200810019 (1) 九、發明說明 【發明所屬之技術領域】 本發明是關於用來例如將銅錳(CuMi!)合金膜或錳 (Μη)膜作爲晶種膜,形成在半導體晶圓等之被處理體的表 面之成膜裝置及成膜方法。 产 【先前技術】 • 一般,製造半導體裝置,係對半導體晶圓反覆進行成 膜處理或圖案蝕刻處理等的各種處理,製造所要的裝置, 不過由於要求半導體裝置的更加高積體化和高微細化,線 寬或孔徑愈發微細化。然後,配線材料或埋入溝道、孔等 的凹部內之埋入材料,由於各種尺寸的微細化,必須更減 低電阻,因而傾向於採用電阻很小且廉價的銅。(日本專 利文獻1)。然後’採用銅來作爲該配線材料或埋入材料_. 情況,考慮到銅擴散該下層的障壁性等,——般是採用鉅金 # 屬(Ta)或鉬氮化膜(TaN)等,作爲障壁層。 然後,埋入上述凹部內的步驟,係先在電漿電鍍裝置 - 內,將由銅膜所組成之薄晶種膜形成在包含該凹部內的壁 > 面全體之晶圓表面全面,接著對晶圓表面全面施予鍍銅處 理,完全埋入凹部內。之後,經由CMP(Chemical Mechanical Polishing)處理等進行硏磨處理,除去晶圓表 面多餘的銅薄膜。 參考第7圖來針對這點進行說明。第7圖爲表示一般埋 入半導體晶圓的凹部的步驟之圖。在被形成在該半導體晶 -4- 200810019 (2) 圓W的例如層間絕緣膜等之絕緣層的表面,形成與導孔 (via hole)或穿孔(through hole)或溝槽(溝道或 Dual Damascene構造)相對應的凹部2,在該凹部2的底部,呈 露出狀態形成例如由銅所組成之下層的配線層3。上述凹 部2隨著設計規則的微細化,該寬度或者內徑非常小例如 120 nm程度,體積比成爲例如2〜4程度。此外,有關擴散 - 防止膜和抗蝕膜等,則是圖示省略且形狀單純化來記載。 φ 以電漿濺鍍裝置,預先在該半導體晶圓W的表面, 也包含上述凹部2內的內面,大致均等地形成例如由TaN 膜和Ta膜的層積構造所組成之障壁層4(參考第7(A)圖)。 然後,以電漿濺鍍裝置,橫跨包含上述凹部2內的表面之 晶圓表面全體,形成由薄銅膜所組成的晶種膜6,作爲金 屬膜(參考第7(B)圖)。在電漿濺鍍裝置內形成該晶種膜6 時,對半導體晶圓側施加高頻的偏壓電力,效率良好地進^ 行銅金屬離子的引進。進而,對上述晶圓表面施予鍍銅處 • 理,用例如由銅膜所組成的金屬膜8來埋入上述凹部2內( 參考第7(C)圖)。之後,經由上述過的CMP處理等進行硏 * 磨處理,除去上述晶圓表面多餘的金屬膜8、晶種膜6以及 . 障壁層4。 然則,最近,以提高上述障壁層的更高可靠度爲目標 ,進行各種的硏發,其中,採用Μη膜或CuMn合金膜來 取代上述Ta膜或TaN膜之自我形成障壁層受到注目(日本 專利文獻2)。該Μη膜或CuMn合金膜則是經由濺鍍處理 來成膜,又該Μη膜或CiiMn合金膜本身變成晶種膜,所 -5- 200810019 (3) 以可以直接在該上方形成鍍銅層。另外,成膜後施予退火 處理,則會自我整合地與屬於下層的絕緣膜之Si02層起 反應,而在該Si〇2層與Mil膜或CuMn合金膜的界面部分 ,形成MnSixOy(x、y:任意的整數)膜之障壁膜,故具有 可以削減製程數的優點。 進而,還具有下述的優點:該Μη膜或CuMn合金膜 " 中的Μη,在例如以CVD法來形成Cu膜時,與進入Cu φ 膜中的鹵元素優先結合,從Cu膜中捕集該鹵元素,可以 改良Cu膜配線的膜質來使配線的可靠度提高。 專利文獻1:日本專利特開2004-1 07747號公報 專利文獻2 :日本專利特開2005-2773 90號公報 然則,目前的實用水準,上述CuMn合金膜只能夠以 濺鍍法來形成,不過對於將來所預測之極微細圖案,例如| 線寬或孔徑爲32 nm以下的溝道或孔,濺鍍法已無法充分, 對應,階差覆蓋性(step coverage)劣化的結果,會有很高 # 度的凹部埋入不充分之虞。 另外,如同上述過,晶種膜6的形成步驟、電鍍處理 ~ 步驟以及退火步驟,必須分別使用與各步驟相對應的裝置 - ’例如濺鍍裝置、電鍍處理以及退火裝置,會有不得已增 大裝置成本(設備成本)的問題。 進而,還會有下述的問題:由於上述晶種膜6的形成 步驟及埋入步驟無法在in-situ進行,即是晶種膜6形成後 ’半導體晶圓搬運到埋入裝置時,半導體晶圓在由清淨空 氣所形成的大氣中進行搬運,所以反應性很高的CuMn合 -6- 200810019 (4) 金膜會被氧化,該結果,妨礙銅的埋入成膜,或者晶種膜 中的Μη成分氧化所形成之Μη氧化物會升高接觸電阻。 另外,還會有下述的問題點··以濺鍍進行成膜中,在 凹部的底部形成比該側壁還要更厚的晶種膜,所以即使經 由退火處理,在凹部的側壁生成十分薄的MnSixOy膜,底 部的部分仍會大量殘存電阻値大於銅的錳或該氧化物,接 - 觸電阻會更加升高。 【發明內容】 本發明係針對以上的問題點來有效解決而提案。本發 明的目的則是提供:經由CVD等的熱處理,形成例如 CuMn合金膜或Μη膜等,即使是微細的凹部,仍可以以 很高的階差包覆性(s t e p c ο ν e r a g e)來進行埋入,而且是以, 相同的處理裝置來連續進行處理,可以大幅降低裝置成本 之成膜方法、成膜裝置、電腦程式及記憶媒體。 φ 本發明的一種成膜方法,其特徵爲,具備有:將被處 理體搬運到可抽真空的處理容器內之步驟、及對處理容器 - 內,至少供應含有過渡金屬之含有過渡金屬原料氣體和還 . 原氣體,並且將被處理體予以加熱,經由熱處理來將薄膜 形成在被處理體的表面之步驟。 如此,在可抽真空的處理容器內,利用含有過渡金屬 之含有過渡金屬原料氣體和還原氣體,經由熱處理來將薄 膜形成在被處理體的表面,所以即使是微細的凹部,仍可 以以很高的階差包覆性(step coverage)來進行埋入,而且 200810019 (5) 是以相同的處理裝置來連續進行處理,可以大幅降低裝置 成本。 本發明的如同上述的成膜方法,其中,對處理容器內 ,供應含有銅之含有銅原料氣體、及含有過渡金屬之含有 過渡金屬原料氣體、及還原氣體,並且將被處理體予以加 熱,經由熱處理來將薄膜形成在被處理體的表面之步驟。 | 如此,在可抽真空的處理容器內,利用含有銅之含有 φ 銅原料氣體、及含有過渡金屬之含有過渡金屬原料氣體、 及還原氣體,經由熱處理來將薄膜形成在被處理體的表面 ’所以即使是微細的凹部,仍可以以很高的階差包覆性:: (step coverage)來進行埋入,而且是以相同的處理裝置來 連續進行處理,可以大幅降低裝置成本。 本發明的如同上述的成膜方法,其中,前述熱處理, 係採用 CVD(Chemical Vapor Deposition)法。 本發明的如同上述的成膜方法,其中,前述熱處理, • 係採用交互地反覆供應前述原料氣體及前述還原氣體來進 行成膜之 ALD(Atomic LayerDeposition)法。 - 本發明的如同上述的成膜方法,其中,前述熱處理, _ 係以隔著間歇期間交互地反覆供應前述2種原料氣體,並 且在前述間歇期間時供應前述還原氣體的方式來進行。 本發明的如同上述的成膜方法,其中,以經由CVD 法,將銅膜堆積在形成了前述薄膜的被處理體上,進行前 述被處理體之凹部的埋入處理的方式來進行。 本發明的如同上述的成膜方法,其中,前述埋入處理 -8- 200810019 (6) ’係在形成了前述薄膜之處理容器內進行。 依據該成膜方法,在相同的裝置內,即是在in-situ 連續進行處理,所以形成不要的金屬氧化膜會受到抑制, 該結果,可以改善埋入性,並且可以防止接觸電阻變大。 本發明的如同上述的成膜方法,其中,進行前述埋入 處理過後,對前述被處理體施行退火處理。 ^ 本發明的如同上述的成膜方法,其中,前述退火處理 φ ,係在形成了前述薄膜之處理容器內進行。 本發明的如同上述的成膜方法,其中,以經由電鍍法 ’將銅膜堆積在形成了前述薄膜的被處理體上,進行前述 被處理體之凹部的埋入處理的方式來進行。 本發明的如同上述的成膜方法,其中,進行前述被處 理體之凹部的埋入處理過後,對前述被處理體施行退火處 理。 本發明的如同上述的成膜方法,其中,爲了要在前述 # 薄膜的膜厚方向上,使前述薄膜中的銅與過渡金屬的組成 比變化,以在前述熱處理的中途就使前述含有銅原料氣體 - 和/或前述含有過渡金屬原料氣體的供應量變化的方式來 一 進行。 本發明的如同上述的成膜方法,其中,以前述薄膜中 之前述過渡金屬的組成比,前述薄膜內的下層側很大,愈 往上層側則愈小的方式,控制前述各原料氣體的供應量。 本發明的如同上述的成膜方法,其中,含在前述薄膜 中之前述過渡金屬的量,換算成前述過渡金屬之純金屬的 -9- 200810019 (7) 膜厚,則在0.7〜2.6 nm的範圍內。 本發明的如同上述的成膜方法,其中,前述處理體的 表面成爲前述薄膜的基底膜,該基底膜則是由從Si02膜 及SiOC膜及SiCOH膜及3川1^膜及多孔質氧化矽膜及多 孔質甲基倍半砂氧院(methylsilsesquioxane ; MSQ)膜及聚 丙炔膜及SiLK(商標名)膜及氟碳(fluorocarbon)膜的群體 | 當中所選出的1種以上的膜所組成。 φ 本發明的如同上述的成膜方法,其中,前述含有過渡 金屬原料氣體的含有過渡金屬原料,係由有機金屬材料或 金屬錯體材料所組成。 本發明的如同上述的成膜方法,其中,前述有機金屬 材料爲M(R-Cp)x(x爲自然數),此處Μ爲表示過渡金屬 ,R爲表示烷基,由 H、CH3、C2H5、C3H7、C4H9的群體 當中所選出的1種,Cp爲環戊院二燃基(cyclopentandienyl ;C 5 Η 4 )。 • 本發明的如同上述的成膜方法,其中,前述有機金屬 材料爲M(R-Cp)x(CO)(x、y爲自然數),此處Μ爲表示過 ~ 渡金屬,R爲表示烷基,由Η、CH3、C2H5、C3H7、C4H9 - 的群體當中所選出的1種,Cp爲環戊烷二烯基 (cyclop entandienyl ; C5H4),CO 爲幾基(carbonyl)。 本發明的如同上述的成膜方法,其中,前述有機金屬 材料係由過渡金屬及C及Η所組成。 本發明的如同上述的成膜方法,其中,前述過渡金屬 爲從 Mn、Nb、Zr、Cr、V、Y、Pd、Ni、Pt、Rh、Tc、Α1 -10- 200810019 (8) 、Mg、Sn、Ge、Ti、Re的群體當中所選出之1種以上的 金屬。 本發明的如同上述的成膜方法,其中,前述過渡金屬 係由錳(Μη)所組成,含有該錳的有機金屬材料則爲由 Cp2Mn[ = Mn(C5H5)2]、(MeCp)2Mn[ = Mn(CH3C5H4)2]、 (EtCp)2Mn[ = Mn(C2H5C5H4)2]、(i-PirCp)2Mn[ = Mn(C3H7C5H4)2] • 、MeCpMn(CO)3[ = (CH3C5H4)Mn(CO)3]、 φ (t-BuCp)2Mn[ = Mn(C4H9C5H4)2]、CH3Mn(CO)5、200810019 (1) EMBODIMENT OF THE INVENTION [Technical Field] The present invention relates to, for example, a copper-manganese (CuMi!) alloy film or a manganese (Mn) film as a seed film formed on a semiconductor wafer or the like. A film forming apparatus and a film forming method for treating the surface of the body. [Prior Art] In general, a semiconductor device is manufactured by repeatedly performing various processes such as a film formation process or a pattern etching process on a semiconductor wafer, and manufacturing a desired device. However, it is required to have a higher integration and high fineness of the semiconductor device. The line width or the aperture is more and more refined. Then, the wiring material or the buried material embedded in the concave portion of the channel, the hole, or the like is required to have a smaller electric resistance due to the refinement of various sizes, and therefore copper tends to be small and inexpensive. (Japanese Patent Document 1). Then, 'using copper as the wiring material or embedding material _. In the case of considering the barrier property of copper diffusion to the lower layer, etc., it is generally adopted by Taejin (Ta) or molybdenum nitride (TaN). As a barrier layer. Then, the step of embedding in the recess is to form a thin seed film made of a copper film in the plasma plating apparatus, and the surface of the wafer including the surface of the recess is comprehensive, and then The surface of the wafer is completely coated with copper and completely buried in the recess. Thereafter, honing is performed by a CMP (Chemical Mechanical Polishing) treatment or the like to remove excess copper film on the surface of the wafer. This point will be explained with reference to Fig. 7. Fig. 7 is a view showing a step of generally embedding a concave portion of a semiconductor wafer. On the surface of the insulating layer formed of, for example, an interlayer insulating film or the like of the semiconductor crystal -4-200810019 (2), a via hole or a through hole or a trench (channel or dual) is formed. In the recessed portion 2 corresponding to the Damascene structure, a wiring layer 3 of, for example, a layer composed of copper is formed in an exposed state at the bottom of the recess 2. The recess 2 is miniaturized according to design rules, and the width or inner diameter is extremely small, for example, about 120 nm, and the volume ratio is, for example, about 2 to 4. Further, the diffusion-preventing film, the resist film, and the like are not shown in the drawings, and the shapes are simplistic and described. In the plasma sputtering apparatus, the inner surface of the recessed portion 2 is also formed on the surface of the semiconductor wafer W in advance, and the barrier layer 4 composed of, for example, a laminated structure of a TaN film and a Ta film is formed substantially uniformly ( Refer to Figure 7(A)). Then, a seed film 6 composed of a thin copper film is formed as a metal film by a plasma sputtering apparatus across the entire surface of the wafer including the surface in the concave portion 2 (refer to Fig. 7(B)). When the seed film 6 is formed in the plasma sputtering apparatus, high-frequency bias power is applied to the semiconductor wafer side, and the introduction of copper metal ions is efficiently performed. Further, a copper plating treatment is applied to the surface of the wafer, and the metal film 8 made of, for example, a copper film is embedded in the concave portion 2 (refer to Fig. 7(C)). Thereafter, the ruthenium treatment is performed by the above-described CMP treatment or the like to remove the excess metal film 8, the seed crystal film 6, and the barrier layer 4 on the wafer surface. However, recently, in order to improve the higher reliability of the above-mentioned barrier layer, various bursts have been carried out, in which the self-forming barrier layer of the above-mentioned Ta film or TaN film is replaced by a Μη film or a CuMn alloy film (Japanese Patent) Literature 2). The Μ 膜 film or the CuMn alloy film is formed by a sputtering process, and the Μ 膜 film or the C ii Mn alloy film itself becomes a seed film, so that a copper plating layer can be formed directly thereon. Further, after the film formation is subjected to the annealing treatment, the SiO 2 layer of the insulating film belonging to the lower layer is self-integrated, and MnSixOy (x, is formed at the interface portion between the Si 2 layer and the Mil film or the CuMn alloy film. y: an arbitrary integer) The barrier film of the film has an advantage that the number of processes can be reduced. Further, there is an advantage that the Μn in the Μn film or the CuMn alloy film is preferentially bonded to the halogen element entering the Cu φ film when the Cu film is formed by the CVD method, for example, and is trapped from the Cu film. By collecting the halogen element, the film quality of the Cu film wiring can be improved to improve the reliability of the wiring. Patent Document 1: Japanese Laid-Open Patent Publication No. 2004-1 07747. Patent Document 2: Japanese Patent Laid-Open Publication No. Hei No. 2005-2773 No. 90, the current practical level, the CuMn alloy film can be formed only by sputtering, but Very fine patterns predicted in the future, such as | line width or channel or hole with a hole diameter of 32 nm or less, the sputtering method is not sufficient, corresponding, the result of step coverage degradation will be high # The concave portion of the degree is buried insufficiently. In addition, as described above, the formation step of the seed film 6, the plating treatment step, and the annealing step must use the respective devices corresponding to the respective steps - 'for example, a sputtering device, a plating treatment, and an annealing device, which may have to be increased. Device cost (equipment cost) issues. Further, there is a problem in that the formation step and the embedding step of the seed crystal film 6 cannot be performed in the in-situ, that is, after the seed film 6 is formed, when the semiconductor wafer is transported to the embedding device, the semiconductor Since the wafer is transported in the atmosphere formed by clean air, the highly reactive CuMn -6-200810019 (4) gold film is oxidized, which results in the embedding of copper into the film, or the seed film. The Μ 氧化物 oxide formed by the oxidation of the Μη component increases the contact resistance. In addition, there are the following problems: In the film formation by sputtering, a seed film thicker than the side wall is formed at the bottom of the concave portion, so that the sidewall of the concave portion is formed very thinly even after the annealing treatment. In the MnSixOy film, the bottom portion still has a large amount of residual manganese, which is larger than copper or the oxide, and the contact resistance is increased. SUMMARY OF THE INVENTION The present invention has been made in view of the above problems. It is an object of the present invention to provide, for example, a CuMn alloy film or a Μη film by heat treatment such as CVD, and to bury a stepped ο ν erage even with a fine recess. In addition, it is a film forming method, a film forming apparatus, a computer program, and a memory medium which can continuously reduce the cost of the apparatus by continuously processing the same processing apparatus. φ A film forming method according to the present invention, comprising the steps of: transporting a target object into a vacuum-processable processing container; and supplying at least a transition metal-containing transition metal-containing material gas to the processing container And a raw gas, and the object to be processed is heated, and a film is formed on the surface of the object to be processed via heat treatment. In this way, in the vacuum-processable processing container, the transition metal-containing transition metal-containing gas and the reducing gas are used to form the film on the surface of the object to be processed by heat treatment, so that even a fine recess can be made high. The step coverage is used for embedding, and 200810019 (5) is continuously processed by the same processing device, which can greatly reduce the cost of the device. According to the film forming method of the present invention, the copper-containing raw material gas containing copper and the transition metal-containing transition metal-containing gas and the reducing gas are supplied to the processing container, and the object to be processed is heated. The step of heat treatment to form a film on the surface of the object to be treated. In the vacuum-processable processing container, the film containing the copper-containing φ copper source gas and the transition metal-containing transition metal source gas and the reducing gas is formed on the surface of the object to be processed by heat treatment. Therefore, even in the case of fine recesses, it is possible to perform embedding with a high step coverage: (step coverage), and continuous processing by the same processing device, which can greatly reduce the device cost. In the film forming method according to the above aspect of the invention, the heat treatment is performed by a CVD (Chemical Vapor Deposition) method. In the film forming method according to the above aspect of the invention, the heat treatment is performed by an ALD (Atomic Layer Deposition) method in which the raw material gas and the reducing gas are alternately supplied to form a film. In the film forming method according to the above aspect of the invention, the heat treatment is carried out by alternately supplying the two kinds of source gases alternately during the intermittent period and supplying the reducing gas during the intermittent period. In the above-described film forming method of the present invention, the copper film is deposited on the object to be processed on which the film is formed by the CVD method, and the recessed portion of the object to be processed is subjected to the embedding treatment. In the film forming method according to the above aspect of the invention, the embedding treatment -8-200810019 (6)' is carried out in a processing container in which the film is formed. According to this film formation method, in the same apparatus, that is, the in-situ process is continuously performed, the formation of an unnecessary metal oxide film is suppressed, and as a result, the embedding property can be improved, and the contact resistance can be prevented from becoming large. In the film forming method according to the above aspect of the invention, after the embedding treatment, the object to be processed is subjected to an annealing treatment. In the film forming method according to the above aspect of the invention, the annealing treatment φ is carried out in a processing container in which the film is formed. In the above-described film forming method of the present invention, the copper film is deposited on the object to be processed on which the film is formed by the plating method, and the embossing process of the concave portion of the object to be processed is performed. In the film forming method according to the above aspect of the invention, after the embedding process of the concave portion of the object to be treated is performed, the object to be processed is subjected to annealing treatment. According to the film forming method of the present invention, in order to change the composition ratio of copper to transition metal in the film thickness in the film thickness direction of the film, the copper material is contained in the middle of the heat treatment. The gas-and/or the aforementioned change in the supply amount of the transition metal-containing raw material gas is carried out. According to the film forming method of the present invention, the composition ratio of the transition metal in the film is such that the lower layer side in the film is large, and the smaller the upper layer side is, the more the supply of the raw material gases is controlled. the amount. In the film forming method according to the above aspect of the invention, the amount of the transition metal contained in the film is 0.7 to 200810019 (7) in terms of a film thickness of the pure metal of the transition metal, and is 0.7 to 2.6 nm. Within the scope. In the film forming method according to the above aspect of the invention, the surface of the processing body is a base film of the film, and the base film is made of a SiO 2 film, a SiOC film, a SiCOH film, a film, and a porous cerium oxide. A membrane and a porous methylsilsesquioxane (MSQ) membrane and a polypropyne membrane and a group of SiLK (trade name) membranes and fluorocarbon membranes are composed of one or more membranes selected. φ The film forming method according to the above aspect of the invention, wherein the transition metal-containing material containing the transition metal source gas is composed of an organic metal material or a metal-based material. In the film forming method according to the above aspect of the invention, the organometallic material is M(R-Cp)x (x is a natural number), wherein Μ represents a transition metal, R represents an alkyl group, and H, CH3, One selected from the group of C2H5, C3H7, and C4H9, and Cp is cyclopentandienyl (C 5 Η 4 ). The film forming method according to the above aspect of the invention, wherein the organometallic material is M(R-Cp)x(CO) (x, y is a natural number), wherein Μ is a transition metal, and R is a representation An alkyl group selected from the group consisting of ruthenium, CH3, C2H5, C3H7, and C4H9-, Cp is cyclopentene diene (C5H4), and CO is a carbonyl group. The film forming method according to the above aspect of the invention, wherein the organometallic material is composed of a transition metal, C and ruthenium. In the film forming method according to the above aspect of the invention, the transition metal is from Mn, Nb, Zr, Cr, V, Y, Pd, Ni, Pt, Rh, Tc, Α1 -10- 200810019 (8), Mg, One or more metals selected from the group consisting of Sn, Ge, Ti, and Re. In the film forming method of the present invention, the transition metal is composed of manganese (Mn), and the organic metal material containing the manganese is Cp2Mn[= Mn(C5H5)2], (MeCp)2Mn[= Mn(CH3C5H4)2], (EtCp)2Mn[ = Mn(C2H5C5H4)2], (i-PirCp)2Mn[ = Mn(C3H7C5H4)2] • MeCpMn(CO)3[ = (CH3C5H4)Mn(CO) 3], φ (t-BuCp) 2Mn[ = Mn(C4H9C5H4)2], CH3Mn(CO)5,
Mn(DPM)3[ = Mn(C, iHi9〇2)3] 'Mn(DPM)3[ = Mn(C, iHi9〇2)3] '
Mn(DMPD(EtCp)[ = Mn(C7H1iC2H5C5H4)) 'Mn(DMPD(EtCp)[ = Mn(C7H1iC2H5C5H4))'
Mn(acac)2[ = Mn(C5H7〇2)2] ' Mn(DPM)2 [ = Mn(C ι ι Η ι 9〇2>2] ' Mn(acac)3[ = Mn(C5H702)3 ]、Mn(hfac)2[ = Mii(C5HF602)3]的 群體當中所選出之1種以上的材料。 本發明的如同上述的成膜方法,其中,前述熱處理則 是倂用電漿。 # 本發明的如同上述的成膜方法,其中,前述原料氣體 與還原氣體在前述處理容器內才開始進行混合。 • 本發明的如同上述的成膜方法,其中,前述還原氣體 . 爲H2氣體。 本發明的一種成膜裝置是經由熱處理,在被處理體的 表面形成含有過渡金屬的薄膜之成膜裝置,其特徵爲,具 備有:可抽真空之處理容器、及被設置在前述處理容器內 ’用來載置前述被處理體之載置台構造、及將前述被處理 體予以加熱之加熱手段、及將氣體導入到前述處理容器內 -11 - 200810019 (9) 之氣體導入手段、及將原料氣體供應至前述氣體導入手段 之原料氣體供應手段、及將還原氣體供應至前述氣體導入 手段之還原氣體供應手段。 本發明的如同上述的成膜裝置,其中,前述原料氣體 存在有複數種’前述原料氣體供應手段具有對每種原料氣 體都設有的不同原料氣體之分歧路,該原料氣體的分歧路 * 會在中途會合。 • 本發明的如同上述的成膜裝置,其中,前述原料氣體 存在有複數種’前述原料氣體供應手段具有對每種原料氣 體都設有的不同原料氣體之分歧路,該原料氣體的分歧路 不會在中途會合,分別共同地連接至前述氣體導入手段。 本發明的如同上述的成膜裝置,其中,爲了要防止流 到該原料氣體流路之前述原料氣體被液化,在前述原料氣 體的分歧路設有用來加熱之流路加熱手段。 本發明的如同上述的成膜裝置,其中,前述原料氣體 ® 至少含有:含有過渡金屬之含有過渡金屬原料氣體。 本發明的如同上述的成膜裝置,其中,前述原料氣體 ^ 含有:含有銅之含有銅原料氣體、及含有過渡金屬之含有 、 過渡金屬原料氣體。 本發明的如同上述的成膜裝置,其中,前述還原氣體 爲H2氣體。 本發明的一種電腦程式,是用於成膜裝置,電腦中用 來執行成膜方法之電腦程式,其特徵爲,成膜方法具備有 :將被處理體搬運到可抽真空的處理容器內之步驟、及對 -12- 200810019 (10) 處理容器內,至少供應含有過渡金屬之含有過渡金屬原料 氣體和還原氣體,並且將被處理體予以加熱,經由熱處理 來將薄膜形成在被處理體的表面之步驟。 本發明的一種電腦程式,是電腦中用來執行成膜方法 ,而該成膜方法所採用的成膜裝置具有:可抽真空之處理 容器、及被設置在前述處理容器內,用來載置前述被處理 • 體之載置台構造、及將前述被處理體予以加熱之加熱手段 φ 、及將氣體導入到前述處理容器內之氣體導入手段、及將 原料氣體供應至前述氣體導入手段之原料氣體供應手段、 及將還原氣體供應至前述氣體導入手段之還原氣體供應手 段、及控制裝置全體之控制手段;利用該成膜裝置,經电 熱處理,將含有過渡金屬的薄膜形成在前述被處理體的表 面之電腦程式,其特徵爲,成膜方法具備有:將被處理體: 搬運到可抽真空的處理容器內之步驟、及對處理容器內, 至少供應含有過渡金屬之含有過渡金屬原料氣體和還原氣 # 體,並且將被處理體予以加熱,經由熱處理來將薄膜形成 在被處理體的表面之步驟。 - 本發明的如同上述的電腦程式,其中,前述原料氣體 ^ 含有:含有銅之含有銅原料氣體、及含有過渡金屬之含有 過渡金屬原料氣體。 本發明的一種儲存電腦程式之電腦中可讀取之記憶媒 體,是用於成膜裝置,將電腦中用來執行成膜方法的電腦 程式予以儲存之記憶媒體,其特徵爲: 成膜方法具備有:將被處理體搬運到可抽真空的處理 -13- 200810019 (11) 容器內之步驟、及對處理容器內,至少供應含有過渡金屬 之含有過渡金屬原料氣體和還原氣體,並且將被處理體予 以加熱,經由熱處理來將薄膜形成在被處理體的表面之步 驟。 本發明的一種儲存電腦程式之電腦中可讀取之記憶媒 體’是將電腦中用來執行成膜方法的電腦程式予以儲存, - 而該成膜方法所採用的成膜裝置具有:可抽真空之處理容 # 器、及被設置在前述處理容器內,用來載置前述被處理體 之載置台構造、及將前述被處理體予以加熱之加熱手段、 及將氣體導入到前述處理容器內之氣體導入手段、及將原 料氣體供應至前述氣體導入手段之原料氣體供應手段、及 將還原氣體供應至前述氣體導入手段之還原氣體供應手段 、及控制裝置全體之控制手段;利用該成膜裝置,經由熱 處理,將含有過渡金屬的薄膜形成在前述被處理體的表面 之記憶媒體,其特徵爲:成膜方法具備有:將被處理體搬 Φ 運到可抽真空的處理容器內之步驟、及對處理容器內,至 少供應含有過渡金屬之含有過渡金屬原料氣體和還原氣體 ^ ,並且將被處理體予以加熱,經由熱處理來將薄膜形成在 - 被處理體的表面之步驟。 本發明的如同上述的儲存電腦程式之電腦中可讀取之 記憶媒體,其中,前述原料氣體含有:含有銅之含有銅原 料氣體、及含有過渡金屬之含有過渡金屬原料氣體。 如同以上所說明過,依據本發明的成膜方法及成膜裝 置,可以發揮以下優異的作用效果。 -14 - 200810019 (12) 將含有銅之含有銅原料氣體、及含有過渡金屬之含有 過渡金屬原料氣體、及還原氣體,供應至可抽真空的處理 容器內,經由熱處理,將薄膜形成在被處理體的表面。因 而,即使是微細的凹部,仍可以以很高的階差包覆性(step coverage)來進行埋入,而且是以相同的處理裝置來連續進 行處理,可以大幅降低裝置成本。 • 另外,將含有過渡金屬之含有過渡金屬原料氣體、及 φ 還原氣體,供應至可抽真空的處理容器內,經由熱處理, 將薄膜形成在被處理體的表面,所以即使是微細的凹部, 仍可以以很高的階差包覆性(step coverage)來進行埋入, 而且是以相同的處理裝置來連續進行處理,可以大幅降低 裝置成本。 進而,依據本發明,可以在相同的裝置內,即是可以 在in-situ連續進行處理,所以形成不要的金屬氧化膜會 受到抑制,該結果,可以改善埋入性,並且可以防止接觸 # 電阻變大’甚致於可以達到提高半導體裝置的可靠度、改 善良品率。 ~ 依據本發明,在前述薄膜的膜厚方向上,使前述薄膜 • 中的銅與過渡金屬的組成比變化,而在前述熱處理的中途 就使各原料氣體的供應量變化,所以可以提高與基底膜的 密著性。 進而,依據本發明,含在薄膜中之過渡金屬的量最適 化,所以可以防止劣化過度量的過渡金屬之銅配線的膜質 特性。 -15- 200810019 (13) 【實施方式】 以下,根據圖面來詳述本發明的成膜方法及成膜裝置 的實施例。第1圖爲表示本發明的成膜裝置的一個例子之 構成圖。如同圖示,本發明的成膜裝置1 2具有例如剖面的 內部呈圓形之鋁製的處理容器14。在該處理容器14的側壁 ,設有用來將該處理容器加熱的加熱棒等的容器加熱手段 (未圖示)。在該處理容器14內的頂棚部,設置用來導入必 要的氣體,例如成膜氣體等之氣體導入手段,也就是設置 噴淋頭部1 6。噴淋頭部1 6係在該下面具有氣體噴射面1 8, 從設置在氣體噴射面18之多數個氣體噴射孔20A、20B, 朝向處理空間S,噴射處理氣體。 在該噴淋頭部16內,形成與氣體噴射孔20A、20B枏 連通之中空狀的被區隔成2個之氣體擴散室22 A、22B,機 導入至之氣體擴散室22A、22B之處理氣體往平面方向擴 散之後,從與各氣體擴散室22 A、22B相連通之各氣體噴 射孔20A、20B噴出。此情況,氣體噴射孔20A、20B係呈 矩陣狀配置,由各氣體噴射孔20 A、20B噴出的各氣體在 處理空間S進行混合。 這種供應形態則是稱爲後混合。該噴淋頭部1 6的全體 係由例如鎳或哈斯得路(音譯,商標名)等的鎳合金、鋁、 或鋁合金所形成。此外,以後述的ALD法來進行成膜的 情況’噴淋頭部1 6也可以具有1個氣體擴散室。然後,在 噴淋頭部1 6與處理容器1 4的上端開口部的接合部,中間裝 -16- 200810019 (14) 設例如由0封圈等的密封構件2 4,維持處理容器1 4內的 氣密性。 另外,在處理容器1 4的側壁,設置將當作被處理體的 半導體晶圓W,對該處理容器14內進行搬進搬出之搬進搬 出口 26,在搬進搬出口 26,氣密地設有可開關之閘閥28。 然後,在該處理容器14的底部30形成排氣空間32。具 。 體上,在該容器底部3〇的中央形成很大的開口 34,在該開 φ 口 34連結往該下方延伸之有底圓筒體狀的圓筒區隔壁36, 而在該內部形成上述排氣空間3 2。然後,在區隔該排氣空 間3 2之圓筒區隔壁3 6的底部3 8,由此處豎起來設置載置台 構造40。該載置台構造40包括由上述底部38豎起之圓筒體 狀的支柱42、及被固定在該支柱42的上端部而在上面載置 屬於被處理體的半導體晶圓W之載置台44。 另外,上述載置台44由例如陶瓷材料或石英玻璃所組 成。在該載置台44內,收容利用通電來產生熱之例如由碳 # 線電熱器等所組成之電阻加熱電熱器46,被載置在該載置 台44的上面之半導體晶圓w則得以進行加熱。 ^ 在上述載置台44,該上下方向貫穿來形成複數個例如 、 3個插銷插入孔48(第1圖中只呈現2個),配置可上下移動 地在滑嵌狀態下插通上述各插銷插入孔48之上推銷50。在 該上推銷50的下端,配置呈圓形環狀形成的例如鋁之陶瓷 製的上推環52,在上述各上推銷50的下端不被固定的狀態 下,支撐在上述上推環52。從該上推環52延伸之臂部54, 連結至貫穿容器底部30所設置之伸縮桿56,該伸縮桿56則 200810019 (15) 是利用致動器(actuator)58來進行伸降。藉由此方式’令 上述各上推銷50在進行晶圓W轉交時從各銷插入孔48的 上端往下方來伸縮。另外,在致動器58的伸縮桿56之容器 底部的貫穿部,中間裝設可伸縮之蛇腹60,上述伸縮桿56 則可以維持處理容器1 4內的氣密性並進行升降。 上述排器空間32之入口側的開口 34係被設定成小於載 • 置台44的直徑,形成爲上述載置台44之周緣部的外側流下 φ 的處理器體流經載置台44的下方才流往開口 3 4。在上述圓 筒區隔壁36的下部側壁,面臨該排氣空間32形成有排氣口 62。該排氣口 62連接真空排氣系統64。該真空排氣系統6單. 具有倍連接至上述排氣口 62之排氣通路66,在該排氣通路 66,中間依序裝設壓力調整閥68、真空幫浦70,將上述處 理容器14內和排氣空間32的雰圍則可以壓力控制並抽真空 進行排氣。 爲了要對噴淋頭部供應特定的氣體,在上述噴淋頭部 # 1 6 ’連接供應原料氣體之原料氣體供應手段72、及用來供 應還原氣體之還原氣體供應手段74。具體上,上述原料氣 - 體供應手段72具有被連接至上述2個氣體擴散室當中其中 - 一之方氣體擴散室2 2 A的氣體入口 7 6之原料氣體流路7 8。 此處則是該原料氣體流路78被分歧成2個,其中一方的分 歧路8 0 ’在中途中間依序裝設開關閥8 2和如同質量控制器 的流量控制器84,連接至收容第1原料之第1原料源8 6。 該第1原料係採用含有過渡金屬之含有過渡金屬原料 ,利用例如被流量控制之Ar氣體等的惰性氣體來加以起 -18- 200810019 (16) 泡,將上述原料氣體化,可以伴隨惰性氣 渡金屬原料氣體。此處,上述原料的蒸氣 了要提升原料的蒸氣壓,上述第1原料源 來加熱。上述含有過渡金屬原料可以採j (MeCp)2Mn(前驅物)。 ' 另外’供應原料氣體,不僅是採用起 | 用液體原料氣化方式或溶液原料氣化方式 • 料氣化方式是指在室溫下用氣化器來令液 方式’溶液原料氣化方式則是指在室溫下 原料溶解在溶媒中而變成液體,用氣化器 的方式。這種方式不僅是適用於供應Μη 以適用於供應Cu原料氣體。 另外,另一方的分歧路8 8,在中途中 閥90和如同質量控制器的流量控制器92, 原料之第2原料源94。該第2原料採用含有 • ,利用例如被流量控制之Ar氣體等的惰 泡,將上述原料氣體化,可以伴隨惰性氣 - 原料氣體。此處,上述原料的蒸氣壓很低 . 升原料的蒸氣壓,上述第2原料源94用電; 。上述含有銅原料可以採用例如含有銅的 、Cu(hfac)2、Cu(dibm)2等(前驅物)。 此外’速可以採用H e、N e等來取代 起泡用的上述惰性氣體。 然後,爲了要防止原料氣體再液化, 體來供應含有過 壓很低的話,爲 丨86用電熱器86a 电例如含有錳的 泡方式,也可採 。此處,液體原 態的原料氣化的 讓固態或液態的 來令該溶液氣化 原料氣體,也可 間依序裝設開關 連接至收容第2: 銅的含有銅原料 性氣體來加以起 體來供應含有銅 的話,爲了要提 熱器94a來加熱 Cu(hfac)TMVS Ar氣體,作爲 形成爲在上述各 -19- 200810019 (17) 分歧路80和88、該兩分岐路中間裝設之開關閥82和9 0、流 量控制器84和92以及原料氣體流路78,繞捲設置帶式電熱 器96,將這些予以加熱。此外,當然還可以依照使用的原 料來設置複數個原料氣體供應手段。 另外,上述還原氣體供應手段74具有被連接至另一方 的氣體擴散室22B的氣體入口 98之還原氣體流路1〇〇。該 還原氣體流路1 〇 〇,在中途中間依序裝設開關閥1 〇2和如同 # 質量控制器的流量控制器1 04,連接至收容還原氣體之還 原氣體源1 06。此處則是上述還原氣體採用H2氣體,不過 也可以採用其他的H20或氣化過的有機溶劑等。 此處,原料氣體連接至位於噴淋頭部1 6的上方之氣體 擴散室22A,還原氣體則連接至位於下方之氣體擴散室 22B。這點是因噴淋頭部16接近載置台44並相對向,導致 處在氣體噴射面1 8的溫度上升傾向,故將原料氣體導入f 方的氣體擴散室22B,會有氣體分解之虞之故。 ® 另外,形成爲淨化用的惰性氣體供應手段(未圖示)連 接至上述噴淋頭部1 6,按照需求來供應淨化氣體 (purge ^ gas)。該淨化氣體可以使用N2氣體、Ar氣體、He氣體、 • N e氣體等的惰性氣體。 然後,爲了要控制該裝置全體的動作,形成爲具有由 例如微電腦等所組成之控制手段1 08,進行上述氣體供應 開I始或停止的控制、供應量的控制、處理容器〗4內的壓力 控制、晶圓W的溫度控制等。然後,上述控制手段1 〇 8具 有用來記憶進行上述控制用的電腦程式之記憶媒體1 1 0。 -20- 200810019 (18) 上述記憶媒體110可以使用例如軟碟、快閃記憶體、 CD(Compact Disc)等。 其次,針對以上方式構成之成膜裝置的動作進行說明 〇 首先’未處理的半導體晶圓W,保持在搬運臂(未圖 示)上,經由成爲開啓狀態的閘閥2 8、搬進搬出口 2 6,搬 尊 入處理容器1 4內。該晶圓W轉交給已上升的上推銷5 〇之 後’令該上推銷5〇下降’就被載置在載置台44的上面。 接著,令原料氣體供應手段72或還原氣體供應手段74 動作,對送往噴淋頭部16作爲處理氣體之成膜氣體等之特: 定的各種氣體’分別進行流量控制並進行供應,該氣體由 氣體噴射孔20A、20B噴出來進行噴射,導入到處理空間 S。如同後述,該各種氣體有各種供應形態。然後,設置 在真空排氣系統64之真空幫浦持續驅動,將處理容器14|% 或排氣空間3 2內予以抽真空,再調整壓力調整閥6 8的張開 Φ 度,將處理空間S的雰圍維持在特定的處理壓力。此時, 晶圓W的溫度利用設置在載置台44內之電阻加熱電熱器 ^ 4 6進行加熱,維持在特定的處理溫度。藉由此方式,經由 • 熱CVD法等的熱處理就會在半導體晶圓w的表面形成所 要的薄膜。Mn(acac)2[ = Mn(C5H7〇2)2] ' Mn(DPM)2 [ = Mn(C ι ι Η ι 9〇2>2] ' Mn(acac)3[ = Mn(C5H702)3 ] And one or more materials selected from the group consisting of Mn(hfac)2[=Mii(C5HF602)3]. The film forming method according to the above aspect of the invention, wherein the heat treatment is a plasma for use. The film forming method as described above, wherein the raw material gas and the reducing gas are mixed in the processing container. The film forming method according to the above aspect, wherein the reducing gas is H2 gas. A film forming apparatus is a film forming apparatus that forms a transition metal-containing film on a surface of a workpiece by heat treatment, and is characterized in that: a vacuum-processable processing container is provided, and a processing container is provided in the processing container a mounting table structure on which the object to be processed is placed, a heating means for heating the object to be processed, a gas introduction means for introducing a gas into the processing container, and a raw material gas to be supplied to the processing container - 111001 (9) a raw material gas supply means of the gas introduction means, and The reducing gas supply means for supplying the reducing gas to the gas introducing means. The film forming apparatus according to the present invention, wherein the material gas is present in a plurality of types, the raw material gas supply means has a function for each of the material gases. The diverging path of the different material gases, the diverging path of the material gas will meet in the middle. The film forming apparatus of the present invention as described above, wherein the raw material gas is present in a plurality of kinds of the above-mentioned raw material gas supply means for each raw material The divergence path of the different material gases provided in the gas, the diverging paths of the material gases are not merged in the middle, and are respectively connected to the gas introduction means. The film forming apparatus of the present invention as described above, in order to prevent the flow The material gas to the material gas flow path is liquefied, and a flow path heating means for heating is provided in the branch path of the material gas. The film forming apparatus according to the present invention, wherein the material gas ® contains at least: The transition metal contains a transition metal source gas. The present invention is as described above In the film forming apparatus, the raw material gas contains: a copper-containing raw material gas containing copper, and a transition metal-containing and transition metal source gas. The film forming apparatus according to the present invention, wherein the reducing gas is H2 gas A computer program for use in a film forming apparatus for performing a film forming method in a computer, characterized in that the film forming method includes: transporting the object to be processed into a vacuumable processing container The step and the -12-200810019 (10) processing container are provided with at least a transition metal-containing transition metal source gas and a reducing gas, and the object to be treated is heated, and the film is formed in the object to be processed through heat treatment. The steps of the surface. A computer program of the present invention is a computer for performing a film forming method, and the film forming apparatus used in the film forming method has: a vacuum-processable processing container, and is disposed in the processing container for mounting The structure of the substrate to be processed, the heating means φ for heating the object to be processed, the gas introduction means for introducing the gas into the processing container, and the material gas for supplying the material gas to the gas introduction means a supply means, a reducing gas supply means for supplying a reducing gas to the gas introduction means, and a control means for controlling the entire apparatus; and the film forming apparatus is formed by electrothermal treatment to form a film containing a transition metal in the object to be processed A surface computer program characterized in that the film forming method includes: a step of transporting the object to be processed into a vacuum-processable processing container; and supplying at least a transition metal-containing transition metal-containing gas containing a transition metal to the processing container; Reducing the gas body, and heating the object to be processed, forming a film by heat treatment The step of surface treatment thereof. In the computer program according to the above aspect of the invention, the material gas ^ contains a copper-containing material gas containing copper and a transition metal-containing material gas containing a transition metal. A memory medium readable by a computer for storing a computer program is a memory medium for a film forming apparatus for storing a computer program for performing a film forming method in a computer, wherein: the film forming method is provided There are: a process of transporting the object to be evacuated to a vacuumable treatment-13-200810019 (11) in a container, and at least a transition metal-containing gas containing a transition metal and a reducing gas in the processing container, and will be processed The body is heated, and a film is formed on the surface of the object to be processed via heat treatment. The readable memory medium in the computer storing the computer program is stored in a computer program for performing a film forming method in the computer, and the film forming device used in the film forming method has: vacuuming And a processing device provided in the processing container, a mounting table structure on which the object to be processed is placed, a heating means for heating the object to be processed, and a gas to be introduced into the processing container a gas introduction means, a raw material gas supply means for supplying the raw material gas to the gas introduction means, a reducing gas supply means for supplying the reducing gas to the gas introduction means, and a control means for controlling the entire control means; a memory medium in which a transition metal-containing film is formed on the surface of the object to be processed by heat treatment, and the film forming method includes a step of transporting the object to be processed into a vacuumable processing container, and Providing at least a transition metal-containing gas and a reducing gas containing a transition metal in the processing container, and The object to be processed is heated, and a film is formed on the surface of the object to be processed by heat treatment. A memory medium readable by a computer storing a computer program according to the present invention, wherein the material gas contains a copper-containing raw material gas containing copper and a transition metal-containing raw material gas containing a transition metal. As described above, the film forming method and the film forming apparatus of the present invention can exhibit the following excellent effects. -14 - 200810019 (12) The copper-containing raw material gas containing copper, the transition metal-containing raw material gas containing the transition metal, and the reducing gas are supplied to a vacuum-processable processing chamber, and the film is formed into a processed film by heat treatment. The surface of the body. Therefore, even a fine recess can be buried with a high step coverage, and the same processing device can be continuously processed, which can greatly reduce the device cost. • The transition metal-containing gas and the φ reducing gas containing the transition metal are supplied to a vacuum-processable processing chamber, and the film is formed on the surface of the object to be processed by heat treatment. Therefore, even if it is a fine recess, The step coverage can be performed with a high step coverage, and the processing is continuously performed by the same processing device, which can greatly reduce the device cost. Further, according to the present invention, it is possible to carry out the treatment continuously in the same apparatus, that is, in-situ, so that the formation of an unnecessary metal oxide film is suppressed, and as a result, the embedding property can be improved, and the contact #resistance can be prevented. Increasingly, it is possible to improve the reliability of semiconductor devices and improve the yield. According to the present invention, the composition ratio of copper to transition metal in the film is changed in the film thickness direction of the film, and the supply amount of each material gas is changed in the middle of the heat treatment, so that the substrate can be improved. Adhesion of the film. Further, according to the present invention, since the amount of the transition metal contained in the film is optimized, it is possible to prevent deterioration of the film quality of the copper wiring of the transition metal. -15- 200810019 (13) [Embodiment] Hereinafter, embodiments of the film forming method and film forming apparatus of the present invention will be described in detail based on the drawings. Fig. 1 is a view showing the configuration of an example of a film forming apparatus of the present invention. As shown in the figure, the film forming apparatus 1 2 of the present invention has, for example, a processing container 14 made of aluminum having a circular inside shape. A container heating means (not shown) for heating the processing container or the like is provided on the side wall of the processing container 14. The ceiling portion in the processing container 14 is provided with a gas introduction means for introducing a necessary gas, for example, a film forming gas, that is, a shower head 16 is provided. The shower head 16 has a gas ejection surface 18 on the lower surface, and a plurality of gas injection holes 20A and 20B provided in the gas injection surface 18 are directed toward the processing space S to eject the processing gas. In the shower head 16, a hollow gas diffusion chamber 22A, 22B which is separated from the gas injection holes 20A, 20B and which is divided into two, is formed, and the gas diffusion chambers 22A, 22B are introduced into the nozzle head. After the gas is diffused in the planar direction, the gas is ejected from the respective gas injection holes 20A and 20B that communicate with the respective gas diffusion chambers 22 A and 22B. In this case, the gas injection holes 20A and 20B are arranged in a matrix, and the respective gases ejected from the respective gas injection holes 20 A and 20B are mixed in the processing space S. This form of supply is called post-mixing. The entire shower head 16 is formed of a nickel alloy such as nickel or Hastelloy (trade name), aluminum, or aluminum alloy. Further, in the case of film formation by the ALD method described later, the shower head 16 may have one gas diffusion chamber. Then, in the joint portion between the shower head 16 and the upper end opening portion of the processing container 14, the intermediate member-16-200810019 (14) is provided with a sealing member 24 such as a 0-ring or the like, and the processing container 14 is maintained. The air tightness. In addition, a semiconductor wafer W to be treated as a target object is placed on the side wall of the processing container 14, and a loading/unloading port 26 for loading and unloading the inside of the processing container 14 is provided, and the loading/unloading port 26 is air-tightly placed. A switchable gate valve 28 is provided. An exhaust space 32 is then formed at the bottom 30 of the processing vessel 14. With . The body has a large opening 34 formed in the center of the bottom of the container, and the opening φ port 34 is connected to the bottomed cylindrical body partition wall 36 extending downward, and the row is formed inside. Gas space 3 2. Then, the stage structure 40 is placed upright from the bottom portion 3 of the cylindrical portion partition wall 36 of the exhaust space 32. The stage structure 40 includes a columnar column 42 that is erected by the bottom portion 38, and a mounting table 44 that is fixed to the upper end portion of the column 42 and on which the semiconductor wafer W belonging to the object to be processed is placed. Further, the above-described mounting table 44 is composed of, for example, a ceramic material or quartz glass. In the mounting table 44, a resistance heating electric heater 46 composed of, for example, a carbon electric heater or the like that generates heat by energization is housed, and the semiconductor wafer w placed on the upper surface of the mounting table 44 is heated. . In the above-described mounting table 44, a plurality of, for example, three latch insertion holes 48 (only two in the first drawing) are formed in the vertical direction, and the above-described plug insertions are inserted in the slide-fit state so as to be vertically movable. The pin 50 is pushed over the hole 48. At the lower end of the upper push pin 50, a push-up ring 52 made of, for example, aluminum, which is formed in a circular ring shape, is disposed, and is supported by the push-up ring 52 in a state where the lower end of each of the upper push pins 50 is not fixed. The arm portion 54 extending from the push-up ring 52 is coupled to a telescopic rod 56 provided through the bottom portion 30 of the container, and the telescopic rod 56 is extended by an actuator 58 in 200810019 (15). In this manner, each of the upper push pins 50 is expanded and contracted downward from the upper end of each pin insertion hole 48 when the wafer W is transferred. Further, a telescopic bellows 60 is disposed in the middle of the penetrating portion of the bottom of the container of the telescopic rod 56 of the actuator 58, and the telescopic rod 56 can maintain the airtightness in the processing container 14 and ascend and descend. The opening 34 on the inlet side of the ejector space 32 is set to be smaller than the diameter of the carrier 44, and the processor body which is formed to φ outside the peripheral portion of the mounting table 44 flows below the mounting table 44 and flows to the lower side. Opening 3 4 . In the lower side wall of the above-described cylindrical portion partition wall 36, an exhaust port 62 is formed facing the exhaust space 32. The exhaust port 62 is connected to the vacuum exhaust system 64. The vacuum exhaust system 6 has a plurality of exhaust passages 66 connected to the exhaust port 62, and a pressure regulating valve 68 and a vacuum pump 70 are sequentially disposed in the exhaust passage 66, and the processing container 14 is disposed. The atmosphere of the inner and exhaust space 32 can be pressure controlled and evacuated for venting. In order to supply a specific gas to the shower head, a material gas supply means 72 for supplying a material gas and a reducing gas supply means 74 for supplying a reducing gas are connected to the shower head #1 6 '. Specifically, the raw material gas supply means 72 has a raw material gas flow path 7 8 connected to the gas inlet 76 of the gas diffusion chamber 2 2 A of the two gas diffusion chambers. Here, the material gas flow path 78 is divided into two, and one of the branch roads 80' is installed with an on-off valve 8 2 and a flow controller 84 like a mass controller in the middle of the middle, and is connected to the storage section. 1 The first raw material source of the raw material is 8 6 . In the first raw material, a transition metal-containing transition metal material is used, and an inert gas such as an Ar gas controlled by a flow rate is used to carry out the -18-200810019 (16) bubble, and the raw material is gasified, and the inert gas can be mixed. Metal raw material gas. Here, the vapor of the raw material is heated to increase the vapor pressure of the raw material, and the first raw material source is heated. The above transition metal-containing material may be obtained from j (MeCp) 2Mn (precursor). 'In addition, the supply of raw material gas is not only the use of liquid raw material gasification method or solution material gasification method. The material gasification method refers to the use of a gasifier at room temperature to make the liquid method. It means a method in which a raw material is dissolved in a solvent at room temperature to become a liquid, and a gasifier is used. This method is not only suitable for supplying Μη to supply Cu raw material gas. Further, the other branching path 8 8 is in the middle of the valve 90 and the flow controller 92 like the mass controller, and the second material source 94 of the raw material. The second raw material is made of an inert gas containing, for example, an Ar gas controlled by a flow rate, and the raw material is gasified, and may be accompanied by an inert gas - a raw material gas. Here, the vapor pressure of the raw material is very low. The vapor pressure of the raw material is raised, and the second raw material source 94 is used for electricity. As the copper-containing raw material, for example, Cu (hfac) 2, Cu (dibm) 2 or the like (precursor) containing copper may be used. Further, the above-mentioned inert gas for foaming may be replaced by He, Ne, or the like. Then, in order to prevent the material gas from being reliquefied, if the supply pressure is low, the 丨86 electric heater 86a can be electrically charged, for example, with manganese. Here, the raw material of the liquid is vaporized to allow the solution to vaporize the raw material gas in a solid or liquid state, or may be connected to the copper-containing raw material gas containing the second: copper to be activated. In the case where the copper is supplied, in order to heat the Cu (hfac) TMVS Ar gas, the heat exchanger 94a is used as a switch which is formed in the middle of the above-mentioned each -19-200810019 (17) branch roads 80 and 88 and the two branch roads. The valves 82 and 90, the flow controllers 84 and 92, and the material gas flow path 78 are wound around the belt heater 140 to heat these. Further, it is of course possible to provide a plurality of raw material gas supply means in accordance with the raw materials used. Further, the reducing gas supply means 74 has a reducing gas flow path 1A connected to the gas inlet 98 of the other gas diffusion chamber 22B. The reducing gas flow path 1 〇 〇 is provided with a switching valve 1 〇 2 and a flow controller 104 like a mass controller in the middle of the middle, and is connected to a reducing gas source 106 that houses the reducing gas. Here, the reducing gas is H2 gas, but other H20 or vaporized organic solvent may be used. Here, the material gas is connected to the gas diffusion chamber 22A located above the shower head 16 and the reducing gas is connected to the gas diffusion chamber 22B located below. This is because the shower head 16 approaches the mounting table 44 and faces each other, and the temperature of the gas ejection surface 18 tends to rise. Therefore, the material gas is introduced into the gas diffusion chamber 22B of the f-side, and the gas is decomposed. Therefore. Further, an inert gas supply means (not shown) formed for purification is connected to the shower head unit 16, and a purge gas is supplied as needed. As the purge gas, an inert gas such as N2 gas, Ar gas, He gas, or N e gas can be used. Then, in order to control the operation of the entire apparatus, the control means 108 composed of, for example, a microcomputer or the like is formed, and the control of the gas supply start or stop, the control of the supply amount, and the pressure in the processing container 4 are performed. Control, temperature control of wafer W, etc. Then, the control means 1 〇 8 has a memory medium 1 1 0 for storing a computer program for performing the above control. -20- 200810019 (18) The above-described memory medium 110 can use, for example, a floppy disk, a flash memory, a CD (Compact Disc), or the like. Next, the operation of the film forming apparatus configured as described above will be described. First, the unprocessed semiconductor wafer W is held by a transport arm (not shown), and passes through the gate valve 28 in the open state and the loading/unloading port 2 6, moved into the processing container 14 within. After the wafer W is transferred to the raised upper push pin 5 ’, the upper push pin 5 〇 is lowered and placed on the upper surface of the mounting table 44. Then, the raw material gas supply means 72 or the reducing gas supply means 74 are operated, and the flow rate control of the various types of gas, which are sent to the shower head 16 as a processing gas, and the like, are separately supplied and supplied. The gas injection holes 20A and 20B are ejected and ejected, and are introduced into the processing space S. As will be described later, the various gases have various supply forms. Then, the vacuum pump provided in the vacuum exhaust system 64 is continuously driven, and the processing container 14|% or the exhaust space 3 2 is evacuated, and then the opening degree Φ of the pressure regulating valve 6 8 is adjusted, and the processing space S is processed. The atmosphere is maintained at a specific processing pressure. At this time, the temperature of the wafer W is heated by the resistance heating heater 44 provided in the mounting table 44, and maintained at a specific processing temperature. In this way, a desired thin film is formed on the surface of the semiconductor wafer w by heat treatment such as thermal CVD.
上述含有銅原料氣體或含有錳原料氣體流動的情況, 要防止流路加熱手段96將原料氣體流路78和兩分歧路80和 8 8加熱而導致該路徑上的原料氣體液化,不過此時的加熱 溫度依照使用的原料氣體有所不同,使用Cu(hfac)TMVS -21 · 200810019 (19) 和(MeCphMn來作爲原料氣體的情況,加熱到兩種氣體都 不會液化,且不會熱分解的溫度,例如5 5〜9 0 t。另外, 噴淋頭部16和處理容器本身加熱到60〜80°C。 其次’也參考第2〜4圖來具體說明本發明的成膜方法 〇 第2圖爲表示以半導體晶圓的凹部爲中心的各步騾之 ' 薄膜的堆積狀況之圖。第3圖爲表示本發明的成膜方法的 # 各步驟之流程圖,第3(A)圖表示第1實施例,第3(B)圖表 示第2實施例。第4圖爲說明形成晶種膜時採用ALD法之 各種氣體的供應狀態之時間圖。 本發明方法的其中1個目的爲在1個成膜裝置內 (insitu)連續進行各種成膜處理和退火處理。例如,晶圓 W搬入上述成膜裝置12內時,如第2(A)圖所示,在被形成 在晶圓W的例如層間絕緣膜等之絕緣層1的表面,形成如 同溝道或孔之凹部2,由銅等所組成之下層的配線層3露出 • 到該凹部2的底部。成爲基底膜的上述絕緣層1則是由含有 矽的氧化物,例如Si〇2所組成。 ~ 於是,本發明方法係在這種狀態之半導體晶圓W的 • 表面,首先如第2(B)圖所示依照晶種膜形成步驟來形成晶 種膜6。此情況,上述晶種膜6可以是CuMn合金膜(第 3(A)圖的S1),也可以是Μη膜(第3(B)圖的S1-1)。另外 ,形成該晶種膜6,可以採用CVD法,也可以採用ALD 法。此處,ALD法是指交互地供應不同的成膜氣體來逐 層反覆形成原子標準或者分子標準的薄膜之成膜方法。 -22· 200810019 (20) 其次,如第2(C)圖所示,經由埋入步驟,形成Cii膜8 來作爲金屬膜,埋入上述凹部2內(第3(A)圖中的S2和第 3(B)圖中的S2)。該埋入步驟,可以採用CVD法,也可以 採用ALD法,還可以與習知的方法同樣,採用PVD法(濺 鍍或蒸鍍)或電鍍法。進而,爲了要確實地形成障壁膜, 若有必要的話,將晶圓W曝露在高溫中來進行退火處理 * ,如第2(D)圖所示在晶種膜6與屬於該基底層之由Si02所 φ 組成之絕緣層1的界面部分自我整合地起反應,確實地形 成由MnSixOy(x、y :任意的整數)膜所組成之障壁層12(第 3(A)圖中的S3和第3(B)圖中的S3)。此外,在已進行高濫 處理的前步驟中已經形成有障壁層1 1 2的話,該退火處理 也可以不進行,但爲了要充分地形成障壁層112,最好是 進行該退火處理。 此處,詳細說明各步驟。 首先,形成CuMn合金膜(第3(A)圖的S1)來作爲晶種 # 膜6的情況,有3種成膜方法。該第1種成膜方法爲含有Cu 原料氣體及含有Μη原料氣體及屬於還原氣體的H2氣體全 • 部同時流動,以CVD法來形成CuMn合金膜的方法。 , 第2種成膜方法係如第4(A)圖所示採用ALD法,同步 供應含有Cu原料氣體及含有Μη原料氣體,且該兩氣體 與Η2氣體交互間歇地反覆流動。上述兩氣體與η2之間的 間歇期間Τ 1爲淨化期間,可以僅在抽真空時除去處理容 器1 4內的殘留氣體,也可以導入Ν2氣體等的惰性氣體, 並抽真空來予以排除。該淨化的方法即使是以下說明的方 -23- 200810019 (21) 法也同樣適用。 該ALD法係例如從供應含有Μη原料氣體起至下一 次供應含有Μη原料氣體爲止之期間爲1週期,在這期間 形成更加薄例如0.4〜〇6 nm程度的CuMn合金膜。此處, 必要晶種膜6的厚度,換算成CuMn膜中之Μη純金屬的 膜厚’例如爲2 nm程度,則上述成膜處理要進行例如 — 〜1 00週期程度。即是進行ALD法的成膜的話,可以提 φ 高膜厚的控制性,能夠控制性良好地形成比CVD法還要 更薄的膜。 此時的處理條件(也包括CVD處理的情況),處理溫 度爲70〜450°C程度,處理壓力爲IPa〜3Pa程度。另外,含 有Μ η原料氣體的流量爲0 · 1〜1 0 s c c m程度,含有C u原料 氣體的流量爲1〜1〇〇 seem程度,無論如何,相對於Μη則 Cu變多1〇倍程度,成爲CuMn合金膜的成分中有充裕的: C u的狀態。另外,Η 2氣體的流量爲5〜5 0 0 s c c m程度。惟 φ ,C u對S i 〇2等的絕緣膜之密著性很微弱,故在成膜初期 ,也可以提高含有含有Μη原料氣體對含有Cu原料氣體 • 的流量比率,使獲得的合金膜中有充裕的Μ η。 • 進而,含有Μη原料氣體的供應期間tl爲10〜15 sec 程度,含有C u原料氣體的供應期間12爲1 0 s e c程度’ Η 2 氣體的供應期間13爲1 0 s e c程度’間歇期間Τ 1爲2 0〜1 2 0 sec程度。此處,如同上述’ Cu對Si〇2等的絕緣膜之密 著性很微弱,故在成膜初期’也可以含有Mn原料氣體的 供應期間11相對於含有C u原料·热體的f共應期間12加長’ -24- 200810019 (22) 例如也可以設定爲15 sec(第4 (A)圖中以點線121表示)。即 是可以以隨著成膜時間的經過或者依照堆積膜厚,依序變 更含有Μη原料氣體與含有Cu原料氣體的供應比率的方 式,組成處理配方。藉由此方式,也能夠將CuMn合金膜 中的成分,從Μη充裕的狀態,逐漸變成Cu充裕的狀態 。因此,可以提高絕緣層1與晶種膜6之間和晶種膜6與Cu ^ 膜8之間的密著性,又可以防止成膜中的膜剝離等。 φ 第4(A)圖所示的情況,改成令含有Μη原料氣體與含 有Cu原料氣體同步來同時供應排出,不過第3種成膜方法 爲第4(B)圖所示的ALD法,隔著間歇期間交互地反覆供 應上述兩氣體,並且在上述間歇期間時,供應H2氣體。 此情況,1週期的期間變成比上述第4(A)圖所示情況還長 出2倍。然後,成爲膜厚0.2〜0.3 nm程度非常薄的Μη膜 與膜厚0.2〜0.3 nm程度非常薄的Cu膜交互層積之合金狀 態的晶種膜6。此時,如第4(B)圖所示,剛開始的步驟’ φ 考慮到晶種膜6與絕緣層1之間的密著性和障壁性’最好是 以先行供應含有Cu原料氣體,再供應含有Μη原料氣體 . 的方式來組成步驟。此外,兩膜都非常薄,所以Μη和 _ Cu相互地進行擴散,而成爲合金狀態。 以這種的ALD法進行成膜,與以CVD法進行成膜作 比較,膜還是會充分附著在微細凹部的內壁,可以更加提 高階差覆蓋性(step coverage),尤其,凹部的尺寸愈變成 更微細化,該ALD法則愈有效果。 其次,第2(C)圖和第3(A)圖中的S2所示的金屬膜8爲 -25· 200810019 (23) 形成Cii膜的情況,可以含有Cu原料氣體及H2氣體同時 流動,以CVD法來形成由Cu膜所組成的金屬膜8,也可 以與第4(A)圖和第4(B)圖同樣,含有Cu原料氣體及112氣 體交互地反覆流動。 或者還可以H2氣體不流動,僅利用熱分解反應來形 成由Cii膜所組成的金屬膜。 〜 * 此時的處理條件(也包括CVD處理的情況),處理溫 # 度爲70〜450°C程度,處理壓力爲IPa〜13Pa程度。另外, 含有Cu原料氣體的流量爲1〜1〇〇 sccm程度,h2氣體的流 量爲5〜500 seem程度。 另外,也可以採用習知的PVD法(濺鍍或蒸鍍)或電鍍‘ 法,形成上述由Cu膜所組成的金屬膜8,進行埋入。 尤其,CVD法或ALD法的情況,薄膜比電鍍法還容 易堆積到微細凹部的內壁,所以即使凹部更加微細化,仍: 可以在內部不產生針孔下進行凹部的埋入。 ® 其次,進行第2(D)圖和第3(A)圖中的S3所示的退火 處理的情況,將上述埋入處理已經結束的晶圓W,加熱到 • 特定的處理溫度,例如100〜450°C程度,藉由此方式,將 . 自我整合地由 MnSixOy膜所組成的障壁層1 12,確實地形 成在晶種膜6與由成爲基底膜的Si02膜所組成之絕緣膜1 的界面部分。此外,也可以設定爲退火處理時,從酵素供 應手段73a來將氧供應至處理容器內,成爲可控制氧分壓 的構成。 該退火處理的目的是要確實地形成上述障壁層112, -26- 200810019 (24) 因此,屬於前步驟的晶種膜形成步驟或C u膜形成步驟在 非常高的溫度,例如1 5 0 °C以上的高溫之處理溫度下進行 的話,上述障壁層1 1 3會變成已形成有足夠厚度的狀態, 所以可以不必進行上述退火處理。此外,依照如第3 (A)圖 中的S2來進行電鍍處理的情況,當然要進行上述退火處 理。 . 此處,上述晶種膜形成步驟、以CVD法或ALD法進 φ 行Cii膜形成步驟以及退火處理,可以全部都在相同的處 理裝置1 2內連續進行。 如此,在可抽真空的處理容器1 4內,利用含有銅的含 有Cu原料氣體及含有屬於過渡金屬的錳的含有Μη原料 氣體及屬於還原氣體的Η2氣體,經由熱處理,將薄膜形 成在晶圓W的表面,所以即使是微細的凹部2,仍可以以; 很局的階差覆蓋性(step coverage)來進行埋入。而且,在: 相同的處理裝置1 2連續進行處理,可以大幅降低裝置成本 另外,可以在相同的裝置12內,即是可以在in-Situ ^ 連續進行處理,所以形成不必要的金屬氧化膜會受到抑制 . ’該結果,可以改善埋入性,並且可以防止接觸電阻變大 ’甚致於可以達到提高半導體裝置的可靠度、改善良品率 〇 另外,形成習知必要的由Ta膜或TaN膜等所組成之 障壁層的步驟則變成不必要,這部分可以使流量提高。 進而,使用CuMn合金膜來作爲晶種膜6的情況,會 -27- 200810019 (25) 局部含有屬於埋入材料的Cll,所以可以提高與該上層之 金屬膜8的密著性。 此處,針對前述過的C u Μ η膜中之C u及Μ η的比率 ’即是針對使這些元素的組成比變化的這點更詳細地進行 說明。 第5圖爲表示隨著成膜時間(熱處理)的經過變化含有 " Μη原料氣體及含有Cu原料氣體的供應量的一個例子之 # 圖形。此外,圖形中,僅是表示供應量的變化趨勢,並不 是表示供應量的絕對値。 此處’如前述過,爲了要在上述薄膜的膜厚方向上, 令上述薄膜中的Cu與屬於過渡金屬的例如Μη之組成比 變化’在上述熱處理的中途就令上述含有銅原料氣體及/ 或上述含有過渡金屬原料氣體的供應量變化。具體上,以 屬於薄膜之CuMn膜的薄膜中之前述過渡金屬的組成比, 上述薄膜內的下層側很大,愈往上層側則愈小的方式,控 ® 制上述各原料氣體的供應量。即是如第5 (A)圖所示,成膜 初期,含有Μη原料氣體以很大的流量流動,經過一段時 * 間之後,隨著成膜時間的經過,依序例如令流量呈直線減 * 少後,最後流量變成大約零。 針對此點,成膜初期,含有Cu原料氣體會有一段時 間幾乎不流動,形成純Μ η金屬膜,然後,對應於含有 Μη原料氣體的減少,隨著成膜時間的經過,令含有Cu 原料氣體的流量,例如呈直線增加,最後將含有Μη原料 氣體的供應量維持在零,而將含有C u原料氣體的流量維 -28 - 200810019 (26) 持最大,進行成膜,此處則是形成純Cu金屬膜。 此情況的薄膜,在成膜的初期爲純Μη金屬膜,最後 變成C U Μ η合金,持續維持Μ η充裕的狀態,中途會反轉 成Cu充裕的狀態,最後變成純Cu金屬膜。 第5(B)圖中,從開始進行成膜起,Μη原料氣體由一 定的供應量起逐漸減少,含有Μη原料氣體反而由零供應 量起逐漸增加。此情況,薄膜的厚度方向的全體均變成 馨 CuMn膜,不會形成如同第5(A)圖所示的純Μη金屬膜或 純Cu金屬膜。此外,第5(A)圖和第5(B)圖中,成爲直線 狀增加的特性或減少的特性,不過也可調整各種原料氣體 的供應量,致使變成曲線狀增加的特性或減少的特性,以 取代該直線狀的特性。 上述第5(A)圖和第5(B)圖的情況,CuMn合金膜的部 分內’ Cu與Μη的組成比,從模厚的下面朝向上方,連 續地從Μη充裕的狀態變成Cu充裕的狀態。第5(C)圖所 ® 示的情況,呈現:令含有Μη原料氣體呈階段地減少,相 對於此’令含有Cu原料氣體呈階段地增加的情況。此情 況下,CuMn合金膜中的Cu與Μη的組成比則呈階段地變 ^ 化。此外,該階段的數量並沒有特別的限定。 上述第5(A)圖〜第5(C)圖所示的情況,膜中的下層變 成純Μη金屬膜或Μη充裕的CuMn合金,上層則變成含 有CU原料氣體或Cu充裕的CuMn合金,所以如同前述過 ’可以更提高基底膜Si 02與Cu膜8的密著性。 另外,上述實施例中,以例子來說明形成CuMn合金 -29- 200810019 (27) 膜來作爲晶種膜6的情況(第3 (A)的SI),不過也如同上述 過,可以形成Μη膜(第3(B)的S卜1)來作爲晶種膜6。形成 該Μη膜的情況,可以採用:含有Μη原料氣體和屬於還 原氣體的Η2氣體同時流通,以CVD法來形成的方法、及 上述含有Μη原料氣體和Η2氣體,如第4(C)圖所示,交互 地反覆流通,以A L D法來形成的方法的任一方法。此情 ’ 況的處理條件,例如處理壓力、處理溫度、各氣體的流量 φ 等,與利用第4(A)圖和第4(B)圖說明過的情況同樣。另外 ,第3(B)圖中的S2和S3爲與第3(A)圖中的S2和S3相同內 容的步驟,即使該情況也是在前步驟充分形成障壁層1 1 2 的話,可以省略第3(B)圖中的S3的退火處理。進而,即 使是將Cu膜堆積在Μη膜上的情況,仍是在in-situ處理 該兩膜,可以提高該兩金屬彼此間的密著性。 形成Μη膜來作爲晶種膜6的情況,上層的Cu配線層 8形成爲在凹部2的底部,藉由電阻値大於Cu膜的Μη膜 # ,連接至下層的Cu配線層3。但是,該晶種膜6比習知的 濺鍍所形成的Μη膜還要更薄,所以經過退火處理等,Μη * 元素大部分會擴散到Cu配線層3和Cu配線層8中,Μη層 . 則不會存在,所以該部分的接觸電阻不會變高。 另外,屬於上述薄膜之CiiMn膜中(也包括具有純Μη 金屬膜或純Cu金屬膜的情況)或Μη膜中之Μη金屬的量 有最適當的値,該値換算成Μη的純金屬膜厚則爲0.7〜2.6 nm的範圍內,以符合上述Μη金屬膜之換算値得範圍內 的方式來形成上述薄膜較佳。即是在退火步驟,如前述過 -30- 200810019 (28) Μη經過化合來變成MnSixOy膜,另外,剩餘的Μη —定 程度藉由擴散到Cu膜內來排出到表面,不過Μη量過度 含在膜中會導致尙未完全排出的Μη成分殘留在埋入凹部 的Cu膜中,該殘留的Μη部分導致上升Cu配線的電阻値 會使配線的可靠度下降。 此情況,薄膜中的Μη含量換算成如同上述的Μη之 • 純金屬的膜厚來設定在0.7〜2.6 nm的範圍內,可以讓必要 % 足夠量的Μη量保持在Cu配線與絕緣層的成爲界面之障 壁層。上述Μ η量小於厚度〇 · 7 n m的話,無法作成特性良 好的障壁層,然則,大於2.6 nm的話,如上述過,過剩量 的Μη成分會殘存在Cu配線中,導致該膜質特性的劣化 〇 此外,第1圖所示的裝置例子中,原料氣體供應手段 72之2種原料氣體的流路在中途會合在一起,但並不侷限 於此,也可以以兩種原料分開的方式構成。第6圖爲表示 % 這種構成的成膜裝置之原料氣體供應手段的變形例之構成 圖。第6圖所示的情況爲表示噴淋頭部1 6及與該噴淋頭部 • 相連接之原料氣體供應手段72,有關與第1圖所示的構成 , 部分相同的構成部分則是附註相同的圖號。 此處則是從含有Μη的第1原料源86和含有Cu的第2 原料源,分別延伸原料氣體流路1 2 0、1 2 2。然後,該各原 料氣體流路120、122在中途不會會合,各前端直接連接至 噴淋頭部1 6所共同的氣體入口 7 6,以在原料氣體的搬運中 途兩者不會相互混合,就導入到噴淋頭部1 6內的方式構成 -31 - 200810019 (29) 此情況也是在上述各原料氣體流路1 20、1 22,繞捲設 置由例如帶式電熱器逖組成之流路加熱手段96a、96b,加 熱來使流到該流路的各種原料氣體不會液化。此情況可以 以對應於流動的原料氣體之最適當的溫度來分別將上述各 原料氣體流路120、122予以加熱並予以維持。具體上,使 用(MeCp)2Mii來作爲原料的情況,設定成··流路加熱手段 96a例如在70〜90°C的範圍進行加熱,使用 Cu(hfac)TM V S 來作爲原料的情況,設定成:流路加熱手段96b例如在 5 5〜7 0°C的範圍進行加熱。此情況,可以發揮與先前說明 過的情況同樣的作用效果。 另外,上述有機金屬材料,並不侷限於先前說明過的 材料,若爲由過渡金屬和C (碳)和Η(氫)所組成的材料的 話,任何一種材料均可以使用。有機金屬材料可以採用 M(R-CP)x(x爲自然數),或是可以採用M(R-Cp)x(CO)y(x 、y爲自然數)。惟,Μ表示過渡金屬,R表示烷基,由Η 、CH3、C2H5、C3H7、C4H9的群體當中所選出的1種,Cp 爲環戊烷二烯基((^〇1〇1^1^311以61^1;(:5:»4),(:0爲羰基 (carbonyl)。 另外,採用上述含有Μη原料的有機金屬材料,可以 採用由 Cp2Mn[ = Mn(C5H5)2]、(MeCp)2Mn[ = Mn(CH3C5H4)2] 、(EtCp)2Mn[ = Mn(C2H6C5H4)2]、(i-PrCp)2Mn[ = Mn(C3H7C5H4)2] 、MeCpMn(CO)3[ = (CH3C5H4)Mn(CO)3]、 (t-BuCp)2Mn[ = Mn(C4H9C5H4)2]、CH3Mn(CO)5、 •32- 200810019 (30)In the case where the copper-containing material gas or the manganese-containing material gas flows, the flow path heating means 96 prevents the material gas flow path 78 and the two branch paths 80 and 8 from heating to cause the material gas in the path to liquefy, but at this time The heating temperature varies depending on the raw material gas used. When Cu(hfac)TMVS -21 · 200810019 (19) and (MeCphMn are used as the raw material gas, heating to neither of the two gases will be liquefied and will not thermally decompose. The temperature is, for example, 5 5 to 9 0 t. In addition, the shower head 16 and the processing container itself are heated to 60 to 80 ° C. Next, the film forming method of the present invention will be specifically described with reference to FIGS. 2 to 4 The figure shows the deposition state of the film in each step centering on the concave portion of the semiconductor wafer. Fig. 3 is a flow chart showing the steps of the film formation method of the present invention, and Fig. 3(A) shows In the first embodiment, Fig. 3(B) shows a second embodiment. Fig. 4 is a timing chart for explaining the supply state of various gases by the ALD method in forming a seed crystal film. One of the objects of the method of the present invention is One film forming device (insitu) continuously carries out various kinds For example, when the wafer W is carried into the film forming apparatus 12, as shown in FIG. 2(A), on the surface of the insulating layer 1 such as an interlayer insulating film formed on the wafer W, A recess 2 is formed like a channel or a hole, and a wiring layer 3 composed of a layer of copper or the like is exposed to the bottom of the recess 2. The insulating layer 1 which becomes a base film is an oxide containing germanium, such as Si 2. The composition of the present invention is such that the method of the present invention is based on the surface of the semiconductor wafer W in this state, first forming the seed film 6 in accordance with the seed film forming step as shown in Fig. 2(B). The seed film 6 may be a CuMn alloy film (S1 in Fig. 3(A)) or a Μn film (S1-1 in Fig. 3(B)). Further, the seed film 6 may be formed. In the CVD method, the ALD method can also be used. Here, the ALD method refers to a film forming method in which different film forming gases are alternately supplied to form a film of an atomic standard or a molecular standard layer by layer. -22· 200810019 (20) Second, As shown in FIG. 2(C), the Cii film 8 is formed as a metal film through the embedding step, and the recess 2 is buried. (S2 in Fig. 3(A) and S2 in Fig. 3(B)). The embedding step may be a CVD method or an ALD method, or may be the same as the conventional method, using a PVD method. (sputtering or vapor deposition) or electroplating. Further, in order to form the barrier film reliably, if necessary, the wafer W is exposed to a high temperature for annealing treatment*, as shown in Fig. 2(D) The seed film 6 is self-integratingly reacted with the interface portion of the insulating layer 1 composed of SiO 2 which belongs to the underlying layer, and the barrier layer 12 composed of the MnSixOy (x, y: arbitrary integer) film is surely formed ( S3 in Fig. 3(A) and S3) in Fig. 3(B). Further, if the barrier layer 11 is already formed in the previous step in which the high-disposal treatment has been performed, the annealing treatment may not be performed, but in order to sufficiently form the barrier layer 112, it is preferable to carry out the annealing treatment. Here, each step will be described in detail. First, in the case of forming a CuMn alloy film (S1 in Fig. 3(A)) as the seed crystal film 6, there are three kinds of film forming methods. In the first method of forming a film, a method of forming a CuMn alloy film by a CVD method is carried out by simultaneously flowing a Cu source gas and a gas containing a Μη material and a H2 gas belonging to a reducing gas. The second film forming method is an ALD method as shown in Fig. 4(A), and a Cu-containing material gas and a Μn-containing material gas are synchronously supplied, and the two gases alternately flow alternately with the Η2 gas. The intermittent period Τ 1 between the two gases and η 2 is a purification period, and the residual gas in the processing container 14 may be removed only during evacuation, or an inert gas such as Ν 2 gas may be introduced and evacuated to be removed. This method of purification is also applicable to the method described in the following section -23-200810019 (21). This ALD method is, for example, a period from the supply of the Μη-containing raw material gas to the next supply of the Μn-containing raw material gas, and a CuMn alloy film having a thickness of, for example, about 0.4 to 〇6 nm is formed during this period. Here, the thickness of the seed crystal film 6 is required to be, for example, about 2 nm in terms of the film thickness η of the Mn pure metal in the CuMn film. The film forming process is performed, for example, to about 10,000 cycles. In other words, when the film formation by the ALD method is performed, the controllability of φ high film thickness can be improved, and a film thinner than the CVD method can be formed with good controllability. The processing conditions at this time (including the case of CVD treatment), the treatment temperature is about 70 to 450 ° C, and the treatment pressure is about IPa to 3 Pa. Further, the flow rate of the raw material gas containing Μη is about 0·1 to 10 sccm, and the flow rate of the material containing the Cu raw material is about 1 to 1 〇〇seem, and in any case, the Cu becomes 1 times more than the Μη. There is ample: C u in the composition of the CuMn alloy film. Further, the flow rate of the Η 2 gas is about 5 to 5 0 s c c m . However, the adhesion of φ and C u to the insulating film such as S i 〇 2 is very weak. Therefore, in the initial stage of film formation, the flow ratio of the gas containing the raw material gas containing Μη to the raw material containing Cu can be increased. There is ample Μ η in it. Further, the supply period t1 containing the 原料n material gas is about 10 to 15 sec, and the supply period 12 containing the C u source gas is about 10 sec' Η 2 The supply period 13 of the gas is about 10 sec. 'Intermittent period Τ 1 It is 2 0~1 2 0 sec. Here, as described above, the adhesion of the insulating film of Cu to Si〇2 is weak, so that the supply period 11 of the Mn source gas may be contained in the initial stage of film formation with respect to the f containing the Cu raw material and the hot body. The period 12 should be lengthened ' -24- 200810019 (22) For example, it can be set to 15 sec (indicated by the dotted line 121 in the figure 4 (A)). That is, it is possible to form a treatment formulation by sequentially changing the supply ratio of the 原料η source gas and the Cu-containing material gas in accordance with the film formation time or in accordance with the thickness of the deposited film. In this way, the components in the CuMn alloy film can be gradually changed from the state in which the Μn is abundant to the state in which Cu is abundant. Therefore, the adhesion between the insulating layer 1 and the seed crystal film 6 and between the seed crystal film 6 and the Cu ^ film 8 can be improved, and peeling of the film during film formation or the like can be prevented. φ In the case shown in Fig. 4(A), the η method is the ALD method shown in Fig. 4(B), in which the 原料η source gas and the Cu source gas are simultaneously supplied and discharged. The above two gases are alternately supplied alternately during the intermittent period, and during the above-described intermittent period, the H 2 gas is supplied. In this case, the period of one cycle becomes twice as long as the case shown in the fourth (A) above. Then, it is a seed crystal film 6 in an alloy state in which an Μη film having a film thickness of 0.2 to 0.3 nm and a film film having a very small thickness of 0.2 to 0.3 nm is alternately laminated. At this time, as shown in Fig. 4(B), the initial step 'φ considers that the adhesion between the seed film 6 and the insulating layer 1 and the barrier property' is preferably supplied in advance to contain the Cu source gas. The step of constituting the step is also carried out by supplying a gas containing Μη. Further, both films are very thin, so Μη and _Cu are mutually diffused to become an alloy state. When the film formation is performed by the ALD method, the film adheres sufficiently to the inner wall of the fine concave portion as compared with the film formation by the CVD method, and the step coverage can be further improved. In particular, the size of the concave portion is increased. It becomes more refined, and the ALD rule becomes more effective. Next, the metal film 8 shown in S2 in the second (C) and the third (A) is -25. 200810019 (23). When the Cii film is formed, the Cu material gas and the H2 gas may be simultaneously flowed. The metal film 8 composed of the Cu film is formed by the CVD method, and similarly to the fourth (A) and fourth (B) views, the Cu source gas and the 112 gas may alternately flow in reverse. Alternatively, it is also possible that the H2 gas does not flow, and only the thermal decomposition reaction is used to form a metal film composed of the Cii film. ~ * Processing conditions at this time (including the case of CVD treatment), the treatment temperature is about 70 to 450 ° C, and the treatment pressure is about IPa to 13 Pa. Further, the flow rate of the raw material gas containing Cu is about 1 to 1 〇〇 sccm, and the flow rate of the h2 gas is about 5 to 500 seem. Alternatively, the metal film 8 composed of the Cu film described above may be formed by a conventional PVD method (sputtering or vapor deposition) or plating method to be buried. In particular, in the case of the CVD method or the ALD method, since the film can be easily deposited on the inner wall of the fine concave portion by the plating method, even if the concave portion is made finer, the concave portion can be buried without generating pinholes inside. Next, in the case of the annealing treatment shown by S3 in the second (D) diagram and the third (A) diagram, the wafer W in which the embedding process has been completed is heated to a specific processing temperature, for example, 100. At a temperature of about 450 ° C, the barrier layer 12 formed of a MnSixOy film by self-integration is surely formed on the seed film 6 and the insulating film 1 composed of the SiO 2 film which becomes the base film. Interface section. Further, when the annealing treatment is performed, oxygen may be supplied from the enzyme supply means 73a to the processing container to control the oxygen partial pressure. The purpose of the annealing treatment is to form the barrier layer 112 as described above, -26-200810019 (24) Therefore, the seed film forming step or the Cu film forming step belonging to the previous step is at a very high temperature, for example, 1 50 °. When the temperature is higher than the processing temperature of C or higher, the barrier layer 1 1 3 is formed to have a sufficient thickness, so that the annealing treatment described above is unnecessary. Further, in the case where the plating treatment is carried out in accordance with S2 in Fig. 3(A), the annealing treatment described above is of course performed. Here, the seed crystal film forming step, the Cii film forming step and the annealing treatment by the CVD method or the ALD method may all be continuously performed in the same processing apparatus 1 2 . In the vacuum-processable processing container 14 , a film containing a Cu-containing raw material gas containing copper and a Mn-containing raw material gas containing a manganese-containing transition metal and a ruthenium-containing gas belonging to a reducing gas are formed on the wafer by heat treatment. The surface of W, so even if it is a fine recess 2, it can be buried with a very large step coverage. Further, in the case where the same processing device 12 is continuously processed, the cost of the device can be greatly reduced. Further, it can be continuously processed in the same device 12, that is, in-Situ ^, so that an unnecessary metal oxide film is formed. It is suppressed. 'The result is that the embedding property can be improved, and the contact resistance can be prevented from becoming large. It is possible to improve the reliability of the semiconductor device and improve the yield. In addition, it is necessary to form a Ta film or a TaN film which is conventionally necessary. The steps of forming the barrier layer become unnecessary, and this part can increase the flow rate. Further, in the case where the CuMn alloy film is used as the seed film 6, the C11 belonging to the buried material is partially contained in -27-200810019 (25), so that the adhesion to the metal film 8 of the upper layer can be improved. Here, the ratio of C u and Μ η in the above-mentioned C u Μ η film is described in more detail with respect to the change in the composition ratio of these elements. Fig. 5 is a graph showing an example of the supply amount of the "Μη material gas and the Cu-containing material gas, as the film formation time (heat treatment) is changed. In addition, in the graph, it only indicates the trend of supply, and it is not the absolute flaw of supply. Here, as described above, in order to change the composition ratio of Cu in the film to the transition metal, for example, Μ in the film thickness direction of the film, the copper-containing material gas and/or the above-mentioned copper-containing material gas and/or Or the supply amount of the above-mentioned transition metal-containing gas is changed. Specifically, the composition ratio of the transition metal in the film of the CuMn film belonging to the film is such that the lower layer side in the film is large, and the smaller the upper layer side is, the more the supply amount of each of the above-mentioned raw material gases is controlled. That is, as shown in Fig. 5(A), in the initial stage of film formation, the raw material gas containing Μη flows at a large flow rate, and after a period of time, the flow rate is linearly reduced in sequence, as time passes through the film formation time. * After a few, the last flow becomes about zero. In this regard, at the initial stage of film formation, the Cu-containing material gas hardly flows for a while to form a pure Μ 金属 metal film, and then, corresponding to the reduction of the Μη-containing material gas, the Cu-containing material is required to follow the film formation time. The flow rate of the gas increases, for example, in a straight line. Finally, the supply amount of the raw material gas containing Μη is maintained at zero, and the flow rate of the gas containing the Cu raw material is maintained at 280 - 200810019 (26) to form a film, and here, A pure Cu metal film is formed. In this case, the film is a pure Μ 金属 metal film at the beginning of film formation, and finally becomes a C U Μ η alloy, and the Μ η is sufficiently maintained, and is reversed to a state where Cu is abundant in the middle, and finally becomes a pure Cu metal film. In Fig. 5(B), since the film formation is started, the 原料η material gas is gradually decreased from a certain supply amount, and the Μη source gas is gradually increased from the zero supply. In this case, the entire thickness direction of the film becomes a sinuous CuMn film, and a pure Μn metal film or a pure Cu metal film as shown in Fig. 5(A) is not formed. In addition, in the fifth (A) diagram and the fifth (B) diagram, the characteristic is increased linearly or the characteristic is reduced. However, the supply amount of each of the material gases can be adjusted to cause a characteristic that is curved or increased. To replace this linear characteristic. In the case of the fifth (A) and the fifth (B), the composition ratio of 'Cu to Μ η in the portion of the CuMn alloy film is continuously increased from the state of the Μη to the Cu. status. In the case shown in Fig. 5(C), the case where the raw material gas containing Μη is gradually reduced, and the content of the raw material containing Cu is increased stepwise. In this case, the composition ratio of Cu to Μη in the CuMn alloy film is gradually changed. In addition, the number of stages is not particularly limited. In the case of the fifth (A) to the fifth (C), the lower layer in the film becomes a pure tantalum metal film or a CuMn alloy which is rich in Μη, and the upper layer becomes a CuMn alloy containing a CU source gas or Cu. As described above, the adhesion of the base film Si 02 and the Cu film 8 can be further improved. Further, in the above-described embodiment, the case where the CuMn alloy -29-200810019 (27) film is formed as the seed film 6 (SI of the third (A)) will be described by way of example, but as described above, the Μη film may be formed. (Sb 1 of the third (B)) is used as the seed film 6. In the case of forming the Μn film, a method in which a 原料n source gas and a Η2 gas belonging to a reducing gas are simultaneously flowed, formed by a CVD method, and the above-mentioned 原料n-containing material gas and Η2 gas can be used, as shown in FIG. 4(C) Any method of forming a method by ALD by alternately circulating in an alternating manner. The processing conditions in this case, such as the processing pressure, the processing temperature, and the flow rate φ of each gas, are the same as those described using the fourth (A) and fourth (B) drawings. Further, S2 and S3 in the third (B) diagram are the same as the steps S2 and S3 in the third (A) diagram, and even if this is the case, the barrier layer 1 1 2 is sufficiently formed in the previous step, the description may be omitted. 3 (B) Annealing treatment of S3 in the figure. Further, even in the case where the Cu film is deposited on the Μη film, the two films are treated in the in-situ, and the adhesion between the two metals can be improved. In the case where the Μn film is formed as the seed film 6, the upper Cu wiring layer 8 is formed at the bottom of the concave portion 2, and is connected to the lower Cu wiring layer 3 by the Μ? film # whose resistance 値 is larger than that of the Cu film. However, the seed film 6 is thinner than the tantalum film formed by conventional sputtering, so that most of the Μη* element is diffused into the Cu wiring layer 3 and the Cu wiring layer 8 after annealing treatment or the like, and the Μn layer It does not exist, so the contact resistance of this part does not become high. Further, the amount of the Μn metal in the CiiMn film belonging to the above film (including the case of having a pure Μn metal film or a pure Cu metal film) or the Μη film has the most suitable 値, and the 値 is converted into a pure metal film thickness of Μη. In the range of 0.7 to 2.6 nm, it is preferable to form the above film in such a manner as to conform to the range of conversion of the above-mentioned Μn metal film. That is, in the annealing step, as described above, -30-200810019 (28) Μη is compounded to become a MnSixOy film, and the remaining Μη is discharged to the surface by diffusion into the Cu film, but the amount of Μη is excessively contained. In the film, the Μn component which is not completely discharged is left in the Cu film buried in the concave portion, and the residual Μn portion causes the resistance of the rising Cu wiring to deteriorate the reliability of the wiring. In this case, the content of Μη in the film is set to be in the range of 0.7 to 2.6 nm as in the above-mentioned Μη• pure metal film thickness, so that a sufficient amount of Μη can be maintained in the Cu wiring and the insulating layer. The barrier layer of the interface. When the amount of Μ η is less than the thickness 〇·7 nm, a barrier layer having good characteristics cannot be formed. However, if it is larger than 2.6 nm, as described above, an excessive amount of Μη component may remain in the Cu wiring, resulting in deterioration of the film quality. Further, in the example of the apparatus shown in Fig. 1, the flow paths of the two kinds of material gases of the material gas supply means 72 are combined in the middle, but the invention is not limited thereto, and the two types of materials may be separated. Fig. 6 is a view showing a configuration of a modification of the material gas supply means of the film forming apparatus having such a configuration. The case shown in Fig. 6 shows the shower head 16 and the material gas supply means 72 connected to the shower head, and the same components as those shown in Fig. 1 are the same. The same figure number. Here, the raw material gas flow paths 1 2 0 and 1 2 2 are respectively extended from the first raw material source 86 containing Μη and the second raw material source containing Cu. Then, the respective material gas channels 120 and 122 do not meet in the middle, and the respective tips are directly connected to the gas inlets 76 of the shower heads 16 so that they do not mix with each other during the transportation of the material gases. In the case of being introduced into the shower head 16 - 31 - 200810019 (29) In this case, in each of the above-mentioned material gas flow paths 1 20, 1 22, a flow path composed of, for example, a belt type electric heater 绕 is provided. The heating means 96a, 96b are heated so that the various raw material gases flowing into the flow path are not liquefied. In this case, the respective material gas channels 120 and 122 can be respectively heated and maintained at an optimum temperature corresponding to the flowing material gas. Specifically, when (MeCp) 2Mii is used as a raw material, the flow path heating means 96a is heated, for example, in a range of 70 to 90 ° C, and Cu (hfac) TM VS is used as a raw material, and is set to The flow path heating means 96b is heated, for example, in the range of 5 5 to 70 °C. In this case, the same effects as those described previously can be exerted. Further, the above organometallic material is not limited to the material previously described, and any material may be used if it is composed of a transition metal and C (carbon) and hydrazine (hydrogen). The organometallic material may be M(R-CP)x (x is a natural number), or M(R-Cp)x(CO)y (x, y is a natural number). However, Μ represents a transition metal, R represents an alkyl group, and one selected from the group consisting of Η, CH3, C2H5, C3H7, and C4H9, and Cp is a cyclopentadienyl group ((^〇1〇1^1^311 Taking 61^1; (:5:»4), (:0 is a carbonyl group. In addition, the above-mentioned organometallic material containing the Μn raw material may be used by Cp2Mn[= Mn(C5H5)2], (MeCp) 2Mn[ = Mn(CH3C5H4)2] , (EtCp)2Mn[ = Mn(C2H6C5H4)2], (i-PrCp)2Mn[ = Mn(C3H7C5H4)2], MeCpMn(CO)3[ = (CH3C5H4)Mn( CO)3], (t-BuCp)2Mn[= Mn(C4H9C5H4)2], CH3Mn(CO)5, •32- 200810019 (30)
Mn(DPM)3[ = Mn(C1 jHi9〇2)3] 'Mn(DPM)3[ = Mn(C1 jHi9〇2)3] '
Mn(DMPD(EtCp)[ = Mn(C7HiiC2H5C5H4))、Mn (DMPD(EtCp)[ = Mn(C7HiiC2H5C5H4)),
Mn(acac)2[ = Mn(C5H7〇2)2]、Mn(DPM)2[ = Mn(CiiHi9〇2)2]、 Mn(acac)3[ = Mn(C5H7〇2)3]、Mn(hfac)2[ = Mn(C5HF602)3 ]的 群體當中所選出之1種以上的材料。另外,可以採用有機 金屬材料,其他還可以採用金屬錯體材料。 另外,此處則是以例子來說明使用si〇2來作爲屬於 基底膜的絕緣層1的情況,不過並不侷限於此,也可以採 用屬於作爲層間絕緣層使用之Low-k(低介電常數)材料之 SiOC膜、SiCOH膜,具體上,上述基底膜可以採用Si02 膜(包含熱氧化膜及電漿TEOS膜)及SiOC膜及SiCOH膜 及SiCN膜及多孔質氧化矽膜及多孔質甲基倍半矽氧烷 (methylsilsesquioxane ; MSQ)膜及聚丙炔膜及 SiLK(商標 名)膜及氟碳(fluorocarbon)膜的群體當中所選出的1種膜、 或這些的層積膜。 、另外,此處則是使用H2氣體來作爲還原氣體,但其 他還可以使用Η 2 Ο或氣化過的有機溶劑,例如乙醇、異 丙醇、丙酮、己烷、辛烷、乙酸丁酯(butyl acetate)等。 進而,此處則是以例子來說明使用Μη來作爲過渡金 屬的情況,不過並不侷限於此,可以使用其他的過度金屬 ,例如從 Mn、Nb、Zr、Cr、V、Υ、Pd、Ni、Pt、Rh、Tc 、A1、Mg、Sn、Ge、Ti、Re的群體當中所選出之1種以 上的金屬。 另外,此處說明過的成膜裝置只不過是例子而已,例 -33- 200810019 (31) 如加熱手段,也可以採用鹵素燈等的加熱燈來取代電阻加 熱電熱器,處理裝置不單是單片式,也可以是批次式。 進而,並不侷限於熱處理進行成膜,也可以例如將噴 淋頭部16作爲上部電極,將載置台作爲下部電極,因應於 需求,將高頻電力施加至兩電極間來形成電漿,也可以在 成膜時加裝電漿輔助裝置。 - 進而,此處雖是以例子來說明了被處理體的半導體晶 φ 圓,但並不侷限於此,即使玻璃基板、L C D基板、陶瓷基 板等都可以適用本發明。 【圖式簡單說明】 第1圖爲表示本發明的成膜裝置的一個例子之構成圖 〇 第2(A)、(B)、(C)、(D)圖爲表示以半導體晶圓的凹瓿 爲中心之各步驟中薄膜的堆積狀況之圖。 φ 第3(A)、(B)圖爲表示本發明的成膜方法的各步驟之 流程圖。 , 第4(A)、(B)、(C)圖爲說明形成晶種膜時ALD法的各 - 氣體的供應狀態之時間圖。 第5圖爲表示隨著成膜時間和熱處理的堆積,變化含 有Μη原料氣體及含有Cu原料氣體的供應量的一個例子 之圖形。 第6圖爲表示成膜裝置之原料氣體供應手段的變形例 之部分構成圖。 -34- 200810019 (32) 第7(A)、(B)、(C)圖爲表示半導體晶圚的凹部之一般 的埋入步驟之圖。 【主要元件符號說明】 1 :絕緣層 ' 2 :凹部 _ 3 :配線層 4 :障壁層 6 :晶種膜 8 :金屬膜 1 2 :成膜裝置 1 4 :處理容器 1 6 :噴淋頭部 1 8 :氣體噴射面 _ 20A :氣體噴射孔 20B :氣體噴射孔 ^ 22A :氣體擴散室 - 22B :氣體擴散室 24 :密封構件 26 :搬進搬出口 28 :閘閥 3 0 :容器底部 32 :排氣空間 -35- 200810019 (33) 34 :開口 3 6 :圓筒區隔壁 3 8 :圓筒區隔壁底部 40 :載置台構造 4 2 :支柱 44 :載置台 ^ 46 :電阻加熱電熱器 • 48 :銷插入孔 50 :上推銷 52 :上推環 54 :臂部 5 6 :伸縮桿 5 8 :致動器 60 :蛇腹 62 :排氣口 _ 64 :真空排氣系統 66 :排氣通路 - 68 :壓力調整閥 - 7 0 :真空幫浦 72 :原料氣體供應手段 74 :還原氣體供應手段 76 :氣體入口 78 :原料氣體流路 8 〇 :分歧路 -36- 200810019 (34) 82 :開關閥 84 :流量控制器 8 6 :第1原料源 86a :電熱器 8 8 :分歧路 90 :開關閥 ~ 92 :流量控制器 φ 94 :第2原料源 94a :電熱器 96 a :流路加熱手段 96b :流路加熱手段 98 :氣體入口 100 :還原氣體流路 102 :開關閥 104 :流量控制器 _ 106 :還原氣體源 1 0 8 :控制手段 - 11 〇 :記憶媒體 , 1 1 2 :障壁層 120 :原料氣体流路 122 :原料氣体流路 -37Mn(acac)2[= Mn(C5H7〇2)2], Mn(DPM)2[= Mn(CiiHi9〇2)2], Mn(acac)3[= Mn(C5H7〇2)3], Mn( One or more materials selected from the group of hfac) 2 [ = Mn(C5HF602) 3 ]. Alternatively, an organometallic material may be used, and other metal dislocation materials may also be used. Here, the case where si〇2 is used as the insulating layer 1 belonging to the base film will be described by way of example, but it is not limited thereto, and Low-k (low dielectric) which is used as the interlayer insulating layer may be used. The SiOC film (including the thermal oxide film and the plasma TEOS film), the SiOC film and the SiCOH film, the SiCN film, the porous yttrium oxide film, and the porous body A can be used as the base film. A film selected from the group consisting of a methylsilsesquioxane (MSQ) film and a polypropyne film and a SiLK (trade name) film and a fluorocarbon film, or a laminated film of these. In addition, here, H2 gas is used as the reducing gas, but other organic solvents such as ethanol, isopropanol, acetone, hexane, octane, and butyl acetate may be used. Butyl acetate) and so on. Further, here, the case where Μη is used as the transition metal will be described by way of example, but it is not limited thereto, and other excessive metals such as Mn, Nb, Zr, Cr, V, yttrium, Pd, Ni may be used. One or more metals selected from the group consisting of Pt, Rh, Tc, A1, Mg, Sn, Ge, Ti, and Re. In addition, the film forming apparatus described here is merely an example. For example, in the heating means, a heating lamp such as a halogen lamp may be used instead of the resistance heating electric heater, and the processing apparatus is not only a single piece. It can also be batch type. Further, for example, the shower head 16 is not used as the upper electrode, and the mounting table is used as the lower electrode. For example, high-frequency power is applied between the electrodes to form a plasma. A plasma auxiliary device can be added at the time of film formation. Further, although the semiconductor crystal φ circle of the object to be processed is described by way of example, the present invention is not limited thereto, and the present invention can be applied to any of a glass substrate, an L C D substrate, a ceramic substrate, and the like. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a block diagram showing an example of a film forming apparatus of the present invention. Figs. 2(A), (B), (C), and (D) are diagrams showing a recess of a semiconductor wafer. A diagram showing the accumulation of film in each step of the center. φ 3(A) and (B) are flowcharts showing the respective steps of the film formation method of the present invention. 4(A), (B), and (C) are time charts for explaining the supply state of each gas of the ALD method when the seed crystal film is formed. Fig. 5 is a view showing an example of a change in the supply amount of the Mn raw material gas and the Cu containing raw material gas in accordance with the film formation time and the deposition of the heat treatment. Fig. 6 is a partial structural view showing a modification of the material gas supply means of the film forming apparatus. -34- 200810019 (32) Figures 7(A), (B), and (C) are diagrams showing a general embedding step of a concave portion of a semiconductor wafer. [Description of main component symbols] 1 : Insulation layer ' 2 : recessed portion _ 3 : wiring layer 4 : barrier layer 6 : seed film 8 : metal film 1 2 : film forming apparatus 1 4 : processing container 1 6 : shower head 1 8 : gas injection surface _ 20A : gas injection hole 20B : gas injection hole ^ 22A : gas diffusion chamber - 22B : gas diffusion chamber 24 : sealing member 26 : loading and unloading port 28 : gate valve 3 0 : container bottom 32 : row Air space -35- 200810019 (33) 34 : Opening 3 6 : cylindrical partition 3 8 : cylindrical partition wall bottom 40 : mounting table structure 4 2 : pillar 44 : mounting table ^ 46 : resistance heating heater • 48 : Pin insertion hole 50: upper push pin 52: push-up ring 54: arm portion 5 6 : telescopic rod 5 8 : actuator 60 : bellows 62 : exhaust port _ 64 : vacuum exhaust system 66 : exhaust passage - 68 : Pressure regulating valve - 70 0 : Vacuum pump 72 : Raw material gas supply means 74 : Reduced gas supply means 76 : Gas inlet 78 : Raw material gas flow path 8 〇 : Divided road - 36 - 200810019 (34) 82 : On-off valve 84 : Flow controller 8 6 : first raw material source 86 a : electric heater 8 8 : branch circuit 90 : switching valve ~ 92 : flow controller φ 94 : second raw material source 94 a : electric heater 96 a : flow path heating means 96b : flow path heating means 98 : gas inlet 100 : reducing gas flow path 102 : switching valve 104 : flow controller _ 106 : reducing gas source 1 0 8 : control means - 11 〇: memory medium , 1 1 2 : barrier layer 120 : raw material gas flow path 122 : raw material gas flow path - 37