JP4727515B2 - Air nozzle structure of fluidized bed combustion furnace - Google Patents

Air nozzle structure of fluidized bed combustion furnace Download PDF

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JP4727515B2
JP4727515B2 JP2006181375A JP2006181375A JP4727515B2 JP 4727515 B2 JP4727515 B2 JP 4727515B2 JP 2006181375 A JP2006181375 A JP 2006181375A JP 2006181375 A JP2006181375 A JP 2006181375A JP 4727515 B2 JP4727515 B2 JP 4727515B2
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fluidized bed
air nozzle
furnace
foreign matter
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洋 永井
良則 寺澤
俊之 坂井
鳥居  功
明用  和幸
龍夫 横式
善久 荒川
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Mitsubishi Heavy Industries Ltd
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Description

本発明は、カットタイヤやスクリーン粕等のリサイクル燃料を処理対象とした流動床燃焼炉の空気ノズル構造に関し、特に、ステッチャ状異物からなる長尺状部位を有した不燃性異物を含むリサイクル燃料を焼却処理した際に、異物が空気ノズル近傍に滞留、蓄積することを防止できる流動床燃焼炉の空気ノズル構造に関する。 The present invention relates to an air nozzle structure of the fluidized bed combustion furnace and processed recycled fuel such as cut tires, screen residue, in particular, recycled fuel containing incombustible foreign matter having an elongated portion comprising a stitcher foreign matter The present invention relates to an air nozzle structure of a fluidized bed combustion furnace that can prevent foreign matter from staying and accumulating in the vicinity of the air nozzle when incineration is performed.

従来、燃焼炉内の底部に流動材を充填し、該流動材に向けて空気を吹き込んで浮遊させた流動床を形成し、高温の流動床内に被処理物を投入して流動材と接触させて燃焼させる流動床式燃焼炉が知られている。このような流動床燃焼炉において処理に適した被処理物としては、異物含有廃棄物のほかにカットタイヤやスクリーン粕等のリサイクル燃料がある。
一般に流動床燃焼炉には、流動床を流動状態とするための空気を吹き込む空気ノズルが、炉底に多数取り付けられている。炉底の下方に設けられた風箱を介して空気ノズルに空気が供給され、該空気ノズルから燃焼室に向けて空気を吹き出すことにより流動材を流動化させている。
Conventionally, a fluidized bed is filled in the bottom of the combustion furnace, air is blown toward the fluidized material to form a fluidized bed, and an object to be treated is put into the high-temperature fluidized bed to contact the fluidized material. 2. Description of the Related Art Fluidized bed combustion furnaces that are made to burn are known. In addition to the foreign matter-containing waste, there are recycle fuels such as cut tires and screen soots as objects to be treated that are suitable for treatment in such a fluidized bed combustion furnace.
In general, in a fluidized bed combustion furnace, a large number of air nozzles for blowing air for bringing the fluidized bed into a fluidized state are attached to the bottom of the furnace. Air is supplied to the air nozzle through a wind box provided below the furnace bottom, and the fluidized material is fluidized by blowing air from the air nozzle toward the combustion chamber.

このような空気ノズルの構成が特許文献1(特開平9−299784号公報)、特許文献2(特開2005−226870号公報)等に記載されている。
特許文献1には、ネジ機構により炉底に取り付けられたノズル本体と、該ノズル本体を覆うキャップ部とからなる二重管構造を有した空気ノズルの構成が開示されており、さらに、ノズル本体下部のガス室側にオリフィス孔を有する差圧調整プラグが取り付けられ、該差圧調整プラグによりノズルの圧損を設定するようになっている。
The configuration of such an air nozzle is described in Patent Document 1 (Japanese Patent Laid-Open No. 9-299784), Patent Document 2 (Japanese Patent Laid-Open No. 2005-226870), and the like.
Patent Document 1 discloses a configuration of an air nozzle having a double tube structure including a nozzle body attached to the furnace bottom by a screw mechanism and a cap portion covering the nozzle body. A differential pressure adjusting plug having an orifice hole is attached to the lower gas chamber side, and the pressure loss of the nozzle is set by the differential pressure adjusting plug.

同様に、特許文献2にも二重管構造を有した空気ノズルが示されている。図7及び図8に示されるように、該空気ノズル51は、炉底57を貫通する内筒管52と、該内筒管52の外側に位置する外筒管55とから構成され、風箱よりから供給される空気が内筒管52内を通過して、内筒管52上方の周面に穿設された円又は楕円形の開口部53を介して外筒管55に供給される。外筒管55に供給された空気は、外筒管55下方の周面に穿設された開口部56を介して燃焼室に向けて水平方向に吹き出すようになっている。   Similarly, Patent Document 2 also shows an air nozzle having a double tube structure. As shown in FIGS. 7 and 8, the air nozzle 51 includes an inner cylindrical pipe 52 that penetrates the furnace bottom 57 and an outer cylindrical pipe 55 that is located outside the inner cylindrical pipe 52. The air supplied from above passes through the inner cylindrical pipe 52 and is supplied to the outer cylindrical pipe 55 through a circular or elliptical opening 53 formed in the peripheral surface above the inner cylindrical pipe 52. The air supplied to the outer tube 55 is blown out horizontally toward the combustion chamber through an opening 56 formed in the peripheral surface below the outer tube 55.

上記したようなリサイクル燃料には不燃性の異物が含まれることが多く、流動床燃焼炉の底部には異物排出口が設けられ、通常はこの異物排出口により炉内から異物を除去している。リサイクル燃料から発生した異物は、流動床内を拡散・移動しながら次第に異物排出口から排出されていくが、一部の異物は分散ノズルからの噴出し空気の脈動、他のノズルからの噴出し空気等によりノズル内部に進入する。リサイクル燃料に含まれる異物には、ステッチャ状の物、長尺状の物、或いは先端が鉤状(かぎ状)の物などがあり、空気ノズルの空気孔に絡み付き易く、炉内に滞留、蓄積し、流動床の流動不良や空気ノズルの閉塞、異物排出口の閉塞等のトラブルに繋がることがあった。   Recycled fuel as described above often contains nonflammable foreign matter, and a foreign substance discharge port is provided at the bottom of the fluidized bed combustion furnace. Normally, this foreign substance discharge port removes foreign matter from the inside of the furnace. . Foreign matter generated from the recycled fuel is gradually discharged from the foreign matter discharge port while diffusing and moving in the fluidized bed, but some foreign matter is pulsating the air blown from the dispersed nozzles and blown from other nozzles. It enters the inside of the nozzle by air or the like. Foreign materials contained in recycled fuel include stitcher-like objects, long objects, or hook-shaped objects (tips), which are easily entangled with the air holes of the air nozzle and stay and accumulate in the furnace. However, it may lead to troubles such as fluidized bed failure, air nozzle blockage, and foreign matter discharge port blockage.

特開平9−299784号公報JP-A-9-299784 特開2005−226870号公報JP 2005-226870 A

特許文献1では、流動化に必要なノズル圧損を差圧調整プラグで調整する構成が開示されているが、この構成によればノズル構造が複雑となり、また燃料変化に伴って圧損調整をする場合、差圧調整プラグの交換が必要となり手間がかかる。また、石炭の燃焼炉等を対象としており、ステッチャ状の異物が混入された被処理物については考慮されておらず、このような異物の滞留、蓄積防止の構成は備えていない。
特許文献2では、内筒管及び外筒管に、夫々空気が通流する開口部を穿設した二重管構造の空気ノズルの構成が開示されており、構造が単純で流動材の逆流防止が可能であり、さらに空気流量のアンバランスが出難いという利点を有するが、外筒管の開口部形状が円形又は楕円形の場合、図7に示されるように開口部56下端からノズル底部に高さが生じ、ノズル内部にポケット60が形成されてしまうため、ポケット60内に異物が滞留、蓄積されてしまうという問題があった。従って、高濃度に異物を含む被処理物に適用することは困難であった。さらに、図8(B)に示されるように、ステッチャ61が隣接する空気孔間を挟み込んだ場合には、簡単に取り除くことができず大変な手間がかかるという問題もあった。
従って、本発明は上記従来技術の問題点に鑑み、被処理物中に含まれる不燃性異物が空気ノズル付近に滞留、蓄積することを防止できる流動床燃焼炉の空気ノズル構造を提供することを目的とする。
Patent Document 1 discloses a configuration in which a nozzle pressure loss necessary for fluidization is adjusted with a differential pressure adjustment plug. However, according to this configuration, the nozzle structure becomes complicated, and the pressure loss adjustment is performed in accordance with a change in fuel. Therefore, it is necessary to replace the differential pressure adjusting plug, which is troublesome. Further, Ri our coal combustion furnace or the like as an object, is not considered treatment object scan Tetcha foreign matter is mixed, the residence of such foreign matter, the configuration of the storage prevention is not provided.
Patent Document 2 discloses a structure of an air nozzle having a double tube structure in which an opening through which air flows is formed in each of an inner tube and an outer tube, and the structure is simple and the backflow of a fluid material is prevented. However, if the shape of the opening of the outer tube is circular or elliptical, as shown in FIG. 7, the lower end of the opening 56 extends from the bottom of the nozzle to the bottom of the nozzle. Since the height is generated and the pocket 60 is formed inside the nozzle, there is a problem that foreign matter stays and accumulates in the pocket 60. Therefore, it has been difficult to apply to an object to be processed containing foreign matter at a high concentration. Further, as shown in FIG. 8B, when the stitcher 61 sandwiches between adjacent air holes, there is a problem that it cannot be easily removed and takes a lot of labor.
Therefore, in view of the above-mentioned problems of the prior art, the present invention provides an air nozzle structure for a fluidized bed combustion furnace that can prevent nonflammable foreign substances contained in the workpiece from staying and accumulating in the vicinity of the air nozzle. Objective.

そこで、本発明はかかる課題を解決するために、ステッチャ状異物からなる長尺状部位を有した不燃性異物を含むリサイクル燃料を処理対象とした流動床燃焼炉の空気ノズル構造であって、前記空気ノズルは燃焼室炉底に多数配設され、該空気ノズルは内筒と外筒からなる二重管構造を有し、前記内筒の周面上方に圧損調整機能を有する噴出孔が穿設されるとともに、前記外筒の周面下方に空気孔が穿設された流動床燃焼炉の空気ノズル構造において、
前記外筒の空気孔は、上縁が曲率線状で且つ下縁が直線状の馬蹄形状若しくは半円形状で且つ直線状の下縁前記炉底の上面と同一面上に位置させ
更に該空気孔は外筒の円周方向に複数存在し、該空気孔のピッチ間隔が、10〜30mmであり、
一方前記内筒の噴出孔が円周方向に沿って複数存在するとともに、該噴出孔が鉛直方向に複数段の噴出孔を設け、該上下に隣接する噴出孔は、千鳥状に配置することを特徴とする。
Therefore, in order to solve such a problem, the present invention is an air nozzle structure of a fluidized bed combustion furnace intended for treating recycled fuel containing non-combustible foreign matter having an elongated portion made of stitcher-like foreign matter , A large number of air nozzles are arranged at the bottom of the combustion chamber, and the air nozzle has a double pipe structure consisting of an inner cylinder and an outer cylinder, and an ejection hole having a pressure loss adjusting function is formed above the peripheral surface of the inner cylinder. In addition, in the air nozzle structure of a fluidized bed combustion furnace having air holes drilled below the peripheral surface of the outer cylinder,
Air hole of the outer cylinder, and the upper edge with a curvature linear lower edge is to position the and the straight lower edge straight horseshoe shape or a semicircular shape on the upper surface and the same surface of the furnace bottom,
Furthermore the air pores Mashimashi multiple exist in the circumferential direction of the outer cylinder, the pitch spacing of the air pores is 10 to 30 mm,
On the other hand, there are a plurality of ejection holes of the inner cylinder along the circumferential direction, the ejection holes are provided with a plurality of ejection holes in the vertical direction, and the ejection holes adjacent to the upper and lower sides are arranged in a staggered manner. Features.

本発明では、外筒の空気孔下縁を直線状とし該下縁と炉底の上面を一致させることにより、空気ノズル内のポケットをなくすことができ、燃焼室内で発生した異物が空気孔に絡み付くことなく、円滑に系外排出されるようになる。即ち、空気孔から異物が進入した場合であっても、進入した異物が空気ノズルのポケット(図7参照、符号60)内に留まることなく、空気の流れに沿って容易に排出されるため、異物が空気孔近傍に滞留、蓄積することを防げる。
さらに、空気ノズルを二重管構造とすることにより、ノズル構造を簡略化でき製造コストを低減でき、また流動材の空気ノズル内への落下防止が図れる。尚、本発明において空気孔の形状としては、馬蹄形、半円形が挙げられる。
In the present invention, by the air hole lower edge of the outer cylinder and the linear to match the upper surface of the lower edge and the furnace bottom, it is possible to eliminate pockets of air nozzles, foreign matter is air holes generated in the combustion chamber It is discharged smoothly from the system without tangling. That is, even if foreign matter enters from the air hole, the entered foreign matter does not stay in the pocket of the air nozzle (see FIG. 7, reference numeral 60), and is easily discharged along the air flow. foreign matter stay in the vicinity of the air hole, that prevent the accumulating.
Furthermore, by making the air nozzle into a double tube structure, the nozzle structure can be simplified, the manufacturing cost can be reduced, and the fluidized material can be prevented from falling into the air nozzle. As the shape of the air holes in the present invention, horse hoof-shaped, semicircular, and the like.

また、本発明は、前記内筒の噴出孔が円周方向に沿って複数存在するとともに、該噴出孔が鉛直方向に複数段存在する。
このように、複数段の噴出孔を設けることにより、必要圧損の確保が図れる。
さらに、本発明において上下に隣接する噴出孔は、千鳥状に配置する。これにより、噴出孔の存在範囲の鉛直方向幅が小さくなり、噴出孔の下端から空気孔までの空気流路の距離を長くすることができ、空気の整流効果が顕著となる。
The present invention also ejection hole of the inner cylinder along with presence of a plurality of circumferentially,該噴Deana exists several stages multiple vertically.
Thus, the required pressure loss can be ensured by providing a plurality of ejection holes.
Further, ejection hole vertically adjacent in the present invention, it staggered. Thereby, the vertical width of the existence range of the ejection holes is reduced, the distance of the air flow path from the lower end of the ejection holes to the air holes can be increased, and the air rectifying effect becomes remarkable.

また、前記外筒の空気孔の上縁形状を、馬蹄形や半円形のように曲率線状の上縁を有する形状とすることにより、加工が容易となり製造コストが低減できる。また、隣接する空気孔間の距離が短い部位が少なくなり、ステッチャ状異物がこの空気孔間に絡み固化することを抑制できる。即ち、図8(B)に示されるように、ステッチャ状異物が堆積する原因の一つとして、隣接する空気孔にステッチャ61の先端が入り込み、ステッチャ61が空気孔間を挟み込むような状態で固定されてしまうことがある。しかし本発明のごとく上縁を曲率線状とすると、図3(a)に示されるように空気孔のピッチ間隔P(隣合う二つの孔の近接する端部の間隔)は、上方に向かうにつれて大きくなる。従って、短いピッチ間隔P2である部位を少なくすることができ、ステッチャが空気孔間を挟み込んで固定される可能性を小さくすることができる。 Further, the outer cylinder upper edge shape of the air holes of, by a shape having a curvature line shape of the upper edge as horseshoe or semicircular, machining is facilitated can be reduced in manufacturing cost. Moreover, the part where the distance between adjacent air holes is short decreases, and it can suppress that a stitcher-like foreign material becomes entangled and solidified between these air holes. That is, as shown in FIG. 8B, one of the causes of the accumulation of the stitcher-like foreign matter is fixed in a state where the tip of the stitcher 61 enters the adjacent air hole and the stitcher 61 sandwiches the air hole. It may be done. However, when the upper edge has a curved line shape as in the present invention, as shown in FIG. 3A, the pitch interval P of the air holes (the interval between the adjacent end portions of the two adjacent holes) increases upward. growing. Therefore, the site | part which is the short pitch space | interval P2 can be decreased, and possibility that a stitcher will pinch | interpose between air holes and will be fixed can be made small.

さらに、空気孔は外筒の円周方向に複数存在し、該空気孔のピッチ間隔が、10〜30mmであることを特徴とする。
これにより、ステッチャ状異物が含まれる被処理物であっても、上記した理由と同様に、空気孔間を挟み込んで異物が固定されることを防止でき、延いては空気ノズル周辺の異物堆積を防止可能である。このように、前記外筒の空気孔のピッチ間隔が、10〜30mmであることにより、一般に多く用いられているステッチャ状異物の大部分に対応できる。
Furthermore, there are a plurality of air holes in the circumferential direction of the outer cylinder, and the pitch interval of the air holes is 10 to 30 mm .
As a result, even for an object to be processed that contains stitcher-like foreign matter, it is possible to prevent foreign matter from being fixed by being sandwiched between the air holes as in the above-described reason. It can be prevented. Thus, the pitch spacing of the air holes of the outer cylinder, more and Dearuko 10 to 30 mm, can be sufficient for most stitcher foreign matter which has been used generally much.

以上記載のごとく本発明によれば、外筒の空気孔下縁と炉底の上面を一致させることにより空気ノズル内のポケットをなくすことができ、燃焼室内で発生した異物が空気ノズル内に滞留、蓄積することを防止でき、延いては流動床燃焼炉の円滑な運転が可能で、且つメンテナンスが容易となる。
また、内筒に複数段の噴出孔を設けることにより、空気ノズル必要圧損の確保ができる。
さらに、外筒の空気孔上縁を曲率線状としたり、また外筒の空気孔のピッチ間隔を異物の平均長さよりも大とすることにより、ステッチャ状異物が空気孔間を挟み込んで固定されることを抑制する。
As described above, according to the present invention, the pockets in the air nozzle can be eliminated by matching the lower edge of the air hole of the outer cylinder with the upper surface of the furnace bottom, and foreign matter generated in the combustion chamber is retained in the air nozzle. Accumulation can be prevented, and as a result, smooth operation of the fluidized bed combustion furnace is possible, and maintenance is facilitated.
Moreover, the required pressure loss of the air nozzle can be ensured by providing a plurality of ejection holes in the inner cylinder.
Furthermore, by making the upper edge of the air hole of the outer cylinder a curved line, or by making the pitch interval of the air holes of the outer cylinder larger than the average length of the foreign object, the stitcher-like foreign object is fixed by sandwiching the air holes. It suppresses that.

以下、図面を参照して本発明の好適な実施例を例示的に詳しく説明する。但しこの実施例に記載されている構成部品の寸法、材質、形状、その相対的配置等は特に特定的な記載がない限りは、この発明の範囲をそれに限定する趣旨ではなく、単なる説明例に過ぎない。
図1は本発明の実施例に係る空気ノズルの構成を示し、(A)は横断面図、(B)は側断面図、図2は図1に示した空気ノズルの内筒の噴出孔配置を示し、(a)は図1(B)のa−a線断面図、(b)は図1(B)のb−b線断面図、図3は図1に示した空気ノズルの外筒の空気孔形状を示し、(a)は馬蹄形状、(b)は半円形状、(c)は矩形状を夫々示す図で、図4は流動床燃焼炉の全体構成を示す側断面図である。
Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention unless otherwise specified, but are merely illustrative examples. Not too much.
1A and 1B show a configuration of an air nozzle according to an embodiment of the present invention, where FIG. 1A is a cross-sectional view, FIG. 2B is a side cross-sectional view, and FIG. (A) is a sectional view taken along line aa in FIG. 1 (B), (b) is a sectional view taken along line bb in FIG. 1 (B), and FIG. 3 is an outer cylinder of the air nozzle shown in FIG. (A) is a horseshoe shape, (b) is a semicircular shape, (c) is a view showing a rectangular shape, and FIG. 4 is a side sectional view showing the overall configuration of the fluidized bed combustion furnace. is there.

本実施例の流動床燃焼炉にて処理される被処理物は、カットタイヤやスクリーン粕等のリサイクル燃料で、長尺状部位を有した不燃性異物を含むものである。異物としては、ステッチャ状異物、ワイヤ状異物等を含む。リサイクル燃料は、一旦製品化された後廃棄され、該廃棄物を焼却することにより熱等のエネルギーとして回収し有効利用することができる被処理物をいう。   An object to be processed in the fluidized bed combustion furnace of the present embodiment is a recycled fuel such as a cut tire or a screen soot, and includes non-combustible foreign matters having a long portion. Examples of the foreign matter include a stitcher-like foreign matter and a wire-like foreign matter. Recycled fuel refers to an object to be treated that can be discarded after it has been commercialized and can be recovered and used as energy, such as heat, by incinerating the waste.

最初に、図4を参照して本実施例の空気ノズルが設置される流動床燃焼炉の全体構成につき説明する。流動床燃焼炉20は、炉本体21と、該炉本体21の側壁に設けられリサイクル燃料を炉内に投入するリサイクル燃料投入口22と、同様に側壁に設けられ流動材を炉内に投入する流動材投入口23と、炉本体の底面を形成する炉底25と、該炉底25に接合され不燃性異物を外部へ抜き出す異物排出配管26と、該炉底25の下方に設けられた風箱27と、異物排出配管26に接続された搬出部28と、該搬出部28の下流側に設けられ流動材と異物を分離する分離機29と、を備える。炉底25には、後述する空気ノズルが多数突設されている。また、本実施例は、水平構造の炉底25に適しているが、傾斜構造の炉底25にも適用可能である。   Initially, with reference to FIG. 4, the whole structure of the fluidized-bed combustion furnace in which the air nozzle of a present Example is installed is demonstrated. The fluidized bed combustion furnace 20 is provided with a furnace main body 21, a recycled fuel inlet 22 provided on a side wall of the furnace main body 21 to input a recycled fuel into the furnace, and a fluidized material provided similarly on the side wall into the furnace. Fluidized material inlet 23, furnace bottom 25 forming the bottom of the furnace body, foreign matter discharge pipe 26 joined to the furnace bottom 25 for extracting non-combustible foreign matter, and wind provided below the furnace bottom 25 A box 27, a carry-out portion 28 connected to the foreign matter discharge pipe 26, and a separator 29 provided on the downstream side of the carry-out portion 28 to separate the fluidized material and the foreign matter. A large number of air nozzles, which will be described later, protrude from the furnace bottom 25. In addition, this embodiment is suitable for the furnace bottom 25 having a horizontal structure, but can also be applied to the furnace bottom 25 having an inclined structure.

このような流動床燃焼炉20では、被処理物を燃焼させる空間である燃焼室30の底部において、炉底25上の空気ノズルから炉内に空気が吹き込まれ、流動材を流動化させて、流動材が高温の状態で浮遊する流動床31が形成されている。リサイクル燃料投入口22から投入されたリサイクル燃料は、高温の流動材と接触して燃焼する。流動床31の空気は、空気供給口24から風箱27へ供給され、ここから多数の空気ノズルを介して炉内に供給される。
炉内の不燃性異物は、流動材の一部とともに異物排出配管26から抜き出される。異物と流動材とは、搬出部28により分離機29へ搬送された後に、分離機29で分別される。そして、流動材は再び流動材投入口23から炉本体21内に戻される。異物は他の処理施設へ移送される。
In such a fluidized bed combustion furnace 20, air is blown into the furnace from the air nozzle on the furnace bottom 25 at the bottom of the combustion chamber 30 which is a space for burning the workpiece, A fluidized bed 31 is formed in which the fluidized material floats in a high temperature state. The recycled fuel input from the recycled fuel inlet 22 comes into contact with the high-temperature fluidized material and burns. The air in the fluidized bed 31 is supplied from the air supply port 24 to the wind box 27 and is supplied into the furnace through a number of air nozzles.
Incombustible foreign matter in the furnace is extracted from the foreign matter discharge pipe 26 together with a part of the fluidized material. The foreign material and the fluidized material are conveyed to the separator 29 by the carry-out unit 28 and then separated by the separator 29. Then, the fluidized material is returned again from the fluidized material inlet 23 into the furnace body 21. The foreign matter is transferred to another processing facility.

次に、図1(A)、(B)及び図2を参照して、本実施例の特徴的構成となる空気ノズルについて説明する。
空気ノズル1は、円筒状の内筒2と外筒5からなる二重管構造を有している。
外筒5は、その下部が炉底25に接するように設けられ、上部が閉塞している。
内筒2は、炉底25を貫通して設けられ、下端側には風箱26に連通する開口部4が設けられている。内筒2の上端は、外筒5の上面に接合されている。
Next, with reference to FIGS. 1A, 1B, and 2, an air nozzle that is a characteristic configuration of the present embodiment will be described.
The air nozzle 1 has a double tube structure including a cylindrical inner cylinder 2 and an outer cylinder 5.
The outer cylinder 5 is provided such that the lower part thereof is in contact with the furnace bottom 25 and the upper part is closed.
The inner cylinder 2 is provided through the furnace bottom 25, and an opening 4 communicating with the wind box 26 is provided on the lower end side. The upper end of the inner cylinder 2 is joined to the upper surface of the outer cylinder 5.

内筒2の上部周面には、噴出孔3が穿設されている。該噴出孔3は、円周方向に沿って複数存在する。さらに、該噴出孔3は鉛直方向に複数段設けられる。噴出孔3は必要圧損確保のため複数段設けられる。このとき、上下に隣接する噴出孔3は、図2(a)、(b)に示されるように千鳥状に配置する。これにより、噴出孔の存在範囲の鉛直方向幅が小さくなり、噴出し流量のアンバランスを軽減でき、噴出孔3の下端から空気孔6までの空気流路7の距離を長くすることで、空気の整流効果も顕著となる。
噴出孔3の形状は、円形状、楕円形状、矩形状などが挙げられる。内筒2の噴出孔3の位置、数、形状及び開口面積は、主として炉底25と燃焼室30との間に所定の圧損を生じさせるように設計で決定される。
A jet hole 3 is formed in the upper peripheral surface of the inner cylinder 2. A plurality of the ejection holes 3 exist along the circumferential direction. Further, the ejection holes 3 are provided in a plurality of stages in the vertical direction. The ejection holes 3 are provided in a plurality of stages to ensure the necessary pressure loss. This and can, injection holes 3 adjacent the upper bottom, the FIG. 2 (a), staggered as shown in (b). As a result, the vertical width of the existence range of the ejection holes is reduced, the imbalance of the ejection flow rate can be reduced, and the distance of the air flow path 7 from the lower end of the ejection holes 3 to the air holes 6 is increased. The rectifying effect is also remarkable.
Examples of the shape of the ejection hole 3 include a circular shape, an elliptical shape, and a rectangular shape. The position, number, shape, and opening area of the ejection hole 3 of the inner cylinder 2 are determined by design so that a predetermined pressure loss is mainly generated between the furnace bottom 25 and the combustion chamber 30.

外筒5の下部周面には、複数の空気孔6が穿設されている。該空気孔6は下縁が直線状であり、該下縁が炉底25の上面と同一面上に位置する。また、該空気孔6は外筒5の円周方向に沿って所定ピッチ間隔Pで複数存在する。外筒5の孔部6の位置、数、形状及び開口面積は、主として燃焼室30へ噴出すジェット流が所定ジェット長となるように設計で決定される。
風箱26より開口部4を介して内筒2内に供給された空気は、内筒2内を上昇し、噴出孔3より外筒5内へ噴出する。噴出孔3では必要圧損確保が行われる。さらに、外筒5内に噴出した空気は、外筒5の内周面と内筒2の外周面で形成された空気流路7を下降し、空気孔6を介して燃焼室へ向けて水平方向に噴出し、燃焼室底部に充填された流動材を流動化する。
本構成によれば、外筒5の空気孔6下縁と炉底25の上面を一致させているため、空気ノズル1内のポケットをなくすことができ、燃焼室内で発生したステッチャ状異物が空気孔6に絡み付くことなく円滑に排出され、該ステッチャ状異物が空気孔6近傍に滞留、蓄積することを防げる。
A plurality of air holes 6 are formed in the lower peripheral surface of the outer cylinder 5. The air pores 6 are lower edge straight, lower edge located on the upper surface and the same surface of the furnace bottom 25. A plurality of the air holes 6 exist at a predetermined pitch interval P along the circumferential direction of the outer cylinder 5. The position, number, shape and opening area of the hole 6 of the outer cylinder 5 are determined by design so that the jet flow ejected mainly into the combustion chamber 30 has a predetermined jet length.
Air supplied from the wind box 26 into the inner cylinder 2 through the opening 4 rises in the inner cylinder 2 and is ejected into the outer cylinder 5 from the ejection hole 3. Necessary pressure loss is ensured in the ejection hole 3. Further, the air jetted into the outer cylinder 5 descends the air flow path 7 formed by the inner peripheral surface of the outer cylinder 5 and the outer peripheral surface of the inner cylinder 2 and is horizontally directed toward the combustion chamber via the air holes 6. The fluidized material ejected in the direction and filled in the bottom of the combustion chamber is fluidized.
According to this configuration, since the lower edge of the air hole 6 of the outer cylinder 5 and the upper surface of the furnace bottom 25 are matched, the pocket in the air nozzle 1 can be eliminated, and the stitcher-like foreign matter generated in the combustion chamber is air. The holes 6 are smoothly discharged without being entangled with the holes 6, and the stitcher-like foreign matters can be prevented from staying and accumulating in the vicinity of the air holes 6.

また、外筒5に穿設された空気孔6の形状は、図3(a)に示される馬蹄形状、(b)に示される半円形状、(c)に示される矩形状、などが挙げられるが、本発明では馬蹄形状、半円形状等のように空気孔6の上縁が曲率線状であるとよい。このように、曲率線状とすると加工が容易となり製造コストが低減できる。また、空気孔3のピッチ間隔Pが短い部位が少なくなり、ステッチャ状異物が空気孔間を挟み込んで固定されることを抑制できる。
さらに、外筒5の空気孔6のピッチ間隔Pが、リサイクル燃料に含まれるステッチャ状異物の平均長さよりも大であることが好ましい。これにより、空気孔間を挟み込んでステッチャ状異物が固定されることを防止でき、延いては空気ノズル周辺の異物堆積を防止可能である。このとき、外筒5の空気孔6のピッチ間隔Pが、10〜30mmであることがよい。一般に用いられているステッチャは、端部が折れ曲がった状態で図8に示す長辺長さLsが20〜40mm程度のものが多い。従って、ピッチ間隔Pを10〜30mmとすることで、ステッチャの開き幅よりもピッチ間隔が大きくなり、これらのステッチャが空気孔間に絡みつくことを防止できる。
Moreover, the shape of the air hole 6 drilled in the outer cylinder 5 includes a horseshoe shape shown in FIG. 3A, a semicircular shape shown in FIG. 3B, a rectangular shape shown in FIG. However, in the present invention, it is preferable that the upper edge of the air hole 6 has a curved line shape such as a horseshoe shape or a semicircular shape. As described above, when the shape is a curved line, the processing becomes easy and the manufacturing cost can be reduced. Moreover, the site | part with the short pitch interval P of the air hole 3 decreases, and it can suppress that a stitcher-like foreign material pinches | interposes between air holes and is fixed.
Furthermore, it is preferable that the pitch interval P of the air holes 6 of the outer cylinder 5 is larger than the average length of the stitcher-like foreign matters contained in the recycled fuel. As a result, it is possible to prevent the stitcher-like foreign matter from being pinched between the air holes, and thus to prevent foreign matter accumulation around the air nozzle. At this time, the pitch interval P between the air holes 6 of the outer cylinder 5 is preferably 10 to 30 mm. Many stitchers that are generally used have a long side length Ls of about 20 to 40 mm shown in FIG. Therefore, by setting the pitch interval P to 10 to 30 mm, the pitch interval becomes larger than the opening width of the stitcher, and the stitcher can be prevented from being entangled between the air holes.

本実施例の空気ノズル1を備えた流動床燃焼炉20を用いて運転を行った時の異物滞留状態を把握するために以下のような試験を行った。
スクリーンかすから発生するステッチャ及びカットタイヤから発生するワイヤを対象に、本実施例にて説明した図1及び図2の空気ノズル1と、比較例として図7及び図8の空気ノズル51を用いて、流動床内での分散試験及び系外への排出試験を行い、夫々を比較することにより本実施例の分散性能向上を確認した。
本実施例では外筒5の空気孔6の形状は馬蹄形(図3(a)参照)とし、比較例では円形を採用した。
In order to grasp the foreign material staying state when the fluidized bed combustion furnace 20 provided with the air nozzle 1 of the present embodiment was operated, the following test was performed.
Targeting wire generated from stitcher and cut the tire generated from the screen dregs, as in FIG. 1 and the air nozzle 1 of FIG. 2 described in this embodiment, the air nozzle 51 in FIGS. 7 and 8 as comparative examples using Then, the dispersion test in the fluidized bed and the discharge test to the outside of the system were conducted, and the improvement of the dispersion performance of this example was confirmed by comparing each of them.
In the present embodiment, the shape of the air hole 6 of the outer cylinder 5 is a horseshoe shape (see FIG. 3A), and a circular shape is employed in the comparative example.

試験機には、図4と同様の構成を有し、約幅0.8m×奥行き1.0m×高さ4mの流動床燃焼炉コールドモデルを用いた。空気ノズルから流動床内に供給する空気は常温とする。流動床31の静止砂高h(図4参照)800mmに対して、所定濃度となる量の不燃性異物(ワイヤ及びステッチャ)をある時間間隔ごとに炉内へ投入し、全量投入後所定時間の間分散させ、流動床を高さ方向hで4区画に分割し、該当する区画ごとの流動砂を掘り出し、そこに分布する異物重量を計測して、流動床内の不燃物分布を調べた。   As the test machine, a fluid bed combustion furnace cold model having the same configuration as that of FIG. 4 and having a width of about 0.8 m × depth of 1.0 m × height of 4 m was used. The air supplied from the air nozzle into the fluidized bed is at room temperature. For a static sand height h (see FIG. 4) of 800 mm in the fluidized bed 31, a non-combustible foreign substance (wire and stitcher) of a predetermined concentration is introduced into the furnace at certain time intervals, and after a total amount of The fluidized bed was divided into four sections in the height direction h, fluidized sand for each corresponding section was dug, and the weight of foreign matter distributed there was measured to examine the distribution of incombustible materials in the fluidized bed.

試験結果を図5及び図6に示す。図5は、本実施例と比較例における異物の分布状態を示すグラフで、(a)は異物がステッチャの場合、(b)は異物がワイヤの場合を示す。
図5(a)に示されるように異物がステッチャの場合、比較例では最下層の相対濃度比が極めて高く、炉底部にステッチャが滞留、蓄積していることがわかる。図6(a)に、比較例における流動材排出後の炉底部の写真を示す。この写真からも明らかなように、ステッチャは空気ノズル近傍に多量に残存している。
一方、本実施例では、何れの層高においてもステッチャの相対濃度比は1に近い値であり、ステッチャの偏析が少ないことがわかる。即ち、本実施例によれば均一で適正な分散状態が得られることが判明した。図6(b)に本実施例における流動材排出後の炉底部の写真を示す。これによれば、図6(a)に比べて炉底でのステッチャの残存がなく、運転時にステッチャが適正に図4の異物排出管路26から排出されることがわかる。
The test results are shown in FIGS. 5A and 5B are graphs showing the distribution state of foreign matter in the present example and the comparative example. FIG. 5A shows a case where the foreign matter is a stitcher, and FIG. 5B shows a case where the foreign matter is a wire.
As shown in FIG. 5A, when the foreign matter is a stitcher, the comparative example has a very high relative concentration ratio in the lowermost layer, and it can be seen that the stitcher stays and accumulates at the bottom of the furnace. FIG. 6A shows a photograph of the bottom of the furnace after discharging the fluidized material in the comparative example. As is apparent from this photograph, a large amount of the stitcher remains in the vicinity of the air nozzle.
On the other hand, in this embodiment, the relative density ratio of the stitcher is a value close to 1 at any layer height, and it can be seen that the segregation of the stitcher is small. That is, it has been found that a uniform and proper dispersion state can be obtained according to this example. FIG. 6B shows a photograph of the bottom of the furnace after discharging the fluidized material in this example. According to this, it can be seen that the stitcher does not remain at the bottom of the furnace as compared with FIG. 6A, and the stitcher is properly discharged from the foreign matter discharge conduit 26 of FIG. 4 during operation.

また、図5(b)に示されるように異物がワイヤの場合、実施例及び比較例ともに何れの区画でも相対濃度比が1に近く、比較的異物分散状態が良好であることがわかるが、本実施例の方が比較例に比べて直線状に分布し、比較例よりも異物の分布が均等となっている。従って、ワイヤにおいても本実施例が適用できるといえる。
これらの試験結果から、本実施例の構成を採用することによりステッチャやワイヤの異物が炉底部に蓄積すること無く、且つ分散状態が良好になることが明らかとなった。
In addition, when the foreign substance is a wire as shown in FIG. 5B, it can be seen that the relative concentration ratio is close to 1 in both sections in both the example and the comparative example, and the foreign substance dispersion state is relatively good. In this example, the distribution is more linear than in the comparative example, and the distribution of foreign matter is more uniform than in the comparative example. Therefore, it can be said that the present embodiment can also be applied to the wire.
These test results, foreign matter stitcher and wire ya By adopting the configuration of this embodiment is not to accumulate in the furnace bottom, and the dispersion state, it became clear that the better.

本発明の実施例に係る空気ノズルの構成を示し、(A)は横断面図、(B)は側断面図である。The structure of the air nozzle which concerns on the Example of this invention is shown, (A) is a cross-sectional view, (B) is a sectional side view. 図1に示した空気ノズルの内筒の噴出孔配置を示し、(a)は図1(B)のa−a線断面図、(b)は図1(B)のb−b線断面図である。1 shows the arrangement of the ejection holes of the inner cylinder of the air nozzle shown in FIG. 1, (a) is a sectional view taken along the line aa in FIG. 1 (B), and (b) is a sectional view taken along the line bb in FIG. It is. 図1に示した空気ノズルの外筒の空気孔形状を示し、(a)は馬蹄形状、(b)は半円形状、(c)は矩形状を夫々示す図である。The air hole shape of the outer cylinder of the air nozzle shown in FIG. 1 is shown, (a) shows a horseshoe shape, (b) shows a semicircular shape, and (c) shows a rectangular shape. 流動床燃焼炉の全体構成を示す側断面図である。It is a sectional side view which shows the whole structure of a fluidized bed combustion furnace. 分散試験にて得られた本実施例と比較例における異物の分布状況を示すグラフで、(a)は異物がステッチャの場合、(b)は異物がワイヤの場合を示す。It is a graph which shows the distribution condition of the foreign material in a present Example and comparative example obtained by the dispersion | distribution test, (a) shows the case where a foreign material is a stitcher, (b) shows the case where a foreign material is a wire. 分散試験後の炉底部の状態を示す写真で、(a)は比較例、(b)は本実施例である。It is the photograph which shows the state of the furnace bottom part after a dispersion test, (a) is a comparative example, (b) is a present Example. 従来の空気ノズルの側断面図である。It is a sectional side view of the conventional air nozzle. 図7の空気ノズルの横断面を示し、(a)は図7のc−c線断面図、(b)はd−d線断面図である。7 is a cross-sectional view of the air nozzle of FIG. 7, (a) is a cross-sectional view taken along the line cc of FIG. 7, and (b) is a cross-sectional view taken along the line dd.

1 空気ノズル
2 内筒
3、3a、3b 噴出孔
5 外筒
6 空気孔
7 空気流路
10 炉底
20 流動床燃焼炉
25 炉底
26 異物排出配管
27 風箱
28 搬出部
29 分離機
30 燃焼室
31 流動床
DESCRIPTION OF SYMBOLS 1 Air nozzle 2 Inner cylinder 3, 3a, 3b Ejection hole 5 Outer cylinder 6 Air hole 7 Air flow path 10 Furnace bottom 20 Fluidized bed combustion furnace 25 Furnace bottom 26 Foreign matter discharge piping 27 Air box 28 Unloading part 29 Separator 30 Combustion chamber 31 Fluidized bed

Claims (1)

ステッチャ状異物からなる長尺状部位を有した不燃性異物を含むリサイクル燃料を処理対象とした流動床燃焼炉の空気ノズル構造であって、前記空気ノズルは燃焼室炉底に多数配設され、該空気ノズルは内筒と外筒からなる二重管構造を有し、前記内筒の周面上方に圧損調整機能を有する噴出孔が穿設されるとともに、前記外筒の周面下方に空気孔が穿設された流動床燃焼炉の空気ノズル構造において、
前記外筒の空気孔は、上縁が曲率線状で且つ下縁が直線状の馬蹄形状若しくは半円形状で且つ直線状の下縁前記炉底の上面と同一面上に位置させ
更に該空気孔は外筒の円周方向に複数存在し、該空気孔のピッチ間隔が、10〜30mmであり、
一方前記内筒の噴出孔が円周方向に沿って複数存在するとともに、該噴出孔が鉛直方向に複数段の噴出孔を設け、該上下に隣接する噴出孔は、千鳥状に配置することを特徴とする流動床燃焼炉の空気ノズル構造。
An air nozzle structure of a fluidized bed combustion furnace intended for treating recycled fuel containing non-combustible foreign matter having an elongated portion made of stitcher-like foreign matter , wherein a large number of the air nozzles are arranged at the bottom of the combustion chamber furnace, The air nozzle has a double-pipe structure composed of an inner cylinder and an outer cylinder. A blow hole having a pressure loss adjusting function is formed above the circumferential surface of the inner cylinder, and air is disposed below the circumferential surface of the outer cylinder. In the air nozzle structure of a fluidized bed combustion furnace with holes,
Air hole of the outer cylinder, and the upper edge with a curvature linear lower edge is to position the and the straight lower edge straight horseshoe shape or a semicircular shape on the upper surface and the same surface of the furnace bottom,
Furthermore the air pores Mashimashi multiple exist in the circumferential direction of the outer cylinder, the pitch spacing of the air pores is 10 to 30 mm,
On the other hand, there are a plurality of ejection holes of the inner cylinder along the circumferential direction, the ejection holes are provided with a plurality of ejection holes in the vertical direction, and the ejection holes adjacent to the upper and lower sides are arranged in a staggered manner. The air nozzle structure of the fluidized bed combustion furnace.
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KR101273312B1 (en) * 2011-08-23 2013-06-11 한국에너지기술연구원 Fluidized bed combustion apparatus with stair type air supplier

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JP6385799B2 (en) * 2014-11-10 2018-09-05 株式会社Ihi環境エンジニアリング Combustion air supply method and apparatus
CN111720817A (en) * 2020-06-23 2020-09-29 杭州航民小城热电有限公司 Hood structure and circulating fluidized bed air supply system
CN111780098B (en) * 2020-07-24 2024-05-10 中国科学院工程热物理研究所 Air distribution device, combustion system and solid material treatment equipment

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JPS60139113U (en) * 1984-02-20 1985-09-14 バブコツク日立株式会社 Fluidized bed combustion equipment with improved fluidity
JPH01111110A (en) * 1987-10-23 1989-04-27 Babcock Hitachi Kk Dispersion plate nozzle for fluidized-bed type combustion apparatus
JP2000088225A (en) * 1998-09-17 2000-03-31 Hitachi Zosen Corp Large type fluidized bed incinerator
JP2005226870A (en) * 2004-02-10 2005-08-25 Mitsubishi Heavy Ind Ltd Fluidized bed incinerator

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JPS60139113U (en) * 1984-02-20 1985-09-14 バブコツク日立株式会社 Fluidized bed combustion equipment with improved fluidity
JPH01111110A (en) * 1987-10-23 1989-04-27 Babcock Hitachi Kk Dispersion plate nozzle for fluidized-bed type combustion apparatus
JP2000088225A (en) * 1998-09-17 2000-03-31 Hitachi Zosen Corp Large type fluidized bed incinerator
JP2005226870A (en) * 2004-02-10 2005-08-25 Mitsubishi Heavy Ind Ltd Fluidized bed incinerator

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101273312B1 (en) * 2011-08-23 2013-06-11 한국에너지기술연구원 Fluidized bed combustion apparatus with stair type air supplier

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