TW200900128A - Delivery of gases from internally regulated cylinders - Google Patents
Delivery of gases from internally regulated cylinders Download PDFInfo
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- TW200900128A TW200900128A TW097105636A TW97105636A TW200900128A TW 200900128 A TW200900128 A TW 200900128A TW 097105636 A TW097105636 A TW 097105636A TW 97105636 A TW97105636 A TW 97105636A TW 200900128 A TW200900128 A TW 200900128A
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- Prior art keywords
- gas
- gas supply
- supply package
- container
- flow
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D83/00—Containers or packages with special means for dispensing contents
- B65D83/14—Containers or packages with special means for dispensing contents for delivery of liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant for a product delivered by a propellant
- B65D83/32—Dip-tubes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D83/00—Containers or packages with special means for dispensing contents
- B65D83/14—Containers or packages with special means for dispensing contents for delivery of liquid or semi-liquid contents by internal gaseous pressure, i.e. aerosol containers comprising propellant for a product delivered by a propellant
- B65D83/44—Valves specially adapted therefor; Regulating devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/035—Flow reducers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
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- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
200900128 九、發明說明: 【發月所屬之技術領域】 :發明有關於具有内部調節能力的材料館存鱼 配合益,該容器的内部具有一分配調 ^ 動式齑麯、 g即衷置’例如 ,〃體5配組件,並且本發明亦有關於改$六." 系統和使用該種容器的方法。 ^工乳 【先前技術】 近年來’半導體工業基於安全上的考量而使用 來供應微電子製程中所使用的流體,以減少因使用 壓氣筒所帶來的危險。 其中—種安全防護氣體供應包裝係使用一種耦 體分配闕頭組件並且在容器內部容積中具有物理吸 儲存介質的氣體儲存及分配容器。此類氣體供應包 是ATMI公司(Danbury,CT,USA)所銷t商標名稱 與SAGE的商品,並且在美國專利5,5 1 8,528號中 整的敘述。由於處在吸附狀態下的氣體蒸氣壓遠低 高壓氣筒的壓力,因此吸附劑式氣體供應包裝可大 意外釋出高壓氣體所帶來的危險。 近幾年研發出另一種新的氣體供應包裝,其在 應容器内部使用一氣體釋放調節組件,例如設定點 節器(set point pressure regulator)。此類内部調節 來控制從容器釋放出之氣體的壓力。此類氣體供應 如購自ATMI公司(Danbury,CT,USA)所銷售商標 體分 力致 分配200900128 IX. Inventor's Note: [Technical field to which the moon belongs]: The invention relates to the material library with internal adjustment ability. The inside of the container has a distribution adjustment, and the g is the same. The corpus callosum 5 is equipped with components, and the present invention also relates to the modification of the system and the method of using the container. ^Working Milk [Prior Art] In recent years, the semiconductor industry has been used to supply fluids used in microelectronics processes based on safety considerations to reduce the risk of using a gas cylinder. One such safety gas supply package utilizes a gas distribution and dispensing container that couples the splitter assembly and has a physical absorbent storage medium within the interior volume of the container. Such a gas supply package is a product of the t-brand name and SAGE sold by the company of the United States of America (Danbury, CT, USA) and is described in U.S. Patent No. 5,5,8,528. Since the vapor pressure in the adsorbed state is much lower than the pressure of the high pressure gas cylinder, the adsorbent gas supply package can unexpectedly release the danger of high pressure gas. In recent years, another new gas supply package has been developed which uses a gas release adjustment assembly inside the container, such as a set point pressure regulator. This type of internal adjustment controls the pressure of the gas released from the container. Such gas supplies, such as trademarks sold by ATMI (Danbury, CT, USA), are distributed.
包裝 統高 一氣 氧體 可以 SDS 更完 傳統 降低 體供 例調 是用 裝例 VAC 200900128 的產品,並且在美國專利6,101,816與6,343,476號中有更 詳盡的敘述。位在容器内部容積中的氣體釋放調節組件允 許流體以高壓力儲存在容器中,並且氣體释放調節組件可 限制氣體釋放而以一設定點壓力或經過調節的壓力來釋出 氣體,該設定點壓力或經過調節的壓力實質低於容器内之 大量流體的儲存壓力。 在使用上,已證實此類可於内部進行壓力調節的氣體 供應包裝是安全而有效的。在此類包裝的各種商業實施商 品中,内部氣體釋放調節組件包含多個流量控制元件,用 以避免顆粒隨著分配氣體離開容器,及/或避免在氣體分配 操作過程中發生流量忽大忽小的情形。 在本領域中,仍不斷努力研發與開拓更安全與有效的 氣體供應包裝。 【發明内容】The packaging system is high in oxygen. The SDS can be used to reduce the body supply. The use of the VAC 200900128 is described in more detail in U.S. Patent Nos. 6,101,816 and 6,343,476. A gas release adjustment assembly positioned in the interior volume of the container allows the fluid to be stored in the container at a high pressure, and the gas release adjustment assembly can limit gas release and release the gas at a set point pressure or a regulated pressure, the set point pressure Or the regulated pressure is substantially lower than the storage pressure of the bulk of the fluid in the container. In use, it has been proven that such a gas supply package that can be internally pressure regulated is safe and effective. In various commercial implementations of such packages, the internal gas release conditioning assembly includes a plurality of flow control elements to prevent particles from exiting the container with the dispensing gas and/or to avoid flux fluctuations during gas distribution operations. The situation. In the field, efforts are constantly being made to develop and develop safer and more efficient gas supply packaging. [Summary of the Invention]
本發明有關於氣體供應設備以及利用内部調節材料儲 存與氣體分配容器的方法,在該容器的内部設置有一分配 調節裝置,例如一壓力致動氣體分配組件。 在一態樣中,本發明有關於一種氣體供應包裝,包括: 一長形容器,其定義出該容器的一縱軸且具有一内部 容積,該内部容積用以容納一氣體或一氣體來源材料,可 在分配條件下從該氣體來源材料釋放出氣體;以及 一氣體釋放組件,其固定至該容器,用以在分配條件 下從該容器中分配出氣體; 6 200900128 該氣體釋放組件包含位在該内部容積中的一氣體釋放 構件,該氣體釋放構件定義出一具有縱軸的長形流動通 道,並且在該流動通道中設置至少一個大致平面狀的過濾 元件,用以從流經該流動通道的氣體中補捉顆粒; 其中該流動通道與該至少一個大致平面狀的過濾元件 係設置用來產生下列作用:The present invention relates to a gas supply apparatus and a method of storing and dispensing a gas distribution container using an internal conditioning material, within which a dispensing adjustment device, such as a pressure actuating gas distribution assembly, is disposed. In one aspect, the invention relates to a gas supply package comprising: an elongate container defining a longitudinal axis of the container and having an internal volume for containing a gas or a gas source material Removing gas from the gas source material under dispensing conditions; and a gas release assembly secured to the container for dispensing gas from the container under dispensing conditions; 6 200900128 The gas release assembly is contained in a gas release member in the interior volume, the gas release member defining an elongated flow passage having a longitudinal axis, and providing at least one substantially planar filter element in the flow passage for flowing through the flow passage Capturing particles in the gas; wherein the flow channel and the at least one substantially planar filter element are configured to produce the following effects:
使該過渡元件附近產生氣導率(gas flow conductance) 的變化;及/或 相對於該容器縱軸及/或相對於該流動通道之縱軸而 言以非零度的角度來引導氣流,以增進該過濾元件的捕集 效率。 在一較佳態樣中,此類氣體供應包裝沒有燒結金屬或 熔塊的氣體過渡元件(frit gas filtration elements)。 本發明的另一態樣係有關於一種氣體供應系統,其包 含一上述的氣體供應包裝,以及耦接至該氣體釋放組件的 流動管線(flow circuitry),以將所分配的氣體輸送至一氣 體利用位置。 在又一態樣中,本發明有關於一種半導體製造設施, 其包含此一氣體供應系統。 本發明的另一態樣有關於一種流體過濾器,其包含一 過濾器外殼與一聚合物薄膜,並且藉由固定於該過濾器外 殼的多個孔狀支撐板將該聚合物薄膜支撐在該些孔狀支撐 板的表面上,該過濾器外殼設置成可供流體流過,使得進 入該外殼中的流體接觸每一個孔狀支撐板和該聚合物薄 7 200900128 膜,而在流體從該外彀釋放出來之前,過濾該流體。 文中所使用的述語「薄膜(membrane)」表不一種内部 具有孔隙的片狀物或網狀物,該孔隙度從該片狀或網狀物 的一面延伸至另一面而佈滿整個片狀或網狀物。構成該孔 隙度的孔隙可具有任何適當的大小、形狀、長度與孔隙大 小分佈。該些孔隙具有適當大小,以允許一目標滲透物種 滲透通過該片狀或網狀物内的孔隙’同時含有該目標滲透 物種之混合物中的一或多種其他物種則會被阻擋或攔住而 無法通過。該些孔隙具有允許薄膜最有利地捕捉住顆粒的 大小與分佈,使得該些顆粒不能通過薄膜。 文中使用的術語「熔塊(frit)」係指含有以顆粒及/或 分離或不連續的材料體在熱及/或壓力下形成之材料的物 體’或由該種材料所構成的物體,而形成一種内部具有孔 隙度的堅固物體。該孔隙度允許目標滲透物種從該物體的 外表面 外表面部分滲透通過該物體而至該物體的 分,同時含有該目標滲透物種之混合物中合 物種則被阻擋或攔住而無法通過。Varying a change in gas flow conductance near the transition element; and/or directing the airflow at a non-zero angle relative to the longitudinal axis of the container and/or relative to the longitudinal axis of the flow channel to enhance The collection efficiency of the filter element. In a preferred aspect, such a gas supply package has no frit gas filtration elements of sintered metal or frit. Another aspect of the invention relates to a gas supply system comprising a gas supply package as described above, and flow circuitry coupled to the gas release assembly for delivering the dispensed gas to a gas Use location. In yet another aspect, the present invention is directed to a semiconductor fabrication facility that includes such a gas supply system. Another aspect of the invention relates to a fluid filter comprising a filter housing and a polymer film, and supporting the polymer film by a plurality of hole-shaped support plates fixed to the filter housing On the surface of the perforated support plates, the filter housing is configured to allow fluid to flow therethrough such that fluid entering the housing contacts each of the perforated support plates and the polymeric thin film 200900128, while the fluid is from the outer Filter the fluid before it is released. As used herein, the term "membrane" refers to a sheet or web having voids therein, the porosity extending from one side of the sheet or web to the other and filling the entire sheet or Mesh. The pores constituting the porosity may have any suitable size, shape, length, and pore size distribution. The pores are of a suitable size to allow a target permeate species to permeate through the pores within the sheet or mesh while one or more other species in the mixture containing the target permeate species are blocked or blocked from passing . The pores have a size and distribution that allows the film to most advantageously capture the particles such that the particles do not pass through the film. As used herein, the term "frit" refers to an object containing or consisting of particles and/or discrete or discontinuous materials formed under heat and/or pressure, and Forms a solid object with porosity inside. The porosity allows the target permeating species to partially penetrate the object from the outer surface of the outer surface of the object to the fraction of the object, while the mixture containing the target permeating species is blocked or blocked from passing.
不會執行任 構或配置成 了解本發明的其他態樣、 特徵與實施例。 冷另一外表面部 的一或多種其他 更加清楚 【實施方式] 8 200900128 本發明有關於内部調節式氣體供應包裝,其包含一材 料儲存與氣體分配容器,該容器的内部容積中設置有一分 配調節裝置,例如壓力致動式氣體分配組件。 在本發明的一態樣中,本發明有關於一種氣體供應包 裝,其具有一長形容器,該長形容器定義出該容器的縱軸 且具有一内部容積用以容納一氣體或一氣體來源材料,在 分配條件下可從該氣體來源材料釋放出氣體;以及 一氣體释放組件,其固定至該容器,用以在該分配條 件下從該容器中分配出氣體; 該氣體釋放組件包含位在該内部容積中的一氣體釋放 構件,該氣體釋放構件定義出一具有縱軸的長形流動通 道,並且在該流動通道中設有至少一個大致平面狀的過遽 元件,用以從流經該流動通道的氣體中補捉顆粒; 其中該流動通道與該至少一個大致平面狀過濾元件係 設置用來產生下列作用: 在該過濾元件附近產生氣導率的變化;及/或 相對於該容器縱軸及/或相對於該流動通道之縱軸而 言非零度角度的氣流方向,以增進該過濾元件的捕集效率。 此類氣體供應包裝不含燒結金屬或熔塊的氣體過濾元 件。 本發明的氣體供應包裝可建構成使該長形流動通道的 縱軸與該容器的縱軸之間定義出一銳夾角,該銳夾角的範 圍約從5°至25°。 本發明之氣體供應包裝中的大致平面狀過濾元件可由 9 200900128 薄膜式過濾元件所構成,或包含一薄膜式過濾元件,例如 片狀聚合物薄膜材料,其能讓該氣體供應包裝所分配的氣 體通過,但是能有效作為阻障物以防止顆粒通過該薄膜材 料,使得從該氣體供應包裝中所分配出來的氣體具有較少 顆粒,較佳者為實質上不含顆粒。Other aspects, features, and embodiments of the present invention are not implemented or configured. One or more other aspects of the cold outer surface portion are more clearly [Embodiment] 8 200900128 The present invention relates to an internally regulated gas supply package comprising a material storage and gas distribution container having a dispensing adjustment disposed in an internal volume of the container A device, such as a pressure actuated gas distribution assembly. In one aspect of the invention, the invention relates to a gas supply package having an elongate container defining a longitudinal axis of the container and having an internal volume for containing a gas or a source of gas a material from which gas can be released under dispensing conditions; and a gas release assembly secured to the container for dispensing gas from the container under the dispensing condition; the gas release component comprising a gas release member in the interior volume, the gas release member defining an elongated flow passage having a longitudinal axis, and having at least one substantially planar transition element in the flow passage for flowing through the Capturing the particles in the gas of the flow channel; wherein the flow channel and the at least one substantially planar filter element are configured to produce the following effects: a change in air permeability is produced adjacent the filter element; and/or relative to the container The direction of the airflow at a non-zero angle relative to the axis and/or the longitudinal axis of the flow channel to enhance the collection efficiency of the filter element. Such gas supply packages contain gas filtering elements that do not contain sintered metal or frit. The gas supply package of the present invention can be constructed such that a sharp angle is defined between the longitudinal axis of the elongate flow channel and the longitudinal axis of the container, the sharp angle being in the range of from about 5 to about 25. The substantially planar filter element of the gas supply package of the present invention may be comprised of 9 200900128 membrane filter elements or comprise a membrane filter element, such as a sheet of polymeric film material, which allows the gas to be supplied to the packaged gas. Passing, but effective as a barrier to prevent particles from passing through the film material, such that the gas dispensed from the gas supply package has fewer particles, preferably substantially free of particles.
在本發明的一特定實施例中,該氣體供應包裝包含一 薄膜過濾元件,該薄膜過濾元件多個孔狀支撐板而定位地 保持在該氣體分配通道中,該些孔狀支撐板可在過濾元件 附近產生氣導率的變化,以及產生方向性的氣流流入其孔 洞中,也就是該孔狀支撐板的固體部分使氣流轉向而流入 該些孔洞中。 在另一實施例中,該氣體供應包裝的大致平面狀過濾 元件可設置成位在該管狀通道中且由多個縱向間隔設置之 盤狀元件所組成的陣列,並且該些盤狀元件之至少其中一 者定義有一氣體流動開口,用以產生相對於該流動通道之 縱軸而言非零度角度的方向性氣流。在一特定實施例中, 該由多個縱向間隔設置之盤狀元件所構成之陣列中的至少 一個盤狀元件(較佳為多個盤狀元件)具有多個橫偏移狹縫 開口(slatted slot openings),用以引導該管狀通道内的氣 體產生渦流。 該氣體供應包裝可具有氣體釋放構件,該氣體釋放構 件包含一導管,該導管具有一第一導管部分和一第二導管 部分,該第一導管部分具有一縱軸且其與該容器的縱軸相 符,該第二導管部分具有一縱軸,並且該第二導管部分的 10 Ο Ο 200900128 縱軸到該容器的縱軸之間具有一非零度的角度。該第二導 f部分較佳配置在該第_導管部分的下方,以及該第二導 管部分終止於_下端處 墒慝且具有一外殼,該過濾器元件容納 在該外殼内且連接至該第二導管部分的該下端。 :第-導管部分可輕接至—塵力致動調節胃,用以在 下游氣體壓力低於該壓力 $ 77双動調節器的一設定點壓力 做出釋放氣體的回應。 一莫2廣泛而S ,氣體供應包裝中的氣體釋放構件可包含 8 ’該導管耦接至一壓力 ^严姑 » » _ ^ ®刀致動調即态。該氣體供應包 裝的該氣體釋放組件可台 』 1 2 3~個或一個以上之設置在該容 益内部容積中的壓力致動調節器。 备 的儲=Γ:該氣體供應包巢可包含氣體或氣體來源材料 ^ ^ . ^ Α以及可在分配條件下從該儲存介質釋放出氣 配 ’、y ,並且氣體從該容器流至期望使用所分 類。在— 利用位置。儲存介質可以是任何適當的種 實施例中’儲存介質包含一物理性吸附材料。在 为—實施例中,料£ + λ 储存介質包含一離子性液體材料。 本發明之氣體供應包裝中的氣體釋放組件可包含一設 置--pt. 言矣 之内部容積中的流體過濾器,該流體過濾器包 11 1 —過濾器外殼,# AL ± 2 _ 該外设内安裝有一大致平面狀的過濾器 疋件’該過瀘哭-仙 、、盗疋件疋位地保持在上游與下游的孔狀支撐 板之間而如同_诘人 人 複合組件般。該大致平面狀過濾元件可包 3 —聚合物键腺_1丄 ^ *膜材料。可使用的聚合物材料範例係如聚對 本一甲酸乙- —醉酯(polyethylene terephthalate)、聚砜 200900128 (polysulfone)、聚醯亞胺(polyimide)與聚四氟乙稀 (polytetrafluoroethylene)。作為過濾器元件的片狀聚合物 材料可具有任何適當的厚度,例如介在0.07毫米至〇.2毫 米(m m)的厚度範圍之間。In a particular embodiment of the invention, the gas supply package comprises a membrane filter element, the membrane filter element being positioned in position in the gas distribution channel, the hole-shaped support plate being filterable A change in air permeability occurs near the element, and a directional air flow flows into the hole, that is, the solid portion of the hole-shaped support plate diverts the air flow into the holes. In another embodiment, the substantially planar filter element of the gas supply package can be disposed in an array of the plurality of longitudinally spaced disc members positioned in the tubular passage and at least the disc-shaped members. One of them defines a gas flow opening for producing a directional gas flow at a non-zero angle relative to the longitudinal axis of the flow channel. In a particular embodiment, the at least one of the plurality of disc-shaped elements (preferably a plurality of disc-shaped elements) of the array of longitudinally spaced disc members has a plurality of laterally offset slit openings (slatted A slot opening) for guiding a vortex of gas in the tubular passage. The gas supply package can have a gas release member comprising a conduit having a first conduit portion and a second conduit portion, the first conduit portion having a longitudinal axis and the longitudinal axis of the container Consistently, the second conduit portion has a longitudinal axis and the longitudinal axis of the second conduit portion 10 Ο Ο 200900128 has a non-zero angle to the longitudinal axis of the container. The second guide portion f is preferably disposed below the first conduit portion, and the second conduit portion terminates at the lower end and has a casing, the filter element being received in the casing and connected to the first The lower end of the second conduit portion. The first-catheter portion can be lightly coupled to the dust-actuated regulating stomach to respond to the release of gas at a set point pressure below the pressure of the lower-pressure regulator. The gas release member in the gas supply package may comprise 8 'the conduit coupled to a pressure ^ » _ ^ ® knife actuation tone state. The gas supply package of the gas supply package can actuate a regulator to actuate the pressure in the internal volume of the containment. Reserve = Γ: The gas supply enclosure may contain a gas or gas source material ^ ^ . ^ Α and may release a gas distribution ', y from the storage medium under dispensing conditions, and the gas flows from the container to the desired use classification. In — use location. The storage medium can be of any suitable type. The storage medium comprises a physical adsorbent material. In the embodiment, the material £ + λ storage medium comprises an ionic liquid material. The gas release assembly in the gas supply package of the present invention may comprise a fluid filter in an internal volume of the setting - pt., the fluid filter package 11 1 - the filter housing, # AL ± 2 _ the peripheral A substantially planar filter element is mounted therein. The overcrowding device is held between the upstream and downstream hole-shaped support plates as if it were a composite assembly. The substantially planar filter element can comprise a polymeric bond gland_1 丄 ^ * membrane material. Examples of polymer materials that can be used are, for example, polyethylene terephthalate, polysulfone 200900128 (polysulfone), polyimide, and polytetrafluoroethylene. The sheet-like polymer material as the filter element may have any suitable thickness, for example, between 0.07 mm and 〇.2 mm (m m).
使用時,該氣體供應包裝的容器可填充一半導體製造 氣體’例如肺(arsine)、氨(ammonia)、氬氣(argon)、三敦 化硼(boron trifluoride)、二硼烷(diborane)、二氧化碳 (carbon dioxide)、一 氧化碳(carbon monoxide)、氟化氪 (hydrogen flU0ride)、膦(phosphine)、三氟化磷(phosphorus trifluoride)、石夕燒(silanes)、四氯化石夕(silicon tetrachloride)、四氟化石夕(siiic〇n tetr a fluoride)、六氟化硫 (sulfur hexafluoride)、鹵素氣體、氫化物氣體、金屬有機 化合物和氧化物氣體。 填充後’所受控制的氣體或氣體來源材料可儲存、輪 送以及適當地部署在所期望的使用位置處。在此使用位置 處’氣體供應包裝可透過一流動管線使該包裝的氣體釋放 組件與一氣體利用位置相互連接,以將所分配的氣體輸送 至該位置。 該使用位置可以是一半導體製造設施,在該設施中使 用含有氣體供應包裝的氣體供應系統,以爲該設施中所執 行的半導體製程提供高純度氣體。 本發明的另一態樣係有關於一種流體過濾器,該流體 過濾器包含一過濾器外殼與一聚合物薄膜,並且藉由固定 於該過濾器外殼的多個孔狀支撐板將該聚合物薄膜支撐在 12In use, the gas supply package container can be filled with a semiconductor manufacturing gas such as arsine, ammonia, argon, boron trifluoride, diborane, carbon dioxide ( Carbon dioxide), carbon monoxide, hydrogen fluoride, phosphine, phosphorous trifluoride, silanes, silicon tetrachloride, tetrafluoroethylene Siiic〇n tetr a fluoride, sulfur hexafluoride, halogen gas, hydride gas, metal organic compound and oxide gas. The gas or gas source material that is controlled after filling can be stored, transferred, and suitably deployed at the desired location of use. The gas supply package at the location of use herein interconnects the gas release assembly of the package with a gas utilization location through a flow line to deliver the dispensed gas to the location. The location of use can be a semiconductor fabrication facility in which a gas supply system containing a gas supply package is used to provide a high purity gas to the semiconductor process performed in the facility. Another aspect of the invention relates to a fluid filter comprising a filter housing and a polymer film, and the polymer is supported by a plurality of hole-shaped support plates fixed to the filter housing Film support at 12
200900128 該些孔狀支撐板的表面上,該過濾器外殼設置 流過,使得進入該外殼中的流體接觸每一個孔 該聚合物薄膜,而在流體從該外殼釋放出來之 流體。在一較佳實施例中,該聚合物薄膜包括5 並且設置每個孔狀支撐板,使得該些孔狀支撐 對齊(in register with)另一孔狀支撐板的孔洞, 流過該過濾器。 現參閱附圖,第1圖是顯示一種内部調節 及氣體分配包裝1 00的剖面正視圖,其可實施 良點。 包裝100包含一大體上呈圓筒形的流體儲 器1 02,並且以一底板構件1 06封住該圓筒側 端。該容器的上端是一頸部108,該頸部108 狀頸圈11 0,用以定義且限定出該容器的頂部β 此如圖所示,該容器壁、底板構件與頸部圍繞 積 128。 在該容器的頸部處,閥頭組件1 1 4的螺紋 該頸圈11 0的内側螺紋開口螺旋接合。閥頭組 一中央流體流動通道1 2 0,該中央流體流動通 體連通的方式與該閥頭組件中的中央工作容積 中央工作容積腔室接著連接至出口 124,出口 外部螺紋或是經過設計而可與一連接器以及相 導管等物品連接。 一閥元件122設置在該中央工作容積腔室 成可供流體 狀支撐板和 前,過濃該 i四氟乙稀, 板中的孔洞 以利於氣體 式材料儲存 本發明的改 存與分配容 壁104的下 包含一圓筒 3 口(埠)。因 出一内部容 栓塞11 2與 件1 1 4包含 道1 2 0以流 腔室連接。 124可帶有 關的管道、 中,如實施 13 200900128 例所示,該閥元件122連接至一手輪,或者閥元 連接至一自動閥促動器、他種控制器或促動裝置 在閥組件(valve bl〇ck)f,閥頭組件114還 . 充通道116,該填充通道Π6與該填充埠116以 的内部容積128流體連通。因此,如圖所示,可 體填充到該容器1 02中,隨後關閉且蓋上該填充 或者,可透過調節器將氣體填充至該容器中 f、 藉著將該流體壓力調節器設定在一適當低的壓力 氣體或蒸氣處在低於該壓力調節器設定點的壓力 可藉由諸如彈簧偏壓元件等偏壓元件將提升閥元 關閉位置的傳統壓力調節器,並且當壓力高於該 力時該提升閥元件會回應而保持關閉,而當壓力 定點壓力時,該提升閥元件則會開啟且允許流體 因此’可藉著在容器中建立出能使壓力調節 閥元件離開閥座且進而允許氣體流入容器中的壓 行將該欲儲存與隨後分配的流體裝載至該容器中 〇 業。以此方法,該容器可僅具有一個開口(埠),該 能允許氣體從容器中釋出以進行分配,亦允許先 ' 一埠以流體來填充該容器。 * 間碩組件1 1 4中之中央流體流動通道丨2 〇的 至一連接器流管130’而連接器流管130接著連 器132。調節器係設定成可使該容器釋放出來的 一選定的壓力。 調節器的下端連接至一管狀接頭 件122可 〇 具有一填 及該容器 將尚壓.氣 ϊρ 〇 ,例如可 值,使得 ,使用一 件壓向一 設定點壓 低於該設 通過。 器之提升 力,來執 的填充作 :開口(埠) 透過該單 下端連接 接至調節 流體保持 (tubular 14 200900128 fitting) 1 36,該管狀接頭隨後利用例如對焊方式而連接至 一過濾器單元134,該過濾器單元134的下方末端處具有 一擴散器端蓋 131。該過濾器單元可能是由不銹鋼所構 成,且該擴散器壁可由燒結不銹鋼所形成,例如 316L不 銹鋼。該過濾器單元具有一器壁孔隙度,以允許從該系統 釋出的氣體可以每分鐘30標準升的流速將尺寸大於預定 直徑(例如大於0 · 003微米)的所有顆粒移除掉。此類過濾 器單元可購自Mott股份有限公司(Farmington,CT)。 使用時,加壓氣體容納在容器102的内部容積128中。 氣體壓力調節器1 3 2設定至一選定的設定點,以當閥頭組 件11 4中的閥開啟時,氣體流經過濾器單元1 3 4、接頭1 3 6、 調節器1 3 2、連接器流管1 3 0、閥頭組件中的中央流體流動 通道120、中央工作容積腔室與出口 124,而提供經過分配 的氣流。依據氣體供應包裝之指定終端使用用途的需要或 要求,閥頭組件可連接至其他管線、導管、流動控制器、 監控裝置等。 第2圖顯示在本發明一較佳實施例中,實施本發明改 良處之閥頭240與相連之雙調節器桿狀裝置的正視圖。該 桿狀裝置包含上壓力調節器242與下壓力調節器244,以 及介在下壓力調節器 244和薄膜過濾器 250之間的管道 246,該管道250含有一彎曲部248。彎曲部248上方的桿 狀裝置之中心線與彎曲部24 8下方之管道中心軸之間所定 義出來的夾角範圍介於約5°至25°之間,較佳範圍介於8° 至1 5。之間,最佳範圍介於9 °至1 2。之間。 15 200900128 第2圖的分配結構沒有任何燒結金屬或熔塊的過濾器 元件,取而代之的是,在桿狀裝置的管道中且接近該管道 之下方開放末端處使用一薄膜過濾器,並且該管道具有一 些微彎曲的彎曲部。此「彎曲桿狀(bent stick)」流動通道 非常有利於使容器内部容積中的氣體引發不對稱渦流,以 為氣體提供延長的流動路徑,而有助於從分配氣體中分離 出固體顆粒。200900128 On the surface of the perforated support plates, the filter housing is disposed to flow such that fluid entering the housing contacts the polymer film of each of the holes and the fluid released from the housing. In a preferred embodiment, the polymeric film comprises 5 and each of the apertured support plates is disposed such that the apertured supports are in register with the apertures of the other apertured support plates and flow through the filter. Referring now to the drawings, FIG. 1 is a cross-sectional elevational view showing an internal adjustment and gas distribution package 100, which can be implemented. The package 100 includes a generally cylindrical fluid reservoir 102 and encloses the cylindrical side end with a bottom plate member 106. The upper end of the container is a neck portion 108 that defines and defines the top portion of the container. As shown, the container wall, floor member and neck portion are surrounded 128. At the neck of the container, the threaded end of the valve head assembly 1 14 is helically engaged with the inner threaded opening of the collar 110. The valve head assembly has a central fluid flow passage 120, the central fluid flow communicates with the central working volume central working volume chamber in the valve head assembly and is then connected to the outlet 124, and the outlet external thread is either designed or Connected to a connector and a phase conduit. A valve element 122 is disposed in the central working volume chamber to provide a fluid-like support plate and front, enriching the i-tetrafluoroethylene, the holes in the plate to facilitate the storage of the gas material of the present invention. The lower part of 104 contains a cylinder 3 (埠). Since the internal cavity plug 11 2 and the piece 1 1 4 contain the channel 1 2 0, the flow chamber is connected. 124 may be associated with a conduit, as shown in the example of Embodiment 13 200900128, the valve element 122 is coupled to a hand wheel, or the valve element is coupled to an automatic valve actuator, other type of controller or actuating device at the valve assembly ( Valve bl〇ck)f, valve head assembly 114 also. Filling passage 116, which is in fluid communication with internal volume 128 of fill ram 116. Thus, as shown, the body can be filled into the container 102, then closed and covered, or the gas can be filled into the container through the regulator, by setting the fluid pressure regulator to A suitably low pressure gas or vapor at a pressure below the set point of the pressure regulator may be a conventional pressure regulator that raises the position of the valve member by a biasing element such as a spring biasing element, and when the pressure is above the force The poppet valve member will remain closed while responding, and when the pressure is at a fixed point pressure, the poppet valve member will open and allow fluid to be established by allowing the pressure regulating valve member to exit the valve seat and thereby allow The impregnation of the gas into the container loads the fluid to be stored and subsequently dispensed into the container. In this way, the container can have only one opening, which allows gas to be released from the container for dispensing, and also allows the container to be filled with fluid first. * The central fluid flow path 间2 中 of the intermediate assembly 1 14 is connected to a connector flow tube 130' and the connector flow tube 130 is connected to the connector 132. The regulator is set to a selected pressure that will release the container. The lower end of the adjuster is coupled to a tubular member 122 which can be filled with a container which is still pressurized. 例如ρ 〇 , for example, may be valued such that a pressure is applied to a set point below the set point. The lifting force of the device, the filling operation: the opening (埠) is connected to the regulating fluid holding (tubular 14 200900128 fitting) 1 36 through the single lower end connection, and the tubular joint is then connected to a filter unit by, for example, butt welding. 134. The filter unit 134 has a diffuser end cap 131 at a lower end thereof. The filter unit may be constructed of stainless steel and the diffuser wall may be formed from sintered stainless steel, such as 316L stainless steel. The filter unit has a wall porosity to allow gas released from the system to remove all particles having a size greater than a predetermined diameter (e.g., greater than 0. 003 microns) at a flow rate of 30 standard liters per minute. Such filter units are available from Mott Corporation (Farmington, CT). In use, pressurized gas is contained within the interior volume 128 of the vessel 102. The gas pressure regulator 1 3 2 is set to a selected set point such that when the valve in the valve head assembly 11 4 is open, gas flows through the filter unit 1 3 4, the joint 1 3 6 , the regulator 1 3 2, the connector The flow tube 130, the central fluid flow channel 120 in the valve head assembly, the central working volume chamber and the outlet 124 provide a distributed gas flow. The valve head assembly can be connected to other lines, conduits, flow controllers, monitoring devices, etc. depending on the needs or requirements of the intended end use of the gas supply package. Figure 2 is a front elevational view of a valve head 240 and associated dual regulator rod assembly embodying the present invention in a preferred embodiment of the invention. The rod assembly includes an upper pressure regulator 242 and a lower pressure regulator 244, and a conduit 246 intermediate the lower pressure regulator 244 and the membrane filter 250, the conduit 250 including a bend 248. The angle defined between the centerline of the rod-like device above the curved portion 248 and the central axis of the conduit below the curved portion 24 is between about 5 and 25 degrees, preferably between 8 and 15 . The best range is between 9 ° and 12. between. 15 200900128 The distribution structure of Figure 2 does not have any sintered metal or frit filter elements. Instead, a membrane filter is used in the pipe of the rod-like device and near the open end of the pipe, and the pipe has Some slightly curved bends. This "bent stick" flow channel is highly advantageous in inducing asymmetrical vortices in the gas in the interior volume of the vessel to provide an extended flow path for the gas and to assist in the separation of solid particles from the distribution gas.
第3圖是根據本發明一實施例,實施本發明多項特徵 之閥頭2 6 0與相連桿狀裝置的正視圖。在此實施例中,位 在調節器262下方之桿狀裝置的管道264具有彎曲約1 0° 的彎曲部 266,使得位於彎曲部下方的管道下部分呈線 性,並且調節器上方之桿狀裝置的中心軸和彎曲部266下 方之管道的中心轴之間具有一夾角,在此實施例中,該夾 角為10°。如圖所示,管道下方的彎折部分中具有一薄膜 過濾裝置2 6 8以及一底部開口 2 7 0,以允許氣體分配容器 之内部容積中的氣體進入且向上流經薄膜過濾器 2 6 8,流 入管道264而流至壓力調節器262。調節器具有一適當的 壓力值設定點,使得當閥頭的閥開啟且壓力調節器感受到 低於設定點的下游壓力時,調節器會開啟。 彎曲部266提供小的流體阻滯(damping),並且發現到 彎曲部266可使薄膜過濾器268能良好地補集顆粒,否則 可能會對調節器與使用該分配氣體的下游製程產生不良影 響。 第4圖顯示各種過濾器介質的包裝外(out-of-package) 16 200900128 ΟFigure 3 is a front elevational view of a valve head 206 and associated rod-like device embodying various features of the present invention, in accordance with an embodiment of the present invention. In this embodiment, the tube 264 of the rod-like device located below the adjuster 262 has a bend 266 that is bent about 10° such that the lower portion of the tube below the bend is linear and the rod-like device above the adjuster The central axis has an included angle with the central axis of the conduit below the curved portion 266, which in this embodiment is 10°. As shown, the bent portion below the conduit has a membrane filtration device 268 and a bottom opening 270 to allow gas in the interior volume of the gas distribution vessel to enter and flow upward through the membrane filter 2 6 8 Flows into the conduit 264 and flows to the pressure regulator 262. The regulator has an appropriate pressure set point such that the regulator opens when the valve of the valve head opens and the pressure regulator experiences a pressure below the set point. The bend 266 provides a small fluid damping and it is found that the bend 266 allows the membrane filter 268 to replenish the particles well, which may otherwise adversely affect the regulator and the downstream process using the dispensed gas. Figure 4 shows the out-of-package of various filter media 16 200900128 Ο
濕氣釋氣(ρ ρ b)和時間(分鐘)的關係圖。曲線1代表ρ τ F Ε 薄膜,曲線2代表鎳熔塊,曲線3代表不鏽鋼炼塊,曲線 4代表陶瓷(Tos)過濾器,曲線5代表陶瓷(Mem)過濾、器的 釋氣性能(outgassing performance)。用來產生這此曲線的 測試方法是SEMASPEC 90120397B-STD。結果顯示,pTFE 薄膜是唯一釋出濕氣量低於1 Oppb的過濾器元件,並且此 類薄膜性能優於鎳和不銹鋼過濾器。沒有_個金屬過遽器 在進行4小時的洗淨(purge)過程後,還能達到小於1 〇 ppb 的雜質含量。 第5圖顯示在包裝外(out_of_package)濕氣釋氣測試中 所使用的相同過濾介質,其包裝外氧氣釋氣(ppb)和時間 (分鐘)的關係圖’曲線1代表PTFE薄膜,曲線2代表鎮炼 塊,曲線3代表不鏽鋼熔塊,曲線4代表陶瓷(T〇s)過濾器, 曲線5代表陶瓷(Mem)過濾器的釋氣性能。 用來產生第5圖所示數據的測試方法是SEMAspEc 90 1 20 39 7B-STD。PTFE 過渡器展 量。在經過一小時的洗淨過程後 持小於1 ppm的釋氣。 現出最低的初始氧氣釋氣 ’ PTFE與不銹鋼過濾器保 第6圖顯示不同過遽介質暴露在環境空氣下暴露μ 小時所展現之水濃度(ppb)與時間(分 一 ^ U刀鐘)的關係圖。此圖顯 不在濕氣釋氣與氧氣釋氣測試中 ,谋汰 π使用之相同薄膜過濾器 在% *兄下暴露24小時後的水釋氣數埔Diagram of moisture outgassing (ρ ρ b) versus time (minutes). Curve 1 represents ρ τ F Ε film, curve 2 represents nickel frit, curve 3 represents stainless steel refining, curve 4 represents ceramic (Tos) filter, curve 5 represents ceramic (Mem) filter, outgassing performance (outgassing performance ). The test method used to generate this curve is SEMASPEC 90120397B-STD. The results show that the pTFE film is the only filter element that releases less than 1 Oppb of moisture and is superior to nickel and stainless steel filters. No _ metal damper can achieve an impurity content of less than 1 pp ppb after a 4 hour purge. Figure 5 shows the same filter media used in the out-of-package moisture outgassing test, the relationship between oxygen outgassing (ppb) and time (minutes) outside the package. Curve 1 represents the PTFE film and curve 2 represents the PTFE film. For the refining block, curve 3 represents a stainless steel frit, curve 4 represents a ceramic (T〇s) filter, and curve 5 represents a gassing performance of a ceramic (Mem) filter. The test method used to generate the data shown in Figure 5 is SEMAspEc 90 1 20 39 7B-STD. PTFE transitioner expansion. After a one hour wash, hold less than 1 ppm of outgassing. The lowest initial oxygen outgassing is shown' PTFE and stainless steel filter protection Figure 6 shows the water concentration (ppb) and time (in one ^ U knife) of different oversized media exposed to ambient air for μ hours of exposure. relation chart. This figure is not in the moisture outgassing and oxygen outgassing test. The same membrane filter used for π is used. The water release gas after 24 hours of exposure under % * brother
枰軋数據,曲線1代表PTFE 缚膜’曲線2代表鎳熔塊,曲線3 4 . , 巩曲踝3代表不鏽鋼熔塊,曲線 4代表陶瓷(T〇s)過濾器,曲線5代表 其)代表陶瓷(Mem)過濾器。 17 200900128 用來產生第6圖所Rolling data, curve 1 represents PTFE bond film 'curve 2 represents nickel frit, curve 3 4 . , chiffon 3 represents stainless steel frit, curve 4 represents ceramic (T〇s) filter, curve 5 represents it) Represents a ceramic (Mem) filter. 17 200900128 used to generate Figure 6
$數據的測試方法是S E M A S P E C 90120397B-STD 。所有 、過瀘、器暴露在2 21且相對濕度 4 5 %之環境空氣中持續2 4小時。結果顯示,PTFE過濾器 的釋氣性能實質上勝過镇4 项和不鱗鋼過濾器的濕度釋氣性能 約5倍。 々崎ου psig下,不同過濾介質在 受到差壓時,差壓舆流进堆、 連(t準公升/分鐘)的關係圖。過濾The test method for $data is S E M A S P E C 90120397B-STD. All, over-the-counter, and the device were exposed to an ambient air of 2 21 and a relative humidity of 4 5 % for 24 hours. The results show that the outgassing performance of the PTFE filter is substantially better than the humidity outgassing performance of the town 4 and non-scale steel filters. 々崎ου psig, when different filter media are subjected to differential pressure, differential pressure turbulent flow into the reactor, even (t quasi liters / min) diagram. filter
Ο 器介質包括該些用於前沭赌名 月J建釋氣測試中的介質,曲線1代表 PTFE薄膜,曲線2代表銼p地 衣錄溶塊’曲線3代表不鏽鋼熔塊, 曲線4代表陶瓷(T〇s)過滴哭,A & ± ~ 愿器 曲線5代表陶曼(Mem)過濾 器。用來產生第 7圖所;虹祕认.,The media includes the media used in the test of the former 沭 名 J J Jian Jian, the curve 1 represents the PTFE film, the curve 2 represents the 锉p lichens recording block 'curve 3 represents the stainless steel frit, and the curve 4 represents the ceramic ( T〇s) A drop of tears, A & ± ~ The curve of the machine 5 represents the megaman (Mem) filter. Used to produce the 7th image;
®·所不數據的測試方法是SEMASPEC 901203 97B-STD。在所有經過測試的過濾器中,pTFE過濾 S在所有入口流速下都是最低壓差。pTFE過濾器的壓降 (pressure drop)比不銹鋼過濾器的壓降要少2〇%,並且約為 鎳過濾器之壓降的二分之—。 對上述釋氣測試t所使用的相同種類薄膜(pTFE薄 膜、錄熔塊、不錄鋼熔塊、陶瓷(T〇s)過濾器與不同陶瓷 (Mem)過濾器)進行顆粒去除效果的評估。所使用的測試方 法是SEMASPEC 930215 1 1A-STD,該方法包括60分鐘的 穩態流動(steady flow)、60分鐘的脈衝流動(pulse flow)、 1 0分鐘的衝擊流動(i m p a c t i ο η)以及3 0分鐘的穩態流動條 件。測得陶瓷過濾器可去除大部分的顆粒,並且PTFE薄 膜表現最佳,且優於金屬與陶瓷過遽器。 在 PTFE 薄膜上進行的完整測試包括在預脈衝 18 ΟThe test method for the data is SEMASPEC 901203 97B-STD. In all tested filters, pTFE Filtration S was the lowest differential pressure at all inlet flow rates. The pressure drop of the pTFE filter is 2% less than the pressure drop of the stainless steel filter and is about two-fifths of the pressure drop of the nickel filter. The same type of film (pTFE film, recorded frit, non-recorded steel frit, ceramic (T〇s) filter and different ceramic (Mem) filter) used for the above-described outgassing test t was evaluated for particle removal. The test method used was SEMASPEC 930215 1 1A-STD, which included 60 minutes of steady flow, 60 minutes of pulse flow, 10 minutes of impact flow (impacti ο η), and 3 0 minute steady state flow conditions. The ceramic filter measures most of the particles and the PTFE film performs best and is superior to metal and ceramic filters. Complete testing on PTFE membranes included in the pre-pulse 18 Ο
200900128 (pre-pulse)與沖洗(flush)步驟之後,接著施以2 χ ι〇7 /分鐘的顆粒衝擊(particle challenge),並計算下游的 數。PTFE薄膜滿足下游零顆粒的測試接受標準。 第8圖是用於上述測試中的pTFE過濾器介質的 照片,顯示出該種材料的微結構。 第9圖顯示可用於本發明之氣體供應包裝中的流 制器200之侧視剖面圖。流動控制器包括—主圓柱 202’其一末端耦接至一較小直徑的圓柱延長部218, 長部218中具有多個開口 220,並且主圓柱外殼2〇2 一末端搞接至一較小直裎的圓柱延長部208,該延長旬 中具有多個開口 210。圓柱延長部208安放在一筒狀 204内且與該筒狀部位204共軸,該筒狀部位具有一 末端206 ’用以在本發明氣體供應容器之内部容積中 桿狀裝置的管道耦接。 在主圓柱外殼202中設置有一連串縱向間隔開來 向延伸且不同構造的盤狀物212、214與216。盤狀啦 内具有一中央開口,以供氣流通過。盤狀物214具有 縫開口,該狹缝開口( s 1 〇 t 〇 p e n i n g)係由盤狀物之彼此 狀物平面朝反向外翻的片段所界定而成。盤狀物216 相對於盤狀物 2 1 4所示之狹缝開口而橫向偏移的狹 口,該橫向偏移的狹缝開口係由該盤狀物之彼此從盤 平面朝反向外翻的片段所界定而成。 使用時,在氣體通過圓柱延伸部218而進入流動 器後,欲分配的氣體受到上述狹缝開口的引導而使流 顆粒 顆粒 顯微 動控 外殼 該延 的另 208 部位 開放 與該 、橫 212 一狹 從盤 具有 缝開 狀物 控制 體引 19 200900128 發渦流流過圓柱外殼2 0 2。藉著使流體渦流地流過主圓柱 外殼,顆粒會從流體流中分出,使得顆粒不會漂流在流體 流中且隨後影響容器中之調節器的性能,或是影響接收來 自供應包裝之氣體的下游氣體利用製程的性能。After the 200900128 (pre-pulse) and flushing steps, a particle challenge of 2 χ 〇 7 /min was then applied and the downstream number was calculated. The PTFE film meets the test acceptance criteria for downstream zero particles. Figure 8 is a photograph of the pTFE filter media used in the above test, showing the microstructure of the material. Figure 9 shows a side cross-sectional view of a flow eliminator 200 that can be used in the gas supply package of the present invention. The flow controller includes a main cylinder 202' having one end coupled to a smaller diameter cylindrical extension 218, a plurality of openings 220 in the elongated portion 218, and the main cylindrical housing 2〇2 being joined to a smaller end The straight cylindrical extension 208 has a plurality of openings 210 in the extended period. The cylindrical extension 208 is seated in a cylindrical shape 204 and coaxial with the cylindrical portion 204 having a distal end 206' for coupling the tubing of the rod-like device in the internal volume of the gas supply container of the present invention. A plurality of longitudinally spaced apart and differently configured discs 212, 214 and 216 are disposed in the main cylindrical outer casing 202. The disc has a central opening for airflow. The disc 214 has slit openings defined by the segments of the disc that are turned outwardly in opposite directions. The disk 216 is laterally offset from the slot opening shown by the disk 2 14 by the laterally offset slit opening of the disk from the disk plane toward the reverse The fragment is defined. In use, after the gas enters the flow device through the cylindrical extension 218, the gas to be dispensed is guided by the slit opening to make the flow granule microscopically move the outer casing of the extended 208 portion open and the transverse 212 The narrow disc has a slit opening control body. 19 200900128 The vortex flows through the cylindrical outer casing 2 0 2 . By vortexing the fluid through the main cylindrical shell, the particles are separated from the fluid stream so that the particles do not drift in the fluid stream and subsequently affect the performance of the regulator in the vessel or affect the receipt of gas from the supply package. The downstream gas utilizes the performance of the process.
第1 0圖顯示流經第9圖流動控制器之連續盤狀元件的 氣體流動路徑之立體圖。如圖所示,盤組件3 0 0包含一頂 盤302,該頂盤302中具有一狹缝開口 304,氣體沿著箭頭 Α指示的方向通過該狹缝開口 3 04,並且受到開口向下定 向之垂片(tab)的引導而引發如頂盤302與中間盤306之間 所示的流體渦流,該中間盤3 0 6中具有一中央開口 3 0 8。 隨後氣體流經該中間盤3 0 6中的中央開口 3 0 8,並且保持 其渦流狀態流向由狹缝結構向下彎折之垂片所界定的狹缝 開口 ,所以當流體離開狹縫開口時,是渦流狀地引導流體 流動。 依此方式,沿著相對於流動控制器之長度而言延長長 度的流動路徑來引導氣體流,並且流經缺乏該些不具備引 導流動彎折狹缝結構(flow diverter angled slot structures) 之盤狀元件的控制器。 第1 1圖是可用於本發明各種實施例之氣體供應包裝 中的薄膜式過濾器5 0 0之部分剖開側視圖。過濾器5 0 0包 含一進氣管5 06,進氣器5 06具有一開放末端5 02。進氣管 506固定至過濾器的主外殼504。主外殼圈圍出一内部體積 5 1 2,在該内部體積5 1 2中設置一個或多個薄膜過濾器元件 5 1 4,使得進入該進氣管5 0 6中的流體流過外殼5 0 4的内部 20 200900128 體積512,並且釋放至具有一開放釋放末端510的出氣管 508 ° 過濾器500可設置在氣體供應包裝容器中的内部容積 中,且在其出氣管處耦接至調節器構件上游的桿狀管部 位,使得過濾器之進氣管506的開放末端502設置成可接 收來自容器的待分配氣體,並且造成流體阻滯以及從氣體 中移除顆粒。Figure 10 shows a perspective view of the gas flow path through the continuous disk member of the flow controller of Figure 9. As shown, the disk assembly 300 includes a top plate 302 having a slit opening 304 through which gas passes in the direction indicated by the arrow , and is oriented downwardly by the opening. The tabs are directed to initiate a fluid vortex as shown between the top tray 302 and the intermediate tray 306, which has a central opening 308 in the middle tray 306. The gas then flows through the central opening 3 0 of the intermediate disk 306 and maintains its vortex state flowing toward the slit opening defined by the tabs that are bent downwardly from the slit structure, so when the fluid exits the slit opening Is to vortex the fluid flow. In this manner, the gas flow is directed along an extended length of flow path relative to the length of the flow controller, and flows through the lack of the disk elements that do not have flow diverter angled slot structures The controller of the piece. Fig. 1 is a partially cutaway side view of a membrane filter 500 which can be used in a gas supply package of various embodiments of the present invention. The filter 500 includes an intake pipe 506 having an open end 502. Intake tube 506 is secured to the main housing 504 of the filter. The main outer casing encloses an inner volume 5 1 2 in which one or more membrane filter elements 51 are disposed such that fluid entering the intake pipe 506 flows through the outer casing 50. 4 of the interior 20 200900128 volume 512 and released to the outlet pipe 508 with an open release end 510. The filter 500 can be disposed in the internal volume in the gas supply packaging container and coupled to the regulator member at its outlet pipe The upstream rod-like tube portion is such that the open end 502 of the filter's intake tube 506 is configured to receive gas to be dispensed from the container and cause fluid blockage and removal of particles from the gas.
第12圖是在23 °C下,當入口壓力分別為30 psig(上方 線)與60 psig(下方線)時,流體流經如第11圖所述之過濾 器種類的差壓與流速的關係圖,其係利用電拋光VAR 3 1 6L 不銹鋼外殼中的模鑄PFA結構來支撐一疏水性PTFE薄膜 過濾元件。該數據顯示差壓隨著流過過濾器的流速升高而 升高,並且整個過濾器的壓降對於引入過濾器入口處的絕 對壓力大小而言是非常小的。 就直徑大於0 · 0 1微来的顆抑品,, _ .a .. 做不07頻粒而言,此類過濾器所達到 的下游顆粒淡度小於每公升桐脑士 Α V u.Uj個顆粒(顆粒/公升),並且 降低揮發至小於1 0 ppb之渴翁。wθ A Α丄 *'' ^ Μ最具滲透力的顆粒大小 來說,PTFE薄膜的顆粒滞 φ 由将性(particle retention characteristic)超過在每分锫 標準公升之流速下移除 99.9999999% (9 LRV)的顆粒。 大體上,可使用任何適當 虛勺所你用的笼脸 枓來建構本發明之氣體供 應包裝中所使用的薄膜過據器, 較'佳為表面自由能班聚四 氟乙烯相當的聚合物材料,以形 曰w此興如四 Λ ^成—氣體通透性阻障結構。 因此本發明之乳體供應包 & 1使氣體供應容器不需要 21 Ο 200900128 任合燒結金屬基質或今麗 逍濟器妹播 、义金屬燒結阻障結構,而是利用 過慮器結構更加有效 較經濟的氣體通透性聚合 結構。氣體通透性命人 η會施心 ㈣料可相對較薄,例 同貫施例中,®庳益 #度把圍約從0.07毫米至約0.2毫米 孔隙大小可為1微米。 女έ :*、同實施例中,本發明提供一種薄膜過濾器 π洗的特性’ $是藉由產生不對稱性或橫向 或流動分量來掃過镇眩主工 屏膜表面而可有效清洗該薄膜過 例如,可藉菩 Β線構造’使一部分的分配流體 I過濾器表面以移除任何累積在表面上之固體 此種自我凊洗。例如,可藉著第9圖之流動控制器 • _牛達成渦流配置以提供此種自我清洗能力,並 應用至類似構造的過濾器,該類似構造的過濾器係 的盤狀元件換成第11圖之過濾器中所示的薄膜元件 第1 3圖是根據本發明另一實施例之氣體供應自 的。卩刀剖開正視圖。該包裝包含一大致圓筒狀容器 其圈圍出一内部容積604,以容納氣體及/或氣體來 氣體來源係例如使用該包裝時可產生欲分配之蒸氣 或固體。在一特定實施例中,内部容積604可包含; 或乳體來源的儲存介質,氣體及/或氣體來源係以可 式留在儲存介質中,並且在分配條件下可從該儲存 出瑕1體。例如’儲存介質可包含或由固相物理性吸 所構成,例如活性碳、分子篩、巨網狀3 (maciroreticulate p〇iyiner)或其他對氣體及/或氣體 比金屬 物阻障 如在不 ,並且 ’其具 的流動 渡器。 轉向而 來提供 中的盤 且也可 將其内 D 裝600 602, 源,該 的液體 I體及/ 逆的方 介質釋 附材料 5·合物 來源具 22 200900128 有吸附親和力(sorptive affinity)且在分配條件下可自其脫 附或釋出(extractible)氣體的其他材料。或者,儲存介質可 包含或由離子性液體所構成,該離子性液體可留住氣體前 驅物且隨後可在分配條件下釋放該氣體前驅物。 在一較佳實施例,内部容積含有一孔隙碳吸附劑,例 如製成珠狀、小團狀、顆粒狀等特定形式的吸附劑以在内 部容積中構成一吸附劑床;或是製成磚狀物、塊狀物、盤 狀物或其他大團塊狀的單塊形式,而在内部容積中設置一 或多個大塊的吸附劑物件,用以儲存氣體或氣體前驅物並 且可在該包裝處於分配模式時脫附而釋放出氣體或氣體前 驅物。 可以任何適當方式達到脫附作用(desorption),例如壓 差(壓力介導脫附)、加熱(熱介導脫附)及/或濃度差(質傳濃 度梯度介導脫附),例如使載氣流經内部容積而接觸吸附材 料。 内部容積604中的桿狀裝置620包含一上導管621, 該上導管621連接該調節器622和閥頭組件606。閥頭組 件包含一塊狀形閥頭(如圖所示),其包含一閥腔室,且在 該閥腔室中設置一閥元件,且該閥元件可藉著手動旋轉連 接至該閥元件之閥桿的手輪608而在閥全開與閥全關位置 之間轉換。 該閥頭亦包含一釋放埠6 1 0,該釋放埠6 1 0流體連通 地耦接至一釋放管線(未顯示)用以將分配氣體從該容器輸 送至一下游的使用位置,例如輸送至化學氣相沉積室或原 23 网即器622可以是任何適Figure 12 is the relationship between the differential pressure and the flow rate of the fluid flowing through the filter type as shown in Figure 11 at 23 °C, when the inlet pressure is 30 psig (upper line) and 60 psig (lower line), respectively. The figure utilizes a die cast PFA structure in an electropolished VAR 3 1 6L stainless steel casing to support a hydrophobic PTFE membrane filter element. This data shows that the differential pressure increases as the flow rate through the filter increases, and the pressure drop across the filter is very small for the magnitude of the absolute pressure introduced into the filter inlet. For a suppressor with a diameter greater than 0 · 0 1 micro, _ .a .. does not have 07 frequency granules, the downstream particle faintness achieved by such a filter is less than liters per liter of the cerebral palsy V u.Uj Particles (particles/liter) and reduced volatilization to less than 10 ppb. Wθ A Α丄*'' ^ Μ The most permeable particle size, the particle lag of PTFE film is removed by the particle retention characteristic exceeding the flow rate per standard liter per minute. 99.9999999% (9 LRV )particle. In general, the membrane substrate used in the gas supply package of the present invention can be constructed using any suitable cage face that is more suitable for the surface free energy PTFE-like polymer material. In the form of a shape, it is as good as a gas-permeable barrier structure. Therefore, the milk supply package & 1 of the present invention makes the gas supply container not require any 21 Ο 200900128 sinter sintered metal matrix or the current smelting device, the metal sintered barrier structure, but utilizes the filter structure more effectively. Economical gas permeable polymeric structure. Gas permeability η will be distressed. (4) The material can be relatively thin. For example, in the same example, the 庳 # # 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 度 约 孔隙 孔隙 孔隙 孔隙 孔隙Nvwa: *, in the same embodiment, the present invention provides a film filter π-washing characteristic '$ is effective to clean the surface of the glare main screen by generating asymmetry or lateral or flow component The film may, for example, be constructed by a botanical line to 'partially distribute the fluid I filter surface to remove any solids accumulated on the surface. For example, the flow controller of Figure 9 can be used to achieve this self-cleaning capability and applied to a filter of similar construction, the disc-like element of the similarly constructed filter system is replaced by the eleventh The film element shown in the filter of Fig. 13 is a gas supplied according to another embodiment of the present invention. The sickle cuts the front view. The package includes a generally cylindrical container encircling an internal volume 604 for containing gas and/or gas. The source of the gas, for example, can produce vapor or solids to be dispensed when the package is used. In a particular embodiment, the internal volume 604 can comprise; or a milk-derived storage medium from which the gas and/or gas source can be left in the storage medium and from which the storage can be stored under the dispensing conditions. . For example, the storage medium may comprise or consist of a solid phase physical attraction, such as activated carbon, molecular sieves, macroscopically, or other barriers to gases and/or gases than metal, and 'There is a mobile ferry. Turning to provide the disc in the middle and also loading the inner D into the 600 602 source, the liquid I body and/or the reverse medium medium release material 5 · the source of the material 22 200900128 has a suction affinity (sorptive affinity) Other materials from which the gas can be desorbed or extracted under dispensing conditions. Alternatively, the storage medium may comprise or consist of an ionic liquid that retains the gas precursor and which can then be released under dispensing conditions. In a preferred embodiment, the internal volume contains a pore carbon adsorbent, such as a specific form of adsorbent in the form of beads, small pellets, granules, etc. to form an adsorbent bed in the internal volume; or to form a brick a monolithic form of a mass, a mass, a disk, or other large agglomerate, and one or more bulk adsorbent articles are disposed in the interior volume for storing a gas or gas precursor and may be The package is desorbed in the dispensing mode to release a gas or gas precursor. Desorption may be achieved in any suitable manner, such as pressure differential (pressure-mediated desorption), heating (thermal-mediated desorption), and/or concentration difference (mass transfer concentration gradient-mediated desorption), such as The gas stream contacts the adsorbent material through the internal volume. The rod-like device 620 in the interior volume 604 includes an upper conduit 621 that connects the regulator 622 and the valve head assembly 606. The valve head assembly includes a one-piece valve head (as shown) including a valve chamber, and a valve member is disposed in the valve chamber, and the valve member is connectable to the valve member by manual rotation The hand wheel 608 of the valve stem is switched between a fully open valve and a fully closed position of the valve. The valve head also includes a release port 610 that is fluidly coupled to a release line (not shown) for transporting the dispensed gas from the container to a downstream use position, such as to The chemical vapor deposition chamber or the original 23 mesh 622 can be any suitable
特疋特徵,就疋顆粒分離室(particulates disengage m e nt 200900128 子層沉積室。 '·»· ^ QC1 /rAr m 設定點調節器或可變設定點(可調式二卩益,例如固定 從容器外部位置傳送訊號給調節 :1。例如可藉著 積内部或於外部詷_ ~ 谷器602的圈圍容 Γ 調整該可調設定點式調節器。 在該容器602之内部容積中,於 626在該内邱交祛由 ° |7器下方的一導管 内部谷積中向下延伸至底端632。導 -口徑開口 634使得當閥頭開啟且 内具有 定點壓力時,氣體铲夠 低於調節器設 上汽動… 箭頭Α指示的方向向 上流動至該調郎器以進行分配。 .在:節器622下方之導管咖的上部份中設置有一薄 膜過慮态兀件628。該薄膜過濾器元件安置在該導管的口 徑開口中且延伸橫跨整個口徑開口。此薄膜過渡器元件可 由PTFE或其他適當材料所製成。 如第13圖所不般,氣體分配包裝的桿狀裝置62〇具有 定特微,讲县JSS ikv人灿 a , .- .. chamber)630 ’該顆粒分離室63〇的特點是其下部分呈現向 外且向上展開的喇D八狀。藉著此種配置方式,此腔室所界 定之流動通道的剖面面積會逐漸向上遞增,直至該腔室的 中間部分。藉著這種遞增的剖面面積,所分配的氣流流速 會逐漸降低至允許顆粒從氣流中分離出來的程度。隨後, 分離出來的顆粒會從分配氣流中掉出而落在該腔室下部分 之向外且向上展開的味| π八狀室壁上。 因此,不含有不想要的顆粒,流體接著流過該腔室的 24Special feature, the particle separation chamber (particulates disengage me nt 200900128 sublayer deposition chamber. '·»· ^ QC1 / rAr m set point regulator or variable set point (adjustable two benefits, such as fixed from the outside of the container The position transmission signal is adjusted: 1. For example, the adjustable set point regulator can be adjusted by the internal or external 詷 _ 谷 谷 602. In the internal volume of the container 602, at 626 The inner Qiu Chuan is extended downward from the inner valley of a duct below the ° |7 to the bottom end 632. The guide-caliber opening 634 allows the gas shovel to be lower than the regulator when the valve head is opened and has a fixed point pressure therein. The direction indicated by the arrow 向上 flows upward to the aligner for distribution. A thin film over-the-counter element 628 is disposed in the upper portion of the catheter coffee below the 624. The membrane filter element is disposed in the The orifice opening of the conduit extends across the entire aperture opening. The membrane transition element can be made of PTFE or other suitable material. As shown in Figure 13, the rod-like device 62 of the gas distribution package has a fixed Special micro, the county JSS ikv can be a, .- .. chamber) 630 'The particle separation chamber 63 〇 is characterized by a lower portion of the lower portion of the outward and upward deployment of the D-eight shape. By this configuration, The cross-sectional area of the flow channel defined by the chamber will gradually increase upward until the middle portion of the chamber. By this incremental cross-sectional area, the flow rate of the dispensed air flow will gradually decrease to allow the particles to separate from the gas stream. Degree. Subsequently, the separated particles will fall out of the distribution gas stream and land on the outwardly and upwardly spreading taste of the lower part of the chamber. Therefore, it does not contain unwanted particles, and the fluid continues. 24 flowing through the chamber
200900128 上部份,該上部份的剖面隨著向上方向 包裝正進行分配操作時,在該腔室的上 流過腔室6 3 0的收縮部分時,氣流的表 velocity)增加,並且進入導管626以及 導管内部通道且實質與流經通道之氣流 過遽器6 2 8來過渡該氣流。 薄膜過濾器6 2 8可由任何適當構造 較佳包含具有適當孔隙度與滲透特性的 分配氣體達到例如製造微電子裝置應用 在一實施例中,該聚合物薄膜包括聚四 他聚合物薄媒材料(例如聚颯、聚醯亞月 器。或者,薄膜過濾器628可由碳織布 述期望之特定用途的編織或非編織材料 通過薄膜過濾器628之後,同樣在 生的過濾後氣體隨後流過調節器622, 通過閥頭組件606中的閥,而於釋放埠 用實,釋放埠610適當地連接至一合適 氣體輸送至下游的使用位置。 將明白到,在調節器622下方的導 曲部(bend),使得調節器622下方的桿 節器上方導管6 2 1之縱向中心線而言以 如,該彎折導管646與導管621之縱向 可能介於10至30度。 在分配操作中,氣體供應包裝的釋 而逐漸縮小。當該 部份中,氣流垂直 面流速(superficial 利用延伸橫跨整個 方向成垂直的薄膜 的材料所製成,且 聚合物薄膜,以使 中的超濾淨品質。 氟乙烯(PTFE)或其 ί等等)的薄膜過濾 或其他適合用於上 听構成。 分配模式下,所產 通過導管621以及 6 1 0分配出去。使 的流動管線,以將 管626可包含一彎 狀裝置相對於該調 一角度而定向。例 中心線之間的夾角 放埠610耦接至一 25 200900128 流動管線,用以輸送所分配的氣體至一下游使 流動官線可能包括管道(piping)、管線(tubing) 以及流量監視和控制裝置,例如流動控制閥、 測器、附加的調節器、溫度監視感測器、 (restricted oriHce device)、幫浦、採樣 口或腔 隨後開啟閥頭組件6 0 6中的閥,例如藉著 輪6 0 8來開啟該閥,或藉著操作一與閥頭組件 的促動器來自動操作該閥。 隨後,若與氣體供應包裝耦接之流動管線 於設定點壓力時,調節器622會運作而開始令 置的設定點壓力流動。用於此種目的的調節器 與一針和提升閥組件接觸的内部固定壓力式 (bellows assembly)或外部可變壓力式波紋管組 由一安裝在提升閥下方的彈簧將該針與提升閥 一正常關閉位置。當波紋管組件感受到一低於 力時’該調節器開啟’造成波紋管擴張而使提 偏壓的正常關閉位置轉換成開啟位置,以讓氣 狀裝置而至該釋放埠以及外接的流動管線。 一但完成該分配操作’可例如藉由手動 608或利用與該閥頭組件之閥耦接的自動促動 閥頭組件606中的閥。 谷器602中的氣體來原材料可以是任何適 料,利如可用於製造微電子產品、製造半導體 製程設備或其他使用可從該容器分配出之氣體 用位置。此 、歧管結才冓 壓力監視感 ^流恐裝置 室等等。 手動旋轉手 中之閥搞接 中的壓力低 氣流以此裝 種類可包括 波紋管組件 件,其中藉 組件偏壓至 設定點的壓 升閥從受到 流流過該桿 旋轉該手輪 器來關閉該 當種類的材 、清洗工業 的應用。例 26 200900128 如,容器602可包含胂、三氟化硼、膦、二硼烷、矽烷或 有機金屬來源試劑。 在本發明使用聚合物薄膜過濾元件之壓力調節氣體供 . 應包裝中,該包裝沒有任何燒結式(frit)過濾器元件或插頭 式金屬基質過濾器元件,故,與過濾氣體有關的壓降問題 可減至最小或完全消除。結果是,桿狀裝置的壓降是由桿 狀裝置中的多個部件所造成,例如整個調節器的壓降、沿 ^ 著桿狀裝置之導管產生的壓降,以及來自桿狀裝置中之分 過濾器元件的壓降。 再者,當薄膜過濾器是由氟化聚合物(例如聚四氟乙烯 或聚對苯二甲酸乙二醇酯)等聚合物材料所形成時,會具有 低表面能量,例如低於30 ergs/cm2的表面自由能。具有此 種特性的薄膜過濾器展現出不明顯的毛細作用,並且能高 效率地從氣流中移除顆粒。因此,相較於在壓力調節容器 中之桿狀裝置内使用熔塊與燒結式金屬基質過濾器作為過 濾器元件時會具有明顯壓降現象而言,薄膜過濾器元件可 Q 達到實質上的進步。 在發展出本發明之前,都相信在内含50至2000 psi " (0.34- 13.8 megaPascals)之高壓氣體來源材料的壓力調節 , 容器中必須使用插座式燒結金屬過濾器或厚熔塊式過濾器 才能達到令人滿意的顆粒捕集效果。本發明表現出不可預 期發現,就是使用薄膜過濾器能有效地從分配氣體中移除 顆粒而不會明顯損害或降低薄膜過濾器的,即使進一步使 用(in extended use)亦然。 27 200900128 此外,使該桿狀裝置的入口偏離該容器内部容積的中 心可具有改善薄膜過濾器之過濾能力的不可預期優點,這 是因為藉由彎曲的桿狀裝置構造來引導氣流,使得分配氣 流具有徑向的流速分量而能掃過薄膜過濾器的表面,進而 改善過濾、效果。In the upper part of 200900128, the section of the upper portion is increased as the upward direction of the package is being distributed, and the flow velocity of the chamber is increased when the chamber passes over the contracted portion of the chamber 630, and the conduit 626 is entered. And the internal passage of the conduit and the gas flow through the damper 6 2 8 flowing through the passage. The membrane filter 268 can be applied, for example, by any suitable configuration, including a distribution gas having suitable porosity and permeation characteristics, for example, in the manufacture of a microelectronic device comprising a polytetracyclic polymer material ( For example, a polyfluorene or a polythene filter. Alternatively, the membrane filter 628 may be passed through a membrane filter 628 after carbon woven to the desired specific use of the woven or non-woven material, and then the raw filtered gas then flows through the regulator. 622, through the valve in the valve head assembly 606, the release 埠 610 is properly connected to a suitable gas for delivery to the downstream use position. It will be understood that the guide portion under the adjuster 622 (bend) For example, the longitudinal centerline of the conduit 621 above the aligner 622 may be, for example, the longitudinal direction of the bend conduit 646 and the conduit 621 may be between 10 and 30 degrees. In the dispensing operation, the gas supply The release of the package is gradually reduced. In this part, the vertical flow velocity of the gas flow (superficial is made of a material that extends across the entire direction of the film, and Film to make the ultra-cleaning quality of the medium. Filtration of fluoroethylene (PTFE) or its ί, etc.) or other suitable for upper listening. In the distribution mode, the distribution is distributed through the conduit 621 and 610. The flow line is configured such that the tube 626 can include a curved device oriented relative to the angle of adjustment. The angle between the centerline 610 is coupled to a 25 200900128 flow line for transporting the dispensed The gas to a downstream allows the flow line to include piping, tubing, and flow monitoring and control devices such as flow control valves, detectors, additional regulators, temperature monitoring sensors, (restricted oriHce device) The pump, the sampling port or the chamber then opens the valve in the valve head assembly 606, for example by opening the valve via the wheel 605, or by operating the valve with the actuator of the valve head assembly. Subsequently, if the flow line coupled to the gas supply package is at the set point pressure, the regulator 622 will operate to initiate the set point pressure flow. The regulator and needle for this purpose The internal fixed pressure (bellows assembly) or external variable pressure bellows set in contact with the component is normally closed by a spring mounted under the poppet valve. When the bellows assembly feels a lower force When the 'opening of the regulator' causes the bellows to expand and the normal closed position of the biasing is switched to the open position, allowing the gas device to reach the release port and the external flow line. Once the dispensing operation is completed, for example The valve in the valve head assembly 606 is automatically actuated by manual 608 or by the use of a valve coupled to the valve head assembly. The gas in the grain 602 can be used as a raw material, such as can be used to manufacture microelectronic products, Manufacturing semiconductor process equipment or other locations where gas can be dispensed from the container. This, the manifold is the result of the pressure monitoring, the flow of equipment, and so on. Manually rotating the valve in the hand to achieve a low pressure air flow. The type of the device may include a bellows assembly member, wherein the pressure riser valve biased to the set point by the component rotates the handwheel from the flow through the rod to close the handle Types of materials, applications in the cleaning industry. Example 26 200900128 For example, vessel 602 can comprise rhodium, boron trifluoride, phosphine, diborane, decane, or an organometallic source reagent. In the pressure regulating gas supply package using the polymer membrane filter element of the present invention, the package does not have any frit filter element or plug metal matrix filter element, so the pressure drop associated with the filtered gas Can be minimized or eliminated altogether. As a result, the pressure drop of the rod-like device is caused by a plurality of components in the rod-like device, such as the pressure drop across the regulator, the pressure drop across the conduit of the rod-like device, and from the rod-like device. Dividing the pressure drop of the filter element. Furthermore, when the membrane filter is formed of a polymer material such as a fluorinated polymer such as polytetrafluoroethylene or polyethylene terephthalate, it will have a low surface energy, for example, less than 30 ergs/ The surface free energy of cm2. The membrane filter having such characteristics exhibits inconspicuous capillary action and can efficiently remove particles from the gas stream. Therefore, the membrane filter element can achieve substantial progress in comparison to the use of a frit and a sintered metal matrix filter as a filter element in a rod-like device in a pressure regulating vessel. . Prior to the development of the present invention, pressure regulation of high pressure gas source materials containing 50 to 2000 psi " (0.34- 13.8 megaPascals) was considered, and a socket sintered metal filter or a thick frit filter must be used in the container. A satisfactory particle trapping effect can be achieved. The present invention exhibits an unpredictable discovery that the use of a membrane filter effectively removes particles from the distribution gas without significantly impairing or reducing the membrane filter, even in extended use. 27 200900128 Furthermore, deviating the entrance of the rod-like device from the center of the internal volume of the container may have the unpredictable advantage of improving the filtration capacity of the membrane filter, since the airflow is directed by the curved rod-like device configuration such that the airflow is distributed It has a radial flow rate component that sweeps across the surface of the membrane filter, improving filtration and effectiveness.
將可明白,相較於使用熔塊式與燒結金屬插座式過濾 元件的容器而言,本發明之使用壓力調節氣體分配容器的 氣體供應包裝可使用單一個或多個薄膜過濾元件,以改善 壓降以及改善分配特性;並且該彎曲的下桿狀裝置構造在 使用該氣體供應包裝時有利於使薄膜過濾器的效率達到最 大。 第1 4圖是根據本發明實施例之流體供應包裝4 0 0的正 視剖面圖,其具有兩個設置在内部的調節器410與412, 以及一薄膜過濾器組件 4 1 8。流體供應包裝包含該容器 406,其界定出一内部容積408且具有一氣體釋放組件,該 氣體釋放組件包含閥頭402以及内部雙調節器流動管線。 下方的調節器412耦接至第一導管414和第二導管416, 該第一導管414與該容器406的縱軸共軸,並且該第二導 管416耦接至該第一導管414和過濾器組件418。第二導 管4 1 6相對於該容器的縱軸設置以一角度,而界定出一銳 夾角。 第15-19圖顯示適用於發明氣體供應包裝之氣體釋放 組件中的薄膜過遽器範例,其在 Anthony DiPrizio、Paul Matthews與Jose Arno於2007年2月16號申請且標題為 28 200900128 「具有聚合物薄膜與金屬支撐件之流體過濾器」的美國臨 時申請案60/901 876號中有更詳細的敘述,且其全文引用 於本案中以供參考。It will be appreciated that the gas supply package of the present invention using a pressure regulating gas distribution container may use a single or multiple membrane filter elements to improve pressure as compared to a container using a fritted and sintered metal receptacle filter element. Lowering and improving dispensing characteristics; and the curved lower rod configuration is advantageous for maximizing the efficiency of the membrane filter when using the gas supply package. Figure 14 is a front cross-sectional view of a fluid supply package 400 having two internally disposed regulators 410 and 412 and a membrane filter assembly 418 in accordance with an embodiment of the present invention. The fluid supply package includes the container 406 defining an interior volume 408 and having a gas release assembly including a valve head 402 and an internal dual regulator flow line. The lower regulator 412 is coupled to the first conduit 414 and the second conduit 416, the first conduit 414 being coaxial with the longitudinal axis of the vessel 406, and the second conduit 416 is coupled to the first conduit 414 and the filter Component 418. The second conduit 4 16 is disposed at an angle relative to the longitudinal axis of the container to define a sharp angle. Figure 15-19 shows an example of a film filter in a gas release assembly for an inventive gas supply package, which was filed on February 16, 2007 by Anthony DiPrizio, Paul Matthews and Jose Arno and titled 28 200900128 "with polymerization The present invention is described in more detail in U.S. Provisional Application Serial No. 60/901,876, the disclosure of which is incorporated herein by reference.
第1 5 -1 9圖的流體過濾器包含一過濾器外殼以及一聚 合物薄膜,該聚合物薄膜設置在多個孔狀支撐板的表面 上,且該些孔狀支撐板固定於該過濾器外殼,該過濾器外 殼配置成可讓流體流過,使得流體從該外殼釋出之前,該 流體會進入該外殼中而接觸到每個孔狀支撐板以及用來過 濾該流體的聚合物薄膜。在一較佳配置中,聚合物薄膜包 括聚四氟乙烯,並且設置每個孔狀支撐板,使一孔狀支撐 板中的該些孔洞與另一孔狀支撐板的孔洞對齊。 第1 5圖是根據本發明實施例之過濾器700的正視剖面 圖。過濾器7 0 0包含一上外殼構件7 0 2,其與下外殼構件 7 0 4的螺紋7 0 6合作地配對接合。在上下外殼構件之間設 置有一過濾、器阻件,該過濾、器阻件包含一下孔狀支樓板 708、一安置在下孔狀支撐板 708上的薄膜過濾器元件 7 1 2,以及設置在該薄膜過濾元件 7 1 2上的上孔狀支撐板 7 1 0。利用該上下外殼構件將此過濾器組件的邊緣壓緊固定 於適當位置。如圖所示,該上下外殼構件可具有相面對的 溝槽,以將〇形環7 14與7 1 6置於溝槽中。 該上外殼構件702定義出一向上收斂的通道722,且 其與導管730的上圓柱狀通道724連通。因此,該過濾器 設置有一流體入口 720,由流體可從該流體入口 720連續 流經下孔狀支撐板7 0 8、薄膜過濾器元件7 1 2以及上孔狀 29 200900128 支撐板710,而流入通道722,且最後進入通道724 第16圖是第15圖過濾器之上部分的立體圖, 該上外殼構件7 0 2的螺紋7 0 6 a以及内含通道7 2 4 I 730。 第17圖是第15圖過濾器之下部分的立體圖, 該下外殼構件704的螺紋706b,以及用來定位該上 板的内側開孔732。 /、 第1 8圖是第1 5圖過濾器之上孔狀支撐板7 1 0 〇 平面圖,顯示其内的多個孔洞744。該板710具有 外周圍742,該無孔外周圍742具有多個延長元件 748,該些延長元件746、748可與該過濾器之下外 的内側開孔(如第1 7圖中所示的開孔7 3 2)配對耦合 第19圖是第15圖之過濾器的底部立體圖,其 下外殼構件704耦接的上外殼構件702。該過濾器 件760包含下孔狀支撐板708,該孔狀支撐板708 多個孔洞 744,以使薄膜元件暴露於流入的氣流中 (J 過含有下孔狀支撐板、薄膜過濾器元件與上孔狀支 過濾器元件組件,並且釋放至導管73 0。 • 雖然文中已舉出多個特定態樣、特徵和實施例 . 本發明,但該領域中具有通常知識者根據本文說明 明白到本發明的應用不僅限於此,而是可擴大應用 多種其他變化、修飾與替換實施例。因此,對於以 求的發明應做最大範圍的理解與解釋,其包含落入 精神與範圍中的所有變化、修飾與替代實施例。 其顯示 的導管 其顯示 下孔狀 的上視 一無孔 746與 殼構件 〇 顯示與 元件組 中具有 ,而通 擇板的 來說明 内容將 且含蓋 下所請 本發明 30 200900128 【圖式簡單說明】 第1圖(先前技藝)顯示一種内部調節材料儲存及氣體 分配包裝的剖面正視圖,其可實施本發明而加以改良。 第2圖係實施本發明改良處所做的閥頭與相連桿狀裝 置之實施例的正視圖。The fluid filter of the first to fifth embodiments includes a filter housing and a polymer film disposed on a surface of the plurality of hole-shaped support plates, and the hole-shaped support plates are fixed to the filter An outer casing, the filter outer casing being configured to allow fluid to flow therethrough such that the fluid enters the outer casing to contact each of the perforated support plates and the polymeric film used to filter the fluid prior to release of the fluid from the outer casing. In a preferred configuration, the polymeric film comprises polytetrafluoroethylene and each of the apertured support plates is disposed such that the apertures in one of the apertured support plates are aligned with the apertures of the other apertured support plate. Figure 15 is a front cross-sectional view of a filter 700 in accordance with an embodiment of the present invention. The filter 700 includes an upper outer casing member 702 that mates with the threads 706 of the lower outer casing member 704. A filter and a blocker are disposed between the upper and lower outer casing members, and the filter and the blocker comprise a lower hole-shaped floor slab 708, a membrane filter element 7 1 2 disposed on the lower hole-shaped support plate 708, and The upper aperture-shaped support plate 7 1 0 on the membrane filter element 7 1 2 . The edges of the filter assembly are pressed and held in place by the upper and lower outer casing members. As shown, the upper and lower outer casing members can have facing grooves to place the shackles 7 14 and 716 in the grooves. The upper outer casing member 702 defines an upwardly converging passage 722 that communicates with the upper cylindrical passage 724 of the conduit 730. Therefore, the filter is provided with a fluid inlet 720 through which fluid can continuously flow through the lower hole-shaped support plate 708, the membrane filter element 711, and the upper hole 29 200900128 support plate 710, and flow in. Channel 722, and finally access channel 724 Figure 16 is a perspective view of the upper portion of the filter of Figure 15, the upper housing member 70 2 thread 70 6 a and the internal channel 7 2 4 I 730. Figure 17 is a perspective view of the lower portion of the filter of Figure 15, the thread 706b of the lower outer casing member 704, and the inner opening 732 for positioning the upper plate. /, Fig. 18 is a plan view of the hole-shaped support plate 7 1 0 之上 above the filter of Fig. 5, showing a plurality of holes 744 therein. The plate 710 has an outer periphery 742 having a plurality of elongate members 748 that are openable to the inner side of the filter (as shown in Figure 17) Opening 7 3 2) Pairing Coupling Fig. 19 is a bottom perspective view of the filter of Fig. 15 with the lower outer casing member 702 coupled to the lower outer casing member 704. The filter device 760 includes a lower hole-shaped support plate 708 having a plurality of holes 744 for exposing the film member to the inflowing airflow (J over the lower hole-shaped support plate, the membrane filter member and the upper hole) The filter element assembly is spliced and released to the conduit 73 0. • While a number of specific aspects, features, and embodiments have been presented herein, the present invention is understood by those of ordinary skill in the art The application is not limited to this, but can be applied to a variety of other variations, modifications and alternative embodiments. Therefore, the invention should be interpreted and interpreted to the fullest extent, including all changes, modifications and modifications falling within the spirit and scope. An alternative embodiment. The catheter shown therein exhibits a lower hole-like top view, a non-porous 746, and a shell member 〇 display and a component set, and the passage of the plate to illustrate the content and cover the present invention 30 200900128 BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 (previous art) shows a cross-sectional elevation view of an internal conditioning material storage and gas distribution package that can be implemented And to be improved. Fig. 2 a front view of the valve head improved system of the embodiment of the present invention is made by means connected to the rod of the embodiment of FIG opposed.
第3圖是根據本發明實施例實施本發明之改良的閥頭 與相連桿狀裝置的正視圖。 第4圖顯示不同過濾介質之包裝外濕氣釋氣(ppb)與 時間(分鐘)的關係圖。 第5圖顯示不同過濾介質之包裝外氧氣釋氣(〇2,ppb) 與時間(分鐘)的關係圖。 第6圖顯示不同過濾介質暴露在環境空氣下暴露24 小時所展現水過濾濃度(ppb)與時間(分鐘)的關係圖。 第7圖顯示入口壓力為60 psig下,不同過濾介質在 受到差壓時,差壓與流速(標準公升/分鐘)的關係圖。 第8圖是PTFE過濾器介質的顯微照片。 第9圖顯示可用於本發明之氣體供應包裝中的流動控 制器之侧視剖面圖。 第1 0圖顯示氣體依次流經第9圖流動控制器之多個盤 狀元件的氣體流動路徑之立體圖。 第11圖是可用於本發明各種實施例之氣體供應包裝 中的薄膜式過濾器之部分剖開側視圖。 第12圖是在23°C下,當入口壓力分別為30psig(上方 31 200900128 線)與60 psig(下方線)時,差壓與流速的關係圖。 第1 3圖是根據本發明另一實施例之氣體供應包裝的 正視且部分剖開圖。 第1 4圖是根據本發明實施例之流體供應包裝的正視 剖面圖,其具有兩個設置在内部的調節器以及一薄膜過濾 器組件。 第1 5圖是根據本發明實施例之過濾器的正視剖面圖。 第16圖是第15圖過濾器之上部分的立體圖。 第17圖是第15圖過濾器之下部分的立體圖。 第18圖是第15圖過濾器之孔板的上視平面圖。 第19圖是第15圖之過濾器的底部立體圖。 [主 •要 •元 .件 符 號說明 ] 100 氣 體 分 配 包裝 102 容 器 104 圓 筒 側壁 106 底 板 構 件 108 頸 部 110 頸 圈 112 螺 紋 栓 塞 114 閥 頭 組 件 116 填 充 通 道 118 手 輪 120 中 央 流 體 流動通 道 122 閥 元 件 124 出 口 128 内 部 容 積 130 連 接 器 流 管 131 擴 散 氣 蓋 端 132 調 A-/T 即 器 134 過 ?慮 器 單 元 136 接 頭 200 流 動 控 制 器 202 主 圓 柱 外 殼 204 筒 狀 部 位 32 200900128 206 開放末端 210 、220 開 α r 212 、214 、 21 6 盤狀物 208 、2 1 8圓柱延長部 240 閥頭 242 上壓力調 即 器 244 下壓力調 即 器 246 管道 248 彎曲部 250 薄膜過濾 器 260 閥頭 262 調節器 264 管道 266 彎曲部 268 過濾裝置 270 底部開口 300 盤組件 302 頂盤 304 狹缝開口 306 中間盤 308 中央開口 310 底盤 400 流體供應 包 裝 402 閥頭 406 容器 408 内部容積 410 、412調節; i 414 第一導管 416 第二導管 41 B 薄膜過濾 器 組件 500 薄膜式過 濾 器 502 開放末端 504 主外殼 506 進氣管 508 出氣管 510 開放釋放 末 端 512 内部體積 5 14 薄膜過濾 器 元件 600 氣體供應 包 裝 602 容器 604 内部容積 606 閥頭組件 608 手輪 610 釋放埠 620 桿狀裝置 621 上導管 622 調節器 624 導管 33 200900128 626 導管 628 薄 膜 過 ;慮 器 630 顆粒分 離室 632 底 端 634 口徑開 口 700 過 滤 器 702 上外殼 構件 704 下 外 殼 構 件 706 ' 706a 、706b螺紋 708 孔 狀 支 撐 板 710 孔狀支 撑板 712 薄 膜 過 遽 元 件 714 、7 1 6 0形環 720 流 體 入 σ 722 通道 724 通 道 730 導管 732 開 孔 742 外周圍 744 孔 洞 746 、748延長元件 760 過 ’/慮 器 元 件 組件Figure 3 is a front elevational view of a modified valve head and associated rod assembly embodying the present invention in accordance with an embodiment of the present invention. Figure 4 shows a plot of moisture outgassing (ppb) versus time (minutes) for different filter media. Figure 5 shows the relationship between oxygen outgassing (〇2, ppb) and time (minutes) outside the package of different filter media. Figure 6 shows the water filtration concentration (ppb) versus time (minutes) for different filter media exposed to ambient air for 24 hours. Figure 7 shows a plot of differential pressure versus flow rate (standard liters per minute) for different filter media at differential pressures at 60 psig. Figure 8 is a photomicrograph of a PTFE filter media. Figure 9 shows a side cross-sectional view of a flow controller that can be used in the gas supply package of the present invention. Figure 10 shows a perspective view of the gas flow path through which the gas sequentially flows through the plurality of disk members of the flow controller of Figure 9. Figure 11 is a partially cutaway side elevational view of a membrane filter useful in a gas supply package in accordance with various embodiments of the present invention. Figure 12 is a plot of differential pressure vs. flow rate at 23 °C for inlet pressures of 30 psig (upper 31 200900128 line) and 60 psig (lower line). Figure 13 is a front and partial cutaway view of a gas supply package in accordance with another embodiment of the present invention. Figure 14 is a front elevational cross-sectional view of a fluid supply package having two internally disposed regulators and a membrane filter assembly in accordance with an embodiment of the present invention. Figure 15 is a front cross-sectional view of a filter in accordance with an embodiment of the present invention. Figure 16 is a perspective view of the upper portion of the filter of Figure 15. Figure 17 is a perspective view of the lower portion of the filter of Figure 15. Figure 18 is a top plan view of the orifice plate of the filter of Figure 15. Figure 19 is a bottom perspective view of the filter of Figure 15. [Main • Elements • Symbol Description] 100 Gas Distribution Package 102 Container 104 Cylinder Side Wall 106 Base Plate Member 108 Neck 110 Collar 112 Threaded Plug 114 Valve Head Assembly 116 Filling Channel 118 Hand Wheel 120 Central Fluid Flow Channel 122 Valve Element 124 Outlet 128 Internal Volume 130 Connector Flow Tube 131 Diffusion Gas Cover End 132 A-/T 134 Transmitter Unit 136 Joint 200 Flow Controller 202 Main Cylindrical Shell 204 Cylindrical Section 32 200900128 206 Open End 210 220 open α r 212 , 214 , 21 6 disc 208 , 2 1 8 cylindrical extension 240 valve head 242 upper pressure regulator 244 lower pressure regulator 246 pipe 248 bending portion 250 membrane filter 260 valve head 262 Regulator 264 Pipe 266 Bend 268 Filter Device 270 Bottom Opening 300 Disc Assembly 302 Top Plate 304 Slit Opening 306 Intermediate Disk 308 Central Opening 310 Chassis 400 Fluid Supply Package 402 Valve Head 406 408 internal volume 410, 412 adjustment; i 414 first conduit 416 second conduit 41 B membrane filter assembly 500 membrane filter 502 open end 504 main housing 506 inlet tube 508 outlet tube 510 open release end 512 internal volume 5 14 Membrane filter element 600 gas supply package 602 container 604 internal volume 606 valve head assembly 608 hand wheel 610 release 埠 620 rod device 621 upper conduit 622 regulator 624 conduit 33 200900128 626 conduit 628 membrane erector 630 particle separation chamber 632 Bottom end 634 aperture opening 700 filter 702 upper housing member 704 lower housing member 706 '706a, 706b thread 708 hole-shaped support plate 710 hole-shaped support plate 712 film over-twist element 714, 7 1 6 0-ring 720 fluid into σ 722 Channel 724 Channel 730 Catheter 732 Opening 742 Outer Peripheral 744 Hole 746, 748 Extension Element 760 Over the component component
3434
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US90187607P | 2007-02-16 | 2007-02-16 | |
US94987007P | 2007-07-15 | 2007-07-15 |
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CN109342555A (en) * | 2018-12-12 | 2019-02-15 | 爱德森(厦门)电子有限公司 | Split eddy current sensor in a kind of in-service track switch crosslinking small―gap suture rail bottom corner |
TWI651258B (en) * | 2012-09-21 | 2019-02-21 | 恩特葛瑞斯股份有限公司 | Fluid supply package and method of suppressing pressure oscillation in gas dispensed from pressure-regulated vessel |
US12025997B2 (en) | 2018-05-04 | 2024-07-02 | Entegris, Inc. | Regulator stability in a pressure regulated storage vessel |
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KR102277235B1 (en) * | 2014-10-03 | 2021-07-13 | 엔테그리스, 아이엔씨. | Pressure-regulated gas supply vessel |
KR102513246B1 (en) * | 2018-06-22 | 2023-03-27 | 린데 게엠베하 | Cylinder valves and methods for inhibiting the formation of contaminants in cylinders and cylinder valves |
CN218914538U (en) * | 2021-04-30 | 2023-04-25 | 恩特格里斯公司 | Storage container for containing reagent material |
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RU2016820C1 (en) * | 1991-06-29 | 1994-07-30 | Анатолий Яковлевич Столяревский | Method for producing excess pressure of gaseous carbon dioxide inside working volume of package |
BE1006130A3 (en) * | 1992-08-19 | 1994-05-17 | Belgium Spray Accessory Factor | Aerosol. |
JPH0622699U (en) * | 1992-08-21 | 1994-03-25 | 株式会社三谷バルブ | Gas burner container |
US6343476B1 (en) * | 1998-04-28 | 2002-02-05 | Advanced Technology Materials, Inc. | Gas storage and dispensing system comprising regulator interiorly disposed in fluid containment vessel and adjustable in situ therein |
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2008
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TWI651258B (en) * | 2012-09-21 | 2019-02-21 | 恩特葛瑞斯股份有限公司 | Fluid supply package and method of suppressing pressure oscillation in gas dispensed from pressure-regulated vessel |
US12025997B2 (en) | 2018-05-04 | 2024-07-02 | Entegris, Inc. | Regulator stability in a pressure regulated storage vessel |
CN109342555A (en) * | 2018-12-12 | 2019-02-15 | 爱德森(厦门)电子有限公司 | Split eddy current sensor in a kind of in-service track switch crosslinking small―gap suture rail bottom corner |
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