TW457123B - Arrangement for combining dissimilar streams - Google Patents
Arrangement for combining dissimilar streams Download PDFInfo
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- TW457123B TW457123B TW088114685A TW88114685A TW457123B TW 457123 B TW457123 B TW 457123B TW 088114685 A TW088114685 A TW 088114685A TW 88114685 A TW88114685 A TW 88114685A TW 457123 B TW457123 B TW 457123B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/10—Mixing gases with gases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/311—Injector mixers in conduits or tubes through which the main component flows for mixing more than two components; Devices specially adapted for generating foam
- B01F25/3111—Devices specially adapted for generating foam, e.g. air foam
- B01F25/31112—Devices specially adapted for generating foam, e.g. air foam with additional mixing means other than injector mixers, e.g. screen or baffles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
- B01F25/3141—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit with additional mixing means other than injector mixers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
- B01F25/4315—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being deformed flat pieces of material
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
- Treatment Of Fiber Materials (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Toys (AREA)
Abstract
Description
457123 經濟部智慧財產局員工消費合作社印製 A7 IS/ 五、發明說明() 發朗领械. 本發明爲關於結合不同;·云知Μ Μ 4丨]邮動的裝配與方法,尤並爲關 於利用輸送管或類似物件之Ψ 0 0 八 Η卞疋肀的檔板形狀,以增加二個(或更 多)不同材料流動(舉例來銳,Α Τ + 平』,在不同溫度下的二個氣流)結合 形成同類型流動。 先前技術枝沐 在許多工業裝置中’常常需要結合許多不同氣體(或液 體)材料。舉例來説,其需自具較低溫度作用空氣(如與空氣 乾燥器接觸時)的傳統燃燒裝置(以氣體或油爲燃料)混合燃 燒及高溫氣體。或者舉例來説’其可需以空氣乾燥器之作用 空氣而混合來自氣體過輪機出口的排出氣體。這些裝配結構 一般包括移經輸送管(或類似箱内)的第一氣流⑺rst stream) ’與藉輸入口而將第二流動(second stream)引進輸送 管。 爲了達到結合不同泥動’先前技術裝配一般憑靠《擾 拌動作”(stirring motion)及第二氣流注射點的下游亂流。一 般而言’此一裝配需要相當能量(因此降低結合流動的流 速),也需較長距離以瑕後結合二個流動,並產生同種特性的 流動。在另一先前技術裝配中,偏轉器風向計插入注入喷射 口,以導致計數管流動於輸送管。 因此,對改善裝配而言仍需先前技術,以促進不同流 動的結合’其中此裝配爲能量敫率與利用附加輸送管的最小 長度。 發明概冰 4 本紙張疋度適用中國國家標準(CNS>A4規格(210 X 297公釐) .- — — —ml! I -----^----.. I (請先閱讀背面之注意事項再填寫本頁) A7 B7 457123 五、發明說明(2 ) 由本發明所保留先前技術的需要爲關於結合不同流動 勺裝配1及方'法’尤其爲關於利用輸送管或類似箱内之中的檔 板形狀’以增加二個(或更多)不同材料流動(舉例來説,在不 同/m度下的一氣流)效率結合形成同種流動。 在發明較佳實施例中,斜形檔板乃配置於第二氣流之 輸入源的輸送管上游’第二氣流與移經輸送管的第一氣流結 口。輸送官包含形成輸送管底部及頂部的平行與間隔分離内 壁。第一泥動輸入口插入經過輸送管底部,1檔板爲斜形, 使待樓板較寬邵分較接近輸入口,當它接近輸送管頂部時, 乃狹f地越過輸送管寬度。第一氣流(例如低溫)形金輸送 管,且第二氣流(例如高溫)藉輸入口引進。第一流動流動經 過樓板’沿較接近輸入口之隔版面產生低壓區域。由輸入口 引進第二流動’然後由本發明檔板形狀產生自然地流入低壓 區域,結果有效的與第一流動混合。457123 Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs A7 IS / 5. Description of the invention () Falang collar. The present invention is about different combinations; · Yunzhi M Μ 4 丨] postal assembly and method, especially for Regarding the use of ducts or similar objects, the shape of the baffle is 0 to 8 to increase the flow of two (or more) different materials (for example, Lai Rui, A T + Ping), two at different temperatures. Air flows) combine to form the same type of flow. Prior art techniques In many industrial installations, it is often necessary to combine many different gas (or liquid) materials. For example, it requires its own traditional combustion device (using gas or oil as fuel) with low temperature acting air (such as when in contact with an air dryer) to mix combustion and high temperature gas. Or, for example, it may require the air from the air dryer to mix the exhaust gas from the outlet of the turbine. These assembly structures generally include a first stream ⑺rst stream 'which is moved through a transfer pipe (or a similar box) and a second stream is introduced into the transfer pipe through an input port. In order to achieve a combination of different mud movements, the prior art assembly generally relied on the "stirring motion" and the downstream turbulent flow of the second gas injection point. Generally, this assembly requires considerable energy (thus reducing the combined flow velocity ), It also takes a long distance to combine the two flows after the flaw and produce a flow of the same characteristics. In another prior art assembly, the deflector wind gauge is inserted into the injection nozzle to cause the counting tube to flow in the delivery tube. Therefore, For the improvement of assembly, the previous technology is still needed to promote the combination of different flows. Among them, the assembly is the energy efficiency and the minimum length of the additional conveying pipe. 发明 约 冰 4 This paper is compatible with Chinese national standards (CNS > A4 specifications) (210 X 297 mm) .- — — —ml! I ----- ^ ---- .. I (Please read the notes on the back before filling this page) A7 B7 457123 V. Description of the invention (2 ) The need of the prior art retained by the present invention is to add two (or more) with regard to the assembly of different flow scoops and methods 'especially with the use of baffle shapes in ducts or similar boxes'. The efficiency of different material flows (for example, an air flow at different degrees / m) is combined to form the same flow. In a preferred embodiment of the invention, the inclined baffle plate is disposed upstream of the conveying pipe of the input source of the second air flow ' The second air flow and the first air flow port moving through the conveying pipe. The conveying officer includes a parallel and spaced inner wall forming the bottom and top of the conveying pipe. The first mud moving input port is inserted through the bottom of the conveying pipe, and the first baffle is inclined. Make the floor slab wider and closer to the input port, and when it approaches the top of the duct, it narrows across the width of the duct. The first air stream (such as low temperature) forms a gold duct, and the second air stream (such as high temperature) borrows The input port is introduced. The first flow flows through the floor slab to generate a low-pressure region along the partition plate closer to the input port. The second flow is introduced from the input port and then naturally flows into the low-pressure region from the shape of the baffle of the present invention. Flow mixing.
在本發明的另一實施例中,可構成檔板,其關於包括 越過揪進輸送管頂部之檔板底端的間隔區域》此實施例尤其 極適合理想結合低溫氣流與高溫氣流的裝配。尤其此間隔允 許低溫氣流通過檔板之下,並拉入檔板前面的低壓區,以便 提供檔板結構的附加冷卻D 本發明的裝配及方法可使用於結合任何二個不同材 料’舉例來説,有流動與空氣、低濕度空氣與高溼度空氣、 氮氣與氧氣或甚至二液體(比如澄清液體與乳狀液或懸浮 液)。尤其結合二個不同材料流動(比如低溫空氣與高溫空氣) 的技巧極有用於紙類與紡織工業。舉例來説,在織造或編織 本紙張尺度適用中國國家標準<CNS)A4規格(210x297公釐) n B— VI ^1 ^1 ^1 ϋ I I I n I a i (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 A7 457123 五、發明說明( 織品的製品以及某-非織造材料中,需要以同類氣流(常稱此 技術爲“經過空氣乾澡”)來“空氣乾燥”此材料。依照本發 明的指示’同類氣流乃由利用插入氣流之間低的檔板之低溫 空氣與高溫空氣的結合而形成。 在本發明的另外其他實施例中,可利用非斜形標板來 提供二個或更多村料流動的結合。尤其非斜形檔板可使用於 第一高速流動與第二低速流動結合狀態。在先前技術中,假 使低速流動注入高速流動路徑,低速流動的輸入口可變得緊 繃,因此指錯低速材料橫跨輸送管頂部的流動方向,結果低 效率混合。依照本發明指示,作爲無斜形板作用的檔板以保 護輸入口免受高速流動的路徑。因此,低速材料能夠延伸越 過輸送管的寬度,結果更有效率混合於下游。 在本發明的更進一步實施例中’可結合大多數不同流 動以利用大多數分離檔板形成一同類流動,每個檔板配置於 大多數樹入口的其中一上游。大多數輸入口可配置於關於箱 内之任何理想位置。舉例來説,這些口可沿箱内長度配置, 或者可沿箱内寬度配置。此外,此檔板可包含一片固體材料, 或者可包括一或更多齒孔。 本發明的迻些及其他實施例在以下討論過程及參考附 圖期間將變得明顯。 圖式简要說朗 引用目前圖示,此處相同數字表示在數個圖中的相同 部分: 圖1爲説明本發明混合装配之示範實施例的立體圖; 本紙張尺度適用中國國家標準(CNS)A4規格(210x 297公釐) <請先閱讀背面之注意事項再填寫本頁) I > n 1_1 I n I f 經濟部智慧財產局員工消費合作社印製 457123 A7 ~---B7___ 五、發明說明(呼) ' 圖2爲包含圖1中沿線2-2的裝配圖示; 圖3爲包含圖!中沿線3 3的另一裝配圖示, 圖4爲祝明本發明中包括間隔權板的另一實施例; 圖5爲圖4中沿線5-5的裝配圖示; 圖6爲圖4中 >'凡竣 Τ σ,,果6-6的另一裝配圖示; 圖7爲圖5中沿線7_7的另一裝配圖示,此尤其説明包 括於示範檔板結構之中的間隔區域; 圖8爲説明本發明利用大多數樓板及結合輸入口之另 一裝配的立體圖; 圖9爲包含圖8中沿線9-9的裝配側面圖; 圖丨0爲利用本發明與先前技術装配比較之裝配達成結 果的曲線圖’尤其當低溫空氣與高溫空氣結合時達到溫度 “混合”(mixing)的改善。 實施例詳 圖1爲説明本發明的示範混合裝配(10)。如圖所示,此 裝配包含配置於輸送管(14)的斜形檔板(12),使得檔板(12) 的較寬邊緣(16)接近輸送管(14)之底部内壁(18)。然後檔板 (1 2)逐漸變細進入在輸送管(14)頂部内壁(22)附近中的一點 (2〇)。當説明包含長方形·橫截面之實施例的輸送管時,乃了 解可利用任何估計幾何形狀之任何適當箱内。此外’檔板(丨2) 的幾何形狀在特别情況不同。對圖丨的裝配而言,檔板(1 2) 爲説明作爲包含一圓錐曲線。可利用其他斜形或非斜形形 狀’並劃入本發明的精神與範圍之中。 輸入口(24)伸出經過檔板(14)的底部内壁,並位於檔板 {請先閲讀背面之注意事項再填寫本頁) -I -裝 -----訂--------- 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) Waws-imi/enAp應〇㈣ 5 删K-OOmsw.Doc ~ 3 & 湖 457123 A7 B7 五、發明說明(5 ) (12)下游(關於流經檔板(12)之輸送管(14)的流動方向)。介於 輸入口(24)中央與檔板(12)之間的距離4(圖2所示)爲一設計 問題,不是在區域之間提供較大空氣壓力就是提供較小空氣 壓力,如間隔4_的作用。 如説明的實施例中,第一氣流G |沿輸送管(1 4)的長度 移動。第一氣流G〗可包含氧氣、氮氣、流勤、空氣或任何其 他氣流。第二氣流〇2移經管道(26),並藉輸入口(24)引進輸 送管(14)。依照本發明的指示,第一氣流G〗的流動經過斜形 檔板(12),其在檔板(12)之下游侧(28)上產生一低壓洞。如圖 1所示,第二氣流G2的路徑因此進入低壓區域。以增加注入 點的距離,則注入氣體的喷射口有變寬的天然趨勢,因此引 起增加第二氣流G2至低壓洞外側的流動量,並橫掃第一氣流 Gi的流動,藉以平等分布橫跨第一氣流Gl面(寬度)。此亂流 乃由斜形檔板結構產生,因此促成橫跨第一氣流G|之正面流 動的擴大混合行動。 經濟部智慧財產局員工消費合作社印製 (請先閱讀背面之注寺華項再填寫本頁) 了解本發明乃利用斜形檔板達到混合,其可藉以下任 特性而k尚:(1)調整輸送官(12)的橫截面區域,以便控制 器流G!(例如減少在檔板(1 2)區域中的輸送管之橫截面,且輸 入口(24)將増加氣流G】速度)的速度;(2)調整輸送管(14)方 向(因此控制氣流G!正面流動的寬度與橫寬);或者(3)調整第 一氣流G2離開輸入口(24)的速度。 圖2説明描述於上面圖1中裝配的侧面圖。如此圖所 不,輸入口(24)仲出一預定高度經過輸送管(14)的底部表面 (18^此圖解輸入口(24)的中央爲配置於估計自檔板(12)背In another embodiment of the present invention, a baffle plate may be formed, which is related to the interval area including the bottom end of the baffle plate that passes over the top of the conveying pipe. This embodiment is particularly suitable for the assembly that ideally combines low temperature airflow and high temperature airflow. In particular, this interval allows low-temperature airflow to pass under the baffle and into the low-pressure area in front of the baffle to provide additional cooling of the baffle structure. The assembly and method of the present invention can be used to combine any two different materials. There are flows with air, low humidity air and high humidity air, nitrogen and oxygen or even two liquids (such as clear liquids and emulsions or suspensions). In particular, the technique of combining two different material flows, such as low temperature air and high temperature air, is extremely useful in the paper and textile industries. For example, when weaving or weaving this paper, the Chinese national standard < CNS) A4 specification (210x297 mm) is applicable. N B— VI ^ 1 ^ 1 ^ 1 ϋ III n I ai (Please read the precautions on the back before (Fill in this page) Printed by A7 457123, Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. 5. Description of the Invention This material is "air-dried." According to the instructions of the present invention, 'the same type of airflow is formed by the combination of low-temperature air and high-temperature air that is inserted between the baffles that are low between the airflows. In still other embodiments of the present invention, non- An oblique target plate provides a combination of two or more material flows. In particular, a non-inclined baffle can be used in a combination of the first high-speed flow and the second low-speed flow. In the prior art, if a low-speed flow is injected into a high-speed flow path , The low-speed flow input port can become tight, so pointing at the flow direction of the low-speed material across the top of the conveying tube, resulting in inefficient mixing. According to the instructions of the present invention, as The baffle plate is used to protect the input port from the high-speed flow path. Therefore, the low-speed material can extend across the width of the conveying pipe, resulting in more efficient mixing downstream. In a further embodiment of the present invention, 'combinable large Many different flows to form a homogeneous flow with most separate baffles, each baffle being configured upstream of one of the most tree inlets. Most input ports can be configured at any desired location within the box. For example, these The mouth may be configured along the length of the box, or may be configured along the width of the box. In addition, the baffle may include a piece of solid material or may include one or more perforations. The process of these and other embodiments of the present invention is discussed below. It will become apparent during reference to the drawings. The drawing briefly describes the current drawing, where the same numbers represent the same parts in several figures: Figure 1 is a perspective view illustrating an exemplary embodiment of a hybrid assembly of the present invention; Paper size applies Chinese National Standard (CNS) A4 (210x 297 mm) < Please read the notes on the back before filling this page) I > n 1_ 1 I n I f Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 457123 A7 ~ --- B7___ V. Description of the invention (calling) '' Figure 2 contains the assembly diagram along line 2-2 in Figure 1; Figure 3 contains the Figure! Another assembly diagram along the middle line 33, FIG. 4 is another embodiment of the present invention including a spacer weight plate; FIG. 5 is an assembly diagram along the line 5-5 in FIG. 4; FIG. 6 is the diagram in FIG. 4 > 'Fan Jun T σ, another assembly diagram of Guo 6-6; Figure 7 is another assembly diagram along line 7_7 in Figure 5, this particularly illustrates the spacing area included in the exemplary baffle structure; Fig. 8 is a perspective view illustrating another assembly of the present invention using most floor plates and joint input ports; Fig. 9 is a side view of the assembly including lines 9-9 in Fig. 8; The graph of the results of the assembly 'especially when the low temperature air is combined with the high temperature air, an improvement in the temperature "mixing" is achieved. DETAILED DESCRIPTION OF THE EMBODIMENTS Figure 1 is an exemplary hybrid assembly (10) illustrating the present invention. As shown in the figure, this assembly includes an inclined baffle plate (12) arranged on the delivery pipe (14) so that the wider edge (16) of the baffle plate (12) is close to the bottom inner wall (18) of the delivery pipe (14). The baffle (1 2) then tapers into a point (20) near the top inner wall (22) of the delivery tube (14). When describing a duct containing an embodiment of a rectangular cross-section, it is understood that any suitable box can be used with any estimated geometry. In addition, the geometry of the 'baffle plate (丨 2) is different in special cases. For the assembly of Figure 丨, the baffle plate (12) is illustrated as including a conical curve. Other oblique or non-oblique shapes may be utilized and are within the spirit and scope of the invention. The input port (24) protrudes past the inner wall of the bottom of the baffle plate (14) and is located on the baffle plate (Please read the precautions on the back before filling this page) -I-装 ----- Order ------ --- Printed by the Employees' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. The paper size is applicable to Chinese National Standard (CNS) A4 (210 X 297 mm) Waws-imi / enAp Ying 0㈣ 5 Delete K-OOmsw.Doc ~ 3 & amp Lake 457123 A7 B7 5. Description of the invention (5) (12) downstream (about the flow direction of the conveying pipe (14) passing through the baffle plate (12)). The distance 4 (shown in Fig. 2) between the center of the input port (24) and the baffle plate (12) is a design issue. Either provide a larger air pressure between the areas or provide a smaller air pressure, such as the interval 4 The role of _. As in the illustrated embodiment, the first air flow G | moves along the length of the conveying pipe (1 4). The first gas flow G may include oxygen, nitrogen, flow, air, or any other gas flow. The second air current 02 moves through the pipe (26) and is introduced into the transmission pipe (14) through the input port (24). According to the instructions of the present invention, the flow of the first air flow G1 passes through the inclined baffle plate (12), which creates a low-pressure hole on the downstream side (28) of the baffle plate (12). As shown in Figure 1, the path of the second airflow G2 therefore enters the low-pressure region. In order to increase the distance of the injection point, the injection port of the injected gas has a natural tendency to widen. Therefore, the flow of the second air flow G2 to the outside of the low-pressure hole is increased, and the flow of the first air flow Gi is swept across, so as to distribute across the An air flow Gl surface (width). This turbulent flow is generated by the oblique baffle structure, thus facilitating an enlarged mixing action across the frontal flow of the first air flow G |. Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs (please read the Note Temple Huaxiang on the back before filling out this page). Understand that the invention uses a slanted baffle to achieve mixing, which can be used by any of the following characteristics: (1) Adjust the cross-sectional area of the transport officer (12) so that the controller flows G! (For example, reduce the cross-section of the duct in the area of the baffle plate (12), and the input port (24) will increase the air flow G] speed) Speed; (2) adjust the direction of the conveying pipe (14) (thus controlling the width and width of the front air flow G!); Or (3) adjust the speed at which the first air flow G2 leaves the input port (24). FIG. 2 illustrates a side view of the assembly described in FIG. 1 above. As shown in this figure, the input port (24) passes through a predetermined height through the bottom surface of the conveying pipe (14). The center of the graphical input port (24) is located on the back of the estimated baffle plate (12).
457123 A7 B7 五、發明說明( 6 經濟部智慧財產局員工消費合作社印製 (30)下游距離尘處。可控制高度匕與距離立,以便提供二流動 更有效率的混合,其中這些限定要素將爲各種不同狀態函數 與二流動(例如溫度、組成物、溼度、流速等等)結合。如清 楚地如圖中所示,檔板(12)的尺寸使得頂點(2〇)無法進入與輸 送管(14)之頂部表面(22)接觸。氣流Gl環繞檔板(12)流動, 因此產生低壓洞區域(32)。當氣流g2離開輸入口(24)時,因 此自然地往洞(32)進入,結果增加氣流Gi及G2的混合效率。 如上所述,影響本發明裝配效率的其他因素爲檔板的 幾何形狀。圖3説明圖1中混合裝配的上端立體圖。如圖所 示’所形成的權板(12)侧壁(34)包含一半徑[的弧形,已發現 此處角位移不但可控制所有低壓洞(32),也可控制洞區域之 中的實際壓力。 如上所述,對本發明方法利用而言的特殊環境爲“完 全空氣”乾燥作用與織造及非織造織品的製造結合,此處長 需結合低溫及咼溫氣流。圖4説明本發明極適合此一環境的 特殊貫施例。此環境爲適合處理輕量柔軟紙製品,此製品包 括這些小於5 g/m及大於200 g/m2的基重。尤其混合裝配(5〇) 包含配置於一導管(54)(或類似箱内)的檔板(52),此處檔板 (52)位於上游(關於流動經過導管(54)的方向)自輸入口(56)的 一預定距離圖5中的圖解)。如圖所示,低溫空氣Al〇w的 第一泥動沿導管(54)長度移動,並碰到檔板(52),以便在檔板 (52)之内側部分產生一低壓洞(56)。高溫空氣Ahigh的第二流 動移動經過管道(58),並藉輸入口(56)進入導管對本發 明的此特殊低溫/向溫實施例而言,檔板(52)包括以預定間隔 ^--- 本紙張尺度適用中國國豕標準(CNS)A4規格(210 X 297公H ) Μά^-ΟΛΡβί^ηΆΡί(001·05~\ΰ56^ΡΚ·Οΰ1,0565-2.〇{χ May 20C, ί請先閲讀背面之注意事項再填寫本頁) -裝457123 A7 B7 V. Description of the invention (6 Printed (30) downstream from the dust by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. The height and distance can be controlled in order to provide a more efficient mixing of the two flows. Combined with two flows (such as temperature, composition, humidity, flow rate, etc.) for various different state functions. As clearly shown in the figure, the size of the baffle plate (12) prevents the vertex (20) from entering and conveying the tube The top surface (22) of (14) is in contact. The air flow G1 flows around the baffle plate (12), thereby creating a low-pressure hole area (32). When the air flow g2 leaves the input port (24), it naturally enters the hole (32). As a result, the mixing efficiency of the airflow Gi and G2 is increased. As mentioned above, the other factor affecting the assembly efficiency of the present invention is the geometry of the baffle plate. Figure 3 illustrates the upper perspective view of the hybrid assembly in Figure 1. As shown in the figure The side wall (34) of the weight plate (12) contains an arc with a radius [, it has been found that the angular displacement here can control not only all low-pressure holes (32), but also the actual pressure in the hole area. invention The special environment in which the method is used is the combination of "complete air" drying with the manufacture of woven and non-woven fabrics. Here it is necessary to combine low temperature and high temperature airflow. Figure 4 illustrates a special embodiment of the invention that is very suitable for this environment. This environment is suitable for handling lightweight soft paper products. This product includes these basis weights less than 5 g / m and more than 200 g / m2. Especially the mixed assembly (50) includes a tube (54) (or similar box) (Inside) of the baffle plate (52), where the baffle plate (52) is located upstream (with respect to the direction of flow through the conduit (54)) a predetermined distance from the inlet (56) as illustrated in Figure 5). As shown in the figure, the first mud movement of the low-temperature air AlOw moves along the length of the duct (54) and hits the baffle plate (52) so as to create a low-pressure hole (56) in the inner part of the baffle plate (52). The second flow of high-temperature air Ahigh moves through the duct (58) and enters the duct through the inlet (56). For this particular low-temperature / temperature-oriented embodiment of the present invention, the baffle plate (52) includes a predetermined interval ^ --- This paper size applies to China National Standard (CNS) A4 (210 X 297 male H) Μά ^ -ΟΛΡβί ^ ηΆΡί (001 · 05 ~ \ ΰ56 ^ ΡΚ · Οΰ1,0565-2.〇 {χ May 20C, ί Please (Read the notes on the back before filling out this page)
-I---.訂---------V 457123 A7-I ---. Order --------- V 457123 A7
裝--------訂---------、 (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 距離£(圖5中的圖解)從導管(54)之下表面(6〇)移走,檔板(52) 之底部表面(58)取代所形成的下方間隔區域。也如圖4所示, 檔板(5 2)包括許多齒孔(53),此處這些齒孔有用於藉大量低溫 空氣通過而“冷卻”檔板(52)。了解需限制齒孔的數目及尺 寸’以便藉檔板結構不產生中斷此低壓區域。此待殊實施例 的其他特色爲輸出口(56)伸至導管(54)高度&,此高度大於間 隔距離£(引用圖5)。與此装配結合的特殊優點爲流動Ahi⑽ 的注入點將停留於流動路徑Alow上方。因此,流動Al〇w的 通行將不中斷流動AHIGH,其將無阻進入低壓區域。 圖6爲説明裝配(5〇)的俯視圖。如説明於此特殊實施例 中’斜形樓板(52)包括一三角幾何形狀,並包含一對間隔估 計爲角度Θ的側璧(62)及(64)。低溫氣流Alow移動經過檔板 (52),以便在輸入口(56)和檔板(52)之間產生一低壓區域 (66)。囡此,高溫氣流Ahiqh將自然地進入此低壓洞,並有 效地與氣流AL0W混合,以形成輸出氣流am1x。 圖7包含圖5中沿線7_7裝配的立體圖。顯示於此圖爲 介於標板和導管(54)之下表面(60)之間的間隔部分(55) ^如 圖’僅少數檔板(52)的支柱部分(57)及(59)與表面(60)接觸(爲 了%定目定)’允許固定的AL0W氣流通過間隔部分(55),並 提供冷卻檔板(52)。 如上所述’依照本發明的檔板裝配之利用尤其有益於 需注入低速流動至高速流動路徑的狀態。圖8説明本發明尤 其極適合此目的的裝配。此外,如最初所討論,自從本發明 技術可延仲提供結合許多不同材料,圖8説明包括一對檔板Packing -------- Order ---------, (Please read the notes on the back before filling out this page) The distance printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs £ (Figure 5) (Illustrated) is removed from the lower surface (60) of the catheter (54), and the bottom surface (58) of the baffle plate (52) replaces the lower interval area formed. As also shown in Fig. 4, the baffle plate (52) includes a plurality of perforations (53), which are here used to "cool" the baffle plate (52) by passing a large amount of low-temperature air. Understand that the number and size of perforations need to be limited so that the borrow plate structure does not interrupt this low-pressure area. Another feature of this alternative embodiment is that the outlet (56) extends to the height of the duct (54) & this height is greater than the separation distance £ (refer to Figure 5). A special advantage combined with this assembly is that the injection point of the flow Ahi⑽ will stay above the flow path Alow. Therefore, the flow of flowing AlOw will not interrupt the flowing AHIGH, which will have unimpeded access to the low-pressure area. FIG. 6 is a plan view illustrating assembly (50). As illustrated in this particular embodiment, the 'slanted floor (52) includes a triangular geometry and includes a pair of side ridges (62) and (64), which are estimated at an angle Θ. The low-temperature air flow Alow moves past the baffle plate (52) to create a low-pressure region (66) between the inlet (56) and the baffle plate (52). At this point, the high-temperature airflow Ahiqh will naturally enter this low-pressure hole and effectively mix with the airflow AL0W to form the output airflow am1x. FIG. 7 includes a perspective view of the assembly in FIG. 5 along line 7_7. Shown in this figure is the space portion (55) between the target plate and the lower surface (60) of the duct (54) ^ As shown in the figure, only the pillar portions (57) and (59) of the few baffles (52) and The surface (60) is in contact (for% fixation) 'to allow a fixed ALOW airflow to pass through the spacer (55) and to provide a cooling baffle (52). As described above, the use of the baffle assembly according to the present invention is particularly advantageous for a state where a low-speed flow to a high-speed flow path needs to be injected. Figure 8 illustrates an assembly in which the present invention is particularly well suited for this purpose. Further, as initially discussed, since the technology of the present invention can be extended to provide a combination of many different materials, FIG. 8 illustrates the inclusion of a pair of baffles.
丨X 297公釐 切 May 3义 2001 457123 經濟部智慧財產局員工消費合作杜印製 A7 B7 五、發明說明(8 ) 及結合輸入口。而且,雖然僅説明二個示範檔板及結合輸入 口,需了解可利用許多理想的檔板及結合輸入口,並劃入本 發明的精神與範圍之中。此外,依照本發明的指示,多數檔 板/ 口裝配可配置於任何理想箱内之中的方式。舉例來説,它 們可沿箱内長度配置,或者橫跨箱内寬度,或任何適當组合。 一般而言,其在箱内之中的位置(與檔板一樣長,配置於結合 輸入口的上游)與本發明的指示無關。 尤其引用圖8’装配(70)包括一第一檔板片(72)及一第 二檔板片(74),每個檔板片配置延伸橫跨箱内(76)的寬度。高 速材料V Η的第一流動(舉例來説,一澄清液體)移動經過箱内 (7 6)’使得其最初碰到’並在第一樓板片(7 2 )移動,後來打到 並在第二檔板片(74)移動。低速材料vL1(舉例來説,一乳化 劑)的第二流勤藉第一輸入口(78)引進箱内(76)。同樣地,低 速材料VLa(舉例來説,一不同組成物與/或者速度的乳化劑) 的第三流動藉第二輸入口(80)引進箱内(76)。依照本發明的指 示,每個輸入口位於其結合檔板片的估計距離下游。如討論 於上的其他實施例,裝配(70)允許在每個檔板與其結合輸入 口之間的區域形成低壓部分。因此,在此特殊實施例中,低 壓部分允許低速流動VL1•及ΛΑ。注入至一足夠的箱内容量, 以便引起有效混合。此外,如圖8所示,本發明的任何檔板 結構可形成作爲多數單位結構,其具有加入或除去分離單位 的能力,以達到不同結果。舉例來説,第二檔板組件(82)可 附著至第一檔板片(72)的頂部部分,此處第二組件(82)可允許 檔板結構甚至以較高速材料運轉。因此了解在剩餘時間可 (請先閱讀背面之注項再填寫本頁) 裝--------訂---------,! !丨 X 297mm Cut May 3 Yi 2001 457123 Duty printing of employee cooperation of Intellectual Property Bureau of the Ministry of Economic Affairs A7 B7 V. Description of invention (8) and combined input port. Moreover, although only two demonstration baffles and combined input ports are described, it should be understood that many ideal baffles and combined input ports can be utilized and fall into the spirit and scope of the present invention. In addition, in accordance with the instructions of the present invention, most baffle / mouth assemblies can be configured in any desired manner. For example, they can be arranged along the length of the box, or across the width of the box, or any suitable combination. Generally speaking, its position in the box (as long as the baffle plate, arranged upstream of the joint input port) has nothing to do with the instructions of the present invention. Particularly referring to FIG. 8 ', the assembly (70) includes a first baffle plate (72) and a second baffle plate (74), and each baffle plate is configured to extend across the width of the box (76). The first flow (for example, a clear liquid) of the high-speed material VΗ moves through the box (7 6) 'so that it initially touches' and moves on the first floor plate (7 2), and then hits and moves on the first The second plate (74) moves. The second flow of the low-speed material vL1 (for example, an emulsifier) is introduced into the box (76) through the first input port (78). Similarly, the third flow of the low-speed material VLa (for example, an emulsifier of a different composition and / or speed) is introduced into the tank (76) through the second input port (80). In accordance with the instructions of the present invention, each input port is located downstream of its estimated distance in conjunction with the baffle plate. As discussed in the other embodiments above, the assembly (70) allows a low-pressure section to be formed in the area between each baffle and its joint input. Therefore, in this particular embodiment, the low-pressure portion allows low-speed flow of VL1 • and ΛA. Inject into a sufficient tank content to cause effective mixing. In addition, as shown in FIG. 8, any baffle structure of the present invention can be formed as a majority unit structure, which has the ability to add or remove separation units to achieve different results. For example, the second baffle assembly (82) may be attached to the top portion of the first baffle sheet (72), where the second assembly (82) may allow the baffle structure to operate even with higher speed materials. So understand that it is available in the remaining time (please read the note on the back before filling this page) -------- Order --------- ,!!
A7 Μ 2 3 ----------Β7^________ 五、發明說明(9 ) 整檔板大小及形狀,以適合各種不同材料的速度,此處調整 最好可利用多數單位檔板結構達成。 圖9包含圖8中沿線9 - 9裝配(7 0)的斜裁側面圖。如事 先所时論’在低速流動注入高速流動之狀態中的構板利用尤 其有利。在本發明無檔板結構的傳統装配中,高速流動VH 力引起第一輸入口(7 8)彎曲,如圖9所示。因此擾亂低速材 料Vli的注入路徑’更進一步降低流動Vh與VL1的混合效 率。因此依照本發明指示之檔板片(72)利用充當介於高速流 動與輸入口之間的自然阻礙,其允許低速材料於理想方向注 入0A7 Μ 2 3 ---------- Β7 ^ ________ V. Description of the invention (9) The size and shape of the entire baffle plate to suit the speed of various materials, it is best to use most unit baffle plates for adjustment here. Structure reached. FIG. 9 includes an oblique side view of the assembly (70) along line 9-9 in FIG. 8. FIG. As previously stated, the use of a slab in a state where low-speed flow is injected into high-speed flow is particularly advantageous. In the traditional assembly of the baffle-free structure of the present invention, the high-speed flowing VH force causes the first input port (78) to bend, as shown in FIG. Therefore, disturbing the injection path 'of the low-speed material Vli further reduces the mixing efficiency of the flowing Vh and VL1. Therefore, the baffle plate (72) according to the present invention utilizes as a natural obstacle between high-speed flow and the input port, which allows low-speed materials to be injected in the ideal direction.
本發明的有效數字敘述乃包括於圖10中。尤其,當利 用本發明裝配結合不同溫度之氣流時,圖1 0爲説明沿一室之 溫度變化(爲距離函數)的曲線圖。對説明於圖9的結果而言, 具有250e F周圍溫度的第一氣流與具有2440。F周圍溫度的 第二氣流結合。氣流結合效率可藉評估在二流動開始結合的 任一點下游之溫度變化而測定。圖1 〇中的曲線圖包括在三分 離位置中的溫度變化測定,此三分離位置爲越過高溫流動輸 入口位置575英吋距離的第一點B,越過輸入口 779英叶距 離的第二點C,以及越過:輸入口 983英吋距離的第三點。與 傳統之先前技術結構結合的溫度變化乃表示於圖9中的循 環。與本發明所利用檔板裝配結合的混合效率之改善可明顯 從測定於三個相同位置B、C及D的溫度變化圖看出,如以 三角形表示。尤其在位置B中,溫度變化從500。F降至60 e F。在位置C中,變化爲從320° F降至24。F,最後,在D $紙張尺度通用中國國家標準(CNS)A4規格(210 X 297公釐) (請先閱讀背面之注竜孝項再填寫本頁) -1 I . -------訂---------. 經濟部智餐財1局員工消費合作社印製 457123 A7 _B7_ 五、發明說明(1Q) 點的變化爲從1 80° F降至1 6° F。需了解這些數據表示爲溫 度變化(如在結合點位置橫跨箱内寬度的函數),並無混合氣 流的實際周圍溫度。 (請先閱讀背面之注意事項再填寫本頁) 褒--------訂---------^ 經濟部智慧財產局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS>A4規格(210 X 297公釐) Waw_s-mPafenAPA001.05~W565W<-001-0565e.D〇cί, 2001 457123 Α7 Β7 五、發明說明(1 Μ 圖示元件簡箪說明 經濟部智慧財產局員工消費合作社印製 10 arrangement 裝配 12 tapered baffle 斜形樓板 14 duct 輸送管 18 wall 内壁 20 point 點 22 wall 内壁 24 input port 輸入口 26 tubing 管道 28 downstream side 下游側 30 back edge 背端 32 cavity area 洞區域 34 sidewall 側壁 50 arrangement 裝配 52 baffle 檔板 53 perforation 齒孔 54 conduit 導管 55 gap area 間隔部分 56 low pressure cavity 低壓洞 57 leg portion 支柱部分 58 tubing 管道 59 leg portion 支柱部分 60 lower surface 下表面 (請先閱讀背面之注意事項再填寫本頁) ϋ I n^OJ* ϋ 1 ϋ ϋ n I * 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐〉 Μβν/5-ΟΑΡ3ίβηί\Ρ*ΰ0ί.ΰ5'ί0565\ΡΚ-ύ01Ό5ί5·2.£)〇ΰ May 31,2001 A7 經濟部智慧財產局員工消費合作社印製 ]23 ___B7 五、發明說明(12) 62 sidewall 侧壁 64 sidewall 側壁 66 low pressure region 低壓區域 70 arrangement 裝配 72 first baffle plate 第一樓板片 74 second baffle plate 弟二檀板片 76 enclosure 箱内 78 first input port 第一輸入α 80 second input port 第二輸入口 82 second baffle section 第二檔板組件 d distance 距離 G, first gas stream 第一氣流 g2 second gas stream 第二氣流 (請先閱讀背面之注意事項再填寫本頁) 裝!----訂------! 本紙張尺度適用_國國家標準(CNS)A4規格(210 X 297公釐)A valid digital description of the present invention is included in FIG. In particular, when using the present invention to assemble airflows of different temperatures, Fig. 10 is a graph illustrating the temperature change (as a function of distance) along a chamber. For the results illustrated in FIG. 9, the first airflow having an ambient temperature of 250e F and the airflow having 2440. F Ambient temperature combined with a second air flow. Airflow binding efficiency can be measured by evaluating the temperature change downstream of any point where the two flows begin to combine. The graph in Figure 10 includes the measurement of the temperature change in a three-separation position, which is the first point B over the 575-inch distance from the high-temperature flow input position, and the second point at the 779-inch distance over the input port. C, and crossed: the third point of the 983-inch input port. The temperature change combined with the conventional prior art structure is shown in the cycle in FIG. The improvement of the mixing efficiency combined with the baffle assembly used in the present invention can be clearly seen from the temperature change diagrams measured at three identical positions B, C, and D, as indicated by triangles. Especially in position B, the temperature changes from 500. F drops to 60 e F. In position C, the change is from 320 ° F to 24. F. Finally, the paper size in D $ is the common Chinese National Standard (CNS) A4 specification (210 X 297 mm) (please read the note on the back before filling out this page) -1 I. ------ -Order ---------. Printed by the Consumers' Cooperative of the 1st Bureau of Intelligent Meal and Finance of the Ministry of Economic Affairs 457123 A7 _B7_ 5. The change of the point of invention (1Q) is from 180 ° F to 16 ° F. It is important to understand that these data are expressed as a change in temperature (as a function of the width across the box at the junction), and there is no actual ambient temperature of the mixed gas flow. (Please read the precautions on the back before filling this page) 褒 -------- Order --------- ^ Printed on paper standards of the Ministry of Economic Affairs, Intellectual Property Bureau, Staff Consumer Cooperatives, this paper applies Chinese national standards (CNS > A4 specifications (210 X 297 mm) Waw_s-mPafenAPA001.05 ~ W565W < -001-0565e.D〇cί, 2001 457123 Α7 Β7 V. Description of the invention (1 Μ Graphical elements briefly explain the intellectual property of the Ministry of Economic Affairs) Printed by the Consumer Cooperative of the Bureau 10 arrangement Assembly 12 tapered baffle Sloped floor 14 duct Conveying pipe 18 wall Inner wall 20 point 22 wall Inner wall 24 input port 26 tubing 28 downstream side 30 back edge 32 cavity area Area 34 sidewall 50 arrangement 52 baffle baffle 53 perforation 54 conduit 54 gap area 56 low pressure cavity 57 leg portion pillar 58 tubing 59 leg portion pillar 60 lower surface Read the notes on the back and fill in this page) ϋ I n ^ OJ * ϋ 1 ϋ ϋ n I * This paper size is applicable to China Standard (CNS) A4 (210 X 297 mm) Μβν / 5-ΟΑΡ3ίβηί \ Ρ * ΰ0ί.ΰ5'ί0565 \ ΡΚ-ύ01Ό5ί5 · 2. £) 〇ΰ May 31,2001 A7 Consumer Consumption Cooperative of Intellectual Property Bureau, Ministry of Economic Affairs Printed] 23 ___B7 V. Description of the invention (12) 62 side wall 64 side wall 66 side wall 66 low pressure region 70 arrangement 70 first baffle plate 74 second baffle plate 76 enclosure 78 first input port first input α 80 second input port 82 second baffle section d distance distance G, first gas stream first gas stream g2 second gas stream second (please read the precautions on the back first) Fill out this page) Install! ---- Order ------! This paper size applies _ National Standard (CNS) A4 specification (210 X 297 mm)
Mavis-/}.lPaienAPAiWi.05~W565lPK-£W 1-0565-2.D〇c May 31,2001Mavis-/}. LPaienAPAiWi.05 ~ W565lPK- £ W 1-0565-2.D〇c May 31, 2001
Claims (1)
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PCT/US1998/017967 WO2000012202A1 (en) | 1998-08-28 | 1998-08-28 | Arrangement for combining dissimilar streams |
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TW088114685A TW457123B (en) | 1998-08-28 | 1999-10-29 | Arrangement for combining dissimilar streams |
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EP (1) | EP1107821B1 (en) |
JP (1) | JP2002523228A (en) |
KR (1) | KR100515233B1 (en) |
CN (1) | CN1105595C (en) |
AR (1) | AR020352A1 (en) |
AU (1) | AU746491B2 (en) |
BR (1) | BR9815994A (en) |
CO (1) | CO4960669A1 (en) |
DE (1) | DE69815403D1 (en) |
HK (1) | HK1039582A1 (en) |
SV (1) | SV1999000142A (en) |
TW (1) | TW457123B (en) |
WO (1) | WO2000012202A1 (en) |
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DE602005021003D1 (en) | 2004-02-27 | 2010-06-17 | Haldor Topsoe As | Device for mixing fluid streams |
DE102006004069A1 (en) | 2006-01-28 | 2007-09-06 | Fisia Babcock Environment Gmbh | Method and device for mixing a fluid with a large gas flow rate |
JP4961847B2 (en) * | 2006-06-12 | 2012-06-27 | いすゞ自動車株式会社 | Exhaust gas purification method and exhaust gas purification system |
DE102007035226A1 (en) * | 2007-07-25 | 2009-01-29 | J. Eberspächer GmbH & Co. KG | Flow guiding device and thus equipped exhaust system |
EP2185274A4 (en) | 2007-09-07 | 2012-12-05 | Turbulent Energy Inc | Dynamic mixing of fluids |
US9708185B2 (en) | 2007-09-07 | 2017-07-18 | Turbulent Energy, Llc | Device for producing a gaseous fuel composite and system of production thereof |
US8715378B2 (en) | 2008-09-05 | 2014-05-06 | Turbulent Energy, Llc | Fluid composite, device for producing thereof and system of use |
US9310076B2 (en) | 2007-09-07 | 2016-04-12 | Turbulent Energy Llc | Emulsion, apparatus, system and method for dynamic preparation |
US9144774B2 (en) | 2009-09-22 | 2015-09-29 | Turbulent Energy, Llc | Fluid mixer with internal vortex |
US8871090B2 (en) | 2007-09-25 | 2014-10-28 | Turbulent Energy, Llc | Foaming of liquids |
US8844495B2 (en) | 2009-08-21 | 2014-09-30 | Tubulent Energy, LLC | Engine with integrated mixing technology |
FR2952311A1 (en) * | 2009-11-09 | 2011-05-13 | Renault Sa | Device for mixing intake air flow with recirculated exhaust gas flow in internal combustion engine of e.g. diesel type motor vehicle, has mixing plate integrated to air duct and comprising downstream edge located upstream of axis of pipe |
US8317390B2 (en) * | 2010-02-03 | 2012-11-27 | Babcock & Wilcox Power Generation Group, Inc. | Stepped down gas mixing device |
WO2012050858A1 (en) | 2010-09-28 | 2012-04-19 | Dow Global Technologies Llc | Reactive flow static mixer with cross-flow obstructions |
DE102011077645A1 (en) | 2011-06-16 | 2012-12-20 | Bosch Emission Systems Gmbh & Co. Kg | Static mixer |
EP2570179A1 (en) * | 2011-09-16 | 2013-03-20 | Air Liquide Deutschland GmbH | Method and apparatus for dynamic gas mixture production |
JP6296884B2 (en) * | 2014-04-30 | 2018-03-20 | 三菱日立パワーシステムズ株式会社 | Flue gas desulfurization equipment |
GB2533331A (en) * | 2014-12-16 | 2016-06-22 | Daimler Ag | Mixing device for an exhaust gas system |
JP6377575B2 (en) * | 2015-05-21 | 2018-08-22 | 住友金属鉱山株式会社 | Fluid blowing apparatus and chemical reaction apparatus using the same |
JP6690485B2 (en) * | 2016-09-20 | 2020-04-28 | 住友金属鉱山株式会社 | Chemical reactor and method for producing particles using the chemical reactor |
CN108479325A (en) * | 2018-05-16 | 2018-09-04 | 山东志伟环保科技有限公司 | A kind of mixing arrangement of oxidation and denitration |
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JPS5233822B2 (en) * | 1972-03-18 | 1977-08-31 | ||
DE3043239C2 (en) * | 1980-11-15 | 1985-11-28 | Balcke-Dürr AG, 4030 Ratingen | Method and device for mixing at least two fluid partial flows |
US5159958A (en) * | 1991-07-18 | 1992-11-03 | Hydro Systems Company | Chemical eductor with integral elongated air gap |
US5409514A (en) * | 1991-09-03 | 1995-04-25 | Ragusa; Guiseppe | Air filter |
CH687831A5 (en) * | 1993-04-08 | 1997-02-28 | Asea Brown Boveri | Premix burner. |
DE4412261C2 (en) * | 1994-04-09 | 1996-10-17 | Jonas Konrad H | Device for merging at least two flow media |
KR0161082B1 (en) * | 1995-10-11 | 1999-01-15 | 김광호 | Coal oil combustion equipment |
-
1998
- 1998-08-28 CN CN98814291A patent/CN1105595C/en not_active Expired - Fee Related
- 1998-08-28 EP EP98944606A patent/EP1107821B1/en not_active Expired - Lifetime
- 1998-08-28 BR BR9815994-1A patent/BR9815994A/en not_active IP Right Cessation
- 1998-08-28 WO PCT/US1998/017967 patent/WO2000012202A1/en active IP Right Grant
- 1998-08-28 JP JP2000567295A patent/JP2002523228A/en active Pending
- 1998-08-28 KR KR10-2001-7002480A patent/KR100515233B1/en not_active IP Right Cessation
- 1998-08-28 DE DE69815403T patent/DE69815403D1/en not_active Expired - Lifetime
- 1998-08-28 AU AU92112/98A patent/AU746491B2/en not_active Ceased
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1999
- 1999-08-27 CO CO99054267A patent/CO4960669A1/en unknown
- 1999-08-27 AR ARP990104329A patent/AR020352A1/en unknown
- 1999-08-27 SV SV1999000142A patent/SV1999000142A/en unknown
- 1999-10-29 TW TW088114685A patent/TW457123B/en not_active IP Right Cessation
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2002
- 2002-02-18 HK HK02101142.3A patent/HK1039582A1/en unknown
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CN1105595C (en) | 2003-04-16 |
AU9211298A (en) | 2000-03-21 |
AU746491B2 (en) | 2002-05-02 |
KR20010106455A (en) | 2001-11-29 |
CN1314824A (en) | 2001-09-26 |
HK1039582A1 (en) | 2002-05-03 |
EP1107821A1 (en) | 2001-06-20 |
WO2000012202A1 (en) | 2000-03-09 |
EP1107821B1 (en) | 2003-06-04 |
SV1999000142A (en) | 2000-07-06 |
CO4960669A1 (en) | 2000-09-25 |
JP2002523228A (en) | 2002-07-30 |
DE69815403D1 (en) | 2003-07-10 |
AR020352A1 (en) | 2002-05-08 |
KR100515233B1 (en) | 2005-09-16 |
BR9815994A (en) | 2001-10-16 |
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