TWI576461B - Thin film deposition method - Google Patents

Thin film deposition method Download PDF

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TWI576461B
TWI576461B TW101102404A TW101102404A TWI576461B TW I576461 B TWI576461 B TW I576461B TW 101102404 A TW101102404 A TW 101102404A TW 101102404 A TW101102404 A TW 101102404A TW I576461 B TWI576461 B TW I576461B
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gas
thin film
substrate supporting
film deposition
supporting portion
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TW201231714A (en
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Young-Hoon Park
Won-Jun Yoon
Ki-Hoon Lee
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Wonik Ips Co Ltd
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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]
    • C23C16/45544Atomic layer deposition [ALD] characterized by the apparatus
    • C23C16/45548Atomic layer deposition [ALD] characterized by the apparatus having arrangements for gas injection at different locations of the reactor for each ALD half-reaction
    • C23C16/45551Atomic layer deposition [ALD] characterized by the apparatus having arrangements for gas injection at different locations of the reactor for each ALD half-reaction for relative movement of the substrate and the gas injectors or half-reaction reactor compartments

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  • Chemical Vapour Deposition (AREA)
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Description

薄膜沉積方法Thin film deposition method

本發明涉及一種半導體製造製程中沉積薄膜的方法,更詳細說是涉及一種藉由一次製程在複數個基板沉積薄膜的方法。The present invention relates to a method of depositing a thin film in a semiconductor fabrication process, and more particularly to a method of depositing a thin film on a plurality of substrates by a single process.

在薄膜製造製程中,隨著半導體元件的設計規則(design rule)逐漸達到物理極限值的程度的超細微化,為了更加提高薄膜的物理性質,研究有原子層沉積法(automic layer deposition,ALD)或循環化學氣相沉積法(cyclic chemical vapor deposition,cyclic CVD)。In the film manufacturing process, as the design rule of the semiconductor component gradually reaches the level of physical limit, in order to further improve the physical properties of the film, an atomic layer deposition (ALD) method is studied. Or cyclic chemical vapor deposition (cyclic CVD).

ALD的原理如下。第一原料氣體當以蒸汽狀態供給到反應器內時,藉由與基板表面的反應而發生單原子層的化學吸附。當表面得到飽和時,單原子層以上的第一原料氣體因相同的配位體(ligand)之間的非反應性而處於物理吸附狀態。該物理吸附狀態的第一原料氣體被吹掃氣體(purge gas)去除。當該第一層被供給第二原料氣體時,藉由配位體相互之間置換反應而使第二層成長,未能與第一層反應的第二原料氣體處於物理吸附狀態,從而被吹掃氣體去除。另外,該第二層的表面處於與第一原料氣體進行反應的狀態。這構成一個循環,反復進行多次循環而沉積薄膜。The principle of ALD is as follows. When the first material gas is supplied into the reactor in a vapor state, chemical adsorption of the monoatomic layer occurs by reaction with the surface of the substrate. When the surface is saturated, the first material gas above the monoatomic layer is in a physically adsorbed state due to non-reactivity between the same ligands. The first material gas in the physically adsorbed state is removed by a purge gas. When the first layer is supplied with the second material gas, the second layer is grown by the displacement reaction between the ligands, and the second material gas that has not reacted with the first layer is in a physical adsorption state, thereby being blown Sweep gas removal. Further, the surface of the second layer is in a state of being reacted with the first material gas. This constitutes a cycle in which a plurality of cycles are repeated to deposit a film.

為了在反應器內維持穩定的ALD反應,需要將第一原料氣體和第二原料氣體以分離的方式供給到反應器內,以免在氣相下相互混合。當前一般的方法有,在安裝有噴頭的單晶片式(single)腔室中,將第一原料氣體和第二原料氣體的交互性噴射反復N次來進行ALD。為此,需要利用不同的氣體供給線(line),隔開時間間隔分別向反應器內供給第一原料氣體和第二原料氣體。另外,為了去除反應器內的殘留氣體,使用向第一原料氣體和第二原料氣體的供給過程之間另行供給吹掃氣體的方法。如上述,為了隔開時間間隔供給第一原料氣體、第二原料氣體及吹掃氣體,會利用閥門(valve)。In order to maintain a stable ALD reaction in the reactor, it is necessary to supply the first material gas and the second material gas to the reactor in a separated manner so as not to be mixed with each other in the gas phase. A current general method is to perform ALD by repeating the interactive ejection of the first material gas and the second material gas N times in a single-chamber chamber in which a shower head is mounted. To this end, it is necessary to supply the first material gas and the second material gas to the reactor separately at different time intervals using different gas supply lines. Further, in order to remove the residual gas in the reactor, a method of separately supplying a purge gas to the supply process of the first source gas and the second source gas is used. As described above, in order to supply the first material gas, the second material gas, and the purge gas at intervals, a valve is used.

閥門的複雜性和對閥門進行的頻繁操作,不僅縮短閥門的壽命,還增加裝備的維護費用,並且由於裝備維護造成的裝備的停機(shut down)時間增加,而造成生產率下降。並且,在以往的單晶片式薄膜沉積裝置中,在固定的加熱器(或是基座(susceptor))上放置基板,將ALD或循環CVD的單位循環反復N次來沉積所需厚度的薄膜。但是,在更加超細微化的元件圖案中,很難滿足所要求的階梯差覆蓋率(step coverage)或薄膜的純度,並且即使滿足了所要求的規格(spec),也由於沉積時間變長,不可避免較大的生產率損失。The complexity of the valve and the frequent operation of the valve not only shorten the life of the valve, but also increase the maintenance cost of the equipment, and the downtime of the equipment due to equipment maintenance increases, resulting in a decrease in productivity. Further, in the conventional single-wafer thin film deposition apparatus, a substrate is placed on a fixed heater (or a susceptor), and a unit cycle of ALD or cyclic CVD is repeated N times to deposit a film of a desired thickness. However, in a more ultra-fine component pattern, it is difficult to satisfy the required step coverage or the purity of the film, and even if the required specification is met, the deposition time becomes long. Inevitably a large loss of productivity.

本發明的目的在於,提供一種相比以往的ALD或循環CVD,能夠以更高的生產率沉積薄膜的薄膜沉積方法。An object of the present invention is to provide a thin film deposition method capable of depositing a thin film with higher productivity than conventional ALD or cyclic CVD.

為了達到上述目的,本發明所涉及的薄膜沉積方法利用一邊使氣體噴射部和基板支承部相對旋轉一邊沉積薄膜的薄膜沉積裝置來沉積薄膜。In order to achieve the above object, a thin film deposition method according to the present invention deposits a thin film by using a thin film deposition apparatus which deposits a thin film while rotating the gas ejecting portion and the substrate supporting portion.

本發明所涉及的薄膜沉積方法係利用一薄膜沉積裝置來沉積薄膜,該薄膜沉積裝置包括:一基板支承部,其具有供複數個基板放置的複數個基板放置部、以及一氣體噴射部,其設置於上述基板支承部的上部,將一種以上的氣體供給到該基板支承部上,該基板支承部和該氣體噴射部能夠相對旋轉進行設置;該薄膜沉積方法包括:步驟(a)在上述基板放置部放置複數個基板;步驟(b),一邊使上述基板支承部和氣體噴射部相對旋轉,一邊藉由該氣體噴射部將原料氣體及與該原料氣體進行反應之反應氣體供給到該基板支承部上,從而在基板上沉積薄膜;步驟(c),一邊使該基板支承部和該氣體噴射部相對旋轉,一邊藉由該氣體噴射部將惰性氣體供給到該基板支承部上,從而進行吹掃(purge);以及步驟(d),一邊使該基板支承部和該氣體噴射部相對旋轉,一邊藉由該氣體噴射部將後處理氣體供給到該基板支承部上,從而進行後處理。The thin film deposition method of the present invention utilizes a thin film deposition apparatus for depositing a thin film, the thin film deposition apparatus comprising: a substrate support portion having a plurality of substrate placement portions for a plurality of substrates, and a gas ejecting portion Provided on an upper portion of the substrate supporting portion, one or more gases are supplied to the substrate supporting portion, and the substrate supporting portion and the gas ejecting portion are relatively rotatable; the thin film deposition method includes: step (a) on the substrate a plurality of substrates are placed in the placing portion, and in step (b), the substrate supporting portion and the gas ejecting portion are relatively rotated, and the material gas and the reaction gas reacting with the material gas are supplied to the substrate by the gas ejecting portion. a film is deposited on the substrate, and in step (c), while the substrate supporting portion and the gas ejecting portion are relatively rotated, the inert gas is supplied to the substrate supporting portion by the gas ejecting portion, thereby blowing Purging; and step (d), while the substrate supporting portion and the gas ejecting portion are relatively rotated, The gas injection unit supplies the post-treatment gas to the substrate support portion to perform post-processing.

在本發明中,至少重複一次由上述步驟(b)至步驟(d)構成的循環,直至得到所需厚度的薄膜。In the present invention, the cycle consisting of the above steps (b) to (d) is repeated at least once until a film of a desired thickness is obtained.

該氣體噴射部和該基板支承部的相對旋轉指的是包含了如下情況的所有概念:在固定該氣體噴射部的狀態下使該基板支承部進行旋轉;相反地,在固定該基板支承部的狀態下使該氣體噴射部進行旋轉;並且,使該氣體噴射部和基板支承部都進行旋轉,此時包含以不同的速度按相同的方向進行旋轉或者按相反的方向進行旋轉的情況。在本發明中,特別是較佳地在固定該氣體噴射部的狀態下使該基板支承部進行旋轉,其理由在於系統的穩定性和效率性。因此,在較佳的實施例中,使該基板支承部進行旋轉,由此,在該步驟(a)和該步驟(b)之間,還包括使上述基板支承部的旋轉速度加速而達到規定RPM的步驟。The relative rotation of the gas ejecting portion and the substrate supporting portion refers to all the concepts including rotating the substrate supporting portion in a state where the gas ejecting portion is fixed; and conversely, fixing the substrate supporting portion In this state, the gas injection unit is rotated; and both the gas injection unit and the substrate support unit are rotated, and in this case, the rotation is performed in the same direction at different speeds or in the opposite direction. In the present invention, in particular, it is preferable to rotate the substrate supporting portion in a state in which the gas ejecting portion is fixed, which is due to stability and efficiency of the system. Therefore, in a preferred embodiment, the substrate supporting portion is rotated, thereby further comprising, between the step (a) and the step (b), accelerating the rotation speed of the substrate supporting portion to a predetermined value. The steps of the RPM.

該沉積薄膜的步驟(b)按CVD方式進行或是按ALD方式進行。在按CVD方式進行的情況下,該氣體噴射部構成為,該氣體噴射部由複數個氣體供給器以放射形配置而成,該等氣體供給器的至少其中之一是用於同時供給原料氣體和反應氣體的製程氣體供給器,該等氣體供給器的至少其中之一的是用於供給惰性氣體的吹掃氣體供給器。在此情況下,上述步驟(b)構成為,在供給原料氣體和反應氣體及惰性氣體的狀態下,使基板以連續地經由製程氣體供給器和吹掃氣體供給器之下方的方式進行。另外,上述步驟(c)構成為,在中斷原料氣體和反應氣體的供給的狀態下,使基板以連續地經由製程氣體供給器和吹掃氣體供給器之下方的方式進行。並且,上述步驟(d)構成為,在中斷原料氣體的供給的狀態下,使基板以連續地經由製程氣體供給器和吹掃氣體供給器之下方的方式進行。這是後處理氣體與上述反應氣體相同時的情況。The step (b) of depositing the film is performed by CVD or by ALD. In the case of performing the CVD method, the gas injection unit is configured such that the gas injection unit is radially disposed by a plurality of gas supply units, and at least one of the gas supply units is for simultaneously supplying the material gas. And a process gas supplier for the reaction gas, at least one of which is a purge gas supplier for supplying an inert gas. In this case, the above step (b) is configured such that the substrate is continuously passed through the process gas supplier and the purge gas supplier in a state where the source gas, the reaction gas, and the inert gas are supplied. Further, in the above step (c), the substrate is continuously passed through the process gas supplier and the purge gas supplier while the supply of the material gas and the reaction gas is interrupted. Further, in the above step (d), the substrate is continuously passed through the process gas supplier and the purge gas supplier while the supply of the material gas is interrupted. This is the case when the post-treatment gas is the same as the above-described reaction gas.

在按ALD方式進行的情況下,上述氣體噴射部構成為,該氣體噴射部由複數個氣體供給器以放射形配置而成,該等的氣體供給器的至少其中之一是用於供給上述原料氣體的原料氣體供給器,另該等氣體供給器的至少其中之一是用於供給上述反應氣體的反應氣體供給器,又該等的氣體供給器的至少其中之一是用於供給上述惰性氣體的吹掃氣體供給器。In the case of performing the ALD method, the gas injection unit is configured such that the gas injection unit is radially disposed by a plurality of gas supply units, and at least one of the gas supply units is for supplying the raw material. a raw material gas supply device of the gas, and at least one of the gas supply devices is a reaction gas supply device for supplying the reaction gas, and at least one of the gas supply devices is for supplying the inert gas Purge gas supply.

此時,上述步驟(b)構成為,在供給原料氣體和反應氣體及惰性氣體的狀態下,使基板以連續地經由上述原料氣體供給器、吹掃氣體供給器、反應氣體供給器,以及另一個吹掃氣體供給器下方的方式進行。另外,上述步驟(c)構成為,在中斷原料氣體和反應氣體的供給的狀態下,使基板以連續地經由上述原料氣體供給器、吹掃氣體供給器、反應氣體供給器,以及另一個吹掃氣體供給器下方的方式進行。並且,上述步驟(d)構成為,在中斷原料氣體的供給的狀態下,使基板連續地經由原料氣體供給器、吹掃氣體供給器、反應氣體供給器,以及另一個吹掃氣體供給器下方的方式進行。In this case, the step (b) is configured such that the substrate is continuously supplied through the material gas supplier, the purge gas supplier, the reaction gas supplier, and the like while supplying the material gas, the reaction gas, and the inert gas. A purge gas supply is carried out underneath. Further, in the above step (c), the substrate is continuously blown through the material gas supplier, the purge gas supplier, the reaction gas supplier, and the other while the supply of the material gas and the reaction gas is interrupted. Scan the way below the gas supply. Further, in the above step (d), the substrate is continuously passed through the material gas supplier, the purge gas supplier, the reaction gas supplier, and the other purge gas supplier while the supply of the material gas is interrupted. The way to proceed.

較佳地,原料氣體供給器和反應氣體供給器分別以氣體噴射部的中心為基準對稱地進行配置。另外,較佳地,吹掃氣體供給器對應每個原料氣體供給器和反應氣體供給器之間地進行配置。Preferably, the material gas supplier and the reaction gas supplier are arranged symmetrically with respect to the center of the gas injection portion, respectively. Further, preferably, the purge gas supplier is disposed between each of the material gas supplier and the reaction gas supplier.

藉由該薄膜沉積方法,能夠沉積單原子金屬薄膜、金屬氮化物薄膜及金屬氧化物薄膜中的至少一種。上述單原子金屬薄膜的例有鉭(Ta)、鈦(Ti)、鎢(W)等,上述金屬氮化物薄膜的例有作為它們的氮化物的氮化鉭(TaN)、氮化鈦(TiN)、氮化鎢(WN)等。並且,金屬氧化物薄膜的例有矽氧化物、氧化鋯(ZrO)等。當然,在使用兩種以上的原料氣體的情況下,也能夠形成二元金屬薄膜、其氮化物薄膜及氧化物薄膜。例如,在按CVD方式構成的情況下,兩種以上的原料氣體可以基於藉由一個製程氣體供給器同時供給的方式。在此情況下,製程氣體供給器構成為,使兩種以上的原料氣體不在製程氣體供給器內相互混合而噴射到處理空間內。另外,在按ALD方式構成的情況下,兩種以上的原料氣體可以基於藉由一個原料氣體供給器,或是藉由相互不同的原料氣體供給器來隨著上述基板的旋轉依次地供給到上述基板上的方式。也就是,在本發明的範圍內,只要能夠沉積單原子金屬薄膜、金屬氮化物薄膜或金屬氧化物薄膜,就當然能夠藉由氣體噴射部的變更來形成二元或其以上的金屬薄膜、其氮化物薄膜及氧化物薄膜。At least one of a monoatomic metal thin film, a metal nitride thin film, and a metal oxide thin film can be deposited by the thin film deposition method. Examples of the above-mentioned monoatomic metal thin film include tantalum (Ta), titanium (Ti), tungsten (W), etc., and examples of the above metal nitride thin film include tantalum nitride (TaN) and titanium nitride (TiN) as their nitrides. ), tungsten nitride (WN), and the like. Further, examples of the metal oxide thin film include cerium oxide, zirconium oxide (ZrO), and the like. Of course, when two or more kinds of source gases are used, a binary metal thin film, a nitride thin film, and an oxide thin film can be formed. For example, in the case of the CVD method, two or more kinds of material gases may be supplied simultaneously by one process gas supplier. In this case, the process gas supplier is configured such that two or more kinds of material gases are mixed with each other in the process gas supplier and injected into the processing space. Further, in the case of the ALD method, two or more kinds of material gases may be sequentially supplied to the above-mentioned substrate by rotation of the substrate by one source gas supplier or by different material gas suppliers. The way on the substrate. That is, within the scope of the present invention, as long as a monoatomic metal thin film, a metal nitride thin film or a metal oxide thin film can be deposited, it is naturally possible to form a binary or more metal thin film by changing the gas ejecting portion, Nitride film and oxide film.

上述惰性氣體是氬氣(Ar)或氮氣(N2)。較佳地,上述後處理氣體是包含氮元素的氮化氣體及包含氧氣的氧化氣體中的至少一種。此時,如果上述反應氣體和上述後處理氣體利用相同的氣體,則能夠沉積金屬氮化物薄膜或金屬氧化物薄膜。The above inert gas is argon (Ar) or nitrogen (N2). Preferably, the post-treatment gas is at least one of a nitriding gas containing nitrogen and an oxidizing gas containing oxygen. At this time, if the same gas is used for the reaction gas and the post-treatment gas, a metal nitride film or a metal oxide film can be deposited.

較佳地,上述複數個基板以上述基板支承部的中心為基準對稱地進行放置,以去除不同基板的差異而實現均勻性。Preferably, the plurality of substrates are placed symmetrically with respect to the center of the substrate supporting portion to remove the difference between the different substrates to achieve uniformity.

在以往,在單晶片式腔室中實現作為改進CVD的缺點的製程方法的ALD或循環CVD時,不可避免地產生較大的生產率損失。作為能夠克服該生產率損失的方法,除了一次同時地沉積多片基板的批次(batch)形式的沉積方法以外,未提出其他方法,由於能夠適用爐(furnace)的製程極其有限,作為具有通融性且容易調節製程的裝置,小批次(mini-batch)形式較為適當。In the past, when ALD or cyclic CVD which is a process method for improving the defects of CVD is realized in a single-wafer type chamber, a large productivity loss is inevitably caused. As a method capable of overcoming this loss of productivity, in addition to a deposition method in the form of a batch in which a plurality of substrates are simultaneously deposited, no other method has been proposed, and since the process capable of applying a furnace is extremely limited, it is as a passability. And the device is easy to adjust the process, and the mini-batch form is more appropriate.

在本發明中,為了解決生產率問題,將複數個基板放置於旋轉的基板支承部上,藉由位於基板的上部面的氣體噴射部噴射原料氣體及反應氣體等製程氣體及惰性氣體的同時沉積薄膜。並且,該方法能夠將薄膜的品質及生產率提高至以往的ALD或循環CVD無法達到的水準。In the present invention, in order to solve the problem of productivity, a plurality of substrates are placed on a rotating substrate supporting portion, and a film is deposited while spraying a process gas such as a source gas and a reactive gas and an inert gas through a gas injection portion located on the upper surface of the substrate. . Moreover, this method can improve the quality and productivity of the film to a level that cannot be achieved by conventional ALD or cyclic CVD.

本發明所涉及的薄膜沉積方法,不僅能夠一次性處理複數個基板,而且是與批次形式不同的方式,因此在沉積金屬薄膜等電阻值低的薄膜時,能夠防止基板的後表面也被沉積,與只處理一張基板的現有技術的單晶片式比較時,能夠以高生產率進行沉積。The thin film deposition method according to the present invention can not only process a plurality of substrates at a time but also be different from the batch form, so that when a film having a low resistance such as a metal film is deposited, the rear surface of the substrate can be prevented from being deposited. When compared with the prior art single wafer type in which only one substrate is processed, deposition can be performed with high productivity.

以下,參照所附的附圖,對本發明的較佳實施例進行詳細說明。然而,本發明並不侷限於以下所揭示的實施例,還能夠以相互不同的多種方式實現,本實施例只是用於完整地揭示本發明,是為了向本領域的技術人員完整地告知本發明的範疇而提供的。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. However, the present invention is not limited to the embodiments disclosed below, and can be implemented in various ways that are different from each other. This embodiment is only for fully revealing the present invention, and is intended to fully inform the present invention to those skilled in the art. The scope provided.

以往的ALD或循環CVD由於是藉由操作閥門來實現氣體供給的方式,所以不僅製程複雜、閥門的頻繁操作引起閥門的壽命縮短,而且裝備的維護費用增加。為了改善這種缺陷,本發明利用無需操作閥門便能實現ALD或循環CVD的薄膜沉積裝置。這種薄膜沉積裝置的簡要結構示於第1圖。第2圖為第1圖II-II線的剖視圖,是本發明第一實施例所涉及的結構。In the conventional ALD or cyclic CVD, since the gas supply is realized by operating the valve, not only the process is complicated, the valve operation is shortened due to frequent operation of the valve, and the maintenance cost of the equipment is increased. In order to improve such defects, the present invention utilizes a thin film deposition apparatus which can realize ALD or cyclic CVD without operating a valve. A schematic structure of such a thin film deposition apparatus is shown in Fig. 1. Fig. 2 is a cross-sectional view taken along line II-II of Fig. 1 and is a configuration according to the first embodiment of the present invention.

參照第1圖及第2圖,薄膜沉積裝置100具備有反應器110、基板支承部120及氣體噴射部130。Referring to FIGS. 1 and 2 , the thin film deposition apparatus 100 includes a reactor 110 , a substrate supporting unit 120 , and a gas injection unit 130 .

反應器110具備底部111、外壁部112及上側板113。底部111形成反應器110的下表面,外壁部112從底部111的邊緣沿著上方垂直延長而形成為封閉曲面形狀。另外,在外壁部112形成有供基板出入的基板移送通路(未圖示)。上側板113形成反應器110的上表面,能夠分離地結合於外壁部112的上表面。當上側板113結合於外壁部112的上表面時,在反應器110內部形成規定的空間,尤其沿著基板支承部120的上方在基板支承部120和氣體噴射部130之間形成薄膜沉積空間140。在上側板113的下表面和外壁部112的上表面之間夾裝O環(O-ring)(未圖示)等封閉部件。另外,在底部111或外壁部112形成有用於排出殘留在反應器110的內部的不必要氣體及微粒(particle)的排氣口(圖面未圖示)。The reactor 110 includes a bottom portion 111, an outer wall portion 112, and an upper side plate 113. The bottom portion 111 forms the lower surface of the reactor 110, and the outer wall portion 112 is vertically elongated from the edge of the bottom portion 111 to form a closed curved shape. Further, a substrate transfer path (not shown) through which the substrate enters and exits is formed in the outer wall portion 112. The upper side plate 113 forms the upper surface of the reactor 110 and is detachably coupled to the upper surface of the outer wall portion 112. When the upper side plate 113 is coupled to the upper surface of the outer wall portion 112, a predetermined space is formed inside the reactor 110, and a thin film deposition space 140 is formed between the substrate supporting portion 120 and the gas ejecting portion 130, particularly along the upper side of the substrate supporting portion 120. . A closing member such as an O-ring (not shown) is interposed between the lower surface of the upper side plate 113 and the upper surface of the outer wall portion 112. Further, an exhaust port (not shown) for discharging unnecessary gas and particles remaining inside the reactor 110 is formed in the bottom portion 111 or the outer wall portion 112.

基板支承部120設置於反應器110內部,並且具備基座121、基板放置部122、軸123及加熱器(未圖示)。基座121以圓盤形狀能夠旋轉地設置在反應器110的內部。在基座121的上表面形成有兩個以上的複數個基板放置部122,本實施例所舉例子為6個的情況。基板放置部122沿著基板支承部120上表面的周向配置,在各基板放置部122放置有基板W1~W6。軸123的兩端部中的一端部與基座121的下表面結合,另一端部貫通反應器110而與例如電機(未圖示)等旋轉驅動單元連接。由此,隨著軸123的旋轉,基座121以第1圖所示的旋轉中心軸A為中心進行旋轉。並且,軸123與能夠使基座121升降的升降驅動單元連接。作為升降驅動單元的例如有電機及齒輪組裝體(未圖示)等。加熱器(未圖示)設置於基座121的下部,來調節基板W1~W6的溫度。較佳地,基板W1~W6以基板支承部120的中心為基準對稱地進行放置,以消除不同基板的差異而實現均勻性。The substrate supporting portion 120 is provided inside the reactor 110 and includes a susceptor 121, a substrate placing portion 122, a shaft 123, and a heater (not shown). The susceptor 121 is rotatably disposed inside the reactor 110 in the shape of a disk. Two or more plural substrate placement portions 122 are formed on the upper surface of the susceptor 121, and the number of examples in the present embodiment is six. The substrate placement portion 122 is disposed along the circumferential direction of the upper surface of the substrate support portion 120, and the substrates W1 to W6 are placed on the respective substrate placement portions 122. One end of both ends of the shaft 123 is coupled to the lower surface of the susceptor 121, and the other end thereof passes through the reactor 110 and is connected to a rotary drive unit such as a motor (not shown). Thereby, the susceptor 121 rotates around the rotation center axis A shown in FIG. 1 as the shaft 123 rotates. Further, the shaft 123 is connected to a lifting drive unit that can raise and lower the susceptor 121. Examples of the elevation drive unit include a motor and a gear assembly (not shown). A heater (not shown) is provided at a lower portion of the susceptor 121 to adjust the temperatures of the substrates W1 to W6. Preferably, the substrates W1 to W6 are placed symmetrically with respect to the center of the substrate supporting portion 120 to eliminate the difference between the different substrates to achieve uniformity.

氣體噴射部130結合於設置在基板支承部120的上方的上側板113,並具備氣體供給器151、152、154、155。氣體供給器151、152、154沿著上側板113的周向按放射形進行配置,其數量及位置關係等可進變更。氣體供給器155是藉由基板支承部120的中央部分供給吹掃氣體以防止與未反應的氣體混合的裝置,起到噴頭的作用,並在板上形成有孔。The gas injection portion 130 is coupled to the upper side plate 113 provided above the substrate support portion 120, and includes gas suppliers 151, 152, 154, and 155. The gas feeders 151, 152, and 154 are radially arranged along the circumferential direction of the upper side plate 113, and the number, positional relationship, and the like can be changed. The gas supplier 155 is a device that supplies a purge gas through a central portion of the substrate support portion 120 to prevent mixing with unreacted gas, functions as a shower head, and has a hole formed in the plate.

氣體供給器151、152、153、154、155在按照不同區域供給不同氣體的情況下,放置於基座121的基板W1~W6旋轉的同時經由氣體供給器151、152、154、155的下方,而這些氣體供給器接觸各自的氣體。在對基板支承部120的旋轉進行控制的情況下,能夠調節基板W1~W6與各自的氣體接觸的時間,並且,藉由調節轉速能夠控制所需厚度的薄膜。When the gas suppliers 151, 152, 153, 154, and 155 supply different gases in different regions, the substrates W1 to W6 placed on the susceptor 121 rotate while passing through the lower portions of the gas suppliers 151, 152, 154, and 155. These gas feeders are in contact with the respective gases. When the rotation of the substrate supporting portion 120 is controlled, the time during which the substrates W1 to W6 are in contact with the respective gases can be adjusted, and the film of a desired thickness can be controlled by adjusting the number of rotations.

在本實施例中,氣體供給器151、152、154、155根據所供給的氣體的種類劃分為:原料氣體供給器151,用於將前體(precursor)等原料氣體供給到基板支承部120上;反應氣體供給器152,用於將與前體的中心元素進行反應而產生反應物的反應氣體供給到基板支承部120上;吹掃氣體供給器154、155,用於將惰性氣體供給到基板支承部120上。In the present embodiment, the gas suppliers 151, 152, 154, and 155 are divided into a material gas supplier 151 for supplying a material gas such as a precursor to the substrate supporting portion 120, depending on the type of the supplied gas. a reaction gas supplier 152 for supplying a reaction gas which reacts with a central element of the precursor to generate a reactant to the substrate supporting portion 120; and a purge gas supplier 154, 155 for supplying an inert gas to the substrate On the support portion 120.

如第2圖所示,將形狀和大小相同的模組單位概念的單元、在本實施例中將十個單元沿著上側板113的周向進配置,並且組合兩個以上、例如三個相鄰的單元來構成一個原料氣體供給器151,組合四個來構成一個反應氣體供給器152。接連排列有多個供給氣體的單位單元,或在供給氣體的單位單元之間配置有吹掃氣體供給器的情況下,也能將這些視作一個組,而定義為一個氣體供給器。並且,在原料氣體為兩種以上的情況下,可以包括兩個以上原料氣體供給器。相同地,反應氣體供給器也可以是兩個以上。As shown in FIG. 2, the unit of the module unit concept having the same shape and size, in the present embodiment, ten units are arranged along the circumferential direction of the upper side plate 113, and two or more, for example, three adjacent ones are combined. The unit constitutes one material gas supplier 151, and four are combined to constitute one reaction gas supplier 152. In the case where a plurality of unit cells for supplying gas are arranged in succession or when a purge gas supplier is disposed between unit units for supplying gas, these may be regarded as one group and defined as one gas supplier. Further, when two or more kinds of material gases are used, two or more material gas suppliers may be included. Similarly, the reaction gas supply device may be two or more.

原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154沿著上側板113的周向配置,在本實施例中,一個原料氣體供給器151和一個反應氣體供給器152相向配置,其之間都配置有吹掃氣體供給器154。吹掃氣體供給器154將用於吹掃前體及反應氣體等製程氣體的惰性氣體供給到基板支承部120上,使殘留在薄膜形成空間140中未反應的氣體排出到反應器110外部,從而使在基板支承部120上與未反應的氣體混合的情況最小化。The material gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154 are arranged along the circumferential direction of the upper side plate 113. In the present embodiment, one material gas supplier 151 and one reaction gas supplier 152 are disposed to face each other. A purge gas supplier 154 is disposed therebetween. The purge gas supplier 154 supplies an inert gas for purging a process gas such as a precursor and a reaction gas to the substrate support portion 120, and discharges unreacted gas remaining in the film formation space 140 to the outside of the reactor 110, thereby The case where the substrate support portion 120 is mixed with the unreacted gas is minimized.

如上所述,氣體噴射部130得到固定,且基板支承部120設置成能夠旋轉,從而當基板支承部120相對於氣體噴射部130相對旋轉時,放置於基板支承部120的基板W~W6依次地經由各個氣體供給器原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154的下方。此時,在基板W1而言,藉由原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154按原料氣體→惰性氣體→反應氣體→惰性氣體順序得到供給,從而實現ALD。As described above, the gas ejecting portion 130 is fixed, and the substrate supporting portion 120 is provided to be rotatable, so that when the substrate supporting portion 120 is relatively rotated with respect to the gas ejecting portion 130, the substrates W to W6 placed on the substrate supporting portion 120 are sequentially It passes through each of the gas supplier material gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154. At this time, in the substrate W1, the raw material gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154 are supplied in the order of the material gas → inert gas → reaction gas → inert gas, thereby realizing ALD.

由此,當利用第1圖中圖示出的薄膜沉積裝置100時,無需操作閥門便能實現ALD。並且,由於不僅能夠一次性處理複數個基板,而且是與批次形式不同的方式,因而在沉積金屬薄膜等電阻值低的薄膜時,無需擔心基板後表面遭到污染,並且與只能處理一張基板的以往的單晶片式比較時,能夠以更高的生產率進行沉積。Thus, when the thin film deposition apparatus 100 illustrated in Fig. 1 is utilized, ALD can be realized without operating the valve. Moreover, since not only a plurality of substrates can be processed at one time, but also in a different manner from the batch form, when depositing a film having a low resistance value such as a metal film, there is no need to worry about contamination of the rear surface of the substrate, and only one can be processed. When the conventional single wafer type comparison of the substrate is performed, deposition can be performed with higher productivity.

第3圖是利用第2圖的裝置結構的薄膜沉積方法的流程圖。Fig. 3 is a flow chart showing a thin film deposition method using the device structure of Fig. 2.

首先,參照第3圖的步驟S1,在基板放置部122放置複數個基板W1~W6。First, referring to step S1 of FIG. 3, a plurality of substrates W1 to W6 are placed on the substrate placement portion 122.

接著,使基板支承部120的旋轉速度加速達到規定RPM(步驟S2)。隨著基板支承部120旋轉,一邊使基板支承部120和氣體噴射部130相對旋轉,一邊藉由氣體噴射部130將原料氣體及反應氣體供給到基板支承部120上,從而在基板W1~W6上沉積薄膜(步驟S3)。該步驟藉由在原料氣體和反應氣體及惰性氣體供給到氣體噴射部130的狀態下基板W1~W6連續地經由原料氣體供給器151、吹掃氣體供給器154、反應氣體供給器152及另一吹掃氣體供給器154的下方來實現。基板W1~W6像這樣藉原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154按原料氣體→惰性氣體→反應氣體→惰性氣體的順序得到供給並實現ALD。藉由如上所述的ALD方式,例如使基板支承部120旋轉a次來沉積薄膜(例如,若以5 RPM旋轉四次則需要48 sec)。惰性氣體是氬氣(Ar)或氮氣(N2)。Next, the rotation speed of the substrate supporting portion 120 is accelerated to a predetermined RPM (step S2). When the substrate supporting portion 120 rotates, the substrate supporting portion 120 and the gas ejecting portion 130 are relatively rotated, and the source gas and the reaction gas are supplied to the substrate supporting portion 120 by the gas ejecting portion 130, thereby being on the substrates W1 to W6. A film is deposited (step S3). In this step, the substrates W1 to W6 are continuously passed through the material gas supplier 151, the purge gas supplier 154, the reaction gas supplier 152, and the other in a state where the material gas, the reaction gas, and the inert gas are supplied to the gas injection unit 130. This is accomplished by purging the gas supply 154 below. The substrates W1 to W6 are supplied by the material gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154 in the order of the material gas → inert gas → reaction gas → inert gas, and realize ALD. The film is deposited by, for example, the ALD method as described above, for example, by rotating the substrate supporting portion 120 a second time (for example, 48 sec is required if it is rotated four times at 5 RPM). The inert gas is argon (Ar) or nitrogen (N2).

藉由如上所述的薄膜沉積方法,能夠沉積單原子金屬薄膜、金屬氮化物薄膜或金屬氧化物薄膜。上述單原子金屬薄膜的例有鉭(Ta)、鈦(Ti)、鎢(W)等,上述金屬氮化物薄膜的例有作為它們的氮化物的氮化鉭(TaN)、氮化鈦(TiN)、氮化鎢(WN)等。並且,金屬氧化物薄膜的例有矽氧化物、氧化鋯(ZrO)等。當然,在使用兩種以上的原料氣體的情況下,也能夠形成二元金屬薄膜、其氮化物薄膜及氧化物薄膜。兩種以上的原料氣體可以基於藉由一個原料氣體供給器同時供給的方式,或是藉由相互不同的原料氣體供給器依次供給的方式。A single atom metal thin film, a metal nitride thin film or a metal oxide thin film can be deposited by the thin film deposition method as described above. Examples of the above-mentioned monoatomic metal thin film include tantalum (Ta), titanium (Ti), tungsten (W), etc., and examples of the above metal nitride thin film include tantalum nitride (TaN) and titanium nitride (TiN) as their nitrides. ), tungsten nitride (WN), and the like. Further, examples of the metal oxide thin film include cerium oxide, zirconium oxide (ZrO), and the like. Of course, when two or more kinds of source gases are used, a binary metal thin film, a nitride thin film, and an oxide thin film can be formed. The two or more kinds of material gases may be supplied in a manner of being simultaneously supplied by one material gas supplier or sequentially supplied from a material gas supplier different from each other.

接著,隨著基板支承部120旋轉,一邊使基板支承部120和氣體噴射部130相對旋轉,一邊藉由氣體噴射部130將惰性氣體供給到基板支承部120上,從而進行吹掃(步驟S4)。該步驟藉由在中斷原料氣體和反應氣體的供給並繼續供給惰性氣體的狀態下使基板W1~W6連續地經由原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154的下方來實現,例如,藉由使基板支承部120旋轉b次來實施。Then, the substrate supporting portion 120 and the gas ejecting portion 130 are rotated relative to each other while the substrate supporting portion 120 is rotated, and the inert gas is supplied to the substrate supporting portion 120 by the gas ejecting portion 130 to perform purging (step S4). . In this step, the substrates W1 to W6 are continuously passed through the source gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154 by interrupting the supply of the material gas and the reaction gas and continuing to supply the inert gas. This is achieved, for example, by rotating the substrate support portion 120 b times.

接著,隨著基板支承部120旋轉,一邊使基板支承部120和氣體噴射部130相對旋轉,一邊藉由氣體噴射部130將後處理氣體供給到基板處理部120上,從而進行後處理(步驟S5)。該步驟藉由在只中斷原料氣體的供給的狀態下供給反應氣體和惰性氣體並使基板W1~W6連續地經由原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154的下方來實現,例如,藉由使基板支承部120旋轉c次來實施。在沉積金屬氮化物薄膜的情況下,後處理氣體較佳為包含氮元素的氮化氣體,其可以是與反應氣體相同的氣體。在沉積金屬氧化物薄膜的情況下,後處理氣體較佳為包含氧元素的氧化氣體,其可以是與反應氣體相同的氣體。例如,作為含氧氣體可以使用氧氣、臭氧等氣體。Then, as the substrate supporting portion 120 rotates, the substrate supporting portion 120 and the gas ejecting portion 130 are relatively rotated, and the post-processing gas is supplied to the substrate processing portion 120 by the gas ejecting portion 130, thereby performing post-processing (step S5). ). In this step, the reaction gas and the inert gas are supplied while the supply of the material gas is interrupted, and the substrates W1 to W6 are continuously passed through the material gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154. This is achieved, for example, by rotating the substrate supporting portion 120 by c times. In the case of depositing a metal nitride thin film, the post-treatment gas is preferably a nitriding gas containing nitrogen, which may be the same gas as the reactive gas. In the case of depositing a metal oxide thin film, the post-treatment gas is preferably an oxidizing gas containing oxygen, which may be the same gas as the reactive gas. For example, as the oxygen-containing gas, a gas such as oxygen or ozone can be used.

至少重複一次由上述步驟S3至S5構成的循環,直至沉積所需厚度的薄膜(步驟S6)。The cycle consisting of the above steps S3 to S5 is repeated at least once until a film of a desired thickness is deposited (step S6).

在利用如上所述的裝置結構的薄膜沉積方法中,基本在基板W1~W6上將已形成薄膜的反應副產物氣體推動到基板W1~W6外側的所謂吹掃效率高。這是因為基板W1~W6進行旋轉,而不是出於靜止的狀態。In the thin film deposition method using the device structure as described above, the so-called purge efficiency in which the reaction by-product gas in which the thin film has been formed is pushed to the outside of the substrates W1 to W6 is substantially high on the substrates W1 to W6. This is because the substrates W1 to W6 are rotated instead of being in a stationary state.

例如,在旋轉a次來形成薄膜後,再接著為了使包含於薄膜內的雜質最小化而使用追加的方法,該方法是在作為薄膜沉積步驟的步驟S3以後,切斷(off)製程氣體,例如執行b次旋轉,只噴射惰性氣體的同時進行吹掃的步驟S4。再接著,為了去除前面的a次旋轉過程中成長的薄膜內雜質,噴射後處理氣體的同時在步驟S5期間旋轉c次。For example, after the film is formed by rotating a time, and then, in order to minimize the impurities contained in the film, an additional method is employed in which the process gas is turned off after the step S3 of the film deposition step. For example, step S4 is performed in which b-rotation is performed and only the inert gas is injected while purging. Next, in order to remove the impurities in the film which grew during the previous a-rotation, the post-process gas was ejected while rotating c times during the step S5.

利用該方法,能夠有效利用上述小批次形式的薄膜沉積裝置來使薄膜的品質更加極大化。即,在使ALD旋轉a次的同時使薄膜成長後,進行b次吹掃旋轉,在上述b次旋轉期間,使膜的旋轉停止,取而代之地藉由旋轉的離心力和惰性氣體的作用力,來將包含於膜內的反應副產物氣體順暢地排出到基板外側。特別是,實際上半導體元件圖案包括具有很深的縱橫比(aspect ratio)的孔(hole),隨著元件的超細微化,順暢地排出在上述孔內部產生的反應副產物氣體變得更加困難,同樣地,較難在確保優秀的階梯差覆蓋率的情況下,在孔內部各處位置進行沉積。With this method, the thin film deposition apparatus of the above-described small batch type can be effectively utilized to further maximize the quality of the film. In other words, after the ALD is rotated a time and the film is grown, b-sweep rotation is performed, and during the b-rotation, the rotation of the film is stopped, and instead the centrifugal force of the rotation and the urging force of the inert gas are used. The reaction by-product gas contained in the film is smoothly discharged to the outside of the substrate. In particular, in practice, the semiconductor element pattern includes pores having a deep aspect ratio, and it becomes more difficult to smoothly discharge the reaction by-product gas generated inside the pores as the element is ultrafinely miniaturized. Similarly, it is more difficult to deposit at various locations inside the hole while ensuring excellent step coverage.

因此,利用上述薄膜沉積裝置能夠提高階梯差覆蓋率的因素之一在於使基板進行旋轉,在執行一次旋轉時,除了沉積以外,還包括藉助配置在基板上表面的惰性氣體供給器154進行的吹掃功能,但更進一步,使吹掃效率更加極大化的因素在於只執行吹掃的步驟S4的b次旋轉。接著,噴射後處理氣體的同時在後處理步驟期間旋轉c次,從而經由將膜內雜質排出到終極的最低水準的同時使膜更加氮化的過程。Therefore, one of the factors capable of improving the step coverage by the above-described thin film deposition apparatus is to rotate the substrate, and when performing one rotation, in addition to deposition, blowing by the inert gas supplier 154 disposed on the upper surface of the substrate The sweep function, but further, the factor that maximizes the purge efficiency is that only b rotations of step S4 of the purge are performed. Next, the post-treatment gas is sprayed while being rotated c times during the post-treatment step, thereby making the film more nitrided while discharging the impurities in the film to the lowest level of the final.

第4圖作為第1圖II-II線的另一剖視圖,表示第二實施例所涉及的結構。Fig. 4 is a cross-sectional view taken along line II-II of Fig. 1 showing the structure of the second embodiment.

參照第4圖,氣體噴射部130具備大小相同的原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154。Referring to Fig. 4, the gas injection unit 130 includes a material gas supplier 151 having the same size, a reaction gas supplier 152, and a purge gas supplier 154.

原料氣體供給器151、反應氣體供給器152及吹掃氣體供給器154按相同的大小構成,在原料氣體供給器151和反應氣體供給器152相向的狀態下,對應每個原料氣體供給器151和反應氣體供給器152之間都具備吹掃氣體供給器154。當基板支承部120相對於氣體噴射部130相對旋轉時,放置於基板支承部120的基板W1~W6依次地經由原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154的下方。此時,由於藉由原料氣體供給器151、反應氣體供給器152,以及吹掃氣體供給器154按原料氣體→惰性氣體→反應氣體→惰性氣體的順序得到供給,利用該裝置結構並按照第3圖中圖示出的流程圖,能夠按ALD方式沉積薄膜。The material gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154 are configured to have the same size, and each of the material gas supplier 151 and the material gas supplier 151 and the reaction gas supplier 152 face each other. A purge gas supplier 154 is provided between the reaction gas suppliers 152. When the substrate supporting portion 120 relatively rotates with respect to the gas ejecting portion 130, the substrates W1 to W6 placed on the substrate supporting portion 120 sequentially pass through the material gas supplier 151, the reaction gas supplier 152, and the lower portion of the purge gas supplier 154. . At this time, the raw material gas supplier 151, the reaction gas supplier 152, and the purge gas supplier 154 are supplied in the order of the material gas → inert gas → reaction gas → inert gas, and the device structure is used in accordance with the third The flow chart illustrated in the figure is capable of depositing a thin film in an ALD manner.

第5圖作為第1圖II-II線的又一剖視圖,表示第三實施例所涉及的結構。Fig. 5 is a cross-sectional view taken along line II-II of Fig. 1 showing the structure of the third embodiment.

參照第5圖,氣體噴射部130包括氣體供給器151’、154、155。氣體供給器151’、154沿著上側板113的周向按放射形進行配置,氣體供給器151’是用於同時供給原料氣體和反應氣體的製程氣體供給器,氣體供給器154、155是用於供給惰性氣體的吹掃氣體供給器。雖然本實施例中圖示出兩個製程氣體供給器151’相向配置,並在其間配置吹掃氣體供給器154的例,但是製程氣體供給器151’和吹掃氣體供給器154分別是一個以上,其數量可以進行變更。Referring to Fig. 5, the gas injection portion 130 includes gas suppliers 151', 154, 155. The gas suppliers 151', 154 are radially arranged along the circumferential direction of the upper side plate 113, and the gas supplier 151' is a process gas supplier for simultaneously supplying the material gas and the reaction gas, and the gas suppliers 154, 155 are used. A purge gas supply for supplying an inert gas. Although the embodiment in which the two process gas suppliers 151' are disposed to face each other and the purge gas supplier 154 is disposed therebetween, the process gas supplier 151' and the purge gas supplier 154 are respectively one or more. The number can be changed.

當基板支承部120相對於氣體噴射部130相對旋轉時,放置於基板支承部120的基板W1~W6依次地經由各個氣體供給器製程氣體供給器151’以及吹掃氣體供給器154的下方。此時,由於原料氣體和反應氣體同時供給到基板W1~W6上,因而能夠實現CVD方式的薄膜沉積。When the substrate supporting portion 120 relatively rotates with respect to the gas ejecting portion 130, the substrates W1 to W6 placed on the substrate supporting portion 120 sequentially pass through the respective gas supplier process gas supplier 151' and the lower portion of the purge gas supplier 154. At this time, since the source gas and the reaction gas are simultaneously supplied to the substrates W1 to W6, thin film deposition by the CVD method can be realized.

利用該裝置結構按第3圖所示的流程圖,能夠沉積薄膜。由此,能夠實現在薄膜沉積後進行後處理步驟的循環CVD。With the structure of the apparatus, a film can be deposited in accordance with the flow chart shown in FIG. Thereby, cyclic CVD which performs a post-treatment step after film deposition can be realized.

第3圖的步驟S3藉由在供給原料氣體和反應氣體及惰性氣體的狀態下使基板W1~W6連續地經由製程氣體供給器151’和吹掃氣體供給器154的下方來實現。另外,步驟S4藉由在中斷原料氣體和反應氣體的供給的狀態下使基板W1~W6連續地經由製程氣體供給器151’和吹掃氣體供給器154的下方來實現。並且,步驟S5藉由在中斷原料氣體的供給的狀態下使基板W1~W6連續地經由製程氣體供給器151’和吹掃氣體供給器154下方來實現。這是後處理氣體與反應氣體相同時的情況。In step S3 of Fig. 3, the substrates W1 to W6 are continuously passed through the process gas supplier 151' and the purge gas supplier 154 in a state where the source gas, the reaction gas, and the inert gas are supplied. Further, in step S4, the substrates W1 to W6 are continuously passed through the process gas supplier 151' and the purge gas supplier 154 in a state where the supply of the material gas and the reaction gas is interrupted. Further, in step S5, the substrates W1 to W6 are continuously passed through the process gas supplier 151' and the purge gas supplier 154 in a state where the supply of the material gas is interrupted. This is the case when the post-treatment gas is the same as the reaction gas.

以上參照附圖對本發明的較佳實施例進行了說明,但是本發明並非限定於上述特徵的較佳實施例,在不脫離申請專利範圍所請求的本發明的技術範圍的情況下,本發明所屬的技術領域的技術人員能夠進行多種變形實施,這種變更也應當屬於申請專利範圍所記載的範圍內。The preferred embodiments of the present invention have been described above with reference to the drawings, but the present invention is not limited to the preferred embodiments of the present invention, and the present invention belongs to the present invention without departing from the technical scope of the present invention as claimed in the appended claims. A person skilled in the art can implement various modifications, and such modifications are also within the scope of the patent application.

產業上的可利用性Industrial availability

本發明所涉及的薄膜沉積方法,無需操作閥門便能沉積能夠實現ALD或循環CVD的薄膜,將薄膜的品質及生產率提高到現有技術的ALD或循環CVD無法達到的水準。並且,由於能夠一次性處理複數個基板,能夠提高生產率。由此,本發明將提高產業上的可利用性。According to the thin film deposition method of the present invention, a film capable of realizing ALD or cyclic CVD can be deposited without operating a valve, and the quality and productivity of the film can be improved to a level that cannot be attained by ALD or cyclic CVD in the prior art. Further, since a plurality of substrates can be processed at one time, productivity can be improved. Thus, the present invention will improve industrial applicability.

100...薄膜沉積裝置100. . . Thin film deposition device

110...反應器110. . . reactor

111...底部111. . . bottom

112...外壁部112. . . Outer wall

113...上側板113. . . Upper side panel

120...基板支承部120. . . Substrate support

121...基座121. . . Pedestal

122...基板放置部122. . . Substrate placement

123...軸123. . . axis

130...氣體噴射部130. . . Gas injection department

140...薄膜沉積空間140. . . Thin film deposition space

151...原料氣體供給器151. . . Raw material gas supplier

151’...製程氣體供給器151’. . . Process gas supplier

152...反應氣體供給器152. . . Reaction gas feeder

154、155...吹掃氣體供給器154, 155. . . Purge gas supplier

A...旋轉中心軸A. . . Rotation center axis

W1~W6...基板W1~W6. . . Substrate

S1、S2、S3、S4、S5、S6...步驟S1, S2, S3, S4, S5, S6. . . step

第1圖是表示利用於本發明中之薄膜沉積裝置的簡要結構的示意圖;Fig. 1 is a schematic view showing a schematic configuration of a thin film deposition apparatus used in the present invention;

第2圖是用於實現本發明第一實施例之第1圖II-II線的剖視圖;Figure 2 is a cross-sectional view showing the first embodiment of the present invention taken along the line II-II of Figure 1;

第3圖是表示利用第2圖之裝置結構在基板上沉積薄膜的方法的流程圖;Figure 3 is a flow chart showing a method of depositing a thin film on a substrate by using the device structure of Figure 2;

第4圖是用於實現本發明第二實施例之第1圖II-II線的另一剖視圖;以及Figure 4 is another cross-sectional view for carrying out the first line II-II of the second embodiment of the present invention;

第5圖是用於實現本發明第三實施例之第1圖II-II線的又一剖視圖。Fig. 5 is still another cross-sectional view for carrying out the first line II-II of the third embodiment of the present invention.

S1、S2、S3、S4、S5、S6...步驟S1, S2, S3, S4, S5, S6. . . step

Claims (10)

一種薄膜沉積方法,其係利用一薄膜沉積裝置來沉積薄膜的方法,該薄膜沉積裝置包括:一基板支承部,其設置在一反應器內部,並具有供複數個基板放置的複數個基板放置部,以及一氣體噴射部,其設置在該基板支承部的上部,將至少一種氣體供給到該基板支承部上;該基板支承部和該氣體噴射部能夠相對旋轉地進行設置,該薄膜沉積方法,包括:步驟(a),在該等基板放置部放置該等基板;步驟(b),一邊使該基板支承部和該氣體噴射部相對旋轉,一邊藉由該氣體噴射部將原料氣體及與該原料氣體進行反應的反應氣體供給到該基板支承部上,從而在該等基板上沉積薄膜;步驟(c),一邊使該基板支承部和該氣體噴射部相對旋轉,一邊藉由該氣體噴射部將惰性氣體供給到該基板支承部上,從而進行吹掃;以及步驟(d),一邊使該基板支承部和該氣體噴射部相對旋轉,一邊藉由該氣體噴射部將後處理氣體供給到該基板支承部上,從而進行後處理;其中,所述步驟(b)藉由同時供給該原料氣體和該反應氣體而依化學氣相沉積方式進行;以及所述步驟(d)中斷該原料氣體的供應,將包含N元素的氮化氣體及含氧氣體中的至少一種作為所述後處理氣體。 A thin film deposition method is a method for depositing a thin film by using a thin film deposition apparatus, the thin film deposition apparatus comprising: a substrate supporting portion disposed inside a reactor and having a plurality of substrate placing portions for a plurality of substrates to be placed And a gas ejecting portion provided on an upper portion of the substrate supporting portion to supply at least one gas to the substrate supporting portion; the substrate supporting portion and the gas ejecting portion being rotatably disposed, the thin film deposition method, The method includes the steps of: (a) placing the substrates in the substrate placing portions; and the step (b), while rotating the substrate supporting portion and the gas injecting portion, the raw material gas and the gas injecting portion The reaction gas from which the raw material gas is reacted is supplied to the substrate supporting portion to deposit a thin film on the substrate; and in the step (c), the substrate supporting portion and the gas ejecting portion are relatively rotated while the gas ejecting portion is used Supplying an inert gas to the substrate supporting portion to perform purging; and step (d), causing the substrate supporting portion and the gas to be ejected The post-processing is performed by supplying the post-treatment gas to the substrate supporting portion by the gas ejecting portion while rotating relative to each other; wherein the step (b) is based on the chemical gas by simultaneously supplying the raw material gas and the reactive gas. The phase deposition method is performed; and the step (d) interrupts the supply of the material gas, and at least one of a nitriding gas containing an N element and an oxygen-containing gas is used as the post-treatment gas. 根據申請專利範圍第1項所述的薄膜沉積方法,其中至少重複一次由該步驟(b)至該步驟(d)構成的循環。 The thin film deposition method according to claim 1, wherein the cycle consisting of the step (b) to the step (d) is repeated at least once. 根據申請專利範圍第1項所述的薄膜沉積方法,其中在該步驟(a)和該步驟(b)之間還包括使該基板支承部的旋轉速度加速的步驟。 The thin film deposition method according to claim 1, wherein the step (a) and the step (b) further includes a step of accelerating a rotational speed of the substrate supporting portion. 根據申請專利範圍第1項所述的薄膜沉積方法,其中該氣體噴射部由複數個氣體供給器按一放射形配置而成,其中該等氣體供給器的至少其中之 一是用於同時通過同一管道供給該原料氣體和該反應氣體的至少一製程氣體供給器,該等氣體供給器的至少其中之一的是用於供給該惰性氣體的至少一吹掃氣體供給器。 The thin film deposition method according to claim 1, wherein the gas injection portion is configured by a plurality of gas suppliers in a radial shape, wherein at least one of the gas supply devices One is at least one process gas supplier for supplying the material gas and the reaction gas through the same pipe at the same time, at least one of the gas suppliers is at least one purge gas supplier for supplying the inert gas . 根據申請專利範圍第4項所述的薄膜沉積方法,其中該步驟(b)藉由在供給該原料氣體、該反應氣體,以及該惰性氣體的狀態下使該等基板以一連續地經由該製程氣體供給器和該吹掃氣體供給器之下方的方式來實現。 The thin film deposition method according to claim 4, wherein the step (b) causes the substrates to be continuously passed through the process by supplying the raw material gas, the reactive gas, and the inert gas. This is accomplished by means of a gas supply and a lower portion of the purge gas supply. 根據申請專利範圍第5項所述的薄膜沉積方法,其中該步驟(c)藉由在中斷該原料氣體和該反應氣體的供給的狀態下使該等基板以一連續地經由該製程氣體供給器和該吹掃氣體供給器之下方的方式來實現。 The thin film deposition method according to claim 5, wherein the step (c) causes the substrates to continuously pass through the process gas supplier by interrupting the supply of the material gas and the reaction gas. This is accomplished in a manner that is below the purge gas supply. 根據申請專利範圍第5項所述的薄膜沉積方法,其中該步驟(d)藉由在中斷該原料氣體的供給的狀態下使該基板以一連續地經由該製程氣體供給器和該吹掃氣體供給器之下方的方式來實現。 The thin film deposition method according to claim 5, wherein the step (d) causes the substrate to continuously pass through the process gas supplier and the purge gas by interrupting the supply of the material gas. The way below the feeder is achieved. 根據申請專利範圍第1項所述的薄膜沉積方法,其中該薄膜是一單原子金屬薄膜、一金屬氮化物薄膜及一金屬氧化物薄膜中的至少其中之一。 The thin film deposition method according to claim 1, wherein the film is at least one of a monoatomic metal film, a metal nitride film, and a metal oxide film. 根據申請專利範圍第1項所述的薄膜沉積方法,其中該惰性氣體是氬氣或氮氣。 The thin film deposition method according to claim 1, wherein the inert gas is argon or nitrogen. 根據申請專利範圍第1項所述的薄膜沉積方法,其中該等基板以該基板支承部的中心為基準對稱地進行放置。The thin film deposition method according to claim 1, wherein the substrates are placed symmetrically with respect to a center of the substrate supporting portion.
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