TWI570230B - Continuous feeding device - Google Patents
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- TWI570230B TWI570230B TW101130383A TW101130383A TWI570230B TW I570230 B TWI570230 B TW I570230B TW 101130383 A TW101130383 A TW 101130383A TW 101130383 A TW101130383 A TW 101130383A TW I570230 B TWI570230 B TW I570230B
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Description
本揭露係關於一種進料裝置,特別是關於一種可將物料連續送至物料儲槽之連續進料裝置。 The present disclosure relates to a feeding device, and more particularly to a continuous feeding device that continuously feeds material to a material storage tank.
隨著科技的日新月異以及大環境的快速發展,人們對於能源亦不斷的消耗,然而如石油等天然資源卻並非取之不盡,用之不竭,因此,各國皆致力於新的替代能源的開發,而生質能源即是目前所致力發展的再生能源的一環。 With the rapid development of science and technology and the rapid development of the environment, people are constantly consuming energy. However, natural resources such as oil are not inexhaustible. Therefore, all countries are committed to the development of new alternative energy sources. And biomass energy is a part of renewable energy that is currently developing.
生質能源的製造過程中,必須將粉狀或粒狀之生質物料以連續進料方式輸送至反應器進行生質物料的裂解,以形成生質油。 In the manufacturing process of biomass energy, powdery or granular raw materials must be transported to the reactor in a continuous feed to crack the raw materials to form a raw oil.
在習知的生質物料連續進料系統中,常以輸送帶或真空吸料方式將生質物料送至物料儲槽中,再送至下游之反應器以進行裂解反應。輸送帶為一簡單之生質物物料輸送裝置,然而因占地面積較大,常以真空吸料裝置取代之,藉由真空吸料裝置,可將生質物料送至物料儲槽中,進而送至物料反應器以進行反應。 In the conventional continuous feeding system of raw materials, the raw materials are usually sent to the material storage tank by means of conveyor belt or vacuum suction, and then sent to the downstream reactor for cracking reaction. The conveyor belt is a simple material conveying device. However, due to the large floor space, it is often replaced by a vacuum suction device. The vacuum material can be used to send the raw materials to the material storage tank. Go to the material reactor to carry out the reaction.
由於生質物料具有質量輕、密度小、安息角大、含水率高及流動性差等特性,習知真空吸料裝置很容易造成架橋現象,幾乎無法正常持續供料。為了解決習知真空吸料裝置的架橋現象,將現有真空吸料裝置之本體錐狀底部之出料重力檔板取消,增加下料斗及旋轉閥,在常壓操作時,可達到連續進料的基本功能。惟,以真空吸料裝置結合正 壓物料儲槽,在連續下料至物料儲槽時,會因為旋轉閥轉動,經由轉子間隙、轉子轉速及進出口壓力差等因素而在物料儲槽內產生局部負壓。此局部負壓將造成連接於物料儲槽下游反應器之高溫氣體往物料儲槽方向逆流。此高溫逆流氣體流至被輸送之物料時,加熱含有水份之生質物料而產生水氣,因此,易在物料進料至反應器時造成物料架橋、結塊、阻塞導致物料無法連續進料,而使反應器無法操作。 Because the raw material has the characteristics of light weight, small density, large angle of repose, high water content and poor fluidity, the conventional vacuum suction device is easy to cause bridging, and it is almost impossible to continuously supply. In order to solve the bridging phenomenon of the conventional vacuum suction device, the discharge gravity plate of the cone bottom of the existing vacuum suction device is cancelled, and the lower hopper and the rotary valve are added, and the continuous feeding can be achieved during the normal pressure operation. basic skills. Only with a vacuum suction device When the material storage tank is continuously discharged to the material storage tank, a partial negative pressure is generated in the material storage tank due to the rotation of the rotary valve and the rotor clearance, the rotor rotation speed and the inlet and outlet pressure difference. This partial negative pressure will cause the high temperature gas connected to the reactor downstream of the material storage tank to flow backward in the direction of the material storage tank. When the high-temperature counter-current gas flows to the material to be conveyed, the raw material containing water is heated to generate moisture, so that it is easy to cause material to be bridged, agglomerated, and blocked when the material is fed to the reactor, so that the material cannot be continuously fed. And the reactor is inoperable.
因此,如何解決習知技術中,進料系統於連續進料時,其物料儲槽中產生物料架橋、結塊等問題,實已成目前亟欲解決的課題。 Therefore, how to solve the problem in the prior art that the feeding system generates material bridging, agglomeration and the like in the material storage tank during continuous feeding has become a problem to be solved at present.
本揭露提供一種連續進料裝置,係包括吸料機、第一旋轉閥、空氣閥、第二旋轉閥、閘閥以及物料儲槽。吸料機係具有吸料口與送料口,該吸料機係自該吸料口將物料吸入並藉由該送料口送出該物料;第一旋轉閥係設置於該吸料機下方並具有第一出料口,用以自該送料口接收該物料並藉由旋轉而自該第一出料口送出該物料;空氣閥係與該第一旋轉閥連通,用以使外界空氣經該第一旋轉閥進入該吸料機,;第二旋轉閥係設置於該第一旋轉閥下方並具有第二出料口,用以自該第一出料口接收該物料並藉由旋轉而自該第二出料口送出該物料;閘閥係設置於該第二出料口以開啟或關閉該第二出料口;物料儲槽係設置於該閘閥下方以接收自該第二出料口送出之物料,同時接收自外 部輸入之正壓氣體,俾使該物料儲槽內在接收該物料時為正壓狀態。 The present disclosure provides a continuous feeding device comprising a suction machine, a first rotary valve, an air valve, a second rotary valve, a gate valve and a material storage tank. The suction machine has a suction port and a feeding port, the suction machine sucks the material from the suction port and sends the material through the feeding port; the first rotary valve is disposed under the suction machine and has the first a discharge port for receiving the material from the feed port and feeding the material from the first discharge port by rotation; the air valve is in communication with the first rotary valve for passing outside air through the first a rotary valve is inserted into the suction machine; a second rotary valve is disposed under the first rotary valve and has a second discharge port for receiving the material from the first discharge port and rotating from the first The second discharge port sends the material; the gate valve is disposed at the second discharge port to open or close the second discharge port; the material storage tank is disposed below the gate valve to receive the material sent from the second discharge port At the same time receiving from the outside The positive pressure gas is input to the positive pressure state when the material is received in the material storage tank.
相較於習知技術,本揭露係利用第一旋轉閥與第二旋轉閥的旋轉得以連續地將物料送至物料儲槽中,並利用空氣閥導入外界空氣以使該外界空氣朝吸料機的方向流動(用以補償吸料機因吸取物料所導致之氣體洩漏量),同時由外部輸入正壓氣體予該物料儲槽內,以避免物料儲槽內產生負壓,使該物料儲槽內在接收該物料時為正壓狀態,阻止物料儲槽下游之高溫氣體逆流,防止物料產生架橋、結塊之情形。 Compared with the prior art, the disclosure utilizes the rotation of the first rotary valve and the second rotary valve to continuously feed the material into the material storage tank, and introduces the outside air by the air valve to make the outside air toward the suction machine. The direction of flow (to compensate for the amount of gas leakage caused by the suction of the material), and the positive pressure gas is externally supplied to the material storage tank to avoid negative pressure in the material storage tank, so that the material storage tank When the material is received internally, it is in a positive pressure state, preventing the high-temperature gas flowing downstream of the material storage tank from flowing back, preventing the material from bridging and agglomerating.
以下藉由特定的具體實施例說明本揭露之實施方式,熟悉此技藝之人士可由本說明書所揭示之內容輕易地瞭解本揭露之其他優點及功效。 The embodiments of the present disclosure are described below by way of specific embodiments, and those skilled in the art can readily appreciate the other advantages and functions of the present disclosure.
須知,本說明書所附圖式所繪示之結構、比例、大小等,均僅用以配合說明書所揭示之內容,以供熟悉此技藝之人士之瞭解與閱讀,並非用以限定本揭露可實施之限定條件,故不具技術上之實質意義,任何結構之修飾、比例關係之改變或大小之調整,在不影響本創作所能產生之功效及所能達成之目的下,均應仍落在本創作所揭示之技術內容得能涵蓋之範圍內。同時,本說明書中所引用之如“第一”、“第二”、“上方”、“下方”等用語,亦僅為便於敘述之明瞭,而非用以限定本創作可實施之範圍,其相對關係之改變或調整,在無實質變更技術內容下,當亦視為本創 作可實施之範疇。 It is to be understood that the structure, the proportions, the size and the like of the present invention are only used to clarify the disclosure of the specification for the understanding and reading of those skilled in the art, and are not intended to limit the disclosure. The conditions are limited, so it is not technically meaningful. Any modification of the structure, change of the proportional relationship or adjustment of the size should remain in this book without affecting the effectiveness and the purpose of the creation. The technical content revealed by the creation can be covered. In the meantime, the terms "first", "second", "above" and "below" are used in this specification for convenience of description only, and are not intended to limit the scope of the present invention. The change or adjustment of the relative relationship, when there is no substantive change in the content of the technology, A range that can be implemented.
請參閱第1圖,其為本揭露之連續進料裝置之基本構件示意圖。本揭露之連續進料裝置1係主要包括吸料機10、第一旋轉閥11、空氣閥12、第二旋轉閥13、閘閥14以及物料儲槽15。 Please refer to FIG. 1 , which is a schematic diagram of the basic components of the continuous feeding device of the present disclosure. The continuous feeding device 1 of the present disclosure mainly includes a suction machine 10, a first rotary valve 11, an air valve 12, a second rotary valve 13, a gate valve 14, and a material storage tank 15.
吸料機10係具有吸料口101與送料口102,用以從吸料口101將物料吸入並藉由送料口102將物料送出。吸料機10通常為一種真空吸料機,連接有鼓風機103,且在吸料機10內部設有濾袋104,由鼓風機103提供一吸力,使吸料機10得以藉由該吸力將物料自吸料口101吸入並自送料口102送出至第一旋轉閥11,而濾袋104可設置於吸料口101與鼓風機103之間以避免物料被鼓風機103吸出。 The suction machine 10 has a suction port 101 and a feed port 102 for taking in material from the suction port 101 and feeding the material through the feed port 102. The suction machine 10 is generally a vacuum suction machine, and is connected with a blower 103, and a filter bag 104 is disposed inside the suction machine 10, and a suction force is provided by the air blower 103, so that the suction machine 10 can take the material by the suction force. The suction port 101 is sucked in and sent out from the feed port 102 to the first rotary valve 11, and the filter bag 104 can be disposed between the suction port 101 and the blower 103 to prevent the material from being sucked out by the blower 103.
第一旋轉閥11係設置於吸料機10之送料口102下方以接收物料,且第一旋轉閥11具有第一出料口111,而吸料機10由送料口102送出之物料進入第一旋轉閥11,並藉由第一旋轉閥11的旋轉而連續地將物料自該第一出料口111送出。第一旋轉閥11之詳細說明係於後續第2圖敘述之。 The first rotary valve 11 is disposed under the feeding port 102 of the suction machine 10 to receive the material, and the first rotary valve 11 has a first discharge port 111, and the material sent by the suction machine 10 from the feeding port 102 enters the first The valve 11 is rotated, and the material is continuously sent out from the first discharge port 111 by the rotation of the first rotary valve 11. The detailed description of the first rotary valve 11 is described in the following second drawing.
於第1圖所示之實施例中,連續進料裝置1可復包括設置於吸料機10與第一旋轉閥11之間的第一下料斗16a,第一下料斗16a可用以接收自送料口102送出之物料再將該物料送至第一旋轉閥11。 In the embodiment shown in Fig. 1, the continuous feeding device 1 may further include a first lower hopper 16a disposed between the suction machine 10 and the first rotary valve 11, and the first lower hopper 16a may be used to receive the self-feeding material. The material sent from the port 102 is then sent to the first rotary valve 11.
空氣閥12係與第一旋轉閥11連通,用以將外界空氣導入第一旋轉閥11以進入吸料機10,使得該外界空氣進 入第一旋轉閥11而朝吸料機10方向的方向流動。空氣閥12可例如為空氣電磁閥。 The air valve 12 is in communication with the first rotary valve 11 for introducing outside air into the first rotary valve 11 to enter the suction machine 10, so that the outside air enters The first rotary valve 11 is introduced and flows in the direction of the suction machine 10. The air valve 12 can be, for example, an air solenoid valve.
第二旋轉閥13係設置於第一旋轉閥11之第一出料口111下方,且第二旋轉閥13具有第二出料口131,第二旋轉閥13可用以將來自於該第一旋轉閥11所送出之物料連續地從該第二出料口131送出。第二旋轉閥13之詳細說明係於後續第2圖敘述之。 The second rotary valve 13 is disposed below the first discharge port 111 of the first rotary valve 11, and the second rotary valve 13 has a second discharge port 131, and the second rotary valve 13 can be used to receive the first rotation The material sent from the valve 11 is continuously sent out from the second discharge port 131. The detailed description of the second rotary valve 13 is described in the following second drawing.
於第1圖所示之實施例中,連續進料裝置1可復包括設置於吸料機10與第一旋轉閥11之間的第二下料斗16b,第二下料斗16b用以接收自第一出料口111送出之物料,並將該物料送至物料儲槽15。此外,空氣閥12可連接於第二下料斗16b,用以使外界空氣經由第二下料斗16b通過第一旋轉閥11進入吸料機10,以補償因吸料機10吸入該物料而產生朝吸料機10方向之氣體洩漏量。 In the embodiment shown in FIG. 1, the continuous feeding device 1 may further include a second lower hopper 16b disposed between the suction machine 10 and the first rotary valve 11, and the second lower hopper 16b is received from the first The material sent out from a discharge port 111 is sent to the material storage tank 15. In addition, the air valve 12 can be coupled to the second lower hopper 16b for allowing outside air to enter the suction machine 10 through the second lower hopper 16b through the first rotary valve 11 to compensate for the suction of the material by the suction machine 10. The amount of gas leakage in the direction of the suction machine 10.
閘閥14,或稱之為空氣閘閥14,係設置於第二出料口131以開啟或關閉第二出料口131。 The gate valve 14, or air curtain valve 14, is disposed at the second discharge port 131 to open or close the second discharge port 131.
物料儲槽15係設置於該閘閥14下方,以接收自該第二出料口131所連續送出之物料,同時接收自外部輸入之正壓氣體20,俾使該物料儲槽15內在接收該物料時為正壓狀態,其中,所謂正壓狀態係指物料儲槽15連接至反應器時,物料儲槽15內部的壓力大於或等於該反應器內部的壓力。 The material storage tank 15 is disposed under the gate valve 14 to receive the material continuously sent from the second discharge port 131, and receives the positive pressure gas 20 input from the outside, so that the material storage tank 15 receives the material. The time is a positive pressure state, wherein the so-called positive pressure state means that the pressure inside the material storage tank 15 is greater than or equal to the pressure inside the reactor when the material storage tank 15 is connected to the reactor.
請參閱第2圖,係為本揭露之第一及第二旋轉閥之剖面示意圖。於第2圖中,係以第一旋轉閥11作為實施方式 之說明,第一旋轉閥11可包括第一殼體112,設於第一殼體112內之第一轉子113、以及連接第一下料斗16a之第一進料口110,且第一轉子間隙114形成於第一殼體112與第一轉子113之間。 Please refer to FIG. 2 , which is a schematic cross-sectional view of the first and second rotary valves of the present disclosure. In the second figure, the first rotary valve 11 is taken as an embodiment. The first rotary valve 11 can include a first housing 112, a first rotor 113 disposed in the first housing 112, and a first inlet 110 connected to the first lower hopper 16a, and the first rotor gap 114 is formed between the first housing 112 and the first rotor 113.
來自於吸料機10之送料口102所送出之物料經第一下料斗16a自第一進料口110進入第一旋轉閥11,圖中所示之箭頭A方向即為物料方向,接著藉由第一轉子113的轉動(例如,朝箭頭方向逆時針轉動)而從第一出料口111送出。在第一轉子113轉動過程中,物料儲槽15中的氣體可能由於吸料機10的吸取物料而依序通過閘閥14、第二旋轉閥13、第二下料斗16b從第一轉子間隙114朝吸料機10的方向(箭頭B方向)洩漏,導致物料儲槽15內產生負壓,此負壓可能造成連接於物料儲槽15下游之反應器中的高溫氣體往物料儲槽15之方向逆流,而這樣的高溫逆流氣體會加熱物料儲槽15中的物料使物料產生水氣,再加上物料本身的特性為質量輕、密度小、安息角大及流動性差等因素,容易於物料儲槽15與其下游之反應器之間造成物料架橋、結塊或阻塞等現象,使得物料難以連續地進料至反應器之內。此時,連接於第二下料斗16b以與第一旋轉閥11連通之空氣閥12,可讓外界空氣經第一旋轉閥11進入吸料機,以補償因吸料機10之吸取物料而產生朝吸料機10方向之氣體洩漏量。 The material sent from the feed port 102 of the suction machine 10 enters the first rotary valve 11 from the first feed port 110 via the first lower hopper 16a, and the arrow A direction shown in the figure is the material direction, and then The rotation of the first rotor 113 (for example, counterclockwise rotation in the direction of the arrow) is sent from the first discharge port 111. During the rotation of the first rotor 113, the gas in the material storage tank 15 may sequentially pass through the gate valve 14, the second rotary valve 13, and the second lower hopper 16b from the first rotor gap 114 due to the suction material of the suction machine 10. The direction of the suction machine 10 (direction of arrow B) leaks, causing a negative pressure in the material storage tank 15, which may cause the high temperature gas in the reactor connected to the downstream of the material storage tank 15 to flow in the direction of the material storage tank 15. And such a high-temperature counter-flow gas will heat the material in the material storage tank 15 to generate moisture, and the characteristics of the material itself are light weight, low density, large angle of repose and poor fluidity, etc., and are easy to be used in the material storage tank. 15 causes bridging, agglomeration or blockage of materials between the reactors downstream thereof, making it difficult to continuously feed the materials into the reactor. At this time, the air valve 12 connected to the second lower hopper 16b and communicating with the first rotary valve 11 allows the outside air to enter the suction machine through the first rotary valve 11 to compensate for the suction of the material by the suction machine 10. The amount of gas leakage in the direction of the suction machine 10.
再者,第二旋轉閥13如同第一旋轉閥11之結構,可包括第二殼體、設於該第二殼體內之第二轉子、及連接該 第二下料斗之第二進料口,且第二轉子間隙形成於該第二轉子與該第二殼體之間,且其中,該物料自該第二進料口進入該第二旋轉閥並藉由該第二轉子的轉動而自第二出料口131送出至物料儲槽15。 Furthermore, the second rotary valve 13 is similar to the structure of the first rotary valve 11, and may include a second housing, a second rotor disposed in the second housing, and a connection a second feed port of the second lower hopper, and a second rotor gap is formed between the second rotor and the second housing, and wherein the material enters the second rotary valve from the second feed port and It is sent from the second discharge port 131 to the material storage tank 15 by the rotation of the second rotor.
請參閱第3圖,為本揭露之連續進料裝置之應用實施例。於本實施例中,物料儲槽15可連接至反應器19,而自物料儲槽15至反應器19之間依序設置有下料輸送機17與進料輸送機18,物料可自物料儲槽15依序藉由下料輸送機17與進料輸送機18而輸送至反應器19以進行裂解反應。 Please refer to FIG. 3, which is an application example of the continuous feeding device of the present disclosure. In this embodiment, the material storage tank 15 can be connected to the reactor 19, and the material feeding conveyor 17 and the feed conveyor 18 are sequentially disposed between the material storage tank 15 and the reactor 19, and the materials can be self-contained. The tank 15 is sequentially conveyed to the reactor 19 by the feed conveyor 17 and the feed conveyor 18 to carry out a cracking reaction.
此外,於本實施例中復可於物料儲槽15與反應器19之間設置壓力差檢測器152,以檢測物料儲槽15與反應器19之間的壓力差。由於反應器19內之高溫正壓氣體會朝物料儲槽15的方向逆流,因此,在本實施例中係將壓力差檢測器152設置於物料儲槽15與下料輸送機17之間,即可檢測反應器19與物料儲槽15之間的壓力差,但是此一設置方式僅係為實施方式之說明,並非用以限制本揭露。 Further, in the present embodiment, a pressure difference detector 152 is provided between the material storage tank 15 and the reactor 19 to detect a pressure difference between the material storage tank 15 and the reactor 19. Since the high-temperature positive pressure gas in the reactor 19 is reversed in the direction of the material storage tank 15, in the present embodiment, the pressure difference detector 152 is disposed between the material storage tank 15 and the discharge conveyor 17, that is, The pressure difference between the reactor 19 and the material storage tank 15 can be detected, but this arrangement is merely illustrative of the embodiments and is not intended to limit the disclosure.
再者,於本實施例中,連續進料裝置1可復包括有控制器153,於第3圖所示之控制器153為伺服馬達,控制器153可接收壓力差檢測器152所回饋之之檢測結果,以根據該檢測結果控制進入物料儲槽15之正壓氣體20的流量,俾使物料儲槽15內部的壓力大於或等於反應器19內部的壓力。另外,連續進料裝置1還可包括與控制器153電性連接之可調流量計(未圖式),控制器153可接收壓力 差檢測器152之檢測結果以產生控制命令,該可調流量計可檢測進入物料儲槽15之正壓氣體20的流量並依據控制器153之控制命令而調整進入物料儲槽15之正壓氣體20的流量,使得物料儲槽15內部的壓力大於或等於反應器19內部的壓力,以控制物料儲槽15與反應器19之間的壓力處於平衡狀態,藉此確保反應器19內的高溫正壓氣體不會經由進料輸送機18或下料輸送機17而進入物料儲槽15內。 Furthermore, in the present embodiment, the continuous feeding device 1 may further include a controller 153, the controller 153 shown in FIG. 3 is a servo motor, and the controller 153 may receive the feedback from the differential pressure detector 152. The result is detected to control the flow rate of the positive pressure gas 20 entering the material storage tank 15 according to the detection result, so that the pressure inside the material storage tank 15 is greater than or equal to the pressure inside the reactor 19. In addition, the continuous feeding device 1 may further include an adjustable flow meter (not shown) electrically connected to the controller 153, and the controller 153 can receive the pressure The detection result of the difference detector 152 is used to generate a control command, which can detect the flow rate of the positive pressure gas 20 entering the material storage tank 15 and adjust the positive pressure gas entering the material storage tank 15 according to the control command of the controller 153. The flow rate of 20 is such that the pressure inside the material storage tank 15 is greater than or equal to the pressure inside the reactor 19 to control the pressure between the material storage tank 15 and the reactor 19 to be in equilibrium, thereby ensuring high temperature in the reactor 19. The pressurized gas does not enter the material storage tank 15 via the feed conveyor 18 or the blank conveyor 17.
本揭露於實際實施時,係由鼓風機103提供吸力予吸料機10,以將物料從吸料機10之吸料口101吸入,並且從送料口102送出,經過第一下料斗16a使物料集中下料至第一旋轉閥11,藉由第一旋轉閥11的旋轉,使物料得以連續地下料而從第一出料口111送出物料,再經由第二下料斗16b入第二旋轉閥13。 In the actual implementation, the suction is provided by the blower 103 to the suction machine 10 to suck the material from the suction port 101 of the suction machine 10, and is sent out from the feed port 102, and the material is concentrated through the first lower hopper 16a. The second rotary valve 11 is fed to the first rotary valve 11, and the material is continuously discharged from the first discharge port 111 by the rotation of the first rotary valve 11, and then introduced into the second rotary valve 13 via the second lower hopper 16b.
在第一旋轉閥11旋轉以連續下料的同時,可藉由空氣閥12導入外界空氣,使該外界氣體經第二下料斗16b通過第一旋轉閥11的第一轉子間隙而朝吸料機10的方向流動,以補償第一旋轉閥11因旋轉而產生朝吸料機10方向之氣體洩漏量,避免由於吸料機10所提供的吸力而導致物料儲槽15內形成負壓。 While the first rotary valve 11 is rotated to continuously feed, the outside air can be introduced through the air valve 12, and the external air passes through the second lower hopper 16b through the first rotor gap of the first rotary valve 11 toward the suction machine. The direction of 10 flows to compensate for the amount of gas leakage from the first rotary valve 11 in the direction of the suction machine 10 due to the rotation, thereby avoiding the formation of a negative pressure in the material storage tank 15 due to the suction force provided by the suction machine 10.
物料進入第二旋轉閥13之後,藉由第二旋轉閥13以連續地下料,使物料連續地從第二旋轉閥13之第二出料口131連續地送出以進入物料儲槽15。 After the material enters the second rotary valve 13, the material is continuously continuously discharged from the second discharge port 131 of the second rotary valve 13 to enter the material storage tank 15 by the second rotary valve 13 in a continuous underground material.
需說明的是,當處於連續下料的運作狀態時,閘閥14 是處於全開啟狀態,以避免影響第二旋轉閥13連續下料。另外,為了避免反應器19之高溫正壓氣體回流至物料儲槽15造成物料的架橋或結塊,可輸入正壓氣體20至物料儲槽15內以平衡反應器19與物料儲槽15之間的壓力,其中,該正壓氣體可為裂解氣、惰性氣體或空氣,但是並不限於此。 It should be noted that when in the continuous operation state, the gate valve 14 It is in the fully open state to avoid affecting the continuous cutting of the second rotary valve 13. In addition, in order to avoid the bridging or agglomeration of the material caused by the high temperature positive pressure gas of the reactor 19 flowing back to the material storage tank 15, a positive pressure gas 20 may be input into the material storage tank 15 to balance between the reactor 19 and the material storage tank 15. The pressure, wherein the positive pressure gas may be a cracking gas, an inert gas or air, but is not limited thereto.
當物料儲槽15需補充物料(例如木屑)時,首先啟動第一旋轉閥11、第二旋轉閥13及閘閥14,同時調整所輸入之正壓氣體20(裂解氣、惰性氣體或空氣)的壓力,以控制物料儲槽15內之壓力與反應器19之壓力平衡。吸料機10的鼓風機103與空氣閥12是採同步啟動(ON)或關閉(OFF)。當啟動鼓風機103以補充物料給物料儲槽15時,在第一旋轉閥11下游,即物料儲槽15內會形成局部負壓,而空氣閥12之啟動可讓外界空氣進入吸料機10以避免物料儲槽15內形成局部負壓。藉此,可避免此局部負壓造成連接於物料儲槽下游之反應器產生往物料儲槽15方向之高溫逆流氣體,使得反應器因無進料而無法操作。 When the material storage tank 15 needs to replenish materials (for example, wood chips), firstly, the first rotary valve 11, the second rotary valve 13 and the gate valve 14 are activated, and the input positive pressure gas 20 (cracking gas, inert gas or air) is adjusted. The pressure is controlled to balance the pressure in the material storage tank 15 with the pressure of the reactor 19. The blower 103 of the suction machine 10 and the air valve 12 are synchronized (ON) or closed (OFF). When the blower 103 is activated to replenish the material to the material storage tank 15, a partial negative pressure is formed in the material storage tank 15 downstream of the first rotary valve 11, and the activation of the air valve 12 allows the outside air to enter the suction machine 10. A partial negative pressure is prevented from forming in the material storage tank 15. Thereby, the partial negative pressure can be prevented from causing the reactor connected to the downstream of the material storage tank to generate a high-temperature countercurrent gas in the direction of the material storage tank 15, so that the reactor cannot be operated due to no feeding.
綜上所述,本揭露之連續進料裝置基本包括吸料機、第一和第二旋轉閥、介於該第一和第二旋轉閥之間的空氣閥、設於該第一和第二旋轉閥下游之閘閥及物料儲槽。該空氣閥用以導入外界氣體以使該外界氣體經該第一旋轉閥進入該吸料機,以避免物料儲槽內形成局部負壓;同時該物料儲槽接收自外部輸入之正壓氣體,以維持該物料儲槽和與其連接之反應器之間的壓力平衡,俾使該物料儲槽內 部的壓力大於或等於該反應器內部的壓力。因此,藉由本揭露之連續進料裝置之運作,物料不會產生架橋或結塊等現象,故能連續進料至下游之反應器中。 In summary, the continuous feeding device of the present disclosure basically comprises a suction machine, first and second rotary valves, an air valve interposed between the first and second rotary valves, and is disposed at the first and second Gate valve and material storage tank downstream of the rotary valve. The air valve is configured to introduce an external gas to allow the outside air to enter the suction machine through the first rotary valve to avoid forming a partial negative pressure in the material storage tank; and the material storage tank receives the positive pressure gas input from the outside, In order to maintain the pressure balance between the material storage tank and the reactor connected thereto, the material storage tank is The pressure in the section is greater than or equal to the pressure inside the reactor. Therefore, with the operation of the continuous feeding device of the present disclosure, the material does not cause bridging or agglomeration, and thus can be continuously fed into the downstream reactor.
上述實施例係用以例示性說明本揭露之原理及其功效,而非用於限制本揭露。任何熟習此項技藝之人士均可在不違背本揭露之精神及範疇下,對上述實施例進行修改。因此本揭露之權利保護範圍,應如後述之申請專利範圍所列。 The above embodiments are intended to illustrate the principles of the disclosure and its functions, and are not intended to limit the disclosure. Any person skilled in the art can modify the above embodiments without departing from the spirit and scope of the disclosure. Therefore, the scope of protection of the present disclosure should be as set forth in the scope of the patent application described later.
1‧‧‧連續進料裝置 1‧‧‧Continuous feeding device
10‧‧‧吸料機 10‧‧‧ suction machine
101‧‧‧吸料口 101‧‧‧ suction port
102‧‧‧送料口 102‧‧‧ Feeding port
103‧‧‧鼓風機 103‧‧‧Blowers
104‧‧‧濾袋 104‧‧‧ filter bag
11‧‧‧第一旋轉閥 11‧‧‧First rotary valve
110‧‧‧第一進料口 110‧‧‧First inlet
111‧‧‧第一出料口 111‧‧‧First discharge opening
112‧‧‧第一殼體 112‧‧‧First housing
113‧‧‧第一轉子 113‧‧‧First rotor
114‧‧‧第一轉子間隙 114‧‧‧First rotor clearance
12‧‧‧空氣閥 12‧‧‧Air valve
13‧‧‧第二旋轉閥 13‧‧‧Second rotary valve
131‧‧‧第二出料口 131‧‧‧Second outlet
14‧‧‧閘閥 14‧‧‧ gate valve
15‧‧‧物料儲槽 15‧‧‧ material storage tank
152‧‧‧壓力差檢測器 152‧‧‧Pressure difference detector
153‧‧‧控制器 153‧‧‧ Controller
16a‧‧‧第一下料斗 16a‧‧‧First hopper
16b‧‧‧第二下料斗 16b‧‧‧Second hopper
17‧‧‧下料輸送機 17‧‧‧Unloading conveyor
18‧‧‧進料輸送機 18‧‧‧feed conveyor
19‧‧‧反應器 19‧‧‧Reactor
20‧‧‧正壓氣體 20‧‧‧ positive pressure gas
第1圖為本揭露之連續進料裝置之基本構件示意圖;第2圖係為本揭露之連續進料裝置之第一及第二旋轉閥之剖面示意圖;以及第3圖為本揭露之連續進料裝置之應用實施例。 1 is a schematic view of the basic components of the continuous feeding device of the present disclosure; FIG. 2 is a schematic cross-sectional view of the first and second rotary valves of the continuous feeding device of the present disclosure; and FIG. 3 is a continuous advance of the disclosure Application examples of the material device.
1‧‧‧連續進料裝置 1‧‧‧Continuous feeding device
10‧‧‧吸料機 10‧‧‧ suction machine
101‧‧‧吸料口 101‧‧‧ suction port
102‧‧‧送料口 102‧‧‧ Feeding port
103‧‧‧鼓風機 103‧‧‧Blowers
104‧‧‧濾袋 104‧‧‧ filter bag
11‧‧‧第一旋轉閥 11‧‧‧First rotary valve
111‧‧‧第一出料口 111‧‧‧First discharge opening
12‧‧‧空氣閥 12‧‧‧Air valve
13‧‧‧第二旋轉閥 13‧‧‧Second rotary valve
131‧‧‧第二出料口 131‧‧‧Second outlet
14‧‧‧閘閥 14‧‧‧ gate valve
15‧‧‧物料儲槽 15‧‧‧ material storage tank
16a‧‧‧第一下料斗 16a‧‧‧First hopper
16b‧‧‧第二下料斗 16b‧‧‧Second hopper
20‧‧‧正壓氣體 20‧‧‧ positive pressure gas
Claims (9)
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CN201210401677.7A CN103625929B (en) | 2012-08-22 | 2012-10-22 | Continuous feeding device |
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TW101130383A TWI570230B (en) | 2012-08-22 | 2012-08-22 | Continuous feeding device |
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CN106218988B (en) * | 2016-09-14 | 2019-05-28 | 钟振东 | A kind of material of counting grain machine is rejected and buffer storage |
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TW496765B (en) * | 2001-11-13 | 2002-08-01 | Ind Tech Res Inst | Powder slaking system and method |
TW201105558A (en) * | 2009-08-06 | 2011-02-16 | Karl-Heinz Tetzlaff | Screw conveyor for feeding biomass into a pressure container |
CN102041102A (en) * | 2010-11-01 | 2011-05-04 | 广州迪森热能技术股份有限公司 | Air curtain feeding device and biomass gasification reaction system using same |
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JPH01162627A (en) * | 1987-12-18 | 1989-06-27 | Showa Eng Kk | Quantative supplier of powder |
BE1011332A3 (en) * | 1997-08-20 | 1999-07-06 | Solvay | Unloading device for reactor polymerization fluidized bed. |
CN2366388Y (en) * | 1999-03-31 | 2000-03-01 | 中国石化齐鲁石油化工公司 | Rotary valve type material filling means with guiding plate |
CN201545512U (en) * | 2009-06-10 | 2010-08-11 | 陈毅 | Limestone continuous conveying system |
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TW496765B (en) * | 2001-11-13 | 2002-08-01 | Ind Tech Res Inst | Powder slaking system and method |
TW201105558A (en) * | 2009-08-06 | 2011-02-16 | Karl-Heinz Tetzlaff | Screw conveyor for feeding biomass into a pressure container |
CN102041102A (en) * | 2010-11-01 | 2011-05-04 | 广州迪森热能技术股份有限公司 | Air curtain feeding device and biomass gasification reaction system using same |
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