TWI485356B - Soot blower in passage and dust recovery apparatus - Google Patents
Soot blower in passage and dust recovery apparatus Download PDFInfo
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Description
本發明是有關流路內除煤裝置及塵埃回收裝置。The invention relates to a coal removal device and a dust recovery device in a flow path.
例如為除去包含從火力發電廠所排出塵埃之廢氣中的氮氧化物(NOx),使用以氨(NH3 )為還原劑的選擇性接觸還原反應的廢氣脫硝法。該選擇性接觸還原反應是將NH3 注入廢氣中所包含的NOx並藉脫硝觸媒還原。具體而言,對排氣管或連結排氣管的流路殼體等廢氣流動的流路,藉配置著格子狀的脫硝觸媒進行脫硝。For example, in order to remove nitrogen oxides (NOx) in exhaust gas containing dust discharged from a thermal power plant, an exhaust gas denitration method using a selective contact reduction reaction using ammonia (NH 3 ) as a reducing agent is used. The selective contact reduction reaction is to inject NH 3 into the NOx contained in the exhaust gas and reduce it by the denitrification catalyst. Specifically, the flow path through which the exhaust gas flows through the exhaust pipe or the flow path casing that connects the exhaust pipe is denitrated by a lattice-shaped denitration catalyst.
以煤炭作為燃料的火力發電廠的廢氣,由於含多量的未燃量的煤等的塵埃,會因此而導致脫硝觸媒的堵塞。為解決此一問題,例如藉著揭示在專利文獻1的除煤裝置(吹灰器),可得知沿著廢氣的流動方向吹除煤的技術。The exhaust gas of a thermal power plant using coal as a fuel causes clogging of the denitration catalyst due to dust containing a large amount of unburned coal. In order to solve such a problem, for example, by disclosing the coal removing device (soot blower) of Patent Document 1, it is known that the coal is blown off in the flow direction of the exhaust gas.
[專利文獻1]日本特開昭62-69015號公報[Patent Document 1] Japanese Laid-Open Patent Publication No. 62-69015
但是,根據煤炭的性質及鍋爐的運轉條件等,在廢氣中會形成比脫硝觸媒的氣體細流路大(粒徑為數mm至十 數mm)的煤塊體(以下稱爆米花狀灰),該爆米花塵堵塞在脫硝觸媒,會有使得在脫硝觸媒形成格子狀的細流路封閉的問題。與粒子狀的煤不同,且由於爆米花狀灰比脫硝觸媒的氣體流路大,因此在以往的除煤裝置無法沿著廢氣的流動方向吹除,因此為將此除去,必須停止設備而以人力來清掃。However, depending on the nature of the coal and the operating conditions of the boiler, a finer flow path than the denitration catalyst is formed in the exhaust gas (the particle size is several mm to ten A coal block of a few mm) (hereinafter referred to as popcorn-like ash), which is clogged with a denitration catalyst, and has a problem that the fine flow path in which the denitration catalyst is formed in a lattice shape is closed. Unlike the particulate coal, since the popcorn-like ash has a larger gas flow path than the denitration catalyst, the conventional coal removal device cannot be blown along the flow direction of the exhaust gas. Therefore, in order to remove this, it is necessary to stop the device. And clean it with manpower.
本發明是考慮以上的狀況所研創而成,其目的是提供即使流體流通於流路內的狀態,即使如爆米花塵埃的吹除之除去困難的塵埃仍可除去的流路內除煤裝置及塵埃回收裝置。The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a fluid removal device in a flow path which can be removed even if dust is difficult to be removed by blowing of popcorn dust even if a fluid flows through the flow path. Dust recovery unit.
為解決上述課題,本發明提供以下的手段。In order to solve the above problems, the present invention provides the following means.
本發明的流路內除煤裝置是設置在流體流動的流路殼體,使上述流體一邊流通於上述流路殼體一邊除去包含於上述流體而堆積在上述流路殼體內的塵埃用的流路內除煤裝置,其特徵為,具備:使前端開口與除去塵埃的除去部相對,從上述流路殼體向外側延伸的同時,以基端側和吸引塵埃用的吸引手段連接的吸入管,及使上述吸入管的開口在流路內進退的驅動手段。The in-stream coal removing device of the present invention is a flow path casing that is provided in a fluid flow, and that the fluid flows through the flow path casing while removing the dust contained in the flow path casing and stored in the flow path casing. The in-street coal removal device is characterized in that the front end opening is opposed to the dust removing portion, and the suction pipe is connected to the base end side and the suction means for attracting dust while extending outward from the flow path casing. And a driving means for advancing and retracting the opening of the suction pipe in the flow path.
根據上述構成,由於是透過吸入管吸引除去塵埃的構成,所以可防止塵埃堆積在除去部。According to the above configuration, since the dust is sucked and removed through the suction pipe, dust can be prevented from accumulating in the removed portion.
上述流路內除煤裝置中,上述吸入管以具備:有和上述除去部相對的上述開口的前端管,及基端與上述吸引手 段連接,前端插入上述前端管內部的基端管,上述驅動手段可使上述前端管進退為佳。In the above-described fluid removal device, the suction pipe includes a front end pipe having the opening facing the removal portion, and a base end and the suction hand The segment is connected, and the front end is inserted into the base end tube inside the front end tube, and the driving means can preferably advance and retreat the front end tube.
根據上述構成,分割成使吸入管進退的前端管與所固定的基端管,藉著將基端管插入前端管內部組合,減小吸入管的占有面積,可使流路內除煤裝置小型化。According to the above configuration, the front end pipe for advancing and retracting the suction pipe and the fixed base pipe are combined, and the base pipe is inserted into the front end pipe to reduce the occupied area of the suction pipe, so that the coal removal device in the flow path can be made small. Chemical.
上述流路內除煤裝置中,上述驅動手段也可透過沿著上述前端管及上述基端管所設置的移動用連動軸使上述前端管進退的構成。In the above-described flow path internal coal removing device, the driving means may transmit the front end pipe forward and backward along the moving interlocking shaft provided in the front end pipe and the base end pipe.
根據上述構成,由於將包含前端管所吸引的塵埃的氣體流動的系統與包含驅動手段的系統分開配置,所以可防止因氣體的熱導致驅動手段的損傷。According to the above configuration, since the system that flows the gas including the dust sucked by the tip end pipe is disposed separately from the system including the driving means, damage of the driving means due to the heat of the gas can be prevented.
上述流路內除煤裝置中,在上述流路殼體內的上述除去部設置捕捉塵埃的網,且上述吸入管的上述開口是以和上述網相對設置為佳。In the above-described fluid removal device for a flow path, a dust-collecting net is provided in the removal portion in the flow path casing, and the opening of the suction pipe is preferably disposed opposite to the mesh.
根據上述構成,可防止較網眼大的塵埃影響到網的後流側。According to the above configuration, it is possible to prevent dust larger than the mesh from affecting the downstream side of the net.
上述流路內除煤裝置中,以具備使上述網所捕捉的塵埃粉碎的粉碎手段為佳。In the above-described fluid removal device for a flow path, it is preferable to include a pulverizing means for pulverizing the dust captured by the mesh.
根據上述構成,藉塵埃的粉碎,更為容易吸引塵埃,並可粉碎較吸入管的開口大塵埃,吸引更大的塵埃。According to the above configuration, it is easier to attract dust by the pulverization of the dust, and it is possible to pulverize the dust larger than the opening of the suction pipe and attract more dust.
上述流路內除煤裝置中,上述除去部以具備噴吹塵埃除去用氣體的噴吹手段為佳。In the above-described fluid removal device for a flow path, the removal unit is preferably provided with a blowing means for blowing a gas for removing dust.
根據上述構成,將塵埃除去用氣體朝著塵埃噴吹使塵埃浮游,可提升塵埃的吸引效率。According to the above configuration, the dust removing gas is blown toward the dust to float the dust, and the dust suction efficiency can be improved.
上述流路內除煤裝置中,上述除去部為複數的細流路沿著上述流路殼體延伸的格子狀的脫硝觸媒,上述吸入管以設置在上述脫硝觸媒的上游側為佳。In the above-described flow path internal coal removing device, the removing portion is a lattice-shaped denitration catalyst in which a plurality of thin flow paths extend along the flow path casing, and the suction pipe is preferably provided on the upstream side of the denitration catalyst. .
上述流路內除煤裝置是以相對於上述吸入管分開設置構成上述驅動手段的馬達為佳。It is preferable that the coal removing device in the flow path is a motor in which the driving means is separately provided with respect to the suction pipe.
根據上述構成,可防止因包含塵埃的氣體的熱導致馬達的損傷。According to the above configuration, damage to the motor due to heat of the gas containing dust can be prevented.
又,本發明提供塵埃回收裝置,其特徵為,具備:上述其中之一的流路內除煤裝置;連接於上述吸入管的基端側的塵埃配送管;捕捉上述塵埃配送管的塵埃的濾器;及上述吸引手段。Moreover, the present invention provides a dust collecting device comprising: one of the above-described flow path coal removing devices; a dust distributing pipe connected to a proximal end side of the suction pipe; and a filter for capturing dust of the dust distributing pipe And the above means of attraction.
根據上述構成,藉著在排出塵埃用的塵埃配送管設置濾器,可捕捉流路內除煤裝置所吸引的塵埃。According to the above configuration, by providing the filter in the dust distribution pipe for discharging dust, it is possible to capture the dust attracted by the coal removal device in the flow path.
上述塵埃回收裝置中,以上述塵埃配送管上,在上述濾器的上游側具備導入冷卻氣體的手段為佳。In the dust collecting device, it is preferable that the dust collecting pipe has a means for introducing a cooling gas on the upstream side of the filter.
根據上述構成,藉導入冷卻空氣使流體的溫度下降,可防止高溫的流體影響到濾器。According to the above configuration, by introducing the cooling air to lower the temperature of the fluid, it is possible to prevent the high-temperature fluid from affecting the filter.
根據本發明,由於是透過吸入管吸引除去塵埃的構成,因此可防止塵埃堆積在除去部。According to the present invention, since the dust is sucked and removed through the suction pipe, dust can be prevented from accumulating in the removed portion.
以下,參閱圖示針對本發明的實施形態詳細說明。Hereinafter, the embodiments of the present invention will be described in detail with reference to the drawings.
如第1圖表示,本實施形態的塵埃回收裝置1是例如設置在連結於火力發電廠燃燒煤炭的鍋爐2的排氣管2a的流路殼體4。塵埃回收裝置1是將附著於安裝在流路殼體4內部的脫硝觸媒3(除去部)的煤等的塵埃,尤其是稱爆米花狀灰的粒徑大的煤塊體,一邊使流體流通於流路殼體4一邊除去之用。As shown in Fig. 1, the dust collecting device 1 of the present embodiment is, for example, a flow path case 4 provided in an exhaust pipe 2a of a boiler 2 that is connected to a coal-fired power plant to burn coal. The dust collecting device 1 is a dust such as coal that adheres to the denitration catalyst 3 (removing portion) attached to the inside of the flow path casing 4, and particularly a coal block having a large particle diameter of popcorn-like ash. The fluid is circulated through the flow path casing 4 for removal.
脫硝觸媒3是在流體的廢氣流動的流路殼體4內部至少安裝一個,與在該流路殼體4流動的廢氣接觸來降低廢氣中所含的氮氧化物(NOx)。例如脫硝觸媒3是以預定的間隔配置使廢氣依序通過。The denitration catalyst 3 is installed at least in the inside of the flow path casing 4 through which the exhaust gas of the fluid flows, and is in contact with the exhaust gas flowing through the flow path casing 4 to reduce nitrogen oxides (NOx) contained in the exhaust gas. For example, the denitration catalyst 3 is disposed at a predetermined interval to sequentially pass the exhaust gas.
如第2圖表示,與脫硝觸媒3的廢氣流動方向F成正交的剖面形狀為矩形形狀,流路殼體4則是依據脫硝觸媒3的形狀形成的形狀。脫硝觸媒3在流動方向具有預定的厚度。在脫硝觸媒3形成有棋盤格狀的沿著流動方向F的複數細流路3a。脫硝觸媒3從流動方向F顯示成格子狀。As shown in FIG. 2, the cross-sectional shape orthogonal to the flow direction F of the exhaust gas of the denitration catalyst 3 is a rectangular shape, and the flow path case 4 is formed in accordance with the shape of the denitration catalyst 3. The denitration catalyst 3 has a predetermined thickness in the flow direction. The denitration catalyst 3 is formed with a plurality of thin flow paths 3a in a checkerboard shape along the flow direction F. The denitration catalyst 3 is displayed in a lattice shape from the flow direction F.
脫硝觸媒3的流動方向一端側及另一端側是成平面(以下,稱端面3b),複數細流路3a是延伸連接著該端面彼此。脫硝觸媒3安裝使得脫硝觸媒3的端面3b與流路殼體4的外壁4a成正交。One end side and the other end side in the flow direction of the denitration catalyst 3 are flat surfaces (hereinafter referred to as end surface 3b), and the plurality of thin flow paths 3a are extended and connected to the end faces. The denitration catalyst 3 is installed such that the end face 3b of the denitration catalyst 3 is orthogonal to the outer wall 4a of the flow path casing 4.
如第1圖表示,塵埃回收裝置1,具有:固定在流路殼體4的外壁4a,相對於一個脫硝觸媒3至少設置一個流路內除煤裝置6,及排出流路內除煤裝置6所除去的塵埃的塵埃處理部5。As shown in Fig. 1, the dust recovery device 1 has an outer wall 4a fixed to the flow path casing 4, at least one flow path inner coal removing device 6 for one denitration catalyst 3, and coal removal in the discharge flow path. The dust processing unit 5 of the dust removed by the device 6.
塵埃處理部5,具有:配送含流路內除煤裝置6所除去塵埃的氣體(以下,稱氣體)的塵埃配送管7;補充氣體所含塵埃的袋式濾器8;及透過塵埃配送管7在流路內除煤裝置6產生吸引力的作為吸引手段的風扇9。The dust processing unit 5 includes a dust distribution pipe 7 that supplies a gas (hereinafter referred to as a gas) containing dust removed from the coal removal device 6 in the flow path, a bag filter 8 that replenishes the dust contained in the gas, and a dust transmission pipe 7 that passes through the dust distribution pipe 7 In the flow path, the coal removing device 6 generates a suction fan 9 as an attraction means.
塵埃處理部5是在塵埃回收裝置1至少設置一個,構成可處理複數流路內除煤裝置6所吸引的塵埃。The dust processing unit 5 is provided at least in the dust collecting device 1, and constitutes dust that can be sucked by the coal removing device 6 in the plurality of flow paths.
流路內除煤裝置6是利用風扇9所產生的負壓,吸引安裝在流路殼體4內部之脫硝觸媒3的端面3b上的塵埃的裝置。對於流路內除煤裝置6的詳細構造是如後述。The in-stream coal removing device 6 is a device that sucks dust attached to the end surface 3b of the denitration catalyst 3 inside the flow path casing 4 by the negative pressure generated by the fan 9. The detailed structure of the in-stream coal removing device 6 will be described later.
接著,針對塵埃處理部5說明。塵埃處理部5是相對於複數流路內除煤裝置6設置一個,選擇風扇9產生的吸引力作用於其中之一的流路內除煤裝置6。Next, it is explained to the dust processing unit 5. The dust processing unit 5 is provided in one of the plurality of coal removing devices 6 in the plurality of flow paths, and selects one of the suction mechanisms generated by the fan 9 to act on one of the flow path removing devices 6 .
塵埃配送管7是連接流路內除煤裝置6與風扇9的配管。以下的說明是以塵埃配送管7的流路內除煤裝置6側為上游側,並以風扇9側為下游側來說明。從上游側流入風扇9的氣體是經由風扇9送至煙道。The dust distribution pipe 7 is a pipe that connects the coal removing device 6 and the fan 9 in the flow path. In the following description, the side of the coal removal device 6 in the flow path of the dust distribution pipe 7 is the upstream side, and the fan 9 side is the downstream side. The gas flowing into the fan 9 from the upstream side is sent to the flue via the fan 9.
在塵埃配送管7上設有補充流動於塵埃配送管7的塵埃用的袋式濾器8。袋式濾器8是例如使用不織布作為濾材,採用使含於塵埃配送管7流動的塵埃堆積在不織布表面的濾器。將袋式濾器8所補充的塵埃送至灰處理設備。A bag filter 8 for replenishing dust flowing through the dust distribution pipe 7 is provided in the dust distribution pipe 7. The bag filter 8 is, for example, a filter that deposits dust contained in the dust distribution pipe 7 on the surface of the nonwoven fabric by using a nonwoven fabric as a filter material. The dust replenished by the bag filter 8 is sent to the ash processing equipment.
袋式濾器8的上游側設有溫度送訊器11,測量導入袋式濾器8的氣體溫度。溫度送訊器11是與溫度控制裝置12連接。在溫度送訊器11的上游側設有可導入作為冷卻氣體的空氣的大氣導入閥13。大氣導入閥13是與溫度 控制裝置12連接。A temperature transmitter 11 is provided on the upstream side of the bag filter 8, and the temperature of the gas introduced into the bag filter 8 is measured. The temperature transmitter 11 is connected to the temperature control device 12. An air introduction valve 13 through which air as a cooling gas can be introduced is provided on the upstream side of the temperature transmitter 11. Atmospheric introduction valve 13 is with temperature The control device 12 is connected.
溫度控制裝置12在當溫度送訊器11所測量的氣體溫度超過預定的溫度(例如200℃)的場合,使大氣導入閥13呈開啟狀態,可藉此將作為冷卻氣體的空氣導入塵埃配送管7來降低氣體的溫度。When the temperature of the gas measured by the temperature transmitter 11 exceeds a predetermined temperature (for example, 200 ° C), the temperature control device 12 causes the air introduction valve 13 to be in an open state, whereby the air as the cooling gas can be introduced into the dust distribution pipe. 7 to lower the temperature of the gas.
在大氣導入閥13的上游側設有測量塵埃配送管7內的壓力的壓力送訊器14。壓力送訊器14是與壓力控制裝置15連接。並且袋式濾器8的下游側,在風扇9的上游側設有吸引力控制閥16。吸引力控制閥16是與壓力控制裝置15連接。A pressure transmitter 14 that measures the pressure in the dust distribution pipe 7 is provided on the upstream side of the air introduction valve 13. The pressure transmitter 14 is connected to the pressure control device 15. Further, on the downstream side of the bag filter 8, an attraction control valve 16 is provided on the upstream side of the fan 9. The attraction control valve 16 is connected to the pressure control device 15.
設定壓力控制裝置15以調整吸引力控制閥16,使壓力送訊器14所測量的氣體壓力形成預定的壓力。The pressure control device 15 is set to adjust the suction force control valve 16 so that the gas pressure measured by the pressure transmitter 14 forms a predetermined pressure.
壓力送訊器14上游側的塵埃配送管7被分支成複數的分支路7a,分別被連接在流路內除煤裝置6。在各分支路7a設有轉換閥17。轉換閥17是藉未圖示的控制裝置來開關的閥,開啟狀態中使風扇9的吸引力產生於流路內除煤裝置6,並在關閉狀態截斷風扇9的吸引力。The dust distribution pipe 7 on the upstream side of the pressure transmitter 14 is branched into a plurality of branch paths 7a, and is connected to the coal removal device 6 in the flow path. A switching valve 17 is provided in each branch path 7a. The switching valve 17 is a valve that is opened and closed by a control device (not shown). In the open state, the suction force of the fan 9 is generated in the flow path in the coal removing device 6, and the suction force of the fan 9 is cut off in the closed state.
接著,針對流路內除煤裝置6的詳細構造說明。Next, the detailed structure of the in-stream coal removing device 6 will be described.
如第3圖及第4圖表示,流路內除煤裝置6,具有:以具備插入流路殼體4的前端管的吹管21,與脫硝觸媒3相對使前端開口,並從流路殼體4向外側延伸的吸入管20;及配置在流路殼體4的外部,收容吸入管20一部份的外罩22;使吹管21進退的驅動機構23(驅動手段)為主要構成元件。外罩22是成角筒形狀。並在外罩22的側 面設有收容控制基板等的端子箱29。As shown in Fig. 3 and Fig. 4, the in-stream coal removing device 6 has a blow pipe 21 having a front end pipe inserted into the flow path casing 4, and the front end opening is opened to the denitration catalyst 3, and the flow path is opened from the flow path. The suction pipe 20 that extends outward of the casing 4; and the outer casing 22 that is disposed outside the flow path casing 4 to accommodate a part of the suction pipe 20; and the drive mechanism 23 (driving means) that advances and retracts the blow pipe 21 are main constituent elements. The outer cover 22 is in the shape of an angled cylinder. And on the side of the outer cover 22 A terminal box 29 for accommodating a control board or the like is provided on the surface.
流路內除煤裝置6是透過牆盒24安裝在流路殼體4的外壁4a。並且,安裝流路內除煤裝置6使吹管21的長方向(以下,僅稱為長方向)沿著脫硝觸媒3的端面3b。The in-stream coal removing device 6 is attached to the outer wall 4a of the flow path casing 4 through the wall box 24. Further, the in-stream coal removing device 6 is installed such that the longitudinal direction of the blow pipe 21 (hereinafter, simply referred to as the long direction) is along the end surface 3b of the denitration catalyst 3.
吸入管20具有吹管21與嵌入吹管21的饋送管25(基端管)。饋送管25是在基端側,即長方向使得和吹管21相反的一側透過塵埃配送管7與風扇9(參閱第1圖)連接。饋送管25為基端側被懸臂狀支撐在外罩22的圓管形狀的構件,前端側被插入於圓管形狀的吹管21的內部。The suction pipe 20 has a blow pipe 21 and a feed pipe 25 (base pipe) embedded in the blow pipe 21. The feed pipe 25 is connected to the fan 9 (see Fig. 1) through the dust distribution pipe 7 on the base end side, i.e., the side opposite to the blow pipe 21 in the longitudinal direction. The feed pipe 25 is a member having a circular tube shape in which the base end side is supported in a cantilever shape on the outer cover 22, and the front end side is inserted into the inside of the circular tube-shaped blow pipe 21.
吹管21是被嵌入於饋送管25的前端側,藉著驅動機構23可朝長方向自由進退的圓管形狀的構件。吹管21是由沿著長方向,與饋送管25組合的吹管主體26,及設置在吹管主體26前端側的吸入管部27所構成。又,吹管21使得包含吸入管部27的前端側突出於外罩22的外部,並貫穿牆盒24,插入於流路殼體4的內部。The blow pipe 21 is a member having a circular tube shape that is fitted to the front end side of the feed pipe 25 and is movable forward and backward in the longitudinal direction by the drive mechanism 23. The blow pipe 21 is composed of a blow pipe main body 26 that is combined with the feed pipe 25 along the longitudinal direction, and a suction pipe portion 27 that is provided at the front end side of the blow pipe main body 26. Moreover, the blow pipe 21 protrudes from the front end side of the outer casing 22 including the suction pipe portion 27, and penetrates the wall case 24 and is inserted into the inside of the flow path casing 4.
吹管主體26是使前端沿著流路殼體4的流動方向F的方向,朝向脫硝觸媒3的方向彎曲,並在彎曲的前端部連接著吸入管部27。The blow pipe main body 26 is bent in the direction of the flow direction F of the flow path case 4 toward the denitration catalyst 3, and the suction pipe portion 27 is connected to the curved front end portion.
吸入管部27是形成與吹管主體26相同的圓管形狀,使其長方向與吹管主體26的長方向正交,並形成與流路殼體4的流動方向F正交。亦即,吸入管部27被形成沿著脫硝觸媒3的端面3b。The suction pipe portion 27 has a circular pipe shape similar to that of the blow pipe main body 26, and has a longitudinal direction orthogonal to the longitudinal direction of the blow pipe main body 26, and is formed to be orthogonal to the flow direction F of the flow path casing 4. That is, the suction pipe portion 27 is formed along the end surface 3b of the denitration catalyst 3.
關閉吸入管部27的兩端部。並在與吸入管部27的脫硝觸媒3相對的一側,沿著吸入管部27的長方向形成有複數吸入口28。吸入口28的形狀是呈沿著吸入管部27的長方向的長圓形狀。Both ends of the suction pipe portion 27 are closed. Further, a plurality of suction ports 28 are formed along the longitudinal direction of the suction pipe portion 27 on the side opposite to the denitration catalyst 3 of the suction pipe portion 27. The shape of the suction port 28 is an oblong shape along the longitudinal direction of the suction pipe portion 27.
驅動機構23,具有:安裝在吹管21基端的移動架30;設置在外罩22外部的馬達33;及將馬達33的動力傳動至移動架30的鏈輪、鍊條。The drive mechanism 23 includes a moving frame 30 attached to the base end of the blow pipe 21, a motor 33 provided outside the cover 22, and a sprocket and a chain for transmitting the power of the motor 33 to the moving frame 30.
如第5圖表示,在吹管21的基端設有可使吹管21沿著外罩22的長方向自由往返移動保持的移動架30。移動架30保持著吹管21的基端,並形成包覆著饋送管25外圍的形狀,具有維持著吹管21與饋送管25之間的氣密的功能。As shown in Fig. 5, the base end of the blow pipe 21 is provided with a moving frame 30 that allows the blow pipe 21 to be freely reciprocated along the longitudinal direction of the cover 22. The moving frame 30 holds the base end of the blow pipe 21 and is formed in a shape covering the periphery of the feed pipe 25, and has a function of maintaining airtightness between the blow pipe 21 and the feed pipe 25.
在與移動架30的饋送管25的接觸面設有將移動架30的內周圍面與饋送管25的外圍面之間密封的密封構件31。作為密封構件31例如可採用壓蓋填料。A sealing member 31 that seals between the inner peripheral surface of the moving frame 30 and the peripheral surface of the feeding tube 25 is provided at a contact surface with the feeding tube 25 of the moving frame 30. As the sealing member 31, for example, a gland packing can be employed.
並在移動架30安裝有在沿著外罩22的長方向所設置的導軌32上移動的導輥40,藉此,可進行沿著保持在移動架30之吹管21的長方向的移動。又,導輥40是設置在抵接於後述的限位開關45、46可進行限位開關ON/OFF的位置。Further, a guide roller 40 that moves on the guide rail 32 provided along the longitudinal direction of the outer cover 22 is attached to the movable frame 30, whereby movement in the longitudinal direction of the blow pipe 21 held by the movable frame 30 can be performed. Further, the guide roller 40 is provided at a position where the limit switches ON and OFF can be performed by abutting the limit switches 45 and 46 which will be described later.
外罩22的基端側且在外罩22的外部配置有馬達33。在該馬達33的輸出軸安裝有第一鏈輪34,並在外罩22內部的基端側安裝有第二鏈輪35。在第一鏈輪34與第二鏈輪35掛設有形成長圓軌道的第一鍊條36。亦即,馬達 33的動力是透過第一鏈輪34、第一鍊條36及第二鏈輪35,傳動至可旋轉支撐著第二鏈輪35的第一轉軸37。A motor 33 is disposed on the proximal end side of the outer cover 22 and outside the outer cover 22. A first sprocket 34 is attached to an output shaft of the motor 33, and a second sprocket 35 is attached to a proximal end side of the outer cover 22. A first chain 36 forming an oblong track is hung on the first sprocket 34 and the second sprocket 35. That is, the motor The power of 33 is transmitted to the first rotating shaft 37 that rotatably supports the second sprocket 35 through the first sprocket 34, the first chain 36, and the second sprocket 35.
在可自由旋轉安裝於外罩22基端側的第一轉軸37安裝有和第二鏈輪35一起旋轉的第三鏈輪38。並在外罩22的前端側安裝有避開與吸入管20干涉的第二轉軸39,在該第二轉軸39安裝有可旋轉第四鏈輪41。在第三鏈輪38與第四鏈輪41掛設有第二鍊條42,藉此,使第二鍊條42形成沿著外罩22的長方向的長圓軌道。A third sprocket 38 that rotates together with the second sprocket 35 is attached to the first rotating shaft 37 that is rotatably mounted to the proximal end side of the outer cover 22. A second rotating shaft 39 that avoids interference with the suction pipe 20 is attached to the front end side of the outer cover 22, and a rotatable fourth sprocket 41 is attached to the second rotating shaft 39. The second chain 42 is hung on the third sprocket 38 and the fourth sprocket 41, whereby the second chain 42 is formed into an oblong orbit along the longitudinal direction of the outer cover 22.
又,第二鍊條42是透過連接構件43連結於移動架30。Further, the second chain 42 is coupled to the movable frame 30 via the transmission member 43.
藉以上的構成,馬達33的動力一旦傳動至第一轉軸37時,使第三鏈輪38旋轉,並使第二鏈輪42在其軌道上旋轉。由於第二鍊條42被連結在移動架30,所以第二鍊條42在軌道上移動,使移動架30沿著長方向移動。亦即,藉馬達33的動力,使得和移動架30成一體的吹管21沿著長方向移動。With the above configuration, once the power of the motor 33 is transmitted to the first rotating shaft 37, the third sprocket 38 is rotated and the second sprocket 42 is rotated on its orbit. Since the second chain 42 is coupled to the moving frame 30, the second chain 42 moves on the track to move the moving frame 30 in the long direction. That is, by the power of the motor 33, the blow pipe 21 integrated with the moving frame 30 is moved in the longitudinal direction.
在外罩22的前端側設有反轉用限位開關45,並在外罩22的基端側設有停止用限位開關46。配置使限位開關45、46根據移動架30的導輥40的接觸而切入開關。A reverse limit switch 45 is provided on the front end side of the outer cover 22, and a stop limit switch 46 is provided on the proximal end side of the outer cover 22. The configuration causes the limit switches 45, 46 to cut into the switch in accordance with the contact of the guide rolls 40 of the moving frame 30.
限位開關45、46是控制吹管21及移動架30的移動範圍的限制及前進、後退動作。The limit switches 45 and 46 control the restriction of the movement range of the blow pipe 21 and the moving frame 30, and the forward and backward movements.
牆盒24是由長方體形的箱主體47與安裝在箱主體47基端側的密封箱48所構成。在箱主體47形成有吹管21貫穿朝向前端側的面與朝向其相反側的基端部的面的 貫穿孔49。在貫穿孔49與吹管21之間設有預定的間隙。The wall box 24 is composed of a rectangular parallelepiped box main body 47 and a sealed box 48 attached to the proximal end side of the tank main body 47. The tank main body 47 is formed with a surface on which the blow pipe 21 penetrates toward the front end side and a surface facing the base end portion on the opposite side thereof. Through hole 49. A predetermined gap is provided between the through hole 49 and the blow pipe 21.
密封箱48為長方體形的箱型構件,設置在箱主體47的基端側。在密封箱48內連接有維持著高壓之密封箱48用的高壓密封供氣管50。藉高壓密封供氣管50所供應的氣體是透過箱主體47基端側的貫穿孔49與吹管21的外圍面之間的間隙在箱主體47內流動。The seal case 48 is a box-shaped member having a rectangular parallelepiped shape and is provided on the proximal end side of the case main body 47. A high-pressure sealed air supply pipe 50 for sealing the high pressure sealing box 48 is connected to the sealed box 48. The gas supplied from the high pressure seal air supply pipe 50 flows through the gap between the through hole 49 on the proximal end side of the tank main body 47 and the outer peripheral surface of the blow pipe 21 in the tank main body 47.
又,在箱主體47的基端側延伸有安裝支撐51,與設置在外罩22前端側的安裝支撐52連結。並在外罩22的前端側設有從下方支撐吹管21的支撐輥53。Further, a mounting support 51 is extended on the proximal end side of the case main body 47, and is coupled to a mounting support 52 provided on the distal end side of the cover 22. A support roller 53 that supports the blow pipe 21 from below is provided on the front end side of the outer cover 22.
接著,針對本實施形態有關的塵埃回收裝置1的作用說明如下。Next, the operation of the dust collecting device 1 according to the present embodiment will be described below.
首先,馬達33一旦啟動時,藉馬達33的旋轉力使第二鍊條42移動,透過連接於第二鍊條42的連接構件43及移動架30使吹管21沿著長方向移動。吹管21是藉著未圖示的控制裝置控制使其朝前端側的方向前進至切入反轉用限位開關45為止,或後退至切入停止用限位開關46為止。First, when the motor 33 is started, the second chain 42 is moved by the rotational force of the motor 33, and the blow pipe 21 is moved in the longitudinal direction by the connecting member 43 and the moving frame 30 connected to the second chain 42. The blow pipe 21 is controlled by a control device (not shown) to advance to the cutting inversion limit switch 45 in the direction of the front end side, or to the cut stop limit switch 46.
在吹管21移動的期間,吸引脫硝觸媒3上的塵埃,使得含塵埃的氣體透過濾器管25流入塵埃配送管7。氣體的壓力是藉壓力送訊器14的測量,對應此壓力控制吸引力控制閥16,來控制吸引力。While the blow pipe 21 is moving, the dust on the denitration catalyst 3 is sucked, and the dust-containing gas permeates into the dust distribution pipe 7 through the filter pipe 25. The pressure of the gas is measured by the pressure transmitter 14, which controls the attractive force control valve 16 to control the attractive force.
又,氣體的溫度是藉溫度送訊器11的測量,對應此溫度控制大氣導入閥13,來控制氣體的溫度。Further, the temperature of the gas is measured by the temperature transmitter 11, and the atmospheric introduction valve 13 is controlled corresponding to the temperature to control the temperature of the gas.
接著,包含於氣體的塵埃是藉著袋式濾器8的補充,送至灰處理設備。將除去塵埃後的氣體,經由風扇9送至煙道。Next, the dust contained in the gas is supplied to the ash processing apparatus by the bag filter 8. The gas after the dust is removed is sent to the flue via the fan 9.
根據上述實施形態,由於附著在脫硝裝置3的塵埃,尤其是將如爆米花狀灰的粒徑大小的煤塊透過流路內除煤裝置6的吸入管20吸引後除去的構造,可防止塵埃堆積在脫硝觸媒3。藉此,可更加增長設備的連續運轉時間。According to the above-described embodiment, the dust adhering to the denitration device 3, in particular, the structure in which the coal piece having the particle size of the popcorn-like ash is sucked and removed by the suction pipe 20 of the coal removal device 6 in the flow path can be prevented. Dust accumulates in the denitrification catalyst 3. Thereby, the continuous running time of the equipment can be further increased.
又,流路殼體4內的塵埃被排出於流路殼體4的外部,因此設備停止時的流路殼體4的清掃簡易。Further, since the dust in the flow path casing 4 is discharged to the outside of the flow path casing 4, the cleaning of the flow path casing 4 when the equipment is stopped is simplified.
並由於將流路內除煤裝置6所吸引含塵埃的氣體透過塵埃配送管7導入袋式濾器8,在袋式濾器8中除去塵埃,可防止塵埃影響到大氣。By introducing the dust-laden gas from the coal removing device 6 in the flow path into the bag filter 8 through the dust distributing pipe 7, the dust is removed from the bag filter 8, and dust is prevented from affecting the atmosphere.
又,藉著將密封箱48的內部維持著比流路殼體4的內部高壓,可防止廢氣從吸入管20的插入部漏出。Further, by maintaining the inside of the sealed casing 48 at a higher internal pressure than the flow path casing 4, it is possible to prevent the exhaust gas from leaking from the insertion portion of the suction pipe 20.
並且,在牆盒24的箱主體47的貫穿孔49與吹管21之間設置預定的間隙,可防止因廢氣的熱產生外壁4a與吹管21的熱膨脹差導致的干涉。Further, a predetermined gap is provided between the through hole 49 of the tank main body 47 of the wall box 24 and the blow pipe 21, and interference due to the difference in thermal expansion between the outer wall 4a and the blow pipe 21 due to the heat of the exhaust gas can be prevented.
又,馬達33相對於吸入管20分開配置在外罩22的外部,可藉此防止因含塵埃的氣體的熱所致馬達33的損傷。Further, the motor 33 is disposed outside the outer casing 22 with respect to the suction pipe 20, thereby preventing damage of the motor 33 due to heat of the dust-containing gas.
再者,上述實施形態雖是在密封箱48與流路殼體4之間設置箱主體47的構成,但也可省略牆盒24的箱主體47。Further, in the above embodiment, the case main body 47 is provided between the seal case 48 and the flow path case 4, but the case main body 47 of the wall case 24 may be omitted.
以下,根據圖示說明本發明第二實施形態有關的流路內除煤裝置。Hereinafter, an in-flow coal removal device according to a second embodiment of the present invention will be described with reference to the drawings.
如第6圖表示,第二實施形態有關的流路內除煤裝置6B與第一實施形態的流路內除煤裝置6(參閱第3圖)比較,吸入管20與牆盒24B的構造不同。As shown in Fig. 6, the flow path inner coal removing device 6B according to the second embodiment is different from the flow path inner coal removing device 6 (see Fig. 3) of the first embodiment in that the suction pipe 20 and the wall box 24B are different in structure. .
本實施形態的吸入管20B,具有:藉驅動機構23可朝著長方向進退的移動用連動軸55;與移動用連動軸55平行設置,基端側被成懸臂是支撐在牆盒24B的濾器管25B;及與移動用連動軸55平行設置,並連接於移動用連動軸55的吹管21B。The suction pipe 20B of the present embodiment has a moving interlocking shaft 55 that can advance and retreat in the longitudinal direction by the drive mechanism 23, and is disposed in parallel with the moving interlocking shaft 55, and the base end side is a cantilever that is supported by the wall box 24B. The tube 25B is provided in parallel with the moving interlocking shaft 55, and is connected to the blowing pipe 21B of the moving interlocking shaft 55.
饋送管25B的前端側是插入吹管21B的內部。移動用連動軸55是貫穿牆盒24B,延伸至流路殼體4的內部,使其前端與吹管21B連接。亦即,藉著移動用連動軸55的進退,構成使吹管21B朝著長方向進退。The front end side of the feed pipe 25B is the inside of the insertion blow pipe 21B. The moving interlocking shaft 55 extends through the wall case 24B and extends inside the flow path casing 4 so that the front end thereof is connected to the blow pipe 21B. In other words, the forward and backward movement of the moving interlocking shaft 55 is configured to advance and retreat the blow pipe 21B in the longitudinal direction.
在吹管21B的基端,設有一邊使吹管21B的內周圍面與饋送管25B的外圍面之間密封,一邊可使吹管21B在饋送管25B上呈望眼鏡伸縮狀進退的密封機構56。在與密封機構56的饋送管25B的接觸面上,設有曲路封件57。At the base end of the blow pipe 21B, while the inner peripheral surface of the blow pipe 21B and the outer peripheral surface of the feed pipe 25B are sealed, the blow pipe 21B can be made to look into the feed pipe 25B by the sealing mechanism 56 which expands and retracts the eyeglasses. A curved path seal 57 is provided on the contact surface with the feed pipe 25B of the sealing mechanism 56.
吹管21B,係由:吹管主體26B;設置在吹管主體26B前端的第一吸入管部58;及設置在吹管主體基端的第二吸入管部59所構成。亦即,本實施形態的吹管21B具有兩個吸入管部58、59,第一吸入管部58是吸引脫硝觸 媒3的長方向一方側,第二吸入管部59則是吸引脫硝觸媒3的長方向另一方側。The blow pipe 21B is composed of a blow pipe main body 26B, a first suction pipe portion 58 provided at the front end of the blow pipe main body 26B, and a second suction pipe portion 59 provided at the base end of the blow pipe main body. That is, the blow pipe 21B of the present embodiment has two suction pipe portions 58, 59, and the first suction pipe portion 58 attracts the denitrification touch. The second suction pipe portion 59 attracts the other side of the denitration catalyst 3 in the longitudinal direction on the one side in the longitudinal direction of the medium 3.
說明本實施形態的流路內除煤裝置6B的作用時,藉馬達33的驅動使移動用連動軸55在長方向進退。藉此,可使連結於移動用連動軸55的吹管21B朝著長方向進退。In the case of the operation of the in-stream coal removing device 6B of the present embodiment, the moving interlocking shaft 55 is advanced and retracted in the longitudinal direction by the driving of the motor 33. Thereby, the blow pipe 21B connected to the moving interlocking shaft 55 can be advanced and retracted in the longitudinal direction.
根據上述實施形態,包含藉吹管21B所吸引的塵埃的氣體不會經由外罩22的內部,送至塵埃配送管7,可防止因氣體的熱導致外罩22內部的損傷。According to the above embodiment, the gas containing the dust sucked by the blow pipe 21B is not sent to the dust distribution pipe 7 through the inside of the outer cover 22, and damage inside the outer cover 22 due to heat of the gas can be prevented.
又,吸入管部58、59是安裝在吹管21B的前端及基端,所以和第一實施形態的流路內除煤裝置6比較,可以是吹管21B行程的大致一半。Further, since the suction pipe portions 58, 59 are attached to the front end and the base end of the blow pipe 21B, they can be substantially half of the stroke of the blow pipe 21B as compared with the flow path internal coal removing device 6 of the first embodiment.
第7圖為說明流路內除煤裝置的其他形態的部份放大圖。Fig. 7 is a partially enlarged view showing another form of the coal removing device in the flow path.
如第7圖表示,在其他形態的流路內除煤裝置6C設有在脫硝觸媒3的上游側補充塵埃的網的金屬網61。金屬網61的網眼大小是補充如爆米花狀灰的粒徑大小的煤塊,可阻止煤塊通過的尺寸。又,金屬網61是配置在脫硝觸媒3的跟前。並且,吹管21的吸入口28是與金屬網61相對設置。As shown in Fig. 7, the coal removing device 6C in the flow path of another embodiment is provided with a metal mesh 61 for replenishing dust on the upstream side of the denitration catalyst 3. The mesh size of the metal mesh 61 is a size that complements the size of the popcorn-like ash, which prevents the passage of the coal. Further, the metal mesh 61 is disposed in front of the denitration catalyst 3. Further, the suction port 28 of the blow pipe 21 is disposed opposite to the metal mesh 61.
又,本實施形態的流路內除煤裝置6C的吹管21設有作為塵埃粉碎用的粉碎手段的刷62。詳細而言,刷62為從吹管主體26朝前端側突出的支撐部63,及焊接於支撐部63的多數金屬製的金屬線64所構成,金屬線64的前 端朝著金屬網61及脫硝觸媒3側突出抵接於金屬網61。Further, the blow pipe 21 of the in-stream coal removing device 6C of the present embodiment is provided with a brush 62 as a grinding means for dust grinding. Specifically, the brush 62 is a support portion 63 that protrudes from the blow pipe main body 26 toward the distal end side, and a plurality of metal wires 64 that are welded to the support portion 63, and the front of the metal wire 64 The end protrudes toward the metal mesh 61 and the denitration catalyst 3 side to abut against the metal mesh 61.
根據上述形態,可防止如爆米花狀灰的大的煤塊到達配置在金屬網61更後游側的脫硝觸媒3,容易進行設備停止時之脫硝觸媒3的清掃。According to the above aspect, it is possible to prevent the large coal mass such as popcorn ash from reaching the denitration catalyst 3 disposed on the rear side of the metal mesh 61, and it is easy to clean the denitration catalyst 3 when the apparatus is stopped.
又,藉著刷62使粒徑大的塵埃粉碎,使得塵埃更為容易吸引。並且,將大於吸入口28的塵埃粉碎,可吸引更大的塵埃。Further, the dust having a large particle size is pulverized by the brush 62, so that the dust is more easily attracted. Further, the dust larger than the suction port 28 is pulverized to attract more dust.
第8圖為說明流路內除煤裝置的另外其他形態的部份放大圖,從沿著流動方向F的方向顯示吹管21D及吸入管部27D的上視圖。Fig. 8 is a partially enlarged view showing still another embodiment of the coal removing device in the flow path, and shows a top view of the blow pipe 21D and the suction pipe portion 27D from the direction along the flow direction F.
如第8圖表示,在本形態的流路內除煤裝置6D的吸入管部27D連接著上述各實施形態的吹管主體26,並連接有構成噴射管65的第二吹管66,該噴射管構成可供給對脫硝觸媒3噴射塵埃除去用氣體的高壓氣體。As shown in Fig. 8, the suction pipe portion 27D of the coal removing device 6D in the flow path of the present embodiment is connected to the blow pipe main body 26 of each of the above embodiments, and the second blow pipe 66 constituting the injection pipe 65 is connected, and the injection pipe is configured. A high-pressure gas that ejects the dust removing gas to the denitration catalyst 3 can be supplied.
噴射管65具有和吸入管20大致相同的構成,不同的點是相對於吸入管20藉風扇9的吸引力從吸入管部27D吸引塵埃,而噴射管65則是藉著高壓氣體從吸入管部27D的吸入口28噴出空氣。The injection pipe 65 has substantially the same configuration as that of the suction pipe 20, and differs in that suction is sucked from the suction pipe portion 27D by the suction force of the fan 9 with respect to the suction pipe 20, and the injection pipe 65 is sucked from the suction pipe portion by high-pressure gas. The suction port 28 of the 27D ejects air.
根據上述形態,在吸引塵埃之前的階段,藉著從吸入管部27D的吸入口28噴射高壓的氣體,使塵埃成浮游狀態,在隨後的吸引過程中可更為容易吸引塵埃。According to the above aspect, the high-pressure gas is injected from the suction port 28 of the suction pipe portion 27D at a stage before the dust is sucked, so that the dust is floated, and the dust can be more easily attracted during the subsequent suction.
供給高壓氣體用的形態,不限於此,如第9圖表示,也可另外設置噴射管部67,在此噴射管部67連接供給高壓氣體的噴射管65的構成。又如第9圖表示,噴射管部 67也可設置兩個構成夾持著吸入管部27D。The form for supplying the high-pressure gas is not limited thereto, and as shown in Fig. 9, the injection pipe portion 67 may be separately provided, and the injection pipe portion 67 is connected to the injection pipe 65 for supplying the high-pressure gas. As shown in Figure 9, the injection tube 67 may also be provided with two components sandwiching the suction pipe portion 27D.
此外,噴射的媒體不限於高壓的空氣,例如也可以噴射高壓的蒸氣使粉塵成浮游狀態的構成。Further, the medium to be ejected is not limited to high-pressure air, and for example, it is also possible to eject high-pressure steam to make the dust into a floating state.
再者,本發明的技術範圍不僅限於上述的實施形態,可在不脫離本發明主旨的範圍內施以種種的變更。例如,除去包含於氣體中的塵埃的方法不限於袋式濾器,也可使用粉塵分離器(旋風分離器)分離氣體中的粉塵。或者在塵埃配送管7上,不除去氣體中的塵埃,而是將氣體再次投入設備內不致造成處理上阻礙的位置的構成。In addition, the technical scope of the present invention is not limited to the above-described embodiments, and various modifications can be made without departing from the spirit and scope of the invention. For example, the method of removing dust contained in the gas is not limited to the bag filter, and the dust in the gas may be separated using a dust separator (cyclone separator). Alternatively, on the dust distribution pipe 7, the dust in the gas is not removed, but the gas is again placed in the apparatus to prevent the processing from being hindered.
又,上述各實施形態有關的塵埃回收裝置只要可以吸入管吸入,則不僅是爆米花狀灰並可回收種種大的灰塵。Moreover, the dust collecting apparatus according to each of the above embodiments can be used not only for popcorn ash but also for collecting various types of dust as long as it can be sucked by the suction pipe.
1‧‧‧塵埃回收裝置1‧‧‧Dust recovery unit
2‧‧‧鍋爐2‧‧‧Boiler
2a‧‧‧排氣管2a‧‧‧Exhaust pipe
3‧‧‧脫硝觸媒3‧‧‧Denitration catalyst
4‧‧‧流路殼體4‧‧‧Flow path housing
5‧‧‧塵埃處理部5‧‧‧Dust Processing Department
6‧‧‧流路內除煤裝置6‧‧‧In-stream coal removal device
7‧‧‧塵埃配送管7‧‧‧Dust distribution tube
8‧‧‧袋式濾器(濾器)8‧‧‧ bag filter (filter)
9‧‧‧風扇(吸引手段)9‧‧‧Fan (attraction means)
11‧‧‧溫度送訊器11‧‧‧Temperature transmitter
12‧‧‧溫度控制裝置12‧‧‧ Temperature control device
13‧‧‧大氣導入閥13‧‧‧Atmospheric introduction valve
14‧‧‧壓力送訊器14‧‧‧Pressure transmitter
15‧‧‧壓力控制裝置15‧‧‧ Pressure control device
16‧‧‧吸引力控制閥16‧‧‧Attraction control valve
17‧‧‧轉換閥17‧‧‧Switching valve
20‧‧‧吸入管20‧‧‧Inhalation tube
21‧‧‧吹管(前端管)21‧‧‧Blowpipe (front end tube)
22‧‧‧外罩22‧‧‧ Cover
23‧‧‧驅動機構(驅動手段)23‧‧‧Drive mechanism (driver)
24‧‧‧牆盒24‧‧‧ wall box
25‧‧‧饋送管(基端管)25‧‧‧Feed tube (base tube)
33‧‧‧馬達33‧‧‧Motor
61‧‧‧金屬網(網)61‧‧‧Metal net (net)
第1圖為本發明實施形態有關的塵埃回收裝置的系統圖。Fig. 1 is a system diagram of a dust collecting device according to an embodiment of the present invention.
第2圖是表示塵埃回收裝置的脫硝觸媒的透視圖。Fig. 2 is a perspective view showing a denitration catalyst of the dust collecting device.
第3圖為本發明第一實施形態有關流路內除煤裝置的側視圖。Fig. 3 is a side view showing a coal removal device in a flow path according to a first embodiment of the present invention.
第4圖為第3圖的A箭頭方向圖,本發明第一實施形態有關流路內除煤裝置的上視圖。Fig. 4 is a view showing the direction of arrow A in Fig. 3, and a top view of the coal removing device in the flow path according to the first embodiment of the present invention.
第5圖為第3圖的B部放大圖。Fig. 5 is an enlarged view of a portion B of Fig. 3.
第6圖為本發明第二實施形態有關流路內除煤裝置的側視圖。Fig. 6 is a side view showing a coal removing device in a flow path according to a second embodiment of the present invention.
第7圖為說明流路內除煤裝置的其他形態的部份放大 圖。Figure 7 is a partial enlargement showing other forms of the coal removal device in the flow path. Figure.
第8圖為說明流路內除煤裝置的另外其他形態的部份放大圖。Fig. 8 is a partially enlarged view showing still another embodiment of the coal removing device in the flow path.
第9圖為說明流路內除煤裝置的再一其他形態的部份放大圖。Fig. 9 is a partially enlarged view showing still another embodiment of the coal removing device in the flow path.
3‧‧‧脫硝觸媒3‧‧‧Denitration catalyst
3b‧‧‧端面3b‧‧‧ end face
4‧‧‧流路殼體4‧‧‧Flow path housing
4a‧‧‧外壁4a‧‧‧ outer wall
6‧‧‧流路內除煤裝置6‧‧‧In-stream coal removal device
7‧‧‧塵埃配送管7‧‧‧Dust distribution tube
20‧‧‧吸入管20‧‧‧Inhalation tube
21‧‧‧吹管(前端管)21‧‧‧Blowpipe (front end tube)
22‧‧‧外罩22‧‧‧ Cover
23‧‧‧驅動機構(驅動手段)23‧‧‧Drive mechanism (driver)
24‧‧‧牆盒24‧‧‧ wall box
25‧‧‧饋送管(基端管)25‧‧‧Feed tube (base tube)
26‧‧‧吹管主體26‧‧‧Blowing pipe body
27‧‧‧吸入管部27‧‧‧Inhalation Pipe Department
29‧‧‧端子箱29‧‧‧Terminal box
33‧‧‧馬達33‧‧‧Motor
34‧‧‧第一鏈輪34‧‧‧First sprocket
35‧‧‧第二鏈輪35‧‧‧Second sprocket
36‧‧‧第一鍊條36‧‧‧First chain
37‧‧‧第一轉軸37‧‧‧First shaft
38‧‧‧第三鏈輪38‧‧‧ Third sprocket
39‧‧‧第二轉軸39‧‧‧second shaft
41‧‧‧第四鏈輪41‧‧‧fourth sprocket
42‧‧‧第二鍊條42‧‧‧Second chain
45‧‧‧限位開關45‧‧‧Limit switch
47‧‧‧箱主體47‧‧‧ box body
48‧‧‧密封箱48‧‧‧ sealed box
49‧‧‧貫穿孔49‧‧‧through holes
50‧‧‧高壓密封供氣管50‧‧‧High pressure sealed air supply pipe
53‧‧‧支撐輥53‧‧‧Support roller
Claims (10)
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TW101119118A TWI485356B (en) | 2012-05-29 | 2012-05-29 | Soot blower in passage and dust recovery apparatus |
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TW101119118A TWI485356B (en) | 2012-05-29 | 2012-05-29 | Soot blower in passage and dust recovery apparatus |
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TWI485356B true TWI485356B (en) | 2015-05-21 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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TWI626984B (en) * | 2015-04-08 | 2018-06-21 | Mitsubishi Hitachi Power Sys | Exhaust gas treatment device |
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