TWI493070B - Gas diffusion chamber - Google Patents

Gas diffusion chamber Download PDF

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TWI493070B
TWI493070B TW101146066A TW101146066A TWI493070B TW I493070 B TWI493070 B TW I493070B TW 101146066 A TW101146066 A TW 101146066A TW 101146066 A TW101146066 A TW 101146066A TW I493070 B TWI493070 B TW I493070B
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gas
cavity
diffusion chamber
substrate
gas diffusion
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TW101146066A
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TW201422839A (en
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Yi Ta Wu
Wei Yu Chen
Chun Sen Wu
Yii Der Wu
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Metal Ind Res & Dev Ct
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氣體擴散室Gas diffusion chamber

本發明係有關於一種氣體擴散室,特別是有關於一種用以將薄膜沉積在基板上的氣體擴散室。This invention relates to a gas diffusion chamber, and more particularly to a gas diffusion chamber for depositing a thin film on a substrate.

不論是半導體的薄膜製程、平面顯示器(flat panel display,FPD)製程或是太陽電池成膜製程中,化學氣相沉積(CVD)扮演著舉足輕重的角色,其主要功能是將特殊反應氣體通入真空腔體中,可同時利用電漿加速氣體的化學反應,於基材表面沉積薄膜,而在CVD製程參數,腔體流場是影響鍍膜結果的關鍵因素之一。Chemical vapor deposition (CVD) plays a pivotal role in semiconductor thin film processes, flat panel display (FPD) processes, or solar cell filming processes. Its main function is to pass special reactive gases into the vacuum. In the cavity, the plasma can be used to accelerate the chemical reaction of the gas to deposit a thin film on the surface of the substrate. In the CVD process parameters, the cavity flow field is one of the key factors affecting the coating result.

台灣公告號TW 405026提出了一種用於半導體裝置之製造的氣體擴散器及具有該擴散器的反應爐。該擴散器以氣密汽缸形式呈現,其中成形一中空部及設置向上開口的進氣口使氣體可流進中空部,及一圓盤形擴散板設置於其底側附有複數噴嘴供導引及控制氣體之流出中空部,此處擴散板於徑向方向由中心開始厚度增加,使氣體通過其中之噴嘴長度隨著於徑向方向距擴散板中心距離之增加而增加。因為噴嘴出口與晶圓的距離縮短,因此可隨噴嘴出口之氣體噴射速度增加而保持恆定或提昇。Taiwan Bulletin No. TW 405026 proposes a gas diffuser for the manufacture of a semiconductor device and a reactor having the same. The diffuser is presented in the form of a gas-tight cylinder, wherein a hollow portion is formed and an upwardly opening air inlet is provided to allow gas to flow into the hollow portion, and a disc-shaped diffusion plate is disposed on the bottom side thereof with a plurality of nozzles for guiding And controlling the outflow of the gas into the hollow portion, where the diffusion plate increases in thickness from the center in the radial direction, so that the length of the nozzle through which the gas passes increases as the distance from the center of the diffusion plate increases in the radial direction. Since the distance between the nozzle outlet and the wafer is shortened, it can be kept constant or increased as the gas injection speed of the nozzle outlet increases.

台灣公告號TW M299917提出了一種用於具有蓋板之電漿處理室的氣體分配板組件,包含:一擴散板,具有:一上游側、一面向處理區的下游側、及多數氣體通道,形 成穿過該擴散板;及一檔板,放置於處理室的蓋板與擴散板之間,具有多數孔,由檔板上表面延伸至下表面,其中該等孔具有至少兩側。該檔板的該等孔分為小針孔及大針孔,該小針孔係用以允許足夠的氣體混合物通過,該大針孔用以改良整個基板的處理均勻性。Taiwan Publication No. TW M299917 proposes a gas distribution plate assembly for a plasma processing chamber having a cover plate, comprising: a diffusion plate having: an upstream side, a downstream side facing the treatment zone, and a plurality of gas passages Passing through the diffuser plate; and a baffle disposed between the cover plate of the process chamber and the diffuser plate, having a plurality of holes extending from the surface of the baffle to the lower surface, wherein the holes have at least two sides. The holes of the baffle are divided into small pinholes and large pinholes for allowing passage of a sufficient gas mixture for improving the uniformity of processing of the entire substrate.

台灣申請號TW 201134979提出了一種氣體分佈噴灑模組,可使氣體充分的混合,解決氣體噴灑到基板之不均勻性,透過一種鍍膜設備其中的氣體分佈噴灑模組,包括第一、第二、第三與第四擴散板,可使得氣體分佈噴灑模組與上述基板之間的距離拉近、增加鍍膜效率。Taiwan Application No. TW 201134979 proposes a gas distribution spray module that allows the gas to be sufficiently mixed to solve the non-uniformity of the gas sprayed onto the substrate, through a gas distribution spray module of a coating device, including the first and second, The third and fourth diffusing plates can bring the distance between the gas distribution spray module and the substrate closer, and increase the coating efficiency.

但是,上述三篇專利前案的進氣方式都採用垂直式的進氣方式,但該方式最大的問題在於氣體被導入腔體後,通常是立即被四周圍的抽氣區帶走,並在距離抽氣區最遠的中央處形成局部滯流區,而該區域在成膜時膜厚往往相對厚於或薄於一般平均值,所以會造成基板中央處與基板周圍成膜分佈不均之型態。因此,氣流垂直的氣進方式與流道幾何結構,是導致化學氣相沉積無法有效的在成膜基板上被均勻分配,而氣流的分配不均是根本問題。However, the air intake methods of the above three patents all adopt the vertical air intake mode, but the biggest problem of this method is that after the gas is introduced into the cavity, it is usually immediately taken away by the exhausting area around the four, and A local stagnant zone is formed at the center farthest from the pumping zone, and the film thickness tends to be relatively thicker or thinner than the average value at the time of film formation, so that the film is unevenly distributed at the center of the substrate and around the substrate. Type. Therefore, the gas inlet mode and the flow channel geometry of the gas flow are such that the chemical vapor deposition cannot be effectively distributed uniformly on the film formation substrate, and the uneven distribution of the gas flow is a fundamental problem.

因此,便有需要提供一種化學氣相沉積用之氣體擴散室,能夠解決前述的問題。Therefore, there is a need to provide a gas diffusion chamber for chemical vapor deposition which can solve the aforementioned problems.

本發明的目的在於,提供一種能大幅被擴散與混合的氣體擴散室。It is an object of the present invention to provide a gas diffusion chamber that can be greatly diffused and mixed.

為達成上述目的,本發明提出一種用以將一薄膜沉積在一基板上之氣體擴散室,包括:一腔體;一基板區,位在該腔體內部,用以承載該基板;至少二個進氣端,相對設置在該腔體的兩側,用以向該基板區區域提供氣體;以及至少二個抽氣端,相對設置在該腔體的另兩側,用以從該基板區區域抽出氣體,且該些抽氣端抽出氣體的方向與該腔體內部之底面平行;其中,抽出氣體方向與提供氣體方向互相垂直。In order to achieve the above object, the present invention provides a gas diffusion chamber for depositing a thin film on a substrate, comprising: a cavity; a substrate region located inside the cavity for carrying the substrate; at least two The air inlet ends are oppositely disposed on opposite sides of the cavity for supplying gas to the substrate area; and at least two pumping ends are oppositely disposed on the other sides of the cavity for receiving from the substrate area The gas is withdrawn, and the direction of the gas extracted by the suction ends is parallel to the bottom surface of the cavity; wherein the direction of the extracted gas is perpendicular to the direction of the supply gas.

本發明是以一種水平兩對向進氣端的進氣設計,搭配兩對向鄰側抽氣端之狹窄型的抽氣設計,當氣體被導入腔體後,能大幅被擴散與混合。The invention is designed with a horizontal two-way intake air inlet, and a narrow suction design with two opposite suction sides. When the gas is introduced into the cavity, it can be greatly diffused and mixed.

因此,腔體內部的流道設計與安排上,透過改變氣流進入腔體的主流場結構,方可使被抽氣端帶走的氣流能更有效、更均勻混合進行化學氣相沉積,進而使薄膜沉積均勻性提升。Therefore, the flow channel design and arrangement inside the cavity can change the airflow into the main flow field structure of the cavity, so that the airflow carried by the suction end can be more effectively and uniformly mixed for chemical vapor deposition, thereby Film deposition uniformity is improved.

為了讓本發明之上述和其他目的、特徵、和優點能更明顯,下文將配合所附圖示,作詳細說明如下。The above and other objects, features, and advantages of the present invention will become more apparent from the accompanying drawings.

圖1為本發明實施例之氣體擴散室之立體透視圖。圖2為本發明實施例之氣體擴散室之上視圖。圖3為圖2之AA’剖線圖。圖4為圖2之BB’剖線圖。請同時參閱圖1~圖4,該氣體擴散室100用以將一薄膜沉積在一基板210上,該氣體擴散室100包括:一腔體110、一基板區120、二個抽氣端、二個進氣端及一補氣端130。為方便說明, 二個抽氣端分別為第一抽氣端141及第二抽氣端142。二個進氣端分別為第一進氣端151及第二進氣端152。BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a perspective perspective view of a gas diffusion chamber in accordance with an embodiment of the present invention. Figure 2 is a top plan view of a gas diffusion chamber in accordance with an embodiment of the present invention. Figure 3 is a cross-sectional view taken along line AA' of Figure 2; Figure 4 is a cross-sectional view taken along line BB' of Figure 2; Referring to FIG. 1 to FIG. 4, the gas diffusion chamber 100 is configured to deposit a film on a substrate 210. The gas diffusion chamber 100 includes a cavity 110, a substrate region 120, two pumping ends, and two Intake end and a supplement end 130. For convenience of explanation, The two pumping ends are a first pumping end 141 and a second pumping end 142, respectively. The two intake ends are a first intake end 151 and a second intake end 152, respectively.

該基板區120位在該腔體110內部,用以承載該基板210。在本發明實施例中,該基板區120有一基板加熱裝置121,且該基板加熱裝置121具有一基板加熱凹陷區122。該基板加熱凹陷區122用以放置該基板210,使該基板210不會在該腔體110內部凸出。該基板加熱裝置121可對該基板210進行加熱動作。The substrate region 120 is located inside the cavity 110 for carrying the substrate 210. In the embodiment of the present invention, the substrate region 120 has a substrate heating device 121, and the substrate heating device 121 has a substrate heating recess region 122. The substrate heating recessed area 122 is used to place the substrate 210 such that the substrate 210 does not protrude inside the cavity 110. The substrate heating device 121 can perform a heating operation on the substrate 210.

二個進氣端151、152相對設置在該腔體110的兩側,用以向該基板區210區域提供氣體。在本發明實施例中,第一進氣端151設置在該腔體110內部之左側面113,第二進氣端152設置在該腔體110內部之右側面114,可用以同時向該基板區120區域提供氣體。請同時參閱圖5,為本發明擴散板示意圖,為了使氣體的流速及流量更加穩定,在該些進氣端151、152到基板區120之間可設置一擴散板160,且該擴散板160上具有多數個孔洞161,可為矩陣或交錯的方式排列,該擴散板160的設置並不限制本發明的專利實施之範圍。Two inlet ends 151, 152 are oppositely disposed on opposite sides of the cavity 110 for supplying gas to the region of the substrate region 210. In the embodiment of the present invention, the first air inlet end 151 is disposed on the left side surface 113 of the interior of the cavity 110, and the second air inlet end 152 is disposed on the right side surface 114 of the interior of the cavity 110, and can be used simultaneously to the substrate area. The 120 area provides gas. Please refer to FIG. 5 , which is a schematic diagram of a diffusion plate according to the present invention. In order to make the flow rate and flow rate of the gas more stable, a diffusion plate 160 may be disposed between the inlet ends 151 , 152 and the substrate region 120 , and the diffusion plate 160 . There are a plurality of holes 161 there, which may be arranged in a matrix or in a staggered manner. The arrangement of the diffuser plate 160 does not limit the scope of the patent implementation of the present invention.

二個抽氣端141、142相對設置在該腔體110的另兩側,用以從該基板區120區域抽出氣體。在本發明實施例中,該第一抽氣端141設置在該腔體110內部之前側面115,該第二抽氣端142設置在該腔體110內部之後側面116,且第一抽氣端141及第二抽氣端142位在該基板區120的中線兩端,使該些抽氣端141、142的抽出氣體方向 與該些進氣端151、152的提供氣體方向互相垂直,且該些抽氣端141、142抽出氣體的方向與該腔體110內部之底面112平行。Two pumping ends 141, 142 are oppositely disposed on opposite sides of the cavity 110 for extracting gas from the region of the substrate region 120. In the embodiment of the present invention, the first pumping end 141 is disposed on the front side 115 of the cavity 110, the second pumping end 142 is disposed inside the cavity 110, and the first pumping end 141. And the second pumping end 142 is located at the two ends of the center line of the substrate region 120, so that the exhausting gas directions of the pumping ends 141, 142 The gas supply directions are perpendicular to the gas supply ends 151, 152, and the gas extraction ends 141, 142 are drawn in a direction parallel to the bottom surface 112 of the cavity 110.

第一抽氣端141及第二抽氣端142由一總抽氣端180控制第一抽氣端141及第二抽氣端142在抽氣時的流速及流量。The first pumping end 141 and the second pumping end 142 are controlled by a total pumping end 180 to control the flow rate and flow rate of the first pumping end 141 and the second pumping end 142 during pumping.

請同時參閱圖6,該第一抽氣端141與該腔體110的前側面115的連接處以弧角設計,能使腔體110內的氣體流進第一抽氣端141時,能更加平順,使腔體110氣體200(圖中以箭頭表示氣體及氣體的流向)的流速及流量更加穩定。同樣地,該第二抽氣端142與該腔體的後側面的連接處也以弧角設計。該第一抽氣端141及該第二抽氣端142用以從該基板區120方向抽出氣體,且抽氣端141、142的截面積介在該些進氣端151、152的截面積的0.08倍到0.14倍之間。Referring to FIG. 6 at the same time, the connection between the first pumping end 141 and the front side 115 of the cavity 110 is designed at an arc angle, so that the gas in the cavity 110 can flow into the first pumping end 141 to be smoother. The flow rate and flow rate of the chamber 110 gas 200 (indicated by the arrows indicating the flow of gas and gas) are more stable. Similarly, the junction of the second pumping end 142 and the rear side of the cavity is also designed at an arc angle. The first pumping end 141 and the second pumping end 142 are used for extracting gas from the direction of the substrate region 120, and the cross-sectional areas of the pumping ends 141 and 142 are 0.08 of the cross-sectional area of the inlet ends 151 and 152. Doubled to 0.14 times.

該補氣端130為長條狀,設置在該腔體110內部之頂面111,並位在該基板區120之正上方,且沿著該基板區120的中線。請同時參閱圖7,該補氣端130具有多數孔洞131,該些孔洞131可為矩陣或交錯的方式排列,且每一該孔洞之孔深在1~5(mm)之間,孔徑在0.5~1(mm)之間,可使從補氣端130送出的氣體的流速及流量更加穩定。The gas supply end 130 is elongated and disposed on the top surface 111 of the cavity 110 and located directly above the substrate region 120 and along the center line of the substrate region 120. Referring to FIG. 7 at the same time, the air supply end 130 has a plurality of holes 131, which may be arranged in a matrix or in a staggered manner, and each of the holes has a hole depth of 1 to 5 (mm) and a hole diameter of 0.5. Between ~1 (mm), the flow rate and flow rate of the gas sent from the gas supply end 130 can be made more stable.

第一進氣端151、第二進氣端152及補氣端130可由一系統之MFC(Mass Flow rate Controller,質流量控制器)來各別控制要進氣的流速或流量。The first intake end 151, the second intake end 152, and the supplemental end 130 can be individually controlled by a system MFC (Mass Flow Rate Controller) to control the flow rate or flow rate of the intake air.

舉例來說:以一般2.5代的基板為例,基板尺寸為300×300(mm),因此氣體擴散室100的長寬高為500×500×60(mm)。氣體擴散室100的腔體110長a寬b介在500~320(mm),高度c為25(mm)。基板區120的面積需大於基板尺寸,因此基板區120的長d寬e可為320×320(mm)。該些進氣端151、152面積的長度與腔體110的長度a同樣介在320~500(mm),該些進氣端151、152的寬度與腔體110高度c同樣為25(mm)。該些抽氣端141、142面積的寬度f為32~50(mm),意即由中央處向兩側約延伸16~25(mm),該些抽氣端141、142的高度與腔體110高度f同樣為25(mm)。該些補氣端151、152面積的長度與腔體110的長度a同樣介在320~500(mm),補氣端130的寬度g為60(mm),意即由中央處向兩側約延伸30(mm)。For example, taking a substrate of 2.5 generations as an example, the substrate size is 300×300 (mm), so the length and width of the gas diffusion chamber 100 are 500×500×60 (mm). The cavity 110 of the gas diffusion chamber 100 has a length a width b of 500 to 320 (mm) and a height c of 25 (mm). The area of the substrate region 120 needs to be larger than the substrate size, so the length d width e of the substrate region 120 may be 320×320 (mm). The lengths of the inlet ends 151, 152 are the same as the length a of the cavity 110 at 320 to 500 (mm), and the widths of the inlet ends 151, 152 are 25 (mm) as the height c of the cavity 110. The width f of the area of the pumping ends 141, 142 is 32~50 (mm), that is, extending from the center to the sides by about 16~25 (mm), the heights of the pumping ends 141, 142 and the cavity The height f of 110 is also 25 (mm). The length of the air supply ends 151, 152 is the same as the length a of the cavity 110 between 320 and 500 (mm), and the width g of the air supply end 130 is 60 (mm), which means that the center extends to the sides. 30 (mm).

假設,該氣體擴散室用於電漿增強化學氣相沉積(Plasma-Enhanced CVD,PECVD)時,在腔體內部需要再增加一上電極板及一下電極板,並分別設置在該腔體的頂面及底面,而腔體的高度就定義為從上電極板到下電極板的距離,因此本發明的氣體擴散室能因應不同的化學氣相沉積製程作相對應的改變,化學氣相沉積製程可為:常壓化學氣相沉積(Atmospheric Pressure CVD,APCVD)、低壓化學氣相沉積(Low-pressure CVD,LPCVD)、電漿增強化學氣相沉積、有機金屬化學氣相沉積(Metalorganic chemical vapor deposition,MOCVD),等不同的化學氣相沉積製程。It is assumed that when the gas diffusion chamber is used for plasma-enhanced CVD (PECVD), an upper electrode plate and a lower electrode plate need to be added inside the cavity, and are respectively disposed at the top of the cavity. The surface and the bottom surface, and the height of the cavity is defined as the distance from the upper electrode plate to the lower electrode plate. Therefore, the gas diffusion chamber of the present invention can be correspondingly changed according to different chemical vapor deposition processes, and the chemical vapor deposition process It can be: Atmospheric Pressure CVD (APCVD), Low Pressure CVD (LPCVD), Plasma Enhanced Chemical Vapor Deposition, Metalorganic Chemical Vapor Deposition (Metalorganic Chemical Vapor Deposition). , MOCVD), and other chemical vapor deposition processes.

本發明是以一種水平兩對向進氣端的進氣設計,搭配 兩對向鄰側抽氣端之狹窄型的抽氣設計,當氣體被導入腔體後,能大幅被擴散與混合。再者,本發明針對兩對向進氣設計在中間處可能會形成局部停滯區,所以再導入腔體上緣補氣端之局部進氣,以避免氣流停滯所衍生的均勻問題,但補氣端所扮演角色僅為輔助功能,所以將形成一長條狀,可使腔體頂面之孔洞需求大幅減少,進而減少加工製作及維護成本。The invention is designed with an air intake of two horizontally opposite intake ends, and is matched with The narrow suction design of the two opposite suction sides can be greatly diffused and mixed when the gas is introduced into the cavity. Furthermore, the present invention may form a local stagnation zone in the middle of the design of the two opposite intake airs, so that the local intake air at the air supply end of the upper edge of the cavity is further introduced to avoid the uniform problem derived from the airflow stagnation, but the qi is supplemented. The role played by the end is only an auxiliary function, so a long strip will be formed, which will greatly reduce the hole requirement of the top surface of the cavity, thereby reducing the processing and maintenance costs.

因此,腔體內部的流道設計與安排上,透過改變氣流進入腔體的主流場結構,方可使被抽氣端帶走的氣流能更有效、更均勻混合進行化學氣相沉積,進而使薄膜沉積均勻性提升。Therefore, the flow channel design and arrangement inside the cavity can change the airflow into the main flow field structure of the cavity, so that the airflow carried by the suction end can be more effectively and uniformly mixed for chemical vapor deposition, thereby Film deposition uniformity is improved.

綜上所述,乃僅記載本發明為呈現解決問題所採用的技術手段之實施方式或實施例而已,並非用來限定本發明專利實施之範圍。即凡與本發明專利申請範圍文義相符,或依本發明專利範圍所做的均等變化與修飾,皆為本發明專利範圍所涵蓋。In the above, it is merely described that the present invention is an embodiment or an embodiment of the technical means for solving the problem, and is not intended to limit the scope of implementation of the present invention. That is, the equivalent changes and modifications made in accordance with the scope of the patent application of the present invention or the scope of the invention are covered by the scope of the invention.

100‧‧‧氣體擴散室100‧‧‧ gas diffusion chamber

110‧‧‧腔體110‧‧‧ cavity

111‧‧‧頂面111‧‧‧ top surface

112‧‧‧底面112‧‧‧ bottom

113‧‧‧左側面113‧‧‧left side

114‧‧‧右側面114‧‧‧ right side

115‧‧‧前側面115‧‧‧ front side

116‧‧‧後側面116‧‧‧Back side

120‧‧‧基板區120‧‧‧Substrate area

121‧‧‧基板加熱裝置121‧‧‧Substrate heating device

122‧‧‧基板加熱凹陷區122‧‧‧Substrate heating recess

130‧‧‧補氣端130‧‧‧ qi end

131‧‧‧孔洞131‧‧‧ holes

141‧‧‧第一抽氣端141‧‧‧first pumping end

142‧‧‧第二抽氣端142‧‧‧second pumping end

151‧‧‧第一進氣端151‧‧‧First intake end

152‧‧‧第二進氣端152‧‧‧second intake end

160‧‧‧擴散板160‧‧‧Diffuser

161‧‧‧孔洞161‧‧‧ hole

180‧‧‧總抽氣端180‧‧‧Total pumping end

200‧‧‧氣體200‧‧‧ gas

210‧‧‧基板210‧‧‧Substrate

a‧‧‧腔體長度距離A‧‧‧ cavity length distance

b‧‧‧腔體寬度距離B‧‧‧ cavity width distance

c‧‧‧腔體高度距離C‧‧‧cavity height distance

d‧‧‧基板區長度距離d‧‧‧Drop area length distance

e‧‧‧基板區寬度距離e‧‧‧Drop area width distance

f‧‧‧抽氣端寬度距離f‧‧‧Exhaust end width distance

g‧‧‧補氣端寬度距離g‧‧‧Vending end width distance

圖1為本發明實施例之氣體擴散室之立體透視圖;圖2為本發明實施例之氣體擴散室之上視圖;圖3為圖2之AA’剖線圖;圖4為圖2之BB’剖線圖;圖5為擴散板之部份放大圖;圖6為第一抽氣端之部份放大圖;以及圖7為補氣端的出風口之部份放大圖。1 is a perspective view of a gas diffusion chamber according to an embodiment of the present invention; FIG. 2 is a top view of a gas diffusion chamber according to an embodiment of the present invention; FIG. 3 is a cross-sectional view taken along line AA' of FIG. 2; 'The line drawing; Fig. 5 is a partial enlarged view of the diffusing plate; Fig. 6 is a partial enlarged view of the first pumping end; and Fig. 7 is a partial enlarged view of the air outlet of the air supply end.

100‧‧‧氣體擴散室100‧‧‧ gas diffusion chamber

120‧‧‧基板區120‧‧‧Substrate area

130‧‧‧補氣端130‧‧‧ qi end

141‧‧‧第一抽氣端141‧‧‧first pumping end

142‧‧‧第二抽氣端142‧‧‧second pumping end

151‧‧‧第一進氣端151‧‧‧First intake end

152‧‧‧第二進氣端152‧‧‧second intake end

180‧‧‧總抽氣端180‧‧‧Total pumping end

Claims (10)

一種用以將一薄膜沉積在一基板上之氣體擴散室,包括:一腔體;一基板區,位在該腔體內部,用以承載該基板;至少二個進氣端,相對設置在該腔體的兩側,用以向該基板區區域提供氣體;以及至少二個抽氣端,相對設置在該腔體的另兩側,用以從該基板區區域抽出氣體,且該些抽氣端抽出氣體的方向與該腔體內部之一底面平行;其中,抽出氣體方向與提供氣體方向互相垂直。A gas diffusion chamber for depositing a film on a substrate comprises: a cavity; a substrate region located inside the cavity for carrying the substrate; at least two inlet ends disposed opposite to each other Two sides of the cavity for supplying gas to the substrate region; and at least two pumping ends disposed opposite to each other on the other side of the cavity for extracting gas from the substrate region, and the pumping The direction in which the gas is withdrawn is parallel to a bottom surface of the interior of the cavity; wherein the direction of the extracted gas is perpendicular to the direction of the gas supply. 如申請專利範圍第1項所述之氣體擴散室,其中該些抽氣端的截面積介在該些進氣端的截面積的0.08倍到0.14倍之間。The gas diffusion chamber of claim 1, wherein the cross-sectional areas of the suction ends are between 0.08 and 0.14 times the cross-sectional area of the intake ends. 如申請專利範圍第1項所述之氣體擴散室,其中該抽氣端設置在該腔體的側面上,且該抽氣端與該腔體的側面的連接處以弧角設計。The gas diffusion chamber of claim 1, wherein the suction end is disposed on a side of the cavity, and the connection between the suction end and the side of the cavity is designed at an arc angle. 如申請專利範圍第1項所述之氣體擴散室,其中該些抽氣端位在該基板區的中線兩端,並設置在該腔體側面上。The gas diffusion chamber of claim 1, wherein the suction ends are located at both ends of the center line of the substrate region and are disposed on a side of the cavity. 如申請專利範圍第1項所述之氣體擴散室,其中該些進氣端到基板區之間設置一擴散板,且該擴散板上具有多數個孔洞。The gas diffusion chamber of claim 1, wherein a diffusion plate is disposed between the inlet ends and the substrate region, and the diffusion plate has a plurality of holes. 如申請專利範圍第1項所述之氣體擴散室,更包括一補 氣端,位在該基板區之正上方。For example, the gas diffusion chamber described in claim 1 of the patent scope includes a supplement The gas end is located directly above the substrate area. 如申請專利範圍第6項所述之氣體擴散室,其中該補氣端為長條狀,沿著該基板區的中線,並設置在該腔體之一頂面上。The gas diffusion chamber of claim 6, wherein the gas supply end is elongated, along a center line of the substrate region, and disposed on a top surface of the cavity. 如申請專利範圍第6項所述之氣體擴散室,其中該補氣端具有多數孔洞。The gas diffusion chamber of claim 6, wherein the gas supply end has a plurality of holes. 如申請專利範圍第8項所述之氣體擴散室,其中每一該孔洞之孔深在1~5(mm)之間。The gas diffusion chamber of claim 8, wherein each of the holes has a depth of between 1 and 5 (mm). 如申請專利範圍第8項所述之氣體擴散室,其中每一該些孔洞之孔徑在0.5~1(mm)之間。The gas diffusion chamber of claim 8, wherein each of the holes has a pore diameter of between 0.5 and 1 (mm).
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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0276386B1 (en) * 1986-12-15 1991-07-31 Siemens-Albis Aktiengesellschaft Process for depositing a solder layer on metallic or metallized surfaces of components
EP0341646B1 (en) * 1988-05-13 1992-04-15 Hoechst Aktiengesellschaft Process and apparatus for drying a liquid layer deposited onto a moving carrier material
TW513489B (en) * 2000-10-24 2002-12-11 Duratek Inc Gas distribution plate for plasma treatment gas and its manufacture method
US20080237141A1 (en) * 2007-03-28 2008-10-02 Kerfoot Technologies, Inc. Treatment for Recycling Fracture Water Gas and Oil Recovery in Shale Deposits
TW200842201A (en) * 2007-04-19 2008-11-01 E Heng Technology Co Ltd Gas deflection device for vacuum process
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0276386B1 (en) * 1986-12-15 1991-07-31 Siemens-Albis Aktiengesellschaft Process for depositing a solder layer on metallic or metallized surfaces of components
EP0341646B1 (en) * 1988-05-13 1992-04-15 Hoechst Aktiengesellschaft Process and apparatus for drying a liquid layer deposited onto a moving carrier material
TW513489B (en) * 2000-10-24 2002-12-11 Duratek Inc Gas distribution plate for plasma treatment gas and its manufacture method
EP1735208B1 (en) * 2004-03-19 2009-12-16 Imre Nehéz Method and system for handling gas diffusion through the envelopes of airships and balloons
US20080237141A1 (en) * 2007-03-28 2008-10-02 Kerfoot Technologies, Inc. Treatment for Recycling Fracture Water Gas and Oil Recovery in Shale Deposits
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