TW201819053A - Coating method, coating device, and storage medium - Google Patents
Coating method, coating device, and storage medium Download PDFInfo
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- TW201819053A TW201819053A TW106128043A TW106128043A TW201819053A TW 201819053 A TW201819053 A TW 201819053A TW 106128043 A TW106128043 A TW 106128043A TW 106128043 A TW106128043 A TW 106128043A TW 201819053 A TW201819053 A TW 201819053A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C11/00—Component parts, details or accessories not specifically provided for in groups B05C1/00 - B05C9/00
- B05C11/02—Apparatus for spreading or distributing liquids or other fluent materials already applied to a surface ; Controlling means therefor; Control of the thickness of a coating by spreading or distributing liquids or other fluent materials already applied to the coated surface
- B05C11/08—Spreading liquid or other fluent material by manipulating the work, e.g. tilting
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/40—Distributing applied liquids or other fluent materials by members moving relatively to surface
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- H10P76/00—
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- Application Of Or Painting With Fluid Materials (AREA)
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- Exposure Of Semiconductors, Excluding Electron Or Ion Beam Exposure (AREA)
Abstract
[課題]在將塗佈液塗佈於晶圓之際,於短時間內進行微粒的去除,並更確實地抑制塗佈膜的不良。 [解決手段]在將塗佈液(102)供給至被搬入塗佈裝置的晶圓(W)之前,首先,供給稀釋劑(100),使晶圓(W)之表面潤濕,其次,使晶圓(W)之表面乾燥。藉此,晶圓(W)之表面的微粒(101)變得容易流動。又,以將晶圓(W)之表面乾燥的方式,接著在將稀釋劑(100)供給至晶圓(W)之表面後時,由於稀釋劑之積液之氣液界面的剖面變圓,並能以較大的力推擠微粒(101),因此,可在短時間內更確實地去除微粒(101)。因此,可抑制在其後將塗佈液(102)塗佈於晶圓(W)後時,因微粒(101)之附著而引起對SOC膜之慧斑的形成。[Problem] When a coating liquid is applied to a wafer, particles are removed in a short time, and defects in the coating film are more reliably suppressed. [Solution] Before supplying the coating liquid (102) to the wafer (W) carried into the coating apparatus, firstly, supply a diluent (100) to wet the surface of the wafer (W), and secondly, The surface of the wafer (W) is dry. Thereby, the particles (101) on the surface of the wafer (W) become easy to flow. In addition, when the surface of the wafer (W) is dried and the diluent (100) is supplied to the surface of the wafer (W), the cross section of the gas-liquid interface of the fluid accumulated in the diluent is rounded. Since the particles (101) can be pushed with a large force, the particles (101) can be removed more reliably in a short time. Therefore, when the coating liquid (102) is applied to the wafer (W) thereafter, the formation of plaque on the SOC film due to the adhesion of the particles (101) can be suppressed.
Description
[0001] 本發明,係關於將塗佈液供給至基板之表面而形成塗佈膜的技術。[0001] The present invention relates to a technique for forming a coating film by supplying a coating liquid to the surface of a substrate.
[0002] 作為半導體製造製程之一,有將塗佈液供給至半導體晶圓(以下稱為「晶圓」),而形成塗佈膜例如光阻膜、反射防止膜或以成為蝕刻遮罩的碳為主成分之SOC(Spin On Cap)膜等的製程。在該製程中,係廣泛使用旋轉塗佈法。 [0003] 例如SOC膜等的蝕刻遮罩,雖係在將階梯圖案形成於晶圓後,以覆蓋晶圓之表面的方式進行成膜,但例如有在將階梯圖案形成於晶圓之蝕刻處理等的前工程中產生之微粒附著於晶圓之表面的情形。其後,在將塗佈液供給至晶圓而進行了旋轉塗佈時,塗佈液之擴展因微粒受到阻礙,而在塗佈膜形成以微粒為核心之慧星型的斑點(慧斑)。由於半導體元件,係趨於逐漸微細化,因此,當在塗佈膜產生像這樣的缺陷時,則成為良率降低的主要原因。 [0004] 作為像這樣的塗佈缺陷之對策,例如如專利文獻1所記載,在塗佈塗佈液之前,將稀釋劑供給至晶圓進行表面之洗淨而進行微粒的去除,從維持晶圓之生產率的觀點來看,有在更短的時間內效率良好地去除微粒之要求。又,從避免裝置大型化的觀點來看,要求在進行塗佈的模組中之微粒的洗淨。 [先前技術文獻] [專利文獻] [0005] [專利文獻1]日本特開2006-208456號公報[0002] As one of semiconductor manufacturing processes, there is a method of supplying a coating liquid to a semiconductor wafer (hereinafter referred to as a “wafer”) to form a coating film such as a photoresist film, an antireflection film, or an etching mask. Manufacturing process of SOC (Spin On Cap) film with carbon as the main component. In this process, a spin coating method is widely used. [0003] For example, an etching mask such as a SOC film is formed by forming a step pattern on a wafer and then covering the surface of the wafer. However, for example, there is an etching process in which a step pattern is formed on a wafer. In the case where particles generated in previous processes are attached to the surface of the wafer. Thereafter, when the coating liquid is supplied to the wafer and spin-coated, the spread of the coating liquid is hindered by the particles, and a comet-type spot (coma) with the particles as the core is formed on the coating film. . Since semiconductor devices tend to be gradually miniaturized, when defects such as these occur in the coating film, it becomes the main cause of the decrease in yield. [0004] As a countermeasure against such coating defects, for example, as described in Patent Document 1, before coating the coating liquid, a diluent is supplied to the wafer, the surface is cleaned, and particles are removed to maintain the crystal. From the viewpoint of productivity, it is required to efficiently remove particles in a shorter period of time. In addition, from the viewpoint of avoiding an increase in the size of the device, cleaning of particles in the module to be coated is required. [Prior Art Document] [Patent Document] [0005] [Patent Document 1] Japanese Patent Laid-Open No. 2006-208456
[本發明所欲解決之課題] [0006] 本發明,係有鑑於像這樣的情事而進行研究者,其目的在於,提供一種如下述之技術:在將塗佈液塗佈至基板而形成塗佈膜之際,可在短時間內進行微粒之去除而抑制塗佈膜之不良的產生。 [用以解決課題之手段] [0007] 本發明之塗佈方法,其特徵係,包含有: 水平地保持基板的工程; 其次,藉由處理液,使基板之表面全體潤濕的工程; 接著,使前述基板繞垂直軸旋轉而使基板之表面乾燥的工程; 其後,一面使前述基板繞垂直軸旋轉,一面將洗淨液供給至基板之表面的工程;及 然後,將塗佈液供給至基板之表面而形成塗佈膜的工程。 [0008] 本發明之記憶媒體,係儲存有塗佈裝置中所使用的電腦程式,該塗佈裝置,係將塗佈液供給至水平地保持並繞垂直軸旋轉的基板而進行塗佈,該記憶媒體,其特徵係,編入有步驟群,以便執行上述的塗佈方法。 [0009] 本發明之塗佈裝置,其特徵係,具備有: 基板保持部,用以水平地保持基板; 旋轉機構,用以使前述基板保持部繞垂直軸旋轉; 塗佈液噴嘴,用以對被保持於前述基板保持部的基板供給塗佈液; 處理液噴嘴,對被保持於前述基板保持部的基板供給處理液; 洗淨液噴嘴,對被保持於前述基板保持部的基板供給洗淨液;及 控制部,執行如下述之步驟:水平地保持基板的步驟;其次,藉由處理液,使基板之表面全體潤濕的步驟;接著,使前述基板繞垂直軸旋轉而使基板之表面乾燥的步驟;其後,一面使前述基板繞垂直軸旋轉,一面將洗淨液供給至基板之表面的步驟;及然後,將塗佈液供給至基板之表面而形成塗佈膜的步驟。 [發明之效果] [0010] 本發明,係在將塗佈液供給至基板之前,在將處理液供給至基板而使基板之表面潤濕後,使基板之表面乾燥。藉此,微粒變得容易從基板之表面脫離。又,以使基板之表面乾燥的方式,可在繼續將洗淨液供給至基板之表面後時,藉由氣液界面,以較大的力推擠微粒,並可在短時間內更確實地進行去除。因此,可抑制在其後將塗佈液塗佈於基板後時,因微粒之附著而引起對塗佈膜之斑點的形成。 又,根據本發明之塗佈裝置,因具備有對基板的洗淨機能,因此,無需單獨地設置洗淨裝置。[Problems to be Solved by the Invention] 0006 [0006] The present invention has been made in view of such circumstances, and an object thereof is to provide a technique such as applying a coating liquid to a substrate to form a coating. In the case of fabric film, fine particles can be removed in a short period of time to prevent the occurrence of defects in the coating film. [Means to Solve the Problem] [0007] The coating method of the present invention is characterized by including: (i) a process of horizontally holding a substrate; (ii) a process of wetting the entire surface of the substrate by a processing liquid; (ii) A process of rotating the substrate around the vertical axis to dry the surface of the substrate; 后 thereafter, a process of supplying the cleaning liquid to the surface of the substrate while rotating the substrate around the vertical axis; and then, supplying a coating liquid The process of forming a coating film on the surface of a substrate. [0008] The memory medium of the present invention stores a computer program used in a coating device that supplies a coating liquid to a substrate that is horizontally held and rotated about a vertical axis to perform coating. The memory medium is characterized by a step group incorporated therein to perform the above-mentioned coating method. [0009] The coating device of the present invention is characterized by having: : a substrate holding section for horizontally holding the substrate; a rotation mechanism for rotating the substrate holding section about a vertical axis; a coating liquid nozzle for A coating liquid is supplied to a substrate held by the substrate holding portion; a processing liquid nozzle supplies a processing liquid to a substrate held by the substrate holding portion; a cleaning liquid nozzle supplies a washing liquid to a substrate held by the substrate holding portion; The cleaning solution and the control unit perform the following steps: a step of holding the substrate horizontally; a step of wetting the entire surface of the substrate by a processing liquid; and then, rotating the substrate about a vertical axis to make the substrate Surface drying step; thereafter, a step of supplying a cleaning solution to the surface of the substrate while rotating the substrate around a vertical axis; and a step of supplying a coating solution to the surface of the substrate to form a coating film. [Effects of the Invention] [0010] In the present invention, before the coating liquid is supplied to the substrate, the processing liquid is supplied to the substrate to wet the surface of the substrate, and then the surface of the substrate is dried. Thereby, the particles become easily detached from the surface of the substrate. In addition, in order to dry the surface of the substrate, when the cleaning liquid is continuously supplied to the surface of the substrate, the particles can be pushed by the gas-liquid interface with a large force, and more reliably in a short time Perform removal. Therefore, it is possible to suppress the formation of specks on the coating film due to the adhesion of particles when the coating liquid is applied to the substrate thereafter. Furthermore, according to the coating apparatus of the present invention, since the substrate has a cleaning function, it is not necessary to separately install a cleaning apparatus.
[0012] 作為本發明之實施形態之塗佈裝置的一例,使用圖1,說明關於在晶圓W形成SOC膜的塗佈裝置。塗佈裝置,係具備有罩杯模組1,罩杯模組1,係具備有吸附晶圓W之背面中央部而水平地保持的基板保持部即旋轉夾盤11。該旋轉夾盤11,係自下方經由軸部12被連接於旋轉機構13,可藉由該旋轉機構13繞垂直軸旋轉。 [0013] 在旋轉夾盤11的下方側,係以經由間隙包圍軸部12的方式,設置有圓形板14。又,在圓形板14,係於周方向等間隔地形成有3處貫穿孔17,在各貫穿孔17,係設置有升降銷15。升降銷15,係被構成為藉由升降機構16進行升降,藉由升降銷15的升降,在塗佈裝置之外部的搬送臂與旋轉夾盤11之間收授晶圓W。 [0014] 以包圍旋轉夾盤11的方式,設置有罩杯體2。罩杯體2,係承接自旋轉之晶圓W飛散或灑落的排液,並將該排液排出至塗佈裝置外。罩杯體2,係在前述圓形板14的周圍具備有剖面形狀被設置成山型之環狀的山型導引部21,並以從山型導引部21之外周端往下方延伸的方式,設置有環狀的垂直壁23。山型導引部21,係將自晶圓W灑落之液體朝晶圓W的外側下方導引。 [0015] 又,設置有:垂直之筒狀部22,包圍山型導引部21的外側;及上側導引部24,從該筒狀部22之上緣朝內側上方傾斜地延伸。在上側導引部24,係於周方向設置有複數個開口部25。又,筒狀部22之下方側,係在山型導引部21及垂直壁23的下方形成有剖面成為凹部型之環狀的液體承接部26。在該液體承接部26中,係在外周側連接有排液路徑27,並且,在比排液路徑27靠內周側,係以從下方突入的形狀,設置有排氣管28。 又,以從上側導引部24之基端側周緣往上方延伸的方式,設置有筒狀部29,以從該筒狀部29之上緣朝內側上方伸出的方式,設置傾斜壁30。因該晶圓W之旋轉而飛散的液體,係被筒狀部29、傾斜壁30、上側導引部24及垂直壁23承接而導入排液路徑27。 [0016] 塗佈裝置,係具備有將塗佈液供給至晶圓W的塗佈液噴嘴3,該塗佈液,係使成為SOC膜之前驅物質的有機材料溶解於溶劑。塗佈液噴嘴3,係經由塗佈液供給管31被連接於塗佈液供給機構32。作為塗佈液,係使用包含有碳化合物的有機材料,例如使持有聚乙烯構造 ((-CH2 -)n )之架構的聚合物原料溶解於溶劑之液體。 [0017] 又,塗佈裝置,係具備有噴嘴單元6,該噴嘴單元6,係設置有:稀釋劑噴嘴4,用以供給兼用為洗淨液與處理液的溶劑即稀釋劑;及N2 氣體噴嘴5,將氮氣(N2 氣體)供給至晶圓W。稀釋劑噴嘴4,係經由稀釋劑供給管41被連接於稀釋劑供給機構42。稀釋劑供給機構42,係具備有例如泵、閥、過濾器等的機器,且被構成為從稀釋劑噴嘴4之前端吐出預定量的稀釋劑。又,N2 氣體噴嘴5,係經由N2 氣體供給管51被連接於N2 氣體供給機構52。N2 氣體供給機構52,係具備有例如泵、閥、過濾器等的機器,且被構成為從N2 氣體噴嘴5吐出N2 氣體。 塗佈液噴嘴3及噴嘴單元6,係被構成為各別藉由未圖示的移動機構,在晶圓W的中央部上方與罩杯體2外的待機位置之間移動。 [0018] 在塗佈裝置,係設置有由例如電腦所構成的控制部10。控制部10,係具有程式儲存部,在程式儲存部,係儲存有編入命令的程式,以便實施外部的搬送臂與旋轉夾盤11之間之晶圓W的收授或旋轉夾盤11的旋轉、塗佈液、稀釋劑及N2 氣體的供給順序。該程式,係藉由例如軟碟片、光碟、硬碟、MO(光磁碟)、記憶卡等的記憶媒體來儲存而安裝於控制部10。 [0019] 接著,參閱圖2之時序圖及圖3~圖10的作用圖,說明關於本發明之實施形態的作用。上述的晶圓W,係藉由未圖示之外部的搬送臂與升降銷15的協同作用,被收授至旋轉夾盤11。 首先,為了使晶圓W的方向一致,如圖2(a)所示,以例如2000rpm的旋轉數,使其從時刻t0 旋轉1秒。又,如圖3所示,使噴嘴單元6從待機位置移動,並使稀釋劑噴嘴4移動至朝向晶圓W之中心吐出處理液即稀釋劑的位置。 [0020] 其次,如圖2(a)所示,於時刻t1 ,使晶圓W之旋轉數下降而維持為1000rpm,並且朝向晶圓W,如圖2(b)及圖4所示,從時刻t1 至t2 的3秒間,以例如75sccm的流量吐出稀釋劑100。藉此,稀釋劑100因離心力而在晶圓W的表面擴散,成為晶圓W之表面全體浸濕的狀態。 [0021] 接著,如圖2(a)所示,於時刻t2 ,使晶圓W之旋轉數上升而維持為3000rpm,並且如圖2(c)及圖5所示,使噴嘴單元6移動而使N2 氣體噴嘴5移動至朝向晶圓W之中心吐出氣體的位置,並進行N2 氣體的吐出。另外,在此,從時刻t2 至時刻t3 的時間為3秒。在之前的工程中,晶圓W,雖係成為被稀釋劑100浸濕的狀態,但藉由使晶圓W之旋轉數上升,並且朝向晶圓W之表面供給N2 氣體的方式,稀釋劑100會被甩掉,將晶圓W之表面乾燥。 [0022] 晶圓W,係在稀釋劑100的供給前,水分吸附於表面。微粒,雖係附著於晶圓W的表面,但當微觀性觀看時,吾人認為成為被晶圓W之表面狀的水分吸附之狀態。因此,在該例子中,係當將稀釋劑100供給至旋轉之晶圓W的中心部而使稀釋劑擴展時,則吸附於晶圓W之表面的水分會被該稀釋劑100沖洗掉。而且,使晶圓W之旋轉數上升而甩掉稀釋劑100,並且噴吹N2 氣體而使晶圓W之表面乾燥,藉此,附著於晶圓W之表面的微粒變得容易移動。於時刻t1 所供給的稀釋劑100,雖係用以去除晶圓W之表面的水分之液體即處理液,但由於藉由晶圓W的旋轉所致之擴展,其發揮了沖洗附著於晶圓W之表面的微粒之一部分的作用,因此,可說是一種洗淨液。 [0023] 其後,停止N2 氣體之吐出,使噴嘴單元6移動而使稀釋劑噴嘴4移動至朝向晶圓W之中心吐出洗淨液即稀釋劑100的位置。而且,如圖2(b)及圖6所示,於時刻t3 ,使晶圓W之旋轉數下降而維持為1000rpm,並且朝向晶圓W,從時刻t3 至t4 的3秒間,以例如75sccm的流量吐出稀釋劑100。 [0024] 如上述,使晶圓W之表面乾燥的工程後之晶圓W,係表面的微粒變得容易移動。又,由於將晶圓W之表面乾燥,因此,在擴展於晶圓W之表面的稀釋劑100之積液的周緣以剖面觀察變圓的狀態下,將微粒沖走。 接著,於時刻t4 ,使晶圓W之旋轉數上升,從時刻t4 起3秒後至時刻t5 ,維持為3000rpm,並且如圖7所示,使噴嘴單元6移動而使N2 氣體噴嘴5移動至朝向晶圓W之中心吐出氣體的位置,並進行N2 氣體的吐出。藉此,晶圓W之表面的稀釋劑100被甩掉,並且將晶圓W之表面乾燥。其後,停止N2 氣體之吐出,使噴嘴單元6移動而使稀釋劑噴嘴4移動至朝向晶圓W之中心吐出稀釋劑的位置。 [0025] 其後,於時刻t5 ,使晶圓W之旋轉數下降而維持為1000rpm,並且如圖8所示,朝向晶圓W,洗淨液在此,係從時刻t5 至t6 的6秒間,以例如75sccm的流量吐出稀釋劑100。藉此,稀釋劑100在乾燥後之晶圓W的表面擴散,殘留於晶圓W之表面的微粒被氣液界面推擠而除去。 亦即,在該例子中,係進行2次如下述之作用:水分從晶圓W之表面被去除,且形成乾燥後的狀態,其次,在沿著晶圓W之表面而擴展的稀釋劑100之積液的周緣以剖面觀察變圓的狀態下,將微粒101沖走。 [0026] 其後,使噴嘴單元6退避至晶圓W外,使晶圓W以2000rpm的旋轉數旋轉0.3秒,其次,使晶圓W以500rpm的旋轉數旋轉0.2秒。又,使塗佈液噴嘴3移動至朝向晶圓W之中心塗佈塗佈液102的位置。而且,從時刻t7 起,使晶圓W之旋轉數上升而維持為3000rpm的旋轉數,並且,如圖2(d)、圖9所示,供給1.5秒的塗佈液102。藉此,供給至晶圓W之表面的塗佈液102因離心力而擴散於被稀釋劑浸濕的晶圓W之表面全體。 [0027] 上述的實施形態,係在將塗佈液102供給至被搬入塗佈裝置的晶圓W之前,首先,供給稀釋劑100,使晶圓W之表面潤濕,其次,使晶圓W之表面乾燥。藉此,晶圓W之表面的水分被去除,微粒101變得容易流動。接著,在將稀釋劑100供給至晶圓W之表面後時,由於稀釋劑100的氣液界面在晶圓W之表面擴散,該氣液界面能以較大的力推擠微粒,因此,可在短時間內更確實地去除微粒。因此,可抑制在其後將塗佈液102塗佈於晶圓W後時,因微粒101之附著而引起對SOC膜之慧斑的形成。 [0028] 此時,以稀釋劑100使晶圓W之表面整體潤濕,其次,使晶圓W之表面乾燥後,供給稀釋劑100,藉此,如後述的檢證試驗所示,微粒變得容易被去除。該機制,係如以下般來推定。當晶圓W之表面浸濕的情況下,晶圓W之表面與稀釋劑100溶合。因此,流經晶圓W之表面的稀釋劑之積液的接觸角變小,如圖10所示,稀釋劑100的氣液界面變得平順。因此,在稀釋劑100擴散於晶圓W之表面後時,從側方推擠微粒101的力變弱,導致在微粒的上方流動,特別是,力在晶圓W之外周的區域會變弱,從而變得容易殘留微粒。 [0029] 對此,以使晶圓W之表面乾燥的方式,晶圓W之表面的撥水性變佳,流經晶圓W之表面的稀釋劑之積液的接觸角變大。因此,如圖11所示,在將稀釋劑100供給至晶圓W之表面後時,稀釋劑100之積液的剖面變圓,可從側方以面來推擠微粒101,並以較大的力進行推擠,即便在晶圓W之外周附近的區域,亦可維持強大的力。因此,推定微粒之去除效率變佳。該結果,如後述的檢證試驗中所示,即便在減少洗淨液之流量的情形或將洗淨液之供給時間設定為較短的情況下,亦可效率良好地去除微粒101。 [0030] 而且,將對晶圓W供給塗佈液102之前之從時刻t5 至t6 之間的朝向晶圓W進行供給之稀釋劑100的供給時間設定成6秒。由於以朝向晶圓W噴吹N2 氣體而促進氣化的方式來加快乾燥,因此,晶圓W之溫度,特別是晶圓W之外周側之區域的溫度會因氣化冷卻而變得容易下降,從而有影響例如塗佈膜的乾燥時間等之虞。由於稀釋劑100,係在常溫(25℃)進行供給,因此,在將光阻液供給至晶圓W之前,拉長朝向晶圓W供給之稀釋劑100的供給時間,藉此,可使因氣體之噴吹而降低之晶圓W的溫度返回到常溫。 [0031] 又,在上述的實施形態中,雖係重複2次將稀釋劑100供給至旋轉之晶圓W的工程與將N2 氣體供給至晶圓W之表面而使晶圓W之表面乾燥的工程,但將稀釋劑100供給至旋轉之晶圓W的工程與將N2 氣體供給至晶圓W之表面而使晶圓W之表面乾燥的工程,係亦可為1次。 [0032] 如上述的實施形態所示,在使晶圓W的表面乾燥後,將稀釋劑100供給至晶圓W,藉此,可藉由氣液界面,以較大的力推擠微粒101。因此,由於以重複將稀釋劑供給至旋轉之晶圓W的工程與將N2 氣體供給至晶圓W之表面而使晶圓W之表面乾燥的工程之方式,可增加在氣液界面推擠微粒101的次數,因此,可更確實地去除微粒。又,亦可重複3次以上將處理液(洗淨液)即稀釋劑100供給至旋轉之晶圓W的工程與將N2 氣體供給至晶圓W之表面而使晶圓W之表面乾燥的工程。 [0033] 又,在使晶圓W之表面乾燥之際,雖然藉由使晶圓W旋轉而甩掉稀釋劑100的方式,亦可使其乾燥,但如後述的檢證試驗3所示,以在將稀釋劑供給至晶圓W後,停止稀釋劑而使晶圓W旋轉,並且朝向晶圓W供給氮氣的方式,即便在較短的乾燥時間內,亦可提高顆粒之去除率。因此,可縮短晶圓W之處理時間。 [0034] 而且,亦可在首先使晶圓W潤濕時,將稀釋劑的供給時間,亦即吐出處理液即稀釋劑的時間設定成比吐出成為洗淨液之稀釋劑的時間短。例如,將圖2所示之吐出處理液之時刻t1 至t2 的時間設定成1秒,將第1次吐出洗淨液之時刻t3 至t4 的時間設定成3秒,將第2次吐出洗淨液之時刻t3 至t4 的時間設定成6秒。處理液,係只要可供給足以使晶圓W之表面潤濕的量即可,發明者們,係可獲得如下述之見解:在縮短處理液之供給時間的情況下,去除性能亦不會產生變化。該結果,可縮短晶圓W之處理時間。又,即便在逐次供給處理液及洗淨液的情況下,亦可使處理液之吐出時間比洗淨液之供給時間短。 [0035] 又,由於供給至晶圓W的處理液,係只可去除晶圓W之表面的水分即可,因此,亦可為例如醇等。又,亦可使用例如TMAH(氫氧化四甲銨)或APM洗淨用處理液(氨/過氧化氫/水混合液)等。由於該些藥液,係當使晶圓W之表面潤濕時,可剝開附著於晶圓W之表面的微粒,因此,可更效率良好地去除微粒。又,由於藉由將純水供給至晶圓W之表面,其次使其乾燥的方式,亦具有去除水分的效果,因此,亦可為純水。而且,亦可在搬入晶圓W後,首先使用稀釋劑作為供給的處理液,在使晶圓W乾燥後,其次供給例如TMAH作為供給至晶圓W的洗淨液,其後,在使晶圓W乾燥後,供給稀釋劑作為洗淨液。又,洗淨液,係亦可為用以進行使晶圓W成為潤濕之狀態而容易使塗佈液擴散的預濕處理之溶劑,且亦可對處理液使用與洗淨液相同之預濕處理用的溶劑。 [0036] 而且,亦可在將處理液及洗淨液供給至晶圓W之際,一面將處理液及洗淨液吐出至晶圓W,一面使噴嘴往晶圓W的周方向移動,並使處理液及洗淨液的吐出位置往晶圓W的周方向移動。又,處理液與洗淨液,係亦可為相同的藥液例如溶劑,或彼此不同的藥液例如彼此不同的溶劑。 [0037] 又,亦可在重複複數次乾燥—洗淨液之供給的情況下,於各次之間交互地切換晶圓W的旋轉方向。在將該手法應用於已述之實施形態的情況下,t3 -t4 間之晶圓的旋轉方向與t1 -t2 間及t5 -t6 間之晶圓W的旋轉方向,係彼此相反。 又,當晶圓W的旋轉數變高時,則晶圓W變得容易被冷卻。因此,使晶圓W乾燥的工程中之晶圓W的旋轉數,係1000~3000rpm為較佳。又,從使晶圓W充分乾燥且抑制對生產率之影響的觀點來看,使晶圓W乾燥的工程(從稀釋劑之供給停止至接著稀釋劑之供給開始的時間),係3秒~6秒為較佳。 而且,將洗淨液供給至晶圓W的時間,係各3秒以上為較佳。 [0038] 又,塗佈有塗佈液的晶圓W,係亦可為形成有階梯圖案的晶圓W。形成例如蝕刻處理等的階梯圖案之工程,係容易產生微粒,且形成有階梯圖案後的晶圓W,係容易附著有微粒。又,當階梯圖案被形成於晶圓W時,微粒容易卡在階梯圖案而有微粒難以流動的問題。如後述的檢證試驗所示,即便在形成有階梯圖案的晶圓W中,亦可應用本發明獲得效果。 又,塗佈液,係亦可為用以形成光阻膜或反射防止膜等的塗佈液。 [0039] [檢證試驗1] 本發明者,係將對晶圓之稀釋劑的供給時間、稀釋劑供給時之旋轉速度、稀釋劑之流量等的參數及洗淨手法作各種設定,且調查對微粒之去除效率的影響而發現本發明。在以下中,記載關於本發明之各種檢證試驗及其結果。另外,在檢證試驗,係亦含有本發明的手法。 [0040] [參考例之資料的取得] 使直徑25μm的聚苯乙烯乳膠粒子(PSL粒子)附著於檢查用晶圓W之表面,並在實施形態所示的塗佈裝置,以2000rpm的旋轉數使該檢查用晶圓W旋轉1秒,其次,一面以1000rpm的旋轉數使其旋轉,一面朝向檢查用晶圓W的中心部,以75ml/分的流量供給稀釋劑(OK73)12秒。其後,以2000rpm的旋轉數使檢查用晶圓W旋轉4.5秒,以100rpm的旋轉數1秒,以1500rpm的旋轉數15秒,而將使表面乾燥後的晶圓W設成為參考例。 [檢證試驗1-1] 將下述之例子設成為檢證試驗1-1:除了將一面使檢查用晶圓W旋轉,一面供給了稀釋劑的時間設定成18秒以外,其他與參考例同樣進行處理。 [檢證試驗1-2] 將下述之例子設成為檢證試驗1-2:除了將一面使檢查用晶圓W旋轉,一面供給稀釋劑時之晶圓W的旋轉數設定成2000rpm以外,其他與檢證試驗1-1同樣進行處理。 [檢證試驗1-3] 將下述之例子設成為檢證試驗1-3:除了將一面使檢查用晶圓W旋轉,一面供給稀釋劑時之晶圓W的旋轉數設定成3000rpm以外,其他與檢證試驗1-1同樣進行處理。 [檢證試驗1-4] 將下述之例子設成為檢證試驗4:除了將一面使檢查用晶圓W旋轉,一面供給稀釋劑時之稀釋劑的流量設定成150ml/分以外,其他與檢證試驗1-1同樣進行處理。 [0041] 針對參考例及各檢證試驗1-1~1-4,從搬送至塗佈裝置之前的檢查用晶圓W中之PSL粒子(直徑1μm以上)的附著數(試驗前附著數)與各處理後的檢查用晶圓W中之PSL粒子(直徑1μm以上)的附著數(試驗後附著數)之差分值,計算出去除率((試驗前附著數-試驗後附著數)/試驗前附著數×100)%。 [0042] 圖12,係表示該結果,並表示參考例及檢證試驗1-1~1-4中之PSL粒子的去除率。在參考例中,PSL粒子的去除率,係10.5%。又,試驗1-1~1-4中之PSL粒子的去除率,係分別為13.0%、14.8%、15.4%、15.6%,與參考例相比,PSL粒子的去除率變高。 [0043] 從參考例及檢證試驗1-1中之PSL粒子的去除率來看,可說是藉由拉長稀釋劑之供給時間的方式,使微粒之去除率提升。又,由檢證試驗1-1~1-3的結果來看,可說是在一面使檢查用晶圓W旋轉,一面供給稀釋劑時,藉由提升檢查用晶圓W之旋轉數的方式,使微粒之去除率提升。又,由於檢證試驗1-4其微粒之去除率比檢證試驗1-1高,因此,可說是在一面使檢查用晶圓W旋轉,一面供給稀釋劑時,藉由增加稀釋劑之流量的方式,使微粒之去除率提升。 [0044] [檢證試驗2] 檢證了在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,使供給稀釋劑之噴嘴移動時的效果。 [檢證試驗2-1] 將下述之例子設成為檢證試驗2-1:除了在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,朝向晶圓W之中心部進行稀釋劑的供給6秒,其次,耗費6秒一面使吐出稀釋劑之噴嘴從朝向晶圓W之中心部吐出的位置往朝向晶圓W之周緣部吐出的位置移動,一面供給稀釋劑以外,其他與參考例同樣進行處理。 [0045] 針對檢證試驗2-1,同樣求出檢查用晶圓W中之PSL粒子的試驗前附著數與PSL粒子的試驗後附著數之差分值,並計算出PSL粒子的去除率。 圖13,係表示該結果,並表示參考例及檢證試驗2-1中之PSL粒子之去除率的特性圖。在檢證試驗2-1中,PSL粒子的去除率,係18.4%,比參考例高。 因此,可說是在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,藉由使供給稀釋劑之噴嘴移動的方式,使微粒之去除率提升。 [0046] [檢證試驗3] 檢證了在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,間歇地供給稀釋劑的效果。 [檢證試驗3-1] 在參考例中,將下述之例子設成為檢證試驗3-1:在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,一面以1000rpm的旋轉數使檢查用晶圓W旋轉6秒,一面朝向晶圓W之中心部進行稀釋劑的供給6秒,其次,於停止了稀釋劑的狀態下,以1000rpm的旋轉數使檢查用晶圓W旋轉6秒而去除了檢查用晶圓W之表面的稀釋劑後,進一步接著一面以1000rpm的旋轉數使檢查用晶圓W旋轉6秒,一面朝向晶圓W之中心部進行稀釋劑的供給6秒。 [檢證試驗3-2] 將下述之例子設成為檢證試驗3-2:除了在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成2000rpm的旋轉數並使其旋轉6秒以外,其他進行與檢證試驗3-1同樣的處理。 [檢證試驗3-3] 將下述之例子設成為檢證試驗3-3:除了在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數並使其旋轉6秒以外,其他進行與檢證試驗3-1同樣的處理。 [檢證試驗3-4] 將下述之例子設成為檢證試驗3-4:除了在一面使檢查用晶圓W旋轉,一面供給稀釋劑之際,在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數並使其旋轉2秒以外,其他進行與檢證試驗3-1同樣的處理。 [檢證試驗3-5] 將下述之例子設成為檢證試驗3-5:除了在一面使檢查用晶圓W旋轉,一面供給稀釋劑後,在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數並使其旋轉4秒以外,其他進行與檢證試驗3-1同樣的處理。 [0047] 針對檢證試驗3-1~3-5,同樣求出檢查用晶圓W中之PSL粒子的試驗前附著數與PSL粒子的試驗後附著數之差分值,並計算出PSL粒子的去除率。 圖14,係表示該結果,並表示參考例及檢證試驗3-1~3-3中之PSL粒子之去除率的特性圖。又,圖15,係表示檢證試驗3-4、3-5與檢證試驗3-3及參考例中之PSL粒子之去除率的特性圖。 [0048] 如圖14所示,在檢證試驗3-1~3-3中,PSL粒子的去除率,係分別為10.7%、12.9%、53.7%。又,試驗後的檢查晶圓W,雖係在檢證試驗3-1及3-2中為未乾燥,但在檢證試驗3-3中為已充分乾燥。 根據該結果,可說是以在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數之方式,可使晶圓W之表面乾燥,接著,在供給了稀釋劑時,可效率良好地去除晶圓W之表面的微粒。 [0049] 又,如圖15所示,在檢證試驗3-4、3-5中,PSL粒子的去除率,係分別為10.5%、14.6%。 根據3-3~3-5的結果,可說是以在去除檢查用晶圓W之表面的稀釋劑之際,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數並使其旋轉4秒以上,更有效果為旋轉6秒以上之方式,可使晶圓W之表面乾燥,接著,在供給了稀釋劑時,可效率良好地去除晶圓W之表面的微粒。 [0050] [檢證試驗3之追加試驗] 又,檢證了在一面使檢查用晶圓W旋轉,一面供給稀釋劑後,停止稀釋劑的供給,並且供給N2 氣體,其後,供給稀釋劑的效果。 [檢證試驗3-3a] 檢證試驗3-3中,將下述之例子設成為檢證試驗3-3a:在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數,並且朝向檢查用晶圓W供給N2 氣體。 [檢證試驗3-4a] 檢證試驗3-4中,將下述之例子設成為檢證試驗3-4a:在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數並使其旋轉2秒,並且朝向檢查用晶圓W供給N2 氣體。 [檢證試驗3-5a] 檢證試驗3-5中,將下述之例子設成為檢證試驗3-5a:在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數並使其旋轉4秒,並且朝向檢查用晶圓W供給N2 氣體。 [檢證試驗3-4b] 將下述之例子設成為檢證試驗3-4b:除了在將N2 氣體供給至檢查用晶圓W之表面後,一面以1000rpm的旋轉數使檢查用晶圓W旋轉,一面將朝向晶圓W之中心部供給稀釋劑的時間設定成3秒以外,其他與檢證試驗3-4a同樣進行處理。 針對檢證試驗3-3a~3-5a、檢證試驗3-4b,同樣求出檢查用晶圓W中之PSL粒子的試驗前附著數與PSL粒子的試驗後附著數之差分值,並計算出PSL粒子的去除率。 [0051] 圖16,係表示檢證試驗3-3a~3-5a中之PSL粒子的去除率與檢證試驗3-3~3-5中之PSL粒子的去除率之特性圖。又,圖17,係表示檢證試驗3-4b中之PSL粒子的去除率與檢證試驗3-4a及參考例中之PSL粒子的去除率之特性圖。 如圖16所示,在檢證試驗3-3a~3-5a中之PSL粒子的去除率,係分別為54.2%、50.2%、53.8%,全部為超過50%的去除率。又,如圖17所示,在檢證試驗3-4b中,PSL粒子的去除率,係表示高至59.1%的值。另外,在檢證試驗3的追加試驗及後述的檢證試驗4中,係重新進行參考例之資料的取得。該結果,參考例之PSL粒子的去除率,係12.2%,與在檢證試驗1中所求出的值大致相同,去除率不變。 [0052] 在將朝向檢查用晶圓W吐出稀釋劑的時間之間隔分別設定成2秒及4秒的檢證試驗3-4及3-5中,由於PSL粒子的去除率,係分別為12.2%、14.6%,因此,可說是藉由在去除檢查用晶圓W之表面的稀釋劑時,將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數,並且朝向檢查用晶圓W供給N2 氣體之方法,即便在短時間內,亦可效率良好地去除微粒。又,如圖17所示,在檢證試驗3-4a及檢證試驗3-4b的任一中,由於PSL粒子之去除率亦為較高的值,因此,可說是以在使晶圓W乾燥時,噴吹N2 氣體而使其乾燥的方式,接著將供給稀釋劑之時間設定為較短的情況下,亦可效率良好地去除微粒。 [0053] [檢證試驗4] 又,檢證了在將稀釋劑間歇地供給至檢查用晶圓W之際,重複複數次停止稀釋劑而使晶圓W乾燥時的乾燥時間及晶圓W之稀釋劑的供給與晶圓W的乾燥之效果。 [檢證試驗4-1] 在檢證試驗3-4b中,將下述之例子設成為檢證試驗4-1:在去除檢查用晶圓W之表面的稀釋劑時,一面朝向檢查用晶圓W供給N2 氣體,一面將檢查用晶圓W的旋轉數設定成3000rpm的旋轉數並使其旋轉3秒。 [檢證試驗4-2] 又,將下述之例子設成為檢證試驗4-2:於接續檢證試驗4-1之處理而停止稀釋劑的狀態下,在一面以1000rpm的旋轉數使檢查用晶圓W旋轉3秒,一面供給N2 氣體而去除檢查用晶圓W之表面的稀釋劑後,進一步接著一面以1000rpm的旋轉數使檢查用晶圓W旋轉,一面朝向晶圓W之中心部進行稀釋劑的供給3秒。 針對檢證試驗4-1~4-2,同樣求出檢查用晶圓W中之PSL粒子的試驗前附著數與PSL粒子的試驗後附著數之差分值,並計算出PSL粒子的去除率。 [0054] 圖18,係表示該結果,並表示檢證試驗3-4b中之PSL粒子的去除率與檢證試驗4-1及檢證試驗4-2中之PSL粒子的去除率之特性圖。在檢證試驗3-4b中,PSL粒子的去除率,雖係表示高至59.1%的值,但在檢證試驗4-1中,PSL粒子的去除率為67.2%,在檢證試驗4-2中,PSL粒子的去除率為72.9%。 [0055] 根據該結果,可說是於停止稀釋劑的狀態下,以一面使檢查用晶圓W旋轉,一面拉長供給N2 氣體之時間的方式,使微粒之去除率提升,並更於停止稀釋劑的狀態下,藉由重複一面使檢查用晶圓W旋轉,一面供給N2 氣體的工程與一面使檢查用晶圓W旋轉,一面將稀釋劑供給至檢查用晶圓W之表面的工程之方式,使微粒之去除率提升。 [0056] 如以上般,在拉長了稀釋劑之供給時間的情況、提升了晶圓W之旋轉速度的情況、增加了稀釋劑之流量的情況下,微粒之去除率會提升,特別是,可說是在稀釋劑供給後而使其乾燥後,進一步以供給稀釋劑的方式,可效率良好地去除微粒。又,在使晶圓W乾燥時,以將氣體噴吹至晶圓W的方式,亦可謀求乾燥時間之縮短,並減少稀釋劑之流量。又,藉由重複複數次將稀釋劑供給至晶圓W的工程與使晶圓W乾燥的工程之方式,可效率良好地去除微粒。 [0057] 又,連續對進行了參考例、檢證試驗3-4b及檢證試驗4之各個處理的檢查用晶圓W形成SOC膜,並計數被形成於SOC膜之慧斑的個數。在參考例、檢證試驗3-4b及檢證試驗4之各個檢查用晶圓W所計數到之慧斑的個數,係分別為214個、118個及7個。與參考例相比,已知檢證試驗3-4b,係慧斑的個數大幅減少,並在檢證試驗4中,係更大幅減少。 [0058] 又,以形成有階梯圖案之晶圓來代替檢查用晶圓W,而在其上進行參考例、檢證試驗3-4b及檢證試驗4的各個處理,接著形成SOC膜,計數被形成於SOC膜之慧斑的個數。在參考例、檢證試驗3-4b及檢證試驗4之晶圓W所計數到之慧斑的個數,係分別為84個、20個及4個。由該結果來看,可說是在將本發明應用於形成有階梯圖案之晶圓W的情況下,亦可同樣地去除微粒,並可抑制塗佈膜之慧斑的形成。[0012] As an example of a coating apparatus according to an embodiment of the present invention, a coating apparatus for forming a SOC film on a wafer W will be described using FIG. 1. The coating device includes a cup module 1 and a cup module 1 including a spin chuck 11 that is a substrate holding portion that holds the central portion of the back surface of the wafer W and holds the wafer horizontally. The rotary chuck 11 is connected to the rotary mechanism 13 through the shaft portion 12 from below, and can be rotated around the vertical axis by the rotary mechanism 13. [0013] A circular plate 14 is provided below the spin chuck 11 so as to surround the shaft portion 12 through a gap. The circular plate 14 has three through holes 17 formed at equal intervals in the circumferential direction, and each of the through holes 17 is provided with a lift pin 15. The lift pin 15 is configured to be raised and lowered by the lift mechanism 16, and the wafer W is transferred between the transfer arm outside the coating apparatus and the rotary chuck 11 by the lift of the lift pin 15. [0014] A cup body 2 is provided so as to surround the rotary chuck 11. The cup body 2 receives the liquid discharged from the rotating wafer W by scattering or dropping, and discharges the liquid to the outside of the coating device. The cup body 2 is provided with a ring-shaped mountain-shaped guide 21 provided in a mountain shape in cross section around the circular plate 14 and extends downward from the outer peripheral end of the mountain-shaped guide 21. An annular vertical wall 23 is provided. The mountain-shaped guide portion 21 guides the liquid spilled from the wafer W toward the outside and below the wafer W. [0015] Furthermore, a vertical cylindrical portion 22 is provided to surround the outer side of the mountain-shaped guide portion 21, and an upper guide portion 24 extends obliquely from the upper edge of the cylindrical portion 22 toward the inside and upward. The upper guide portion 24 is provided with a plurality of openings 25 in the circumferential direction. In the lower side of the tubular portion 22, a ring-shaped liquid receiving portion 26 having a recessed cross section is formed below the mountain-shaped guide portion 21 and the vertical wall 23. The liquid receiving portion 26 is connected to a liquid discharge path 27 on the outer peripheral side, and is provided on the inner peripheral side of the liquid discharge path 27 in a shape protruding from below, and an exhaust pipe 28 is provided. In addition, a cylindrical portion 29 is provided so as to extend upward from the peripheral edge of the proximal end side of the upper guide portion 24, and an inclined wall 30 is provided so as to protrude from the upper edge of the cylindrical portion 29 toward the inside and upward. The liquid scattered by the rotation of the wafer W is received by the cylindrical portion 29, the inclined wall 30, the upper guide portion 24, and the vertical wall 23, and is introduced into the liquid discharge path 27. [0016] The coating apparatus is provided with a coating liquid nozzle 3 for supplying a coating liquid to the wafer W, and the coating liquid dissolves an organic material that becomes a precursor substance of the SOC film in a solvent. The coating liquid nozzle 3 is connected to the coating liquid supply mechanism 32 via a coating liquid supply pipe 31. As the coating liquid, an organic material containing a carbon compound is used, for example, a liquid in which a polymer raw material having a structure of a polyethylene structure ((-CH 2- ) n ) is dissolved in a solvent. [0017] The coating device includes a nozzle unit 6 provided with a diluent nozzle 4 for supplying a diluent, which is a solvent serving as a cleaning liquid and a processing liquid; and N 2 The gas nozzle 5 supplies nitrogen (N 2 gas) to the wafer W. The diluent nozzle 4 is connected to the diluent supply mechanism 42 via a diluent supply pipe 41. The diluent supply mechanism 42 is provided with a device such as a pump, a valve, and a filter, and is configured to discharge a predetermined amount of diluent from the front end of the diluent nozzle 4. The N 2 gas nozzle 5 is connected to an N 2 gas supply mechanism 52 via an N 2 gas supply pipe 51. The N 2 gas supply mechanism 52 is provided with a device such as a pump, a valve, a filter, and the like, and is configured to discharge N 2 gas from the N 2 gas nozzle 5. The coating liquid nozzle 3 and the nozzle unit 6 are each configured to move between the upper portion of the wafer W and the standby position outside the cup body 2 by a moving mechanism (not shown). [0018] The coating device is provided with a control unit 10 composed of, for example, a computer. The control unit 10 has a program storage unit. The program storage unit stores a program programmed in order to receive and deliver wafers W between the external transfer arm and the rotary chuck 11 or rotate the rotary chuck 11. , Supply sequence of coating liquid, diluent and N 2 gas. This program is stored in a storage medium such as a floppy disk, an optical disk, a hard disk, a MO (optical disk), or a memory card, and is installed in the control unit 10. [0019] Next, the operation of the embodiment of the present invention will be described with reference to the timing chart of FIG. 2 and the operation diagrams of FIGS. 3 to 10. The wafer W described above is transferred to the spin chuck 11 by the cooperation of an external transfer arm (not shown) and the lift pin 15. First, in order to make the directions of the wafers W coincide, as shown in FIG. 2 (a), the wafer W is rotated for 1 second from the time t 0 at a rotation number of, for example, 2000 rpm. As shown in FIG. 3, the nozzle unit 6 is moved from the standby position, and the thinner nozzle 4 is moved to a position where the thinner, which is a processing liquid, is discharged toward the center of the wafer W. [0020] Next, FIG. 2 (a) as shown at time t 1, the number of rotations of the wafer W is maintained at 1000 rpm for the decline, and toward the wafer W, as shown in FIG 2 (b) and FIG. 4, From the time t 1 to t 2 , the diluent 100 is discharged at a flow rate of, for example, 75 sccm. As a result, the diluent 100 diffuses on the surface of the wafer W due to the centrifugal force, and the entire surface of the wafer W becomes wet. [0021] Next, FIG. 2 (a) as shown at time t 2, the number of rotations of the wafer W is maintained at 3000 rpm for rises, and FIG. 2 (c) and 5, the nozzle unit 6 is moved Then, the N 2 gas nozzle 5 is moved to a position where the gas is discharged toward the center of the wafer W, and N 2 gas is discharged. The time from time t 2 to time t 3 is 3 seconds. In the previous process, although the wafer W was in a state of being wetted by the diluent 100, the diluent was supplied by increasing the number of rotations of the wafer W and supplying N 2 gas toward the surface of the wafer W. 100 will be thrown away to dry the surface of the wafer W. [0022] Before the wafer W is supplied, moisture is adsorbed on the surface. Although the fine particles are adhered to the surface of the wafer W, when viewed microscopically, we think that the particles are in a state of being adsorbed by the surface-like moisture of the wafer W. Therefore, in this example, when the diluent 100 is supplied to the center portion of the rotating wafer W to expand the diluent, the moisture adsorbed on the surface of the wafer W is washed away by the diluent 100. In addition, the number of rotations of the wafer W is increased to shake off the diluent 100, and the surface of the wafer W is dried by spraying N 2 gas, whereby the particles attached to the surface of the wafer W are easily moved. Although the diluent 100 supplied at time t 1 is a liquid for removing water on the surface of the wafer W, that is, a processing liquid, it expands due to the rotation of the wafer W, and it exerts flushing and adhesion to the crystal. A part of the particles on the surface of the circle W acts as a cleaning solution. [0023] Thereafter, to stop the discharge gas of N 2, the nozzle unit 6 is moved to the diluent nozzle 4 is moved toward the center of the wafer W is discharged cleaning liquid diluent i.e. position 100. Further, as shown in FIG. 2 (b) and FIG. 6, at time t 3, the number of rotations of the wafer W is maintained at 1000 rpm for the decline, and toward the wafer W, between 3 seconds from time t 3 to t. 4 to For example, the diluent 100 is discharged at a flow rate of 75 sccm. [0024] As described above, on the wafer W after the process of drying the surface of the wafer W, the particles on the surface become easy to move. In addition, since the surface of the wafer W is dried, the particles are washed away in a state where the peripheral edge of the liquid of the diluent 100 spreading on the surface of the wafer W is rounded in a cross-sectional view. Next, at time t 4 , the number of rotations of the wafer W is increased, and after 3 seconds from time t 4 to time t 5 , it is maintained at 3000 rpm. As shown in FIG. 7, the nozzle unit 6 is moved to make N 2 gas. The nozzle 5 is moved to a position where gas is discharged toward the center of the wafer W, and N 2 gas is discharged. Thereby, the diluent 100 on the surface of the wafer W is thrown away, and the surface of the wafer W is dried. Thereafter, the discharge of the N 2 gas is stopped, the nozzle unit 6 is moved, and the diluent nozzle 4 is moved to a position where the diluent is discharged toward the center of the wafer W. [0025] Thereafter, at time t 5, the number of rotations of the wafer W is maintained at 1000 rpm for the decline, and 8, toward the wafer W, the cleaning liquid in this system from time t 5 to t 6 In 6 seconds, the diluent 100 is discharged at a flow rate of, for example, 75 sccm. Thereby, the diluent 100 diffuses on the surface of the wafer W after drying, and the particles remaining on the surface of the wafer W are pushed and removed by the gas-liquid interface. That is, in this example, the effect is performed twice as follows: moisture is removed from the surface of the wafer W and formed into a dried state, and secondly, the diluent 100 spreading along the surface of the wafer W In a state where the peripheral edge of the accumulated liquid was rounded in cross-section, the particles 101 were washed away. [0026] Thereafter, the nozzle unit 6 is retracted out of the wafer W, and the wafer W is rotated at a rotation number of 2000 rpm for 0.3 seconds, and then, the wafer W is rotated at a rotation number of 500 rpm for 0.2 seconds. Further, the coating liquid nozzle 3 is moved to a position where the coating liquid 102 is applied toward the center of the wafer W. From time t 7 , the number of rotations of the wafer W is increased to maintain the number of rotations of 3000 rpm, and as shown in FIG. 2 (d) and FIG. 9, the coating liquid 102 is supplied for 1.5 seconds. Thereby, the coating liquid 102 supplied to the surface of the wafer W is diffused by centrifugal force to the entire surface of the wafer W wetted with the diluent. [0027] In the above-mentioned embodiment, before the coating liquid 102 is supplied to the wafer W carried into the coating apparatus, the diluent 100 is first supplied to wet the surface of the wafer W, and secondly, the wafer W is supplied. The surface is dry. Thereby, the water | moisture content on the surface of the wafer W is removed, and the particle 101 becomes easy to flow. Next, when the diluent 100 is supplied to the surface of the wafer W, since the gas-liquid interface of the diluent 100 diffuses on the surface of the wafer W, the gas-liquid interface can push the particles with a large force. Remove particles more reliably in a short time. Therefore, when the coating liquid 102 is applied to the wafer W after that, the formation of plaque on the SOC film due to the adhesion of the particles 101 can be suppressed. [0028] At this time, the entire surface of the wafer W is wetted with the diluent 100, and then, the surface of the wafer W is dried, and then the diluent 100 is supplied. As a result, as shown in a verification test described later, the particles are changed To be easily removed. This mechanism is estimated as follows. When the surface of the wafer W is wet, the surface of the wafer W is fused with the diluent 100. Therefore, the contact angle of the fluid of the diluent flowing through the surface of the wafer W becomes smaller, and as shown in FIG. 10, the gas-liquid interface of the diluent 100 becomes smooth. Therefore, when the diluent 100 diffuses on the surface of the wafer W, the force pushing the particles 101 from the side becomes weak, causing the particles to flow above the particles, and in particular, the area of the force outside the wafer W becomes weaker. This makes it easy to leave particles. [0029] In this regard, in a manner that the surface of the wafer W is dried, the water repellency of the surface of the wafer W is improved, and the contact angle of the accumulated liquid of the diluent flowing through the surface of the wafer W is increased. Therefore, as shown in FIG. 11, when the diluent 100 is supplied to the surface of the wafer W, the cross section of the accumulated liquid of the diluent 100 becomes round, and the particles 101 can be pushed from the side to the surface, and Even if it is pushed in the vicinity of the outer periphery of the wafer W, a strong force can be maintained. Therefore, it is estimated that the removal efficiency of the fine particles is improved. As a result, as shown in a verification test described later, even when the flow rate of the cleaning solution is reduced or the supply time of the cleaning solution is set to be short, the particles 101 can be efficiently removed. [0030] Further, before the wafer W will be supplied from the coating liquid 102 toward the wafer W between the time t 5 to t. 6 of the supply time for supplying the diluent 100 is set to 6 seconds. Since drying is accelerated by injecting N 2 gas toward the wafer W to promote vaporization, the temperature of the wafer W, especially the temperature of the area outside the wafer W, is facilitated by the vaporization cooling. If it falls, there exists a possibility that it may affect the drying time of a coating film, for example. Since the diluent 100 is supplied at normal temperature (25 ° C.), before the photoresist liquid is supplied to the wafer W, the supply time of the diluent 100 supplied to the wafer W is lengthened. The temperature of the wafer W, which is lowered by the blowing of the gas, returns to normal temperature. [0031] In the above embodiment, the process of supplying the diluent 100 to the rotating wafer W and the supply of N 2 gas to the surface of the wafer W are repeated twice to dry the surface of the wafer W. The process of supplying the diluent 100 to the rotating wafer W and the process of supplying N 2 gas to the surface of the wafer W and drying the surface of the wafer W may be performed once. [0032] As shown in the above embodiment, after the surface of the wafer W is dried, the diluent 100 is supplied to the wafer W, whereby the particles 101 can be pushed by the gas-liquid interface with a large force. . Therefore, since the process of supplying the diluent to the rotating wafer W and the process of supplying the N 2 gas to the surface of the wafer W and drying the surface of the wafer W are repeated, the pushing at the gas-liquid interface can be increased. The number of times of the fine particles 101 makes it possible to more reliably remove the fine particles. In addition, the process of supplying the treatment liquid (cleaning liquid), ie, the diluent 100, to the rotating wafer W and the process of supplying N 2 gas to the surface of the wafer W to dry the surface of the wafer W may be repeated three or more times. engineering. [0033] When the surface of the wafer W is dried, the wafer W may be dried by rotating the wafer W by rotating the wafer W, but as shown in the verification test 3 described later, After the diluent is supplied to the wafer W, the diluent is stopped to rotate the wafer W, and a nitrogen gas is supplied toward the wafer W, so that the particle removal rate can be improved even in a short drying time. Therefore, the processing time of the wafer W can be shortened. [0034] Furthermore, when the wafer W is first wetted, the supply time of the diluent, that is, the time to discharge the diluent, which is the processing liquid, may be set to be shorter than the time to discharge the diluent that becomes the cleaning liquid. For example, the time from the time t 1 to t 2 when the processing liquid is discharged as shown in FIG. 2 is set to 1 second, the time from the time t 3 to t 4 when the cleaning liquid is first discharged is 3 seconds, and the second The time from the time t 3 to t 4 at which the washing liquid is ejected twice is set to 6 seconds. As long as the processing liquid can be supplied in an amount sufficient to wet the surface of the wafer W, the inventors can obtain the following insights: in the case of shortening the supply time of the processing liquid, the removal performance does not occur. Variety. As a result, the processing time of the wafer W can be shortened. In addition, even when the processing liquid and the cleaning liquid are sequentially supplied, the discharge time of the processing liquid can be made shorter than the supply time of the cleaning liquid. [0035] In addition, since the processing liquid supplied to the wafer W only needs to remove the water on the surface of the wafer W, it may be, for example, alcohol. In addition, for example, TMAH (tetramethylammonium hydroxide) or APM cleaning treatment solution (ammonia / hydrogen peroxide / water mixed solution) can be used. Since these chemical liquids wet particles on the surface of the wafer W, the particles attached to the surface of the wafer W can be peeled off. Therefore, the particles can be removed more efficiently. In addition, since the method of supplying pure water to the surface of the wafer W and then drying it also has the effect of removing moisture, it can also be pure water. Furthermore, after the wafer W is carried in, a diluent may be used as the supplied processing liquid first, and after the wafer W is dried, for example, TMAH may be supplied as the cleaning liquid supplied to the wafer W, and thereafter, the crystal After the circle W was dried, a diluent was supplied as a washing liquid. The cleaning liquid may be a solvent for performing a pre-wetting treatment in which the coating liquid is easily diffused while the wafer W is in a wet state, and the same pretreatment as the cleaning liquid may be used for the processing liquid. Solvent for wet processing. [0036] In addition, when the processing liquid and the cleaning liquid are supplied to the wafer W, the processing liquid and the cleaning liquid may be discharged to the wafer W while the nozzle is moved in the circumferential direction of the wafer W, and The discharge positions of the processing liquid and the cleaning liquid are moved in the circumferential direction of the wafer W. The treatment liquid and the cleaning liquid may be the same chemical liquid such as a solvent, or different chemical liquids such as different solvents. [0037] When the supply of the drying-cleaning liquid is repeated a plurality of times, the rotation direction of the wafer W may be switched alternately between each time. When this method is applied to the embodiment described above, the rotation direction of the wafer between t 3 -t 4 and the rotation direction of the wafer W between t 1 -t 2 and t 5 -t 6 are Opposite each other. When the number of rotations of the wafer W becomes higher, the wafer W becomes easier to be cooled. Therefore, the number of rotations of the wafer W in the process of drying the wafer W is preferably 1000 to 3000 rpm. In addition, from the viewpoint of sufficiently drying the wafer W and suppressing the influence on productivity, the process of drying the wafer W (the time from the stop of the supply of the diluent to the start of the supply of the diluent) is 3 seconds to 6 Second is better. The time for supplying the cleaning liquid to the wafer W is preferably 3 seconds or more. [0038] The wafer W coated with the coating liquid may be a wafer W formed with a step pattern. In the process of forming a step pattern such as an etching process, particles are easily generated, and the wafer W after the step pattern is formed is liable to be adhered with particles. In addition, when the step pattern is formed on the wafer W, particles are likely to be caught in the step pattern and there is a problem that the particles are difficult to flow. As shown in the verification test to be described later, the present invention can also be used to obtain an effect even on a wafer W formed with a step pattern. The coating liquid may be a coating liquid for forming a photoresist film or an antireflection film. [Certification Test 1] The present inventors made various settings for the parameters such as the supply time of the diluent to the wafer, the rotation speed when the diluent was supplied, the flow rate of the diluent, and the cleaning method, and investigated The present invention was found to have an effect on particle removal efficiency. In the following, various verification tests related to the present invention and their results are described. In addition, the verification method also includes the method of the present invention. [Acquisition of Reference Example Materials] Polystyrene latex particles (PSL particles) with a diameter of 25 μm were attached to the surface of the inspection wafer W, and the coating device shown in the embodiment was rotated at a number of revolutions of 2000 rpm. The inspection wafer W was rotated for 1 second. Next, the inspection wafer W was rotated at a rotation number of 1000 rpm, and the diluent (OK73) was supplied at a flow rate of 75 ml / min for 12 seconds while facing the center of the inspection wafer W. Thereafter, the inspection wafer W was rotated at a rotation number of 2000 rpm for 4.5 seconds, rotated at a speed of 100 rpm for 1 second, and rotated at a speed of 1500 rpm for 15 seconds, and the wafer W after the surface was dried was used as a reference example. [Certification Test 1-1] The following example is referred to as the certification test 1-1. The time period during which the diluent is supplied while the inspection wafer W is rotated is set to 18 seconds. Do the same. [Certification Test 1-2] The following example is referred to as the certification test 1-2: except that the inspection wafer W is rotated while the diluent is supplied while the number of rotations of the wafer W is set to 2000 rpm, Others are treated in the same way as the verification test 1-1. [Certification Test 1-3] The following example is referred to as the certification test 1-3: except that the inspection wafer W is rotated while the diluent is supplied while the number of rotations of the wafer W is set to 3000 rpm, Others are treated in the same way as the verification test 1-1. [Certification Test 1-4] The following example is set as the certification test 4: except that the flow rate of the diluent when the diluent is supplied while rotating the inspection wafer W is set to 150 ml / min. The verification test 1-1 is also processed. [0041] For the reference example and each verification test 1-1 to 1-4, the number of adhesion (the number of adhesion before the test) of PSL particles (diameter 1 μm or more) in the inspection wafer W before being transferred to the coating apparatus The difference between the number of adhesion (the number of adhesions after the test) with the PSL particles (diameter 1 μm or more) in the inspection wafer W after each treatment, and the removal rate ((the number of adhesions before the test-the number of adhesions after the test) / test Number of front attachments × 100)%. [0042] FIG. 12 shows the results, and shows the removal rate of PSL particles in the reference examples and verification tests 1-1 to 1-4. In the reference example, the removal rate of PSL particles was 10.5%. In addition, the removal rates of PSL particles in Tests 1-1 to 1-4 were 13.0%, 14.8%, 15.4%, and 15.6%, respectively. Compared with the reference example, the removal rates of PSL particles were higher. [0043] From the point of view of the removal rate of the PSL particles in the reference example and the verification test 1-1, it can be said that the removal rate of the fine particles is improved by lengthening the supply time of the diluent. From the results of the verification tests 1-1 to 1-3, it can be said that when the inspection wafer W is rotated while the diluent is supplied, the number of rotations of the inspection wafer W is increased. To improve the removal rate of particles. In addition, since the removal rate of fine particles in the verification test 1-4 is higher than that in the verification test 1-1, it can be said that when the inspection wafer W is rotated and the diluent is supplied while the diluent is supplied, The method of flow improves the removal rate of particles. [Verification Test 2] The effect of moving the nozzle for supplying the diluent while rotating the inspection wafer W while supplying the diluent was verified. [Certification Test 2-1] The following example is referred to as the certification test 2-1. The diluent is supplied toward the center of the wafer W when the diluent is supplied while the inspection wafer W is rotated. 6 seconds. Secondly, it takes 6 seconds to move the nozzle that discharges the diluent from the position to the center of the wafer W to the position to the periphery of the wafer W. The diluent is supplied while the other is for reference. The example is also processed. [0045] For the verification test 2-1, the difference between the number of adhesion of the PSL particles before the test and the number of adhesion of the PSL particles after the test in the inspection wafer W was similarly calculated, and the removal rate of the PSL particles was calculated. FIG. 13 is a characteristic diagram showing the results and the removal rate of the PSL particles in the reference example and the verification test 2-1. In the verification test 2-1, the removal rate of PSL particles was 18.4%, which was higher than the reference example. Therefore, it can be said that when the inspection wafer W is rotated and the diluent is supplied, the removal rate of the particles is improved by moving the nozzle for supplying the diluent. [Verification Test 3] The effect of intermittently supplying the diluent while rotating the inspection wafer W while supplying the diluent was verified. [Certification Test 3-1] In the reference example, the following example is referred to as the certification test 3-1. The inspection wafer W is rotated while the diluent is supplied, and the number of revolutions is 1000 rpm. The inspection wafer W is rotated for 6 seconds, and the diluent is supplied for 6 seconds while facing the center of the wafer W. Next, the inspection wafer W is rotated by 1000 rpm for 6 seconds while the diluent is stopped. After removing the diluent on the surface of the inspection wafer W in seconds, the inspection wafer W was further rotated for 6 seconds at a rotation number of 1000 rpm, and the diluent was supplied toward the center of the wafer W for 6 seconds. [Verification Test 3-2] The following example is referred to as verification test 3-2: In addition to rotating the inspection wafer W while supplying diluent, the surface of the inspection wafer W is removed. In the case of the thinner, the number of rotations of the inspection wafer W is set to a number of rotations of 2000 rpm and the rotation is performed for 6 seconds, and the other processes are performed in the same manner as in the verification test 3-1. [Verification Test 3-3] The following example is referred to as Verification Test 3-3. In addition to rotating the inspection wafer W while supplying diluent, the surface of the inspection wafer W is removed. In the case of the thinner, the number of rotations of the inspection wafer W is set to a rotation number of 3000 rpm and the rotation is performed for 6 seconds, and the same processing as that of the verification test 3-1 is performed. [Certification Test 3-4] The following example is referred to as the certification test 3-4. In addition to rotating the inspection wafer W while supplying diluent, the surface of the inspection wafer W is removed. In the case of the thinner, the number of rotations of the inspection wafer W is set to a number of rotations of 3000 rpm and the rotation is performed for 2 seconds, and the same processing as in the verification test 3-1 is performed. [Certification Test 3-5] The following example is referred to as the certification test 3-5: In addition to rotating the inspection wafer W on one side and supplying diluent on the other, the dilution on the surface of the inspection wafer W is removed. In the case of a chemical agent, the number of rotations of the inspection wafer W is set to a number of rotations of 3000 rpm and the rotation is performed for 4 seconds. [0047] For the verification tests 3-1 to 3-5, the difference between the number of adhesion of the PSL particles before the test and the number of adhesion of the PSL particles after the test in the inspection wafer W is similarly calculated, and the number of PSL particles is calculated. Removal rate. FIG. 14 is a characteristic diagram showing the results and the removal rate of PSL particles in the reference examples and verification tests 3-1 to 3-3. 15 is a characteristic diagram showing removal rates of PSL particles in the verification tests 3-4, 3-5, the verification tests 3-3, and the reference examples. [0048] As shown in FIG. 14, in the verification tests 3-1 to 3-3, the removal rates of the PSL particles were 10.7%, 12.9%, and 53.7%, respectively. The inspection wafer W after the test was not dried in the verification tests 3-1 and 3-2, but was sufficiently dried in the verification test 3-3. Based on the results, it can be said that the surface of the wafer W can be dried when the number of rotations of the inspection wafer W is set to 3000 rpm when the diluent on the surface of the inspection wafer W is removed. When the diluent is supplied, particles on the surface of the wafer W can be efficiently removed. [0049] As shown in FIG. 15, in the verification tests 3-4 and 3-5, the removal rates of the PSL particles were 10.5% and 14.6%, respectively. Based on the results of 3-3 to 3-5, it can be said that when the thinner on the surface of the inspection wafer W is removed, the number of revolutions of the inspection wafer W is set to 3000 rpm and the number of revolutions is 4 For more than seconds, it is more effective to rotate the surface for more than 6 seconds to dry the surface of the wafer W. Then, when a diluent is supplied, particles on the surface of the wafer W can be efficiently removed. [0050] [Additional Test for Verification Test 3] It was also verified that after the inspection wafer W is rotated and the diluent is supplied, the supply of the diluent is stopped, and N 2 gas is supplied, and thereafter, the dilution is supplied. Agent effect. [Certification Test 3-3a] In the Certification Test 3-3, the following example is referred to as the Certification Test 3-3a. When the thinner on the surface of the inspection wafer W is removed, the inspection wafer W is removed. The number of rotations is set to the number of rotations of 3000 rpm, and N 2 gas is supplied to the inspection wafer W. [Certification Test 3-4a] In the Certification Test 3-4, the following example is set as the Certification Test 3-4a. When the thinner on the surface of the inspection wafer W is removed, the inspection wafer W is removed. The number of rotations is set to the number of rotations of 3000 rpm and the rotation is performed for 2 seconds, and N 2 gas is supplied toward the inspection wafer W. [Certification Test 3-5a] In the Certification Test 3-5, the following example is set as the Certification Test 3-5a. When the thinner on the surface of the inspection wafer W is removed, the inspection wafer W is removed. The number of rotations is set to the number of rotations of 3000 rpm and the rotation is performed for 4 seconds, and N 2 gas is supplied toward the inspection wafer W. [Certification Test 3-4b] The following example is referred to as the certification test 3-4b: Except that N 2 gas is supplied to the surface of the inspection wafer W, the inspection wafer is rotated at 1000 rpm on one side. W is rotated, and the time for supplying the diluent toward the center of the wafer W is set to other than 3 seconds, and other processing is performed in the same manner as in the verification test 3-4a. For the verification tests 3-3a to 3-5a and verification tests 3-4b, the difference between the number of PSL particles before the test and the number of PSL particles after the test is also calculated and calculated. The removal rate of PSL particles is shown. 16 is a characteristic diagram showing the removal rate of PSL particles in verification tests 3-3a to 3-5a and the removal rate of PSL particles in verification tests 3-3a to 3-5a. 17 is a characteristic diagram showing the removal rate of the PSL particles in the verification test 3-4b and the removal rate of the PSL particles in the verification test 3-4a and the reference example. As shown in FIG. 16, the removal rates of the PSL particles in the verification tests 3-3a to 3-5a were 54.2%, 50.2%, and 53.8%, respectively, and the removal rates exceeded 50%. As shown in FIG. 17, in the verification test 3-4b, the removal rate of the PSL particles showed a value as high as 59.1%. In addition, in the additional test of the verification test 3 and the verification test 4 to be described later, the reference example is acquired again. As a result, the removal rate of the PSL particles in the reference example was 12.2%, which was approximately the same as the value obtained in the verification test 1, and the removal rate was unchanged. [0052] In the verification tests 3-4 and 3-5 in which the time intervals during which the diluent was discharged toward the inspection wafer W were set to 2 seconds and 4 seconds, respectively, the removal rates of the PSL particles were 12.2, respectively. %, 14.6%. Therefore, it can be said that when the diluent on the surface of the inspection wafer W is removed, the rotation number of the inspection wafer W is set to 3000 rpm, and the inspection wafer W is supplied to the inspection wafer W. The method of N 2 gas can efficiently remove particles even in a short time. In addition, as shown in FIG. 17, in either of the verification test 3-4a and the verification test 3-4b, the removal rate of the PSL particles is also a high value. Therefore, it can be said that the wafer In the case of W drying, the method of blowing N 2 gas to dry it, and then setting the time for supplying the diluent to a short time can also efficiently remove particles. [Verification Test 4] In addition, when the diluent was intermittently supplied to the inspection wafer W, the drying time and the wafer W when the diluent was repeatedly stopped to dry the wafer W were verified. The effect of supply of thinner and drying of wafer W. [Certification Test 4-1] In the certification test 3-4b, the following example is set as the certification test 4-1. When the thinner on the surface of the inspection wafer W is removed, one side faces the inspection crystal. The circle W is supplied with N 2 gas, and the number of rotations of the inspection wafer W is set to the number of rotations of 3000 rpm, and the rotation is performed for 3 seconds. [Certificate Test 4-2] The following example is referred to as the Certify Test 4-2. In a state where the diluent is stopped following the processing of the certify test 4-1, the number of revolutions is set to 1000 rpm on one side. The inspection wafer W is rotated for 3 seconds, and while the N 2 gas is supplied to remove the diluent on the surface of the inspection wafer W, the inspection wafer W is further rotated at a rotation speed of 1000 rpm, while the inspection wafer W faces the wafer W. The central portion was supplied with the diluent for 3 seconds. For the verification tests 4-1 to 4-2, the difference between the number of PSL particles before the test and the number of PSL particles after the test in the inspection wafer W was similarly calculated, and the removal rate of the PSL particles was calculated. [0054] FIG. 18 is a graph showing the results and characteristic diagrams of the removal rate of PSL particles in verification test 3-4b and the removal rate of PSL particles in verification test 4-1 and verification test 4-2 . In the verification test 3-4b, the removal rate of PSL particles is as high as 59.1%, but in the verification test 4-1, the removal rate of PSL particles is 67.2%, and in the verification test 4- In 2, the removal rate of PSL particles was 72.9%. [0055] Based on the results, it can be said that the inspection wafer W is rotated while the diluent is stopped, and the time for supplying the N 2 gas is lengthened, so that the removal rate of the particles is improved, and more In a state where the diluent is stopped, the inspection wafer W is rotated while supplying the N 2 gas while the inspection wafer W is rotated, and the diluent is supplied to the surface of the inspection wafer W while the inspection wafer W is rotated. The engineering method improves the removal rate of particles. [0056] As described above, in the case where the supply time of the diluent is lengthened, the rotation speed of the wafer W is increased, and the flow rate of the diluent is increased, the removal rate of the particles will be improved, in particular, It can be said that after the diluent is supplied and dried, fine particles can be efficiently removed by further supplying the diluent. In addition, when drying the wafer W, it is also possible to shorten the drying time and reduce the flow rate of the diluent by blowing gas onto the wafer W. In addition, by repeating the process of supplying the diluent to the wafer W several times and the process of drying the wafer W, particles can be efficiently removed. [0057] The SOC film was continuously formed on the inspection wafer W subjected to each of the reference example, verification test 3-4b, and verification test 4, and the number of plaques formed on the SOC film was counted. The number of plaques counted in each of the inspection wafers W of the reference example, verification test 3-4b, and verification test 4 were 214, 118, and 7, respectively. Compared with the reference example, the number of genital plaques was significantly reduced in the known verification test 3-4b, and in the verification test 4, the number was significantly reduced. [0058] Instead of the inspection wafer W, a wafer having a step pattern is formed, and each of the reference example, verification test 3-4b, and verification test 4 is performed thereon, and then a SOC film is formed and counted The number of plaques formed on the SOC film. The number of plaques counted in wafer W of the reference example, verification test 3-4b, and verification test 4 were 84, 20, and 4, respectively. From the results, it can be said that when the present invention is applied to a wafer W on which a step pattern is formed, particles can be similarly removed, and the formation of plaque in the coating film can be suppressed.
[0059][0059]
2‧‧‧罩杯體2‧‧‧ cup body
3‧‧‧塗佈液噴嘴3‧‧‧ coating liquid nozzle
4‧‧‧稀釋劑噴嘴4‧‧‧ thinner nozzle
5‧‧‧N2氣體噴嘴5‧‧‧N 2 gas nozzle
6‧‧‧噴嘴單元6‧‧‧ Nozzle unit
100‧‧‧稀釋劑100‧‧‧ thinner
101‧‧‧微粒101‧‧‧ particles
102‧‧‧塗佈液102‧‧‧coating liquid
W‧‧‧晶圓W‧‧‧ Wafer
[0011] [圖1]本發明之實施形態之SOC膜塗佈裝置的剖面圖。 [圖2]使晶圓之旋轉數的時序圖與處理工程對應的說明圖。 [圖3]說明本發明之實施形態之作用的說明圖。 [圖4]說明本發明之實施形態之作用的說明圖。 [圖5]說明本發明之實施形態之作用的說明圖。 [圖6]說明本發明之實施形態之作用的說明圖。 [圖7]說明本發明之實施形態之作用的說明圖。 [圖8]說明本發明之實施形態之作用的說明圖。 [圖9]說明本發明之實施形態之作用的說明圖。 [圖10]說明本發明之實施形態之作用的說明圖。 [圖11]說明本發明之實施形態之作用的說明圖。 [圖12]表示檢證試驗1中之PSL粒子之去除率的特性圖。 [圖13]表示檢證試驗2中之PSL粒子之去除率的特性圖。 [圖14]表示檢證試驗3中之PSL粒子之去除率的特性圖。 [圖15]表示檢證試驗3中之PSL粒子之去除率的特性圖。 [圖16]表示檢證試驗3中之PSL粒子之去除率的特性圖。 [圖17]表示檢證試驗3中之PSL粒子之去除率的特性圖。 [圖18]表示檢證試驗4中之PSL粒子之去除率的特性圖。[0011] [FIG. 1] A cross-sectional view of an SOC film coating apparatus according to an embodiment of the present invention. [Fig. 2] An explanatory diagram corresponding to the timing chart of the number of wafer rotations and the corresponding process. [Fig. 3] An explanatory diagram for explaining the effect of the embodiment of the present invention. [Fig. 4] An explanatory diagram for explaining the effect of the embodiment of the present invention. [FIG. 5] An explanatory diagram for explaining the effect of the embodiment of the present invention. [FIG. 6] An explanatory diagram for explaining the effect of the embodiment of the present invention. [FIG. 7] An explanatory diagram for explaining the effect of the embodiment of the present invention. [FIG. 8] An explanatory diagram for explaining the effect of the embodiment of the present invention. [FIG. 9] An explanatory diagram for explaining the effect of the embodiment of the present invention. [FIG. 10] An explanatory diagram for explaining the effect of the embodiment of the present invention. [FIG. 11] An explanatory diagram for explaining the effect of the embodiment of the present invention. [Fig. 12] A characteristic diagram showing the removal rate of PSL particles in the verification test 1. [Fig. [Fig. 13] A characteristic diagram showing the removal rate of PSL particles in the verification test 2. [Fig. [Fig. 14] A characteristic diagram showing the removal rate of PSL particles in the verification test 3. [Fig. [Fig. 15] A characteristic diagram showing the removal rate of PSL particles in the verification test 3. [Fig. [Fig. 16] A characteristic diagram showing the removal rate of PSL particles in the verification test 3. [Fig. [Fig. 17] A characteristic diagram showing the removal rate of PSL particles in the verification test 3. [Fig. [Fig. 18] A characteristic diagram showing the removal rate of PSL particles in the verification test 4. [Fig.
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| JP7607230B2 (en) * | 2020-09-16 | 2024-12-27 | パナソニックIpマネジメント株式会社 | Coating device and coating method |
| KR102845108B1 (en) | 2022-12-12 | 2025-08-13 | 세메스 주식회사 | Apparatus for treating substrate and method for treating a substrate |
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| JP2003086491A (en) * | 2001-09-12 | 2003-03-20 | Tokyo Electron Ltd | Substrate processing method and coating film forming method |
| JP4040063B2 (en) * | 2003-11-18 | 2008-01-30 | 東京エレクトロン株式会社 | Substrate cleaning method, substrate cleaning apparatus, and computer-readable recording medium |
| JP4817887B2 (en) * | 2006-03-02 | 2011-11-16 | ジルトロニック アクチエンゲゼルシャフト | Semiconductor substrate cleaning method |
| JP2007273567A (en) * | 2006-03-30 | 2007-10-18 | Hitachi High-Technologies Corp | Substrate processing apparatus, substrate processing method, and substrate manufacturing method |
| JP5173900B2 (en) * | 2009-03-12 | 2013-04-03 | 東京エレクトロン株式会社 | Resist application method |
| JP5813495B2 (en) * | 2011-04-15 | 2015-11-17 | 東京エレクトロン株式会社 | Liquid processing method, liquid processing apparatus, and storage medium |
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- 2017-06-21 JP JP2018535485A patent/JP6690717B2/en active Active
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| JP6690717B2 (en) | 2020-04-28 |
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