TWI901951B - semiconductor processing equipment - Google Patents
semiconductor processing equipmentInfo
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- TWI901951B TWI901951B TW112115914A TW112115914A TWI901951B TW I901951 B TWI901951 B TW I901951B TW 112115914 A TW112115914 A TW 112115914A TW 112115914 A TW112115914 A TW 112115914A TW I901951 B TWI901951 B TW I901951B
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- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical 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
- C23C16/448—Chemical 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 generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials
- C23C16/4481—Chemical 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 generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials by evaporation using carrier gas in contact with the source material
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical 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
- C23C16/448—Chemical 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 generating reactive gas streams, e.g. by evaporation or sublimation of precursor materials
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical 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
- C23C16/455—Chemical 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
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical 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
- C23C16/455—Chemical 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
- C23C16/45523—Pulsed gas flow or change of composition over time
- C23C16/45525—Atomic layer deposition [ALD]
- C23C16/45544—Atomic layer deposition [ALD] characterized by the apparatus
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical 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
- C23C16/52—Controlling or regulating the coating process
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Abstract
本申請案係關於一種半導體處理裝置。在本申請案之一個實施例中,半導體處理裝置包括製程腔、汽化裝置及氣體管線。上述汽化裝置用以使經由第一管線進入上述汽化裝置之液態反應源物質汽化。上述氣體管線耦接在上述汽化裝置與上述製程腔之間,用以向上述製程腔輸送上述汽化裝置產生之經汽化之反應源物質。This application relates to a semiconductor processing apparatus. In one embodiment of this application, the semiconductor processing apparatus includes a process chamber, a vaporization device, and a gas line. The vaporization device is used to vaporize a liquid reaction source substance that enters the vaporization device via a first line. The gas line is coupled between the vaporization device and the process chamber for delivering the vaporized reaction source substance generated by the vaporization device to the process chamber.
Description
本申請案大體上係關於半導體製造領域,且更具體而言,係關於半導體處理裝置。This application is generally related to the field of semiconductor manufacturing, and more specifically to semiconductor processing devices.
在半導體製造領域,原子層沈積(ALD)製程係最廣泛應用的沈積製程之一。在ALD製程中,通常將少量反應源物質(例如前驅體(precursor)或反應物(reactant))裝入一個小鋼瓶中,將載氣通入反應源物質液體中,進而攜帶反應源物質蒸汽流入製程腔,然後進行薄膜沈積。為滿足沈積需求,通常採用以下兩種方法來提高反應源物質之蒸汽量:第一,增大載氣之流量,以藉由增大反應源物質液體內部之鼓泡量來提高反應源物質之蒸發量;第二,加熱反應源物質液體至一定的溫度(例如對容納反應源物質之鋼瓶瓶體包加熱套),由於反應源物質在較高溫度時具有較高的飽和蒸汽壓,藉由升高溫度可提高反應源物質之蒸發量。然而,一些反應源物質(例如Zr類或Ta類反應源物質)常溫下之飽和蒸汽壓比較低(例如0.01托至1托),且其飽和蒸汽壓隨溫度之變化不顯著,使用上述兩種方法很難獲得高蒸汽濃度,因此,在使用此類反應源物質進行薄膜沈積時,為使沈積反應具備足夠的蒸汽濃度,使晶圓表面能夠飽和吸附一層反應源物質分子,往往需要較長時間之反應源物質注入,否則將會引起薄膜生長不均一的問題。但因此類反應源物質活性較低、薄膜之沈積速率較低,從而導致使用此類反應源物質之ALD設備產能較低且沈積薄膜之成本較高。In the semiconductor manufacturing field, atomic layer deposition (ALD) is one of the most widely used deposition processes. In the ALD process, a small amount of reaction source material (such as a precursor or reactant) is typically placed in a small steel cylinder. A carrier gas is passed into the liquid reaction source material, which in turn carries the vapor of the reaction source material into the process chamber, where thin film deposition takes place. To meet the deposition requirements, the following two methods are typically used to increase the vapor volume of the reactant: First, increase the flow rate of the carrier gas to increase the evaporation rate of the reactant by increasing the amount of bubbling inside the reactant liquid; Second, heat the reactant liquid to a certain temperature (e.g., by covering the cylinder containing the reactant with a heating jacket). Since the reactant has a higher saturated vapor pressure at higher temperatures, the evaporation rate of the reactant can be increased by raising the temperature. However, some reaction source materials (such as Zr-based or Ta-based reaction source materials) have relatively low saturated vapor pressures at room temperature (e.g., 0.01 Torr to 1 Torr), and their saturated vapor pressures do not change significantly with temperature. It is difficult to obtain high vapor concentrations using the two methods mentioned above. Therefore, when using such reaction source materials for thin film deposition, in order to ensure that the deposition reaction has a sufficient vapor concentration so that the wafer surface can be saturated with a layer of reaction source material molecules, a longer reaction source material injection time is often required. Otherwise, it will cause the problem of uneven film growth. However, because these types of reaction source materials have lower activity and lower film deposition rates, ALD equipment using these reaction source materials has lower production capacity and higher film deposition costs.
此外,在較深的凹槽中沈積薄膜時,保型性及底部覆蓋率係重要的效能指標。現有的ALD設備所生產之此類薄膜所實現的側壁與底部之台階覆蓋率通常小於90%,無法滿足製程之需要。Furthermore, when depositing films in deeper grooves, shape retention and bottom coverage are important performance indicators. Existing ALD equipment typically achieves sidewall and bottom step coverage of less than 90% for this type of film, which cannot meet the process requirements.
因此,需要改良之半導體處理裝置來滿足對於沈積速率、成膜品質、產能及經濟性之需求。Therefore, improved semiconductor processing devices are needed to meet the requirements for deposition rate, film quality, capacity and economy.
本申請案提供一種半導體處理裝置,上述半導體處理裝置具有使液態反應源物質汽化之汽化裝置,因此可在製程過程中增大反應源物質之蒸汽濃度,提高反應源物質之有效利用率,以此提高沈積速率及薄膜之保型性,縮短薄膜沈積週期,提高製程生產品質及效率,並創造良好的生產經濟價值。This application provides a semiconductor processing apparatus having a vaporization device for vaporizing liquid reactive material. Therefore, the vapor concentration of the reactive material can be increased during the process, thereby improving the effective utilization rate of the reactive material, thus improving the deposition rate and the shape retention of the film, shortening the film deposition cycle, improving the production quality and efficiency of the process, and creating good production economic value.
在本申請案之半導體處理裝置中,可利用載氣協助汽化裝置產生之反應源物質蒸汽快速進入製程腔,並協助其在製程腔內均勻擴散,從而有效地縮短反應源物質之注入時間,大幅度地提高產能並改善薄膜品質。上述載體可提供至汽化裝置中,或提供至汽化裝置前端或後端。In the semiconductor processing apparatus of this application, the vapor of the reactant material generated by the carrier gas-assisted vaporization device can be rapidly introduced into the process chamber and assisted in its uniform diffusion within the process chamber, thereby effectively shortening the injection time of the reactant material, significantly increasing productivity, and improving film quality. The aforementioned carrier can be provided in the vaporization device, or at the front or back end of the vaporization device.
根據本申請案之一些實施例,半導體處理裝置可包括:製程腔;汽化裝置,其用以使經由第一管線進入上述汽化裝置之液態反應源物質汽化;及氣體管線,其耦接在上述汽化裝置與上述製程腔之間,用以向上述製程腔輸送上述汽化裝置產生之經汽化之反應源物質。According to some embodiments of this application, a semiconductor processing apparatus may include: a process chamber; a vaporization device for vaporizing a liquid reaction source substance that enters the vaporization device via a first pipeline; and a gas pipeline coupled between the vaporization device and the process chamber for delivering the vaporized reaction source substance generated by the vaporization device to the process chamber.
根據本申請案之一些實施例,上述半導體處理裝置進一步包括第一氣體源,上述第一氣體源藉由上述第一管線耦接至上述汽化裝置,上述第一管線上設置有靠近上述汽化裝置之第一閥及靠近上述第一氣體源之第二閥。According to some embodiments of this application, the semiconductor processing apparatus further includes a first gas source, which is coupled to the vaporization device via the first pipeline, and the first pipeline is provided with a first valve near the vaporization device and a second valve near the first gas source.
根據本申請案之一些實施例,上述半導體處理裝置進一步包括反應源物質槽,上述反應源物質槽用以容納液態反應源物質,上述反應源物質槽藉由第一支管線耦接至位於上述第二閥遠離上述第一氣體源之一端的上述第一管線,且藉由第二支管線耦接至位於上述第二閥靠近上述第一氣體源之一端的上述第一管線,其中上述第一支管線之端部位於上述反應源物質槽中之反應源物質液面下方,且上述第二支管線之端部位於上述反應源物質槽中之反應源物質液面上方。According to some embodiments of this application, the semiconductor processing apparatus further includes a reaction source material tank for containing liquid reaction source material. The reaction source material tank is coupled via a first branch line to the first pipeline located at the end of the second valve away from the first gas source, and via a second branch line to the first pipeline located at the end of the second valve near the first gas source. The end of the first branch line is below the liquid surface of the reaction source material in the reaction source material tank, and the end of the second branch line is above the liquid surface of the reaction source material in the reaction source material tank.
根據本申請案之一些實施例,上述第一支管線上設置有第三閥,及/或上述第二支管線上設置有第四閥。According to some embodiments of this application, a third valve is provided on the first branch line and/or a fourth valve is provided on the second branch line.
根據本申請案之一些實施例,上述半導體處理裝置進一步包括第二氣體源,上述第二氣體源藉由第二管線耦接在上述第一閥與上述汽化裝置之間的上述第一管線上,或耦接至上述汽化裝置之進氣口,或耦接至上述氣體管線。According to some embodiments of this application, the semiconductor processing apparatus further includes a second gas source, which is coupled to the first pipeline between the first valve and the vaporization device via a second pipeline, or coupled to the air inlet of the vaporization device, or coupled to the gas pipeline.
根據本申請案之一些實施例,上述氣體管線上設置有第五閥。According to some embodiments of this application, a fifth valve is provided on the gas pipeline.
根據本申請案之一些實施例,上述氣體管線進一步包括支路,上述支路之一端耦接在上述第五閥與上述汽化裝置之間的上述氣體管線上,且另一端耦接至真空泵,上述支路上設置有排氣閥。According to some embodiments of this application, the gas pipeline further includes a branch, one end of which is coupled to the gas pipeline between the fifth valve and the vaporization device, and the other end is coupled to a vacuum pump, and an exhaust valve is provided on the branch.
根據本申請案之一些實施例,上述半導體處理裝置進一步包括第二氣體源,上述第二氣體源藉由第二管線耦接在上述汽化裝置與上述支路之間的上述氣體管線上,或耦接至上述汽化裝置之進氣口,或耦接至上述第一管線。According to some embodiments of this application, the semiconductor processing device further includes a second gas source, which is coupled to the gas pipeline between the vaporization device and the branch via a second pipeline, or coupled to the air inlet of the vaporization device, or coupled to the first pipeline.
根據本申請案之一些實施例,上述半導體處理裝置進一步包括控制器,上述控制器經組態以:在反應源物質注入階段期間,關閉上述第二閥,開啟上述第一閥、上述第三閥及上述第四閥,以使上述反應源物質槽中之液態反應源物質在來自上述第一氣體源之第一氣體的推動下進入上述汽化裝置。According to some embodiments of this application, the semiconductor processing apparatus further includes a controller configured to: close the second valve and open the first, third and fourth valves during the reaction source material injection phase, so that the liquid reaction source material in the reaction source material tank enters the vaporization device under the impetus of the first gas from the first gas source.
根據本申請案之一些實施例,上述控制器進一步經組態以控制上述第一閥在上述反應源物質注入階段期間保持開啟之時間,以控制進入上述汽化裝置之液態反應源物質之量。According to some embodiments of this application, the controller is further configured to control the duration during which the first valve remains open during the reaction source material injection phase, so as to control the amount of liquid reaction source material entering the vaporization device.
根據本申請案之一些實施例,上述控制器進一步經組態以:在淨化階段期間,使上述第三閥及上述第四閥保持開啟,關閉上述第一閥及上述第二閥,以使上述反應源物質槽中之液態反應源物質在上述第一氣體的推動下進入上述第一管線而不進入上述汽化裝置。According to some embodiments of this application, the controller is further configured to: keep the third valve and the fourth valve open and close the first valve and the second valve during the purification phase, so that the liquid reaction source material in the reaction source material tank enters the first pipeline under the push of the first gas and does not enter the vaporization device.
根據本申請案之一些實施例,上述半導體處理裝置進一步包括控制器,上述控制器經組態以:在反應源物質注入階段期間,關閉上述排氣閥,開啟上述第五閥,以使來自上述第二氣體源之第二氣體攜帶上述汽化裝置產生之經汽化之反應源物質進入上述製程腔。According to some embodiments of this application, the semiconductor processing apparatus further includes a controller configured to: close the exhaust valve and open the fifth valve during the reaction source material injection phase, so that the second gas from the second gas source carries the vaporized reaction source material generated by the vaporization device into the process chamber.
根據本申請案之一些實施例,上述控制器進一步經組態以:在淨化階段期間,關閉上述第五閥,開啟上述排氣閥,以使上述第二氣體攜帶上述氣體管線中之殘留反應源物質進入上述真空泵。According to some embodiments of this application, the controller is further configured to: close the fifth valve and open the exhaust valve during the purification phase, so that the second gas carries the residual reaction source material in the gas pipeline into the vacuum pump.
根據本申請案之一些實施例,上述氣體管線上設置有加熱裝置,上述加熱裝置用以使上述氣體管線中之上述經汽化之反應源物質保持一定的溫度。According to some embodiments of this application, a heating device is provided on the gas pipeline to maintain the vaporized reaction source material in the gas pipeline at a certain temperature.
本申請案亦提供一種操作上述半導體處理裝置之方法,上述方法可有效地縮短沈積時間,大幅度地提高產能並改善薄膜品質。This application also provides a method for operating the above-mentioned semiconductor processing apparatus, which can effectively shorten the deposition time, significantly increase production capacity and improve film quality.
在以下附圖及描述中闡述本申請案之一或多個實例之細節。其他特徵、目標及優勢將根據上述描述及附圖以及申請專利範圍而顯而易見。Details of one or more examples of this application are illustrated in the following figures and description. Other features, objectives and advantages will become apparent from the foregoing description and figures and from the scope of the patent application.
為更好地理解本申請案之精神,以下結合本申請案之部分實施例對其作進一步說明。To better understand the spirit of this application, the following examples of some of its embodiments will be used to further illustrate it.
本說明書內使用之詞彙「在一實施例中」或「根據一實施例」並不必要參照相同具體實施例,且本說明書內使用之「在其他(一些/某些)實施例中」或「根據其他(一些/某些)實施例」並不必要參照不同的具體實施例。其目的在於例如主張之主題包括全部或部分範例具體實施例之組合。本文所指「上」及「下」之意義並不限於圖式所直接呈現之關係,其應可包含具有其他明確對應關係之描述,例如「左」及「右」,或係「上」及「下」之相反。本文所稱之「連接」應理解為涵蓋「直接連接」及「經由一或多個中間部件連接」。本文中之詞彙「晶圓」應理解為可與術語「晶元」、「基板」、「基材」、「基底」等術語互換使用,可指任何在其上進行沈積製程之元件,而非某一具有特定結構及組成之元件。本說明書中所使用之各種部件之名稱僅出於說明之目的,並不具備限定作用,不同廠商可使用不同的名稱來指代具備相同功能之部件。The use of the terms "in one embodiment" or "according to one embodiment" in this specification does not necessarily refer to the same specific embodiment, and the use of "in other (some/certain) embodiments" or "according to other (some/certain) embodiments" does not necessarily refer to different specific embodiments. The purpose is to, for example, ensure that the claimed subject matter includes combinations of all or some of the specific embodiments of the examples. The meaning of "up" and "down" as used herein is not limited to the relationship directly presented in the diagrams; it may include descriptions with other clearly corresponding relationships, such as "left" and "right," or the opposite of "up" and "down." The term "connection" as used herein should be understood to encompass both "direct connection" and "connection via one or more intermediate components." The term "wafer" used in this document should be understood as interchangeable with terms such as "chip," "substrate," "material substrate," and "base," referring to any component on which a deposition process is performed, rather than a specific component with a particular structure and composition. The names of the various components used in this specification are for illustrative purposes only and are not intended to be limiting; different manufacturers may use different names to refer to components with the same function.
以下詳細地論述本申請案之各種實施方案。儘管論述了具體的實施方案,但應當理解,此等實施方案僅用於示出之目的。熟習相關技術者將認識到,在不偏離本申請案之精神及保護範疇的情況下,可使用其他部件及組態。本申請案之實施方案可不必包含說明書所描述之實施例中之所有部件或步驟,亦可根據實際應用而調整各步驟之執行順序。The various embodiments of this application are described in detail below. Although specific embodiments are described, it should be understood that these embodiments are for illustrative purposes only. Those skilled in the art will recognize that other components and configurations can be used without departing from the spirit and scope of this application. The embodiments of this application do not necessarily need to include all components or steps described in the embodiments, and the execution order of each step can be adjusted according to the actual application.
如前所述,當前用於ALD製程之半導體處理裝置具有沈積速率低、沈積時間長、沈積成本高、產能低、保型性低等缺點。本申請案提供了改良之半導體處理裝置及方法來解決上述問題中之至少一者。As mentioned above, current semiconductor processing devices used in ALD processes suffer from drawbacks such as low deposition rate, long deposition time, high deposition cost, low productivity, and poor form retention. This application provides an improved semiconductor processing device and method to solve at least one of the above problems.
本申請案之半導體處理裝置及方法可用於形成SnO 2、InO 2、TaN、HfO 2、ZrO 2等薄膜,但本申請案不限於此。本申請案之半導體處理裝置可用於包括但不限於熱原子層沈積(Thermal ALD)、電漿增強型原子層沈積(PEALD)等之ALD製程,亦可用於其他類似製程。 The semiconductor processing apparatus and method of this application can be used to form thin films such as SnO2 , InO2 , TaN, HfO2 , and ZrO2 , but this application is not limited to these. The semiconductor processing apparatus of this application can be used in ALD processes including but not limited to thermal atomic layer deposition (TALD) and plasma-enhanced atomic layer deposition (PEALD), and can also be used in other similar processes.
圖1為根據本申請案之實施例之半導體處理裝置100的結構示意圖。如圖1所示,半導體處理裝置100包括製程腔1、汽化裝置2及氣體管線3。製程腔1用於容納晶圓,可在其內部對晶圓執行沈積製程。汽化裝置2用以使經由第一管線4進入汽化裝置2之液態反應源物質汽化。在一些實施例中,進入汽化裝置2之反應源物質可為前驅體或反應物。氣體管線3耦接在汽化裝置2與製程腔1之間,用以向製程腔1輸送汽化裝置2產生之經汽化之反應源物質。在一些實施例中,汽化裝置2可藉由加熱之方式使液態反應源物質汽化。在一些實施例中,汽化裝置2之溫度可小於或等於200℃。熟習此項技術者應瞭解可用於使液體汽化之各種裝置及方法,此等裝置及方法可用於實施汽化裝置2。Figure 1 is a schematic structural diagram of a semiconductor processing apparatus 100 according to an embodiment of this application. As shown in Figure 1, the semiconductor processing apparatus 100 includes a process chamber 1, a vaporization device 2, and a gas line 3. The process chamber 1 is used to house a wafer, and deposition processes can be performed on the wafer within it. The vaporization device 2 is used to vaporize the liquid reaction source material that enters the vaporization device 2 via the first line 4. In some embodiments, the reaction source material entering the vaporization device 2 may be a precursor or a reactant. The gas line 3 is coupled between the vaporization device 2 and the process chamber 1 to deliver the vaporized reaction source material generated by the vaporization device 2 to the process chamber 1. In some embodiments, the vaporization device 2 may vaporize the liquid reaction source material by heating. In some embodiments, the temperature of the vaporization device 2 may be less than or equal to 200°C. Those skilled in the art will be familiar with various devices and methods that can be used to vaporize liquids, and these devices and methods can be used to implement the vaporization device 2.
根據本申請案之實施例,液態反應源物質在汽化裝置2中汽化,可實現高蒸汽濃度。經汽化之高濃度之反應源物質通過氣體管線3進入製程腔1,可提高沈積速率。因此,本申請案可縮短沈積週期,增加每小時可處理之製程片數量,使得產能大幅度提高。According to an embodiment of this application, the liquid reactant is vaporized in the vaporization device 2, achieving a high vapor concentration. The vaporized, high-concentration reactant enters the process chamber 1 through the gas pipeline 3, increasing the deposition rate. Therefore, this application can shorten the deposition cycle, increase the number of process wafers that can be processed per hour, and significantly improve production capacity.
氣體管線3可具有任意的長度及形狀。在一些實施例中,氣體管線3具有0.1 m至10 m之長度。在一些實施例中,氣體管線3上亦可設置圖1中未示出之其他裝置,例如,加熱裝置等。在一些實施例中,氣體管線3上之加熱裝置可使得進入氣體管線3中之反應源物質蒸汽保持在一定的溫度(例如,等於或大於汽化裝置2之溫度),使得反應源物質蒸汽經由氣體管線3順利進入製程腔1且保持良好的反應活性。The gas pipeline 3 can have any length and shape. In some embodiments, the gas pipeline 3 has a length of 0.1 m to 10 m. In some embodiments, other devices not shown in FIG. 1, such as heating devices, can also be installed on the gas pipeline 3. In some embodiments, the heating device on the gas pipeline 3 can maintain the reactant vapor entering the gas pipeline 3 at a certain temperature (e.g., equal to or greater than the temperature of the vaporization device 2), so that the reactant vapor smoothly enters the process chamber 1 through the gas pipeline 3 and maintains good reactivity.
如圖1所示,半導體處理裝置100進一步包括第一氣體源5。第一氣體源5藉由第一管線4耦接至汽化裝置2。第一氣體源5可提供用於推動液態反應源物質進入汽化裝置2之第一氣體。第一氣體又可稱為推動氣(push gas)。在一些實施例中,第一氣體包括惰性氣體,例如氬氣(Ar),或氮氣(N2),或氦氣(He)等。在一些實施例中,第一氣體源5提供之第一氣體可具有較大的流速,以滿足推動力需求。在一些實施例中,第一氣體源5提供之第一氣體之流速可大於或等於約0.1 L/min且小於約10 L/min。As shown in Figure 1, the semiconductor processing apparatus 100 further includes a first gas source 5. The first gas source 5 is coupled to the vaporization apparatus 2 via a first line 4. The first gas source 5 provides a first gas for propelling the liquid reaction source material into the vaporization apparatus 2. The first gas may also be referred to as a push gas. In some embodiments, the first gas includes an inert gas, such as argon (Ar), nitrogen (N2), or helium (He). In some embodiments, the first gas provided by the first gas source 5 may have a relatively high flow rate to meet the propulsion requirements. In some embodiments, the flow rate of the first gas provided by the first gas source 5 may be greater than or equal to about 0.1 L/min and less than about 10 L/min.
第一管線4上設置有靠近汽化裝置2之第一閥41及靠近第一氣體源5之第二閥42。在一些實施例中,第一閥41可為快速開關之氣動閥,可藉由控制器控制該閥之開關時間來控制流入汽化裝置2之液體之量。在一些實施例中,第一閥41可為ALD閥,但其不限於此。The first pipeline 4 is provided with a first valve 41 near the vaporization device 2 and a second valve 42 near the first gas source 5. In some embodiments, the first valve 41 may be a fast-opening pneumatic valve, and the amount of liquid flowing into the vaporization device 2 can be controlled by a controller to control the opening and closing time of the valve. In some embodiments, the first valve 41 may be an ALD valve, but it is not limited to this.
第一管線4可具有任意的長度及形狀。在一些實施例中,第一管線4具有0.1 m至10 m之長度。在一些實施例中,第一管線4上亦可設置圖1中未示出之其他裝置。The first pipeline 4 can have any length and shape. In some embodiments, the first pipeline 4 has a length of 0.1 m to 10 m. In some embodiments, other devices not shown in Figure 1 may also be installed on the first pipeline 4.
在一些實施例中,半導體處理裝置100進一步包括反應源物質槽6。反應源物質槽6用以容納液態反應源物質,反應源物質槽6藉由第一支管線7耦接至位於第二閥42遠離第一氣體源5之一端的第一管線4,且藉由第二支管線8耦接至位於第二閥42靠近第一氣體源5之一端的第一管線4。第一支管線7之端部位於反應源物質槽6中之反應源物質液面下方,且第二支管線8之端部位於反應源物質槽6中之反應源物質液面上方。在此組態下,經由第一管線4及第二支線管8進入反應源物質槽6中之第一氣體集中在反應源物質液面上方並對反應源物質液面施加一定的壓力。液態反應源物質在第一氣體之壓力作用下經由第一支線管7及第一管線4進入汽化裝置2。在一些實施例中,第一支管線7之端部位於反應源物質槽6之底部,第二支管線8之端部位於反應源物質槽6之頂部。In some embodiments, the semiconductor processing apparatus 100 further includes a reaction source material tank 6. The reaction source material tank 6 is used to contain a liquid reaction source material. The reaction source material tank 6 is coupled via a first branch line 7 to a first line 4 located at the end of the second valve 42 away from the first gas source 5, and via a second branch line 8 to the first line 4 located at the end of the second valve 42 near the first gas source 5. The end of the first branch line 7 is below the surface of the reaction source material liquid in the reaction source material tank 6, and the end of the second branch line 8 is above the surface of the reaction source material liquid in the reaction source material tank 6. In this configuration, the first gas entering the reaction source material tank 6 via the first line 4 and the second branch line 8 is concentrated above the surface of the reaction source material liquid and applies a certain pressure to the surface of the reaction source material liquid. The liquid reaction source material enters the vaporization device 2 through the first branch pipe 7 and the first pipeline 4 under the pressure of the first gas. In some embodiments, the end of the first branch pipe 7 is at the bottom of the reaction source material tank 6, and the end of the second branch pipe 8 is at the top of the reaction source material tank 6.
參照圖1,第一支管線7上設置有第三閥71,且第二支管線8上設置有第四閥81。在需要向汽化裝置2提供液態反應源物質時(例如在反應源物質注入階段期間),可關閉第二閥42並開啟第一閥41、第三閥71及第四閥81,以使來自第一氣體源5之第一氣體經由第一管線4及第二支管線8進入反應源物質槽6,並使反應源物質槽6中之液態反應源物質在第一氣體的推動下經由第一支管線7及第一管線4進入汽化裝置2。在不需要向汽化裝置2提供液態反應源物質時(例如在淨化階段期間),可關閉第一閥41及第二閥42並使第三閥71及第四閥81保持開啟,以使反應源物質在第一氣體的推動下進入第一管線4而不進入汽化裝置2;等下一反應源物質注入階段開始時,第一管線4中之反應源物質可快速進入汽化裝置2。在一些製程階段(例如需要清除第一管線4中殘留之反應源物質時),可開啟第二閥42並關閉第三閥71及第四閥81,以使來自第一氣體源5之第一氣體直接進入第二閥42後端的第一管線4。在一些實施例中,可省略第三閥71及第四閥81中之一者。例如,第一支管線7上設置有第三閥71,而第二支管線8上沒有閥;或者,第二支管線8上設置有第四閥81,而第一支管線7上沒有閥。Referring to Figure 1, a third valve 71 is provided on the first branch line 7, and a fourth valve 81 is provided on the second branch line 8. When it is necessary to supply liquid reaction source material to the vaporization device 2 (for example, during the reaction source material injection stage), the second valve 42 can be closed and the first valve 41, the third valve 71 and the fourth valve 81 can be opened, so that the first gas from the first gas source 5 enters the reaction source material tank 6 through the first line 4 and the second branch line 8, and the liquid reaction source material in the reaction source material tank 6 enters the vaporization device 2 through the first branch line 7 and the first line 4 under the push of the first gas. When it is not necessary to supply liquid reactant to vaporization device 2 (e.g., during the purification phase), the first valve 41 and the second valve 42 can be closed while the third valve 71 and the fourth valve 81 remain open, allowing the reactant to enter the first pipeline 4 under the impetus of the first gas without entering the vaporization device 2; when the next reactant injection phase begins, the reactant in the first pipeline 4 can quickly enter the vaporization device 2. In some process stages (e.g., when it is necessary to remove residual reactant in the first pipeline 4), the second valve 42 can be opened while the third valve 71 and the fourth valve 81 are closed, allowing the first gas from the first gas source 5 to directly enter the first pipeline 4 downstream of the second valve 42. In some embodiments, one of the third valve 71 and the fourth valve 81 may be omitted. For example, the first branch line 7 may have a third valve 71, while the second branch line 8 may not have a valve; or the second branch line 8 may have a fourth valve 81, while the first branch line 7 may not have a valve.
由於半導體處理裝置100藉由汽化裝置2汽化反應源物質,因此反應源物質槽6可保持常溫而無需加熱。在一些實施例中,反應源物質槽6中之反應源物質可係飽和蒸汽壓隨溫度之變化不顯著的反應源物質,例如Zr類或Ta類反應源物質。由於此類反應源物質藉由習知提高蒸發量之方法難以獲得高蒸汽濃度,因此使用現有半導體處理裝置難以獲得較高的沈積速率。本申請案之半導體處理裝置100使用第一氣體將液態反應源物質推入汽化裝置2,在汽化裝置2中將反應源物質汽化,並使汽化後之反應源物質通過氣體管線3進入製程腔1,因此可提高反應源物質之蒸汽濃度,從而提高沈積速率,縮短沈積週期。在一些實施例中,反應源物質槽6中之反應源物質可係常溫(例如約25℃)蒸汽壓較低(例如0.01托至10托)之反應源物質。Since the semiconductor processing apparatus 100 vaporizes the reactant material via the vaporization device 2, the reactant material tank 6 can be kept at room temperature without heating. In some embodiments, the reactant material in the reactant material tank 6 may be a reactant material whose saturated vapor pressure does not change significantly with temperature, such as Zr-based or Ta-based reactant materials. Because it is difficult to obtain high vapor concentrations for such reactant materials using conventional methods to increase evaporation rate, it is difficult to obtain high deposition rates using existing semiconductor processing apparatuses. The semiconductor processing apparatus 100 of this application uses a first gas to push liquid reactive material into a vaporization device 2, where the reactive material is vaporized. The vaporized reactive material then enters the process chamber 1 through a gas line 3, thereby increasing the vapor concentration of the reactive material, thus increasing the deposition rate and shortening the deposition cycle. In some embodiments, the reactive material in the reactive material tank 6 may be a reactive material with a low vapor pressure (e.g., 0.01 Torr to 10 Torr) at room temperature (e.g., about 25°C).
再參照圖1,氣體管線3上設置有第五閥31。當第五閥31敞開時,氣體管線3中之氣體可進入製程腔1。Referring again to Figure 1, a fifth valve 31 is provided on the gas pipeline 3. When the fifth valve 31 is open, the gas in the gas pipeline 3 can enter the process chamber 1.
在一些實施例中,氣體管線3進一步包括支路9。支路9之一端耦接在第五閥31與汽化裝置2之間的氣體管線3上,且另一端耦接至真空泵10。支路9上設置有排氣閥91。當排氣閥91敞開時,氣體管線3中之氣體可經由支路9釋放至真空泵10 (例如,藉由真空泵10之抽吸)。支路9上亦可設置圖1中未示出之其他裝置。在一些實施例中,支路9上亦可設置加熱裝置,使得支路9可具有等於或大於汽化裝置2之溫度,從而氣體管線3中之氣體可經由支路9順利排出而不會冷凝在支路9中。在半導體處理裝置100之操作期間,真空泵10可一直開啟或僅在需要抽吸氣體管線3中之氣體時才開啟。In some embodiments, the gas line 3 further includes a branch 9. One end of the branch 9 is coupled to the gas line 3 between the fifth valve 31 and the vaporization device 2, and the other end is coupled to the vacuum pump 10. A vent valve 91 is provided on the branch 9. When the vent valve 91 is open, the gas in the gas line 3 can be released to the vacuum pump 10 via the branch 9 (e.g., by suction from the vacuum pump 10). Other devices, not shown in FIG. 1, may also be provided on the branch 9. In some embodiments, a heating device may also be provided on the branch 9 so that the branch 9 can have a temperature equal to or greater than that of the vaporization device 2, so that the gas in the gas line 3 can be smoothly discharged through the branch 9 without condensing in the branch 9. During the operation of the semiconductor processing device 100, the vacuum pump 10 may be kept on continuously or only turned on when it is necessary to pump gas from the gas line 3.
在一些實施例中,半導體處理裝置100進一步包括第二氣體源11。如圖1所示,第二氣體源11藉由第二管線12耦接至汽化裝置2之進氣口(圖中未示出)。第二氣體源11可提供用於攜帶反應源物質之第二氣體。第二氣體又可稱為載氣(carrier)。在一些實施例中,第二氣體包括惰性氣體,例如氬氣(Ar),或氮氣(N2),或氦氣(He)等。一方面,第二氣體源11提供之第二氣體可協助汽化裝置2產生之反應源物質蒸汽快速進入製程腔1,並協助反應源物質在製程腔1內擴散,以使反應源物質在製程腔1內分佈更均勻,從而使得沈積之薄膜均一性更好。另一方面,第二氣體源11提供之第二氣體可用於吹掃氣體管線3,加速氣體管線3之淨化,使氣體管線3內殘留之反應源物質經由支路9釋放至真空泵10,以避免氣體管線3內殘留有反應源物質而在後續的作業中流入製程腔1並引起顆粒問題。在一些實施例中,第二氣體源11提供之第二氣體具有較大的流速以加快輸送經汽化之反應源物質。在一些實施例中,第二氣體源11提供之載氣之流速可大於或等於約0.5 L/min且小於約30 L/min,例如約0.5 L/min至約10 L/min或約5 L/min至約10 L/min等。第二管線12上亦可設置圖1中未示出之其他裝置。在一些實施例中,第二管線12亦包括加熱裝置,以使進入第二管線12之第二氣體加熱至一定的溫度。在一些實施例中,第二氣體之溫度可小於或等於80℃。In some embodiments, the semiconductor processing apparatus 100 further includes a second gas source 11. As shown in FIG. 1, the second gas source 11 is coupled to the inlet (not shown) of the vaporization device 2 via a second conduit 12. The second gas source 11 provides a second gas for carrying the reactant material. The second gas may also be referred to as a carrier gas. In some embodiments, the second gas includes an inert gas, such as argon (Ar), nitrogen (N2), or helium (He). On the one hand, the second gas provided by the second gas source 11 can assist the reactant material vapor generated by the vaporization device 2 to quickly enter the process chamber 1 and assist the reactant material to diffuse within the process chamber 1, so that the reactant material is more uniformly distributed within the process chamber 1, thereby resulting in better uniformity of the deposited film. On the other hand, the second gas provided by the second gas source 11 can be used to purge the gas line 3, accelerating its purification and releasing any residual reactant material within the gas line 3 to the vacuum pump 10 via the branch 9. This prevents residual reactant material from flowing into the process chamber 1 during subsequent operations and causing particle problems. In some embodiments, the second gas provided by the second gas source 11 has a higher flow rate to accelerate the transport of the vaporized reactant material. In some embodiments, the flow rate of the carrier gas provided by the second gas source 11 can be greater than or equal to about 0.5 L/min and less than about 30 L/min, for example, from about 0.5 L/min to about 10 L/min or from about 5 L/min to about 10 L/min. Other devices not shown in Figure 1 may also be installed on the second line 12. In some embodiments, the second pipeline 12 also includes a heating device to heat the second gas entering the second pipeline 12 to a certain temperature. In some embodiments, the temperature of the second gas may be less than or equal to 80°C.
根據本申請案之一些實施例,使用半導體處理裝置100進行之沈積製程可包括反應源物質注入階段。在反應源物質注入階段期間,可關閉第二閥42及排氣閥91,開啟第一閥41、第三閥71、第四閥81及第五閥31。在此種組態下,反應源物質槽6中之液態反應源物質在來自第一氣體源5之第一氣體的推動下進入汽化裝置2,並在汽化裝置2中汽化,與此同時,來自第二氣體源11之第二氣體進入汽化裝置2並攜帶經汽化之反應源物質通過氣體管線3進入製程腔1。According to some embodiments of this application, the deposition process using the semiconductor processing apparatus 100 may include a reactant injection stage. During the reactant injection stage, the second valve 42 and the exhaust valve 91 may be closed, and the first valve 41, the third valve 71, the fourth valve 81, and the fifth valve 31 may be opened. In this configuration, the liquid reactant in the reactant tank 6 is propelled by the first gas from the first gas source 5 into the vaporization device 2 and vaporized in the vaporization device 2. At the same time, the second gas from the second gas source 11 enters the vaporization device 2 and carries the vaporized reactant through the gas line 3 into the process chamber 1.
根據本申請案之一些實施例,沈積製程亦可包括淨化階段。在淨化階段期間,可關閉第一閥41、第二閥42及第五閥31,開啟第三閥71、第四閥81及排氣閥91。在此種組態下,反應源物質槽6中之液態反應源物質在來自第一氣體源5之第一氣體的推動下進入第一管線4而不進入汽化裝置2,氣體管線3中殘留之反應源物質將隨第二氣體一起被抽吸至真空泵10。通常ALD之沈積反應需重複循環多次,直至達到指定的膜厚才停止,因此在整個沈積過程中,反應源物質注入階段及淨化階段會多次重複進行,且每一階段之時間可在0.01 ms至10 s之範圍內。According to some embodiments of this application, the deposition process may also include a purification stage. During the purification stage, the first valve 41, the second valve 42, and the fifth valve 31 may be closed, while the third valve 71, the fourth valve 81, and the exhaust valve 91 may be opened. In this configuration, the liquid reactant material in the reactant material tank 6 is propelled into the first pipeline 4 by the first gas from the first gas source 5 without entering the vaporization device 2, and the reactant material remaining in the gas pipeline 3 is drawn into the vacuum pump 10 along with the second gas. Typically, the deposition reaction of ALD needs to be repeated multiple times until the specified film thickness is reached. Therefore, during the entire deposition process, the reaction source material injection stage and the purification stage are repeated multiple times, and the time of each stage can be in the range of 0.01 ms to 10 s.
半導體處理裝置100藉由汽化裝置2增大了進入製程腔1之反應源物質濃度,而且,藉由載氣之攜帶,可加速反應源物質在氣體管線及製程腔內之擴散,提高反應效率,從而可縮短反應源物質注入之脈衝時間,使得單位時間內流入製程腔1之反應源物質之量得到有效提昇,因而可縮短製程腔1之沈積時間。因此,本申請案可縮短沈積週期,增加每小時可處理之製程片數量,使得產能大幅度提高。此外,增大之反應源物質濃度可使得沈積而成之薄膜具有高的保型性,有效提高薄膜品質。The semiconductor processing apparatus 100 increases the concentration of the reactant entering the process chamber 1 through the vaporization device 2. Furthermore, the carrier gas accelerates the diffusion of the reactant within the gas pipeline and process chamber, improving reaction efficiency and shortening the pulse time of reactant injection. This effectively increases the amount of reactant flowing into the process chamber 1 per unit time, thus shortening the deposition time in the process chamber 1. Therefore, this application can shorten the deposition cycle, increase the number of wafers that can be processed per hour, and significantly improve production capacity. In addition, the increased reactant concentration allows the deposited film to have high conformability, effectively improving film quality.
半導體處理裝置100可進一步包括控制器(圖中未示出),其用以控制並完成各個部件之操作及配合。例如,可將關於在各製程階段中各閥門需要設定之狀態(例如,開啟或關閉)之資料(亦可稱為「配方(recipe)」)儲存在控制器(或與控制器耦接之記憶體)中,控制器可根據所儲存之資料及將要進行之製程階段產生各別控制信號控制各閥門之狀態,從而執行製程。The semiconductor processing device 100 may further include a controller (not shown) for controlling and coordinating the operation of the various components. For example, data (also known as a "recipe") regarding the states (e.g., open or closed) that need to be set for each valve at each process stage can be stored in the controller (or memory coupled to the controller). The controller can generate individual control signals based on the stored data and the process stage to be performed to control the state of each valve, thereby executing the process.
在一些實施例中,控制器經組態以:在反應源物質注入階段期間,關閉第二閥42,開啟第一閥41、第三閥71及第四閥81,以使反應源物質槽6中之液態反應源物質在來自第一氣體源5之第一氣體的推動下進入汽化裝置2。In some embodiments, the controller is configured to close the second valve 42 and open the first valve 41, the third valve 71 and the fourth valve 81 during the reaction source material injection phase, so that the liquid reaction source material in the reaction source material tank 6 enters the vaporization device 2 under the impetus of the first gas from the first gas source 5.
在一些實施例中,控制器進一步經組態以:在反應源物質注入階段期間,關閉排氣閥91,開啟第五閥31,以使來自第二氣體源11之第二氣體攜帶汽化裝置2產生之經汽化之反應源物質進入製程腔1。In some embodiments, the controller is further configured to: close the exhaust valve 91 and open the fifth valve 31 during the reaction source material injection phase, so that the second gas from the second gas source 11 carries the vaporized reaction source material generated by the vaporization device 2 into the process chamber 1.
在一些實施例中,控制器進一步經組態以控制第一閥41在反應源物質注入階段期間保持開啟之時間,以控制進入汽化裝置2之液態反應源物質之量。ALD反應具有自終止之特性,即當單原子層吸附達到飽和後,就無法繼續吸附多餘的反應源物質。因此,在每一沈積週期內,由汽化裝置2汽化後之反應源物質在晶圓表面之吸附達到飽和後,剩餘的反應源物質將無法繼續有效使用,只能排出。本申請案利用ALD之此反應特性設計採用第一閥41控制汽化時間之方法來控制反應源物質之量,即,只要反應源物質之量夠即可,而無需採用更為精準的液體流量計來控制反應源物質之量。在使用液體流量計之情形中,需要等待液體流量計穩定(通常需要約7 s之時間)後才能精確控制進入汽化裝置之反應源物質液體之量,即,在液體流量計穩定前汽化裝置產生之反應源物質蒸汽不能流入製程腔,只能排掉,此會造成昂貴的浪費。為節省沈積時間及成本,本申請案之半導體處理裝置100可藉由控制器控制第一閥41之開啟與關閉來控制液態反應源物質進入汽化裝置2之時間及流量。當第一閥41開啟時,液態反應源物質直接進入汽化裝置2並在汽化裝置2中汽化,因此,反應源物質可在較短時間內汽化並流入製程腔1。由於液體反應源物質可在第一閥41的控制下進入汽化裝置2並進行汽化,而無需像使用液體流量計那樣等待額外的穩定時間,因此本申請案之半導體處理裝置100可應用於沈積週期較短的ALD沈積製程,且成本較低。In some embodiments, the controller is further configured to control the duration for which the first valve 41 remains open during the reactant injection phase, thereby controlling the amount of liquid reactant entering the vaporization device 2. The ALD reaction has a self-terminating characteristic; that is, once the monolayer adsorption reaches saturation, it can no longer adsorb excess reactant. Therefore, in each deposition cycle, once the adsorption of the reactant vaporized by the vaporization device 2 on the wafer surface reaches saturation, the remaining reactant cannot be effectively used and must be discharged. This application utilizes the reaction characteristics of ALD to design a method that uses a first valve 41 to control the vaporization time in order to control the amount of the reaction source substance. That is, as long as the amount of reaction source substance is sufficient, there is no need to use a more precise liquid flow meter to control the amount of reaction source substance. When using a liquid flow meter, it is necessary to wait for the liquid flow meter to stabilize (usually about 7 seconds) before the amount of reaction source substance liquid entering the vaporization device can be accurately controlled. That is, before the liquid flow meter stabilizes, the reaction source substance vapor generated by the vaporization device cannot flow into the process chamber and can only be discharged, which will cause expensive waste. To save deposition time and cost, the semiconductor processing apparatus 100 of this application can control the time and flow rate of the liquid reactant entering the vaporization device 2 by controlling the opening and closing of the first valve 41. When the first valve 41 is open, the liquid reactant directly enters the vaporization device 2 and vaporizes there. Therefore, the reactant can vaporize and flow into the process chamber 1 in a shorter time. Since the liquid reactant can enter the vaporization device 2 and vaporize under the control of the first valve 41 without waiting for additional stabilization time as with liquid flow meters, the semiconductor processing apparatus 100 of this application can be applied to ALD deposition processes with shorter deposition cycles and lower costs.
在一些實施例中,控制器進一步經組態以:在淨化階段期間,使第三閥71及第四閥81保持開啟,關閉第一閥41及第二閥42,以使反應源物質槽6中之液態反應源物質在第一氣體的推動下進入第一管線4而不進入汽化裝置2。In some embodiments, the controller is further configured to keep the third valve 71 and the fourth valve 81 open and close the first valve 41 and the second valve 42 during the purification phase, so that the liquid reaction source material in the reaction source material tank 6 enters the first pipeline 4 under the impetus of the first gas and does not enter the vaporization device 2.
在一些實施例中,控制器進一步經組態以:在淨化階段期間,關閉第五閥31,開啟排氣閥91,以使第二氣體攜帶氣體管線3中之殘留反應源物質進入真空泵10。In some embodiments, the controller is further configured to: during the purification phase, close the fifth valve 31 and open the exhaust valve 91 so that the second gas carries the residual reaction source material in the gas line 3 into the vacuum pump 10.
圖2為根據本申請案之又一實施例之半導體處理裝置200的結構示意圖。圖2中之半導體處理裝置200與圖1中之半導體處理裝置100的區別之處僅在於:圖2中之第二氣體源11藉由第二管線12a耦接在汽化裝置2之後端(例如汽化裝置2與支路9之間的氣體管線3上)。Figure 2 is a schematic diagram of the structure of a semiconductor processing apparatus 200 according to another embodiment of this application. The only difference between the semiconductor processing apparatus 200 in Figure 2 and the semiconductor processing apparatus 100 in Figure 1 is that the second gas source 11 in Figure 2 is coupled to the downstream end of the vaporization device 2 (e.g., on the gas pipeline 3 between the vaporization device 2 and the branch 9) via a second pipeline 12a.
如圖2所示,在反應源物質注入階段期間,可關閉第二閥42及排氣閥91,開啟第一閥41、第三閥71、第四閥81及第五閥31。在此種組態下,反應源物質槽6中之液態反應源物質在來自第一氣體源5之第一氣體的推動下進入汽化裝置2,並在汽化裝置2中汽化,經汽化之反應源物質進入氣體管線3,與此同時,來自第二氣體源11之第二氣體經由第二管線12a進入氣體管線3,並攜帶經汽化之反應源物質一起通過氣體管線3進入製程腔1。在淨化階段期間,可關閉第一閥41、第二閥42及第五閥31,開啟第三閥71、第四閥81及排氣閥91。在此種組態下,反應源物質槽6中之液態反應源物質在來自第一氣體源5之第一氣體的推動下進入第一管線4而不進入汽化裝置2,氣體管線3中殘留之反應源物質將隨第二氣體一起被抽吸至真空泵10。As shown in Figure 2, during the reaction source material injection stage, the second valve 42 and the exhaust valve 91 can be closed, while the first valve 41, the third valve 71, the fourth valve 81, and the fifth valve 31 can be opened. In this configuration, the liquid reaction source material in the reaction source material tank 6 is propelled into the vaporization device 2 by the first gas from the first gas source 5, and vaporizes in the vaporization device 2. The vaporized reaction source material enters the gas pipeline 3. At the same time, the second gas from the second gas source 11 enters the gas pipeline 3 through the second pipeline 12a, and carries the vaporized reaction source material together through the gas pipeline 3 into the process chamber 1. During the purification phase, the first valve 41, the second valve 42, and the fifth valve 31 can be closed, while the third valve 71, the fourth valve 81, and the exhaust valve 91 can be opened. In this configuration, the liquid reactant material in the reactant material tank 6 enters the first pipeline 4 under the impetus of the first gas from the first gas source 5, but does not enter the vaporization device 2. The reactant material remaining in the gas pipeline 3 will be drawn into the vacuum pump 10 along with the second gas.
與半導體處理裝置100類似,半導體處理裝置200亦可進一步包括控制器(圖中未示出),其用以控制並完成各個部件之操作及配合。Similar to semiconductor processing device 100, semiconductor processing device 200 may further include a controller (not shown in the figure) for controlling and completing the operation and coordination of the various components.
圖3為根據本申請案之又一實施例之半導體處理裝置300的結構示意圖。圖3中之半導體處理裝置300與圖1中之半導體處理裝置100的區別之處僅在於:圖3中之第二氣體源11藉由第二管線12b耦接在汽化裝置2之前端(例如,第一閥41與汽化裝置2之間的第一管線4上)。Figure 3 is a schematic diagram of the structure of a semiconductor processing apparatus 300 according to another embodiment of this application. The only difference between the semiconductor processing apparatus 300 in Figure 3 and the semiconductor processing apparatus 100 in Figure 1 is that the second gas source 11 in Figure 3 is coupled to the front end of the vaporization device 2 (e.g., on the first pipeline 4 between the first valve 41 and the vaporization device 2) via the second pipeline 12b.
半導體處理裝置300中各閥門之狀態設定可與半導體處理裝置100及200相似,此處不再贅述。與半導體處理裝置100及200類似,半導體處理裝置300亦可進一步包括控制器(圖中未示出),其用以控制並完成各個部件之操作及配合。The state settings of each valve in the semiconductor processing device 300 can be similar to those in semiconductor processing devices 100 and 200, and will not be described in detail here. Similar to semiconductor processing devices 100 and 200, semiconductor processing device 300 may also further include a controller (not shown in the figure), which is used to control and complete the operation and coordination of each component.
根據本申請案之一些實施例,一種操作半導體處理裝置(例如半導體處理裝置100、200或300)之方法可包括:在反應源物質注入階段期間,將液態反應源物質提供至汽化裝置(例如汽化裝置2),在汽化裝置中將液態反應源物質汽化,並將經汽化之反應源物質通過氣體管線(例如氣體管線3)提供至製程腔(例如製程腔1) (例如,藉由關閉第二閥42及排氣閥91,並開啟第一閥41、第三閥71、第四閥81及第五閥31);及在淨化階段期間,將液態反應源物質提供至第一管線(例如第一管線4)而不提供至汽化裝置(例如,藉由關閉第二閥42及第一閥41,並開啟第三閥71及第四閥81),並將氣體管線中殘留之反應源物質釋放至真空泵(例如真空泵10)中(例如,關閉第五閥31並開啟排氣閥91)。淨化階段可緊接在反應源物質注入階段之後進行。According to some embodiments of this application, a method of operating a semiconductor processing apparatus (e.g., semiconductor processing apparatus 100, 200, or 300) may include: during a reactant injection phase, providing a liquid reactant to a vaporization apparatus (e.g., vaporization apparatus 2), vaporizing the liquid reactant in the vaporization apparatus, and providing the vaporized reactant through a gas line (e.g., gas line 3) to a process chamber (e.g., process chamber 1). (For example, by closing the second valve 42 and the exhaust valve 91, and opening the first valve 41, the third valve 71, the fourth valve 81, and the fifth valve 31); and during the purification phase, liquid reactant is supplied to the first pipeline (e.g., the first pipeline 4) but not to the vaporization device (e.g., by closing the second valve 42 and the first valve 41, and opening the third valve 71 and the fourth valve 81), and any reactant residue in the gas pipeline is released into the vacuum pump (e.g., the vacuum pump 10) (e.g., by closing the fifth valve 31 and opening the exhaust valve 91). The purification phase may immediately follow the reactant injection phase.
在一些實施例中,操作半導體處理裝置之方法可進一步包括:在反應源物質注入階段期間,提供第二氣體(例如,來自第二氣體源11之第二氣體)攜帶經汽化之反應源物質進入製程腔;及在淨化階段期間,提供第二氣體攜帶氣體管線中殘留之反應源物質蒸汽一起被抽吸至真空泵。第二氣體可協助經汽化之反應源物質快速進入製程腔及快速排出,因此可縮短反應源物質注入及淨化時間,從而縮短沈積週期並提高產能。In some embodiments, the method of operating the semiconductor processing apparatus may further include: during the reactant injection phase, providing a second gas (e.g., a second gas from a second gas source 11) to carry the vaporized reactant into the process chamber; and during the purification phase, providing the second gas to carry the reactant vapor remaining in the gas line and being drawn to a vacuum pump. The second gas can assist the vaporized reactant in rapidly entering and exiting the process chamber, thus shortening the reactant injection and purification time, thereby shortening the deposition cycle and increasing productivity.
圖1至圖3中僅示出半導體處理裝置中向製程腔提供一種經汽化之反應源物質(例如前驅體或反應物)之相關氣體管路及部件。應瞭解,半導體處理裝置亦可包括向上述製程腔提供其他反應源物質(例如反應物或前驅體)之相關氣體管路及部件,其可採用與圖1至圖3類似的結構。在一些實施例中,操作半導體處理裝置之方法可包括多個製程循環,每一製程循環包括:前驅體注入階段、前驅體淨化階段、反應物注入階段及反應物淨化階段。應瞭解,該方法亦可包含其他階段或步驟(例如製程腔淨化等)。前驅體注入階段及前驅體淨化階段係藉由提供前驅體之相關氣體管路及部件來進行(例如,依照本文所描述之反應源物質注入階段及淨化階段之相關設定)。反應物注入階段及反應物淨化階段係藉由提供反應物之相關氣體管路及部件來進行(例如,依照本文所描述之反應源物質注入階段及淨化階段之相關設定)。因此,前驅體注入階段、前驅體淨化階段、反應物注入階段及反應物淨化階段不必順序地進行,某些階段前驅體與反應物相關作業可同時並列進行。Figures 1 to 3 only illustrate gas lines and components in a semiconductor processing apparatus that supply a vaporized reaction source material (e.g., a precursor or reactant) to a process chamber. It should be understood that the semiconductor processing apparatus may also include gas lines and components that supply other reaction source materials (e.g., reactants or precursors) to the aforementioned process chamber, which may employ a structure similar to that of Figures 1 to 3. In some embodiments, the method of operating the semiconductor processing apparatus may include multiple process cycles, each process cycle including: a precursor injection stage, a precursor purification stage, a reactant injection stage, and a reactant purification stage. It should be understood that the method may also include other stages or steps (e.g., process chamber purification). The precursor injection and precursor purification stages are performed by providing the relevant gas lines and components for the precursor (e.g., according to the settings for the reactant injection and purification stages described herein). The reactant injection and reactant purification stages are performed by providing the relevant gas lines and components for the reactants (e.g., according to the settings for the reactant injection and purification stages described herein). Therefore, the precursor injection, precursor purification, reactant injection, and reactant purification stages do not necessarily have to be performed sequentially; some precursor and reactant-related operations can be performed simultaneously.
在一組對比實驗中,藉由使用汽化裝置汽化反應源物質(例如,前驅體)之方法(例如,結合附圖1至3中任一者描述之方法)與習知不使用汽化裝置之方法分別製備氧化鋯薄膜。實驗中兩種方法製備之氧化鋯薄膜之生長速率都約為0.83 Å/循環且厚度均勻性都約為98%,但是,習知方法中前驅體注入時間為4 s,而使用汽化裝置之方法中前驅體注入時間可縮短至1.5 s甚至更短。由此可見,根據本申請案之實施例的使用汽化裝置汽化反應源物質之沈積方法可使液態源汽化後之蒸汽具備較高的溫度,此不僅可有效縮短吸附時間,亦能縮短吹掃時間,在保證薄膜品質的同時,並進一步縮短循環週期,從而提高前驅體之有效利用率,降低沈積成本。In a set of comparative experiments, zirconia films were prepared by a method using a vaporization device to vaporize the reaction source material (e.g., a precursor) (e.g., the method described in conjunction with any of Figures 1 to 3) and a conventional method without a vaporization device. In the experiments, the zirconia films prepared by both methods showed a growth rate of approximately 0.83 Å/cycle and a thickness uniformity of approximately 98%. However, the precursor injection time in the conventional method was 4 s, while the precursor injection time in the method using the vaporization device could be reduced to 1.5 s or even less. Therefore, the deposition method of vaporizing the source material using a vaporization device according to the embodiment of this application can make the vapor after vaporization of the liquid source have a higher temperature. This can not only effectively shorten the adsorption time, but also shorten the purging time. While ensuring the quality of the film, it can further shorten the cycle, thereby improving the effective utilization rate of the precursor and reducing the deposition cost.
圖4示出採用根據本申請案之實施例之半導體處理裝置在凹槽中沈積薄膜後用掃描電子顯微鏡拍攝的凹槽剖面圖。圖5A至圖5C分別示出圖4中位於凹槽之不同位置處之薄膜的部分放大圖。具體而言,圖5A示出圖4中位於凹槽頂部1之薄膜的部分放大圖,圖5B示出圖4中位於凹槽側壁2之薄膜的部分放大圖,圖5C示出圖4中位於凹槽底部3之薄膜的部分放大圖。圖5A至圖5C顯示位於凹槽頂部1之薄膜之厚度為56.5 nm,位於凹槽側壁2之薄膜之厚度為54.2 nm,位於凹槽底部3之薄膜之厚度為55.1 nm。可見,位於凹槽之不同位置處之薄膜之厚度基本相近。因此,薄膜基本上均勻地形成在凹槽之頂部、側壁及底部上,具有較高的保型性。Figure 4 shows a cross-sectional view of the groove after a thin film has been deposited in the groove using a semiconductor processing apparatus according to an embodiment of this application, taken with a scanning electron microscope. Figures 5A to 5C show enlarged views of the thin film at different locations in the groove of Figure 4. Specifically, Figure 5A shows an enlarged view of the thin film at the top 1 of the groove in Figure 4, Figure 5B shows an enlarged view of the thin film at the sidewall 2 of the groove in Figure 4, and Figure 5C shows an enlarged view of the thin film at the bottom 3 of the groove in Figure 4. Figures 5A to 5C show that the thickness of the thin film at the top 1 of the groove is 56.5 nm, the thickness of the thin film at the sidewall 2 of the groove is 54.2 nm, and the thickness of the thin film at the bottom 3 of the groove is 55.1 nm. It can be seen that the thickness of the thin film at different locations in the groove is basically similar. Therefore, the film is formed basically uniformly on the top, sidewalls and bottom of the groove, and has high shape retention.
下表示出圖4中之凹槽之深寬比以及位於凹槽之側壁及底部之薄膜之台階覆蓋率。如下表所示,採用本申請案之實施例之半導體處理裝置對深寬比為10:1之深凹槽沈積薄膜,凹槽側壁具有95.9%之台階覆蓋率(側壁薄膜厚度/頂部薄膜厚度),且凹槽底部具有97.5%之台階覆蓋率(底部薄膜厚度/頂部薄膜厚度)。
由此可見,採用本申請案提供之裝置及方法可提高沈積薄膜之生長速率、厚度均勻性及保型性。Therefore, the apparatus and method provided in this application can improve the growth rate, thickness uniformity and shape retention of the deposited film.
本說明書中之描述經提供以使熟習此項技術者能夠進行或使用本申請案之技術方案。熟習此項技術者將易於顯而易見對本申請案之各種修改,且本說明書中所定義之一般原理可應用於其他變化形式而不會脫離本申請案之精神或範疇。因此,本申請案不限於本說明書所述之實例及設計,而是被賦予與本說明書所揭示之原理及新穎特徵一致的最寬範疇。The descriptions in this specification are provided to enable those skilled in the art to perform or use the technical solutions of this application. Those skilled in the art will readily see various modifications to this application, and the general principles defined in this specification can be applied to other variations without departing from the spirit or scope of this application. Therefore, this application is not limited to the examples and designs described in this specification, but is given the widest scope consistent with the principles and novel features disclosed in this specification.
1:製程腔 2:汽化裝置 3:氣體管線 4:第一管線 5:第一氣體源 6:反應源物質槽 7:第一支管線 8:第二支管線 9:支路 10:真空泵 11:第二氣體源 12:第二管線 12a:第二管線 12b:第二管線 31:第五閥 41:第一閥 42:第二閥 71:第三閥 81:第四閥 91:排氣閥 100:半導體處理裝置 200:半導體處理裝置 300:半導體處理裝置 1: Process Chamber 2: Vaporization Device 3: Gas Pipeline 4: First Pipeline 5: First Gas Source 6: Reaction Source Material Tank 7: First Branch Pipeline 8: Second Branch Pipeline 9: Branch Line 10: Vacuum Pump 11: Second Gas Source 12: Second Pipeline 12a: Second Pipeline 12b: Second Pipeline 31: Fifth Valve 41: First Valve 42: Second Valve 71: Third Valve 81: Fourth Valve 91: Exhaust Valve 100: Semiconductor Processing Device 200: Semiconductor Processing Device 300: Semiconductor Processing Device
本說明書中之揭示內容提及且包含以下各圖: 圖1為根據本申請案之實施例之半導體處理裝置的結構示意圖; 圖2為根據本申請案之又一實施例之半導體處理裝置的結構示意圖; 圖3為根據本申請案之另一實施例之半導體處理裝置的結構示意圖; 圖4示出採用根據本申請案之實施例之半導體處理裝置在凹槽中沈積薄膜後用掃描電子顯微鏡拍攝的凹槽剖面圖; 圖5A示出圖4中位於凹槽頂部之薄膜的部分放大圖; 圖5B示出圖4中位於凹槽側壁之薄膜的部分放大圖;且 圖5C示出圖4中位於凹槽底部之薄膜的部分放大圖。 The disclosure in this specification mentions and includes the following figures: Figure 1 is a schematic structural diagram of a semiconductor processing apparatus according to an embodiment of this application; Figure 2 is a schematic structural diagram of a semiconductor processing apparatus according to yet another embodiment of this application; Figure 3 is a schematic structural diagram of a semiconductor processing apparatus according to yet another embodiment of this application; Figure 4 shows a cross-sectional view of the groove after a thin film has been deposited in the groove using the semiconductor processing apparatus according to an embodiment of this application, taken with a scanning electron microscope; Figure 5A shows a partially enlarged view of the thin film located at the top of the groove in Figure 4; Figure 5B shows a partially enlarged view of the thin film located on the side wall of the groove in Figure 4; and Figure 5C shows a partially enlarged view of the thin film located at the bottom of the groove in Figure 4.
根據慣例,圖示中所繪示之各種特徵可能並非按比例繪製。因此,為了清晰起見,可能任意擴大或減小各種特徵之尺寸。圖示中所繪示之各部件之形狀僅為例示性形狀,並非限定部件之實際形狀。另外,為了清楚起見,可能簡化圖示中所繪示之實施方案。因此,圖示可能並未繪示給定設備或裝置之全部組件。最後,可貫穿說明書及圖示使用相同參考標號來表示相同特徵。As is customary, the features depicted in the illustrations may not be drawn to scale. Therefore, for clarity, the dimensions of various features may be arbitrarily enlarged or reduced. The shapes of the components depicted in the illustrations are merely illustrative and do not limit the actual shapes of the components. Furthermore, for clarity, the embodiments depicted in the illustrations may be simplified. Therefore, the illustrations may not show all components of a given device or apparatus. Finally, the same reference numerals may be used throughout the manual and illustrations to represent the same features.
1:製程腔 1: Manufacturing Cavity
2:汽化裝置 2: Vaporization device
3:氣體管線 3: Gas pipelines
4:第一管線 4: First Pipeline
5:第一氣體源 5: First gas source
6:反應源物質槽 6: Reaction Source Material Tank
7:第一支管線 7: First branch pipeline
8:第二支管線 8: Second branch pipeline
9:支路 9: Side Road
10:真空泵 10: Vacuum Pump
11:第二氣體源 11: Second gas source
12:第二管線 12: Second Pipeline
31:第五閥 31: The Fifth Valve
41:第一閥 41: First Valve
42:第二閥 42: Second valve
71:第三閥 71: The Third Valve
81:第四閥 81: Fourth Valve
91:排氣閥 91: Exhaust valve
100:半導體處理裝置 100: Semiconductor Processing Device
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| US6098964A (en) * | 1997-09-12 | 2000-08-08 | Applied Materials, Inc. | Method and apparatus for monitoring the condition of a vaporizer for generating liquid chemical vapor |
| US20060032444A1 (en) * | 2004-08-10 | 2006-02-16 | Tokyo Electron Limited | Film forming apparatus and film forming method |
| US20170056912A1 (en) * | 2014-05-09 | 2017-03-02 | Korea Institute Of Industrial Technology | Liquid precursor delivery system |
| TW201843343A (en) * | 2017-03-16 | 2018-12-16 | 美商蘭姆研究公司 | Flow monitoring system and method in substrate processing system pre-discharge vapor supply system |
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| US6204204B1 (en) * | 1999-04-01 | 2001-03-20 | Cvc Products, Inc. | Method and apparatus for depositing tantalum-based thin films with organmetallic precursor |
| TWI277140B (en) * | 2002-07-12 | 2007-03-21 | Asm Int | Method and apparatus for the pulse-wise supply of a vaporized liquid reactant |
| JP5121196B2 (en) * | 2006-09-15 | 2013-01-16 | 株式会社Adeka | Metal alkoxide compound, raw material for thin film formation, and method for producing thin film |
| CN103688339B (en) * | 2011-07-22 | 2016-09-28 | 应用材料公司 | Reactant Delivery Systems for ALD/CVD Processes |
| WO2022026271A1 (en) * | 2020-07-29 | 2022-02-03 | Lam Research Corporation | Concentration control using a bubbler |
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| US6098964A (en) * | 1997-09-12 | 2000-08-08 | Applied Materials, Inc. | Method and apparatus for monitoring the condition of a vaporizer for generating liquid chemical vapor |
| US20060032444A1 (en) * | 2004-08-10 | 2006-02-16 | Tokyo Electron Limited | Film forming apparatus and film forming method |
| US20170056912A1 (en) * | 2014-05-09 | 2017-03-02 | Korea Institute Of Industrial Technology | Liquid precursor delivery system |
| TW201843343A (en) * | 2017-03-16 | 2018-12-16 | 美商蘭姆研究公司 | Flow monitoring system and method in substrate processing system pre-discharge vapor supply system |
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