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TW201819676A - Atomic layer deposition equipment and pumping speed controlling method therefor - Google Patents

Atomic layer deposition equipment and pumping speed controlling method therefor Download PDF

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Publication number
TW201819676A
TW201819676A TW105137536A TW105137536A TW201819676A TW 201819676 A TW201819676 A TW 201819676A TW 105137536 A TW105137536 A TW 105137536A TW 105137536 A TW105137536 A TW 105137536A TW 201819676 A TW201819676 A TW 201819676A
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Taiwan
Prior art keywords
gas
reaction
reaction chamber
load
pumping
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TW105137536A
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Chinese (zh)
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TWI608119B (en
Inventor
吳學憲
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矽碁科技股份有限公司
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Priority to TW105137536A priority Critical patent/TWI608119B/en
Priority to CN201611112747.1A priority patent/CN108070844B/en
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Publication of TW201819676A publication Critical patent/TW201819676A/en

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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45523Pulsed gas flow or change of composition over time
    • C23C16/45525Atomic layer deposition [ALD]
    • C23C16/45527Atomic layer deposition [ALD] characterized by the ALD cycle, e.g. different flows or temperatures during half-reactions, unusual pulsing sequence, use of precursor mixtures or auxiliary reactants or activations
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/52Controlling or regulating the coating process

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

The invention discloses a pumping speed controlling method for an atomic layer deposition equipment and an atomic layer deposition equipment using the pumping speed controlling method. The atomic layer deposition equipment includes a reaction chamber, a gas supply device, a pumping device, and a parallel line. The gas supply device is connected to the reaction chamber so as to selectively provide at least two reaction gases and at least one purge gas to the reaction chamber. The pumping device is connected to the reaction chamber so as to evacuate the reaction chamber. The parallel line connects the gas supply device and the pumping device and includes a parallel control valve. The gas supply device provides a loading gas through the parallel line to the pumping device. Thereby, opening or closing the parallel control valve can change the pumping loading to the pumping device, leading to a change in the pumping efficiency to the reaction chamber.

Description

原子層沉積設備及其抽氣速率控制方法Atomic layer deposition equipment and method for controlling pumping rate

本發明關於一種原子層沉積設備,尤指一種關於原子層沉積設備之抽氣速率控制方法。The present invention relates to an atomic layer deposition device, and more particularly, to a method for controlling a pumping rate of an atomic layer deposition device.

原子層沉積(atomic layer deposition, ALD)製程是使基板在兩種不同反應氣體(前驅物)環境下交替浸泡(soak),經反應後於其上形成單層膜(monolayer)。兩種不同反應氣體不能同時存在於反應室中,否則兩種反應氣體反應而產生大量顆粒狀汙染物,因此反應氣體的交替過程間要經過適當的清洩(purge)程序(例如以清洩氣體清洗反應室)。為提昇反應氣體的使用率,反應室的容積(volume)愈小愈好。此外,在浸泡狀態時關閉抽氣閥門可進一步提昇反應氣體使用率。然而,瞬間啟動的真空(抽氣)易使粉塵(particulates) (包含存在於反應室內的汙染物)揚起而破壞鍍膜品質,且於較小的反應室中,此問題將更形嚴重。對此問題,通常於浸泡狀態時,可對反應室保持抽氣,以使反應室內的氣體能保持一定程度流動狀態,進而抑制粉塵的揚起。此時,為避免反應氣體過度浪費,抽氣幫浦通常以較低的抽氣速率運作。但於清潔程序時,抽氣幫浦需增加抽氣速率以縮短清潔程序所耗時間。In the atomic layer deposition (ALD) process, the substrate is alternately soaked in two different reaction gas (precursor) environments, and a monolayer is formed thereon after the reaction. Two different reaction gases cannot exist in the reaction chamber at the same time, otherwise the two reaction gases react to produce a large amount of particulate pollutants, so the appropriate purge procedure (for example, to purge the gas) is required between the alternating processes of the reaction gases. Clean the reaction chamber). In order to increase the utilization rate of the reaction gas, the smaller the volume of the reaction chamber, the better. In addition, closing the suction valve during the immersion state can further increase the utilization rate of the reaction gas. However, the instantaneous vacuum (exhaust) easily raises the particulates (including the pollutants existing in the reaction chamber) and destroys the coating quality. In the smaller reaction chamber, this problem will become more serious. For this problem, usually in the immersion state, it is possible to keep the reaction chamber evacuated so that the gas in the reaction chamber can maintain a certain degree of flow state, thereby suppressing the rise of dust. At this time, in order to avoid excessive waste of reaction gas, the pump is usually operated at a lower pumping rate. However, during the cleaning process, the pump needs to increase the pumping rate to reduce the time taken by the cleaning process.

對此抽氣速率需求目前有以改變(或切換)氣體流路(例如使用特殊設計之進氣室或進氣網(Shower)或快速轉動孔狀輪盤)的方式實作者,但其反應室機構複雜,且切換動作均為機械式,速度慢,製程時間因而增加。另有以改變抽氣閥門之閥體設計(例如節流閥、蝴蝶閥)的方式實作者,但此閥體動作均為機械式,速度仍不夠快,且容易在閥體的組件之間累積粉塵,進而影響鍍膜品質。亦有以改變幫浦抽氣端(例如抽氣管路大小為可調變)的方式實作者,但其反應室機構設計相當複雜,且可能會影響其電漿阻抗,又其切換動作均為機械式,速度慢,容易於曲折處累積粉塵,進而影響鍍膜品質。還有以改變幫浦排氣端(exhaust)氣導以降低幫浦抽氣效率的方式實作,但此僅適用於渦輪分子(turbo molecular)幫浦,其他種類的幫浦則有油氣回流的疑慮。The demand for this pumping rate currently exists in the way of changing (or switching) the gas flow path (for example, using a specially designed air inlet chamber or air inlet (Shower) or quickly turning the hole-shaped wheel disc), but its reaction chamber The mechanism is complex, and the switching actions are all mechanical, the speed is slow, and the process time is increased. In addition, the author has changed the design of the valve body of the suction valve (such as a throttle valve and a butterfly valve), but the valve body is all mechanical, the speed is still not fast enough, and it is easy to accumulate between the components of the valve body Dust, which in turn affects coating quality. There are also authors who change the pumping end of the pump (for example, the size of the pumping line is adjustable), but the design of the reaction chamber mechanism is quite complicated, and may affect its plasma impedance, and its switching action is mechanical Type, slow speed, easy to accumulate dust in the twists and turns, and then affect the coating quality. It can also be implemented by changing the exhaust gas conductance of the pump to reduce the pumping efficiency, but this is only applicable to turbo molecular pumps. Other types of pumps have oil and gas return. doubt.

鑑於先前技術中的問題,本發明提供一種抽氣速率控制方法,用於一原子層沉積設備。該抽氣速率控制方法利用改變抽氣裝置的抽氣負載(loading),以達到改變該抽氣裝置對該反應室的抽氣速率的目的。In view of the problems in the prior art, the present invention provides a pumping rate control method for an atomic layer deposition apparatus. The pumping rate control method uses changing the pumping load of the pumping device to achieve the purpose of changing the pumping rate of the pumping device to the reaction chamber.

根據本發明之抽氣速率控制方法用於一原子層沉積設備,該原子層沉積設備包含一反應室、一供氣裝置、一抽氣裝置及一並聯管路,該供氣裝置連接至該反應室以選擇性提供該反應室至少二反應氣體及至少一清洩氣體,該抽氣裝置連接至該反應室以對該反應室抽氣,該並聯管路連接該供氣裝置及該抽氣裝置並包含一並聯控制閥門,該供氣裝置經由該並聯管路提供該抽氣裝置不與該至少二反應氣體反應之一負載氣體。該抽氣速率控制方法包含下列步驟:當該供氣裝置提供該反應室該至少二反應氣體其中之一時,打開該並聯控制閥門以使該抽氣裝置同時對該反應室及該並聯管路抽氣,降低對該反應室之抽氣速率;以及當該供氣裝置提供該反應室該至少一清洩氣體時,關閉該並聯控制閥門以使該抽氣裝置對該反應室抽氣但不對該並聯管路抽氣。藉此,該抽氣裝置對該反應室始終保持抽氣,可避免揚起粉塵,且於該反應室進行清洩程序時,該抽氣裝置對該反應室的抽氣,能以較大的抽氣速率進行,故該抽氣速率控制方法兼具維護鍍膜品質及縮短該反應室切換不同反應氣體的時間。The gas extraction rate control method according to the present invention is used in an atomic layer deposition device, which includes a reaction chamber, a gas supply device, a gas extraction device, and a parallel pipeline, and the gas supply device is connected to the reaction The chamber selectively provides at least two reaction gases and at least one purge gas of the reaction chamber. The pumping device is connected to the reaction chamber to pump the reaction chamber. The parallel pipeline is connected to the gas supply device and the pumping device. A parallel control valve is included, and the gas supply device provides a load gas through which the gas extraction device does not react with the at least two reaction gases via the parallel pipeline. The pumping rate control method includes the following steps: when the gas supply device provides the reaction chamber with one of the at least two reaction gases, opening the parallel control valve to cause the pumping device to pump the reaction chamber and the parallel pipeline at the same time Gas, reducing the pumping rate of the reaction chamber; and when the gas supply device provides the reaction chamber with the at least one purge gas, closing the parallel control valve so that the pumping device pumps the reaction chamber but does not Pump in parallel. Thereby, the gas extraction device can keep the gas extraction to the reaction chamber at all times, and dust can be prevented from being raised. When the reaction chamber is vented, the gas extraction device can evacuate the reaction chamber in a larger manner. The pumping rate is performed, so the pumping rate control method has both the maintenance of the coating quality and the shortening of the time for the reaction chamber to switch between different reaction gases.

本發明之另一目的在於提供一種原子層沉積設備,具有一並聯管路,透過此並聯管路可改變抽氣裝置的抽氣負載,以達到改變該抽氣裝置對該反應室的抽氣速率的目的。Another object of the present invention is to provide an atomic layer deposition device having a parallel pipeline through which the suction load of a suction device can be changed so as to change the suction speed of the reaction device by the suction device. the goal of.

根據本發明之原子層沉積設備包含一反應室、一抽氣裝置、一供氣裝置及一並聯管路。該抽氣裝置連接至該反應室。該供氣裝置包含至少三個氣源,用以提供一第一反應氣體、一第二反應氣體、一清洩氣體及一負載氣體,該供氣裝置連接至該反應室以選擇性提供該反應室該第一反應氣體、該第二反應氣體及該清洩氣體,該清洩氣體及該負載氣體均是不與該第一反應氣體及該第二反應氣體反應的。該並聯管路直接連接該抽氣裝置及用以提供該負載氣體之氣源,該並聯管路包含一並聯控制閥門,該供氣裝置經由該並聯管路提供該抽氣裝置該負載氣體。其中,當該供氣裝置提供該反應室該第一反應氣體或該第二反應氣體時,該並聯控制閥門打開以使該抽氣裝置同時對該反應室及該並聯管路抽氣,以及當該供氣裝置提供該反應室該至少一清洩氣體時,該並聯控制閥門關閉以使該抽氣裝置對該反應室抽氣但不對該並聯管路抽氣。藉此,該抽氣裝置對該反應室始終保持抽氣,可避免揚起粉塵,且於該反應室進行清洩程序時,該抽氣裝置對該反應室的抽氣,能以較大的抽氣速率進行,故該抽氣速率控制方法兼具維護鍍膜品質及縮短該反應室切換不同反應氣體的時間。The atomic layer deposition apparatus according to the present invention includes a reaction chamber, an air extraction device, a gas supply device, and a parallel pipeline. The suction device is connected to the reaction chamber. The gas supply device includes at least three gas sources for providing a first reaction gas, a second reaction gas, a purge gas, and a load gas. The gas supply device is connected to the reaction chamber to selectively provide the reaction. The first reaction gas, the second reaction gas, and the purge gas in the chamber are not reacted with the first reaction gas and the second reaction gas. The parallel pipeline is directly connected to the pumping device and an air source for providing the load gas. The parallel pipeline includes a parallel control valve, and the gas supply device provides the pumping device with the load gas through the parallel pipeline. Wherein, when the gas supply device provides the first reaction gas or the second reaction gas in the reaction chamber, the parallel control valve is opened so that the pumping device simultaneously evacuates the reaction chamber and the parallel pipeline, and when When the air supply device provides the reaction chamber with the at least one purge gas, the parallel control valve is closed to make the air extraction device evacuate the reaction chamber but not the parallel pipeline. Thereby, the gas extraction device can keep the gas extraction to the reaction chamber at all times, and dust can be prevented from being raised. When the reaction chamber is vented, the gas extraction device can evacuate the reaction chamber in a larger manner. The pumping rate is performed, so the pumping rate control method has both the maintenance of the coating quality and the shortening of the time for the reaction chamber to switch between different reaction gases.

相較於先前技術,根據本發明之原子層沉積設備及其抽氣速率控制方法係利用額外的抽氣空間(即該並聯管路)來調節該抽氣裝置的抽氣負載,該原子層沉積設備之其他構件無需配合修改,亦即其他構件結構上均可保持不變。因此,該原子層沉積設備經由結構上簡單的變化(即相對於慣用之原子層沉積設備增加該並聯管路),即可輕易地滿足於浸泡狀態時對該反應室保持抽氣以避免揚起粉塵及於清洩程序時對該反應室加速抽氣以縮短切換反應氣體的時間之要求。Compared with the prior art, the atomic layer deposition device and the pumping rate control method thereof according to the present invention utilize additional pumping space (ie, the parallel pipeline) to adjust the pumping load of the pumping device. The atomic layer deposition The other components of the equipment do not need to be modified, that is, the other components can remain unchanged in structure. Therefore, the atomic layer deposition equipment can be easily satisfied with maintaining the air extraction of the reaction chamber to avoid lifting when it is immersed through a simple structural change (that is, adding the parallel pipeline relative to the conventional atomic layer deposition equipment). Dust and accelerated pumping of the reaction chamber during the purge procedure to reduce the time required to switch the reaction gas.

關於本發明之優點與精神可以藉由以下的發明詳述及所附圖式得到進一步的瞭解。The advantages and spirit of the present invention can be further understood through the following detailed description of the invention and the accompanying drawings.

請參閱圖1。根據本發明之一實施例之一原子層沉積設備1包含一反應室10、一供氣裝置12、一抽氣裝置14、一並聯管路16及一控制系統(未顯示於圖中)。抽氣裝置14連接至反應室10。供氣裝置12包含一第一氣源122、一第二氣源124、一第三氣源126及一第四氣源127,第一氣源122用以提供一第一反應氣體,第二氣源124用以提供一第二反應氣體,第三氣源126用以提供一清洩氣體,第四氣源127用以提供一負載氣體。供氣裝置12連接至反應室10以選擇性提供反應室10該第一反應氣體、該第二反應氣體及該清洩氣體,該清洩氣體及該負載氣體均是不與該第一反應氣體及該第二反應氣體反應的;於實作上,該清洩氣體及該負載氣體可為惰性氣體或氮氣,但本發明不以此為限;例如其他不與反應室10內的反應氣體(即該第一反應氣體及該第二反應氣體)反應的氣體。並聯管路16直接連接抽氣裝置14及用以提供該負載氣體之第四氣源127並包含一並聯控制閥門162,供氣裝置12經由並聯管路16提供抽氣裝置14該負載氣體。See Figure 1. According to an embodiment of the present invention, an atomic layer deposition apparatus 1 includes a reaction chamber 10, a gas supply device 12, a suction device 14, a parallel pipeline 16, and a control system (not shown in the figure). A suction device 14 is connected to the reaction chamber 10. The gas supply device 12 includes a first gas source 122, a second gas source 124, a third gas source 126, and a fourth gas source 127. The first gas source 122 is used to provide a first reaction gas and a second gas source. The source 124 is used to provide a second reaction gas, the third gas source 126 is used to provide a purge gas, and the fourth gas source 127 is used to provide a load gas. The gas supply device 12 is connected to the reaction chamber 10 to selectively provide the first reaction gas, the second reaction gas, and the purge gas in the reaction chamber 10, and the purge gas and the load gas are not related to the first reaction gas. And the second reaction gas; in practice, the purge gas and the load gas may be inert gas or nitrogen, but the present invention is not limited thereto; for example, other reaction gases that do not react with the reaction chamber 10 ( That is, the first reaction gas and the second reaction gas) react. The parallel pipeline 16 is directly connected to the extraction device 14 and a fourth gas source 127 for providing the load gas, and includes a parallel control valve 162. The gas supply device 12 provides the extraction device 14 with the load gas through the parallel pipeline 16.

具體來說,於本實施例中,供氣裝置12包含一第一連接管路128、一第二連接管路130、一第一旁通管路132及一第二旁通管路134。第一連接管路128連接至反應室10且經由一閥門V1a連接至第一氣源122,第三氣源126經由一閥門V3a連接至第一連接管路128;第二連接管路130連接至反應室10且經由一閥門V2a連接至第二氣源124,第三氣源126經由一閥門V3b連接至第二連接管路130;第一旁通管路132連接至抽氣裝置14且經由閥門V1b連接至第一氣源122;第二旁通管路134連接至抽氣裝置14且經由閥門V2b連接至第二氣源124。並聯管路16連接至抽氣裝置14且經由閥門V4連接至第四氣源127。並聯管路16獨立於第一連接管路128、第二連接管路130、第一旁通管路132及第二旁通管路134,故並聯管路16不會有該第一反應氣體及該第二反應氣體流通。抽氣裝置14經由一抽氣閥門142連接至反應室10。該控制系統與電連接反應室10、供氣裝置12、抽氣裝置14及各閥門V1a、V1b、V2a、V2b、V3a、V3b、V4、142、162電連接,以控制原子層沉積設備1的運作。抽氣裝置14經由其排氣氣導將氣體排出。於實作上,原子層沉積設備1可由一般原子層沉積設備加上並聯管路16實作,故關於原子層沉積設備1之其他說明,可參酌一般原子層沉積設備,不另贅述,例如抽氣裝置14使用一般抽氣幫浦。另外,於實作上,閥門V1a、V2a、V3a、V3b、162均得以膜片閥實作,以能快速作動。Specifically, in this embodiment, the gas supply device 12 includes a first connection pipeline 128, a second connection pipeline 130, a first bypass pipeline 132, and a second bypass pipeline 134. The first connection line 128 is connected to the reaction chamber 10 and is connected to the first gas source 122 through a valve V1a, and the third gas source 126 is connected to the first connection line 128 through a valve V3a; the second connection line 130 is connected to The reaction chamber 10 is connected to the second air source 124 via a valve V2a, and the third air source 126 is connected to the second connection pipe 130 via a valve V3b; the first bypass line 132 is connected to the suction device 14 and via a valve V1b is connected to the first air source 122; the second bypass line 134 is connected to the air extraction device 14 and is connected to the second air source 124 via the valve V2b. The parallel line 16 is connected to the air extraction device 14 and is connected to the fourth air source 127 via the valve V4. The parallel pipeline 16 is independent of the first connection pipeline 128, the second connection pipeline 130, the first bypass pipeline 132, and the second bypass pipeline 134, so the parallel pipeline 16 will not have the first reaction gas and This second reaction gas circulates. The suction device 14 is connected to the reaction chamber 10 via a suction valve 142. The control system is electrically connected to the reaction chamber 10, the gas supply device 12, the air extraction device 14 and the valves V1a, V1b, V2a, V2b, V3a, V3b, V4, 142, 162 to control the atomic layer deposition equipment 1 Operation. The air extraction device 14 discharges gas via its exhaust air guide. In practice, the atomic layer deposition equipment 1 may be implemented by a general atomic layer deposition equipment and a parallel pipeline 16. Therefore, for other descriptions of the atomic layer deposition equipment 1, reference may be made to the general atomic layer deposition equipment without further description, such as pumping. The air device 14 uses a general suction pump. In addition, in practice, the valves V1a, V2a, V3a, V3b, and 162 are all implemented as diaphragm valves to enable fast operation.

於原子層沉積設備1運作時,當供氣裝置12順序交替提供反應室10該第一反應氣體或該第二反應氣體以於設置於反應室10內之一基板W上形成鍍膜時(亦即反應室10處於浸泡狀態),該控制系統打開並聯控制閥門162以使抽氣裝置14同時對反應室10及並聯管路16抽氣。換言之,此時抽氣裝置14的抽氣負載包含反應室10及並聯管路16(即其內形成的空間,邏輯上得以一負載空間16a表示,如圖1中虛線框所示者);從另一方面而言,此時抽氣裝置14持續不斷地抽取反應室10內的氣體(即該第一反應氣體或該第二反應氣體)並經由並聯管路16抽取該負載氣體。因此,此時反應室10的抽氣速率較低。此外,當供氣裝置12提供反應室10該清洩氣體用於清洩反應室10內的反應氣體(即該第一反應氣體或該第二反應氣體)時,該控制系統關閉並聯控制閥門162以使抽氣裝置14對反應室10抽氣但不對並聯管路16抽氣。換言之,此時抽氣裝置14的抽氣負載不包含並聯管路16,故反應室10可獲得較高的抽氣速率,有利於反應室10內反應氣體的切換作業。When the atomic layer deposition equipment 1 is operating, when the gas supply device 12 sequentially supplies the reaction chamber 10 with the first reaction gas or the second reaction gas to form a coating film on a substrate W provided in the reaction chamber 10 (that is, The reaction chamber 10 is in a soaking state), and the control system opens the parallel control valve 162 so that the air extraction device 14 simultaneously evacuates the reaction chamber 10 and the parallel pipeline 16. In other words, the extraction load of the extraction device 14 at this time includes the reaction chamber 10 and the parallel pipeline 16 (that is, the space formed therein is logically represented by a load space 16a, as shown by the dashed box in FIG. 1); On the other hand, at this time, the gas extraction device 14 continuously extracts the gas (that is, the first reaction gas or the second reaction gas) in the reaction chamber 10 and extracts the load gas through the parallel pipe 16. Therefore, the pumping rate of the reaction chamber 10 is low at this time. In addition, when the gas supply device 12 provides the reaction chamber 10 and the purge gas is used to purge the reaction gas in the reaction chamber 10 (that is, the first reaction gas or the second reaction gas), the control system closes the parallel control valve 162 This allows the suction device 14 to evacuate the reaction chamber 10 but not the parallel line 16. In other words, at this time, the pumping load of the pumping device 14 does not include the parallel pipeline 16, so the reaction chamber 10 can obtain a higher pumping rate, which is beneficial to the switching operation of the reaction gas in the reaction chamber 10.

於本實施例中,原子層沉積設備1於鍍膜沉積運作時,抽氣閥門142保持開啟狀態,抽氣裝置14對反應室10始終保持抽氣,此可避免揚起粉塵,且於反應室10進行清洩程序時,抽氣裝置14對反應室10的抽氣,能以較大的抽氣速率進行,故原子層沉積設備1採用之抽氣速率控制方法兼具維護鍍膜品質及縮短反應室10切換不同反應氣體的時間。另外,於實作上,並聯管路16可實體上包含一負載腔體164(如圖2所示),用以容置該負載氣體,並聯控制閥門162位於負載腔體164及抽氣裝置14之間。因此,當並聯控制閥門162打開時,抽氣裝置14對負載腔體164抽氣,亦對並聯管路16管路內的空間(即前述負載空間16a);當並聯控制閥門162關閉時,抽氣裝置14不對負載腔體164抽氣。故負載腔體164增加抽氣裝置14的抽氣負載,透過控制負載腔體164的容積,有助於控制抽氣裝置14對反應室10的抽氣速率。例如當負載腔體164與反應室10體積相同時,大體上,反應室10處於浸泡狀態時的抽氣速率約為清洩程序實施時的一半;於實作上,負載腔體164容積為反應室10容積的1/5到5倍,但本發明不以此為限。In this embodiment, when the atomic layer deposition device 1 is in the operation of coating deposition, the extraction valve 142 is kept open, and the extraction device 14 always keeps the extraction of the reaction chamber 10, which can avoid raising dust, and the reaction chamber 10 When carrying out the purge procedure, the evacuation of the reaction chamber 10 by the evacuation device 14 can be performed at a relatively large evacuation rate, so the evacuation rate control method adopted by the atomic layer deposition equipment 1 has both the maintenance of the coating quality and the shortening of the reaction chamber. 10 Time to switch between different reaction gases. In addition, in practice, the parallel pipeline 16 may physically include a load cavity 164 (as shown in FIG. 2) for containing the load gas, and the parallel control valve 162 is located in the load cavity 164 and the air extraction device 14. between. Therefore, when the parallel control valve 162 is opened, the suction device 14 evacuates the load cavity 164 and also the space in the parallel pipeline 16 (ie, the aforementioned load space 16a); when the parallel control valve 162 is closed, the pump The air device 14 does not evacuate the load cavity 164. Therefore, the load chamber 164 increases the pumping load of the pumping device 14. By controlling the volume of the load chamber 164, it is helpful to control the pumping rate of the pumping device 14 to the reaction chamber 10. For example, when the load chamber 164 has the same volume as the reaction chamber 10, generally, the pumping rate of the reaction chamber 10 when it is in the soaking state is about half that when the purge procedure is performed; in practice, the volume of the load chamber 164 is the reaction The volume of the chamber 10 is 1/5 to 5 times, but the present invention is not limited to this.

請併參閱圖3。圖3為根據本發明之一實施例之一抽氣速率控制方法之流程圖。於本實施例中,該抽氣速率控制方法實施於如前述之原子層沉積設備1(圖1或圖2所示者),原子層沉積設備1之相關說明如前文所述,不再贅述。原子層沉積設備1於運作時,閥門142、V4保持開啟,抽氣裝置14保持抽氣狀態,故閥門142、V4可使用作動速度較慢的閥門,但本發明不以此為限;此外,閥門V1b、V2b保持關閉。閥門V1a、V2a、V3a、V3b初始為關閉狀態,原子層沉積設備1依該抽氣速率控制方法進行抽氣控制。如圖3所示,該抽氣速率控制方法對反應室10抽真空至一預期背景壓力,如步驟S110所示;接著,打開並聯控制閥門162以降低反應室10的抽氣速率,並使該第一反應氣體進入反應室10,例如保持閥門V2a、V3a、V3b關閉,打開閥門V1a使得該第一反應氣體能經由第一連接管路128進入反應室10,以使反應室10能處於該第一反應氣體浸泡狀態,如步驟S120所示。See also Figure 3. FIG. 3 is a flowchart of a method for controlling an extraction rate according to an embodiment of the present invention. In this embodiment, the pumping rate control method is implemented in the aforementioned atomic layer deposition apparatus 1 (shown in FIG. 1 or FIG. 2), and the related description of the atomic layer deposition apparatus 1 is as described above, and will not be described again. When the atomic layer deposition equipment 1 is in operation, the valves 142 and V4 are kept open and the suction device 14 is kept in the suction state. Therefore, the valves 142 and V4 can be used as valves with a slower moving speed, but the present invention is not limited thereto; moreover, The valves V1b, V2b remain closed. The valves V1a, V2a, V3a, and V3b are initially closed, and the atomic layer deposition device 1 performs pumping control according to the pumping rate control method. As shown in FIG. 3, the pumping rate control method evacuates the reaction chamber 10 to a desired background pressure, as shown in step S110; then, the parallel control valve 162 is opened to reduce the pumping rate of the reaction chamber 10 and make the The first reaction gas enters the reaction chamber 10, for example, the valves V2a, V3a, and V3b are kept closed, and the valve V1a is opened so that the first reaction gas can enter the reaction chamber 10 through the first connection pipe 128, so that the reaction chamber 10 can be at the first A state of reaction gas soaking, as shown in step S120.

於該第一反應氣體與基板W(包含其上之膜層)反應完畢後,該抽氣速率控制方法關閉閥門V1a使得該第一反應氣體停止經由第一連接管路128進入反應室10,關閉並聯控制閥門162以提高抽氣裝置14對反應室10的抽氣速率,並使該清洩氣體進入反應室10,例如保持閥門V3b關閉,打開閥門V3a使得該清洩氣體能經由第一連接管路128進入反應室10,以清潔反應室10,如步驟S130所示。After the reaction of the first reaction gas with the substrate W (including the film layer thereon) is completed, the pumping rate control method closes the valve V1a so that the first reaction gas stops entering the reaction chamber 10 through the first connection pipe 128 and is closed. Control valve 162 in parallel to increase the pumping rate of pumping device 14 to reaction chamber 10 and allow the purge gas to enter reaction chamber 10, for example, keep valve V3b closed and open valve V3a so that the purge gas can pass through the first connection line 128 enters the reaction chamber 10 to clean the reaction chamber 10, as shown in step S130.

於反應室10清潔完畢後,該抽氣速率控制方法關閉閥門V3a使得該清洩氣體停止經由第一連接管路128進入反應室10,打開並聯控制閥門162以降低反應室10的抽氣速率,並使該第二反應氣體進入反應室10,例如保持閥門V1a、V3a、V3b關閉,打開閥門V2a使得該第二反應氣體能經由第二連接管路130進入反應室10,以使反應室10能處於該第二反應氣體浸泡狀態,如步驟S140所示。After the reaction chamber 10 is cleaned, the pumping rate control method closes the valve V3a so that the purge gas stops entering the reaction chamber 10 via the first connection line 128, and the parallel control valve 162 is opened to reduce the pumping rate of the reaction chamber 10. The second reaction gas is allowed to enter the reaction chamber 10, for example, the valves V1a, V3a, and V3b are kept closed, and the valve V2a is opened so that the second reaction gas can enter the reaction chamber 10 through the second connection pipe 130 so that the reaction chamber 10 can The second reaction gas is soaked, as shown in step S140.

於該第二反應氣體與基板W(包含其上之膜層)反應完畢後,該抽氣速率控制方法關閉閥門V2a使得該第二反應氣體停止經由第二連接管路130進入反應室10,關閉並聯控制閥門162以提高抽氣裝置14對反應室10的抽氣速率,並使該清洩氣體進入反應室10,例如保持閥門V3a關閉,打開閥門V3b使得該清洩氣體能經由第二連接管路130進入反應室10,以清潔反應室10,如步驟S150所示。After the reaction of the second reaction gas with the substrate W (including the film layer thereon) is completed, the pumping rate control method closes the valve V2a so that the second reaction gas stops entering the reaction chamber 10 through the second connection pipe 130 and is closed. Control valve 162 in parallel to increase the pumping rate of pumping device 14 to reaction chamber 10 and allow the purge gas to enter reaction chamber 10, for example, keep valve V3a closed and open valve V3b so that the purge gas can pass through the second connection line 130 enters the reaction chamber 10 to clean the reaction chamber 10, as shown in step S150.

於反應室10清潔完畢後,即完成一次基板W上的鍍膜沉積。接著,該抽氣速率控制方法判斷基板W上的鍍膜是否達預定厚度,如步驟S160所示。若判斷尚未達到預定厚度,該流程回到步驟S120,並重覆步驟S120~S150;若判斷已達到預定厚度,則結束沉積作業。接著,該抽氣速率控制方法對反應室10充氣,如步驟S170所示;例如關閉抽氣閥門142,再透過打開閥門V3a、V3b以該清洩氣體或以其他氣體(經由現有管路或另行配合設置的管路)對反應室10充氣。充完氣後,即可自反應室10取出鍍完膜的基板W。After the reaction chamber 10 is cleaned, the plating film deposition on the substrate W is completed once. Next, the pumping rate control method determines whether the plating film on the substrate W has a predetermined thickness, as shown in step S160. If it is determined that the predetermined thickness has not been reached, the process returns to step S120 and repeats steps S120 to S150; if it is determined that the predetermined thickness has been reached, the deposition operation is ended. Next, the pumping rate control method inflates the reaction chamber 10, as shown in step S170; for example, the pumping valve 142 is closed, and then the valves V3a, V3b are opened by the purge gas or other gas (via the existing pipeline or otherwise) Cooperatingly provided pipelines) aerate the reaction chamber 10. After filling the gas, the coated substrate W can be taken out from the reaction chamber 10.

補充說明的是,前述實施例係基於兩種反應氣體,但本發明不以此為限;於實作上,本技術領域中具有通常知識基於前述說明可推得以更多種反應氣體形成鍍膜之原子層沉積設備及其抽氣速率控制方法,不待贅述。此外,於前述實施例中,使用相同的清洩氣體來清除反應室10內的氣體(包含該第一反應氣體及該第二反應氣體),但本發明不以此為限。於實作上,配合不同的反應氣體可使用不同的清洩氣體,而該負載氣體可與其中一種清洩氣體相同,或是以其他的氣體實作。此外,於前述實施例中,該負載氣體與該清洩氣體分別由第三氣源126及第四氣源127提供,故該負載氣體與該清洩氣體可為不同的氣體。於實作上,該負載氣體與該清洩氣體亦可為相同的氣體,此時可省略第四氣源127而由第三氣源126(或謂該第三氣源與該第四氣源合併)同時提供該負載氣體與該清洩氣體,如圖4所示。 以上所述僅為本發明之較佳實施例,凡依本發明申請專利範圍所做之均等變化與修飾,皆應屬本發明之涵蓋範圍。It is added that the foregoing embodiments are based on two types of reaction gases, but the present invention is not limited thereto. In practice, there is general knowledge in the technical field based on the foregoing description, and it is possible to infer more types of reaction gases to form a coating film. The atomic layer deposition equipment and its pumping rate control method need not be described in detail. In addition, in the foregoing embodiment, the same purge gas is used to purge the gas in the reaction chamber 10 (including the first reaction gas and the second reaction gas), but the present invention is not limited thereto. In practice, different purge gases can be used with different reaction gases, and the load gas can be the same as one of the purge gases, or can be implemented with other gases. In addition, in the foregoing embodiment, the load gas and the purge gas are provided by the third gas source 126 and the fourth gas source 127, respectively, so the load gas and the purge gas may be different gases. In practice, the load gas and the purge gas can also be the same gas. In this case, the fourth gas source 127 can be omitted and the third gas source 126 (or the third gas source and the fourth gas source) can be omitted. (Merge) Provide the load gas and the purge gas at the same time, as shown in FIG. 4. The above description is only a preferred embodiment of the present invention, and all equivalent changes and modifications made in accordance with the scope of patent application of the present invention shall fall within the scope of the present invention.

1‧‧‧原子層沉積設備1‧‧‧ Atomic Layer Deposition Equipment

10‧‧‧反應室10‧‧‧ Reaction Room

12‧‧‧供氣裝置12‧‧‧Air supply device

122‧‧‧第一氣源122‧‧‧ the first gas source

124‧‧‧第二氣源124‧‧‧Second gas source

126‧‧‧第三氣源126‧‧‧Third gas source

127‧‧‧第四氣源127‧‧‧Fourth gas source

128‧‧‧第一連接管路128‧‧‧first connection line

130‧‧‧第二連接管路130‧‧‧Second connection line

132‧‧‧第一旁通管路132‧‧‧The first bypass line

134‧‧‧第二旁通管路134‧‧‧Second bypass line

14‧‧‧抽氣裝置14‧‧‧Exhaust device

142‧‧‧抽氣閥門142‧‧‧Exhaust valve

16‧‧‧並聯管路16‧‧‧ parallel pipeline

16a‧‧‧負載空間16a‧‧‧Load space

162‧‧‧並聯控制閥門162‧‧‧parallel control valve

164‧‧‧負載腔體164‧‧‧load cavity

V1a、V1b、V2a、V2b、V3a、V3b、V4‧‧‧閥門V1a, V1b, V2a, V2b, V3a, V3b, V4‧‧‧ valves

W‧‧‧基板W‧‧‧ substrate

S110~S170‧‧‧實施步驟S110 ~ S170‧‧‧Implementation steps

圖1為根據本發明之一實施例之一原子層沉積設備之配置示意圖。 圖2為根據另一實施例之一原子層沉積設備之配置示意圖。 圖3為根據本發明之一實施例之一抽氣速率控制方法之流程圖。 圖4為根據另一實施例之一原子層沉積設備之配置示意圖。FIG. 1 is a schematic configuration diagram of an atomic layer deposition apparatus according to an embodiment of the present invention. FIG. 2 is a schematic configuration diagram of an atomic layer deposition apparatus according to another embodiment. FIG. 3 is a flowchart of a method for controlling an extraction rate according to an embodiment of the present invention. FIG. 4 is a schematic configuration diagram of an atomic layer deposition apparatus according to another embodiment.

Claims (12)

一種抽氣速率控制方法,用於一原子層沉積設備,該原子層沉積設備包含一反應室、一供氣裝置、一抽氣裝置及一並聯管路,該供氣裝置連接至該反應室以選擇性提供該反應室至少二反應氣體及至少一清洩氣體,該抽氣裝置連接至該反應室以對該反應室抽氣,該並聯管路連接該供氣裝置及該抽氣裝置並包含一並聯控制閥門,該供氣裝置經由該並聯管路提供該抽氣裝置不與該至少二反應氣體反應之一負載氣體,該抽氣速率控制方法包含下列步驟: 當該供氣裝置提供該反應室該至少二反應氣體其中之一時,打開該並聯控制閥門以使該抽氣裝置同時對該反應室及該並聯管路抽氣;以及 當該供氣裝置提供該反應室該至少一清洩氣體時,關閉該並聯控制閥門以使該抽氣裝置對該反應室抽氣但不對該並聯管路抽氣。An extraction rate control method for an atomic layer deposition device. The atomic layer deposition device includes a reaction chamber, a gas supply device, a gas extraction device, and a parallel pipeline. The gas supply device is connected to the reaction chamber to Selectively providing at least two reaction gases and at least one purge gas in the reaction chamber, the pumping device is connected to the reaction chamber to pump the reaction chamber, and the parallel pipeline is connected to the gas supply device and the pumping device and includes A parallel control valve, the gas supply device provides a load gas through which the gas extraction device does not react with the at least two reaction gases via the parallel pipeline, and the gas extraction rate control method includes the following steps: when the gas supply device provides the reaction Opening one of the at least two reaction gases in the chamber, opening the parallel control valve so that the pumping device simultaneously pumps the reaction chamber and the parallel pipeline; and when the gas supply device provides the reaction chamber with the at least one purge gas At this time, the parallel control valve is closed so that the pumping device pumps the reaction chamber but does not pump the parallel pipeline. 如請求項1所述之抽氣速率控制方法,其中該並聯管路包含一負載腔體,用以容置該負載氣體,該並聯控制閥門位於該負載腔體及該抽氣裝置之間,當該並聯控制閥門打開時,該抽氣裝置對該負載腔體抽氣,且當該並聯控制閥門關閉時,該抽氣裝置不對該負載腔體抽氣。The pumping rate control method according to claim 1, wherein the parallel pipeline includes a load chamber for containing the load gas, and the parallel control valve is located between the load chamber and the pumping device. When the parallel control valve is opened, the pumping device evacuates the load cavity, and when the parallel control valve is closed, the pumping device does not evacuate the load cavity. 如請求項2所述之抽氣速率控制方法,其中該負載腔體容積為該反應室容積的1/5到5倍。The pumping rate control method according to claim 2, wherein the volume of the load chamber is 1/5 to 5 times the volume of the reaction chamber. 如請求項1所述之抽氣速率控制方法,其中該清洩氣體為氮氣或惰性氣體。The pumping rate control method according to claim 1, wherein the purge gas is nitrogen or an inert gas. 如請求項1所述之抽氣速率控制方法,其中該負載氣體為氮氣或惰性氣體。The pumping rate control method according to claim 1, wherein the load gas is nitrogen or an inert gas. 如請求項1所述之抽氣速率控制方法,其中該清洩氣體及該負載氣體均是不與該第一反應氣體及該第二反應氣體反應的。The pumping rate control method according to claim 1, wherein the purge gas and the load gas do not react with the first reaction gas and the second reaction gas. 一種原子層沉積設備,包含: 一反應室; 一抽氣裝置,連接至該反應室; 一供氣裝置,包含至少三個氣源,用以提供一第一反應氣體、一第二反應氣體、一清洩氣體及一負載氣體,該供氣裝置連接至該反應室以選擇性提供該反應室該第一反應氣體、該第二反應氣體及該清洩氣體,該清洩氣體及該負載氣體均是不與該第一反應氣體及該第二反應氣體反應的;以及 一並聯管路,直接連接該抽氣裝置及用以提供該負載氣體之氣源,該並聯管路包含一並聯控制閥門,該供氣裝置經由該並聯管路提供該抽氣裝置該負載氣體; 其中,當該供氣裝置提供該反應室該第一反應氣體或該第二反應氣體時,該並聯控制閥門打開以使該抽氣裝置同時對該反應室及該並聯管路抽氣,以及當該供氣裝置提供該反應室該至少一清洩氣體時,該並聯控制閥門關閉以使該抽氣裝置對該反應室抽氣但不對該並聯管路抽氣。An atomic layer deposition device includes: a reaction chamber; an air extraction device connected to the reaction chamber; a gas supply device including at least three gas sources for providing a first reaction gas, a second reaction gas, A purge gas and a load gas, the gas supply device is connected to the reaction chamber to selectively provide the first reaction gas, the second reaction gas and the purge gas, the purge gas and the load gas in the reaction chamber Both do not react with the first reaction gas and the second reaction gas; and a parallel pipeline directly connected to the pumping device and a gas source for providing the load gas, the parallel pipeline includes a parallel control valve The gas supply device provides the pumping device and the load gas through the parallel pipeline; wherein when the gas supply device provides the first reaction gas or the second reaction gas in the reaction chamber, the parallel control valve is opened so that The pumping device evacuates the reaction chamber and the parallel pipeline at the same time, and when the gas supply device provides the reaction chamber with the at least one purge gas, the parallel control valve is closed to make the pumping equipment The reaction chamber is not evacuated, but the parallel exhaust line. 如請求項7所述之原子層沉積設備,其中該並聯管路包含一負載腔體,用以容置該負載氣體,該並聯控制閥門位於該負載腔體及該抽氣裝置之間,當該並聯控制閥門打開時,該抽氣裝置對該負載腔體抽氣,且當該並聯控制閥門關閉時,該抽氣裝置不對該負載腔體抽氣。The atomic layer deposition equipment according to claim 7, wherein the parallel pipeline includes a load cavity for containing the load gas, and the parallel control valve is located between the load cavity and the pumping device. When the parallel control valve is opened, the pumping device evacuates the load cavity, and when the parallel control valve is closed, the pumping device does not evacuate the load cavity. 如請求項8所述之原子層沉積設備,其中該負載腔體容積為該反應室容積的1/5到5倍。The atomic layer deposition apparatus according to claim 8, wherein the volume of the load chamber is 1/5 to 5 times the volume of the reaction chamber. 如請求項7所述之原子層沉積設備,其中該清洩氣體為氮氣或惰性氣體。The atomic layer deposition apparatus according to claim 7, wherein the purge gas is nitrogen or an inert gas. 如請求項7所述之原子層沉積設備,其中該負載氣體為氮氣或惰性氣體。The atomic layer deposition apparatus according to claim 7, wherein the load gas is nitrogen or an inert gas. 如請求項7所述之原子層沉積設備,其中該清洩氣體及該負載氣體均是不與該第一反應氣體及該第二反應氣體反應的。The atomic layer deposition apparatus according to claim 7, wherein the purge gas and the load gas do not react with the first reaction gas and the second reaction gas.
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