TWI296532B - A method for generation of an atomized liquid and a sprinkler - Google Patents

A method for generation of an atomized liquid and a sprinkler Download PDF

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TWI296532B
TWI296532B TW94115267A TW94115267A TWI296532B TW I296532 B TWI296532 B TW I296532B TW 94115267 A TW94115267 A TW 94115267A TW 94115267 A TW94115267 A TW 94115267A TW I296532 B TWI296532 B TW I296532B
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liquid
flow
sprinkler
partition wall
axial passage
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TW94115267A
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Chinese (zh)
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Andrey Leonidovich Dushkin
Alexander Vladimirovich Karpyshev
Nikolai Nikolaevich Ryazanczev
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Andrey Leonidovich Dushkin
Alexander Vladimirovich Karpyshev
Nikolai Nikolaevich Ryazanczev
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1296532 九、發明說明: 【發明所屬之技術領域】 本务明係關於液體霧化過程及設計用於液體霧化之技術 構件,例如喷灑器。特定言之,本發明可用作自動滅火系 統之一部分用於撲滅諸如醫院、圖書館、博物館、辦公大 樓、倉庫、車庫等内之房間内具有諸多可能之起火點之火 災。 【先前技術】 當前已知有多種產生霧化液體流之方法。例如,德國專 利 10010881(IPC A62C 37/00,2001.09.13頒佈)即闡述一種 產生霧化液體流之方法,包括在壓力下將液體供應至一液 體霧化器之軸向通道中。該液體流藉由安裝在該霧化器軸 向通道中之分隔牆分割成兩個流。於流動通道内形成與該 分隔牆之一對稱平面對稱之液體流。將液體以切線方式供 入該等流動通道内會促進液體流於流動通道内在相反方向 上之璇流。於設置在流動通道出口處一腔室之流動通道内 所產生之液體流經混合以生成一湍動液體流。該腔室内所 產生之該合成滿動液體流經由該喷灑器通道之一出口開口 而霧化。 該先前技術之方法及設備允許產生具有一大範圍錐度之 錐形霧化液體流並允許改變液滴大小。藉由改變出口開口 部分即可以供入霧化器中液體之一恒定壓力調節氣體與液 滴喷射流之參數。可藉助使用對置於出口開口設置之一異 形折流板進一步湍流化該液體流。應指出,該先前技術之 101695.doc 1296532 設備未配備一 啟動一霧化器 熱 門後,液體即被供入霧化器中。 響應單元以在達到―預定周圍溫度時自動 當打開安裝於-主管線内之-共用分配闕 於自動滅火系統中1296532 IX. Description of the invention: [Technical field to which the invention pertains] The present invention relates to a liquid atomization process and a technical component designed for liquid atomization, such as a sprayer. In particular, the present invention can be used as part of an automatic fire suppression system for extinguishing fires with many possible fire points in rooms such as hospitals, libraries, museums, office buildings, warehouses, garages, and the like. [Prior Art] A variety of methods for generating an atomized liquid stream are currently known. For example, German Patent No. 10010881 (issued by IPC A62C 37/00, issued Jun. 2001.13) describes a method of producing a flow of atomized liquid comprising supplying the liquid under pressure into an axial passage of a liquid atomizer. The liquid stream is split into two streams by a dividing wall installed in the axial passage of the atomizer. A liquid flow symmetrically planar to one of the dividing walls is formed in the flow passage. The tangential supply of liquid into the flow channels promotes turbulent flow of liquid in the opposite direction within the flow channel. The liquid produced in the flow passage provided in a chamber at the outlet of the flow passage is mixed to produce a turbulent liquid flow. The synthetic full-flooding liquid stream produced within the chamber is atomized via an outlet opening of the sprinkler channel. The prior art method and apparatus allow for the production of a conical atomized liquid stream having a wide range of taper and allows for varying droplet sizes. By varying the outlet opening portion, one of the liquids in the nebulizer can be supplied with a constant pressure regulating gas and droplet ejection stream parameters. The liquid stream can be further turbulent by using a shaped baffle disposed opposite the outlet opening. It should be noted that the prior art 101695.doc 1296532 device is not equipped with a starter-atomizer hot door and the liquid is supplied to the atomizer. The response unit automatically opens when installed in the -main line, when the predetermined ambient temperature is reached, in the automatic fire extinguishing system

可使用具有單動閥門之噴灑器來進 行液體霧化,該閥門配備有熱響應單元。 美國專利48_61(IPC Μ% 37/1〇,聊〇1丄頒佈)揭示 -種喷濃器之結構’其包含一具有圓柱形軸向液體供應通 道之外殼。。該轴向通道之―出σ與四個流動通道相連通。 -熱響應單元係藉助一附裝配件而固定於該喷灑器外殼Liquid atomization can be performed using a sprinkler with a single-acting valve equipped with a thermal response unit. U.S. Patent No. 48_61 (IPC 37% 37/1, issued by 〇 〇 ) ) ) ) 揭示 揭示 揭示 揭示 揭示 揭示 揭示 揭示 揭示 揭示 揭示 揭示 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 . The "out" of the axial passage is in communication with the four flow passages. - the thermal response unit is fixed to the sprinkler housing by means of an attachment

^ -偏㈣係連接至-閥門’該闕⑽閉該圓柱形轴向 液體供應通道之-人口開口。可藉助_組態為—水平定位 測溫球頭之熱響應單元將該閥門連同該偏轉板—起維持在 :初始位置中。該等流動通道之出口開口皆均句分配在該 喷m器外殼-端部表面上之圓周周圍。設置該等流動通道 之對稱軸線與該轴向液體供應通道之對稱軸線成一角度。 一渦流產生腔室係設置在該喷灑器外殼之中心。 +使用-該先前技術之喷灑器可產生一具有大液滴之霧化 喷射流以提高滅火效率且降低液體消耗。然而,由於液體 2朝向附裝配件之結構組件霧化,故在分配霧化液體噴射 流之過程中產生遮蔽效應、4#上述效齡增㈣滴喷射 之非均勻分配。 自馱’州專利 0701842(IPC A62C 37/08,1996.03.20 頒佈) 中,人們知曉一種產生霧化液體喷射流之喷灑器及方法。 該噴灑器包括:具有一圓柱形軸向通道之外殼、一包括一 101695.doc Ϊ296532 杜^熱響應單元及一包括柩架臂之熱響應單元附裝配 。畲達到-預定周圍溫度且熱響應單元打㈣,液體將 會在一壓力下被供入噴灑器之軸向通道。根據先前技術之 卷明,可藉助安裝在噴灑器軸向通道内之一環形分割分 隔牆將液體流分割成兩個共軸流。在設置於分隔牆一二 面上之螺旋流動通道内會產生__外側職液體流。在分隔 牆之-内部軸向通道内會產生一中心軸向液體流。而該等^ - Partial (four) is connected to the - valve 'The 阙 (10) closes the cylindrical axial liquid supply channel - the population opening. The valve can be maintained in the initial position together with the deflector by means of a _configured-horizontal positioning thermal response unit of the temperature measuring ball. The outlet openings of the flow channels are all distributed around the circumference of the end surface of the sprayer housing. The axis of symmetry of the flow channels is set at an angle to the axis of symmetry of the axial liquid supply channel. A vortex generating chamber is disposed in the center of the sprinkler housing. + Use - This prior art sprinkler produces an atomized jet with large droplets to increase fire suppression efficiency and reduce liquid consumption. However, since the liquid 2 is atomized toward the structural component of the attached fitting, a shadowing effect is generated in the process of dispensing the atomized liquid jet, and the non-uniform distribution of the above-mentioned four-in-one (four) drop jet is generated. A sprinkler and method for producing an atomized liquid jet is known from the 'state patent 0701842 (IPC A62C 37/08, issued 1996.03.20). The sprinkler includes a housing having a cylindrical axial passage, a housing including a 101695.doc 296532 thermal response unit, and a thermal response unit including a truss arm. The 畲 reaches - the predetermined ambient temperature and the thermal response unit is hit (4), and the liquid will be supplied to the axial passage of the sprinkler under a pressure. According to the prior art, the liquid flow can be split into two coaxial flows by means of a circular split partition wall mounted in the axial passage of the sprinkler. In the spiral flow channel disposed on the second side of the partition wall, a liquid flow of __ outside is generated. A central axial flow of fluid is created within the internal axial passage of the dividing wall. And so

合成流被送人設置於噴讓器出口開口之—軸向通道上游的 一渦流化腔室中。 ”亥既疋方法及㈣允許產生可精細分散之霧化液體喷射 流’該等噴射流具有適於滅火之最佳液滴大小並可對一火 災現場提供快速及有狀滅火。然而,先前技術之喷灑器 結構無法產生空間均勻霧化之液體喷射流。 該霧化液體流與熱響應單元附裝配件之組件之接合將會 導致產生有助於提高霧化液體分配之非均勻性之遮蔽效 應。自軸向通道開口流出之液體流之一部分會在接觸熱響 應單元附裝配件之框架臂後改變其方向。在由附裝配件之 框架臂所遮蔽之區域内產生多個低喷灑強度之區域,而在 一自由空間内该專經分割流之接合邊界處產生多個喷灌強 度增大之區域。由此,不能對一巨大面積之火災現場提供 均勻滅火。 最接近於所申請專利方法之類似方法係一於美國專利 6073700(IPC A62C39/00,2000.06.13頒佈)中所闡述之產生 一霧化液體喷射流之方法。熱響應單元之一熱敏組件在一 101695.doc 1296532 預疋周圍溫度時之啟動會導致一液體供應閥門被打開以將 液體供入τ麗器之一圓柱形軸向通道中。相應地,與該閥 門安裝在同一桿上的液體流偏轉板移位至其較低運作位 置。液體在一預定壓力下被送入噴灑器軸向通道内,並於 其中藉助安裝於喷灑器軸向通道内之分隔牆被分割成兩個 單獨的流。對稱於分隔牆之一對稱平面之液體流形成於彎 曲开》流動通道内。由此形成之液體流被供應至喷灑器之一 Φ 會聚軸向通道之出口開口以因該等流與偏轉板之接合而在 環繞空間内被霧化。此將導致產生一精細分散之霧化液體 噴射流。 應注意,該噴灑器結構之一重要組件係一用於偏轉板及 熱響應單元之附裝配件,包括固定在該噴灑器外殼上之框 架臂。因此,在液體於置放有附裝配件框架臂之空間區域 内霧化後,該等液體流部分地與喷灑器結構組件相貫穿。 作為一結果,將產生具有不同霧化強度且因此具有對一擬 保護之表面不同噴灑強度之區域。 最接近於所請求專利設備之類似設備係上述美國專利 6073700中所揭示之一喷灑器。該先前技術之噴灑器包括一 具有一圓柱形軸向液體供應通道之外殼,其中安裝有一八 隔牆以將該軸向通道分割成兩個與該分隔牆之一對稱平2 對稱之彎曲形流動通道。藉助該噴灑器之下部部分内一附 裝配件安裂一熱響應單元及一液體流偏轉板。 、 熱響應單元係由兩個熱敏機構組成。第一機構包括一I 一閥門相連接且由一形狀記憶合金製作之組件。一熱敏^ 101695.doc 1296532 献塑\:外成之τ部部分内並連接至-液體供應閥門。該 、、、曰’單元之第-熱敏機構位於該軸向通道之出口開口對 ^ 口於將分隔牆維持在其上部4立置。言亥第二熱敏機構 包:t一由易熔合金製作之組件所夾持之多個板。The resultant stream is sent to a vortex chamber located upstream of the axial passage of the sprayer outlet opening. "Hai 疋 method and (4) permit the production of finely dispersible atomized liquid jets. These jets have an optimum droplet size suitable for fire suppression and provide rapid and fire extinguishing for a fire scene. However, prior art The sprinkler structure is incapable of producing a spatially uniform atomized liquid jet. The engagement of the atomized liquid stream with the components of the thermal response unit attachment assembly will result in a shadow that contributes to the non-uniformity of the atomized liquid distribution. Effect: A portion of the liquid flow exiting the axial passage opening changes its orientation after contacting the frame arm of the thermal response unit attachment. A plurality of low spray intensities are produced in the area shielded by the frame arms of the attached fitting. The area, and the area where the sprinkling intensity is increased at the joint boundary of the dedicated split flow in a free space. Therefore, it is impossible to provide uniform fire extinguishing to a large area of the fire scene. The closest to the patented method A similar method is a method of generating an atomized liquid jet as described in U.S. Patent No. 6,073,700 (issued to IPC A62C39/00, issued Jun. 2000. The activation of one of the unit's heat-sensitive components at a pre-clamping ambient temperature in 101695.doc 1296532 results in a liquid supply valve being opened to supply liquid into one of the cylindrical axial passages of the τ 丽. Accordingly, with the valve The liquid flow deflector mounted on the same rod is displaced to its lower operating position. The liquid is fed into the axial passage of the sprinkler at a predetermined pressure and is separated therein by means of an axial passage mounted in the sprinkler The wall is divided into two separate streams. A liquid flow symmetrical to one of the symmetrical planes of the dividing wall is formed in the curved opening. The liquid stream thus formed is supplied to one of the sprinklers Φ Converging axial channels The outlet opening is atomized in the surrounding space due to the engagement of the flow with the deflector plate. This will result in a finely dispersed atomized liquid jet. It should be noted that one of the important components of the sprinkler structure is used for The attachment member of the deflector plate and the thermal response unit includes a frame arm fixed to the sprinkler housing. Therefore, after the liquid is atomized in a space region in which the attachment member frame arm is placed, the liquid The body flow partially penetrates the sprinkler structure assembly. As a result, regions having different atomization intensities and thus different spray strengths to a surface to be protected are produced. The closest device to the claimed patented device A sprinkler disclosed in the above-mentioned U.S. Patent No. 6,073,700. The prior art sprinkler includes a housing having a cylindrical axial liquid supply passage, wherein an eight partition wall is mounted to divide the axial passage into two a curved flow passage symmetrical with one of the partition walls. The heat-responsive unit and a liquid flow deflecting plate are separated by an attachment fitting in the lower portion of the sprinkler. The thermal response unit is composed of two heats. The first mechanism comprises an I-valve connected and assembled by a shape memory alloy. A thermal ^ 101695.doc 1296532 plastic \: externally formed in the τ portion and connected to the - liquid supply valve . The first heat-sensitive mechanism of the unit, the 曰' unit is located at the outlet opening of the axial passage to maintain the partition wall at its upper portion 4. The second thermal mechanism of the haihai package: t a plurality of plates held by components made of fusible alloy.

田卷生火x時,該由形狀記憶合金製作之熱敏元件被加 ”、、至形狀"己憶恢復溫度。該熱敏組件會在一垂直方向上 伸長以將閥門維持在其關閉位置。喷灑器周圍空氣溢度之 進步増加導致由易熔合金製作之組件熔化。作為一結 果支撐板與噴灑器分離以致使偏轉板移至其下部運作位 置。與此同時,液體供應閥門打開將液體供入喷灑器之圓 柱形軸向通道内。 〜之根據上述揭示於美國專利6 〇 7 3 7 〇 〇中之用於產生霧 化液體噴射流之方法可達成喷灑器之作業並產生霧化液體 喷射流。應注意,該方法及設備之一本質特徵係與因該等 液體AIL與附裝配件組件間之貫穿而致使受保護表面上液體 非均句霧化相關之一限制。 【發明内容】 欲申請專利之本發明之目標係解決一旨在消除與組件結 構對一所產生霧化液體噴射流内液滴空間分配之影響相關 之問題之技術任務。 所達成之技術結果包括產生具有高動能液滴及液滴之均 勻空間分配之精細分散氣體及液滴喷射流,此對有效撲诚 火災現場具特別重要之意義。 上述技術效果係藉由實施一產生霧化液體噴射流之方法 10l695.doc -10- 1296532 ===2括:當—-預定值且該 灑器之-軸向通道内。= :麼力下將液體供入該噴 助安襄在該噴過程進一步包括:藉 割成兩個流,且二.道内之一分隔牆將該液體流分 平面之”於^動通道内形成對稱於-分隔牆之對稱 十面之多個液體流。兮笙# $ a 7蚺 接合而被霧化,液體流藉由與—偏轉板When the field coil is fired, the heat-sensitive element made of the shape memory alloy is added to the shape and the temperature is restored. The heat-sensitive assembly is elongated in a vertical direction to maintain the valve in its closed position. An increase in the air spill around the sprinkler causes the assembly of the fusible alloy to melt. As a result, the support plate is separated from the sprinkler to cause the deflector to move to its lower operating position. At the same time, the liquid supply valve opens to liquid Served into the cylindrical axial passage of the sprinkler. The method for producing an atomized liquid jet according to the above-mentioned U.S. Patent No. 6, 〇7 3 7 可 can achieve the operation of the sprinkler and generate fog. Liquid jet flow. It should be noted that one of the essential features of the method and apparatus is limited by the penetration of the liquid non-uniform spray on the protected surface due to the penetration between the liquid AIL and the accessory component. The object of the invention to be patented is to solve a problem associated with the elimination of the effect of the component structure on the spatial distribution of droplets within an atomized liquid jet produced. Technical Tasks The technical results achieved include the production of finely dispersed gases and droplet jets with a uniform spatial distribution of high kinetic energy droplets and droplets, which is of particular importance for effective fire scenes. The method for producing an atomized liquid jet by the implementation of a method is described in the following: 10: 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 The spray-assisted ampoule further comprises: by cutting into two streams, and one of the dividing walls of the second channel divides the liquid flow into a plane, and forms a symmetrical ten-sided symmetry in the partition wall. Multiple liquid streams.兮笙# $ a 7蚺 Engaged and atomized, liquid flow by means of - deflector

^^ ^ ^ μ偏轉板係藉助—用於偏轉板及用於該噴 / 麗窃之敎塑廡n 姑…應早凡之附裝配件固定在喷麗器外殼上。該附 裝配件包括數個框架臂。 根據本Is明,於流動通道内產生該等液體流,以繞過用 ,該偏轉板及用於該熱響應單元之附裝配件之該等框架 # »亥等框架臂係定位於安裝在該軸向通道内之分隔牆之 、一對稱平面中。在框架臂之此一佈置下,在該喷麗器轴向 通道=出口處產生水流’以繞過用於該偏轉板及用於該熱 響應單元之附裝配件之該等框架臂。 述附4配件之框架臂及流動通道出口之相對佈置會減 少通常在液體流與障礙物(在特定情形下,與附裝配件之框 架臂)交切時所發生之流之動能損失。 為提供一最適合於使液體流能夠繞過框架臂且因此最適 合於改良霧化液體喷射流内液滴分配之均勻性之模式,需 要創造各種條件以在靠近出口開口之區域内於具有一組態 為一圓環段之橫截面之流動通道内產生液體流。 該等藉助流動通道所形成之液體流具有數個中心區,於 該些中心區内液體平行於分隔牆之一對稱平面流動。此一 101695.doc 11 1296532 流動會促使產生一均勾液體膜且在液體流與偏轉板接合時 使该液體流有效地偏轉。 為產生具有高動能液滴之—均勾精細分散之氣體及液滴 喷射流’在具有一根據4Du】〇D條件所選擇之一長度[之 流動通道内形成該等液體流,其中㈣—内切於流動通道之 一出口部分内之圓環之最大直徑。 該等流動通道之m絲據提供液體之穩定流動之 φ條件選擇。該等流動通道之長度L大於i〇d會因液體流與流 動通道表面之摩擦而導致液體動能之損失增加。該等流動 通道之長度L小於4D可能導致液體流㈣偏離確保擬霧化 液體之最大均勻空間分配之方向。 為增大液滴速度及該霧化喷射流内液滴空間分配之均勻 性,在液體流動過程中會聚之流動通道内產生液體流。 為防止固體污染物阻礙流動通道,在被供應經過該等流 動通道之刖,流過喷灑器軸向通道之液體流須經過濾。 • 較佳藉助具有一扁平連續中心部分之偏轉板霧化所產生 之液體流’該扁平連續中心部分被限制在該圓柱形軸向通 道之伸出部分之幾何邊界内。此外,該偏轉板之邊緣可製 成夕孔狀且可組態為一能夠在液體流動過程中分散液體流 之錐形表面。使用偏轉板之上述實施例來霧化液體允許以 一氣體及液滴噴射流之預定均勻性、分散性及強度增加喷 麗面積。 上述技術結果亦可藉由使用一噴灑器而達成,該噴灑器 & &:—包括一圓柱形軸向液體供應通道之外殼,在該液 101695.doc -12- 1296532 體供應通道中安裝有一分隔牆以將該軸 、 對稱於該分隔牆之-對稱平面的流動通道通道分割成兩個 之熱響應單元;-液體流偏轉板;及包括一閥門 及用於包括多個框架臂之偏轉板之附用於5亥熱響應單元 明,用於熱響應單元及用於偏轉板之附根據本發 臂皆定位於該軸向通道内該分隔牆之=< °亥等框架The ^^ ^ ^ μ deflection plate is attached to the squirt housing by means of the yoke for the yoke and the shovel. The accessory accessory includes a number of frame arms. According to the present invention, the liquid flow is generated in the flow passage for bypassing, and the frame and the frame arm for the attachment member of the thermal response unit are positioned to be mounted thereon. In a plane of symmetry of the dividing wall in the axial passage. In this arrangement of frame arms, a flow of water is produced at the axial passage = outlet of the lance to bypass the frame arms for the deflector and the attachment for the thermal response unit. The relative arrangement of the frame arms and flow channel outlets of the 4 fittings reduces the kinetic energy loss that typically occurs when the liquid flow intersects the obstacle (in certain instances, the frame arm of the attachment). In order to provide a mode that is most suitable for enabling liquid flow to bypass the frame arm and is therefore most suitable for improving the uniformity of droplet distribution within the atomized liquid jet, various conditions need to be created to have a region near the outlet opening. A liquid flow is created in the flow channel configured as a cross section of a ring segment. The liquid stream formed by the flow channels has a plurality of central regions in which the liquid flows parallel to a plane of symmetry of the dividing wall. This 101695.doc 11 1296532 flow causes a uniform liquid film to be produced and effectively deflects the liquid stream as it is engaged with the deflector. In order to produce a gas with high kinetic energy droplets - the finely dispersed gas and the droplet jet stream 'in the flow channel having a length selected according to 4Du 〇D conditions [the liquid flow is formed, wherein (4) - Cut to the largest diameter of the ring in the exit portion of one of the flow channels. The m filaments of the flow channels are selected according to the φ condition which provides a steady flow of liquid. The length L of the flow channels greater than i 〇 d causes an increase in the loss of liquid kinetic energy due to friction between the liquid flow and the surface of the flow passage. The length L of the flow channels less than 4D may cause the liquid flow (4) to deviate from the direction of ensuring the maximum uniform spatial distribution of the liquid to be atomized. To increase the droplet velocity and the uniformity of the droplet space distribution within the atomized jet, a liquid stream is created in the flow channel that converges during the flow of the liquid. To prevent solid contaminants from obstructing the flow passage, the liquid flow through the axial passage of the sprinkler must be filtered after being supplied through the flow passages. • The liquid stream produced by atomization of the deflector plate having a flat continuous central portion is preferably confined within the geometrical boundary of the projecting portion of the cylindrical axial passage. In addition, the edge of the deflector plate can be formed into a matte shape and can be configured as a tapered surface capable of dispersing the flow of liquid during the flow of the liquid. The use of the above embodiments of the deflector plate to atomize the liquid allows the spray area to be increased with a predetermined uniformity, dispersibility and strength of a gas and droplet jet. The above technical results can also be achieved by using a sprinkler, which includes a housing of a cylindrical axial liquid supply passage, installed in the liquid supply passage of the liquid 101695.doc -12-1296532 a partition wall to divide the shaft, the flow passage channel symmetric to the -symmetric plane of the partition wall into two thermal response units; - a liquid flow deflecting plate; and including a valve and for deflecting comprising a plurality of frame arms The board is attached to the 5 Hz thermal response unit, and is used for the thermal response unit and the attachment for the deflection plate. The frame according to the present arm is positioned in the axial passage.

於其出口開口之區域内之兩個流動通道3平面中。靠近 皆可組態為-圓環段。 之母-個之橫斷面 根據伽㈣D條件選擇該等流動通道之長度以 際,其中D係一内切於流動通道之一出 ® 口斷面内之圓環之最 广實現該等既定條件可使液體以最小之動能摩擦損 失穩疋地流過流動通道。 ' 為增大液體流速度,可使流動通道在液體流動過程中會 聚液體。為提供流動通道之一會聚形狀,較佳使用一在液 體流動過程中分散液體之分隔牆。 可藉由提供一以3-25%梯度在液體流動過程中分散液體 之分隔牆達成足以滿足一最有效霧化液體流之液體流穿過 該等流動通道之最佳速度。於此情形下,皆可產生具有高 動能液滴之一精細分散之氣體及液滴喷射流。在分隔牆梯 度小於3%之情形下,於流動通道出口處注意到液體流速度 基本上未增加。在分隔牆梯度大於25%之情形下,流過流 動通道之液體流之動能損失增加。 5亥分隔牆可安裝在固定於圓柱形軸向通道中之一定心套 内。於此情形下,可達成對分割分隔牆之一精確定位以藉 101695.doc 13 1296532 此相對於該分隔牆之一對稱平面達成流動通道内液體流之 最大均勻分配。 於”亥噴灑器之一較佺實施例中,該等框架臂鄰接其附裝 點至外殼之寬度不應超過該等流動通道之出口開口附近該 为隔牆之寬度。該既定之結構實施例允許液體流之動能損 失減小至一更大程度且增大該霧化喷射流内液滴分配之均 勻性。此將導致消除改變液體流流動路線之可能性,此乃 • 因液體流繞過用於熱響應單元及用於偏轉板之附裝配件之 该等框架臂之表面。 可將一具有一等於或小於0.8D之最大孔隙直徑之過濾器 安裝在一進入流動通道之入口之噴灑器上游之圓柱形軸向 通道内。在喷灑器結構内使用該過濾器可防止流動通道受 到阻礙以藉此增強喷灑器作業之可靠性。 為增加喷灑面積,液體流偏轉板可具有一定位於該圓柱 形軸向通道之一伸出部分之幾何邊界内之扁平連續中心部 • 分。關於該喷灑器之此實施例,合意之情形係:該偏轉板 中心部分之直徑超過該軸向通道之直徑不大於兩倍。給定 該限制乃因當喷灑器在偏轉板中心部分之直徑具有明顯增 大時可能會即刻減小欲喷灑面積之中心區内之噴麗強产。 於本發明之較佳實施例中,將液體流偏轉板之邊緣製作 成多孔狀且製作成一於液體流動過程中分散液體之錐形表 面形狀。可在自約10。至約30。之範圍内選擇該錐形表面母 點與一垂直於該軸向通道之一對稱軸線平面之傾斜角。該 嘴灑器結構之實施例之既定型式會保證提高在大喷灑面積 1〇1695.d〇c -14· 1296532 上分配一精細分散之氣體及液滴喷射流之均勻性。 右傾斜角大於30。,將會導致液體流與偏轉 會導致在喑臂、两# 士 ^ 将才反I面分離且 iLl 之中心區域處之嘴灑強度較周 邊&域彡曰加。若該錐形表面之傾斜角小 流速度之轴向分量減小至一零值且導致中心區;= 度減小。 < 麗強 【實施方式】 喷灑器包括一外殼1,該外殼在其外表面上且有田 喷灑器接合至一液體分 八有—用於將 從骽刀配管線(圖中未顯示)之螺紋。 包括一其中安裝有一分隔牆3之圓柱形轴向液體 ^ 分隔牆3適合用於將舳内、g、若〇、金丨立 w通道2 〇 f+r… 軸向通道2分割成對稱於分隔腾之― =個流動通道4且被岐於位於軸向通道 之一疋心套5内。於所考慮之本發明實施例之該型式中^ 使分隔牆3以—按照自3%至25%之最佳梯 之一 Γ:梯度在流通過程中分散液體。可使由分隔 面及疋〜套5所界定之流動通道愤液體流動過程 : 體以符合分隔牆3之形狀。 ㈢h 在其出口開口區域内 匕4内兩個流動通道4之每一個 皆組態為一圓環段。^ 仏截面 圖3圖解闌釋一内切於流動通 出口部分内且具有-最大直徑D之圓環。 之一 於所考慮之本發明訾:始y , 月貫施例之該型式中,流動通道4 L係6D以符合選擇流 之長度 佩側。長度之條件: 位於進入流動通道4之 入口上游之外殼之軸向通道2 101695.doc -15- 1296532 内之過遽器6可組態為圓柱形多孔插件,其中該插件之孔徑 7之直#為〇.仍以符合根據本發明申請專利範圍選擇過滅 器孔控之-最大大小之條件:不大於〇.8〇。 一具有-閥塞且由聚合材料製作之閥門8適合用於關閉 軸向通道2之一出口開口。可蕤 一 一 ,, 9 …θ應早元(其一熱敏 組件玻璃球頭9)將_8S)定於其初始位置中。玻璃 球頭9充滿一液體,該液體具有一當周圍溫度達到一預定π 度位準時因液體膨脹而足以毀壞該玻璃球頭之體積膨脹: 數。 可藉助用於該熱響應單元及用於該偏轉板之—附裝配件 將具有玻璃球頭9之熱響應單元及液體流偏轉㈣附装至 該喷遽器之外殼卜該附裝配件包括:—用於附裝偏轉板10 且用於將玻璃球頭9保持在其初始位置内之固持架U、用於 使固持木11與外般i接合之框架臂12及用於使玻璃球頭9保 持在其初始垂直位置内夕嘴# 円之调即螺絲13。該調節螺絲13位於 固持架11之軸向開口内。 用於…應單70及用於液體流偏轉板之該附裝配件之該 等框架臂12皆佈置於軸向通道2之分隔牆3之一對稱平面内 U見圖1及3)。6亥等框架臂在其附裝至外殼^之區域内之寬 又FA不超過刀牆在流動通道4出口部分之平面内之寬度 Lpw(參見圖3 )。 液體流偏轉板Π)具有—扁平連續中心部分14。該中心部 刀14係疋位於軸向通道2之_伸出部分之幾何邊界内。於所 考慮之喷灑器實施例之—實例中,中心部分14之一直徑係 101695.doc -16- 1296532 DCP=I ·5〇(:Η,其中Dch係該喷灑器之軸向通道2之一直徑。 根據選擇IWDW最佳值之條件,直徑〜超過直徑〜 不大於兩倍。 位於軸向通道2之一伸出部分之幾何邊界外之液體流偏 轉㈣之邊緣15係製作成多孔狀且組態為—在液體流動過 程中分散液體之錐形纟面。肖錐形表面之一母點與一垂直 於該軸向通道之對稱㈣之平面之_傾斜角_〇。,亦 即’其在自約10。至約30。之最佳值〇[之範圍内(參見圖2)。 以下述方式提供該噴灌器之作業及實施一用於產生霧化 液體噴射流之方法。 該噴灑器經由-螺紋連接器連接至_分配管線(圖中未 顯示)’由此給該管線及該噴灑器之軸向通道2充滿一具有 自約0.4 MPa至約i MPa之壓力範圍之工作液體。於所;慮 之實例中,該壓力為0.6 MPa。 當周圍溫度達到一預定值(於所考慮實施例之實例中,該 預定值為68°C)時,玻璃球頭9因液體膨脹之壓力而毁壞。 -旦玻璃球頭被毀壞,具有—閥塞之_8在充滿軸向通道 2之工作液體之壓力作用了自軸向通道2之“開口上移 開。 在打開關閉喷濃器之軸向通道2之閥門後,液體流在〇6 MPa壓力下流過過濾器6’以由過遽器6捕獲妨礙嘴灑器正 常作業之固體顆粒。在軸向通道2内,液體流被分隔牆3分 割成兩個流。彳藉助定心#5達成分隔牆3於軸口二 精確定位。 内之 101695.doc -17- 1296532 、、;、後液體被送入藉由分隔牆3之侧表面及定心套5之内 表面所限界之流動通道4内。在會聚流動通道2内所產生之 兩個液體流之特徵係具有最大密度之中心區域之可用性。 2為等中心1 μ ’液體與分隔牆3之一對稱平面平行流動, 其中該平面内置放有熱響應單元附裝配件之框架臂12。因 此,在已分割之液體流流過會聚流動通道4之過程中,可產 生以預疋速度流動之定向液體流。 • 於流動通道4内所產生且對稱於分隔牆3之對稱平面流動 之液體流進-步被導向至流動通道4之出口開口且隨後導 向至軸向通道2之出口開口,藉此使所產生之液體流霧化。 液體係在由用於偏轉板1〇及用於熱響應單元之附裝配件之 4等框架臂12所限定之一空間區域内被霧化。 藉助-有料連續中心部分14之偏轉板哪化所產 之液體w之過程中’可形成_經霧化之液體流並在一徑 =轴向方向上排放。在分離此—液體流時,在偏轉板10之 _ ?緣5之夕孔部分上產生-均勻精細分散之氣體及液滴喷 射流。 j體流到達偏轉板10之中心部分14之表面以繞過用於熱 …早7C及用於偏轉板之附裝配件之框架臂^。在偏轉板 中15刀14之表面上,已在流動通道4内初步分割之液 :流經組合以形成一在徑向_軸向方向上流向偏轉板就 邊緣1 5之薄膜形式靈 ώ & 弋務化,瓜。备此一流流至偏轉板10之邊 :15之夕孔錐形表面上時,該薄膜之厚度減小且當液體自 面之邊緣滑脫並流過設置在偏轉板Η)之邊緣15上之 101695.doc -18- 1296532 凹陷(孔眼)時,該液體將被分割成細小之液滴。作為該既定 過程之一結果,產生具有一以流速之一軸向分量可用性為 特徵之徑向-轴向流動方向之霧化液體喷射流。 所實施之貫驗已顯示·應用該用於產生一霧化液體噴射 流之方法及應用該用於實施該產生一霧化液體喷射流之方 法之喷灑器能夠藉助一具有足以有效撲滅火災現場之一液 滴均勻空間分配及一液滴動能之精細分散之氣體及液滴噴 射流來增加喷灑面積。 在液體霧化過程中,水被分割成具有等於或小於14〇微米 大小之細小液滴且在一 14米2之面積上以一 〇 〇45公斤/米2 之噴灑強度及一在該面積上等於或小於2〇%之強度均方根 偏差產生一均勻氣體及液滴之喷射流。 應指出:使用歐洲專利〇7〇 1182中所闡述之一噴灑器可在 一 10米2之面積上以一 〇·05公斤/米2之喷灑強度及一在該面 積上等於或大於36%之強度均方根偏差產生具有、丨〇微米 大小之液滴及相同壓力之一液體噴射流。 使用Gnnell公司之一眾所周知之AM25_型喷灑器可在6 米2面積上以〇.075公斤/米2之噴麗強度及-在該面積上42% 之強度均方根偏差產生具有相同壓力及3 8 〇微米平均液滴 直徑之一氣體及液滴噴射流。 / 因此,與先前技術相比,實施所中請專利之方法及喷灑 器可確保在欲噴灑表面上產生具有高動能液滴及均句^門 分配液滴之-精細分散之氣體及液滴噴射流。 本發明之工業應用 101695.doc -19- J296532 根據该專上述優點, 間(且特定言之,Wp二口用於配備有貴重設備之房 車庫算戶門μ 博物館、辦公樓、倉庫、 車庫專房間)内所配置的自動滅火系統中。 ==發明之實例係較佳實例,,此並不能排 明之貫施例基於本發明之申請專利範圍可具有任何 2可能之型式,該等其它可能之型式可藉助熟悉此 術者習知之技術手段及方法來實施。 【圖式簡單說明】 可藉助實施本發明之一具體實例進一步闡述本發明,包 括根據所申請專利之-產生一霧化液體噴射流之方法運作 的一喷灑器之實施例之實例。可藉助下述附圖解釋該實施 實例: / ^ 圖1係一喷灑器於分隔牆之一對稱平面内之縱向剖視圖· 圖2係圖1所示喷灑器於一平面a-A中之縱向剖視圖· 圖3係圖1所示喷灑器於一平面B_B中之橫向剖視圖|圖中 以一放大比例顯示打開熱響應單元及閥門後之喷灑器) 【主要元件符號說明】 ° 1 外殼 2 圓柱形軸向液體供應通道 3 分隔牆 4 流動通道 5 定心套 6 過施為 7 孔徑 101695.doc -20- 1296532 8 閥門 9 玻璃球頭 10 偏轉板 11 固持架 12 框架臂 13 調節螺絲 14 扁平連續中心部分 15 邊緣In the plane of the two flow channels 3 in the region of its outlet opening. Close can be configured as a - ring segment. The mother-to-segment cross-section selects the length of the flow channels according to the gamma (four) D condition, wherein the D-system is inscribed in one of the flow channels and the ring in the section of the port is the widest to achieve the established conditions. The liquid can be steadily flowed through the flow channel with minimal kinetic energy frictional losses. To increase the flow rate of the liquid, the flow channel can be concentrated during the flow of the liquid. In order to provide a converging shape of one of the flow passages, it is preferred to use a partition wall which disperses the liquid during the flow of the liquid. The optimum velocity of the liquid stream sufficient to satisfy a most efficient atomized liquid stream through the flow channels can be achieved by providing a dividing wall that disperses the liquid during the liquid flow with a 3-25% gradient. In this case, a gas having a fine dispersion of one of the high kinetic energy droplets and a droplet discharge stream can be produced. In the case where the partition wall gradient is less than 3%, it is noted that the liquid flow velocity is not substantially increased at the outlet of the flow passage. In the case where the gradient of the partition wall is greater than 25%, the kinetic energy loss of the liquid flow flowing through the flow passage increases. The 5H partition wall can be mounted in a certain core sleeve that is fixed in the cylindrical axial passage. In this case, a precise positioning of one of the divided partition walls can be achieved to achieve a maximum uniform distribution of liquid flow in the flow passage relative to one of the planes of symmetry of the partition wall by 101695.doc 13 1296532. In one embodiment of the "Haispray", the width of the frame arms adjacent to their attachment points to the outer casing should not exceed the width of the partition opening adjacent the outlet openings of the flow channels. The established structural embodiment allows The kinetic energy loss of the liquid stream is reduced to a greater extent and the uniformity of droplet distribution within the atomized jet is increased. This will result in the elimination of the possibility of changing the flow path of the liquid stream, which is due to the bypass of the liquid stream. On the surface of the frame of the thermal response unit and the attachment for the deflection plate. A filter having a maximum pore diameter equal to or less than 0.8D can be installed upstream of the sprinkler entering the inlet of the flow channel. The cylindrical axial passage. The use of the filter within the sprinkler structure prevents the flow passage from being obstructed thereby enhancing the reliability of the sprinkler operation. To increase the spray area, the liquid flow deflector may have a certain location A flat continuous center portion within the geometrical boundary of one of the cylindrical axial passages. With respect to this embodiment of the sprinkler, it is desirable that the deflector is The diameter of the portion exceeds the diameter of the axial passage by no more than two times. This limitation is given because the sprayer may immediately reduce the area to be sprayed when the diameter of the center portion of the deflector plate is significantly increased. In the preferred embodiment of the present invention, the edge of the liquid flow deflecting plate is made porous and formed into a tapered surface shape for dispersing the liquid during the flow of the liquid. It can be from about 10 to Selecting an angle of inclination of the conical surface mother point to a plane perpendicular to the axis of symmetry of the axial channel within a range of about 30. The established version of the nozzle sprinkler embodiment will ensure an increase in the large spray area 1 〇1695.d〇c -14· 1296532 distributes the uniformity of a finely dispersed gas and droplet jet. The right tilt angle is greater than 30. This will cause the liquid flow and deflection to result in the arm, two #士^ The surface of the iL1 is separated from the peripheral area and the intensity of the nozzle is increased compared to the surrounding & the axial component of the inclined surface of the tapered surface is reduced to a zero value and the central area is caused. ;= Degree is reduced. < Li Qiang Embodiments The sprinkler includes a casing 1 having an outer surface on its outer surface and a field sprayer coupled to a liquid portion for use in a thread for a boring tool (not shown). The cylindrical axial liquid partition wall 3 in which a partition wall 3 is installed is suitable for dividing the inner channel, the g, the ruthenium, the gold iridium, the w channel 2 〇f+r... the axial channel 2 into symmetry and separation. The flow channel 4 is enclosed in a core sleeve 5 located in the axial passage. In the type of embodiment of the invention considered, the partition wall 3 is made to be the best ladder from 3% to 25%. One step: the gradient disperses the liquid during the circulation process, and the flow channel defined by the partition surface and the 疋~ sleeve 5 can be in a liquid flow process: the body conforms to the shape of the partition wall 3. (3) h in the outlet opening area 匕4 Each of the two flow channels 4 is configured as a ring segment. ^ 仏 Cross-section Figure 3 illustrates a ring that is inscribed in the flow through-port portion and has a - maximum diameter D. In the present invention, the flow channel 4 L is 6D to conform to the length of the selected stream. Condition of length: The filter 6 located in the axial passage 2 101695.doc -15-1296532 of the outer casing entering the inlet of the flow passage 4 can be configured as a cylindrical porous insert, wherein the insert has an aperture of 7 In order to meet the patent application range according to the present invention, the condition of the maximum size of the extruder is selected: not more than 〇.8〇. A valve 8 having a valve plug and made of a polymeric material is suitable for closing an outlet opening of the axial passage 2. One can be, 9 ... θ should be in the initial position (the thermal component glass ball head 9) _8S) in its initial position. The glass ball head 9 is filled with a liquid having a volume expansion which is sufficient to destroy the glass ball head due to liquid expansion when the ambient temperature reaches a predetermined π level. The thermal response unit having the glass ball head 9 and the liquid flow deflection (four) can be attached to the outer casing of the squirt by means of the attachment means for the thermal response unit and the deflector for the deflection plate. The attachment comprises: a holder U for attaching the deflection plate 10 and for holding the glass ball head 9 in its initial position, a frame arm 12 for engaging the holding wood 11 with the outer casing i, and for making the glass ball head 9 Keep it in its initial vertical position. The adjusting screw 13 is located in the axial opening of the holder 11. The frame arms 12 for the singular 70 and the attachment for the liquid flow deflection plate are all arranged in a plane of symmetry of the partition wall 3 of the axial passage 2 (see Figs. 1 and 3). The width of the frame arm of 6 hai and so on in the area to which it is attached to the outer casing ^ does not exceed the width Lpw of the knives in the plane of the outlet portion of the flow passage 4 (see Fig. 3). The liquid flow deflector plate has a flat continuous central portion 14. The central cutter 14 is located within the geometrical boundary of the extension of the axial passage 2. In the example of the sprinkler embodiment considered, one of the central portions 14 has a diameter of 101695.doc -16-1296532 DCP=I ·5〇(:Η, where Dch is the axial passage 2 of the sprinkler One of the diameters. According to the condition of selecting the optimum value of IWDW, the diameter ~ exceeds the diameter ~ not more than twice. The edge of the liquid flow deflection (4) located outside the geometrical boundary of one of the axial passages 2 is made porous and It is configured to disperse the conical surface of the liquid during the flow of the liquid. One of the mother points of the Schiffon surface is inclined to a plane perpendicular to the plane of the symmetry (4) of the axial channel, ie, The optimum value 自 [within the range of from about 10 to about 30. (see Fig. 2). The operation of the sprinkler is provided in the following manner and a method for producing an atomized liquid jet is provided. Connected via a threaded connector to the _distribution line (not shown), thereby filling the line and the axial passage 2 of the sprinkler with a working fluid having a pressure range from about 0.4 MPa to about i MPa. In the example, the pressure is 0.6 MPa. When the ambient temperature By a predetermined value (in the example of the embodiment considered, the predetermined value is 68 ° C), the glass ball head 9 is destroyed by the pressure of liquid expansion. - Once the glass ball head is destroyed, it has a valve plug. 8 The pressure of the working fluid filled in the axial passage 2 acts on the "opening" of the axial passage 2. After opening and closing the valve of the axial passage 2 of the injector, the liquid flow flows under a pressure of 〇6 MPa. The filter 6' captures the solid particles that interfere with the normal operation of the nozzle sprinkler by the filter 6. In the axial passage 2, the liquid flow is divided into two streams by the partition wall 3. The partition wall 3 is achieved by means of centering #5 Precisely positioned on the shaft port 2. The inner liquid is fed into the flow passage 4 bounded by the side surface of the partition wall 3 and the inner surface of the centering sleeve 5 in the 101695.doc -17- 1296532 , . The two liquid streams generated in the converging flow channel 2 are characterized by the availability of a central region of maximum density. 2 is an isocenter 1 μ 'liquid parallel to a plane of symmetry of the partition wall 3, wherein the plane is internally filled with heat The response unit is attached to the frame arm 12 of the accessory. During the flow of the cut liquid through the converging flow channel 4, an directional liquid flow flowing at a pre-twisting speed is generated. • The liquid flowing in the flow channel 4 and flowing symmetrically to the symmetrical plane of the partition wall 3 flows in a step-by-step manner It is guided to the outlet opening of the flow channel 4 and then to the outlet opening of the axial channel 2, whereby the resulting liquid stream is atomized. The liquid system is used for the deflection plate 1 and for the thermal response unit The space region defined by the frame arm 12 of the assembly 4 is atomized. By means of the deflecting plate of the continuous central portion 14 of the material, the liquid liquid can be formed in the process of forming the liquid Discharge in a diameter = axial direction. When this liquid flow is separated, a uniformly finely dispersed gas and a droplet jet are generated on the portion of the edge of the deflecting plate 10 at the edge of the edge 5. The body flow reaches the surface of the central portion 14 of the deflector 10 to bypass the frame arm for the heat 7C and the attachment for the deflector. On the surface of the 15 knives 14 in the deflector plate, the liquid which has been initially divided in the flow channel 4: flows through a combination to form a film form in the radial_axial direction flowing toward the deflector plate at the edge 15 &弋 化, melon. When the flow is first to the edge of the deflector 10: on the tapered surface of the eleventh hole, the thickness of the film is reduced and when the liquid slips off the edge of the face and flows over the edge 15 provided on the deflector plate) 101695.doc -18- 1296532 When the hole (hole), the liquid will be divided into small droplets. As a result of one of the established processes, an atomized liquid jet having a radial-axial flow direction characterized by the availability of one of the axial components is produced. The practice has been shown to apply the method for producing an atomized liquid jet and to apply the sprayer for carrying out the method for producing an atomized liquid jet capable of effectively extinguishing a fire scene One of the droplets is evenly spatially distributed and a finely dispersed gas and droplet jet of droplet kinetic energy is added to increase the spray area. In the liquid atomization process, the water is divided into fine droplets having a size of 14 μm or less and a spray intensity of 45 kg/m 2 on an area of 14 m 2 and one on the area. A root mean square deviation equal to or less than 2% produces a jet of uniform gas and droplets. It should be noted that one of the sprayers described in European Patent No. 7 to 1182 can have a spray intensity of one 〇·05 kg/m 2 on an area of 10 m 2 and a ratio equal to or greater than 36% on the area. The intensity root mean square deviation produces a liquid jet having one droplet of 丨〇 micron size and one of the same pressure. Using the well-known AM25_sprinkler from Gnnell, the same pressure can be produced on a 6 m2 area with a spray intensity of 075.075 kg/m2 and a root mean square deviation of 42% of the area. And a gas and droplet jet of one of the average droplet diameters of 3 8 μm. / Therefore, compared to the prior art, the method and sprinkler of the patent application are implemented to ensure that finely dispersed gases and droplets are produced on the surface to be sprayed with high kinetic energy droplets and uniform droplets. Jet stream. Industrial application 101695.doc -19- J296532 of the present invention According to the above-mentioned advantages, and in particular, Wp two ports are used for housing garages equipped with valuable equipment, museums, office buildings, warehouses, garages The room is equipped with an automatic fire extinguishing system. == Instances of the Invention are preferred examples, and the examples of the invention that are not exemplified may have any two possible types based on the invention, and such other possible types may be obtained by means of techniques known to those skilled in the art. And methods to implement. BRIEF DESCRIPTION OF THE DRAWINGS The invention may be further illustrated by the practice of one embodiment of the invention, including an example of an embodiment of a sprayer that operates in accordance with the method of the invention for producing an atomized liquid jet. The embodiment can be explained by means of the following figures: / ^ Figure 1 is a longitudinal cross-sectional view of a sprinkler in a plane of symmetry of the dividing wall. Figure 2 is a longitudinal sectional view of the sprinkler of Figure 1 in a plane aA Figure 3 is a transverse cross-sectional view of the sprinkler shown in Figure 1 in a plane B_B | in the figure shows the sprinkler after opening the thermal response unit and the valve in an enlarged scale. [Key symbol description] ° 1 Housing 2 Cylindrical Axial liquid supply channel 3 partition wall 4 flow channel 5 centering sleeve 6 over-applied 7 aperture 101695.doc -20- 1296532 8 valve 9 glass ball head 10 deflection plate 11 holder 12 frame arm 13 adjustment screw 14 flat continuous Center section 15 edge

101695.doc •21101695.doc •21

Claims (1)

1296532 十、申請專利範圍: 1 · 一種用於產生一霧化液體噴射流之方法,其包括:當該 周圍溫度達到一預定溫度且一喷灑器之一熱響應單元打 開時’在壓力下將一液體供應至該喷灑器之一軸向通道 (2)中;藉助安裝在該喷灑器之該軸向通道2内之一分隔牆 3將一液體流分割成兩個流;在該流動通道4内形成多個 液體流,該等流相對於該分隔牆之一對稱平面對稱地 流動’且藉由接合一藉助用於該偏轉板(1〇)且用於該熱響 應單元之一附裝配件固定在該喷灑器之一外殼(1)上之該 偏轉板(10)來霧化該等所產生之液體流,該附裝配件包括 多個框架臂(12),該方法之特徵在於:液體流係形成於該 等流動通道(4)内以繞過用於該偏轉板(1〇)且用於該熱響 應單兀之該附裝配件之該等框架臂(12)流動,其中該等框 木筹(12)係定位於該軸向通道(2)之該分隔牆(3)之一對稱 平面内。 2·如睛求項丄之方法,其特徵在於··該等液體流係形成於該 :流動通道⑷中,其中在靠近其出口開口之區域内該等 流動通道之每一個之橫截面係組態為一圓環段。 3· ^月求項i之方法,其特徵在於:該等液體流係形成於該 等二動通道(4)内’其中其之長度以根據4D^贈之條 件選擇,其中D係一内切入該等流動通道(4)之-出口部分 内之一圓環之最大直徑。 4. 如味求項1之方法,其特微在 行倣在於·邊等液體流係形成於在 以液歧之流動過程中會聚之該等流動通道(4)内。 101695.doc 1296532 月长項1之方法’其特徵在於·在該液體之流動過程中 會聚之該等流動通道(4)内提供該噴灑器之該軸向通道 (2)内該液體流之該分割。 6·如請求項1之方法,其特徵在於:在將該液體供入該等流 動通道(4)中之前,流過該喷灑器之該軸向通道(2)之該液 體流經過濾。 月求項1之方法,其特徵在於:藉助具有一扁平連續中 心部分(14)之該偏轉板(10)霧化該等所產生之液體流,、該 扁平連續中心部分(14)係定位於該圓柱形軸向通道(2)之 伸出部分之一幾何邊界内。 8.如了求項1之方法,其特徵在於:藉助該偏轉板⑽霧化 該等所產生之液體流,該偏轉板⑽之伸出該圓柱形轴向 =成θ’::出部,之一幾何邊界外之該等邊緣〇5)係 "成夕孔狀且組態為在該液體之流動過程中會聚之一 錐形表面。 9. =噴灑:’其包括:一具有一圓柱形軸向液體供應通 二:外殼(1),其中安裝—分隔牆⑺以相對於該分隔牆 、雨)之-對稱平面將該軸向通道⑺分割成兩個對稱流動 板( ’、有㈤門(8)之熱響應單元;—液體流偏轉 :1)及:用於附裝該熱響應單元及該偏轉板⑽且包 於臂(12)之附裝配件,該喷灑器之特徵在於:用 等框二且用於該偏轉板⑽之該附裝配件之該 == 於該轴向通道⑺之該分隔牆⑺之- 對稱千面内’其中在靠 闹口之4 (he域内該兩個 101695.doc 1296532 流動通道⑷之每-個之一橫截面係組態為一圓環段。 10.如凊求項9之喷灑器’其特徵在於:該等流動通道⑷之長 度L係根據4DK! 0D之條件選擇,其中d係一内切入又 流動通道⑷之-出口部分内之一圓環之最大直徑。 η.如請求項9之喷麗器’其特徵在於:該等流動通道⑷係製 作成在該液體之流動過程中會聚。 12. 如請求項9之㈣器,其特徵在於··該分隔牆(3)係製作成 • 在錢體之流動過程中幻·25%之梯度分散。 13. 如請求項9之噴麗器’其特徵在於:該分隔牆⑺係安裝在 固定於該圓柱形軸向通道(2)中之一定心套⑺内。 14. 如請求項9之喷灑器’其特徵在於:該等框架臂⑽在Α 附裝至該外殼⑴之區域内之寬度不超過該分隔牆⑺在 靠近該等流動通道之該等出口開口之該區域内之寬度。 •如請求項9之噴麗器,其特徵在於:將一過遽器⑷定位於 進入該等流動通道⑷之該人σ上游之該圓柱形轴向通道 _ m胃具有最大直徑等於或小於g.8d之孔徑 ⑺。 1 士月长員9之噴灑器,其特徵在於··該液體流偏轉板⑽ 具有-定位於該圓柱形軸向通道⑺之—伸出部分之該幾 何邊界内之扁平連續中心部分⑽,其中該偏轉板⑽之 該中心部分U4)之直徑超過該軸向通道(2)之直徑不大於 兩倍。 .如請求項9之喷灌器,其特徵在於:位於該圓柱形袖向通 道⑺之-伸出部分之該幾何邊界外之該液體流偏轉板 101695.doc 1296532 (10)之邊緣(15)皆製作成多孔狀且組態為在該液體之冷 動過程中分散之-錐形表面,其中該錐形表面母點鱼: 直於该軸向通道之—對稱軸線之—平面一 約10。至約30。之範圍内。 、斜角介於自1296532 X. Patent Application Range: 1 . A method for generating an atomized liquid jet comprising: when the ambient temperature reaches a predetermined temperature and a thermal response unit of a sprinkler is opened, 'under pressure a liquid is supplied to one of the axial passages (2) of the sprinkler; a liquid flow is divided into two streams by a partition wall 3 installed in the axial passage 2 of the sprinkler; Forming a plurality of liquid streams in the channel 4, the streams flowing symmetrically with respect to a plane of symmetry of the partition wall' and by means of a joint for the deflector plate (1〇) and for one of the thermal response units The deflection plate (10) is attached to the outer casing (1) of the sprinkler to atomize the liquid flow generated by the assembly, the attachment assembly comprising a plurality of frame arms (12), the method features Wherein a liquid flow system is formed in the flow channels (4) to bypass the flow of the frame arms (12) for the deflection plate (1〇) for the attachment of the thermal response unit, Where the frame wood (12) is positioned in the axial channel (2) One of the partition walls (3) in the plane of symmetry. 2. A method according to the present invention, characterized in that the liquid flow system is formed in the flow channel (4), wherein each of the flow channels is in a region close to the outlet opening thereof. The state is a ring segment. The method of claim i is characterized in that: the liquid flow system is formed in the two moving channels (4), wherein the length thereof is selected according to the condition of the 4D^, wherein the D system is internally cut into The maximum diameter of one of the annular passages in the outlet portion of the flow passages (4). 4. The method of claim 1, wherein the liquid flow system is formed such that the liquid flow is formed in the flow channels (4) that are concentrated during the flow of the liquid. 101695.doc 1296532 The method of monthly term 1 is characterized in that the liquid flow in the axial passage (2) of the sprinkler is provided in the flow channels (4) which are concentrated during the flow of the liquid segmentation. 6. The method of claim 1, characterized in that the liquid flowing through the axial passage (2) of the sprinkler flows through the filter before the liquid is supplied into the flow channels (4). The method of claim 1, characterized in that the liquid flow generated by atomizing the deflector (10) having a flat continuous central portion (14) is positioned in the flat continuous central portion (14) Within one of the geometric boundaries of the projecting portion of the cylindrical axial passage (2). 8. The method of claim 1, wherein the liquid flow generated by the atomization is atomized by the deflector plate (10), and the deflection plate (10) protrudes from the cylindrical axis = θ':: The edges 之一5) outside one of the geometric boundaries are formed into a hole and configured to converge a tapered surface during the flow of the liquid. 9. = Spraying: 'It consists of: having a cylindrical axial liquid supply 2: the outer casing (1), wherein the installation-partition wall (7) is in a symmetrical plane relative to the partition wall, rain) (7) divided into two symmetrical flow plates (', a thermal response unit with (5) door (8); - liquid flow deflection: 1) and: for attaching the thermal response unit and the deflection plate (10) and enclosing the arm (12) Attached to the accessory, the sprinkler is characterized in that the frame 2 is used for the attachment of the deflector (10) == the partition (7) of the axial passage (7) - symmetrical Inside one of the four sections of the intersection of the two 101695.doc 1296532 flow channels (4) in the he is configured as a ring segment. 10. The sprinkler of claim 9 'It is characterized in that the length L of the flow channels (4) is selected according to the condition of 4DK! 0D, wherein d is the maximum diameter of one of the rings in the outlet portion of the flow channel (4). The squirting device of '9' is characterized in that the flow channels (4) are made to converge during the flow of the liquid. 2. The apparatus of claim 4, characterized in that the partition wall (3) is made into a gradient of 25% in the flow of the money body. 13. The spray device of claim 9 'It is characterized in that the partition wall (7) is mounted in a certain core sleeve (7) fixed in the cylindrical axial passage (2). 14. The sprayer of claim 9 is characterized in that: the frame arms (10) The width in the region to which the casing (1) is attached does not exceed the width of the partition wall (7) in the region of the outlet openings adjacent to the flow passages. The positioning of a filter (4) upstream of the person σ entering the flow channel (4) of the cylindrical axial channel _ m stomach has a maximum diameter equal to or less than g. 8d aperture (7). 1 士月长员9 a sprinkler, characterized in that the liquid flow deflecting plate (10) has a flat continuous central portion (10) positioned within the geometrical boundary of the cylindrical axial passage (7), wherein the deflecting plate (10) The diameter of the central portion U4) exceeds the diameter of the axial passage (2) is not greater than Twice. A sprinkler according to claim 9, characterized in that the edge (15) of the liquid flow deflecting plate 101695.doc 1296532 (10) is located outside the geometric boundary of the cylindrical sleeve-way passage (7). A conical surface that is made porous and configured to disperse during the cold motion of the liquid, wherein the conical surface is a fish that is straight to the plane of the axis of symmetry - about 10 . Up to about 30. Within the scope. , the bevel is between 101695.doc -4-101695.doc -4-
TW94115267A 2005-05-11 2005-05-11 A method for generation of an atomized liquid and a sprinkler TWI296532B (en)

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