TW531439B - Connecting device of exhaust treatment device for use in semiconductor manufacturing process - Google Patents
Connecting device of exhaust treatment device for use in semiconductor manufacturing process Download PDFInfo
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531439 --鐘89126533_年月日 修心_ 五、發明說明(1) ' 發明之領域 。,發明提供一種連接裝置,尤指一種用於一半導體製 私廢$處理系統中連接一真空泵浦出口端管線以及一濕式 刷洗裝置(wet scrubber)之連接裝置,以有效避免真空泵 浦出口端官線的阻塞(c 1 〇 g g i n g )。 背景說明531439-钟 89112633_ 年月 日 修 心 _ V. Description of invention (1) '' Field of invention. The invention provides a connection device, in particular a connection device for connecting a vacuum pump outlet line and a wet scrubber in a semiconductor private waste processing system to effectively avoid the vacuum pump outlet end official Blocking of the line (c 1 ogging). Background note
氮化石夕(si 1 iC0n nitride,Si 3n4)是一種在半導體製 程中常見的介電材料,最主要的應用是做為矽氧層的蝕刻 遮罩(etch mask),而由於其不易被氧滲透的特性,也被 應用於區域氧化(local oxidati〇n silic〇n,L〇c〇s) 製程中’做為場氧化層成長時的遮罩層。此外,氮化矽對 驗金屬離子的防堵能力以及對水氣的阻擋能力也使得它被 廣泛地應用在做為半導體元件的保護層上。Si 1 iC0n nitride (Si 3n4) is a common dielectric material used in semiconductor manufacturing. The most important application is as an etch mask for the silicon-oxygen layer, but because it is not easily penetrated by oxygen The characteristics are also used in the local oxidation (local oxidation) process as a masking layer when the field oxide layer grows. In addition, silicon nitride's ability to prevent metal ions and its ability to block water vapor has also made it widely used as a protective layer for semiconductor devices.
一般形成氮化矽的方法是利用化學氣相沈積法,包括 有電漿增強化學氣相沈積法(Plasma-enhanced CVD, PECVD)以及低壓化學氣相沈積法(i〇w — pressure CVD, LPCVD)兩種。其中由於PECVD法屬於一較低溫(低於45 0°C ) 的製程,因此氮化矽保護層的製作皆是利用PECVD 法。LPCVD法則屬於較高溫( 7 0 0至8 0 0°C )的製程,係在一 稱為氮化石夕高溫氧化爐管(high temperature oxidationThe general method for forming silicon nitride is to use chemical vapor deposition, including plasma enhanced chemical vapor deposition (Plasma-enhanced CVD, PECVD) and low pressure chemical vapor deposition (iow-pressure CVD, LPCVD). Both. Among them, the PECVD method belongs to a relatively low temperature (less than 45 ° C) process, so the production of the silicon nitride protective layer is made by the PECVD method. The LPCVD rule belongs to a higher temperature (700 to 800 ° C) process, which is a high temperature oxidation furnace tube called high temperature oxidation
第5頁 531439 _案號 89126533___年 月_g_修正_ 五、發明說明(2) furnace,HTO furnace)中進行。在進行LPCVD氮化矽沈積 時,一般是使用二氯矽烷(dichlorosi lane,SiH2Cl 2)以及 氨氣(ammonia,NH 3)為反應氣體,將其通入高溫氧化爐管 中並將壓力控制在0· 1至1托耳(Torr)之間。由於二氯矽烷 在常溫下為液體,產生二氯矽烷氣體的方法係將盛有二氯 矽烧液體的容器加熱。此外,為避免二氯石夕炫冷凝成液 體,輸送二氯矽烷氣體的製程管線皆利用加熱帶(tape heater)包覆加熱。形成LPVCD氮化矽的化學反應式如式 (1 )所示: 3SiH2Cl2(g) + 7NH3(g)-Page 5 531439 _ Case No. 89126533 _ month_g_ amendment_ V. Description of the invention (2) furnace, HTO furnace). When performing LPCVD silicon nitride deposition, dichlorosi lane (SiH2Cl 2) and ammonia (ammonia, NH 3) are generally used as reaction gases, which are passed into a high-temperature oxidation furnace tube and the pressure is controlled at 0. · Between 1 and 1 Torr. Since dichlorosilane is a liquid at normal temperature, the method for generating dichlorosilane gas is to heat the container containing the dichlorosilane fired liquid. In addition, in order to avoid condensing dichlorite, the process pipelines that transport dichlorosilane gas are covered and heated by a tape heater. The chemical reaction formula for forming LPVCD silicon nitride is shown in formula (1): 3SiH2Cl2 (g) + 7NH3 (g)-
Si 3N4(s) + 3NH4C1 (g) + 3HCl (g) + 6H2(g) (1 ) 由於在進行LPCVD氮化矽沈積之後所產生的製程廢氣 中包括有氯化鏔(ammonium chloride,NH4C1)氣體有毒氣 體,因此製程廢氣經由真空泵浦抽出高溫氧化爐管之後, 需再經由一製程廢氣處理系統處理,一般是利用濕式刷洗 裝置。利用水與含有氣化銨氣體之製程廢氣接觸,由於氯 化銨氣體有易溶於水的特性’經由式(2 )之反應’可有效 去除氯化銨氣體。 NH4C1 (g) + H20( 1 )-> NH4+〇H-(aq) + HCl (aq) (2) 請參閱圖一,圖一為習知LPCVD氮化矽廢氣處理系統Si 3N4 (s) + 3NH4C1 (g) + 3HCl (g) + 6H2 (g) (1) Because the process waste gas produced after LPCVD silicon nitride deposition includes ammonium chloride (NH4C1) gas Toxic gas, so the process waste gas is pumped out of the high-temperature oxidation furnace tube through a vacuum pump, and then needs to be processed by a process waste gas treatment system. Generally, a wet scrubbing device is used. The use of water in contact with the exhaust gas of the process containing the gasified ammonium gas can effectively remove the ammonium chloride gas due to its characteristic of being easily soluble in water ′ via the reaction of formula (2). NH4C1 (g) + H20 (1)-> NH4 + 〇H- (aq) + HCl (aq) (2) Please refer to Figure 1. Figure 1 shows the conventional LPCVD silicon nitride exhaust gas treatment system.
531439 案號 89126533 五、發明說明(3) 配置示意圖。如圖一所示, ,一鬲溫氧化爐管1 0中進行 氧化爐管1 〇中的壓力控制在 溫氧化爐管1 0所抽出之製程 ,程管線1 4輸送至真空泵浦 氣體、氯化氫、氫氣以及微 程管線1 2以及製程管線1 4之 ^4 ’用來移除製程廢氣18中 氣體’以免造成對真空泵浦 習知LPCVD氮化矽沈積反應係 ’並利用一真空泵浦2 0將高溫 〇· 1至1托耳(T〇rr)之間。從高 廢氣1 8經由一製程管線1 2以及 2 0 °製程廢氣丨8中含有氯化銨 量的氮化矽固體微粒。介於製 間為一冷凝器(cold trap) 的固體顆粒並初步冷凝氯化銨 2 0的傷害。 卜 經由冷凝器1 4處理過之製程廢氣1 9含有氣化銨氣體、 氯化虱以及氫氣,並再由真空泵浦20轉為具有較大壓力的 製程廢氣2 3,藉由一輸送管線2 2輸送至一冷凝器2 4。經由 冷凝器2 4,製程廢氣2 3中的氣化銨氣體濃度可再減少成為 製程廢氣2 5,並經由輸送管線2 6輸送至一濕式刷洗裝置 3 〇。冷凝器1 4以及2 4可以為E D W A R D S公司所提供之冷凝 器。濕式刷洗裝置3 0與輸送管線之間係藉由一特殊接頭裝 置2 8連接以避免製程廢氣2 5的外洩。連接裝置2 8係直立安 裝於輸送管線2 6以及濕式刷洗裝置3 0之間。 需注意的是,為方便說明本發明,圖一中所示之管線 與裝置僅為示意本發明之背景’因此其它管線配件例如控 制閥、儀表以及控制電路因非本發明之重點,在圖一中予 以省略。531439 Case number 89126533 V. Description of the invention (3) Configuration diagram. As shown in Fig. 1, the pressure in the oxidation furnace tube 10 is controlled in the temperature oxidation furnace tube 10, and the process drawn from the temperature oxidation furnace tube 10 is controlled, and the pipeline 14 is sent to the vacuum pump gas, hydrogen chloride, Hydrogen and micro-range line 12 and process line 14 ^ 4 'for removing gas from process exhaust gas 18' so as not to cause vacuum pumping known LPCVD silicon nitride deposition reaction system 'and use a vacuum pump 20 to heat 0.1 to 1 Torr. From the high exhaust gas 18 through a process line 12 and the 20 ° process exhaust gas 8, the silicon nitride solid particles in the amount of ammonium chloride are contained. The damage between the solid particles in the system as a cold trap and the initial condensation of ammonium chloride 2 0. The process exhaust gas 19 processed by the condenser 14 contains ammonium gas, chloride lice and hydrogen gas, and is then converted from the vacuum pump 20 to a process exhaust gas having a large pressure 2 3 through a transmission line 2 2 Conveyed to a condenser 24. Through the condenser 24, the concentration of the vaporized ammonium gas in the process exhaust gas 23 can be further reduced to the process exhaust gas 25, and it is transported to a wet scrubbing device 30 via the transfer line 26. The condensers 14 and 24 can be the condensers provided by E D W A R D S. The wet scrubbing device 30 and the transfer line are connected by a special joint device 28 to avoid the leakage of process exhaust gas 25. The connection device 2 8 is installed upright between the conveying line 26 and the wet brushing device 30. It should be noted that, for the convenience of explaining the present invention, the pipelines and devices shown in FIG. 1 are only for illustrating the background of the present invention. Omitted.
531439 案號 89126533 五、發明說明(4) 月 曰 修正 請茶閱圖 意圖。如圖二 5 1。中空殼體 線,而另一端 知之連接裝置 附近,用來避 接頭5 7外接氮 包含有一導流 水流6 5經由一 製程廢氣7 0與 的氣化銨氣體 一*,圖一為圖〜 所示,連接袈蓄中連接裝置 51之一端(上一 28包含有一(下端開π 4 2二,口 4 1 )連接 2 8另包含有、二用來連接濕 免製程廢氣的$封結構5 3位 氣供應系統5 l攻。氮封結 板69設於接近^此外,習知 連接頭67流緩導j開口 42附 導流板69上的通 〜水流接觸後 移除。 2 8之剖面 圓柱型中 製程廢氣 式刷洗裝 於接近上 構5 3係藉 之連接裝 近,並且 過連接裝 將製程廢 放大示 空殼體 輸送管 置。習 端開口 由一連 置2 8另 提供一 置2 8的 氣70中 丄5而’習知之連接裝置2 8處理製程廢氣中的氯化銨氣 體效率極低,加上氯化銨氣體易附著在管壁上,因此易造 成連接裝置2 8上端開口 4 1以及廢氣輸送管線的堵塞。一般 來說’安裝有習知連接裝置2 8之廢氣系統約三天就必須清 洗廢氣輸送管線一次。此外,由於真空泵浦2 0兩端的壓降 若超過5 p s i則會立刻停止運作。因此為了避免造成製程臨 時中斷,就必須確保真空泵浦2 0出口端氣體輸送管線的暢 通。 發明概述531439 Case number 89126533 V. Description of the invention (4) Month Revision Please read the drawing for the intention. See Figure 2 5 1. Hollow shell line, while the other end is known near the connection device, to avoid the joint 5 7 The external nitrogen contains a diversion water flow 6 5 through a process exhaust gas 70 0 and the gasified ammonium gas 1 *, Figure 1 is a picture ~ As shown in the figure, one end of the connection device 51 (the upper 28 contains one (the lower end is open π 4 2 2 and the port 4 1) is connected to 2 8 and the other is a seal structure used to connect the wet process-free exhaust gas 5 3 Position gas supply system 5 l attack. Nitrogen sealing plate 69 is set close to ^ In addition, the conventional connector 67 flow slow guide j opening 42 attached to the flow guide 69 on the deflector 69 is removed after contact with the water flow. 2 8 section cylinder The middle process exhaust gas scrubbing is installed near the upper structure 5 3 series by the connection equipment, and the process waste is enlarged to show the empty casing conveying pipe. The opening of the learning end is connected by a continuous 2 8 and a second 2 8 5 in the gas 70, and the conventional connection device 2 8 is very low in the efficiency of the treatment of ammonium chloride gas in the process waste gas, plus the ammonium chloride gas is easy to adhere to the pipe wall, so it is easy to cause the upper end of the connection device 2 8 to open 4 1 and the blockage of the exhaust gas pipeline. Generally speaking, 'installation is known The exhaust gas system connected to the device 28 must clean the exhaust gas pipeline once every three days. In addition, if the pressure drop across the vacuum pump 20 exceeds 5 psi, it will stop immediately. Therefore, in order to avoid temporary interruption of the process, you must ensure that The unblocking of the gas pumping line at the outlet of the vacuum pump 20. Summary of the invention
531439 _案號89126533_年月日__ 五、發明說明(5) 因此本發明之主要目的在提供一種連接裝置,以解決 上述習知技術之問題。 本發明之另一目的在於提供一種不需氮封的連接裝 置,可以減緩管線的阻塞情形,進而延長管線清洗週期。 在本發明之最佳實施例中,該裝置包含有一環形殼 體,且該環形殼體包含有一上開口以及一下開口分別用來 連接該氣體輸送管線以及該刷洗裝置,且該環形殼體之側 邊設有至少一流體輸送接頭,該裝置另包含有至少一可拆 卸式多孔喷嘴,藉由一連接管路與該流體輸送接頭相連 接,使該可拆卸式多孔喷嘴固定於該上開口下方一預定距 離接近該環形殼體中心的位置。 在本發明之最佳實施例中,該連接管路係為一 L型不 鏽鋼管,且該可拆卸式多孔喷嘴上具有1 2個細孔分為上下 兩層平均分佈於該多孔喷嘴上。 依據本發明之裝置,當該氣體輸送管線中的氣體經由 該上開口通過該連接裝置時,一預定流體會經由該流體輸 送接頭傳送至該多孔喷嘴,並且經由該多孔喷嘴將該預定 流體以一 1 5 Q至4 5。角度朝該環形殼體之内壁喷灑,以延長 該氣體輸送管線的清理週期。531439 _Case No. 89126533_year month day__ V. Description of the invention (5) Therefore, the main object of the present invention is to provide a connection device to solve the problems of the conventional technology. Another object of the present invention is to provide a connection device that does not require nitrogen sealing, which can reduce the blockage of the pipeline, thereby extending the pipeline cleaning cycle. In a preferred embodiment of the present invention, the device includes a ring-shaped housing, and the ring-shaped housing includes an upper opening and a lower opening for connecting the gas delivery line and the brushing device, respectively, and a side of the ring housing There is at least one fluid transport joint on the side, and the device further includes at least one detachable porous nozzle, which is connected to the fluid transport joint through a connecting pipe, so that the detachable porous nozzle is fixed below the upper opening for a predetermined time. A distance close to the center of the annular casing. In a preferred embodiment of the present invention, the connecting pipe is an L-shaped stainless steel pipe, and the detachable porous nozzle has 12 fine holes divided into two layers, which are evenly distributed on the porous nozzle. According to the device of the present invention, when the gas in the gas transfer line passes through the connection device through the upper opening, a predetermined fluid is transferred to the porous nozzle through the fluid transfer joint, and the predetermined fluid is transferred to the porous nozzle through the porous nozzle. 1 5 Q to 4 5. Spray at an angle toward the inner wall of the annular casing to extend the cleaning cycle of the gas delivery line.
531439 _» 89126533___年月 日 修正 五、發明說明(6) 發明之詳細說明 請參閱圖三’圖三為本發明LPCVD氮化矽廢氣處理系 統配置示意圖。如圖三所示,本發明LPCVD氮化矽沈積反 ,係,一高溫氧化爐管丨〇中進行,並利用一真空泵浦2 〇將 =溫氧化爐管1 0中的壓力控制在〇 ·丨至1托耳之間。從高溫 爐管1 0所抽出之製程廢氣丨8經由一製程管線丨2以及製 程管,1 4輸送至真空泵浦2 〇。製程廢氣丨8中含有氣化銨氣 ,、氯化氫、氫氣以及微量的氮化矽固體微粒。介於製程 官ί 12以及製程管線14之間為一冷凝器(cold trap)14, 用來移除製程廢氣1 8中的固體顆粒並初步冷凝氯化銨氣 一制以免造成對真空泵浦2 0的傷害。經由冷凝器1 4處理過 $ = 廢氣1 9含有氯化銨氣體、氯化氫以及氫氣,並再由 ^ ^豕浦20轉為具有較大壓力的製程廢氣82,藉由一管徑 …呀之輸送管線8 4輸送至一濕式刷洗裝置3 0。 輸、关ί發明之接頭裝置88係直立安裝於濕式刷洗裝置30與 ^ ^嘗線84之間。值得注意的是,本發明之LPCVD氮化矽 ^ ,理系統在真空泵浦2 0出口端至濕式刷洗裝置3 0之間 送管广要任何的冷凝器,取而代之的是利用加熱帶8 6將輸 以i ί 84以及本發明之接頭裝置88包覆起來。加熱帶86可 佳實=送管線8 4的溫度加熱至3 0 0至4 0 0°C,在本發明之較 中^ ί例中,則是將溫度加熱至1 5 0°C,目的是確保廢氣 '氣化錢氣體在輪送過程中不會凝結下來。531439 _ »89126533___ year, month, day, amendment 5. Description of the invention (6) Detailed description of the invention Please refer to FIG. 3 ′ FIG. 3 is a schematic diagram of the configuration of the LPCVD silicon nitride exhaust gas treatment system of the present invention. As shown in FIG. 3, the LPCVD silicon nitride deposition process of the present invention is performed in a high-temperature oxidation furnace tube, and a vacuum pump is used to control the pressure in the = temperature oxidation furnace tube to 10 To 1 Torr. The process exhaust gas 8 extracted from the high-temperature furnace tube 10 is transmitted to a vacuum pump 20 through a process line 2 and a process tube 14. The process waste gas 8 contains ammonium gasification, hydrogen chloride, hydrogen, and a small amount of silicon nitride solid particles. Between the process officer 12 and the process line 14 is a cold trap 14 for removing solid particles in the process exhaust gas 18 and preliminarily condensing the ammonium chloride gas to avoid causing a vacuum pump 2 0 s damage. Processed by condenser 1 4 = Waste gas 19 contains ammonium chloride gas, hydrogen chloride and hydrogen, and then changes from ^ 豕 20 to process pressure exhaust gas 82 with a larger pressure, through a pipe diameter ... Line 84 is conveyed to a wet scrubbing device 30. The joint device 88 of the invention of transmission and closing is installed upright between the wet brushing device 30 and the taste line 84. It is worth noting that the LPCVD silicon nitride ^ of the present invention provides a condenser between the vacuum pump 20 outlet and the wet brushing device 30, and requires any condenser, and replaces it with a heating belt 86. It is covered with i 84 and the joint device 88 of the present invention. The heating belt 86 may be good = the temperature of the sending line 8 4 is heated to 300 to 400 ° C. In the comparative example of the present invention, the temperature is heated to 150 ° C, the purpose is Make sure that the waste gas' gasification gas does not condense during the rotation process.
531439 案號 89126533 五、發明說明(7) 修正 在,發明之5實施例t,加熱帶86亦可以用加 套(heating jacket)取代。需強調的是,由於本發明 LPCVD氮化石夕廢介氣處理系統配置本發明之接頭裂置^,因 此可以洎=泵浦20出口端至至式刷洗裝 冷凝器,☆了節省成本,同時也避免了冷凝器堵塞的 形。 月 請參閱圖:,圖四為本發明 一 意圖。如前所述:ί發明之連接裝置88係用來。 浦出口端1體輸达及廢氣 示,連接裝置8 8包含右_士>山〜 如圖四所 送接頭92、一 L型連接管路9二一環形殼體一流體輪 9 6。環形殼體9 0的直立高产為可拆/式多孔噴嘴 縮上開口 1 2 5以及一下開〇 ] 9 兄丨丨田::f 匕各有一漸 以及濕式刷洗裝置。上開口 1 25的直徑為3付,而丁 t線 直徑為4吋。流體輸送接_ q ^ 二 下開口的 ,、+ 钱碩9」係δ又於%形殼體9 0之側邊 上,對外連接一 >’,L體輪送管路丨〇 〇,對一 路9 4。可拆卸式多孔噴喈q ώ T刑 、連接Li連接管 開口】Μ下方约8八八Z ^猎型連接管路94固定於上 明之較佳實施例中,環开,妒_ ± 叼伹置在本發 I, (carbon s t e e 1 ^ ^ (SS316)^^ 内壁。然❿,本發明於t 無孔洞或突起之 蝕之類似堅硬材質皆可::J明土述之材質’任何对腐 J作為本發明%形殼體9 〇之材料,例531439 Case number 89126533 V. Description of the invention (7) Amendment In the fifth embodiment of the invention, the heating belt 86 can also be replaced by a heating jacket. It should be emphasized that, because the LPCVD nitride gas waste gas treatment system of the present invention is configured with the joint of the present invention, it can be 洎 = pump 20 outlet end to the brush scrub condenser, saving costs, and also Avoid clogging the condenser. Please refer to Figure: Figure 4 is the intention of the present invention. As mentioned before: The invention of the connecting device 88 is used. The connection and exhaust gas at the exit end of the Pu body is shown. The connection device 8 8 includes a right-side connector. As shown in Fig. 4, the connector 92, an L-shaped connection pipe 921, a ring casing, and a fluid wheel 96 are provided. The upright and high-yield production of the annular housing 90 is a detachable / type porous nozzle. The upper opening 1 2 5 and the lower opening 0] 9 Brother 丨 丨 :: f each has a gradual and wet brushing device. The diameter of the upper opening 125 is 3 pairs, and the diameter of the T-line is 4 inches. The fluid conveying connection _ q ^ Two openings, + Qianshuo 9 ″ system δ is connected to the side of the% -shaped housing 90, and is connected to a > ', L body rotary pipeline 丨 〇〇, the All the way 9 4. Detachable multi-hole spray gun (Freezing, connecting to the connection port of Li connection pipe)] about 88.8Z ^ hunting type connection pipe 94 is fixed in the preferred embodiment of Shangming, ring open, jealous _ ± set In the present article I, (carbon stee 1 ^ ^ (SS316) ^^ inner wall. However, the present invention can be used with similar hard materials without holes or protrusions :: J The material described in Mingtu 'any pair of rot J As a material of the% -shaped casing 9 of the present invention, for example
531439 案號 89126533 年 月 曰 修正 五、發明說明(8) 如合金。 在圖四下方處顯示本發明可拆卸式多孔喷嘴9 6之放大 圖。由圖中可清楚的看見多孔喷嘴9 6係類似一金字塔型並 藉由螺紋部份9 9鎖緊固定於L型連接管路9 4之末端。1 2個 細孔9 8分為上下兩層(排)平均分佈於多孔喷嘴9 6上,較佳 為上層六個、下層六個。在本發明之較佳實施例中,細孔 98係為圓形孔洞,孔徑約為0. 2至2mm之間。經由上層細孔 9 8所喷灑出之水柱與水平面的角度應小於一特定角度6» ,531439 Case No. 89126533 Month, Amendment V. Description of Invention (8) Such as alloy. An enlarged view of the detachable porous nozzle 96 according to the present invention is shown at the bottom of FIG. It can be clearly seen from the figure that the multi-hole nozzle 9 6 is similar to a pyramid shape and is fastened and fixed to the end of the L-shaped connection pipe 9 4 by a threaded portion 9 9. The 12 fine holes 98 are divided into two upper and lower layers (rows) evenly distributed on the porous nozzle 96, preferably six in the upper layer and six in the lower layer. 2 至 2mm 之间。 In a preferred embodiment of the present invention, the pores 98 are circular holes, the diameter of about 0.2 to 2mm. The angle between the water column sprayed through the upper pores 98 and the horizontal plane should be less than a specific angle 6 »,
0較佳範圍介於1 5。至4 5之間。需注意的是,經由上層細 孔9 8所喷灑出之水柱不可直接朝上喷灑,也就是不可朝上 開口 1 2 5喷灑,以避免水氣累積於前端廢氣輸送管線中。 此外,細孔9 8的數量、形狀以及大小,可視製程狀態的改 變而隨之調整,例如,當製程廢氣流量增加時,可增加分 佈於多孔喷嘴9 6上的細孔9 8數量至2 0個,甚至2 4個,同時 縮小細孔9 8的孔徑以增加喷灑水流的水壓。A preferred range of 0 is between 15. Between 4 and 5. It should be noted that the water column sprayed through the upper pores 9 8 cannot be sprayed directly upwards, that is, the openings 1 2 5 cannot be sprayed upwards to avoid water vapor accumulating in the front-end exhaust gas transmission pipeline. In addition, the number, shape, and size of the pores 98 can be adjusted according to changes in the process state. For example, when the flow of the exhaust gas in the process increases, the number of pores 9 8 distributed on the porous nozzle 96 can be increased to 20 , Even 2 or 4 at the same time, reducing the pore size of 9 8 to increase the water pressure of the spraying water flow.
在本發明之較佳實施例中,流體輸送管路1 0 0係用來 提供一固定壓力之水流,其包含有水泵浦1 0 3、一控制閥 101,例如電磁閥(solenoid valve)以及一旁支管路(by p a s s ) 1 0 2。水溫為室溫,然而可視需要使用溫水或熱水。 旁支管路1 0 2係藉由一手動閥1 0 2 a控制通過的水流量。為 了避免多孔喷嘴9 6上的細孔9 8被阻塞,旁支管路1 0 2需經 常具備有一固定小流量之水流,因此手動閥1 〇 2係為可控In a preferred embodiment of the present invention, the fluid delivery pipeline 100 is used to provide a fixed pressure water flow, which includes a water pump 103, a control valve 101, such as a solenoid valve, and A side branch pipe (by pass) 1 0 2. The water temperature is room temperature, but warm or hot water can be used if necessary. The bypass line 10 2 is controlled by a manual valve 10 2 a for the flow of water passing through it. In order to prevent the fine holes 98 in the porous nozzle 96 from being blocked, the side branch pipe 10 2 must always have a fixed small flow of water, so the manual valve 1 02 is controllable.
第12頁 531439 _案號 89126533___年月日_修正 五、發明說明(9) "" - 制流量大小之閥’例如球型閥(g 1 0 b a 1 v a 1 v e )或碟闕 (butterfly valve)。當該氣體輸送管線中的氣體i2〇經由 上開口 1 2 5通過連接裝置8 8時,一表示廢氣排出之爐管atm 壓力訊號1 0 5將會傳送至控制閥1 〇丨,同時使控制閥1 〇 啟,此時一具有固定水壓之水流會經由流體輸送接頭9 2以 及L型連接管路9 4傳送至多孔喷嘴9 6,並且經由多孔喷嘴 9 6上的孔洞9 8將水流以一 1 5。至4 5。角度朝環形殼體9 0之光 滑内壁喷灑。壓力訊號1 〇 5係由爐管上的壓力計直接傳送 至控制閥1 0 1上做回饋控制(feedback control)。 相較於習知技術,本發明不需氮封的連接裝置,可以 減緩管線的阻塞情形,進而延長管線清洗週期。此外,由 於本發明LPCVD氮化矽廢氣處理系統配置本發明之接頭裝 置8 8,因此可以省略真空泵浦2 〇出口端至至濕式刷洗裝置 3 0之間的冷凝器,除了節省成本,同時也避免了冷凝器堵 塞的情形。利用本發明之接頭裝置8 8,可使得清理週期由 原先的每週兩次延長至約每三至六個月一次。 以上所述僅本發明之較佳實施例,凡依本發明申請專利範 圍所做之均等變化與修飾,皆應屬本發明專利之涵蓋範 圍0Page 12 531439 _Case No. 89126533 _ Month and Day _ Amendment V. Description of the Invention (9) " "-Valves for regulating the flow rate, such as ball valves (g 1 0 ba 1 va 1 ve) or dishes ( butterfly valve). When the gas i2〇 in the gas transmission line passes through the upper opening 1 2 5 and passes through the connecting device 8 8, a pressure signal 1 0 5 of the furnace tube atm indicating exhaust gas emission will be transmitted to the control valve 1 〇 丨10 〇 At this time, a water flow with a fixed water pressure will be transmitted to the porous nozzle 96 through the fluid transfer joint 9 2 and the L-shaped connection pipe 9 4, and the water flow will be passed through the hole 9 8 on the porous nozzle 96. 1 5. To 4 5. The angle is sprayed towards the light sliding inner wall of the annular housing 90. The pressure signal 105 is directly transmitted from the pressure gauge on the furnace tube to the control valve 101 for feedback control. Compared with the conventional technology, the present invention does not require a nitrogen-sealed connection device, which can reduce the blockage of the pipeline, thereby extending the pipeline cleaning cycle. In addition, since the LPCVD silicon nitride exhaust gas treatment system of the present invention is configured with the joint device 88 of the present invention, the condenser between the vacuum pump 20 outlet end and the wet brushing device 30 can be omitted, in addition to saving costs, it also Avoid the situation that the condenser is blocked. With the joint device 88 of the present invention, the cleaning cycle can be extended from the original twice a week to about once every three to six months. The above are only the preferred embodiments of the present invention. Any equal changes and modifications made in accordance with the scope of the patent application of the present invention shall fall within the scope of the patent of the present invention.
第13頁 531439 _案號89126533_年月日__ 圖式簡單說明 圖示之簡單說明 圖一為習知LPCVD氮化矽廢氣處理系統配置示意圖。 圖二為圖一中連接裝置之剖面放大示意圖。 圖三為本發明LPCVD氮化矽廢氣處理系統配置示意 圖。 圖四為本發明連接裝置之剖面放大示意圖。 圖示之符號說明 10 氮 化 矽 高溫氧化爐管 12 製 程 管 線 14 冷 凝 器 16 製 程 管 線 18 製 程 廢 氣 19 製 程 廢 氣 20 真 空 泵 浦 22 送 管 線 23 製 程 廢 氣 24 冷 凝 器 25 製 程 廢 氣 26 ¥m 送 管 線 28 接 頭 裝 置 30 濕 式 刷 洗裝置 41 上 端 開 a 42 下 端 開 V 51 中 空 殼 體 53 氮 封 結 構 55 氮 氣 供 應系統 57 連 接 頭 65 水 流 67 連 接 頭 69 導 流 板 70 製 程 廢 氣 82 製 程 廢 氣 84 送 管 線 86 加 熱 帶 88 接 頭 裝 置Page 13 531439 _Case No. 89126533_Year Month Day__ Brief description of the diagram Brief description of the diagram Figure 1 shows the configuration of a conventional LPCVD silicon nitride exhaust gas treatment system. FIG. 2 is an enlarged schematic cross-sectional view of the connecting device in FIG. 1. Figure 3 is a schematic configuration diagram of the LPCVD silicon nitride exhaust gas treatment system of the present invention. FIG. 4 is an enlarged schematic cross-sectional view of a connecting device according to the present invention. Explanation of symbols in the diagram 10 Silicon nitride high temperature oxidation furnace tube 12 Process line 14 Condenser 16 Process line 18 Process exhaust 19 Process exhaust 20 Vacuum pump 22 Send line 23 Process exhaust 24 Condenser 25 Process exhaust 26 ¥ m Send line 28 Connector Device 30 Wet scrubbing device 41 Upper end open a 42 Lower end open V 51 Hollow case 53 Nitrogen seal structure 55 Nitrogen supply system 57 Connector 65 Water flow 67 Connector 69 Baffle 70 Process exhaust gas 82 Process exhaust gas 84 Feed line 86 plus Tropical 88 joint device
第14頁Page 14
531439 年 案號 89126533 月 曰 修正 圖式簡單說明 90 直立中空環形殼體 92 流體輸送接頭 94 L型連接管 96 可拆卸式多孔喷嘴 98 細孑L 99 螺紋部份 100 流體輸送管路 101 控制閥 102 旁支管路 102a 手動閥 103 水泵浦 120 製程廢氣 125 上開口 126 下開口531439 Case No. 89126533 Modified diagram of the month Simple explanation 90 Upright hollow ring housing 92 Fluid delivery joint 94 L-shaped connecting pipe 96 Removable porous nozzle 98 Fine L 99 Threaded part 100 Fluid delivery pipe 101 Control valve 102 By-pass line 102a Manual valve 103 Water pump 120 Process exhaust gas 125 Upper opening 126 Lower opening
第15頁Page 15
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