TW509829B - Method and system for preventing the transmission pipeline of a process from backfill - Google Patents
Method and system for preventing the transmission pipeline of a process from backfill Download PDFInfo
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發明領域: 本發明係關於一種避免一製程反應室之輪送总& 回流(backfill )的方法和系統,尤指一種藉由二斷If 在製程設備中之一管線上的一流量計(MFC )的流 向,並對該管線施以關閉或開通控制的方法和系統 發明背景: 在一些相關之技術領域中,例如半導體積體 之化學氣相沈積(CVD)、電漿蝕刻(ΡΕ)或其他製以柱 及製造平面顯示器(flat panei displays)和硬 器(hard disk drives )等產品之製程,常使用流量叶 (mass flow controller ;MFC)來控制在一特定製程中 所需之一流體之一特定流動量。 $ 流量計可以感應(sens i ng )流過該流量計之流 (f 1 ow )並且視需求改變或控制該流,以便達成控制傳送 至該特定製程之該流體的量的目的。對該流的感應係為戶斤 使用流體的種類和用來感應該流量之物理作用(phy s i ca 1 effects )的函數。而用來感應該流量(mass flow)的物 理作用的類型有許多種,例如可使用絕對和/或差壓力變 化(absolute and/or differential pressure changes )、溫度差(temperature differential)、光吸收作用Field of the Invention: The present invention relates to a method and system for avoiding total & backfill of a process reaction chamber, especially a flow meter (MFC Method and system for controlling the flow direction of the pipeline and closing or opening the pipeline Background of the invention: In some related technical fields, such as chemical vapor deposition (CVD), plasma etching (PE) or other The process of manufacturing columns and manufacturing products such as flat panei displays and hard disk drives often uses mass flow controllers (MFCs) to control one of the fluids required in a particular process. Specific flow. $ The flow meter can sense the flow (f 1 ow) flowing through the flow meter and change or control the flow as needed to achieve the purpose of controlling the amount of the fluid delivered to the particular process. The response to this flow is a function of the type of fluid used by the household and the physical effects (phys i ca 1 effects) used to sense the flow. There are many types of physical effects used to sense the mass flow. For example, absolute and / or differential pressure changes, temperature differential, and light absorption can be used.
509829 五、發明說明(2) (light absorption)或動量變化(momentum change) 來測量。 如圖一所示,一種典型之用來感應流量(mass fl〇w )的物理作用’乃係測5:為該流體流(t h e f 1 u i d f 1 o w ) 所流經之熱感應為線圈(t h e r in a 1 s e n s o r c o i 1 s )的上游 線圈R u與下私線圈R d之間的溫度差△ τ,而該流量計之感 應器所得之測量值V0即會產生一對應的流動控制信號 (flow control signal ),來控制該流體的流速。 就半導體積體電路製程而言,在晶圓尺寸和製程複雜 度與日漸增的情況下,製作積體電路時所使用之氣體的純 度和流量就顯得相當地重要。於是,乃將一流量計安插在 供應該製程設備所需之一反應氣體的一管線(p i pe丨丨ne ) 中以便控制該反應氣體在製程步驟中之流速。 今以圖一(係為連接至一製程反應室之氣體輸送管線 的部份示意圖)來說明該製程反應室在輸入所需反應氣體 或是進行流量計校正時所遭遇的氣體回流倒灌(backfin )的問題。 如圖一所不,该反應室10包括有Δ、B、c、D和E:五個 氣體源(gaS tray )各別透過相對應之管線a、b、c、d辛 e匯集至一連接到該反應室l〇之管線f,在該管線f上有-509829 V. Description of the invention (2) (light absorption) or momentum change (momentum change) to measure. As shown in Figure 1, a typical physical action used to sense the flow (mass fl0w) is the measurement 5: the thermal induction through which the fluid flow (thef 1 uidf 1 ow) flows is a coil (ther in a 1 sensorcoi 1 s), the temperature difference Δ τ between the upstream coil Ru and the lower private coil Rd, and the measurement value V0 obtained by the sensor of the flow meter will generate a corresponding flow control signal (flow control signal ) To control the flow rate of the fluid. As far as the semiconductor integrated circuit manufacturing process is concerned, the purity and flow rate of the gases used in the fabrication of integrated circuits have become very important in the context of increasing wafer size and process complexity. Therefore, a flow meter is inserted in a pipeline (pipe, ne) that supplies a reaction gas required by the process equipment in order to control the flow rate of the reaction gas in the process steps. Now use Figure 1 (a partial schematic diagram of the gas delivery pipeline connected to a process reaction chamber) to illustrate the backflow of gas that the process reaction chamber encounters when entering the required reaction gas or performing flowmeter calibration. The problem. As shown in FIG. 1, the reaction chamber 10 includes Δ, B, c, D, and E: five gas sources (gaS trays) are collected through a corresponding line a, b, c, and d, respectively, to a connection. The line f to the reaction chamber 10 has-
509829 五、發明說明(3) 最終閥(final valve ) 7,並藉由該最終閥7來控制該等 氣體源之氣體輸入該反應室1 0。 在該等管線a、b、c、d和e上各別依序具有一手動閥 (manual valve) al 、bl 、cl 、dl 和 el 、一 壓力言周節器 (regulator ) a2、b2、c2、d2 和e2、一 過濾器(filter )a3、b3、c3、d3 和 e3、一 上游閥(UpStream valve) a4、b4、c4、d4 和e4、一 流量計(MFC ) a5、b5、c5、d5 和e5 以及一下游閥(downstream valve ) a6、b6、c6、d6 和e 6 〇 該等A、B、C、D和E五個氣體源之氣體壓力乃視製程 所需而各不相同和/或相同,舉例而言,該A和b氣體源之 氣體壓力皆為l5pSi,該C、d和E氣體源之氣體壓力皆為 35psi °,該製程之反應控制機台(未顯示)發出訊號欲 ,將該C氣體輪入該反應室丨〇時(假設此時其餘氣體源之 管線皆關閉),該C氣體流經該管線c,通過該手動閥cl、 該壓力調節器c2、該過濾器C3、該上游閥C4、該流量計c、5 =及該下游閥c6,並進入該管線f而抵達該最終閥7。在°^ 常的情況下,該最終閥7亦會從該反應控制機台接收到♦正 開的訊號,而讓該C氣體順利輸入該反應室丨〇 (者 ^ 為零)。 田$ ^力 但有時,該最終閥7因電子訊號傳遞差池或機械作動509829 V. Description of the invention (3) Final valve 7, and the gas from the gas source is controlled to enter the reaction chamber 10 by the final valve 7. A manual valve al, bl, cl, dl, and el, and a pressure regulator a2, b2, and c2 are sequentially provided on the pipelines a, b, c, d, and e, respectively. D2 and e2, a filter a3, b3, c3, d3 and e3, an upstream valve (UpStream valve) a4, b4, c4, d4 and e4, a flow meter (MFC) a5, b5, c5, d5 and e5 and a downstream valve (a6, b6, c6, d6, and e6) The gas pressures of the five gas sources A, B, C, D, and E are different depending on the process requirements and / Or the same, for example, the gas pressures of the A and b gas sources are 15 pSi, the gas pressures of the C, d, and E gas sources are all 35 psi °, and the reaction control machine (not shown) of the process sends a signal When the C gas is turned into the reaction chamber (assuming that the pipelines of other gas sources are closed at this time), the C gas flows through the pipeline c, passes the manual valve cl, the pressure regulator c2, and the filter Device C3, the upstream valve C4, the flow meter c, 5 = and the downstream valve c6, and enter the pipeline f to reach the final valve 7. Under normal circumstances, the final valve 7 will also receive a signal of ♦ positive opening from the reaction control machine, so that the C gas can be smoothly input into the reaction chamber (or ^ is zero).田 $ ^ 力 But sometimes, the final valve 7 is actuated due to a difference in electronic signal transmission or mechanical
第6頁 509829 五、發明說明(4) 不良,如氣管破裂或未插接,而沒有開通時,所欲輸入之 壓力為3 5 p s i的該C氣體就停滯在該下游閥c 6和該最終閥7 之間。在未知情的情形下,如果此時又執行流通該管線3 之壓力為15psi的該A氣體至該反應室10或是校正 (calibrate)該管線a之該流量計a5,則停滯在該丁游閥 c6和該最終閥7之間的較高壓之該c氣體就會往較低壓之該 管線a回流倒灌(backfill)而導致該管線a被他種氣體 (即該C氣體)污染。 當管線有氣體回流倒灌問題發生時,不但要耗費很多 額外時間和成本來清理恢復該管線之原狀,且亦可能因發 現為時已晚,倒灌的他種氣體已回流至該管線之氣體源 處’造成同樣透過該氣體源供應所需氣體之其他反應室的 相關管線也被污染,而影響其他反應室之反應氣體的純 度。因此,如何預防和控制在製程管線輸 的問題,便成為當前製程一個重要的課題。出見之上31 發明概述: 制本發明之主要目的,即是在提供一種藉由判斷安插在 士程設備中之一管線上的一流量計(MFC )的流體流向, 亚對該管線施以關閉或開通控制的方法,以避免製程中之 輪送管線發生回流倒灌(backfill )的問題。Page 6 509829 V. Description of the invention (4) Defective, such as when the trachea is ruptured or not plugged in but not opened, the C gas at a pressure of 3 5 psi will be stagnated at the downstream valve c 6 and the final Between valve 7. Under unknown circumstances, if at this time the A gas with a pressure of 15 psi in the pipeline 3 is passed to the reaction chamber 10 or the flow meter a5 in the pipeline a is calibrated, it will stagnate in the Ding You The higher pressure of the c gas between the valve c6 and the final valve 7 will be backfilled to the lower pressure line a, causing the line a to be contaminated with another gas (ie, the C gas). When the pipeline has a problem of backflow and gas backflow, not only will it take a lot of extra time and cost to clean up and restore the original state of the pipeline, but it may also be because it is too late to find that other gases have been backflowed to the gas source of the pipeline. 'Cause the relevant pipelines of other reaction chambers that also supply the required gas through the gas source are also contaminated, which affects the purity of the reaction gases in other reaction chambers. Therefore, how to prevent and control the problem of pipeline transportation has become an important issue in the current process. See above 31. Summary of the invention: The main purpose of the present invention is to provide a flow meter (MFC) by judging the flow direction of a flow meter (MFC) installed on a pipeline in Shi Cheng equipment. Close or open the control method to avoid the backfill problem of the rotary pipeline in the manufacturing process.
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五、發明說明(5) 本發明之另一目的,即是在提供一種具有一流量計控 制面板(M F C c ο n t r ο 1 b 〇 a r d )和螺線管閥(s 〇 1 e n 〇 土己 v a 1 v e )的輸送管線系統’以防止另一管線内之他種氣體 回流。 本發明揭示一種用來避免一製程反應室之輸送管線發 生回流的方法’其中’複數個輸送流體的管線係經匯集^ 接至該反應室’以供給該反應室進行該製程時所需之不同 的流體;該方法係藉由判斷各別設置在該等複數個管線上 的一流量計(MFC )中的流體流向,來對該等管線施以關 閉或開通的控制。 在本發明方法之一實施例中,提供一控制面板 (control board) ’來測知其相對應之該流量計中的流 體流向。當該控制面板測知該流量計中的流體流向改變 時,即傳遞指令驅動一控制閥關閉該流量計所在之該管線 的一上游閥和/或一下游閥。 在上述本發明之一較佳實施態樣中,該控制閥係為一 螺線管閥(s ο 1 e η 〇 i d v a 1 v e ),該流量計係由一熱感應器 所構成。因此,當該熱感應器流量計中的流體流向改變 時’該熱感應器流量計的讀數(reading )係為一負值, 而該控制面板係可設定一特定負電壓值(其可依所需來作 調整變動)作為控制基準點,當該控制面板測知到該熱感5. Description of the invention (5) Another object of the present invention is to provide a flow meter control panel (MFC c ο ntr ο 1 b 〇ard) and a solenoid valve (s 〇 1 en 〇 土 己 va 1 ve) transmission line system 'to prevent other gases in another line from flowing back. The present invention discloses a method for avoiding the backflow of the transportation pipeline of a reaction chamber in a process, in which 'a plurality of pipelines for transporting fluids are collected ^ and connected to the reaction chamber' to supply the reaction chamber with the difference required for the process The method is to control the closing or opening of the pipelines by judging the flow direction of the fluid in a flow meter (MFC) provided on the plurality of pipelines. In one embodiment of the method of the present invention, a control board is provided to detect the flow direction of the fluid in the flow meter corresponding to the control board. When the control panel detects a change in the fluid flow direction in the flowmeter, it transmits a command to drive a control valve to close an upstream valve and / or a downstream valve of the pipeline where the flowmeter is located. In a preferred embodiment of the present invention, the control valve is a solenoid valve (s ο 1 e η ω d v a 1 v e), and the flow meter is composed of a thermal sensor. Therefore, when the fluid flow direction in the thermal sensor flowmeter changes, the reading of the thermal sensor flowmeter is a negative value, and the control panel can set a specific negative voltage value (which can be set according to Need to make adjustments and changes) as the control reference point, when the control panel detects the thermal
第8頁 509829 五、發明說明(6) ---------- 應器流量計的讀數不大於或小於該特定負電壓值時 驅動-個螺線管閥關閉該管線的該上游閥或該下游閥、」 者是驅動兩個螺線管閥各別關閉該上游閥和該下游閥。 再者,本發明亦揭示一種用來避免—製程反應室 送管線發生回流的系統,其中,該等管線上各別設置有一 流量計(MFC ),該系統係包括一流量計控制面板(MFc control board)和一控制閥。該MFC控制面板係用來測知 相對應之該流量計中的流體流向改變,並傳遞出一關閉指 令,該控制閥係接收該MFC控制面板所送出之該關閉指曰 令,並關閉該流量計所在之該管線的一上游閥和/或二 游閥。 〆 在本發明系統之一較佳實施態樣中,該控制閥係為— 螺線管閥(solenoid valve ),該流量計係由一熱感廡哭 所構成。當該熱感應器流量計中的流體流向改變時,該熱 感應器流量計的讀數(reading )係為一負值,而該控制”' 面板係可設定一特定負電壓值(其可依所需來作調整變動 )作為控制基準點,當該控制面板測知到該熱感應界流量 計的讀數不大於或小於該特定負電壓值時,則即驅動一個 螺線管閥關閉該管線的該上游閥或該下游閥,或者是驅動 兩個螺線管閥各別關閉該上游閥和該下游閥。 發明之詳細說明:Page 509829 V. Description of the invention (6) ---------- When the reading of the reactor flow meter is not greater than or less than the specific negative voltage value, a solenoid valve is driven to close the upstream of the pipeline. The valve, or the downstream valve, is one that drives two solenoid valves to close the upstream valve and the downstream valve, respectively. In addition, the present invention also discloses a system for avoiding backflow of the pipelines in the process chamber. The pipelines are respectively provided with a flow meter (MFC). The system includes a flow meter control panel (MFc control). board) and a control valve. The MFC control panel is used to detect the corresponding change in the fluid flow direction in the flowmeter, and transmits a closing instruction. The control valve receives the closing instruction sent by the MFC control panel, and closes the flow. An upstream valve and / or a two-way valve of the pipeline are considered. 〆 In a preferred embodiment of the system of the present invention, the control valve is a solenoid valve, and the flow meter is constituted by a thermal sensor. When the flow direction of the fluid in the thermal sensor flowmeter changes, the reading of the thermal sensor flowmeter is a negative value, and the control '' panel can set a specific negative voltage value (which can be set according to (Need to make adjustment and change) as the control reference point. When the control panel detects that the reading of the thermal sensing flowmeter is not greater than or less than the specific negative voltage value, it drives a solenoid valve to close the pipeline. The upstream valve or the downstream valve, or the two solenoid valves are driven to close the upstream valve and the downstream valve respectively. Detailed description of the invention:
第9頁 509829Page 9 509829
五、發明說明(7) 以前述圖/所示之熱感應器流量計以及圖二所示之氣 體輸送管線示意圖來舉例說明本發明的方法。 ;; 請參見圖三,其係為本發明之連接至一製程反應室之 氣體輸送管線的部份示意圖,其中除了 MFC控制面板 (control board) a8、b8、c8、d8 和 e8 以及螺線管閥 (solenoid valve ) a91 、a92 、b91 、b92 、c9l 、C92 、 d91、d92 、e91和e92以外,其餘之元件係與圖二所示者 相同,故標號亦相同。 一首先,如圖三所示,當該製程之反應控制機台(未顯 不)發出訊號欲先將該C氣體輸入該反應室丨〇時(假設此 時其餘氣體源之管線皆關閉),該C氣體流經該管線。,通 過該手動閥cl、該壓力調節器c2、該過濾器c3、該上游閥 C4:該流量計c5以及該下游閥c6,並進 抵達 勃π旛-、古曰斗、ς '工制面板c8會測知到該流量計(一 熱感應益流罝计)之電壓測量值ν〇 一大於零之數 值,顯示氣體的流向是從一卜、、检 〜 動。在正常的情況下,該最:主;下游闊的方向流 號,而讓該C氣體順利輪入兮反伐會接收到打開的机 、。 八5亥反應室1 〇 (當時壓力為零 但若該最終閥7因電子性或機械 ^生知作因素而未開通V. Description of the invention (7) The method of the present invention will be exemplified by the schematic diagram of the thermal sensor flowmeter shown in the figure / shown above and the gas transmission pipeline shown in figure 2. ; Please refer to FIG. 3, which is a partial schematic diagram of a gas transmission pipeline connected to a process reaction chamber of the present invention, except for MFC control board a8, b8, c8, d8, and e8 and solenoid Valves (solenoid valve) a91, a92, b91, b92, c9l, C92, d91, d92, e91 and e92, the rest of the components are the same as those shown in Figure 2, so the same reference numerals. First, as shown in Figure 3, when the reaction control machine (not shown) of the process sends a signal to input the C gas into the reaction chamber (assuming that the pipelines of other gas sources are closed at this time), The C gas flows through the pipeline. , Through the manual valve cl, the pressure regulator c2, the filter c3, the upstream valve C4: the flowmeter c5 and the downstream valve c6, and reach the π 幡-, Gu Yuedou, ς 'work panel c8 The voltage measurement value ν〇 of this flow meter (a thermal induction flow meter) will be measured, a value greater than zero, indicating that the flow of the gas is from one to one. Under normal circumstances, the most: main; downstream wide direction flow number, and let the C gas smoothly turn into the anti-cutting will receive the open machine. Eighty-five Hai reaction chamber 10 (at that time the pressure is zero, but if the final valve 7 is not opened due to electronic or mechanical factors)
509829 五、發明說明(8) 時,所欲輸入之[力為35psi的該C氣體就停滯在該下游閥 c6和該最終閥7之間,此日守该MFC控制面板“會測知到該流 量計C5之電壓測量值V0,係為一等於零之數值,顯示該^ 氣體的動向為一停滯狀態。在未知情的情形下,此時又執 行流通該管線a之壓力為15psi的該A氣體至該反應室1〇, 或是校正該管線a之該流量計a5,則停滯在該下游閥c6和 該最終閥7間之較冋壓的该C氣體,就開始往較低壓、開通 的該管線a回流倒灌(backf i 11 ),先經過該管線a之該下 游閥a6,之後流過該流量計a5,並將接著繼續往該上游閥 a4方向倒灌。 當回流之遠C氣體流過該流量計a5時,由於此時氣體 的流向是從一下游閥往一上游閥的方向流動,該M F C控制 面板a8就會測知到該流量計a5所送出之電壓測量值(f 1 〇w output) V0是一小於零之數值。於是,該MFC控制面板a8 即會傳遞信號,驅動該等螺線管閥a 9 1、a 9 2分別關閉該管 線a之該上游閥a 4和該下游閥a 6,以阻止該C氣體繼續往該 上游閥a 4以上的方向倒灌回流。 如此一來,即有效地控制和防止該管線a整條被他種 氣體(即該C氣體)倒灌污染的嚴重後果,至於被阻滯在 該管線a之該上游閥a4和該下游閥a6之間的該污染C氣體, 則只要經稍微的通氣處理(purge )即可清除掉。而且, 該MFC控制面板a8是接收到該流量計a5送出之電壓測量值509829 5. In the description of the invention (8), the [gas with a force of 35 psi of the C gas stagnates between the downstream valve c6 and the final valve 7. On this day, the MFC control panel will detect that The voltage measurement value V0 of the flow meter C5 is a value equal to zero, showing that the movement of the gas is a stagnant state. Under unknown circumstances, the A gas with a pressure of 15 psi flowing through the pipeline a is then executed. To the reaction chamber 10, or to calibrate the flow meter a5 of the pipeline a, the relatively high pressure C gas that is stagnated between the downstream valve c6 and the final valve 7 starts to go to a lower pressure and open. The pipeline a backflow backfill (backf i 11), first passes through the downstream valve a6 of the pipeline a, then flows through the flow meter a5, and will then continue to backflow to the upstream valve a4. When the returning gas flows through C In the flow meter a5, since the gas flow direction is from a downstream valve to an upstream valve at this time, the MFC control panel a8 will detect the voltage measurement value (f 1 〇w) sent by the flow meter a5. output) V0 is a value less than zero. Therefore, the MFC control panel a8 will A signal is transmitted to drive the solenoid valves a 9 1 and a 9 2 to close the upstream valve a 4 and the downstream valve a 6 of the pipeline a, respectively, to prevent the C gas from continuing in a direction above the upstream valve a 4 In this way, the serious consequence of the pipeline a being contaminated by other gas (ie, the C gas) is effectively controlled and prevented. As for the upstream valve a4 and the downstream which are blocked in the pipeline a The contaminated C gas between the valves a6 can be removed only after a slight purge. Moreover, the MFC control panel a8 receives the voltage measurement value sent by the flow meter a5.
509829 五、發明說明(9) V0 ’再利用該等螺線管閥對該上游閥a4和該下游閥a6進行 關閉動作,由於並未直接或間接傳遞信號給該流量計&5, 因此不會對該流量計a5造成干擾。 圖四係顯示該MFC控制面板a8與該等螺線管閥a9 1、 a92的傳訊作動電路示意圖,其中,該MFC控制面板&8可視 需要設定一特定負電壓值來作為該MFC a5讀數的控制基準 點’即利用如圖四所示之R1和R2可調節電阻來調整設定。 當該MFC控制面板a8讀取該流量計a5流送出的讀數(即該 電壓測量值V0 ),進行比較,並測知該v〇值不大於該MFC 控制面板a8之的該特定負電壓值時(或亦可設定成小於該 2寺定負電壓值),該肝C控制面板a8立即透過電路傳遞信 號’令一繼電器r ( 1 ay )作動而使分別驅動該等螺線管 閥a91、= 92打開該管線a之該上游閥a4和該下游閥a6的20 直流電壓形成斷路,如此一來,該上游閥a4和該下游閥a6 就被關閉’而達成阻止他種氣體繼續回流倒灌。 士若該MFC控制面板a8讀取該V0值是大於該特定負電壓 值時,該MFC控制面板a8就不會命令該繼電器R作動,如 此,2 4 V直机電壓仍是通路而驅動該等螺線管閥a 9 j、a 9 2 分別打開該管線a之該上游閥a4和該下游閥a6,使該管線a 暢通。 509829509829 V. Description of the invention (9) V0 'Reuse the solenoid valve to close the upstream valve a4 and the downstream valve a6, because the signal is not directly or indirectly transmitted to the flow meter & 5, so it is not Will cause interference to the flow meter a5. Figure 4 shows a schematic diagram of the communication operation circuit of the MFC control panel a8 and the solenoid valves a9 1 and a92. Among them, the MFC control panel & 8 can set a specific negative voltage value as the reading of the MFC a5. The control reference point 'uses the adjustable resistors R1 and R2 shown in Figure 4 to adjust the setting. When the MFC control panel a8 reads the reading sent by the flow meter a5 (that is, the voltage measurement value V0), compares it, and determines that the value of v0 is not greater than the specific negative voltage value of the MFC control panel a8 (Or it can be set to be less than the 2 negative voltage values), the liver C control panel a8 immediately transmits a signal through the circuit 'makes a relay r (1 ay) to actuate to drive the solenoid valves a91, = 92 opens the DC voltage of the upstream valve a4 and the downstream valve a6 of the pipeline a to form an open circuit. In this way, the upstream valve a4 and the downstream valve a6 are closed ', so as to prevent other gases from continuing to flow back and back. If the MFC control panel a8 reads that the V0 value is greater than the specific negative voltage value, the MFC control panel a8 will not command the relay R to operate. In this way, the direct voltage of 2 4 V is still the path to drive such. The solenoid valves a 9 j and a 9 2 respectively open the upstream valve a4 and the downstream valve a6 of the pipeline a to make the pipeline a unblocked. 509829
509829 圖式簡單說明 藉由以下詳細之描述結合所附圖式,將可輕易地了解 上述之技術内容及本發明之諸多優點,其中: 圖一,係為一典型之熱感應器線圈之原理示意圖; 圖二,係為一習知技術之連接至一製程反應室之氣體輸送 管線的部份示意圖;509829 Brief description of the drawings The above-mentioned technical content and many advantages of the present invention can be easily understood through the following detailed description combined with the attached drawings, of which: Figure 1 is a schematic diagram of a typical thermal sensor coil Figure 2 is a partial schematic view of a conventional technology for a gas delivery pipeline connected to a process reaction chamber;
圖三,係為本發明之連接至一製程反應室之氣體輸送管線 的部份示意圖;以及 圖四,係為MFC控制面板與螺線管閥的傳訊作動電路示意 圖。 圖號說明:Figure 3 is a schematic diagram of a part of a gas delivery pipeline connected to a process reaction chamber according to the present invention; and Figure 4 is a schematic diagram of a communication operation circuit of an MFC control panel and a solenoid valve. Figure number description:
Ru上游線圈 Rd下游線圈Ru upstream coil Rd downstream coil
A T溫度差 V 0流量計之電壓測量值 10反應室 A,B,C,D,E氣體源 a,b,c,d,e,f管線 7最終閥 a 1,b 1,c 1,d 1,e 1手動閥 R繼電器 a2, b2, c2, d2, e2壓力調節器 a3, b3, c3, d3, e3過濾器 R1和R2 可調節電阻AT Temperature difference V 0 Voltage measurement value of flow meter 10 Reaction chamber A, B, C, D, E Gas source a, b, c, d, e, f Line 7 Final valve a 1, b 1, c 1, d 1, e 1 manual valve R relays a2, b2, c2, d2, e2 pressure regulators a3, b3, c3, d3, e3 filters R1 and R2 adjustable resistance
第14頁 509829 圖式簡單說明 a4,b4,c4,d4,e4 上游閥 a 5,b 5,c 5,d 5,e 5 流量計 a6,b6,c6,d6,e6 下游閥 a8,b8,c8,d8,e8 MFC控制面板 a91,a92,b91,b92,c91,c92,d91,d92,e91,e92 螺線管閥Page 14 509829 The diagram briefly explains a4, b4, c4, d4, e4 upstream valve a 5, b 5, c 5, d 5, e 5 flow meter a6, b6, c6, d6, e6 downstream valve a8, b8, c8, d8, e8 MFC control panel a91, a92, b91, b92, c91, c92, d91, d92, e91, e92 solenoid valve
第15頁Page 15
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