TWI299029B - - Google Patents

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Publication number
TWI299029B
TWI299029B TW95124427A TW95124427A TWI299029B TW I299029 B TWI299029 B TW I299029B TW 95124427 A TW95124427 A TW 95124427A TW 95124427 A TW95124427 A TW 95124427A TW I299029 B TWI299029 B TW I299029B
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TW
Taiwan
Prior art keywords
bed
receiving chamber
quantitative
discharge device
quantitative discharge
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TW95124427A
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Chinese (zh)
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TW200804157A (en
Inventor
Jing-Yu Peng
Chung Cheng Han
Zong-Jie Wu
Ming-Jun Li
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Ind Tech Res Inst
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Priority to TW95124427A priority Critical patent/TW200804157A/en
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Publication of TWI299029B publication Critical patent/TWI299029B/zh

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Description

1299029 九、發明說明: 【發明所屬之技術領域】 置:應用敎業之粉粒體供 維護容易並可彈性調整顆粒 本發明係有關於一種出料裝 應,特別是一種低成本、耐高溫、 床定量出料裝置。 【先前技術】 顆粒床是工業上常用儲存裝置,其主 出料口定量下料至下游處理單元,例如,^丸 槽分下游儲槽以便加工處理。一般而言成二= =㈣考慮送料口有上下游氣體壓力(差)控制(例如氣^ 游進入上端床翻影響床體之·;或減地,上體 氣體不希望進人下端床體内產生加4理之 = 問題,傳統之輸送帶/振動t、輸送管、扣鏈齒、輪里^ (HYDRAULIC^ACTUATED)、鉤爪結構輸送(KNUckled STACKING CONVEYOR)即可使用,否貝,須使用螺旋輸送 (Screwer Feeder)、氣送(pneumatic Transfer)方式或往復式輸送 (Reciprocating Conveyor)。 為了角午決上下游間之氣密性與壓力問題,常使用較小螺 旋間隙(Pitch)、較長軸距之螺旋輸送裝置或須搭配旋轉閥 (Rotary Valve)使用,如美國專利公告第4,〇58,227號專利,但 這些裝置利用機械強力輸送之過程,容易造成設備與原料之磨 損,此外,如系統必須應用於高溫或強酸強鹼環境操作,則所 需空間及整體造價相當高。 又如以喷嘴氣送方式可以應用於高溫環境,但對於計算 或控制包括粉粒體比重、粒徑與出料量之效果不佳,此外須加 強設計減少氣體與顆粒體磨損管路(前案美國專利公告\第 1299029 容5/。15,830號專利等),因此實際上之應用、操控與 後上ΐ送’例如前案GB 2G39262號專利,係在輸送 ϊ 粒外漏’亦可作為顆粒體分離之用。US 4,043,471 淮㈣I用於間歇式煤炭進入氣化爐(GASIFIER UNIT)之 ϋί认設計利用兩組直立式密封活塞,循環地將顆粒送出 特殊iim械精密度度非常高,成本高,且不適用於 送之二:俨+ 乂:所面臨之另-瓶頸為設計必須針對所要輸 圪之叔粒體粒徑1身訂作,缺者 粒體麵時,如粒徑大小有—㊉"床體要更換粉 組更換。 】有疋乾圍之1距,則下料裝置須整 【發明内容】 量二本發二 室以=職於補室兩端之㈣ 料 動;藉此,不僅成本鎌,且祕轉,運 ::象 須之動力。 轉大崎健動機構所 1299029 有關本發明之詳_容及觀,兹就配 【實施方式】 根據本發明所揭露之顆粒床定量出料史 圖」所示,係包含有進料儲槽10、定量下料本體;;二“ 14驅動控制杈組40,進料儲槽1〇連接於定量下料本體2〇 =進料π 21卜粉粒體由進料騎1G自然落人定量下料本體 5 ΪΓί槽^内並具有流場改錄置1卜其係可為架橋破 猎由流場改良裝置11之作用,可消除粉粒體於 儲槽10之七留現象同時減輕進料儲槽1〇内粉粒體之靜置 反力,相對大幅降低驅動機構所須之動力。 而定量下料本體20包含有承料室21以及連接於承料室 „之出料斗槽22、23 ’而承料室2"既略中央處具有進料 進料口 211連接於進料儲槽1〇,粉粒體藉由進料儲槽 刑从通ΐ進料口 211進人至承料室2卜承料室21概略為直線 ,腔體’而推料桿30可於承料室21内左右直線運動,推料 L Λ具,有至少一個的推樹反31,其可視氣密性之需求設計 示係為三片),且可於推料桿3〇卸下後 驅動控制模組40包含有馬達41與曲柄滑塊機構42,如 2圖」所不’曲柄滑塊機構42包含圓形曲柄42卜連桿 、滑塊423(即推料板叩,利用此機構可將馬達Μ等速轉 ^之^向轉變為往復左右運動,且消除了滑動磨擦,减小了振 ^降低了噪音’同時也提高了設備的壽命和可靠性;上下游 f壓力之影響可藉由連接桿⑽粒體積料與純板之阻隔 而有效降低。 此,粉粒體藉由進料儲槽10落入定量下料本體20之 推^ ^ ^域由推料桿3G之左右直線運動,使粉粒體隨 " 移動頻率移動定量粉粒體至左右兩側,落入兩側之 1299029 出料斗槽22、23,進入下游儲槽或加工單元,$、 動作。如須分離不同粒徑粉粒體,則定量下 %成整個出料 粉粒體定餘岐,可裝設錄體分離本體20將 料波道及跳_板,使粉_在向下運動時裝置包含下 態,有利於大小顆粒之分離,再湘抽氣罩 或篩網分離不同粒徑粉粒體。 早x乳體作質量分選 雖然本發明以前述之較佳實施例揭露如上, ^m明’ _熟習此技藝者,在不脫用 視後附之申請專利範圍所界定者為準。月之保護乾圍當 l299〇29 Γ圖式簡單說明】 ^1圖係為本發明顆粒床定量出料裝置之示意圖。 —第2圖係為本發明顆粒床定量出料裝置之驅動控制模組 之示意圖。 【主要元件符號說明】 10 11 201299029 IX. Description of the invention: [Technical field to which the invention belongs]: application of powder and granules for maintenance and easy adjustment and elastic adjustment of particles. The invention relates to a discharge assembly, in particular, a low-cost, high-temperature resistant, Bed quantitative discharge device. [Prior Art] The granular bed is a commonly used storage device in the industry, and the main discharge port is quantitatively fed to the downstream processing unit, for example, the pill is divided into a downstream storage tank for processing. Generally speaking, it is two == (4) Consider that the feed port has upstream and downstream gas pressure (difference) control (for example, the gas enters the upper bed to affect the bed body; or the ground gas does not want to enter the lower end of the bed) The problem is that the traditional conveyor belt/vibration t, the conveying pipe, the sprocket, the wheel (HYDRAULIC^ACTUATED), and the KNUckled STACKING CONVEYOR can be used. Sender (Screwer Feeder), pneumatic transfer (Reciprocating Conveyor). For the airtightness and pressure between the upstream and downstream, often use a small spiral gap (Pitch), longer axis The screw conveyor of the distance may be used with a Rotary valve, such as U.S. Patent No. 4, No. 5,227, 227, but these devices utilize mechanical strength conveying processes, which are liable to cause wear of equipment and materials, and, for example, systems. Must be used in high temperature or strong acid and alkali environment operation, the required space and overall cost are quite high. Another example is the nozzle gas delivery method can be applied to high temperature environment, but for calculation or control including powder The effect of bulk specific gravity, particle size and discharge volume is not good. In addition, it is necessary to strengthen the design to reduce the gas and granule wear pipeline (previously US Patent Publication \1299029 容5/.15,830 patent, etc.), so the actual application , control and post-upper delivery, such as the patent GB 2G39262, which is used to transport granules, can also be used as granule separation. US 4,043,471 Huai (4) I for intermittent coal into gasifier (GASIFIER UNIT) The 认 design recognizes the use of two sets of upright sealed pistons to circulate the particles out of the special iim. The precision is very high, the cost is high, and it is not suitable for sending two: 俨 + 乂: the other bottleneck is the design must For the size of the granules to be transported, the granule surface is ordered. If the granule surface is missing, if the particle size is -10" the bed should be replaced with a powder group. The device must be completed [invention content] The amount of two hairs is two rooms to work at the two ends of the room (4). In this way, not only the cost, but also the secret transfer, the operation:: the power of the elephant. 1299029 Details of the invention and its concept According to the particle bed quantitative discharge history disclosed in the present invention, the invention includes a feed storage tank 10 and a quantitative discharge body; and a second “14 drive control unit 40, a feed storage tank 1”. Connected to the quantitative blanking body 2〇=feeding π 21bu powder granules by feeding 1G natural falling people quantitative feeding body 5 ΪΓί slots ^ with flow field re-recording 1 Bu can be used for bridging By the action of the flow field improving device 11, the phenomenon of the retention of the powder and granules in the storage tank 10 can be eliminated and the static reaction force of the powder and granules in the feed storage tank 1 can be alleviated, and the power required for the driving mechanism can be relatively greatly reduced. The quantitative blanking body 20 comprises a receiving chamber 21 and a discharge hopper groove 22, 23' connected to the receiving chamber „, and the receiving chamber 2" has a feed inlet 211 connected to the feed storage tank at the center 1〇, the powder and granules are taken from the overnight feed port 211 into the receiving chamber 2, and the receiving chamber 21 is substantially straight, and the cavity is in the receiving chamber 21 In the left and right linear motion, push the L cookware, there is at least one push tree reverse 31, the design of the visual airtightness is designed to be three pieces), and the drive control module can be driven after the pusher bar 3〇 is removed. 40 includes a motor 41 and a crank slider mechanism 42. As shown in FIG. 2, the crank slider mechanism 42 includes a circular crank 42 and a slider 423 (ie, a pusher plate 叩, by which the motor can be Μ The constant velocity transfer turns into a reciprocating left and right movement, and eliminates the sliding friction, which reduces the vibration and reduces the noise. It also improves the life and reliability of the equipment; the influence of the upstream and downstream f pressure can be achieved by the connecting rod (10) The particle volume material is effectively reduced by the barrier of the pure plate. Therefore, the powder and granules fall into the quantitative blank body 20 by the feed storage tank 10. ^ ^ ^ The field moves linearly from the left and right sides of the push rod 3G, so that the powder and granules move the quantitative powder and granules to the left and right sides with the moving frequency, and fall into the 1299029 discharge hopper grooves 22 and 23 on both sides, and enter the downstream storage tank. Or processing unit, $, action. If it is necessary to separate the powder particles of different particle sizes, the % of the powder can be divided into the entire discharge powder and the volume of the powder, and the body separation body 20 can be installed to feed the channel and the jump plate. When the powder _ is moved downward, the device comprises the lower state, which is beneficial to the separation of the sized particles, and the granules of different sizes are separated by the hood or the screen. The early x-mass is used for mass sorting, although the invention is The preferred embodiment is disclosed above, and the skilled person is familiar with the art, and the definition of the patent application scope is not limited. The protection of the month is as simple as l299〇29 Γ 1 is a schematic view of a granular bed quantitative discharging device of the present invention. - Fig. 2 is a schematic view of a driving control module of the granular bed quantitative discharging device of the present invention. [Main component symbol description] 10 11 20

21 211 22、23 30 31 40 41 42 421 42221 211 22, 23 30 31 40 41 42 421 422

進料儲槽 流場改良裝置 定量下料本體 承料室 進料口 出料斗槽 推料桿 推料板 控制驅動模組 馬達 曲柄滑塊機構 圓形曲柄 連桿 滑塊 423Feed storage tank Flow field improvement device Quantitative blanking body Feeding chamber Feeding port Outlet hopper groove Pusher bar Pusher plate Control drive module Motor Crank slider mechanism Round crank Link rod Slider 423

Claims (1)

Ϊ299029 十、申請專利範圍: 今]午f…-‘无 L =2=粒床定量出料裝置,係包含有: 疋置下料本體,具有一承料室以及分別位於該承料室兩端 之出料斗槽,且該承料室具有一進料口; 一推料桿,其上具有至少一推料板,並可於該承料室左右直 線移動; 一驅動控麵組,連接贿轉桿,贱控繼推之左 右直線運動;及 一^料儲槽,内具有-流場改良裝置,裝設於該定量下料本 體之進料口。 2. 3. 4. 5. 6. 7. if,1項所述之顆粒床定量出料裝置,其中該 推料板係概略密合於該承料室。 所述之顆粒床定量出料裝置,其中該 推料杯係具有二個推料板。 如:請專利範圍第1項所述之顆粒床定量出料裝置,皇中該 驅ϊΐΐ模組係包含有一馬達與一曲柄滑塊機構。 床定*咖置,其中該 斗槽置’。更包含 述之顆粒床定量出料裝置,其中該 刀離裝置匕3有-下枓波道及—跳_板。 如申料利範圍第7酬述之顆粒床定量 分離裝置係糊-抽氣罩⑽氣體作f量。八“ 如申明專利I巳圍第7項所述之顆粒床定料 分離裝置侧_網分離。 里巾概置,其中違 9.Ϊ299029 X. Patent application scope: Today] noon f...-'No L = 2=granular bed quantitative discharge device, including: 疋 下 下 body, with a receiving chamber and respectively located at the two ends of the receiving chamber a discharge hopper groove, and the receiving chamber has a feeding port; a pushing rod having at least one pushing plate thereon, and being linearly movable to the left and right of the receiving chamber; a driving control surface group connecting the bribe The rod, the left and right linear motion of the stepping push; and a material storage tank having a flow field improving device installed in the feeding port of the quantitative blanking body. 2. 3. 5. 5. 6. 7. If the particle bed quantitative discharge device of item 1, wherein the pusher plate is substantially in close contact with the receiving chamber. The granular bed quantitative discharge device, wherein the pusher cup has two pusher plates. For example, please refer to the granular bed quantitative discharge device described in the first item of the patent scope. The system of the drive system includes a motor and a crank slider mechanism. The bed is set to be placed, and the bucket is placed. Further included is a granular bed quantitative discharge device, wherein the cutter has a lower jaw channel and a skip plate. For example, the particle bed quantitative separation device of the seventh remuneration range is the paste-exhaust hood (10) gas for the amount of f.八" As stated in the patent I, the particle bed fixed material separation device side _ net separation described in item 7 of the patent.
TW95124427A 2006-07-05 2006-07-05 Quantitative output device for particle bed TW200804157A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106953222A (en) * 2017-05-02 2017-07-14 东莞市精钜机械科技有限公司 A kind of carbon brush forming machine and its powder quantitative-feedingdevice device
CN110395592A (en) * 2019-03-01 2019-11-01 沈阳工业大学 A kind of doffer
CN110905221B (en) * 2019-12-05 2021-07-23 宁波润爵科技有限公司 Throw brick device with regulatory function

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