG. 3), you may make this parallel to an axis | shaft. Further, the injection hole forming portion 41B is not limited to the hollow portion spherical shape, and may have a square shape on both the inner and outer surfaces as shown in FIG. In that case, each dimension is defined as shown in the figure. In addition, the outer surface may be round and the inner surface may be square, or vice versa, and the shape of the injection hole forming portion 41B is not particularly limited.
また、前記実施形態では、噴射弁を基板に対向するように、成膜室の上部に設けるようにしていたが、基板に対向するように、成膜室の下部に設けるようにしてもよいし、噴射弁を基板に対向するように、成膜室の側面に設けるようにしても良い。 In the above embodiment, the injection valve is provided in the upper part of the film forming chamber so as to face the substrate. However, the injection valve may be provided in the lower part of the film forming chamber so as to face the substrate. The injection valve may be provided on the side surface of the film forming chamber so as to face the substrate.
その他本発明はその趣旨を逸脱しない範囲で種々変形が可能である。 In addition, the present invention can be variously modified without departing from the gist thereof.
1・・・成膜装置
2・・・基板
3・・・成膜室
4・・・噴射弁
H・・・噴射孔
DESCRIPTION OF SYMBOLS 1 ... Film-forming apparatus 2 ... Board | substrate 3 ... Film-forming chamber 4 ... Injection valve
H ... Injection hole
Claims (10)
前記噴射弁に設けられた噴射孔の横断面形状が、短手方向にはほぼ一定寸法であるとともに、長手方向には入口から出口に近づくほど徐々に拡開し、出口近傍において少なくとも細長い帯状をなすように構成されている成膜装置。 A film forming chamber that accommodates the substrate therein, and an injection valve that is disposed at a predetermined distance from the substrate and injects a film forming material into the film forming chamber in a liquid state,
The cross-sectional shape of the injection hole provided in the injection valve has a substantially constant dimension in the short side direction, and gradually expands from the inlet to the outlet in the long side direction, and at least in the vicinity of the outlet, has an elongated strip shape. A film forming apparatus configured to be made.
前記成膜原料を噴射する噴射孔を有してなり、その噴射孔の横断面形状が、短手方向にはほぼ一定寸法であるとともに、長手方向には入口から出口に近づくほど徐々に拡開し、出口近傍において少なくとも細長い帯状をなすように構成されている成膜装置用噴射弁。 A film forming chamber that houses the substrate is provided at a predetermined distance from the substrate, and the film forming material is jetted in a liquid state toward the substrate.
It has injection holes for injecting the film forming raw material, and the cross-sectional shape of the injection holes is substantially constant in the short direction and gradually expands in the longitudinal direction as it approaches the outlet from the inlet. And a film forming apparatus injection valve configured to form at least an elongated strip in the vicinity of the outlet.
前記成膜原料を噴射する噴射孔を有してなり、その噴射孔の横断面形状が、短手方向にはほぼ一定寸法であるとともに、長手方向には入口から出口に近づくほど徐々に拡開し、出口近傍において少なくとも細長い帯状をなすように構成されている成膜装置用噴射弁。 It has injection holes for injecting the film forming raw material, and the cross-sectional shape of the injection holes is substantially constant in the short direction and gradually expands in the longitudinal direction as it approaches the outlet from the inlet. And a film forming apparatus injection valve configured to form at least an elongated strip in the vicinity of the outlet.
前記噴射弁が前記成膜原料を噴射する噴射孔を有してなり、その噴射孔の横断面形状が、短手方向にはほぼ一定寸法であるとともに、長手方向には入口から出口に近づくほど徐々に拡開し、出口近傍において少なくとも細長い帯状をなすように構成されている気化器。 The injection valve has an injection hole for injecting the film forming raw material, and the cross-sectional shape of the injection hole has a substantially constant dimension in the lateral direction, and the closer to the outlet from the inlet in the longitudinal direction, A carburetor configured to gradually expand and form at least an elongated strip in the vicinity of the outlet.
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| JP5051023B2 (en) * | 2008-06-23 | 2012-10-17 | スタンレー電気株式会社 | Film forming apparatus and semiconductor element manufacturing method |
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