TWI651752B - Etching device, etching method, method of manufacturing substrate, and substrate - Google Patents
Etching device, etching method, method of manufacturing substrate, and substrate Download PDFInfo
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Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/67—Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
- H01L21/677—Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations
- H01L21/67739—Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations into and out of processing chamber
- H01L21/6776—Continuous loading and unloading into and out of a processing chamber, e.g. transporting belts within processing chambers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/302—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to change their surface-physical characteristics or shape, e.g. etching, polishing, cutting
- H01L21/306—Chemical or electrical treatment, e.g. electrolytic etching
- H01L21/30604—Chemical etching
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/67—Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
- H01L21/67005—Apparatus not specifically provided for elsewhere
- H01L21/67011—Apparatus for manufacture or treatment
- H01L21/67017—Apparatus for fluid treatment
- H01L21/67063—Apparatus for fluid treatment for etching
- H01L21/67075—Apparatus for fluid treatment for etching for wet etching
- H01L21/67086—Apparatus for fluid treatment for etching for wet etching with the semiconductor substrates being dipped in baths or vessels
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/67—Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
- H01L21/67005—Apparatus not specifically provided for elsewhere
- H01L21/67011—Apparatus for manufacture or treatment
- H01L21/67155—Apparatus for manufacturing or treating in a plurality of work-stations
- H01L21/67161—Apparatus for manufacturing or treating in a plurality of work-stations characterized by the layout of the process chambers
- H01L21/67173—Apparatus for manufacturing or treating in a plurality of work-stations characterized by the layout of the process chambers in-line arrangement
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- Condensed Matter Physics & Semiconductors (AREA)
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- Microelectronics & Electronic Packaging (AREA)
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Abstract
本發明之蝕刻裝置(100)包含:蝕刻槽(110),其具有基板搬入口(111)及基板搬出口(112);搬送裝置(120),其自基板搬入口(111)朝向基板搬出口(112)搬送基板(500);噴嘴(130),其設置於蝕刻槽(110)內部,將反應氣體吹送至藉由搬送裝置(120)搬送之基板500之背面(510);及氣流控制裝置(140),其設置於蝕刻槽(110)內部,抑制自基板搬入口(111)及基板搬出口(112)流入蝕刻槽(110)內部之外部空氣流入基板(500)之背面(510)與噴嘴(130)間之間隙(131)。 The etching apparatus (100) of the present invention includes an etching tank (110) having a substrate carrying inlet (111) and a substrate carrying outlet (112), and a conveying device (120) that is moved from the substrate carrying inlet (111) toward the substrate. (112) transporting the substrate (500); the nozzle (130) is disposed inside the etching bath (110), and blowing the reaction gas to the back surface (510) of the substrate 500 transported by the transport device (120); and the air flow control device (140), which is disposed inside the etching bath (110), and prevents external air flowing into the etching tank (110) from the substrate carrying inlet (111) and the substrate carrying outlet (112) from flowing into the back surface (510) of the substrate (500) and A gap (131) between the nozzles (130).
Description
本發明係關於蝕刻裝置、蝕刻方法、基板之製造方法、及基板者。 The present invention relates to an etching apparatus, an etching method, a method of manufacturing a substrate, and a substrate.
已知於平面顯示器之製造過程中,已知會由於基板與平台等接觸時所產生之靜電使得基板帶電。因此,為了抑制此種帶電,已有提出將基板載置於平台等側之面(以下,稱為「背面」)藉由包含HF系氣體之電漿進行蝕刻,將基板的背面粗面化之方法(例如,參照專利文獻1)。又,已知有使含氟之氣體與水蒸氣及電漿反應而產生含HF系氣體之反應氣體,並將該反應氣體吹送至基板而蝕刻基板之方法(例如,參照專利文獻2)。 It is known that in the manufacturing process of a flat panel display, it is known that the substrate is charged by static electricity generated when the substrate is in contact with a stage or the like. Therefore, in order to suppress such charging, it has been proposed that the substrate is placed on the side of the platform or the like (hereinafter referred to as "back surface"), and the back surface of the substrate is roughened by etching with a plasma containing an HF-based gas. Method (for example, refer to Patent Document 1). Further, a method of reacting a fluorine-containing gas with steam and a plasma to generate a reaction gas containing an HF-based gas, and blowing the reaction gas onto a substrate to etch the substrate is known (for example, see Patent Document 2).
作為蝕刻裝置,已知有於進行玻璃基板之化學處理之槽(以下,稱為「蝕刻槽」)設置有基板搬入口及基板搬出口之構成(例如,參照專利文獻3)。為了連續地進行自搬入基板至搬出基板之工序,將基板搬入口及基板搬出口設為開放,一面自基板搬入口至基板搬出口搬送基板,並自設置於基板搬送路徑上之噴嘴將反應氣體吹送至基板之一面。 As the etching apparatus, a configuration in which a substrate carrying port and a substrate carrying port are provided in a groove for performing chemical treatment of a glass substrate (hereinafter referred to as "etching groove") is known (for example, see Patent Document 3). In order to continuously carry out the process of loading the substrate into the substrate, the substrate transfer port and the substrate transfer port are opened, and the substrate is transferred from the substrate transfer port to the substrate transfer port, and the reaction gas is supplied from the nozzle provided on the substrate transfer path. Blow to one side of the substrate.
專利文獻1:國際公開第2010/128673號 Patent Document 1: International Publication No. 2010/128673
專利文獻2:日本國特開2007-201067號公報 Patent Document 2: Japanese Patent Laid-Open No. 2007-201067
專利文獻3:日本國特開2012-216581號公報 Patent Document 3: Japanese Patent Laid-Open Publication No. 2012-216581
基板背面內的各部位之粗度係根據其部位所暴露之反應氣體之濃度、及其部位暴露於反應氣體之累積時間這2個要因而決定。該等要因會因自基板搬入口及基板搬出口流入之外部空氣引起之氣流干擾而大幅變動。然而,於先前之蝕刻裝置中,由於無法充分地抑制氣流干擾之影響,故隨著外部空氣流入蝕刻槽內部,產生粗度之不均一性。結果,難以降低基板背面中靜電之帶電量。 The thickness of each portion in the back surface of the substrate is determined based on the concentration of the reaction gas exposed at the portion thereof and the cumulative time at which the portion is exposed to the reaction gas. These factors may vary greatly due to airflow disturbances caused by external air flowing in from the substrate transfer port and the substrate transfer port. However, in the prior etching apparatus, since the influence of the airflow disturbance cannot be sufficiently suppressed, the unevenness of the thickness occurs as the outside air flows into the inside of the etching bath. As a result, it is difficult to reduce the amount of charge of static electricity in the back surface of the substrate.
本發明係鑑於上述狀況而完成者,其目的在於提供一種可抑制隨著外部空氣流入蝕刻槽內部引起粗度不均一性之蝕刻裝置及蝕刻方法。 The present invention has been made in view of the above circumstances, and an object thereof is to provide an etching apparatus and an etching method capable of suppressing thickness unevenness caused by external air flowing into an etching bath.
本發明一態樣之蝕刻裝置包含:蝕刻槽,其具有基板搬入口及基板搬出口;搬送裝置,其自上述基板搬入口朝向上述基板搬出口搬送基板;噴嘴,其設置於上述蝕刻槽之內部,將反應氣體吹送至藉由上述搬送裝置搬送之上述基板之一面;及氣流控制裝置,其設置於上述蝕刻槽之內部,抑制自上述基板搬入口及上述基板搬出口流入上述蝕刻槽內部之外部空氣流入上述基板之一面與上述噴嘴之間之間隙。 An etching apparatus according to an aspect of the present invention includes: an etching tank having a substrate carrying port and a substrate carrying port; and a conveying device that transports the substrate from the substrate carrying port toward the substrate carrying port; and the nozzle is disposed inside the etching groove a reaction gas is blown to one surface of the substrate conveyed by the transfer device, and a gas flow control device is provided inside the etching groove to prevent the inside of the etching groove from flowing into the inside of the etching groove from the substrate transfer port and the substrate transfer port Air flows into a gap between one of the surfaces of the substrate and the nozzle.
於本發明一態樣之蝕刻裝置中,上述氣流控制裝置可包含:第一通氣路徑,其係使自上述基板搬入口朝向上述間隙流入上述蝕刻槽內部之外部空氣,自設置於上述基板搬入口與上述噴嘴之間之第1通氣口流入;及第二通氣路徑,其係使自上述基板搬出口朝向上述間隙流入上述蝕刻槽內部之外部空氣,自設置於上述基板搬出口與上述噴嘴之間之第二通氣口流入。 In an etching apparatus according to an aspect of the present invention, the airflow control device may include: a first ventilation path that allows external air flowing into the etching groove from the substrate carrying inlet toward the gap, and is disposed at the substrate carrying inlet a first vent opening between the nozzle and the second venting path, the outside air flowing into the etching groove from the substrate carrying port toward the gap is provided between the substrate carrying port and the nozzle The second vent flows in.
本發明一態樣之蝕刻裝置可包含:連接路徑,其係連接上述第 一通氣路徑與上述第二通氣路徑。 An etching apparatus according to an aspect of the present invention may include: a connection path connecting the above a venting path and the second venting path described above.
本發明一態樣之蝕刻裝置可包含:抽吸裝置,其抽吸自上述第一通氣路徑及上述第二通氣路徑流入上述連接路徑之外部空氣。 An etching apparatus according to an aspect of the present invention may include: a suction device that sucks outside air flowing from the first ventilation path and the second ventilation path into the connection path.
於本發明一態樣之蝕刻裝置中,可自上述基板搬入口觀察,以封塞上述噴嘴前方之方式設置上述第一通氣路徑,且自上述基板搬出口觀察,以封塞上述噴嘴前方之方式設置上述第二通氣路徑。 In an etching apparatus according to an aspect of the present invention, the first ventilation path may be provided to block the front side of the nozzle as viewed from the substrate carrying inlet, and the front side of the nozzle may be blocked by observing the front side of the nozzle. The second ventilation path described above is set.
本發明一態樣之蝕刻方法係自具有基板搬入口及基板搬出口之蝕刻槽之上述基板搬入口朝向上述基板搬出口搬送基板,一面抑制自上述基板搬入口及上述基板搬出口流入上述蝕刻槽內部之外部空氣流入上述基板之一面與噴嘴之間之間隙,一面自上述噴嘴將反應氣體吹送至上述基板之一面。 In the etching method of the present invention, the substrate is carried out from the substrate transfer port having the substrate transfer port and the substrate transfer port toward the substrate transfer port, and the etching port is prevented from flowing into the etching groove from the substrate transfer port and the substrate transfer port. The outside air flows into the gap between the one surface of the substrate and the nozzle, and the reaction gas is blown from the nozzle to one surface of the substrate.
於本發明一態樣之蝕刻方法中,藉由使自上述基板搬入口朝向上述間隙流入上述蝕刻槽內部之外部空氣自設置於上述基板搬入口與上述噴嘴之間之第一通氣口流入第一通氣路徑,抑制自上述基板搬入口流入上述蝕刻槽內部之外部空氣流入上述間隙,且,藉由使自上述基板搬出口朝向上述間隙流入上述蝕刻槽內部之外部空氣自設置於上述基板搬出口與上述噴嘴之間之第二通氣口流入第二通氣路徑,抑制自上述基板搬出口流入上述蝕刻槽內部之外部空氣流入上述間隙,於本發明一態樣之蝕刻方法中,可抽吸流入連接上述第一通氣路徑與上述第二通氣路徑之連接路徑之外部空氣。 In an etching method according to an aspect of the present invention, external air flowing into the etching chamber from the substrate carrying port toward the gap flows into the first vent port provided between the substrate carrying port and the nozzle. The air passage prevents the outside air flowing into the etching tank from the substrate carrying inlet from flowing into the gap, and the outside air that flows into the etching tank from the substrate carrying port toward the gap is provided in the substrate carrying port and The second vent port between the nozzles flows into the second air passage, and the outside air flowing into the etching tank from the substrate carrying port is prevented from flowing into the gap. In an etching method according to an aspect of the present invention, the inflow and the inflow connection may be The outside air of the connection path of the first ventilation path and the second ventilation path.
本發明一態樣之基板之製造方法係包含藉由上述蝕刻方法而蝕刻基板之工序的基板之製造方法。 A method of manufacturing a substrate according to an aspect of the present invention includes a method of manufacturing a substrate in which a substrate is etched by the etching method.
本發明一態樣之基板係具有第一面、及與上述第一面相反側之第二面之基板者,且上述第一面整體之算術平均表面粗度之平均值係0.3~1.5nm,上述第一面之周緣部之算術平均表面粗度之平均值與上述第一面之中央 部之算術平均表面粗度不同,上述第一面整體之算術平均表面粗度之標準偏差為0.06以下。 A substrate according to an aspect of the present invention has a first surface and a substrate on a second surface opposite to the first surface, and an average value of an arithmetic mean surface roughness of the entire first surface is 0.3 to 1.5 nm. The average of the arithmetic mean surface roughness of the peripheral portion of the first surface and the center of the first surface The arithmetic mean surface roughness of the portion is different, and the standard deviation of the arithmetic mean surface roughness of the entire first surface is 0.06 or less.
於本發明一態樣之基板中,上述基板之尺寸可為1500mm×1500mm以上。 In the substrate of one aspect of the invention, the substrate may have a size of 1500 mm × 1500 mm or more.
於本發明一態樣之基板中,上述第一面之中央部之算術平均表面粗度與上述第一面整體之算術平均表面粗度之平均值之差可為-0.13以上0.13以下。 In the substrate according to one aspect of the invention, the difference between the arithmetic mean surface roughness of the central portion of the first surface and the average of the arithmetic mean surface roughness of the entire first surface may be -0.13 or more and 0.13 or less.
根據本發明,可抑制隨著外部空氣流入蝕刻槽內部引起之粗度之不均一性。 According to the present invention, it is possible to suppress the unevenness of the thickness caused by the flow of outside air into the inside of the etching bath.
100‧‧‧蝕刻裝置 100‧‧‧ etching device
110‧‧‧蝕刻槽 110‧‧‧etching trough
111‧‧‧基板搬入口 111‧‧‧Substrate entrance
112‧‧‧基板搬出口 112‧‧‧Substrate removal
120‧‧‧搬送裝置 120‧‧‧Transporting device
121‧‧‧滾筒 121‧‧‧Roller
130‧‧‧噴嘴 130‧‧‧Nozzles
131‧‧‧間隙 131‧‧‧ gap
132‧‧‧氣體供給路徑 132‧‧‧ gas supply path
132a‧‧‧吹出口 132a‧‧‧Blowing out
133‧‧‧第一氣體抽吸路徑 133‧‧‧First gas aspiration path
133a‧‧‧第一抽吸口 133a‧‧‧first suction port
134‧‧‧第二氣體抽吸路徑 134‧‧‧Second gas suction path
134a‧‧‧第二抽吸口 134a‧‧‧second suction port
135‧‧‧頂板 135‧‧‧ top board
140‧‧‧氣流控制裝置 140‧‧‧Airflow control device
141‧‧‧第一通氣路徑 141‧‧‧First ventilation path
141a‧‧‧第一背面板 141a‧‧‧First back panel
141b‧‧‧第一前面板 141b‧‧‧ first front panel
141c‧‧‧第一通氣口 141c‧‧‧First vent
142‧‧‧第二通氣路徑 142‧‧‧second ventilation path
142a‧‧‧第二背面板 142a‧‧‧second back panel
142b‧‧‧第二前面板 142b‧‧‧ second front panel
142c‧‧‧第二通氣口 142c‧‧‧second vent
143‧‧‧第一排氣口 143‧‧‧first exhaust
144‧‧‧第二排氣口 144‧‧‧Second vent
144c‧‧‧第一通氣口 144c‧‧‧First vent
150‧‧‧連接路徑 150‧‧‧Connection path
160‧‧‧抽吸裝置 160‧‧‧Suction device
500‧‧‧基板 500‧‧‧Substrate
510‧‧‧背面 510‧‧‧ back
520‧‧‧正面 520‧‧‧ positive
600‧‧‧氣體回收裝置 600‧‧‧ gas recovery unit
700‧‧‧空間 700‧‧‧ space
711‧‧‧基板搬入口 711‧‧‧Substrate entrance
712‧‧‧基板搬出口 712‧‧‧Substrate removal
730‧‧‧噴嘴 730‧‧‧Nozzle
731‧‧‧間隙 731‧‧‧ gap
732‧‧‧氣體供給路徑 732‧‧‧ gas supply path
732a‧‧‧吹出口 732a‧‧‧Blowing
733‧‧‧第一氣體抽吸路徑 733‧‧‧First gas aspiration path
733a‧‧‧第一抽吸口 733a‧‧‧first suction port
734‧‧‧第二氣體抽吸路徑 734‧‧‧Second gas suction path
734a‧‧‧第二抽吸口 734a‧‧‧second suction port
741‧‧‧第一通氣路徑 741‧‧‧First ventilation path
742‧‧‧第二通氣路徑 742‧‧‧second ventilation path
750‧‧‧基板 750‧‧‧Substrate
751‧‧‧背面 751‧‧‧Back
1000‧‧‧基板製造系統 1000‧‧‧Substrate Manufacturing System
1010‧‧‧第一清洗槽 1010‧‧‧First cleaning tank
1020‧‧‧第一緩衝槽 1020‧‧‧First buffer tank
1030‧‧‧蝕刻槽 1030‧‧‧etching groove
1031‧‧‧基板搬入口 1031‧‧‧Substrate entrance
1032‧‧‧基板搬出口 1032‧‧‧Substrate removal
1040‧‧‧第二緩衝槽 1040‧‧‧Second buffer tank
1050‧‧‧第二清洗槽 1050‧‧‧Second cleaning tank
1051‧‧‧高壓沖淋 1051‧‧‧High pressure shower
1070‧‧‧搬送裝置 1070‧‧‧Transporting device
1071‧‧‧滾筒 1071‧‧‧Roller
1080‧‧‧噴嘴 1080‧‧‧Nozzles
dA‧‧‧大小 dA‧‧‧Size
dB‧‧‧大小 dB‧‧‧Size
dC‧‧‧大小 dC‧‧‧Size
dD‧‧‧大小 dD‧‧‧Size
EXH1‧‧‧排氣口 EXH1‧‧ vent
EXH2‧‧‧排氣口 EXH2‧‧ vent
FFU1‧‧‧風扇過濾單元 FFU1‧‧‧Fan filter unit
FFU2‧‧‧風扇過濾單元 FFU2‧‧‧Fan filter unit
I1‧‧‧距離 I1‧‧‧ distance
I2‧‧‧距離 I2‧‧‧ distance
圖1係示意性顯示本發明第一實施形態之蝕刻裝置之側視圖。 Fig. 1 is a side view schematically showing an etching apparatus according to a first embodiment of the present invention.
圖2係本發明第一實施形態之蝕刻裝置之噴嘴之剖視圖。 Fig. 2 is a cross-sectional view showing a nozzle of the etching apparatus according to the first embodiment of the present invention.
圖3係自基板搬入口側觀察之噴嘴及氣流控制裝置之前視圖。 Fig. 3 is a front view of the nozzle and the air flow control device as viewed from the substrate carrying inlet side.
圖4係顯示蝕刻槽內外部空氣之流動之示意圖,(a)係顯示於噴嘴附近設置有第一通氣路徑與第二通氣路徑時外部空氣之流動之圖,(b)係顯示於噴嘴附近不設置此種通氣路徑時外部空氣之流動之圖。 4 is a schematic view showing the flow of outside air in the etching bath, (a) showing a flow of external air when the first ventilation path and the second ventilation path are provided near the nozzle, and (b) showing not near the nozzle. A diagram showing the flow of outside air when such a ventilation path is set.
圖5係顯示包含本發明第一實施形態之蝕刻裝置之基板製造系統之一部分之側視圖。 Fig. 5 is a side view showing a part of a substrate manufacturing system including an etching apparatus according to a first embodiment of the present invention.
圖6係顯示蝕刻槽不包含氣流控制裝置時噴嘴周邊之氣壓變動分佈之圖,(a)係顯示基板之前端部到達噴嘴附近之狀態之圖,(b)係基板自基板搬入口被搬送至基板搬出口之中途階段之狀態之圖,(c)係基板之後端部被搬送至噴嘴附近之狀態之圖。 6 is a view showing a distribution of air pressure fluctuation around the nozzle when the etching groove does not include the air flow control device, wherein (a) shows a state in which the end portion of the substrate reaches the vicinity of the nozzle, and (b) the substrate is transferred from the substrate transfer port to the substrate. (c) a diagram showing a state in which the end portion of the substrate is conveyed to the vicinity of the nozzle.
圖7係顯示反應氣體濃度分佈相關之數值模擬計算模型之圖,(a)係顯示比蝕刻槽內之基板更下面之空間之計算模型,(b)係擴大模擬空間中噴嘴與基板之間隙之圖。 7 is a diagram showing a numerical simulation calculation model relating to a concentration distribution of a reaction gas, (a) showing a calculation model of a space lower than a substrate in an etching bath, and (b) expanding a gap between a nozzle and a substrate in the simulation space. Figure.
圖8係顯示反應氣體濃度分佈相關之數值模擬結果之抽吸壓力依存性之圖,(a)係顯示於導入氣流控制裝置之前之比較例中,計算間隙中反應氣體濃度分佈的結果之例之圖,(b)、(c)及(d)係依序顯示對於PBB=-0.5 Pa、-1 Pa、-1.5 Pa時之實施例之計算結果之圖。 Fig. 8 is a graph showing the dependence of the suction pressure on the numerical simulation results relating to the concentration distribution of the reaction gas, and (a) shows an example of the result of calculating the concentration distribution of the reaction gas in the gap in the comparative example before the introduction of the gas flow control device. Fig., (b), (c) and (d) are graphs showing the calculation results of the examples for PBB = -0.5 Pa, -1 Pa, -1.5 Pa, in order.
圖9係顯示反應氣體濃度分佈相關之數值模擬結果之抽吸壓力依存性之圖,(a)係顯示比較例之計算結果之圖,(b)、(c)及(d)係依序顯示於PBB=-0.5 Pa、-1 Pa、-1.5 Pa時之實施例之計算結果之圖。 Fig. 9 is a graph showing the dependence of the suction pressure on the numerical simulation results relating to the concentration distribution of the reaction gas, (a) showing the calculation results of the comparative examples, and (b), (c) and (d) are sequentially displayed. A graph of the calculation results of the examples at PBB = -0.5 Pa, -1 Pa, -1.5 Pa.
於本發明之實施形態中,使用圖1至圖4進行說明。圖1係示意性顯示蝕刻裝置100之側視圖。圖2係噴嘴130之剖視圖。圖3係自基板搬入口側觀察噴嘴及氣流控制裝置之前視圖。圖4係顯示蝕刻槽中之外部空氣流動之示意圖。圖4(a)係顯示於噴嘴130附近設置有第一通氣路徑141與第二通氣路徑142時外部空氣之流動之圖,圖4(b)係顯示於噴嘴130附近不設置此種通氣路徑時外部空氣之流動之圖。於圖4(a)及圖4(b)中,以較粗之箭頭表示外部空氣之流動。 In the embodiment of the present invention, description will be made using Figs. 1 to 4 . FIG. 1 is a side view schematically showing an etching apparatus 100. 2 is a cross-sectional view of the nozzle 130. Fig. 3 is a front view of the nozzle and the air flow control device viewed from the substrate carrying inlet side. Figure 4 is a schematic diagram showing the flow of outside air in an etch bath. 4(a) is a view showing the flow of outside air when the first ventilation path 141 and the second ventilation path 142 are provided in the vicinity of the nozzle 130, and FIG. 4(b) shows that the ventilation path is not provided near the nozzle 130. A map of the flow of outside air. In Figs. 4(a) and 4(b), the flow of the outside air is indicated by a thicker arrow.
以下,對本實施形態之蝕刻裝置100,使用圖1進行說明。 Hereinafter, the etching apparatus 100 of the present embodiment will be described with reference to Fig. 1 .
如圖1所示,蝕刻裝置100包含:蝕刻槽110、搬送裝置120、噴嘴130、氣流控制裝置140。蝕刻裝置100係對基板500之一表面(例如背面510)實施使用外部空氣壓電漿之化學處理。藉此,將基板500之一表面粗面化。 As shown in FIG. 1, the etching apparatus 100 includes an etching bath 110, a conveying device 120, a nozzle 130, and a gas flow control device 140. The etching apparatus 100 performs a chemical treatment using an external air piezoelectric slurry on one surface of the substrate 500 (for example, the back surface 510). Thereby, the surface of one of the substrates 500 is roughened.
基板500係例如使用於液晶顯示器或有機EL顯示器之平板顯示器、有機EL照明、太陽電池、蓄電池等電子器件之玻璃基板。基板500係於後述之基板500之製造過程中被切成矩形。基板500之尺寸例如於寬度方向(圖1之與紙面正交之方向)為2880mm,於搬送方向(圖1紙面內左右方向)為3130mm。又,基板500之厚度係例如0.6mm。另,基板500之尺寸及厚度並非限定於該等值者。基板500之形狀亦不 限定於矩形狀,可為圓形狀或帶狀。 The substrate 500 is, for example, a glass substrate used for a liquid crystal display, a flat panel display of an organic EL display, an organic EL illumination, a solar cell, a battery, or the like. The substrate 500 is cut into a rectangular shape in the manufacturing process of the substrate 500 to be described later. The size of the substrate 500 is, for example, 2880 mm in the width direction (the direction orthogonal to the plane of the drawing in FIG. 1), and 3130 mm in the conveyance direction (the horizontal direction in the paper surface in FIG. 1). Further, the thickness of the substrate 500 is, for example, 0.6 mm. In addition, the size and thickness of the substrate 500 are not limited to the equivalent. The shape of the substrate 500 is also not It is limited to a rectangular shape and may be a circular shape or a ribbon shape.
蝕刻槽110具有基板搬入口111及基板搬出口112。基板搬入口111及基板搬出口112如圖1所示位於相同高度。基板搬入口111及基板搬出口112具有於基板500之寬度方向延伸之縫隙形狀。基板搬入口111及基板搬出口112之寬度(圖1之與紙面正交之方向之長度)係以基板500可通過之方式,設為若干大於基板500之寬度之值。又,基板搬入口111及基板搬出口112之高度(圖1之紙面內上下方向之長度)係設為充分大於基板500之厚度之值。例如,基板搬入口111及基板搬出口112之高度為5~20mm。基板搬入口111及基板搬出口112例如於將基板500自基板搬入口111搬送至基板搬出口112之期間始終開放。 The etching bath 110 has a substrate carrying inlet 111 and a substrate carrying port 112. The substrate transfer port 111 and the substrate transfer port 112 are located at the same height as shown in FIG. 1 . The substrate carrying inlet 111 and the substrate carrying opening 112 have a slit shape extending in the width direction of the substrate 500. The width of the substrate carrying port 111 and the substrate carrying port 112 (the length in the direction orthogonal to the plane of the drawing in FIG. 1) is set to a value larger than the width of the substrate 500 so that the substrate 500 can pass therethrough. Moreover, the height of the substrate carrying port 111 and the substrate carrying port 112 (the length in the vertical direction of the paper surface in FIG. 1) is set to be sufficiently larger than the thickness of the substrate 500. For example, the height of the substrate carrying inlet 111 and the substrate carrying opening 112 is 5 to 20 mm. The substrate transfer port 111 and the substrate transfer port 112 are always open during the transfer of the substrate 500 from the substrate transfer port 111 to the substrate transfer port 112, for example.
搬送裝置120係自基板搬入口111朝向基板搬出口112搬送基板500。搬送裝置120係例如由複數個滾筒121構成之滾筒運送機。複數個滾筒121係於基板500之搬送方向隔開適當間隔互相平行地、且配合基板搬入口111及基板搬出口112之高度而設置。藉由複數個滾筒121,形成如下之搬送路徑:自基板500之搬送方向上游通過基板搬入口111進入蝕刻槽110之內部,通過基板搬出口112搬出至蝕刻槽110之外部,送往基板500之搬送方向下游。複數個滾筒121支持背面510並搬送基板500。因此,後述之正面520不接觸滾筒121,不會對正面520造成由滾筒121引起之傷。 The transport device 120 transports the substrate 500 from the substrate transfer port 111 toward the substrate transfer port 112. The conveying device 120 is, for example, a drum conveyor composed of a plurality of rollers 121. The plurality of rollers 121 are provided in parallel with each other at an appropriate interval in the transport direction of the substrate 500, and are matched with the heights of the substrate transfer port 111 and the substrate transfer port 112. The plurality of rollers 121 form a transport path that enters the inside of the etching bath 110 from the substrate transfer inlet 111 upstream of the substrate 500, and is carried out to the outside of the etching bath 110 through the substrate transfer port 112, and is sent to the substrate 500. The transport direction is downstream. The plurality of rollers 121 support the back surface 510 and transport the substrate 500. Therefore, the front surface 520 which will be described later does not contact the drum 121, and the front surface 520 is not damaged by the drum 121.
複數個滾筒121係藉由驅動控制機構(省略圖示)同步旋轉。藉由複數個滾筒121同步於相同朝向(圖1中係順時針)旋轉,基板500自基板搬入口111朝向基板搬出口水平地被搬送。另,搬送裝置120不限定於滾筒運送機,亦可藉由帶式運送機、機器臂等機構實現。 The plurality of rollers 121 are synchronously rotated by a drive control mechanism (not shown). When the plurality of rollers 121 are rotated in the same direction (clockwise in FIG. 1), the substrate 500 is horizontally transported from the substrate loading port 111 toward the substrate carrying port. Further, the conveying device 120 is not limited to the drum conveyor, and may be realized by a mechanism such as a belt conveyor or a robot arm.
噴嘴130係將反應氣體吹送至藉由搬送裝置120搬送之基板500之一表面(例如,背面510)。噴嘴130設置於蝕刻槽110之內部。 The nozzle 130 blows a reaction gas to one surface (for example, the back surface 510) of the substrate 500 conveyed by the transfer device 120. The nozzle 130 is disposed inside the etching bath 110.
以下,使用圖1至圖3,對噴嘴130之詳細構造進行說明。 Hereinafter, the detailed structure of the nozzle 130 will be described with reference to Figs. 1 to 3 .
噴嘴130例如如圖2所示,包含:氣體供給路徑132、第一氣體抽吸路徑133及第二氣體抽吸路徑134。噴嘴130之上端係平面狀。於噴嘴130之上端,設置氣體供給路徑132之吹出口132a、第一氣體抽吸路徑133之第一抽吸口133a、及第二氣體抽吸路徑134之第二抽吸口134a。第一抽吸口133a設置於吹出口132a與基板搬入口111之間,第二抽吸口134a設置於吹出口132a與基板搬出口112之間。氣體供給路徑132、第一氣體抽吸路徑133及第二氣體抽吸路徑134於圖2之與紙面正交之方向具有相同之剖面。吹出口132a、第一抽吸口133a及第二抽吸口134a呈於圖2之與紙面正交之方向延伸之縫隙狀。吹出口132a、第一抽吸口133a及第二抽吸口134a之寬度(圖2之與紙面正交之方向之長度)係為了可遍及基板500之背面510整面進行粗面化,設為若干大於基板500之寬度。 The nozzle 130 includes, for example, a gas supply path 132, a first gas suction path 133, and a second gas suction path 134 as shown in FIG. 2 . The upper end of the nozzle 130 is planar. At the upper end of the nozzle 130, an air outlet 132a of the gas supply path 132, a first suction port 133a of the first gas suction path 133, and a second suction port 134a of the second gas suction path 134 are provided. The first suction port 133a is provided between the air outlet 132a and the substrate carrying port 111, and the second suction port 134a is provided between the air outlet 132a and the substrate carrying port 112. The gas supply path 132, the first gas suction path 133, and the second gas suction path 134 have the same cross section in the direction orthogonal to the plane of the drawing of FIG. The air outlet 132a, the first suction port 133a, and the second suction port 134a have a slit shape extending in a direction orthogonal to the plane of the paper of Fig. 2 . The width of the air outlet 132a, the first suction port 133a, and the second suction port 134a (the length in the direction orthogonal to the plane of the paper in FIG. 2) is designed to be roughened over the entire surface 510 of the substrate 500. A number is greater than the width of the substrate 500.
氣體供給路徑132連接於設置於蝕刻槽110外部之反應氣體生成裝置(省略圖示)。反應氣體生成裝置係自原料氣體生成反應氣體,並將反應氣體供給於氣體供給路徑132。又,於反應氣體生成裝置,設置原料氣體供給部(省略圖示)。原料氣體供給部供給反應氣體之原料,即原料氣體。原料氣體係例如包含氟系原料氣體、與載體氣體。 The gas supply path 132 is connected to a reaction gas generating device (not shown) provided outside the etching bath 110. The reaction gas generating device generates a reaction gas from the material gas, and supplies the reaction gas to the gas supply path 132. Further, a raw material gas supply unit (not shown) is provided in the reaction gas generating device. The material gas supply unit supplies a raw material of the reaction gas, that is, a material gas. The raw material gas system contains, for example, a fluorine-based source gas and a carrier gas.
氟系原料氣體係用於生成與基板500之表面反應之氟系反應成分。氟系反應成分可藉由將氟系原料氣體與水分子導入至電漿中使其反應而生成。載體氣體係用於進行氟系原料氣體之搬送及稀釋、或進行電漿放電。於本實施形態中,使用CF4作為氟系原料氣體,使用酒精作為載體氣體。又,以下作為氟系反應成分之例使用氟化氫(HF)進行說明。另,氟系原料氣體不限定於此,可使用C2F6、C3F8等其他全氟碳化物,CHF3、CH2F2、CH3F等氫氟碳,SF6、NF3、XeF2等其他含氟化合物。又,載體氣體不限定於此,可使用氦、氖、氙等其他惰性氣體。 The fluorine-based raw material gas system is used to generate a fluorine-based reaction component that reacts with the surface of the substrate 500. The fluorine-based reaction component can be produced by introducing a fluorine-based source gas and water molecules into a plasma to cause a reaction. The carrier gas system is used to carry out the transfer and dilution of the fluorine-based raw material gas or to perform plasma discharge. In the present embodiment, CF 4 is used as the fluorine-based source gas, and alcohol is used as the carrier gas. Further, the following description will be made using hydrogen fluoride (HF) as an example of a fluorine-based reaction component. Further, the fluorine-based source gas is not limited thereto, and other perfluorocarbons such as C 2 F 6 and C 3 F 8 may be used, and hydrofluorocarbons such as CHF 3 , CH 2 F 2 and CH 3 F, SF 6 and NF 3 may be used. Other fluorine-containing compounds such as XeF 2 . Further, the carrier gas is not limited thereto, and other inert gases such as helium, neon or xenon may be used.
原料氣體例如包含水蒸氣。於本實施形態中,原料氣體供給部包含對CF4及酒精添加水之水添加部。水添加部係例如將液體水作為飽和水蒸氣而供給之加濕器。水之添加量可藉由加濕器之溫度調節而調節。藉由調節水之添加量,可設定原料氣體內之水蒸氣分壓。藉此,可改變電漿中生成之氟系反應成分及水蒸氣之凝縮溫度(即,形成引起與基板反應之氫氟酸之溫度)。 The material gas contains, for example, water vapor. In the present embodiment, the material gas supply unit includes a water addition unit that adds water to CF 4 and alcohol. The water addition unit is, for example, a humidifier that supplies liquid water as saturated steam. The amount of water added can be adjusted by the temperature adjustment of the humidifier. The water vapor partial pressure in the material gas can be set by adjusting the amount of water added. Thereby, the condensation temperature of the fluorine-based reaction component and the water vapor generated in the plasma (that is, the temperature at which the hydrofluoric acid which causes the reaction with the substrate is formed) can be changed.
於反應氣體形成裝置,設置與原料氣體供給部連接之電漿生成部(省略圖示)。電漿生成部包含一對電極。一對電極係隔著供給原料氣體之通路而配置。一對電極之一者連接於電源,另一者接地。藉由自電源施加高電壓,於一對電極間產生電場進行放電。藉此,於一對電極間生成電漿,並藉由將原料氣體導入至電漿中與CF4及水分子反應,而生成與基板500之表面反應之氟化氫。即,藉由將原料氣體導入至電漿中而成為反應氣體。反應氣體係自吹出口132a吹送至基板500之背面510。 A plasma generating unit (not shown) connected to the material gas supply unit is provided in the reaction gas forming device. The plasma generating portion includes a pair of electrodes. The pair of electrodes are disposed via a passage for supplying the material gas. One of the pair of electrodes is connected to the power source and the other is grounded. By applying a high voltage from the power source, an electric field is generated between the pair of electrodes to discharge. Thereby, a plasma is generated between the pair of electrodes, and the raw material gas is introduced into the plasma to react with CF 4 and water molecules to generate hydrogen fluoride which reacts with the surface of the substrate 500. That is, the raw material gas is introduced into the plasma to become a reaction gas. The reaction gas system is blown from the air outlet 132a to the back surface 510 of the substrate 500.
頂板135係如圖1至圖3所示,對向於噴嘴130之上端,水平地設置於噴嘴130之上方。基板500自基板搬入口111被搬入後,通過噴嘴130之上端與頂板135之下表面之間,並自基板搬出口112搬出。噴嘴130之上端與頂板135之下表面間之距離係以基板500可通過之方式,設為與基板搬入口111及基板搬出口112之厚度(圖1之紙面內上下方向之長度)大致相等。 The top plate 135 is disposed above the nozzle 130 horizontally opposite to the upper end of the nozzle 130 as shown in FIGS. 1 to 3. After the substrate 500 is carried in from the substrate carrying inlet 111, it passes between the upper end of the nozzle 130 and the lower surface of the top plate 135, and is carried out from the substrate carrying opening 112. The distance between the upper end of the nozzle 130 and the lower surface of the top plate 135 is substantially equal to the thickness of the substrate carrying inlet 111 and the substrate carrying opening 112 (the length in the vertical direction of the paper surface in FIG. 1) so that the substrate 500 can pass therethrough.
於基板500通過噴嘴130之上端與頂板135之下表面間之期間,自吹出口132a吹出之反應氣體充滿於基板500之背面510與噴嘴130間之間隙131(參照圖2)。背面510暴露於反應氣體之期間,背面510被粗面化。 While the substrate 500 passes between the upper end of the nozzle 130 and the lower surface of the top plate 135, the reaction gas blown from the air outlet 132a fills the gap 131 between the back surface 510 of the substrate 500 and the nozzle 130 (see FIG. 2). The back surface 510 is roughened while the back surface 510 is exposed to the reaction gas.
背面510之算術平均表面粗度較好為0.3~1.5nm。若算術平均表面粗度為0.3nm以上,則於將基板500自平台剝離時難以產生剝離帶 電。若算術平均表面粗度為1.5nm以下,則粗面化處理不會耗費時間,亦無基板500之面內強度不足之虞。 The arithmetic mean surface roughness of the back surface 510 is preferably from 0.3 to 1.5 nm. When the arithmetic mean surface roughness is 0.3 nm or more, it is difficult to produce a peeling tape when the substrate 500 is peeled off from the stage. Electricity. When the arithmetic mean surface roughness is 1.5 nm or less, the roughening treatment does not take time, and the in-plane strength of the substrate 500 is not insufficient.
於頂板135之下表面,設置有自由調節溫度之平板狀加熱器(省略圖示)。藉由該加熱器,可加溫與基板500之背面510相反側之面(以下稱為「正面520」)中之位於頂板135正下方之區域。加熱器之寬度(如圖2之與紙面正交之方向之長度)係以可加溫基板500之正面520整面之方式,若干大於基板500之寬度。於將背面510定義為第一面之情形時,將與第一面相反側之正面520定義為第二面。 A flat heater (not shown) that freely adjusts the temperature is provided on the lower surface of the top plate 135. By the heater, a region on the side opposite to the back surface 510 of the substrate 500 (hereinafter referred to as "front surface 520") which is located immediately below the top plate 135 can be heated. The width of the heater (as shown in Fig. 2 in the direction orthogonal to the plane of the paper) is such that the entire surface of the front surface 520 of the substrate 500 can be warmed, a number of which is greater than the width of the substrate 500. When the back surface 510 is defined as the first surface, the front surface 520 on the opposite side to the first surface is defined as the second surface.
配合氟化氫與水蒸氣之上述凝縮溫度,適當設定將基板500搬入至蝕刻槽110時之溫度、及頂板135之加熱器之溫度。藉此,於基板500通過頂板135上之期間,可將背面510之溫度設為上述凝縮溫度以下,將正面520之溫度設為上述凝縮溫度以上。因此,氟化氫與水蒸氣僅於背面510凝縮,形成氫氟酸。藉此,即使自吹出口132a吹出之反應氣體之一部分進入頂板135與正面520之間隙,亦可僅對背面510選擇性地進行基板500之蝕刻。因此,形成電子構件或配線之正面520可不被粗面化而保持平滑。 The temperature at which the substrate 500 is carried into the etching bath 110 and the temperature of the heater of the top plate 135 are appropriately set in accordance with the condensation temperature of hydrogen fluoride and water vapor. Thereby, while the substrate 500 is passing through the top plate 135, the temperature of the back surface 510 can be set to be equal to or lower than the condensation temperature, and the temperature of the front surface 520 can be set to be equal to or higher than the condensation temperature. Therefore, hydrogen fluoride and water vapor condense only on the back surface 510 to form hydrofluoric acid. Thereby, even if one part of the reaction gas blown out from the air outlet 132a enters the gap between the top plate 135 and the front surface 520, the substrate 500 can be selectively etched only on the back surface 510. Therefore, the front surface 520 forming the electronic component or wiring can be kept smooth without being roughened.
第一氣體抽吸路徑133及第二氣體抽吸路徑134係於蝕刻槽110之外部,連接於氣體回收裝置600(參照圖1)。氣體回收裝置600包含一般之抽吸機構、例如旋轉泵。供給至間隙131之反應氣體自第一抽吸口133a及第二氣體抽吸口134a被抽吸,並通過第一氣體抽吸路徑133及第二氣體抽吸路徑134,由氣體回收裝置600被回收。 The first gas suction path 133 and the second gas suction path 134 are external to the etching bath 110 and are connected to the gas recovery device 600 (see FIG. 1). The gas recovery device 600 includes a general suction mechanism, such as a rotary pump. The reaction gas supplied to the gap 131 is sucked from the first suction port 133a and the second gas suction port 134a, and is passed through the first gas suction path 133 and the second gas suction path 134 by the gas recovery device 600. Recycling.
以下,使用圖1、圖3及圖4,對氣流控制裝置140進行說明。 Hereinafter, the air flow control device 140 will be described with reference to Figs. 1, 3, and 4.
氣流控制裝置140係如圖1所示,設置於蝕刻槽110之內部。氣流控制裝置140抑制自基板搬入口111及基板搬出口112流入蝕刻槽110內部之外部空氣流入基板500之一面(於本實施形態中為背面510)與噴嘴130間之間隙131(參照圖2)。如圖1所示,氣流控制裝置140例如包含 第一通氣路徑141、與第二通氣路徑142。 The air flow control device 140 is disposed inside the etching bath 110 as shown in FIG. The airflow control device 140 suppresses the gap 131 between the surface of one side of the substrate 500 (in the present embodiment, the back surface 510) and the nozzle 130 from the outside of the substrate carrying port 111 and the substrate carrying port 112 into the etching bath 110 (see FIG. 2). . As shown in FIG. 1, the airflow control device 140 includes, for example, The first ventilation path 141 and the second ventilation path 142.
第一通氣路徑141係於基板搬入口111與噴嘴130之間具有第一通氣口141c。第一通氣口141係如圖4(a)所示,使自基板搬入口111朝向間隙131流入蝕刻槽110內部之外部空氣自第一通氣口141c流入。藉此,第一通氣路徑141抑制自基板搬入口111流入蝕刻槽110內部之外部空氣流入間隙131。 The first ventilation path 141 has a first vent 141c between the substrate carrying inlet 111 and the nozzle 130. As shown in FIG. 4( a ), the first air vent 141 flows in the outside air flowing into the etching groove 110 from the substrate carrying inlet 111 toward the gap 131 from the first air vent 141 c. Thereby, the first air passage 141 suppresses the inflow of the outside air flowing into the inside of the etching bath 110 from the substrate carrying inlet 111 into the gap 131.
如圖1所示,第一通氣路徑141例如於噴嘴130附近依序包含:第一背面板141a、與第一前面板141b。第一背面板141a與第一前面板141b例如隔開50~100mm之間隔設置。第一背面板141a與第一前面板141b係藉由省略圖示之第一側面板連接。第一背面板141a及第一前面板141b之寬度若干長於基板500之寬度。藉由第一背面板141a、第一前面板141b及第一側面板包圍之空間之上部開放,且該開放之上部空間成為第一通氣口141c。 As shown in FIG. 1 , the first ventilation path 141 includes, for example, a first back panel 141 a and a first front panel 141 b in the vicinity of the nozzle 130 . The first back panel 141a and the first front panel 141b are disposed, for example, at intervals of 50 to 100 mm. The first back panel 141a and the first front panel 141b are connected by a first side panel (not shown). The width of the first back panel 141a and the first front panel 141b is somewhat longer than the width of the substrate 500. The upper portion of the space surrounded by the first back panel 141a, the first front panel 141b, and the first side panel is open, and the open upper space becomes the first vent 141c.
如圖3所示,第一背面板141a、第一前面板141b及第一側面板自基板搬入口111觀察,以封塞噴嘴130的前方之方式,自蝕刻槽110之底面設置到接近滾筒121之高度。藉此,第一通氣路徑141作為遮蔽外部空氣自基板搬入口111流入間隙131之遮蔽機構發揮功能。第一前面板141b之高度低於第一背面板141a。藉此,第一通氣路徑141於第一通氣口141c朝向基板搬入口111側開口之寬度方向具有長箱型之形狀。因此,自基板搬入口111流入之外部空氣更容易流入第一通氣口141c。 As shown in FIG. 3, the first back panel 141a, the first front panel 141b, and the first side panel are disposed from the bottom surface of the etching tank 110 to the vicinity of the drum 121 as viewed from the substrate carrying inlet 111. The height. Thereby, the first air passage 141 functions as a shielding mechanism that shields the outside air from flowing into the gap 131 from the substrate loading port 111. The height of the first front panel 141b is lower than that of the first back panel 141a. Thereby, the first air passage 141 has a long box shape in the width direction of the opening of the first air vent 141c toward the substrate carrying inlet 111 side. Therefore, the outside air that has flowed in from the substrate carrying inlet 111 is more likely to flow into the first vent 141c.
如圖1所示,第一背面板141a之上端部例如以進入鄰接之2組滾筒121間之方式而設置。第一背面板141a之上端部係於不干涉藉由搬送裝置120搬送之基板500之範圍,設置於儘可能較高之位置。藉此,可抑制自基板搬入口111流入蝕刻槽110內部之外部空氣流入間隙131。例如,以基板500之背面510與第一背面板141a上端部之距離為1~10 mm之方式設定。第一前面板141b上端部位置例如設定於較第一背面板141a上端部之位置更低50~100mm之位置。 As shown in FIG. 1, the upper end portion of the first back plate 141a is provided, for example, so as to enter between the adjacent two sets of the rollers 121. The upper end portion of the first back surface plate 141a is disposed at a position as high as possible without interfering with the range of the substrate 500 conveyed by the transport device 120. Thereby, it is possible to suppress the outside air flowing into the etching groove 110 from the substrate carrying inlet 111 from flowing into the gap 131. For example, the distance between the back surface 510 of the substrate 500 and the upper end portion of the first back surface plate 141a is 1 to 10 The mode setting of mm. The upper end position of the first front panel 141b is set, for example, at a position 50 to 100 mm lower than the position of the upper end portion of the first back panel 141a.
於設置有第一通氣路徑141之部分之蝕刻槽110之底面,第一排氣口143開口。第一排氣口143係例如於第一通氣路徑141之寬度方向設為縫隙狀,但第一排氣口143之形狀並不限定於此。 The first exhaust port 143 is open at the bottom surface of the etching groove 110 where the first ventilation path 141 is provided. The first exhaust port 143 is, for example, a slit shape in the width direction of the first air passage 141, but the shape of the first exhaust port 143 is not limited thereto.
第二通氣路徑142係於基板搬出口112與噴嘴130之間具有第二通氣口142c。第二通氣路徑142係如圖4(a)所示,使自基板搬出口112朝向間隙131流入蝕刻槽110內部之外部空氣自第二通氣口142c流入。藉此,第二通氣路徑142抑制自基板搬出口112流入蝕刻槽110內部之外部空氣流入間隙131。 The second ventilation path 142 has a second air vent 142c between the substrate carrying port 112 and the nozzle 130. As shown in FIG. 4( a ), the second air passage 142 allows the outside air flowing into the etching tank 110 from the substrate carrying port 112 toward the gap 131 to flow in from the second air vent 142 c. Thereby, the second air passage 142 suppresses the inflow of the outside air flowing into the inside of the etching bath 110 from the substrate carrying port 112 into the gap 131.
如圖1所示,第二通氣路徑142例如於噴嘴130附近依序包含:第二背面板142a、與第二前面板142b。第二背面板142a與第二前面板142b係例如隔開50~100mm之間隔設置。第二背面板142a與第二前面板142b藉由省略圖示之第二側面板連接。第二背面板142a及第二前面板142b之寬度若干長於基板500之寬度。藉由第二背面板142a、第二前面板142b及第二側面板包圍之空間之上部開放,且該開放之上部空間成為第二通氣口142c。 As shown in FIG. 1 , the second ventilation path 142 includes, for example, a second back panel 142 a and a second front panel 142 b in the vicinity of the nozzle 130 . The second back panel 142a and the second front panel 142b are disposed, for example, at intervals of 50 to 100 mm. The second back panel 142a and the second front panel 142b are connected by a second side panel (not shown). The width of the second back panel 142a and the second front panel 142b is somewhat longer than the width of the substrate 500. The upper portion of the space surrounded by the second back panel 142a, the second front panel 142b, and the second side panel is open, and the open upper space becomes the second vent 142c.
與圖3所示者相同,第二背面板142a、第二前面板142b及第二側面板自基板搬出口112觀察,以封塞噴嘴130前方之方式,自蝕刻槽110之底面設置到接近滾筒121之高度。藉此,第二通氣路徑142作為遮蔽外部空氣自基板搬出口112流入間隙131之遮蔽機構發揮功能。第二前面板142b之高度低於第二背面板142a。藉此,第二通氣路徑142於第二通氣口142c朝向基板搬出口112側開口之寬度方向具有長箱型之形狀。因此,自基板搬出口112流入之外部空氣更容易流入第二通氣口142c。 As shown in FIG. 3, the second back panel 142a, the second front panel 142b, and the second side panel are viewed from the substrate carrying opening 112, and are disposed from the bottom surface of the etching groove 110 to the vicinity of the roller so as to block the front of the nozzle 130. The height of 121. Thereby, the second air passage 142 functions as a shielding mechanism that shields the outside air from flowing into the gap 131 from the substrate carrying port 112. The second front panel 142b has a lower height than the second back panel 142a. Thereby, the second air passage 142 has a long box shape in the width direction of the opening of the second air vent 142c toward the substrate carrying port 112 side. Therefore, the outside air that has flowed in from the substrate carrying port 112 is more likely to flow into the second vent 142c.
如圖1所示,第二背面板142a之上端部係例如以進入鄰接之2組滾 筒121間之方式而設置。第二背面板142a之上端部係於不干涉藉由搬送裝置120搬送之基板500之範圍,設置於儘可能較高之位置。藉此,可抑制自基板搬出口112流入蝕刻槽110內部之外部空氣流入間隙131。例如,以基板500之背面510與第二背面板142a上端部之距離成為1~10mm之方式設定。第二前面板142b上端部位置例如設定於較第二背面板142a上端部之位置更低50~100mm之位置。 As shown in FIG. 1, the upper end portion of the second back panel 142a is, for example, a group of two adjacent rollers. It is provided in the manner of the tube 121. The upper end portion of the second back plate 142a is disposed at a position as high as possible without interfering with the range of the substrate 500 conveyed by the transfer device 120. Thereby, it is possible to suppress the outside air flowing into the etching groove 110 from the substrate carrying port 112 from flowing into the gap 131. For example, the distance between the back surface 510 of the substrate 500 and the upper end portion of the second back surface plate 142a is set to be 1 to 10 mm. The upper end position of the second front panel 142b is set, for example, at a position 50 to 100 mm lower than the position of the upper end portion of the second back panel 142a.
於設置有第二通氣路徑142之部分之蝕刻槽110之底面,第二排氣口144開口。第二排氣口144係例如於第二通氣路徑142之寬度方向設為縫隙狀,但第二排氣口144之形狀並不限定於此。 The second exhaust port 144 is open at the bottom surface of the etching groove 110 where the second ventilation path 142 is provided. The second exhaust port 144 is, for example, a slit shape in the width direction of the second air passage 142, but the shape of the second exhaust port 144 is not limited thereto.
第一通氣路徑141與第二通氣路徑142係如圖1所示,例如,於蝕刻槽110之外部,藉由連接路徑150而連接。連接路徑150係經由設置於第一通氣路徑141底部之第一排氣口143、及設置於第二通氣路徑142底部之第二排氣口144,貫通第一通氣路徑141之內部空間及第二通氣路徑142之內部空間。 The first ventilation path 141 and the second ventilation path 142 are connected as shown in FIG. 1 , for example, outside the etching groove 110 by a connection path 150 . The connecting path 150 penetrates the internal space of the first ventilation path 141 and the second through the first exhaust port 143 disposed at the bottom of the first ventilation path 141 and the second exhaust port 144 disposed at the bottom of the second ventilation path 142. The internal space of the ventilation path 142.
第一通氣路徑141、連接路徑150及第二通氣路徑142形成用以使朝向間隙131之外部空氣迂迴之迂迴路徑。自基板搬入口111或基板搬出口112流入蝕刻槽110內部之外部空氣通過該迂迴路徑而於基板搬出口112側或基板搬入口111側流出。因此,抑制流入蝕刻槽110內部之外部空氣直接流入間隙131。 The first ventilation path 141, the connection path 150, and the second ventilation path 142 form a bypass path for bypassing the outside air toward the gap 131. The outside air that has flowed into the inside of the etching bath 110 from the substrate loading port 111 or the substrate carrying port 112 flows out through the bypass path on the substrate carrying port 112 side or the substrate carrying port 111 side. Therefore, the outside air flowing into the inside of the etching bath 110 is prevented from flowing directly into the gap 131.
於連接路徑150,連接有抽吸裝置160。抽吸裝置160包含一般之抽吸機構,例如旋轉泵。藉由使抽吸裝置160運作,可排放連接路徑150之內部氣體,進而可排放第一通氣路徑141及第二通氣路徑142內部之氣體。不需要使抽吸裝置160不斷運作,於流入蝕刻槽110之外部空氣較多之情形等時,根據需要使其運作即可。 A suction device 160 is connected to the connection path 150. Suction device 160 includes a general suction mechanism, such as a rotary pump. By operating the suction device 160, the internal gas of the connection path 150 can be discharged, and the gases inside the first ventilation path 141 and the second ventilation path 142 can be discharged. It is not necessary to continuously operate the suction device 160, and when the outside air flowing into the etching bath 110 is large, it is necessary to operate it as needed.
以下,使用圖5,說明包含蝕刻裝置100之基板製造系統1000之構成。圖5係顯示基板製造系統1000之一部分之側視圖。於圖5中,符 號1030對應於圖1所示之蝕刻槽110。於圖5中,於構成蝕刻槽1030之各構成要素之符號旁一併記載圖1所示之符號。 Hereinafter, the configuration of the substrate manufacturing system 1000 including the etching apparatus 100 will be described with reference to FIG. 5. FIG. 5 is a side view showing a portion of the substrate manufacturing system 1000. In Figure 5, the symbol No. 1030 corresponds to the etching bath 110 shown in FIG. In FIG. 5, the symbols shown in FIG. 1 are collectively indicated by the symbols constituting the constituent elements of the etching bath 1030.
基板製造系統1000包含第一清洗槽1010、第一緩衝槽1020、蝕刻槽1030、第二緩衝槽1040、第二清洗槽1050及搬送裝置1070。 The substrate manufacturing system 1000 includes a first cleaning tank 1010, a first buffer tank 1020, an etching tank 1030, a second buffer tank 1040, a second cleaning tank 1050, and a conveying device 1070.
搬送裝置1070係自圖示左側向圖示右側搬送基板500。搬送裝置1070係例如由複數個滾筒1071構成之滾筒運送機。藉由複數個滾筒1071,形成如下之搬送路徑:自第一清洗槽1010之上游側依序通過第一清洗槽1010、第一緩衝槽1020、蝕刻槽1030、第二緩衝槽1040、及第二清洗槽1050,送往第二清洗槽1050之下游側。 The conveying device 1070 conveys the substrate 500 from the left side of the drawing to the right side of the drawing. The conveying device 1070 is, for example, a drum conveyor composed of a plurality of rollers 1071. The plurality of rollers 1071 form a transport path that sequentially passes through the first cleaning tank 1010, the first buffer tank 1020, the etching tank 1030, the second buffer tank 1040, and the second from the upstream side of the first cleaning tank 1010. The cleaning tank 1050 is sent to the downstream side of the second cleaning tank 1050.
省略圖示,但於第一清洗槽1010之上游側,例如設置進行基板500之成形或研磨之裝置。於第二清洗槽1050之下游側,例如設置進行基板500之乾燥或檢查之裝置。 Although not shown in the drawings, on the upstream side of the first cleaning tank 1010, for example, a device for forming or polishing the substrate 500 is provided. On the downstream side of the second cleaning tank 1050, for example, means for performing drying or inspection of the substrate 500 is provided.
第一清洗槽1010、第一緩衝槽1020、第二緩衝槽1040、及第二清洗槽1050各自包含基板搬入口及基板搬出口。各槽之基板搬入口及基板搬出口係設為與蝕刻槽1030之基板搬入口1031及基板搬出口1032相同高度、相同大小。各槽之基板搬出口依序連接於與搬送方向下游側鄰接之槽之基板搬入口。 The first cleaning tank 1010, the first buffer tank 1020, the second buffer tank 1040, and the second cleaning tank 1050 each include a substrate transfer port and a substrate transfer port. The substrate transfer port and the substrate transfer port of each groove are the same height and the same size as the substrate transfer port 1031 and the substrate transfer port 1032 of the etching bath 1030. The substrate transfer ports of the respective grooves are sequentially connected to the substrate transfer inlets of the grooves adjacent to the downstream side in the transfer direction.
以下,使用圖5,說明基板500之製造過程。 Hereinafter, the manufacturing process of the substrate 500 will be described using FIG.
基板500例如藉由浮式法成形為帶狀後,經過切斷為所期望尺寸之基板500之切斷工序、將基板500之端面倒角之倒角工序、及研磨基板500表面(正面520)之研磨工序,而被搬送至第一清洗槽1010。作為研磨方法,例如使用將漿料供給至基板進行研磨之方法。漿料係使研磨顆粒分散於水或有機溶媒之液體而成之分散液。作為研磨顆粒,例如使用氧化鈰。 After the substrate 500 is formed into a strip shape by a floating method, for example, a cutting step of cutting the substrate 500 to a desired size, a chamfering step of chamfering the end surface of the substrate 500, and a surface of the polishing substrate 500 (front surface 520) The polishing process is carried to the first cleaning tank 1010. As the polishing method, for example, a method of supplying a slurry to a substrate for polishing is used. The slurry is a dispersion in which abrasive particles are dispersed in a liquid of water or an organic solvent. As the abrasive particles, for example, cerium oxide is used.
經研磨之基板500係藉由搬送裝置1070搬送至第一清洗槽1010。於第一清洗槽1010中,自基板500之表面去除研磨顆粒。於第一清洗 槽1010中,例如,首先沖淋洗淨基板500,以水沖去基板500表面之研磨顆粒。其後,以漿料洗淨基板500。漿料洗淨係將洗淨用之漿料自噴嘴吹送至基板並使用圓板刷等洗淨機構,去除沖淋清洗所無法去除之研磨顆粒之清洗方法。作為清洗用漿料,例如使用使氧化鈰、碳酸鈣、或碳酸鎂分散於有機溶媒之液體而成之分散液。 The polished substrate 500 is transferred to the first cleaning tank 1010 by the conveying device 1070. In the first cleaning bath 1010, abrasive particles are removed from the surface of the substrate 500. For the first cleaning In the tank 1010, for example, the substrate 500 is first washed by washing, and the abrasive particles on the surface of the substrate 500 are washed away with water. Thereafter, the substrate 500 is washed with a slurry. In the slurry cleaning, the cleaning slurry is blown from the nozzle to the substrate, and a cleaning mechanism such as a circular brush is used to remove the cleaning method of the abrasive particles that cannot be removed by the shower cleaning. As the cleaning slurry, for example, a dispersion obtained by dispersing cerium oxide, calcium carbonate, or magnesium carbonate in a liquid of an organic solvent is used.
基板500藉由搬送裝置1070自第一清洗槽1010被搬出,且被搬入至第一緩衝槽1020。第一緩衝槽1020係為了防止反應氣體自基板搬入口1031洩漏至第一清洗槽1010而設置。藉此,於第一清洗槽1010中進行之清洗步驟不會被反應氣體污染。 The substrate 500 is carried out from the first cleaning tank 1010 by the conveying device 1070, and is carried into the first buffer tank 1020. The first buffer tank 1020 is provided to prevent the reaction gas from leaking from the substrate carrying inlet 1031 to the first cleaning tank 1010. Thereby, the cleaning step performed in the first cleaning tank 1010 is not contaminated by the reaction gas.
第一緩衝槽1020例如於頂板具有風扇過濾單元FFU1,於底板具有排氣口EXH1。風扇過濾單元FFU1將外部空氣過濾並導入至第一緩衝槽1020內部,將第一緩衝槽1020內部設為正壓狀態。以風扇過濾單元FFU1導入之外部空氣與第一緩衝槽1020內部之灰塵或氣體一起,自排氣口EXH1排出至壓力相對較低之第一緩衝槽1020之外部。 The first buffer tank 1020 has, for example, a fan filter unit FFU1 on the top plate and an exhaust port EXH1 on the bottom plate. The fan filter unit FFU1 filters the outside air and introduces it into the inside of the first buffer tank 1020, and sets the inside of the first buffer tank 1020 to a positive pressure state. The outside air introduced by the fan filter unit FFU1 is discharged from the exhaust port EXH1 to the outside of the first buffer tank 1020 having a relatively low pressure together with the dust or gas inside the first buffer tank 1020.
基板500係藉由搬送裝置1070自第一緩衝槽1020搬出,並被搬入至蝕刻槽1030。於蝕刻槽1030中,對基板500之背面510,自噴嘴1080(圖1之130)吹送反應氣體,將基板500之背面510粗面化。 The substrate 500 is carried out from the first buffer tank 1020 by the transport device 1070, and is carried into the etching bath 1030. In the etching bath 1030, the reaction gas is blown from the nozzle 1080 (130 in FIG. 1) on the back surface 510 of the substrate 500, and the back surface 510 of the substrate 500 is roughened.
經粗面化之基板500藉由搬送裝置1070自蝕刻槽1030搬出,並被搬入至第二緩衝槽1040。第二緩衝槽1040係為了防止反應氣體自基板搬出口1032洩漏至第二清洗槽1050而設置。藉此,於第二清洗槽1050中進行之清洗步驟不會被反應氣體污染。 The roughened substrate 500 is carried out from the etching bath 1030 by the transfer device 1070, and is carried into the second buffer tank 1040. The second buffer tank 1040 is provided to prevent the reaction gas from leaking from the substrate discharge port 1032 to the second cleaning tank 1050. Thereby, the washing step performed in the second washing tank 1050 is not contaminated by the reaction gas.
第二緩衝槽1040例如於頂板具有風扇過濾單元FFU2,於底板具有排氣口EXH2。風扇過濾單元FFU2將外部空氣過濾並導入至第二緩衝槽1040內部,將第二緩衝槽1040內部設為正壓狀態。以風扇過濾單元FFU2導入之外部空氣與第二緩衝槽1040內部之灰塵或氣體一起,自排氣口EXH2排出至壓力相對較低之第一緩衝槽1020之外部。 The second buffer tank 1040 has, for example, a fan filter unit FFU2 on the top plate and an exhaust port EXH2 on the bottom plate. The fan filter unit FFU2 filters the outside air and introduces it into the inside of the second buffer tank 1040, and sets the inside of the second buffer tank 1040 to a positive pressure state. The outside air introduced by the fan filter unit FFU2 is discharged from the exhaust port EXH2 to the outside of the first buffer tank 1020 having a relatively low pressure together with the dust or gas inside the second buffer tank 1040.
基板500係藉由搬送裝置1070自第二緩衝槽1040搬出,並被搬入至第二清洗槽1050。第二清洗槽1050包含高壓沖淋1051。於第二清洗槽1050中,洗淨基板500之兩面,去除藉由粗面化產生之玻璃屑或蝕刻衍生生成物等。清洗方法無特別限定,例如,例舉高壓沖淋清洗、刷洗、超音波清洗、或組合其等者等。洗淨後之基板500係藉由搬送裝置1070自第二清洗槽1050搬出,供於乾燥工序或檢測工序。 The substrate 500 is carried out from the second buffer tank 1040 by the transport device 1070, and is carried into the second cleaning tank 1050. The second cleaning tank 1050 includes a high pressure shower 1051. In the second cleaning bath 1050, both surfaces of the substrate 500 are cleaned, and glass swarf generated by roughening, etching-derived products, and the like are removed. The cleaning method is not particularly limited, and examples thereof include high pressure shower cleaning, brushing, ultrasonic cleaning, or the like. The cleaned substrate 500 is carried out from the second cleaning tank 1050 by the conveying device 1070, and is supplied to a drying step or a detecting step.
以下,使用圖4至圖6,說明氣流控制裝置140之功能。圖6係顯示蝕刻槽1030不包含氣流控制裝置140時之噴嘴1080周邊氣體變動分佈之圖。 Hereinafter, the function of the airflow control device 140 will be described using Figs. 4 to 6 . FIG. 6 is a view showing a distribution of gas fluctuations around the nozzle 1080 when the etching bath 1030 does not include the air flow control device 140.
如圖4(a)所示,藉由自噴嘴130吹出之反應氣體,將基板500之背面510粗面化。基板500之背面510內各部位之粗度係藉由其部位所暴露之反應氣體之濃度、及其部位暴露於反應氣體之累積時間這2個要因而決定。該等要因會因基板500與噴嘴130間之間隙131所產生之氣流干擾而大幅變動。氣流干擾係因經由基板搬入口111及基板搬出口112流入蝕刻槽110內部之外部空氣所引起。 As shown in FIG. 4(a), the back surface 510 of the substrate 500 is roughened by the reaction gas blown from the nozzle 130. The thickness of each portion in the back surface 510 of the substrate 500 is determined by the concentration of the reaction gas exposed at the portion thereof and the cumulative time at which the portion is exposed to the reaction gas. These factors greatly vary due to airflow disturbances generated by the gap 131 between the substrate 500 and the nozzles 130. The airflow disturbance is caused by the outside air flowing into the inside of the etching bath 110 through the substrate carrying port 111 and the substrate carrying port 112.
外部空氣之流入是由圖5所示之第一緩衝槽1020與第二緩衝槽1040之間產生壓力差所引起。由發明者之探討可明確,尤其是當基板500之尺寸大到跨及複數個槽之長度之情形時,該壓力差顯著產生。又,由發明者之探討亦可明確,外部空氣之流入程度會隨著基板500之搬送而產生時間變動。 The inflow of the outside air is caused by a pressure difference between the first buffer tank 1020 and the second buffer tank 1040 shown in FIG. As will be apparent from the inventors' investigation, especially when the size of the substrate 500 is large enough to span the length of a plurality of grooves, the pressure difference is remarkably generated. Moreover, it has been clarified by the inventors that the degree of inflow of outside air varies with time due to the conveyance of the substrate 500.
第一緩衝槽1020與第二緩衝槽1040之間產生壓力差之原因認為有各種。例如,在第一清洗槽1010與第二清洗槽1050中作動之裝置不同,是為可能的原因之一。 The reason why a pressure difference is generated between the first buffer tank 1020 and the second buffer tank 1040 is considered to be various. For example, the difference between the first cleaning tank 1010 and the second cleaning tank 1050 is one of the possible causes.
於第一清洗槽1010中,於搬出基板500之前,例如進行沖淋清洗及漿料清洗。然而,即使該等裝置作動,第一清洗槽1010內部全域之氣壓分佈並不會產生較大變動。另一方面,當將基板500搬入第二清 洗槽1050時,藉由高壓沖淋1051進行高壓沖淋清洗。當高壓沖淋1051作動時,第二清洗槽1050內部全域之氣體分佈產生較大變動。其變動會經由第二清洗槽1050之基板搬入口,使鄰接之第二緩衝槽1040內部之壓力變動。尤其於基板500之尺寸較大之情形時,會產生基板500自蝕刻槽1030橫跨至第二清洗槽1050之狀態。於該情形時,於基板500之一部分於蝕刻槽1030中經粗面化之期間,基板500之另外部分於第二清洗槽1050中經實施高壓沖淋,因此,於粗面化之期間產生壓力變動,而產生外部空氣之流入。此種狀況係於基板500之搬送方向中,基板500之長度為自噴嘴1080吹出口至第二清洗槽1050之基板搬入口為止之長度的情形時產生。 In the first cleaning tank 1010, for example, shower cleaning and slurry cleaning are performed before the substrate 500 is carried out. However, even if the devices are activated, the air pressure distribution throughout the first cleaning tank 1010 does not vary greatly. On the other hand, when the substrate 500 is moved into the second clear When the tank 1050 is washed, high pressure shower cleaning is performed by the high pressure shower 1051. When the high pressure shower 1051 is actuated, the gas distribution in the entire interior of the second cleaning tank 1050 is greatly changed. The fluctuation is changed by the substrate inlet of the second cleaning tank 1050, and the pressure inside the adjacent second buffer tank 1040 is varied. Particularly in the case where the size of the substrate 500 is large, a state in which the substrate 500 straddles from the etching groove 1030 to the second cleaning bath 1050 is generated. In this case, during the roughening of one portion of the substrate 500 in the etching bath 1030, another portion of the substrate 500 is subjected to high pressure showering in the second cleaning bath 1050, thereby generating pressure during roughening. Change, and the inflow of outside air. Such a situation occurs when the length of the substrate 500 is the length from the nozzle 1080 to the substrate transfer inlet of the second cleaning tank 1050 in the transport direction of the substrate 500.
於第一緩衝槽1020與第二緩衝槽1040之間產生壓力差,亦可考量其他原因。 A pressure difference is generated between the first buffer tank 1020 and the second buffer tank 1040, and other reasons may also be considered.
例如,如圖6所示,於基板500之尺寸較大之情形時,根據基板500與蝕刻槽1030之相對位置,第一緩衝槽1020與第二緩衝槽1040之氣壓產生差異。結果,於蝕刻槽1030內部產生壓力分佈,並於噴嘴1080前後產生氣流。所謂尺寸較大之基板500係指於基板500之搬送方向上,自噴嘴1080之吹出口132a至第一緩衝槽1020之基板搬入口之長度以上,或,自噴嘴1080之吹出口132a至第二緩衝槽1040之基板搬出口之長度以上之基板。 For example, as shown in FIG. 6, when the size of the substrate 500 is large, the air pressure of the first buffer tank 1020 and the second buffer tank 1040 differs depending on the relative positions of the substrate 500 and the etching bath 1030. As a result, a pressure distribution is generated inside the etching bath 1030, and an air flow is generated before and after the nozzle 1080. The substrate 500 having a large size refers to a length from the air outlet 132a of the nozzle 1080 to the substrate loading port of the first buffer tank 1020 in the transport direction of the substrate 500, or from the air outlet 132a to the second of the nozzle 1080. The substrate of the buffer tank 1040 has a length greater than or equal to the length of the substrate.
例如,如圖6(a)所示,當基板500之前端部達到噴嘴1080附近時,第一緩衝槽1020係藉由基板500被分斷為上下之空間。此時,藉由風扇過濾單元FFU1導入外部空氣,第一緩衝槽1020之上側空間成為正壓。由於導入之外部空氣由基板500遮斷,故第一緩衝槽1020之下側空間係相對成為負壓。另一方面,第二緩衝槽1040藉由風扇過濾單元FFU2導入外部空氣,整個空間均成為正壓。蝕刻槽1030係由基板500劃分基板搬入口1031與噴嘴1080間之空間。由於基板500之下側 空間經由第一緩衝槽1020之下側空間而與基板搬入口1031相連,故為負壓。另一方面,由於噴嘴1080與基板搬出口1032間之空間經由第二緩衝槽1040之整個空間而與基板搬出口1032相連,故成為正壓。結果,於蝕刻槽1030之內部,產生自基板搬出口1032朝向基板搬入口1031之氣流。 For example, as shown in FIG. 6(a), when the front end portion of the substrate 500 reaches the vicinity of the nozzle 1080, the first buffer tank 1020 is divided into upper and lower spaces by the substrate 500. At this time, the outside air is introduced by the fan filter unit FFU1, and the space above the first buffer tank 1020 becomes a positive pressure. Since the introduced outside air is blocked by the substrate 500, the space on the lower side of the first buffer tank 1020 becomes a negative pressure. On the other hand, the second buffer tank 1040 introduces outside air through the fan filter unit FFU2, and the entire space becomes a positive pressure. The etching bath 1030 divides a space between the substrate carrying inlet 1031 and the nozzle 1080 by the substrate 500. Due to the underside of the substrate 500 The space is connected to the substrate transfer inlet 1031 via the space below the first buffer tank 1020, and thus is a negative pressure. On the other hand, since the space between the nozzle 1080 and the substrate transfer port 1032 is connected to the substrate transfer port 1032 via the entire space of the second buffer tank 1040, it becomes a positive pressure. As a result, inside the etching bath 1030, a gas flow from the substrate carrying port 1032 toward the substrate carrying port 1031 is generated.
如圖6(c)所示,當基板500之後端部被搬送到噴嘴1080附近時,由於第一緩衝槽1020中不存在基板500,故藉由風扇過濾單元FFU1導入外部空氣,第一緩衝槽1020之整個空間成為正壓。另一方面,第二緩衝槽1040係藉由基板500被分斷為上下之空間。此時,藉由風扇過濾單元FFU2導入外部空氣,第二緩衝槽1040之上側空間成為正壓。由於導入之外部空氣係藉由基板500被遮斷,故第二緩衝槽1040下側之空間相對成為負壓。蝕刻槽1030係以基板500劃分噴嘴1080與基板搬出口1032間之空間。由於基板500之下側空間經由第二緩衝槽1040之下側空間而與基板搬出口1032相連,故成為負壓。另一方面,由於噴嘴1080與基板搬如口1031間之空間經由第一緩衝槽1020之整個空間而與基板搬入口1031相連,故成為正壓。結果,於蝕刻槽1030之內部,產生自基板搬入口1031朝向基板搬出口1032之氣流。 As shown in FIG. 6(c), when the rear end portion of the substrate 500 is transported to the vicinity of the nozzle 1080, since the substrate 500 does not exist in the first buffer tank 1020, the outside air is introduced through the fan filter unit FFU1, and the first buffer tank is introduced. The entire space of 1020 becomes positive pressure. On the other hand, the second buffer tank 1040 is divided into upper and lower spaces by the substrate 500. At this time, the outside air is introduced by the fan filter unit FFU2, and the space above the second buffer tank 1040 becomes a positive pressure. Since the introduced outside air is blocked by the substrate 500, the space on the lower side of the second buffer tank 1040 becomes a negative pressure. The etching bath 1030 partitions the space between the nozzle 1080 and the substrate carrying port 1032 by the substrate 500. Since the space on the lower side of the substrate 500 is connected to the substrate carry-out port 1032 via the space on the lower side of the second buffer tank 1040, it becomes a negative pressure. On the other hand, since the space between the nozzle 1080 and the substrate transfer opening 1031 is connected to the substrate transfer inlet 1031 through the entire space of the first buffer tank 1020, it becomes a positive pressure. As a result, an air flow from the substrate carrying inlet 1031 toward the substrate carrying port 1032 is generated inside the etching bath 1030.
另,如圖6(b)所示,於將基板500自基板搬入口1031搬送至基板搬出口1032之中途階段,根據基板500是否分斷第一緩衝槽1020及第二緩衝槽1040之空間,實現各種氣壓分佈。 Further, as shown in FIG. 6(b), in the middle of transporting the substrate 500 from the substrate loading port 1031 to the substrate carrying port 1032, depending on whether or not the substrate 500 separates the spaces of the first buffer tank 1020 and the second buffer tank 1040, Achieve various pressure distributions.
如以上說明般,尤其於使用較大尺寸之基板之情形時,根據基板500與蝕刻槽1030之相對位置,於蝕刻槽1030內之噴嘴1080之前後會產生不同之壓力分佈。由於通過基板搬入口1031及基板搬出口1032,順次連續地搬送複數個基板500,故噴嘴1080前後之壓力差會隨著時間而變動。 As described above, particularly in the case of using a substrate of a larger size, depending on the relative position of the substrate 500 and the etching groove 1030, a different pressure distribution is generated before and after the nozzle 1080 in the etching groove 1030. Since the plurality of substrates 500 are sequentially and continuously transported through the substrate transfer port 1031 and the substrate transfer port 1032, the pressure difference between the nozzles 1080 and the like changes with time.
如圖4(b)所示,於蝕刻槽110內不設置氣流控制裝置140之情形 時,自基板搬入口111及基板搬出口112流入之外部空氣幾乎不被遮擋,而到達基板500之背面510與噴嘴130間之間隙131。因此,充滿於間隙131之反應氣體之濃度分佈直接受到氣流干擾之影響。結果,基板500之背面510之粗度產生不均一性。 As shown in FIG. 4(b), the airflow control device 140 is not disposed in the etching bath 110. At the time, the outside air that has flowed in from the substrate carrying inlet 111 and the substrate carrying opening 112 is hardly blocked, and reaches the gap 131 between the back surface 510 of the substrate 500 and the nozzle 130. Therefore, the concentration distribution of the reaction gas filled in the gap 131 is directly affected by the disturbance of the gas flow. As a result, the thickness of the back surface 510 of the substrate 500 produces unevenness.
另一方面,如圖4(a)所示,於蝕刻槽110內設置有氣流控制裝置140之情形時,自基板搬入口111及基板搬出口112流入之外部空氣,流入藉由第一通氣路徑141、連接路徑150及第二通氣路徑142形成之迂迴路徑,而抑制其直接到達間隙131。又,由於藉由連接路徑150,將第一通氣路徑141與第二通氣路徑142內部之壓力設為始終等壓,故亦緩和第一緩衝槽1020與第二緩衝槽1040間之壓力差之時間變動帶來之影響。藉此,充滿於間隙131之反應氣體之濃度分佈難以受氣流干擾之影響,因而提高基板500之背面510之粗度均一性。 On the other hand, as shown in FIG. 4(a), when the airflow control device 140 is provided in the etching bath 110, the outside air that has flowed in from the substrate carrying inlet 111 and the substrate carrying port 112 flows into the first ventilation path. 141. The bypass path formed by the connection path 150 and the second ventilation path 142 is prevented from directly reaching the gap 131. Moreover, since the pressure inside the first ventilation path 141 and the second ventilation path 142 is always equal pressure by the connection path 150, the time difference between the first buffer tank 1020 and the second buffer tank 1040 is also moderated. The impact of changes. Thereby, the concentration distribution of the reaction gas filled in the gap 131 is hardly affected by the airflow interference, thereby increasing the roughness uniformity of the back surface 510 of the substrate 500.
又,於使抽吸裝置160運作之情形時,連接路徑150之內壓長時間維持在負壓(例如-1~-2 Pa)。藉此,即使於第一緩衝槽1020與第二緩衝槽1040間產生壓力差(例如最大±3 Pa左右),外部空氣之流動幾乎發生於基板搬入口111與第一通氣口141c之間、及基板搬出口112與第二通氣口142c之間。因此,於基板500之背面510與噴嘴130間之間隙131中,外部空氣流入之影響降低。另,由於第一通氣口141c與第二通氣口142c朝向與噴嘴130相反之側開口,故藉由使抽吸裝置160運作,間隙131之氣流不會受到大幅干擾。 Further, when the suction device 160 is operated, the internal pressure of the connection path 150 is maintained at a negative pressure for a long time (for example, -1 to -2 Pa). Thereby, even if a pressure difference (for example, a maximum of ±3 Pa) occurs between the first buffer tank 1020 and the second buffer tank 1040, the flow of the outside air occurs almost between the substrate carrying port 111 and the first vent 141c, and Between the substrate carrying outlet 112 and the second vent 142c. Therefore, in the gap 131 between the back surface 510 of the substrate 500 and the nozzle 130, the influence of the inflow of the outside air is lowered. Further, since the first vent 141c and the second vent 142c are opened toward the side opposite to the nozzle 130, the airflow of the gap 131 is not greatly disturbed by operating the suction device 160.
如以上說明般,於本實施形態之蝕刻裝置中,如圖4(a)所示,自具有基板搬入口111及基板搬出口112之蝕刻槽110之基板搬入口111朝向基板搬出口112搬送基板500,並自噴嘴130將反應氣體吹送至基板500之背面510。反應氣體之吹送係一面抑制自基板搬入口111及基板搬出口112流入蝕刻槽110內部之外部空氣流入基板500之背面510與噴嘴130間之間隙131、一面進行。 As described above, in the etching apparatus of the present embodiment, as shown in FIG. 4(a), the substrate transfer port 111 having the etching groove 110 having the substrate transfer port 111 and the substrate transfer port 112 is transferred to the substrate transfer port 112. 500, and the reaction gas is blown from the nozzle 130 to the back surface 510 of the substrate 500. The blowing system of the reaction gas is prevented from flowing into the gap 131 between the back surface 510 of the substrate 500 and the nozzle 130 from the substrate carrying port 111 and the substrate carrying port 112 into the gap 131 between the back surface 510 of the substrate 500 and the nozzle 130.
例如,為了抑制自基板搬入口111流入蝕刻槽110內部之外部空氣流入間隙131,如圖4(a)所示,使自基板搬入口111朝向間隙131流入蝕刻槽110內部之外部空氣,自設置於基板搬入口111與噴嘴130間之第一通氣口141c流入第一通氣路徑141。 For example, in order to prevent the outside air flowing into the etching groove 110 from the substrate carrying inlet 111 from flowing into the gap 131, as shown in FIG. 4(a), the outside air flowing into the etching groove 110 from the substrate carrying port 111 toward the gap 131 is set. The first vent 141c between the substrate carrying inlet 111 and the nozzle 130 flows into the first air passage 141.
為了抑制自基板搬出口112流入蝕刻槽110內部之外部空氣流入間隙131,如圖4(a)所示,使自基板搬出口112朝向間隙131流入蝕刻槽110內部之外部空氣,自設置於基板搬出口112與噴嘴130間之第二通氣口142c流入第二通氣路徑142。 In order to prevent the outside air flowing into the etching groove 110 from the substrate carrying port 112 from flowing into the gap 131, as shown in FIG. 4(a), the outside air flowing into the etching groove 110 from the substrate carrying port 112 toward the gap 131 is provided on the substrate. The second vent 142c between the outlet 112 and the nozzle 130 flows into the second ventilation path 142.
因此,可抑制隨著外部空氣流入蝕刻槽110內部而產生之基板500之背面510上之粗度不均一性。 Therefore, it is possible to suppress the thickness unevenness on the back surface 510 of the substrate 500 which occurs as the outside air flows into the inside of the etching bath 110.
以上,參照圖式說明本發明之較佳實施形態例,但本發明自當不限定於上述之例。上述之例中所示之各構成構件之諸形狀或組合等乃一例,於不脫離本發明主旨之範圍內可基於設計要求等進行各種變更。 The preferred embodiments of the present invention have been described above with reference to the drawings, but the present invention is not limited to the above examples. The shapes and combinations of the constituent members shown in the above examples are merely examples, and various modifications can be made based on design requirements and the like without departing from the spirit of the invention.
例如,於上述實施形態中,第一通氣路徑141與第二通氣路徑142連接於共通之抽吸裝置160,但亦可將第一通氣路徑141與第二通氣路徑142分別連接於不同之抽吸裝置。於該情形時,各自獨立地排放自基板搬入口111流入蝕刻槽110內部之外部空氣、與自基板搬出口112流入蝕刻槽110內部之外部空氣。即使於該情形時,亦可抑制流入蝕刻槽110內部之外部空氣流入基板500之背面510與噴嘴130間之間隙131。結果,可抑制基板500之背面510中之粗度不均一性。 For example, in the above embodiment, the first ventilation path 141 and the second ventilation path 142 are connected to the common suction device 160, but the first ventilation path 141 and the second ventilation path 142 may be respectively connected to different suctions. Device. In this case, the outside air that has flowed into the inside of the etching bath 110 from the substrate carrying inlet 111 and the outside air that has flowed into the inside of the etching bath 110 from the substrate carrying port 112 are independently discharged. Even in this case, the outside air flowing into the inside of the etching bath 110 can be prevented from flowing into the gap 131 between the back surface 510 of the substrate 500 and the nozzle 130. As a result, the thickness unevenness in the back surface 510 of the substrate 500 can be suppressed.
又,於本發明一態樣之基板之製造方法中,藉由浮式法或熔融法成形為帶狀後,包含:切斷為所期望尺寸之基板500之切斷工序;將基板500端面倒角之倒角工序;及對經過研磨基板500之表面(正面520)之研磨工序之基板500,藉由上述實施形態中說明之蝕刻方法蝕刻背面510之工序。結果,可獲得抑制背面510中之粗度不均一性之基 板500。 Further, in the method for producing a substrate according to an aspect of the present invention, after forming into a strip shape by a float method or a melt method, the method includes: a cutting step of cutting the substrate 500 to a desired size; and pouring the end surface of the substrate 500 The corner chamfering step and the step of etching the back surface 510 by the etching method described in the above embodiment on the substrate 500 subjected to the polishing step of the surface (front surface 520) of the substrate 500. As a result, a basis for suppressing the thickness unevenness in the back surface 510 can be obtained. Board 500.
又,於本發明一實施形態之基板中,背面510整體之算術平均表面粗度之平均值係0.3~1.5nm,且背面510之周緣部之算術平均表面粗度之平均值,與背面510之中央部之算術平均表面粗度不同,背面510整體之算術平均表面粗度之標準偏差為0.06nm以下。 Further, in the substrate according to the embodiment of the present invention, the average value of the arithmetic mean surface roughness of the entire back surface 510 is 0.3 to 1.5 nm, and the average of the arithmetic mean surface roughness of the peripheral portion of the back surface 510 is opposite to the back surface 510. The arithmetic mean surface roughness of the central portion is different, and the standard deviation of the arithmetic mean surface roughness of the entire back surface 510 is 0.06 nm or less.
於將基板500劃分為縱橫各3個之9個區域時,將其中央區域設為中央部,將其以外之中央部周圍之區域設為周緣部。周緣部係處於與邊端相距500mm之範圍之區域。所謂周緣部之算術平均表面粗度之平均值,係除了中央部以外之8個區域之算術平均表面粗度之平均值。中央部與周緣部之算術平均表面粗度不相同,但藉由將背面510整體之算術平均表面粗度之偏差設為以標準偏差表示為0.06以下,可有效地抑制剝離帶電量,可抑制因剝離帶電引起之基板損傷。另,中央部之算術平均表面粗度可高於周緣部之算術平均表面粗度。 When the substrate 500 is divided into nine regions of three vertical and horizontal directions, the central portion thereof is defined as a central portion, and the region around the central portion other than the central portion is referred to as a peripheral portion. The peripheral portion is in the region of 500 mm from the edge. The average value of the arithmetic mean surface roughness of the peripheral portion is the average of the arithmetic mean surface roughness of the eight regions except the central portion. The arithmetic mean surface roughness of the central portion and the peripheral portion is not the same, but the deviation of the arithmetic mean surface roughness of the entire back surface 510 is represented by a standard deviation of 0.06 or less, thereby effectively suppressing the peeling charge amount and suppressing the cause Stripping damage caused by charging. Further, the arithmetic mean surface roughness of the central portion may be higher than the arithmetic mean surface roughness of the peripheral portion.
另,基板尺寸越大,藉由一定時間載置於真空抽吸平台時之剝離帶電引起基板損傷之可能性越提高。因此,於本發明一實施形態之基板中,由於基板尺寸為1500mm×1500mm以上則具有抑制剝離帶電量之效果,故較佳。此外,若基板尺寸為2000mm×2000mm以上則效果更佳。 In addition, the larger the size of the substrate, the more the possibility of damage to the substrate caused by the peeling electrification when placed on the vacuum suction platform for a certain period of time. Therefore, in the substrate according to the embodiment of the present invention, since the substrate size is 1500 mm × 1500 mm or more, the effect of suppressing the peeling charge amount is preferable, which is preferable. Further, if the substrate size is 2000 mm × 2000 mm or more, the effect is further improved.
又,若自背面510中央部之算術平均表面粗度減去背面510整體之算術平均表面粗度之平均值時之值為-0.13以上0.13以下,則可更有效地抑制剝離帶電量。 In addition, when the value of the arithmetic mean surface roughness of the center portion of the back surface 510 minus the average value of the arithmetic mean surface roughness of the entire back surface 510 is -0.13 or more and 0.13 or less, the peeling charge amount can be more effectively suppressed.
以下,使用圖7至圖9,說明本發明之實施例。圖7係顯示反應氣體濃度分佈相關之數值模擬計算模型及計算結果例之圖。圖8及圖9係顯示反應氣體之濃度分佈相關之數值模擬計算結果之吸壓依存性之圖。 Hereinafter, an embodiment of the present invention will be described using Figs. 7 to 9 . Fig. 7 is a view showing a numerical simulation calculation model relating to a concentration distribution of a reaction gas and an example of calculation results. Fig. 8 and Fig. 9 are graphs showing the pressure dependence of numerical simulation results relating to the concentration distribution of the reaction gas.
圖7係顯示反應氣體之濃度分佈相關之數值模擬之計算模型。此處,進行噴嘴與間隙中之反應氣體流動之模擬計算。作為計算軟體使用ANSYS(註冊商標)(產品名稱:ANSYS FLUENT,版本:14.5,ANSYS,Inc公司製造),藉由直接法進行流體計算。 Fig. 7 is a calculation model showing numerical simulation relating to the concentration distribution of the reaction gas. Here, a simulation calculation of the flow of the reaction gas in the nozzle and the gap is performed. As a calculation software, fluid calculation was performed by a direct method using ANSYS (registered trademark) (product name: ANSYS FLUENT, version: 14.5, manufactured by ANSYS, Inc.).
圖7(a)係顯示蝕刻槽內之基板750下方之空間700之計算模型。於實施例之計算中,相對於噴嘴730,於基板750搬送方向上游側(圖之左右)設置第一通氣路徑(氣流控制裝置)741,於下游側(右側)設置第二通氣路徑(氣流控制裝置)742。於比較例之計算中,未設置第一通氣路徑741及第二通氣路徑742。 Figure 7(a) shows a computational model of the space 700 below the substrate 750 in the etched trench. In the calculation of the embodiment, a first ventilation path (air flow control device) 741 is provided on the upstream side (left and right of the drawing) in the transport direction of the substrate 750 with respect to the nozzle 730, and a second ventilation path is provided on the downstream side (right side) (air flow control) Device) 742. In the calculation of the comparative example, the first ventilation path 741 and the second ventilation path 742 are not provided.
作為壓力相關之邊界條件設定如下。基板搬入口711之壓力係與第一緩衝槽之氣壓PLD相等。基板搬出口712之壓力係與第二緩衝槽之氣壓PNT相等。第一通氣路徑741及第二通氣路徑742內部之壓力係與連接路徑之氣壓(抽吸裝置之抽吸壓力)PBB相等。 The boundary conditions as pressure related are set as follows. The pressure of the substrate transfer inlet 711 is equal to the pressure P LD of the first buffer tank. The pressure of the substrate transfer port 712 is equal to the air pressure P NT of the second buffer tank. The pressure inside the first ventilation path 741 and the second ventilation path 742 is equal to the air pressure of the connection path (suction pressure of the suction device) P BB .
圖7(b)係模擬空間中之放大噴嘴730與基板750之間隙者。於本模擬計算中,將吹出口732a之大小dA設為2mm,將第一抽吸口733a之大小dB設為7~10mm,將第二抽吸口734a之大小dC設為7~10mm。又,將間隙731之間隔dD設為2~5mm。又,將自吹出口732a之中央至第一抽吸口733a之中央之距離I1設為70mm,將自吹出口732a之中央至第二抽吸口734a中央之距離I2設為70mm。網目尺寸係於0.1~4mm之範圍內,選擇適合每個模擬空間內的位置之值。 Fig. 7(b) shows the gap between the amplification nozzle 730 and the substrate 750 in the simulation space. In the simulation calculation, the size d A of the air outlet 732a is set to 2 mm, the size d B of the first suction port 733a is set to 7 to 10 mm, and the size d C of the second suction port 734a is set to 7~. 10mm. Further, the interval d D of the gap 731 is set to 2 to 5 mm. Further, the outlet 732a of the center to boast a first suction mouth 733a of the center distance I 1 is set to 70mm, the center 734a of the boast from the center to the outlet 732a of the second suction port I 2 is set to 70mm. The mesh size is in the range of 0.1 to 4 mm, and the value suitable for the position within each simulation space is selected.
關於參數dB、dC、dD,於上述之範圍內選擇數個,並對各個值進行計算。然而,於使用氣流控制裝置提高粗度均一性之結論、及藉由使抽吸裝置運作,可進一步提高粗度均一性之結論不變。於圖8及圖9中,顯示設定dB=7mm、dC=10mm、dD=4mm時之計算結果。 Regarding the parameters d B , d C , and d D , a plurality of them are selected within the above range, and each value is calculated. However, the conclusion that the coarseness uniformity is improved by using the airflow control device and the conclusion that the coarseness uniformity can be further improved by operating the suction device. In Figs. 8 and 9, the calculation results when d B = 7 mm, d C = 10 mm, and d D = 4 mm are set.
反應氣體通過氣體供給路徑732自吹出口732a被吹出至間隙731。反應氣體係自第一抽吸口733a朝第一氣體抽吸路徑733抽吸。又,反 應氣體係自第二抽吸口734a朝第二氣體抽吸路徑734抽吸。為了表現該狀況,設置氣體通給路徑732中之反應氣體之流入速度為一定值之邊界條件。又,設置第一氣體抽吸路徑733及第二氣體抽吸路徑734各者之內部壓力為一定之負值之邊界條件。於本模擬計算中,將氣體供給路徑732之反應氣體流入速度設為0.07m/s。又,將第一氣體抽吸路徑733之內部壓力設為-1.9 Pa,將第二氣體抽吸路徑734之內部壓力設為-1.9 Pa。 The reaction gas is blown out from the air outlet 732a to the gap 731 through the gas supply path 732. The reaction gas system is sucked from the first suction port 733a toward the first gas suction path 733. Again The gas system is sucked from the second suction port 734a toward the second gas suction path 734. In order to express this condition, a boundary condition in which the inflow velocity of the reaction gas in the gas passage path 732 is a constant value is set. Further, a boundary condition in which the internal pressure of each of the first gas suction path 733 and the second gas suction path 734 is a constant value is set. In the present simulation calculation, the reaction gas inflow velocity of the gas supply path 732 was set to 0.07 m/s. Further, the internal pressure of the first gas suction path 733 was set to -1.9 Pa, and the internal pressure of the second gas suction path 734 was set to -1.9 Pa.
於間隙731中,自左向右(圖7(b)所示之箭頭方向)搬送基板750。為了表現該狀況,設定基板750之背面751於向右方向具有一定速度之移動邊界條件。於本模擬計算中,將基板750之背面751之移動速度設為167mm/s。 In the gap 731, the substrate 750 is transported from left to right (in the direction of the arrow shown in FIG. 7(b)). In order to express this, the back surface 751 of the substrate 750 is set to have a moving boundary condition of a certain speed in the right direction. In this simulation calculation, the moving speed of the back surface 751 of the substrate 750 was set to 167 mm/s.
改變條件而計算間隙731中反應氣體之濃度分佈。改變之條件係第一緩衝槽之氣壓PLD、第二緩衝槽之氣壓PNT、及連接路徑之氣壓(抽吸裝置之抽吸壓力)PBB。 The concentration distribution of the reaction gas in the gap 731 is calculated by changing the conditions. The conditions of the change are the air pressure P LD of the first buffer tank, the air pressure P NT of the second buffer tank, and the air pressure of the connection path (suction pressure of the suction device) P BB .
相對於所賦予之PBB,試著改變數種PLD與PNT之組合,調查間隙731中之反應氣體之濃度分佈、尤其是最大值如何變化。考慮PLD與PNT之差對應於流入蝕刻槽之外部空氣流動之大小。因此,根據本模擬,可掌握間隙731中之反應氣體之濃度分佈對於外部空氣之流入之反應敏銳程度。 With respect to the given P BB , it was tried to change the combination of several kinds of P LD and P NT to investigate how the concentration distribution of the reaction gas in the gap 731, especially the maximum value, changes. It is considered that the difference between P LD and P NT corresponds to the magnitude of the external air flow flowing into the etching bath. Therefore, according to the simulation, the degree of sensitivity of the concentration distribution of the reaction gas in the gap 731 to the inflow of the outside air can be grasped.
基板750背面751之粗度係藉由基板750之背面751所暴露之反應氣體之濃度、及暴露於反應氣體之累積時間這2個要因而決定。累積時間主要由搬送基板750之速度決定。於本模擬計算中,如上述般,將搬送基板750之速度設為一定值167mm/s。因此,基板750之背面751之粗度主要以由濃度分佈之最大值決定(隨著最大值增大,粗度增大)。因此,根據本模擬,可掌握基板750之背面751之粗度受外部空氣流入之影響程度高低。 The thickness of the back surface 751 of the substrate 750 is determined by the concentration of the reaction gas exposed on the back surface 751 of the substrate 750 and the cumulative time of exposure to the reaction gas. The accumulation time is mainly determined by the speed at which the substrate 750 is transferred. In the simulation calculation, as described above, the speed at which the substrate 750 is transferred is set to a constant value of 167 mm/s. Therefore, the thickness of the back surface 751 of the substrate 750 is mainly determined by the maximum value of the concentration distribution (the thickness increases as the maximum value increases). Therefore, according to the simulation, it is understood that the thickness of the back surface 751 of the substrate 750 is affected by the inflow of external air.
圖8(a)係顯示於導入氣流控制裝置之上述比較例中,計算間隙731中反應氣體濃度分佈之結果之例。橫軸(Position:位置(m))係噴嘴730內之位置,縱軸([HF](ppm))係反應氣體之濃度。噴嘴730內之位置係以將吹出口732a作為原點,將第一抽吸口733a側設為負,將第二抽吸口734a側設為正之座標表示。反映自圖之左向右搬送基板750,且反應氣體亦受基板750影響,於吹出口732a之右側(Position>0)具有濃度分佈。 Fig. 8(a) shows an example of the result of calculating the concentration distribution of the reaction gas in the gap 731 in the above comparative example of the introduction of the gas flow control device. The horizontal axis (Position: position (m)) is the position inside the nozzle 730, and the vertical axis ([HF] (ppm)) is the concentration of the reaction gas. The position in the nozzle 730 is such that the blowing port 732a is used as the origin, the side of the first suction port 733a is set to be negative, and the side of the second suction port 734a is set to be a positive coordinate. The substrate 750 is transferred from the left to the right of the drawing, and the reaction gas is also affected by the substrate 750, and has a concentration distribution on the right side (Position>0) of the air outlet 732a.
對應於上述之PLD、PNT之各組合,獲得複數條濃度分佈曲線。範例如下。 Corresponding to each combination of P LD and P NT described above, a plurality of concentration distribution curves are obtained. An example is as follows.
pm:PLD=PNT=0 Pa,pm_LD_0 pa_NT_-1 pa:PLD=0 Pa,PNT=-1 pa,pm_LD_1 pa_NT_0 pa:PLD=1 Pa,PNT=0 pa,pm_LD_1pa_NT_1 pa:PLD=1 Pa,PNT=1 pa,pm_LD_-1 pa_NT_-1 pa:PLD=-1 Pa,PNT=-1 pa,pm_NT_0 pa_LD_-1 pa:PLD=-1 Pa,PNT=0 pa,pm_NT_1 pa_LD_0 pa:PLD=0 Pa,PNT=1 pa,自圖8(a)可知,有PLD<PNT時峰值變高、PLD>PNT時峰值變低之趨勢。另一方面,峰值之位置幾乎不變,存在於第二抽吸口734a附近。 Pm:P LD =P NT =0 Pa,pm_LD_0 pa_NT_-1 pa:P LD =0 Pa,P NT =-1 pa,pm_LD_1 pa_NT_0 pa:P LD =1 Pa,P NT =0 pa,pm_LD_1pa_NT_1 pa:P LD =1 Pa, P NT =1 pa, pm_LD_-1 pa_NT_-1 pa: P LD =-1 Pa, P NT =-1 pa, pm_NT_0 pa_LD_-1 pa: P LD =-1 Pa, P NT =0 Pa, pm_NT_1 pa_LD_0 pa: P LD =0 Pa, P NT =1 pa. It can be seen from Fig. 8(a) that there is a tendency that the peak value becomes higher when P LD <P NT and the peak value becomes lower when P LD >P NT . On the other hand, the position of the peak is hardly changed and exists in the vicinity of the second suction port 734a.
於導入氣流控制裝置後之實施例中,當於所賦予之PBB之下改變PLD與PNT之組合時,峰值高度變動範圍之大小(以下,稱為「峰值變動幅度」)較顯著。峰值變動幅度之大小對應於外部空氣流入對基板750粗面化之影響之大小。發明者已針對PBB與峰值變動幅度之關係,基於本模擬計算進行探討。 In the embodiment after the introduction of the air flow control device, when the combination of P LD and P NT is changed under the given P BB , the magnitude of the peak height variation range (hereinafter referred to as "peak fluctuation range") is remarkable. The magnitude of the peak variation corresponds to the magnitude of the effect of external air inflow on the roughening of the substrate 750. The inventors have explored the relationship between P BB and the peak variation range based on this simulation calculation.
圖8(b)、(c)及(d)係依序顯示針對PBB=-0.5 Pa、-1 Pa、-1.5 Pa時之實施例(本發明之設置有氣流控制裝置之蝕刻裝置)之計算結果。橫 軸與縱軸及範例係與圖8(a)相同。於圖8(a)、(b)、(c)、及(d)中,峰值變動幅度之大小分別為272ppm、114ppm、75ppm、23ppm。 8(b), (c), and (d) show an embodiment in which P BB = -0.5 Pa, -1 Pa, -1.5 Pa (the etching apparatus provided with the air flow control device of the present invention) Calculation results. The horizontal axis and the vertical axis and the example are the same as in Fig. 8(a). In Figs. 8(a), (b), (c), and (d), the magnitudes of the peak fluctuation ranges were 272 ppm, 114 ppm, 75 ppm, and 23 ppm, respectively.
將PBB之絕對值自零依序增大時,峰值變動幅度逐漸減小。此意指藉由以抽吸裝置抽吸流入蝕刻槽內之外部空氣,可減少外部空氣流入對基板粗面化之影響。 When the absolute value of P BB is sequentially increased from zero, the peak fluctuation amplitude gradually decreases. This means that the influence of the inflow of outside air on the roughening of the substrate can be reduced by sucking the outside air flowing into the etching bath by the suction device.
圖9係顯示於所賦予之PBB下,改變PLD與PNT組合獲得之、複數個濃度分佈曲線之峰值。橫軸(△P(Pa))表示PLD與PNT之差(△P=PLD-PNT)。縱軸係各濃度分佈之峰值([HF]max(ppm))。如(PLD、PNT)=(-1 Pa、0 Pa)與(PLD、PNT)=(0 Pa、+1 Pa)般,有相對於PLD與PNT之不同組合△P為相等之情形。因此,於圖9中,對相同△P之值,繪圖複數個(圖9中係3點)資料點。圖9(a)係顯示比較例之結算結果。圖9(b)、(c)、及(d)係依序表示PBB=-0.5 Pa、-1 Pa、-1.5 Pa時實施例之計算結果。標註於圖中資料點之序號分別對應如下。 Figure 9 is a graph showing the peaks of a plurality of concentration profiles obtained by changing the combination of P LD and P NT under the given P BB . The horizontal axis (ΔP(Pa)) represents the difference between P LD and P NT (ΔP = P LD - P NT ). The vertical axis is the peak of each concentration distribution ([HF] max (ppm)). For example, (P LD , P NT )=(-1 Pa, 0 Pa) and (P LD , P NT )=(0 Pa, +1 Pa), there is a different combination ΔP with respect to P LD and P NT Equal situation. Therefore, in Fig. 9, a plurality of (three points in Fig. 9) data points are plotted for the same value of ΔP. Fig. 9(a) shows the settlement result of the comparative example. 9(b), (c), and (d) show the calculation results of the examples in the case where PBB = -0.5 Pa, -1 Pa, -1.5 Pa. The serial numbers of the data points marked in the figure correspond to the following.
#1:(PLD、PNT)=(0 Pa、0 Pa) #1:(P LD , P NT )=(0 Pa, 0 Pa)
#2:(PLD、PNT)=(0 Pa、-1 Pa) #2:(P LD , P NT )=(0 Pa, -1 Pa)
#3:(PLD、PNT)=(0 Pa、-0.5 Pa) #3:(P LD , P NT )=(0 Pa, -0.5 Pa)
#4:(PLD、PNT)=(1 Pa、0 Pa) #4:(P LD , P NT )=(1 Pa, 0 Pa)
#5:(PLD、PNT)=(1 Pa、1 Pa) #5:(P LD , P NT )=(1 Pa, 1 Pa)
#6:(PLD、PNT)=(1 Pa、0.5 Pa) #6:(P LD , P NT )=(1 Pa, 0.5 Pa)
#7:(PLD、PNT)=(0.5 Pa、0 Pa) #7:(P LD , P NT )=(0.5 Pa, 0 Pa)
#8:(PLD、PNT)=(0.5 Pa、0.5 Pa) #8:(P LD , P NT )=(0.5 Pa, 0.5 Pa)
#9:(PLD、PNT)=(0.5 Pa、-0.5 Pa) #9:(P LD , P NT )=(0.5 Pa, -0.5 Pa)
#10:(PLD、PNT)=(-1 Pa、-1 Pa) #10:(P LD , P NT )=(-1 Pa, -1 Pa)
#11:(PLD、PNT)=(-0.5 Pa、-0.5 Pa) #11:(P LD , P NT )=(-0.5 Pa, -0.5 Pa)
#12:(PLD、PNT)=(-1 Pa、0 Pa) #12:(P LD , P NT )=(-1 Pa, 0 Pa)
#13:(PLD、PNT)=(-0.5 Pa、0 Pa) #13:(P LD , P NT )=(-0.5 Pa, 0 Pa)
#14:(PLD、PNT)=(0 Pa、1 Pa) #14:(P LD , P NT )=(0 Pa, 1 Pa)
#15:(PLD、PNT)=(0.5 Pa、1 Pa) #15:(P LD , P NT )=(0.5 Pa, 1 Pa)
#16:(PLD、PNT)=(0 Pa、0.5 Pa) #16:(P LD , P NT )=(0 Pa, 0.5 Pa)
#17:(PLD、PNT)=(-0.5 Pa、0.5 Pa) #17:(P LD , P NT )=(-0.5 Pa, 0.5 Pa)
#18:(PLD、PNT)=(0 Pa、0 Pa) #18:(P LD , P NT )=(0 Pa, 0 Pa)
如圖9所示,當PBB之絕對值自零依據增大時,峰值大致逐漸相等。因此,若使用本發明之氣流控制裝置之抽吸裝置,可使上述間隙中反應氣體之濃度分佈不受第一緩衝槽與第二緩衝槽之壓力之時間變動影響而穩定分佈。此意指藉由使抽吸裝置運作,可容易提高粗度均一性。 As shown in FIG. 9, when the absolute value of P BB increases from zero, the peaks are approximately equal. Therefore, when the suction device of the air flow control device of the present invention is used, the concentration distribution of the reaction gas in the gap can be stably distributed without being affected by the time variation of the pressures of the first buffer tank and the second buffer tank. This means that the roughness uniformity can be easily improved by operating the suction device.
表1及表2係顯示以原子力顯微鏡測定經粗面化之基板粗度(算術平均表面粗度Ra(JIS B0601-2013))之面內分佈之結果。表1表示於蝕刻槽不導入本發明之氣流控制裝置之情形時之測定結果。表2表示於蝕刻槽導入本發明之氣流控制裝置之情形之測定結果。製作條件如下。蝕刻槽尺寸:850mm,基板:無鹼玻璃(產品名:AN100,旭玻璃公司製),基板尺寸:寬度2880mm×搬送方向長度3130mm,基板搬送速度:10m/min,反應氣體組成:CF4、N2、水蒸氣,噴嘴部之反應氣體噴出流速:0.07m/sec。 Tables 1 and 2 show the results of measuring the in-plane distribution of the roughened substrate thickness (arithmetic average surface roughness Ra (JIS B0601-2013)) by atomic force microscopy. Table 1 shows the measurement results when the etching tank was not introduced into the gas flow control device of the present invention. Table 2 shows the measurement results in the case where the etching tank was introduced into the gas flow control device of the present invention. The production conditions are as follows. Etching groove size: 850 mm, substrate: alkali-free glass (product name: AN100, manufactured by Asahi Glass Co., Ltd.), substrate size: width 2880 mm × transport direction length 3130 mm, substrate transport speed: 10 m/min, reaction gas composition: CF 4 , N 2. Water vapor, reaction gas ejection flow rate at the nozzle portion: 0.07 m/sec.
測定點係於基板之寬度方向3列、於基板之搬送方向3行合計9個點。測定點之行係沿著基板之寬度方向,依序排列於距最左端500mm、中央部、距最右端500mm之位置(以下,稱為「第1行」、「第2行」、「第3行」)。測定點之列係沿著基板之搬送方向,依序排列於距最前端500mm、中央部、距最後端500mm之位置(以下,稱為「第1列」、「第2列」、「第3列」)。 The measurement points are three rows in the width direction of the substrate, and nine points in total in three rows in the transport direction of the substrate. The measurement points are arranged in the width direction of the substrate, in the order of 500 mm from the leftmost end, at the center, and at the right end of 500 mm (hereinafter referred to as "1st line", "2nd line", "3rd" Row"). The measurement points are arranged in the direction in which the substrate is transported, and are arranged at a position 500 mm from the foremost end, at the center, and at a distance of 500 mm from the last end (hereinafter referred to as "first column", "second column", "third" Column").
測定係以如下方法進行。首先,自經粗面化之基板切出包含各測定點之寬度5mm×長度5mm之試料。接著,使用原子力顯微鏡(產 品名:SPI-3800N,精工電子公司製)觀察各試料之經粗面化之表面。懸臂使用SI-DF40P2。觀察係針對掃描區域5μm×5μm,使用動態力模型,以掃描比率1Hz進行(區域內資料數:256×256)。基於該觀察,算出各測定點之算術平均表面粗度Ra。計算軟體使用附於原子力顯微鏡之軟體(軟體名:SPA-400)。 The measurement was carried out in the following manner. First, a sample having a width of 5 mm × a length of 5 mm including each measurement point was cut out from the roughened substrate. Next, use an atomic force microscope Product Name: SPI-3800N, manufactured by Seiko Instruments Inc.) Observe the roughened surface of each sample. The cantilever uses the SI-DF40P2. The observation system was performed for a scanning area of 5 μm × 5 μm using a dynamic force model at a scan ratio of 1 Hz (number of data in the area: 256 × 256). Based on this observation, the arithmetic mean surface roughness Ra of each measurement point was calculated. The calculation software uses a software attached to an atomic force microscope (software name: SPA-400).
於表1及表2中,以陣列形式表示各測定點之算術平均表面粗度Ra(單位:nm)。表1及表2之各行自左起依序對應於測定點之第1行、第2行、第3行。表1及表2之各列自上起依序對應於測定點之第1列、第2列、第3列。 In Tables 1 and 2, the arithmetic mean surface roughness Ra (unit: nm) of each measurement point is shown in an array form. Each row of Table 1 and Table 2 sequentially corresponds to the first row, the second row, and the third row of the measurement point from the left. The columns of Tables 1 and 2 correspond to the first column, the second column, and the third column of the measurement points in order from the top.
如表1表示,於不導入氣流控制裝置之情形時,粗度之均一性較低,且基板中央部之粗度小於平均值。具體而言,Ra之平均值係0.43,標準偏差係0.073,基板中央部之Ra與平均值之差係-0.144。另一方面,如表2所示,於導入氣流控制裝置之情形時,可改善粗度之均一性、基板中央部之粗度兩者。具體而言,Ra之平均值係0.45,標準偏差係0.057,基板中央部之Ra與平均值之差為+0.11。 As shown in Table 1, when the airflow control device is not introduced, the uniformity of the roughness is low, and the thickness of the central portion of the substrate is smaller than the average value. Specifically, the average value of Ra is 0.43, the standard deviation is 0.073, and the difference between Ra and the average value in the central portion of the substrate is -0.144. On the other hand, as shown in Table 2, in the case of introducing the air flow control device, both the uniformity of the thickness and the thickness of the central portion of the substrate can be improved. Specifically, the average value of Ra is 0.45, the standard deviation is 0.057, and the difference between Ra and the average value in the central portion of the substrate is +0.11.
剝離帶電量之測定係以如下之方法進行。首先,自粗面化之基板切出寬度410mm×長度510mm之試料。接著,將試料載置於真空抽 吸平台達一定時間。自上述真空抽吸平台,使用提昇銷剝離試料。以表面電位計(產品名:MODEL 341B,Trek Japan公司製)測定緊接著剝離後之試料帶電量。 The measurement of the peeling charge amount was carried out in the following manner. First, a sample having a width of 410 mm and a length of 510 mm was cut out from the roughened substrate. Next, the sample is placed in a vacuum pump Suction the platform for a certain period of time. From the above vacuum suction platform, the sample was peeled off using a lift pin. The amount of charge of the sample immediately after peeling was measured by a surface potentiometer (product name: MODEL 341B, manufactured by Trek Japan Co., Ltd.).
測定係對實施例、比較例1、及比較例2進行。實施例係使用具備本發明之氣流控制裝置之蝕刻裝置進行粗面化後之玻璃基板。比較例1係使用不具備本發明之氣流控制裝置之蝕刻裝置進行粗面化之玻璃基板。比較例2係市售之玻璃基板。實施例及比較例1之製作條件如下。蝕刻槽尺寸:850mm,基板:無鹼玻璃(產品名:AN100,旭玻璃公司製),基板尺寸:寬度2880mm×搬送方向長度3130mm,基板搬送速度:10m/min,反應氣體組成:CF4、N2、水蒸氣,噴嘴部之反應氣體噴出流速:0.07m/sec。 The measurement was performed on Examples, Comparative Example 1, and Comparative Example 2. The embodiment is a glass substrate which is roughened by using an etching apparatus including the air flow control device of the present invention. Comparative Example 1 is a glass substrate which is roughened using an etching apparatus which does not include the gas flow control device of the present invention. Comparative Example 2 is a commercially available glass substrate. The production conditions of the examples and comparative example 1 are as follows. Etching groove size: 850 mm, substrate: alkali-free glass (product name: AN100, manufactured by Asahi Glass Co., Ltd.), substrate size: width 2880 mm × transport direction length 3130 mm, substrate transport speed: 10 m/min, reaction gas composition: CF 4 , N 2. Water vapor, reaction gas ejection flow rate at the nozzle portion: 0.07 m/sec.
測定之剝離帶電量係相對比較值,為實施例:比較例1:比較例2=0.84:1.0:0.91。實施例之帶電量與比較例1、比較例2相比減低。如表1及表2所示,此係由於藉由以本發明之蝕刻槽進行粗面化,提高粗面化之均一性之故。 The measured peeling charge amount was a relative comparative value, and was an example: Comparative Example 1: Comparative Example 2 = 0.84: 1.0: 0.91. The charge amount of the Example was lower than that of Comparative Example 1 and Comparative Example 2. As shown in Tables 1 and 2, this is because the roughening of the etching groove of the present invention is carried out to improve the uniformity of the roughening.
如以上實施例所示,根據本發明,基板之要粗面化之一面與噴嘴間之間隙中之反應氣體之濃度分佈不受第一緩衝槽及第二緩衝槽之壓力變動影響,而可大致穩定分佈。藉此,可抑制基板背面之粗度不均一性。結果,可減少基板之剝離帶電之量。 As shown in the above embodiment, according to the present invention, the concentration distribution of the reaction gas in the gap between the surface to be roughened and the nozzle of the substrate is not affected by the pressure fluctuation of the first buffer tank and the second buffer tank, but may be substantially Stable distribution. Thereby, the thickness unevenness of the back surface of the substrate can be suppressed. As a result, the amount of peeling electrification of the substrate can be reduced.
本申請案係基於2014年4月16日提出申請之日本專利申請案,特願2014-084732者,該案之全文以引用的方式併入本文中。 The present application is based on a Japanese patent application filed on Apr. 16, 2014, the entire disclosure of which is hereby incorporated by reference.
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