JP2009192176A - Vertical kiln - Google Patents

Vertical kiln Download PDF

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JP2009192176A
JP2009192176A JP2008034948A JP2008034948A JP2009192176A JP 2009192176 A JP2009192176 A JP 2009192176A JP 2008034948 A JP2008034948 A JP 2008034948A JP 2008034948 A JP2008034948 A JP 2008034948A JP 2009192176 A JP2009192176 A JP 2009192176A
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solid fuel
raw material
pipe
furnace
fuel supply
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JP5436784B2 (en
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Tatsu Chisaki
達 地崎
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Chisaki Co Ltd
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Chisaki Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a vertical kiln distributing solid fuel in raw material and capable of supplying it on a hearth. <P>SOLUTION: A raw material storage tank 1 arranged in an upper position of a lid wall 16 in an exterior is connected to a raw material supply opening via a plurality of raw material supply pipes 3, a fuel supply apparatus is connected to a fuel supply opening of the lid wall 16, the fuel supply apparatus has a fluid fuel supply apparatus and a solid fuel supply apparatus, the fluid fuel supply apparatus is connected to a fluid fuel supply opening 23 formed in a furnace lid part 20, the solid fuel supply apparatus has solid fuel drop pipes 11, 12 suspended from a force feed pipe at plural positions in a force feed direction of the force feed pipe 6, the solid fuel drop pipe 12 of a force feed direction downstream end side position is pierced through the raw material storage tank 1 and connected to a solid fuel supply opening of the furnace lid part, each of the other solid fuel drop pipes 11 is penetratingly arranged in the raw material storage tank 1, and lower end openings are positioned above corresponding upper end openings of the raw material supply pipe 3 in the raw material storage tank 1. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、竪型焼成炉装置に関する。   The present invention relates to a vertical firing furnace apparatus.

竪型焼成炉装置としては、例えば、特許文献1に開示されている装置が知られている。この特許文献1では、炉内空間を、炉床より上方を予熱空間、そして炉床より下方へ延びる炉本体の空間内を焼成空間としている。焼成されるべき原料は、炉床で堆積され、燃焼室に面する堆積層の自由表面が、炉蓋に設けられたバーナから燃焼室へ噴出される液体燃料の燃焼による燃焼ガスから熱を受けると共に、そして焼成空間を上昇し上記自由表面から堆積層内に進入し透過する高温ガスから熱を受けることにより、予熱される。この予熱は主として上記自由表面側からなされる。予熱された原料はプッシャー等により上記自由表面側から順次炉床の中央に形成された落下開口に落下して上記焼成空間で再び堆積層をなし、ここで焼成される。   As a vertical firing furnace apparatus, for example, an apparatus disclosed in Patent Document 1 is known. In Patent Document 1, the furnace space is defined as a preheating space above the hearth and a space of the furnace body extending downward from the hearth as a firing space. The raw material to be fired is deposited on the hearth, and the free surface of the deposited layer facing the combustion chamber receives heat from the combustion gas from the combustion of the liquid fuel ejected from the burner provided on the furnace lid to the combustion chamber At the same time, it is preheated by receiving heat from a hot gas that rises in the firing space and enters the deposition layer from the free surface and permeates. This preheating is mainly performed from the free surface side. The preheated raw material falls from the free surface side to the drop opening formed in the center of the hearth by the pusher or the like to form a deposited layer again in the firing space, and is fired here.

このような特許文献1にあっては、バーナからの液体燃料は燃焼室内へ噴射される。したがって、燃焼は燃焼室内で行われ、原料は自由表面で加熱を受けて予熱される。又、特許文献1では、燃料として、液体燃料に加え、固体燃料をも使用可能としている。固体燃料の供給口は、バーナに隣接して炉蓋に設けられている。この固体燃料を併せて用いる例の場合でも、該固体燃料は燃焼室内へ供給されるので、固体燃料は液体燃料と共に、上記燃焼室内で燃焼して炉床上の原料の堆積層を自由表面から加熱する。
特開平08−337447
In such Patent Document 1, the liquid fuel from the burner is injected into the combustion chamber. Accordingly, combustion is performed in the combustion chamber, and the raw material is preheated by being heated on the free surface. Moreover, in patent document 1, in addition to liquid fuel, solid fuel can also be used as fuel. The solid fuel supply port is provided in the furnace lid adjacent to the burner. Even in the case of using this solid fuel together, the solid fuel is supplied into the combustion chamber, so the solid fuel is burned together with the liquid fuel in the combustion chamber to heat the deposited layer of the raw material on the hearth from the free surface. To do.
JP 08-337447 A

しかしながら、特許文献1にあっては、炉床上の原料の堆積層は、その自由表面側が燃焼ガスに面しているために層内部にくらべて高く加熱されるので、自由表面側と層内部とでは温度差が大きい。   However, in Patent Document 1, the raw material deposition layer on the hearth is heated higher than the inside of the layer because the free surface side faces the combustion gas. The temperature difference is large.

この温度差はなるべく小さい方が好ましい。例えば、プッシャー等により原料は押されて自由表面側から逐次落下するが、落下量が多いと、自由表面よりも少し内部の原料であっても、十分に予熱されないうちに落下してしまうことにもなりかねない。すると、予熱不足、温度のムラという問題を生ずる。   This temperature difference is preferably as small as possible. For example, the raw material is pushed by the pusher etc. and falls sequentially from the free surface side, but if the amount of fall is large, even if the raw material is slightly inside the free surface, it will fall before it is sufficiently preheated It can be. As a result, problems such as insufficient preheating and uneven temperature occur.

そこで、固体燃料を予め原料に混合しておいて、混合物として炉床上に供給し、堆積層内の固体燃料を燃焼させて、堆積層の自由表面からの加熱に加え堆積層内でも固体燃料の燃焼により原料を加熱させる方法が考えられる。しかし、炉床へ原料を供給する前の工程で上記固体燃料を原料に混合するには、大がかりな混合装置を必要とする。又、混合物を炉床に向けて移送する間に、原料と固体燃料の粒径差そして比重量差によって、混合物内で固体燃料が偏在して均一に分散しなくなる虞れがある。   Therefore, the solid fuel is mixed with the raw material in advance, supplied as a mixture onto the hearth, the solid fuel in the deposited layer is burned, and in addition to heating from the free surface of the deposited layer, the solid fuel is also contained in the deposited layer. A method of heating the raw material by combustion is conceivable. However, in order to mix the solid fuel with the raw material in the step before supplying the raw material to the hearth, a large mixing device is required. Further, during the transfer of the mixture toward the hearth, there is a possibility that the solid fuel is unevenly distributed in the mixture and is not uniformly dispersed due to a difference in particle size and specific weight between the raw material and the solid fuel.

本発明は、このような事情に鑑み、固体燃料を流体燃料と共に燃焼室で燃焼させると共に、固体燃料を原料内に混合させて原料の堆積層内でも燃焼させ、しかも、堆積層内での固体燃料を原料内に均一に分散させることのできる竪型焼成炉装置を提供することを課題とする。   In view of such circumstances, the present invention burns solid fuel together with fluid fuel in the combustion chamber, mixes the solid fuel into the raw material and burns it in the raw material deposition layer, and solids in the deposition layer. It is an object of the present invention to provide a vertical firing furnace apparatus that can uniformly disperse fuel in a raw material.

本発明に係る竪型焼成炉装置は、竪型の炉本体の上部で該炉本体の鉛直中心線に対して半径方向に延び半径方向中央域に落下開口が形成された環板状の炉床を有し、該炉床と、炉床外周縁位置で上方に延びる筒壁と、該筒壁の上端を塞ぐ蓋壁とで囲まれた空間により予熱空間を形成し、上記炉床の落下開口内縁から垂下する炉本体内に焼成空間を形成し、上記蓋壁が半径方向外側領域部をなす環状の天板部と該天板部より半径方向内側領域部をなす炉蓋部とを有し、炉外にて上記蓋壁の上方位置に配設された原料貯留槽が、槽底から垂下する複数の原料供給管を経て、天板部の原料供給口に接続され、炉外に設けられた燃料供給装置が蓋壁の燃料供給口に接続されている。   A vertical firing furnace apparatus according to the present invention includes an annular plate-shaped hearth that extends in the radial direction with respect to the vertical center line of the vertical furnace body and has a drop opening formed in the central area in the radial direction. A preheat space is formed by a space surrounded by the hearth, a cylindrical wall extending upward at the outer peripheral edge of the hearth, and a lid wall that closes an upper end of the cylindrical wall, and a drop opening of the hearth A firing space is formed in the furnace body depending from the inner edge, and the lid wall has an annular top plate portion forming a radially outer region portion and a furnace lid portion forming a radially inner region portion from the top plate portion. The raw material storage tank disposed at the upper position of the lid wall outside the furnace is connected to the raw material supply port of the top plate portion through a plurality of raw material supply pipes hanging from the tank bottom, and is provided outside the furnace. A fuel supply device connected to the fuel supply port of the lid wall.

かかる竪型焼成炉装置において、本発明では、燃料供給装置は、流体燃料供給装置と固体燃料供給装置とを有し、流体燃料供給装置は蓋壁中央部の炉蓋部に形成された流体燃料供給口に接続され、固体燃料供給装置は、固体燃料供給源から延びる圧送管の圧送方向複数位置に該圧送管から垂下する固体燃料落下管を有し、圧送方向下流端側位置の固体燃料落下管が、上記炉蓋部の固体燃料供給口に接続され、他の各固体燃料落下管は原料貯留槽内に突入配置され、下端開口が原料貯留槽内で対応する原料供給管の上端開口の上方に位置していることを特徴としている。本発明において、流体燃料とは液体燃料と気体燃料の少なくとも一方を有する燃料をいう。   In such a vertical firing furnace apparatus, in the present invention, the fuel supply apparatus includes a fluid fuel supply apparatus and a solid fuel supply apparatus, and the fluid fuel supply apparatus is a fluid fuel formed in the furnace lid portion at the center of the lid wall. The solid fuel supply device, connected to the supply port, has a solid fuel dropping pipe that hangs down from the pumping pipe at a plurality of positions in the pumping direction of the pumping pipe extending from the solid fuel supply source, and the solid fuel falling at the downstream end position in the pumping direction A pipe is connected to the solid fuel supply port of the furnace lid, each other solid fuel dropping pipe is rushed into the raw material storage tank, and the lower end opening is the upper end opening of the corresponding raw material supply pipe in the raw material storage tank. It is characterized by being located above. In the present invention, fluid fuel refers to fuel having at least one of liquid fuel and gaseous fuel.

このような構成の本発明によると、流体燃料は、炉蓋部に設けられた流体燃料供給口、例えばバーナから噴射されて、炉蓋部の直下に形成される燃焼室で燃焼する。   According to the present invention having such a configuration, fluid fuel is injected from a fluid fuel supply port provided in the furnace lid portion, for example, a burner, and burns in a combustion chamber formed immediately below the furnace lid portion.

一方、固体燃料は、圧送管内で圧送されて、圧送方向上流側の固体燃料落下管から順に該固体燃料落下管に落下する。圧送方向下流端側の固体燃料落下管を除いた、他の固体燃料落下管はその下端開口が原料貯留槽内で原料供給管の上端開口の上方に位置しているので、上記固体燃料落下管の下端開口から落下する固体燃料は、該下端開口の周囲で槽内底部にて原料供給管へ導入される原料により固体燃料落下管から引き出されるようにして原料と共に原料供給管内を落下し、炉床上に原料と混合された状態で堆積層をなす。圧送される固体燃料は、圧送中に順次固体燃料落下管を落下した後も残余分があり、これは炉蓋部に位置する下流端側の固体燃料落下管から落下する。かくして、圧送された固体燃料はすべて、固体燃料落下管から落下する。   On the other hand, the solid fuel is pumped in the pumping pipe and falls into the solid fuel dropping pipe in order from the solid fuel dropping pipe on the upstream side in the pumping direction. Since the lower end opening of the other solid fuel dropping pipes, excluding the solid fuel dropping pipe on the downstream end side in the pumping direction, is located above the upper end opening of the raw material supply pipe in the raw material storage tank, The solid fuel falling from the lower end opening of the gas is dropped in the raw material supply pipe together with the raw material so as to be drawn out from the solid fuel dropping pipe by the raw material introduced into the raw material supply pipe at the bottom of the tank around the lower end opening. A deposited layer is formed on the floor while being mixed with the raw material. The solid fuel to be pumped remains even after the solid fuel dropping pipe is sequentially dropped during the pumping, and it falls from the solid fuel dropping pipe on the downstream end side located in the furnace cover. Thus, all of the pumped solid fuel falls from the solid fuel drop tube.

したがって、炉蓋部に位置する圧送方向下流端側の固体燃料落下管から落下する固体燃料は、炉蓋部直下に形成される燃焼室へ供給されることとなり、該燃焼室で流体燃料と共に燃焼し、炉床上の原料と固体燃料の混合物をその堆積層の自由表面側から加熱する。   Therefore, the solid fuel falling from the solid fuel dropping pipe on the downstream end side in the pumping direction located in the furnace lid is supplied to the combustion chamber formed immediately below the furnace lid, and combusted together with the fluid fuel in the combustion chamber. Then, the mixture of the raw material and the solid fuel on the hearth is heated from the free surface side of the deposited layer.

上記下流端側の固体燃料落下管よりも上流側の固体燃料落下管から落下した固体燃料は、上述のごとく、炉床上の混合物の堆積層内に存在しており、該堆積層内で燃焼し原料を堆積層内で加熱する。   As described above, the solid fuel that has fallen from the solid fuel dropping pipe on the upstream side of the solid fuel dropping pipe on the downstream end side exists in the deposited layer of the mixture on the hearth, and burns in the deposited layer. The raw material is heated in the deposited layer.

かくして、堆積層をなす原料は、自由表面側からそして内部から加熱され、熱効率よく、しかも堆積層全体でほぼ均一に混合された状態で予熱される。   Thus, the raw material forming the deposited layer is heated from the free surface side and from the inside, and is preheated in a thermally efficient and almost uniformly mixed state throughout the deposited layer.

本発明では、圧送方向下流端側の固体燃料落下管以外の固体燃料落下管から落下する固体燃料は、上述のように、原料貯留槽内にて、該固体燃料落下管の下端開口の周囲で落下する原料に引き出されるように落下するので、原料の落下量が多いときには、固体燃料も落下量が多くなり、きわめて、混合比が安定する。しかも、原料と固体燃料は同じ原料供給管を落下するので、炉床上では、両者は混合されてきわめて均一に分布する。   In the present invention, the solid fuel falling from the solid fuel drop pipe other than the solid fuel drop pipe on the downstream end side in the pumping direction is, as described above, around the lower end opening of the solid fuel drop pipe in the raw material storage tank. Since it falls so as to be drawn out by the falling raw material, when the amount of the raw material falls is large, the solid fuel also falls and the mixing ratio is extremely stable. Moreover, since the raw material and the solid fuel fall through the same raw material supply pipe, they are mixed and distributed extremely uniformly on the hearth.

本発明において、原料供給管は炉本体の鉛直中心線まわりの周方向の複数位置に設けられ、圧送管は上記原料供給管の上方位置で上記周方向に延びる周回部と、該圧送管の下流端側で半径内方に向って、炉蓋部の固体燃料供給口に接続されている固体燃料落下管に至る半径方向部と、上記周回部上流端と固体燃料供給源とを接続する圧送上流部とを有しているようにすることができる。かかる構成では、圧送される固体燃料は周回部で圧送されているときに、該周回部から順次、固体燃料落下管そして原料供給管を経て原料と共に炉床上に落下し、又、下流端側では半径方向部から固体燃料落下管を経て燃焼室へ落下供給される。   In the present invention, the raw material supply pipes are provided at a plurality of positions in the circumferential direction around the vertical center line of the furnace main body, the pressure feed pipe is a circumferential portion extending in the circumferential direction above the raw material supply pipe, and a downstream of the pressure feed pipe On the end side, radially inward, reaching the solid fuel drop pipe connected to the solid fuel supply port of the furnace lid, and the upstream of pumping connecting the upstream end of the circulating portion and the solid fuel supply source Part. In such a configuration, when the solid fuel to be pumped is pumped in the circulating section, the solid fuel falls on the hearth together with the raw material sequentially from the circulating section through the solid fuel dropping pipe and the raw material supply pipe, and at the downstream end side. The gas is supplied to the combustion chamber from the radial direction through the solid fuel dropping pipe.

本発明において、原料貯留槽内に突入せる固体燃料落下管は下端開口もしくはその直上位置で半径外方に突出するフランジ状の抵抗部を有していることが好ましい。上記固体燃料落下管は、その下端開口が原料貯留槽内の原料中に位置するが、上記抵抗部の直下には原料不存在の空間が形成されるので、上記下端開口からの固体燃料の落下は円滑になされる。   In the present invention, it is preferable that the solid fuel dropping pipe that enters into the raw material storage tank has a flange-shaped resistance portion that protrudes radially outward at the lower end opening or at a position immediately above the lower end opening. The lower end opening of the solid fuel dropping pipe is located in the raw material in the raw material storage tank, but since a space without raw material is formed immediately below the resistance portion, the solid fuel falls from the lower end opening. Is done smoothly.

本発明において、圧送方向下流端側位置の固体燃料落下管の下端開口が、流体燃料供給口を有するインジェクタに接続され、該インジェクタで固体燃料と流体燃料が混合されて炉内に噴射されるようになっているようにすることができる。こうすることにより、インジェクタから噴出されるときには、すでに固体燃料と流体燃料は混合されていて燃焼が安定する。   In the present invention, the lower end opening of the solid fuel dropping pipe at the downstream end position in the pumping direction is connected to an injector having a fluid fuel supply port so that the solid fuel and the fluid fuel are mixed and injected into the furnace by the injector. It can be made to be. By doing so, when the fuel is ejected from the injector, the solid fuel and the fluid fuel are already mixed and the combustion is stabilized.

上記インジェクタを設ける場合、固体燃料落下管の下端開口は、インジェクタの噴射方向を中心線とする円周に対して接線方向に開口していることが好ましい。こうすることにより、燃焼室内の燃焼ガスは旋回流を生じ、燃焼室内で広い範囲にわたり均一な燃焼がなされる。   When the injector is provided, the lower end opening of the solid fuel dropping pipe is preferably opened in a tangential direction with respect to a circumference having the injection direction of the injector as a center line. By doing so, the combustion gas in the combustion chamber generates a swirling flow, and uniform combustion is performed over a wide range in the combustion chamber.

本発明において、圧送管は、周回部における固体燃料落下管の上端開口位置にて、圧送される固体燃料の流れに対して抵抗を与えると共に上記状端開口への固体燃料の落下を促進せしめる落下促進装置を有していることが好ましい。この落下促進装置としては、種々の形態が考えられる。例えば、上記上端開口の下流側縁部位置に、圧送されている固体燃料の流れの一部を受け止めて上記上端開口へ案内する抵抗板、あるいは上記流れを一時的に完全に止めるように閉じてから再び開放されるダンパ部材、さらには、固体燃料落下管を定期的あるいは常時振動させて固体燃料の落下を促進せしめる振動部材とすることができる。   In the present invention, the pressure feeding pipe falls at the upper end opening position of the solid fuel dropping pipe in the circulating portion to provide resistance to the flow of the solid fuel to be pumped and promote the fall of the solid fuel to the above-mentioned end opening. It is preferable to have a promotion device. Various forms are conceivable as the drop promoting device. For example, at the downstream edge position of the upper end opening, a part of the flow of the solid fuel being pumped is received and guided to the upper end opening, or closed so that the flow is temporarily stopped. Further, the damper member can be reopened, and the solid fuel dropping pipe can be periodically or constantly vibrated to promote the falling of the solid fuel.

本発明において、上記落下促進装置は、周回部における各固体燃料落下管の上端開口の下流側縁部に位置して設けられたダンパ部材により構成され、該ダンパ部材は閉位置では上記上端開口を閉じ、開位置では、周回部管内の下層流に対して抵抗を与え上層流の流れを許容するように位置し、上記各ダンパ部材のうち選定されたダンパ部材が順次開位置にもたらされ他のダンパ部材が閉位置にあるようにすることができる。   In the present invention, the fall facilitating device is constituted by a damper member provided at the downstream edge of the upper end opening of each solid fuel dropping pipe in the circulating portion, and the damper member opens the upper end opening in the closed position. In the closed and open positions, it is positioned so as to provide resistance to the lower flow in the circulating pipe and allow the upper flow, and the selected damper member among the above-mentioned damper members is brought to the open position in turn. The damper member can be in the closed position.

このような形態では、例えば、周回部における固体燃料落下管が周回部の周方向8箇所に設けられているとき、最上流位置の固体燃料落下管のダンパ部材のみが開位置にあって、他の7つのダンパ部材が閉位置にあると、周回部を流れる固体燃料は、周回部管内の下層流が上記開位置にある最上流位置のダンパ部材に衝突して固体燃料落下管の上端開口に流れ込み、周回部管内の上層流はこの上記ダンパ部材を通過して下流へ流れる。固体燃料は粗粒と微細粒とが混在しているが、それらの重量の差から、下層流は、固体燃料中の重い粗粒で占められており、この粗粒が上記固体燃料落下管に流入する。一方、上層流は軽い微細粒で占められていて、これらは上記ダンパ部材を通過し周回部内を下流に向け流れ、下流端側の固体燃料落下管から燃焼室へ供給される。又、上記開位置にあるダンパ部材以外の周回部の他の7つのダンパ部材は閉位置にあり、固体燃料は粗粒も微細粒も固体燃料落下管には流入せず通過して下流側に流れる。又、上記下流端側の固体燃料落下管には、ダンパ部材が設けられておらず、常に、上記微細粒が流入し、燃焼室へ供給される。   In such a configuration, for example, when the solid fuel dropping pipes in the circulating part are provided at eight places in the circumferential direction of the circulating part, only the damper member of the solid fuel dropping pipe in the most upstream position is in the open position, When the seven damper members are in the closed position, the solid fuel flowing in the circulating section collides with the damper member in the uppermost flow position in the open position, and the solid fuel flowing in the circulating section pipe enters the upper end opening of the solid fuel dropping pipe. The upper layer flow in the circulating pipe passes through the damper member and flows downstream. The solid fuel is a mixture of coarse particles and fine particles, but due to the difference in weight between them, the lower flow is occupied by heavy coarse particles in the solid fuel. Inflow. On the other hand, the upper layer flow is occupied by light fine particles, which pass through the damper member and flow downstream in the circulation portion, and are supplied from the solid fuel dropping pipe on the downstream end side to the combustion chamber. Further, the other seven damper members of the rotating part other than the damper member in the open position are in the closed position, and the solid fuel passes neither the coarse particles nor the fine particles into the solid fuel drop pipe and passes downstream. Flowing. Further, the solid fuel dropping pipe on the downstream end side is not provided with a damper member, and the fine particles always flow in and are supplied to the combustion chamber.

上記最上流位置にあるダンパ部材が開位置にある状態が所定時間経過すると、このダンパ部材は閉位置にもたらされ、次に位置するダンパ部材が開となる。このように、周回部では、一つづつダンパ部材が開位置にもたらされ、ダンパ部材が開となった各固体燃料落下管へ順に固体燃料が流入され落下する。この場合も、流入するのは粗粒の固体燃料であり、微細粒は周回部管内で上層流をなして下流に向け上記ダンパ部材を通過する。   When the state in which the damper member at the most upstream position is in the open position has elapsed for a predetermined time, the damper member is brought to the closed position, and the damper member positioned next is opened. As described above, in the circulating portion, the damper members are brought into the open position one by one, and the solid fuel is sequentially introduced and dropped into each solid fuel dropping pipe in which the damper member is opened. Also in this case, the coarse solid fuel flows in, and the fine particles form an upper layer flow in the circulating pipe and pass through the damper member toward the downstream.

開位置にもたらされるダンパ部材の数、開位置状態となる順序、開位置にある時間は、炉内の焼成状況により、任意に設定される。   The number of damper members brought to the open position, the order of the open position state, and the time at the open position are arbitrarily set according to the firing state in the furnace.

さらには、本発明において、炉本体は、外部から受けた空気を炉本体内で上方に向け吹き上げる空気吹上げ装置を有しているようにすることができる。こうすることにより、吹き上げられた空気が燃焼室へ燃焼用空気として供給されて燃焼を促進させると共に、燃焼ガスを撹拌しつつもち上げて燃焼室に長く留め原料の予熱を有効に行なう。   Furthermore, in the present invention, the furnace body may have an air blowing device that blows air received from the outside upward in the furnace body. By doing so, the blown-up air is supplied to the combustion chamber as combustion air to promote combustion, while the combustion gas is stirred up and kept in the combustion chamber for a long time to effectively preheat the raw material.

本発明は、以上のように、原料供給管を経て炉床へ原料を供給するために原料を一時的に貯留している原料貯留槽内へ固体燃料落下管を進入させ、この固体燃料落下管の下端開口を、原料貯留槽内で、上記原料供給管の上端開口の上方に位置せしめることとしたので、原料貯留槽内の原料が上記原料供給管から炉床へ落下供給される際に、上記固体燃料落下管の下端開口から固体燃料が落下原料に引き出されるように落下して、上記原料と混合された状態で炉床上に堆積される。したがって、複雑な可動部を有する装置を要せずに、固体燃料と原料は混合され、しかも、両者は同じ原料供給管から落下して炉床上に堆積するので混合状態は均一となる。さらには、圧送される固体燃料は、複数の固体燃料落下管から順次落下した後、圧送方向下流端側の固体燃料落下管から残りの固体燃料が炉蓋部位置で流体燃料と共に燃焼に供されるので、圧送される固体燃料をすべて使い切ってしまうこととなり、残余の固体燃料の処分などの処置は不要となる。   In the present invention, as described above, the solid fuel dropping pipe is inserted into the raw material storage tank in which the raw material is temporarily stored in order to supply the raw material to the hearth through the raw material supply pipe. Since the lower end opening of the material storage tank is positioned above the upper end opening of the raw material supply pipe, when the raw material in the raw material storage tank is dropped from the raw material supply pipe to the hearth, The solid fuel falls from the lower end opening of the solid fuel dropping pipe so as to be drawn out to the dropped raw material, and is deposited on the hearth while being mixed with the raw material. Therefore, the solid fuel and the raw material are mixed without requiring an apparatus having a complicated movable part, and both are dropped from the same raw material supply pipe and deposited on the hearth, so that the mixed state becomes uniform. Furthermore, after the solid fuel to be pumped falls sequentially from a plurality of solid fuel dropping pipes, the remaining solid fuel from the solid fuel dropping pipe on the downstream end side in the pumping direction is combusted together with the fluid fuel at the furnace lid position. Therefore, all of the solid fuel to be pumped is used up, and treatment such as disposal of the remaining solid fuel becomes unnecessary.

以下、添付図面にもとづき、本発明の実施の形態を説明する。   Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.

図1は、本発明の一実施形態の竪型焼成炉装置の縦断面図である。   FIG. 1 is a longitudinal sectional view of a vertical firing furnace apparatus according to an embodiment of the present invention.

この竪型焼成炉装置は、図1に見られるように、上方から、原料及び燃料供給部I、予熱部II、焼成部IIIそして排出部IVを順に備えている。   As shown in FIG. 1, the vertical firing furnace device includes a raw material and fuel supply unit I, a preheating unit II, a firing unit III, and a discharge unit IV in this order from above.

原料及び燃料供給部Iは、予熱部IIの上方に設けられていて、天板そして底板が上方に向く円錐状をなす原料貯留槽1を有し、内部空間に原料Mが貯留される。原料Mは頂部に設けられた投入口2からコンベア等(図示せず)により原料貯留槽1内へ投入され、底壁の周方向複数位置から垂下して設けられた原料供給管3を経て予熱部IIへ落下供給される。原料Mは、上記投入口2からの投入量そして原料供給管3での落下量により、原料貯留槽1で、原料層の上面M−1のレベルが変動する。   The raw material and fuel supply part I is provided above the preheating part II, has a raw material storage tank 1 having a conical shape with the top plate and the bottom plate facing upward, and the raw material M is stored in the internal space. The raw material M is supplied into the raw material storage tank 1 from a charging port 2 provided at the top by a conveyor or the like (not shown), and preheated through a raw material supply pipe 3 provided to hang from a plurality of circumferential positions on the bottom wall. Drop supplied to Part II. The level of the upper surface M-1 of the raw material layer in the raw material storage tank 1 varies depending on the amount of the raw material M input from the input port 2 and the amount of falling from the raw material supply pipe 3.

上記原料貯留槽1外には、固体燃料供給装置4が設けられている。この固体燃料供給装置4は、固体燃料としてコークスあるいは石炭等の粉粒体を圧送し、圧送用のポンプ5そして圧送管6を有している。該圧送管6は、ポンプ5から上方に延びる圧送上流部7、該圧送上流部7の上端から延びる周回部8、該周回部8の圧送方向下流側から半径内方に延びる半径方向部9とを有しており、上記周回部8の複数位置でそして半径方向部9の下流端側位置で、それぞれ固体燃料落下管10が垂下している。この固体燃料落下管10は、周回部8から垂下するものに符号11、半径方向部9から垂下するものに符号12を付して区別することとする。   A solid fuel supply device 4 is provided outside the raw material storage tank 1. This solid fuel supply device 4 pumps powder particles such as coke or coal as solid fuel, and has a pump 5 and a pumping pipe 6 for pumping. The pumping pipe 6 includes a pumping upstream portion 7 extending upward from the pump 5, a circumferential portion 8 extending from the upper end of the pumping upstream portion 7, and a radial portion 9 extending radially inward from the downstream side of the circumferential portion 8 in the pumping direction. The solid fuel dropping pipes 10 hang down at a plurality of positions of the circulating portion 8 and at a downstream end side position of the radial direction portion 9, respectively. The solid fuel dropping pipe 10 is distinguished by attaching a reference numeral 11 to one that hangs down from the circulating portion 8 and a reference numeral 12 to the one that hangs down from the radial direction portion 9.

上記圧送管6は、ポンプ5を経て固体燃料供給源(図示せず)に接続されていて、固体燃料Sは圧送管6内で空気圧により圧送され、周回部8そして半径方向部9へと達する。周回部8は上記原料貯留槽1の円錐状天板の上方でほぼ一周するように設けられ、半径方向部9は周回部8の下流端側位置から半径内方に延びて上記原料貯留槽1の中心部に突入している。周回部8の複数位置から垂下する固体燃料落下管11は上記天板部を貫通して原料貯留槽1内に突入し、各固体燃料落下管11の下端開口11Aは、原料貯留槽1の底壁1Aから垂下する各原料供給管3の上部開口3Aの直上に対応して位置している。この固体燃料落下管11については、後に、再度説明する。一方、半径方向部9の下流端側から垂下する固体燃料落下管12は、原料貯留槽1の底壁1Aをも貫通し、後述の予熱部IIにおける炉蓋へ達し、ここで下端が開口している。圧送管6の周回部8の周方向複数位置から垂下し下端開口11Aを有する固体燃料落下管11は、図2に見られるように、周回部8に対する接続部11Bが漏斗状のテーパ部をなし、この接続部11Bから直管部11Cが下方に延びている。本実施形態では、上記固体燃料落下管11は、下端開口11A近傍位置に外周面から半径方向外方に延びる環板フランジ状の抵抗部13を有し、又、上記接続部11Bの直下部で直管部11Cを開閉するダンパ部材14を有している。   The pumping pipe 6 is connected to a solid fuel supply source (not shown) via a pump 5, and the solid fuel S is pumped by air pressure in the pumping pipe 6 to reach the circulation part 8 and the radial part 9. . The orbiting portion 8 is provided so as to make one round above the conical top plate of the raw material storage tank 1, and the radial direction portion 9 extends radially inward from the downstream end side position of the orbiting portion 8 to extend the raw material storage tank 1. It has rushed into the center. A solid fuel dropping pipe 11 hanging from a plurality of positions of the circulating portion 8 penetrates the top plate portion and enters the raw material storage tank 1, and a lower end opening 11 </ b> A of each solid fuel dropping pipe 11 is formed at the bottom of the raw material storage tank 1. It is located corresponding to directly above the upper opening 3A of each raw material supply pipe 3 depending from the wall 1A. The solid fuel dropping pipe 11 will be described later again. On the other hand, the solid fuel dropping pipe 12 that hangs from the downstream end side of the radial portion 9 also penetrates the bottom wall 1A of the raw material storage tank 1 and reaches the furnace lid in the preheating section II described later, where the lower end opens. ing. As shown in FIG. 2, the solid fuel dropping pipe 11 hanging from a plurality of positions in the circumferential direction 8 of the circulating portion 8 of the pumping pipe 6 and having a lower end opening 11A has a connecting portion 11B with respect to the circulating portion 8 having a funnel-shaped taper portion. The straight pipe portion 11C extends downward from the connection portion 11B. In the present embodiment, the solid fuel dropping pipe 11 has an annular plate flange-shaped resistance portion 13 extending radially outward from the outer peripheral surface at a position near the lower end opening 11A, and directly below the connection portion 11B. It has a damper member 14 for opening and closing the straight pipe portion 11C.

図2に見られるように、圧送管6の周回部8は、上記接続部11Bの上方位置で若干下流寄り位置に、制御板15が設けられている。該制御板15は、図示せぬ駆動手段によって、圧送管6の上壁部から該圧送管6内への進入量を制御されるようになっている。又、固体燃料落下管11の接続部11Bはその下流側が上記周回部8内へ突出する突出部11B−1を有している。かくして、上記制御板15と突出部11B−1が相俟って、上記周回部8内で圧送される固体燃料Sの流れを積極的に固体燃料落下管11へ向ける。又、接続部11Bの直下に設けられたダンパ部材14は適宜時に間欠的に閉じられて、該ダンパ部材14の直下に固体燃料不在の空間を形成し、該ダンパ部材14の開放時に固体燃料Sの落下を良好とならしめる。かくして、上記制御板15、突出部11B−1そしてダンパ部材14は、相俟って、落下促進装置を形成する。   As shown in FIG. 2, a control plate 15 is provided in the circulating portion 8 of the pressure feeding pipe 6 at a position slightly upstream of the connecting portion 11 </ b> B. The control plate 15 is configured such that the amount of entry from the upper wall portion of the pressure feed pipe 6 into the pressure feed pipe 6 is controlled by driving means (not shown). The connecting portion 11B of the solid fuel dropping pipe 11 has a protruding portion 11B-1 that protrudes into the circulating portion 8 on the downstream side. Thus, the control plate 15 and the protruding portion 11B-1 combine to positively direct the flow of the solid fuel S fed in the circulating portion 8 to the solid fuel dropping pipe 11. Further, the damper member 14 provided immediately below the connecting portion 11B is intermittently closed as appropriate to form a space without solid fuel immediately below the damper member 14, and the solid fuel S is opened when the damper member 14 is opened. Makes the fall of the good. Thus, the control plate 15, the protrusion 11B-1 and the damper member 14 together form a fall promoting device.

原料貯留槽1の底壁1Aから垂下する原料供給管3の上端開口3Aの直上に位置する固体燃料落下管11の下端開口11Aの近傍には、フランジ状の抵抗部13が設けられているので、該抵抗部13の直下には安息角をもった空間13Aが形成される。この空間13Aの存在によって周囲の原料Mは円滑に上記上端開口3Aへ流下する。この流下する原料Mによって、上記固体燃料落下管11の下端開口11Aから固体燃料Sが引き出されるように落下し、原料Mと共に落下する。その際、図2にも見られるように、上記原料供給管3内では、固体燃料Sは中心部に、そして原料Mはこの固体燃料の落下流をとりまくようにして流れを形成しながら、落下する。   Since a flange-shaped resistance portion 13 is provided in the vicinity of the lower end opening 11A of the solid fuel dropping pipe 11 located immediately above the upper end opening 3A of the raw material supply pipe 3 depending from the bottom wall 1A of the raw material storage tank 1. A space 13 </ b> A having an angle of repose is formed immediately below the resistance portion 13. Due to the presence of the space 13A, the surrounding raw material M smoothly flows down to the upper end opening 3A. With the raw material M flowing down, the solid fuel S falls so as to be drawn out from the lower end opening 11A of the solid fuel dropping pipe 11 and falls together with the raw material M. At that time, as seen in FIG. 2, in the raw material supply pipe 3, the solid fuel S falls in the center, and the raw material M falls while forming a flow around the falling flow of the solid fuel. To do.

図1に見られるように、原料及び燃料供給部Iの下方に予熱部IIが設けられている。該予熱部IIは、非回転の蓋壁16の周縁から垂下する筒壁17と、該筒壁17に対して相対回転する縦筒状の炉本体18の上端から上記筒壁17の下端位置まで半径方向にひろがる炉床19との間の空間で予熱空間を形成している。   As shown in FIG. 1, a preheating section II is provided below the raw material and fuel supply section I. The preheating section II includes a cylindrical wall 17 that hangs down from the periphery of the non-rotating lid wall 16, and an upper end of a vertical cylindrical furnace body 18 that rotates relative to the cylindrical wall 17 to a lower end position of the cylindrical wall 17. A preheating space is formed in a space between the hearth 19 extending in the radial direction.

蓋壁16は、中央部の炉蓋部20と、該炉蓋部20の周囲に位置する天板部21とを有し、炉蓋部20は略球面の一部の形状をなしていて、その周縁から垂立する短筒部22によって、上記天板部21の内縁と接続されている。上記天板部21には、その周方向複数位置に、上記原料供給管3が接続されており、該原料供給管3から落下供給される原料と固体燃料が上記炉床19上に堆積され、その堆積層の上面は安息角をもって筒壁17と短筒部22との間の空間に形成される。上記炉蓋部20の中央位置には、既述の圧送管6の半径方向部9の下流端側から垂下する固体燃料落下管12が接続されていて、その下端開口11Aから落下する固体燃料は、この下端開口11Aに隣接して設けられている流体燃料供給装置としてのバーナ23から噴射される流体燃料と共に燃焼する。この燃焼ガスは、上記炉蓋部20の下方に形成される燃焼室にひろがる。上記筒壁17には、その周方向複数位置で、半径方向に延び同方向に往復動する棒状のプッシャ24が支持されている。このプッシャ24の往復動により、上記炉床19上に形成された原料と固体燃料の混合物の堆積層が上記燃焼室に対して安息角をもって面する自由表面から炉床19の中央に形成された落下開口25を経て原料Mが落下する。   The lid wall 16 has a central furnace lid portion 20 and a top plate portion 21 located around the furnace lid portion 20, and the furnace lid portion 20 has a substantially spherical shape. It is connected to the inner edge of the top plate portion 21 by a short cylindrical portion 22 that hangs from the periphery. The top plate portion 21 is connected to the raw material supply pipes 3 at a plurality of positions in the circumferential direction, and the raw material and solid fuel dropped and supplied from the raw material supply pipes 3 are deposited on the hearth 19. The upper surface of the deposited layer is formed in a space between the cylindrical wall 17 and the short cylindrical portion 22 with an angle of repose. A solid fuel dropping pipe 12 that hangs down from the downstream end side of the radial section 9 of the aforementioned pressure feeding pipe 6 is connected to the center position of the furnace lid section 20, and the solid fuel falling from the lower end opening 11 </ b> A is Then, it combusts together with the fluid fuel injected from the burner 23 as the fluid fuel supply device provided adjacent to the lower end opening 11A. This combustion gas spreads in a combustion chamber formed below the furnace lid portion 20. The cylindrical wall 17 supports rod-like pushers 24 that extend in the radial direction and reciprocate in the same direction at a plurality of positions in the circumferential direction. By the reciprocating motion of the pusher 24, a deposition layer of a mixture of raw material and solid fuel formed on the hearth 19 is formed in the center of the hearth 19 from a free surface facing the combustion chamber with an angle of repose. The raw material M falls through the drop opening 25.

上記原料供給管3には、炉外で、斜方に分枝管が設けられており、該分枝管が排気管26をなしている。該排気管2は、排気ガスを処理する装置(図示せず)に接続されている。   The raw material supply pipe 3 is provided with a branch pipe obliquely outside the furnace, and the branch pipe forms an exhaust pipe 26. The exhaust pipe 2 is connected to a device (not shown) for processing exhaust gas.

上記予熱部IIの下方には、上記炉床19の落下開口25から下方に延びる縦筒状の炉本体18内を焼成空間として焼成部IIIが形成されている。   Below the preheating part II, a firing part III is formed with a vertical cylindrical furnace main body 18 extending downward from the drop opening 25 of the hearth 19 as a firing space.

この焼成部IIIをなす炉本体18は、駆動手段(図示せず)により鉛直中心線まわりに回転駆動を受けており、炉床19の外周縁部と上記筒壁17の下端縁との間の回転シール19Aで、非回転の筒壁17との間の相対回転がシール状態で許容されている。   The furnace body 18 forming the firing part III is rotationally driven around a vertical center line by a driving means (not shown), and is located between the outer peripheral edge of the hearth 19 and the lower edge of the cylindrical wall 17. With the rotary seal 19A, relative rotation with the non-rotating cylinder wall 17 is allowed in a sealed state.

炉本体18は、炉床19の落下開口25の位置から下方に向け若干拡径された後に縦筒状に下方に延び、下部にて下方に向け縮径されている。この炉本体18内には、図3に見られるように、該炉本体18の鉛直中心線上に、送気筒27が配されている。この送気筒27は、周方向の複数位置で半径方向に延びるブリッジ28によって炉本体18に接続されることで支持されている。この送気筒27は、従来用いられているエジェクタで内径面が喉部を有し上方に向け拡径されているものであっても、二点鎖線で示されるように上下方向で等径をなす円筒内面のものであってもよい。   The furnace body 18 is slightly expanded downward from the position of the drop opening 25 of the hearth 19, then extends downward in a vertical cylindrical shape, and is reduced in diameter downward at the lower part. In the furnace body 18, as shown in FIG. 3, a feed cylinder 27 is disposed on the vertical center line of the furnace body 18. The feed cylinder 27 is supported by being connected to the furnace body 18 by bridges 28 extending in the radial direction at a plurality of positions in the circumferential direction. This feed cylinder 27 has a constant diameter in the vertical direction as shown by a two-dot chain line, even if the inner diameter surface of the feed cylinder 27 is a conventionally used ejector and has a throat portion and is expanded upward. A cylindrical inner surface may be used.

上記炉本体18内の下部域には、空気吹上げ装置29が設けられている。該空気吹上げ装置29は、送気箱30とこれに取り付けられた吹出し管31とを有していて、上記送気箱30は、周方向の複数位置にて、半径方向に延びる支持腕32により炉本体18で支持されている。送気箱30の下部に接続された管33を経て外部からの空気を受け、上部に接続された吹出し管31の先端(図にて上端)から上方に空気を吹き出すようになっている。該吹出し管31の上端は上記送気筒27の下部開口内に位置している。上記送気箱30の側面には、小さな複数の窓部が形成されていて、該窓部の上縁にひさし状の斜板34が設けられている。したがって、この斜板34の直下には原料等の不存在域が形成され、上記送気箱30内に送り込まれた外部空気の一部が上記窓部から側方に吹き出される。上記炉本体18は、その下方に設けられた非回転の排出部IVとの間で、回転シール35により、シール状態で相対回転が許容されている。   An air blowing device 29 is provided in the lower area in the furnace body 18. The air blowing device 29 has an air sending box 30 and a blow pipe 31 attached thereto, and the air sending box 30 has a support arm 32 extending in the radial direction at a plurality of positions in the circumferential direction. Is supported by the furnace body 18. Air from outside is received through a pipe 33 connected to the lower part of the air sending box 30, and air is blown upward from the tip (upper end in the figure) of the blowing pipe 31 connected to the upper part. The upper end of the blow pipe 31 is located in the lower opening of the feed cylinder 27. A plurality of small window portions are formed on the side surface of the air supply box 30, and an eaves-like swash plate 34 is provided on the upper edge of the window portion. Therefore, a non-existence area of raw materials and the like is formed immediately below the swash plate 34, and a part of the external air sent into the air supply box 30 is blown out sideways from the window portion. The furnace body 18 is allowed to rotate relative to the non-rotating discharge part IV provided below the furnace body 18 in a sealed state by a rotary seal 35.

排出部IVは、下端に排出口36A を有し、下方に向けて縮径されている略円錐状の排出筒体36を有し、内部に送気装置37を有している。該送気装置37は、箱状の受気体38と二種の受気管39A,39Bとを有している。受気体38の内部は上室38Aと下室38Bとに区分されていて、該上室38Aそして下室38Bは、周方向の複数位置で半径方向外方に延びる受気管39Aそして受気管39Bが接続されている。これらの受気管39Aそして受気管39Bは、それぞれ外部からの空気を受けるようになっている。   The discharge part IV has a discharge port 36A at the lower end, has a substantially conical discharge cylinder body 36 whose diameter is reduced downward, and has an air supply device 37 inside. The air supply device 37 includes a box-shaped gas reception gas 38 and two types of gas reception pipes 39A and 39B. The interior of the receiving gas 38 is divided into an upper chamber 38A and a lower chamber 38B. The upper chamber 38A and the lower chamber 38B are configured by an air receiving tube 39A and an air receiving tube 39B extending radially outward at a plurality of circumferential positions. It is connected. These air receiving pipes 39A and air receiving pipes 39B receive air from the outside.

上記上室38Aは、上記管33によって、送気箱30に接続されている。上記受気体38の下部からは傘状に錐筒部40が延出しており、該錐筒部40内にて、上記下室38Bから下方に向けて空気を吹き出す吹出し管41が延びている。又、上記下室38Bに接続されている受気管39B、そして半径方向に突出している受気管延長部39B−1には、下方に向け空気を吹き出す吹出孔42が形成されている。   The upper chamber 38A is connected to the air sending box 30 by the pipe 33. A conical cylinder portion 40 extends from the lower portion of the gas receiving portion 38 in an umbrella shape, and a blow pipe 41 for blowing air downward from the lower chamber 38B extends in the conical tube portion 40. In addition, the air receiving pipe 39B connected to the lower chamber 38B and the air receiving pipe extension 39B-1 projecting in the radial direction are formed with blowout holes 42 for blowing air downward.

かくして、受気管39Aを経て上室38Aに受け入れられた外部の空気が管33から送気箱30に達した後、吹出し管31から上方に吹き出されると共に、上記送気箱30から上記空気の一部が該送気箱30の窓部から側方へ吹き出される。一方、受気管39Bを経て下室38Bに受け入れられた外部の空気は、上記錐筒部40の直下に形成された原料不存在の空間へ吹出し管41から吹き出されると共に、受気管39Bそして受気管延長部39B−1の直下に形成された空間へ吹出孔42から吹き出される。これらの吹出し管41そして吹出孔42から吹き出された空気は上記空間における原料堆積層の自由表面を冷却した後、原料堆積層中を上昇する。   Thus, after the outside air received in the upper chamber 38A through the air receiving pipe 39A reaches the air sending box 30 from the pipe 33, it is blown upward from the air blowing pipe 31, and the air from the air sending box 30 A part is blown out sideways from the window of the air supply box 30. On the other hand, the external air received in the lower chamber 38B through the air receiving tube 39B is blown out from the air blowing tube 41 into the space where there is no raw material formed immediately below the cone tube portion 40, and the air receiving tube 39B and the air receiving tube. The air is blown out from the blowout hole 42 into a space formed immediately below the tracheal extension 39B-1. The air blown out from the blow pipe 41 and the blow hole 42 cools the free surface of the raw material deposition layer in the space and then moves up in the raw material deposition layer.

上記吹出し管31から吹き出され送気筒27を経て燃焼室へ上昇する空気と、上記送気筒27の外側の原料堆積層中を透過上昇して燃焼室へ達する空気とは、その流量比が調整可能となっていることが好ましい。この流量比は、上記堆積層の温度が所定値となるように設定される。なお、上記送気筒27が喉部を有するエジェクタであるときには、送気筒27の下端開口における圧力が大きく負圧となって堆積層内の空気がこの下端開口へ流入しないように、上記吹出し管31からの吹出し空気の流速を高めないことが望まれる。堆積層内の空気が上記下端開口に流入するということは、該下端開口よりも上方における堆積層中の空気が堆積層内を降下するということであり、空気が堆積層内を上昇して燃焼室へ到達し、上記送気筒27内からの空気と相俟って燃焼用空気として燃焼室内での燃焼を促進させるという機能を低下させてしまうからである。   The flow rate of the air blown out from the blow-out pipe 31 and rising to the combustion chamber through the feed cylinder 27 and the air permeating and rising through the raw material deposition layer outside the feed cylinder 27 and reaching the combustion chamber can be adjusted. It is preferable that This flow rate ratio is set so that the temperature of the deposited layer becomes a predetermined value. When the feed cylinder 27 is an ejector having a throat, the outlet pipe 31 prevents the pressure in the lower end opening of the feed cylinder 27 from becoming a large negative pressure so that the air in the deposited layer does not flow into the lower end opening. It is desirable not to increase the flow rate of the blown air from the air. The fact that the air in the deposition layer flows into the lower end opening means that the air in the deposition layer above the lower end opening falls in the deposition layer, and the air rises in the deposition layer and burns. This is because the function of reaching the chamber and accelerating combustion in the combustion chamber as combustion air in combination with the air from the inside of the feed cylinder 27 is reduced.

次に、上述のごとくの本実施形態装置について、その作動原理を説明する。   Next, the operation principle of the apparatus of this embodiment as described above will be described.

先ず、原料Mは、図1にて、投入口2から原料貯留槽1内へ投入される。又、固体燃料Sはポンプ5により圧送されて圧送管6を経て、周回部8から垂下する複数の固体燃料落下管11内を順次落下しそして最後に残った固体燃料が半径方向部9の下流端側から垂下する固体燃料落下管12内を落下する。   First, the raw material M is input into the raw material storage tank 1 from the input port 2 in FIG. Further, the solid fuel S is pumped by the pump 5, passes through the pumping pipe 6, and sequentially falls in a plurality of solid fuel dropping pipes 11 hanging from the circulating part 8, and the last remaining solid fuel is downstream of the radial part 9. It falls in the solid fuel dropping pipe 12 depending from the end side.

固体燃料Sは、図2に見られるように、周回部8に設けられた制御板15によって、固体燃料落下管11の上端における接続部11Bへ案内され、ダンパ部材14が開のときに上記固体燃料落下管11内を落下する。原料貯留槽1内には、その底壁1A上に原料Mの堆積層が形成されており、上記固体燃料落下管11内の固体燃料Sは該固体燃料落下管11の下端開口11Aの直下で上記原料Mと接している。   As shown in FIG. 2, the solid fuel S is guided to the connection portion 11 </ b> B at the upper end of the solid fuel dropping pipe 11 by the control plate 15 provided in the circulating portion 8, and when the damper member 14 is opened, the solid fuel S It falls in the fuel dropping pipe 11. In the raw material storage tank 1, a deposition layer of the raw material M is formed on the bottom wall 1 </ b> A, and the solid fuel S in the solid fuel dropping pipe 11 is directly below the lower end opening 11 </ b> A of the solid fuel dropping pipe 11. It is in contact with the raw material M.

上記固体燃料落下管11の下端側外周面にはフランジ状の抵抗板13が設けられており、この抵抗板13の直下には原料不存在の空間が形成されており、その周辺における原料Mが円滑に原料供給管3の上端開口3Aへ流下して行く。流下する原料Mは上記固体燃料落下管11の下端開口11Aから固体燃料Sを引き出すように作用し、上記原料供給管3内ではその中心線位置で固体燃料Sが落下し、原料Mがこの固体燃料の流れをとりまくようにして落下する。このように、同一の原料供給管3を落下する原料Mと固体燃料Sは、回転せる炉床19上に落下して堆積層を形成するので、その堆積層は、原料と固体燃料が良好に混合された状態となっている。   A flange-like resistance plate 13 is provided on the outer peripheral surface on the lower end side of the solid fuel dropping pipe 11, and a space in which no raw material is present is formed immediately below the resistance plate 13. It smoothly flows down to the upper end opening 3A of the raw material supply pipe 3. The raw material M that flows down acts to pull out the solid fuel S from the lower end opening 11A of the solid fuel dropping pipe 11, and the solid fuel S falls at the center line position in the raw material supply pipe 3, and the raw material M becomes this solid. Drops around the fuel flow. In this way, the raw material M and the solid fuel S that fall through the same raw material supply pipe 3 fall on the rotating hearth 19 to form a deposited layer, so that the deposited layer is excellent in the raw material and the solid fuel. It is in a mixed state.

炉蓋20に位置するバーナ23からは流体燃料が噴出され、又、固体燃料落下管12からは固体燃料Sが落下する。この流体燃料と固体燃料とは混合された状態で、炉蓋20直下の燃焼室で燃焼する。この燃焼による燃焼ガスは、炉床19上の原料Mと固体燃料Sとの混合物で成る堆積層をその自由表面から加熱すると共に、この燃焼ガスの一部が後述の高温上昇ガスと共に堆積層を透過して混合物中の固体燃料Sを燃焼させることにより原料を加熱する。かくして、炉床19上で加熱を受けて予熱された原料は、プッシャ24の作用により、堆積層の自由表面から徐々に落下開口25を経て炉本体18へ落下する。   Fluid fuel is ejected from the burner 23 located in the furnace lid 20, and solid fuel S falls from the solid fuel dropping pipe 12. The fluid fuel and the solid fuel are mixed and burned in a combustion chamber directly under the furnace lid 20. The combustion gas generated by this combustion heats the deposition layer made of the mixture of the raw material M and the solid fuel S on the hearth 19 from its free surface, and a part of this combustion gas forms the deposition layer together with the high temperature rising gas described later. The raw material is heated by burning the solid fuel S in the mixture. Thus, the raw material preheated by being heated on the hearth 19 gradually falls from the free surface of the deposited layer to the furnace body 18 through the drop opening 25 by the action of the pusher 24.

落下開口25から落下した予熱後の原料Mは、炉本体18内で再び堆積層を形成する。この堆積層の原料は、焼成完了後の原料の排出口36Aでの取出しによって徐々に降下するが、その上記排出口36Aまで到達するまでの間に十分焼成され、又、送気箱30の窓部から送り出された空気、そして吹出し管41及び吹出孔42から吹き出された後に上記堆積層中を上昇する空気によって、原料が排出口に達したときには、十分冷却されている。   The preheated raw material M dropped from the drop opening 25 forms a deposition layer again in the furnace body 18. The raw material of the deposited layer gradually descends by taking out the raw material at the discharge port 36A after the completion of the baking, but is sufficiently baked before reaching the discharge port 36A. When the raw material reaches the discharge port by the air sent out from the section and the air rising from the blow-out pipe 41 and the blow-out hole 42 and then rising in the deposition layer, the raw material is sufficiently cooled.

上記送気箱30の窓部から送り出された空気、そして吹出し管41、吹出孔42から吹き出された空気は原料の堆積層を上昇中に原料を冷却しつつ自らは原料から加熱されて堆積層の上面上に到達する。この加熱された空気そして上記送気筒27から上方に送り出された空気は、燃焼室での燃焼に寄与すると共に、燃焼室内の燃焼ガスをもち上げることにより長時間燃焼室内に留めて、炉床19上の堆積層の自由表面での加熱を有効ならしめる。なお、この炉床19上の堆積層を透過した燃焼ガスは、排ガスとして、排気管26から排気される。   The air sent out from the window portion of the air supply box 30 and the air blown out from the blow-out pipe 41 and the blow-out hole 42 are heated from the raw material while cooling the raw material while the raw material deposited layer is rising, and the deposited layer Reach on the top surface. The heated air and the air sent upward from the feed cylinder 27 contribute to combustion in the combustion chamber, and are kept in the combustion chamber for a long time by raising the combustion gas in the combustion chamber. Make heating on the free surface of the upper deposited layer effective. The combustion gas that has permeated the deposition layer on the hearth 19 is exhausted from the exhaust pipe 26 as exhaust gas.

かくして、焼成そして冷却された原料は、排出口36Aから製品として取り出される。   Thus, the fired and cooled raw material is taken out as a product from the discharge port 36A.

本発明は、図示された上述の形態には限定されず、種々変更可能である。例えば、圧送管6の周回部8から垂下する固体燃料落下管11は、周回部8からの固体燃料の円滑な流入、そして円滑な落下が求められる。固体燃料落下管11への固体燃料の円滑な流入のためには、例えば、図2に見られるような圧送管の周回部に対し絞りを行う制御でなく、一時的に閉じて再び開放、例えば定期的に開放されるダンパ部材でもよいし、又、周回部の上壁から固体燃料落下管11の上端開口に向け空気を吹き付けることとしてもよい。又、固体燃料落下管11内での固体燃料の落下を円滑に行うには、固体燃料落下管を下方に向け若干内径が大きくなるテーパ管としたり、この固体燃料落下管自体を蛇腹管としてその特定箇所に長手方向の変位を与えて部分的に伸縮させることにより蛇腹管を振動して管内の詰まりを防止してもよい。   The present invention is not limited to the above-described embodiment shown in the drawings, and various modifications can be made. For example, the solid fuel dropping pipe 11 that hangs from the circulating portion 8 of the pressure feeding pipe 6 is required to smoothly flow in and smoothly drop the solid fuel from the circulating portion 8. For smooth inflow of the solid fuel into the solid fuel dropping pipe 11, for example, it is not a control for restricting the circumference of the pressure feeding pipe as shown in FIG. The damper member may be periodically opened, or air may be blown from the upper wall of the circulating portion toward the upper end opening of the solid fuel dropping pipe 11. In order to smoothly drop the solid fuel in the solid fuel dropping tube 11, the solid fuel dropping tube is a tapered tube whose inner diameter is slightly increased downward, or the solid fuel dropping tube itself is used as a bellows tube. The bellows tube may be vibrated by giving a displacement in the longitudinal direction to a specific location and partially expanding and contracting to prevent clogging in the tube.

さらには、圧送管6の下流端側から垂下する固体燃料供給管は、流体燃料を噴射するバーナと、一つのインジェクタに接続されていて、このインジェクタで固体燃料と流体燃料が混合状態で噴射されるようにしてもよい。その場合、図4のようにインジェクタ43に対して、流体燃料Lが上方から、そして固体燃料Sが接線方向から供給されて、両者が混合されてから、下方に噴射され、その噴射流が旋回流を伴うようにすることできる。さらに、その際、図4において、流体燃料と固体燃料のインジェクタへの流入方向を逆にして、すなわち、固体燃料を上方からそして流体燃料を接線方向から供給してもよい。   Further, the solid fuel supply pipe hanging from the downstream end side of the pressure feed pipe 6 is connected to a burner for injecting fluid fuel and one injector, and the solid fuel and the fluid fuel are injected in a mixed state by this injector. You may make it do. In this case, as shown in FIG. 4, the fluid fuel L is supplied to the injector 43 from above and the solid fuel S is supplied from the tangential direction, mixed together, and then injected downward, and the injection flow swirls. Can be accompanied by a flow. Furthermore, in that case, in FIG. 4, the inflow directions of the fluid fuel and the solid fuel into the injector may be reversed, that is, the solid fuel may be supplied from above and the fluid fuel may be supplied from the tangential direction.

さらに、本発明では、周回部における固体燃料落下管11の上端の接続部11Bに突出部11B−1を設けず、そして制御板15そしてダンパ部材14を設けず、これらに代えて上記固体燃料落下管の上端開口の後縁位置にヒンジを有する回動自在なダンパ部材を設け、該ダンパ部材が横向きとなって上記上端開口を閉じる閉位置と、垂立して上記上端開口を開くことにより周回部内の固体燃料の流れに抵抗を示す開位置との間で回動されるようにしてもよい。ただし、上記開位置にあるとき、ダンパ部材は周回部の管内を流れる固体燃料の下層流に対して抵抗を示し、上層流に対しては上記上端開口を通過して周回部の下流へ流れることを許容する空間を形成していることが好ましい。周回部における各固体燃料落下管のダンパ部材は、所定数のものが順次開位置にあって、他は閉位置としておく。こうすると、ダンパ部材が開位置にある各固体燃料落下管へ順次固体燃料が落下する。固体燃料は、微細粒そして粗粒のものが混在しているが、両者の重量差から、微細粒は周回部内で上層流、そして粗粒が下層流をなして流れる。したがって、ダンパ部材が開いている固体燃料落下管へは粗粒が流入し、微細粒は下流端側でダンパ部材を有していない固体燃料落下管へ到達して、常時微細粒が流入する。   Further, in the present invention, the projecting part 11B-1 is not provided in the connecting part 11B at the upper end of the solid fuel dropping pipe 11 in the circulating part, and the control plate 15 and the damper member 14 are not provided. A rotatable damper member having a hinge is provided at the rear edge position of the upper end opening of the pipe, and the damper member is turned sideways to close the upper end opening, and to stand up to open the upper end opening. You may make it rotate between the open positions which show resistance to the flow of the solid fuel in a part. However, when in the open position, the damper member exhibits resistance to the lower layer flow of the solid fuel flowing in the pipe of the circulation part, and flows to the downstream of the circulation part through the upper end opening for the upper layer flow. It is preferable to form a space that allows the above. A predetermined number of damper members of the solid fuel dropping pipes in the circulating portion are sequentially in the open position, and the others are in the closed position. If it carries out like this, solid fuel will fall to each solid fuel fall pipe in which a damper member is an open position one by one. The solid fuel is a mixture of fine and coarse particles, but due to the difference in weight between the two, the fine particles flow in the upper layer flow and the coarse particles flow in the lower layer flow in the circulating portion. Accordingly, the coarse particles flow into the solid fuel dropping pipe in which the damper member is open, and the fine particles reach the solid fuel dropping pipe that does not have the damper member on the downstream end side, and the fine particles always flow in.

本発明の一実施形態装置を示し、(A)は縦断面図、(B)は圧送管のみを示す平面図である。1 shows an apparatus according to an embodiment of the present invention, in which (A) is a longitudinal sectional view, and (B) is a plan view showing only a pumping tube. 図1装置の圧送管の周回部から垂下する固体燃料落下管及びその周辺を示す断面図である。FIG. 2 is a cross-sectional view showing a solid fuel dropping pipe hanging from a circulating portion of the pressure feeding pipe of the apparatus and its periphery. 図1装置の焼成部及び排出部を示す拡大断面図である。1 is an enlarged cross-sectional view showing a firing portion and a discharge portion of the apparatus. 図1装置の燃料供給装置として、流体燃料と固体燃料を混合して噴射する、インジェクタを示す、他の実施形態の原理図である。It is a principle figure of other embodiments which shows an injector which mixes and injects fluid fuel and solid fuel as a fuel supply device of Drawing 1 device.

符号の説明Explanation of symbols

1 原料貯留槽
1A 槽底
3 原料供給管
6 圧送管
7 圧送上流部
8 周回部
9 半径方向部
11 固体燃料落下管
11B−1 突出部
12 固体燃料落下管
13 抵抗部
14 ダンパ部材
15 制御板
16 蓋壁
17 筒壁
18 炉本体
19 炉床
20 炉蓋部
21 天板部
23 流体燃料供給口(バーナ)
25 落下開口
43 インジェクタ
M 原料
S 固体燃料
DESCRIPTION OF SYMBOLS 1 Raw material storage tank 1A Tank bottom 3 Raw material supply pipe 6 Pressure feed pipe 7 Pressure feed upstream part 8 Circulation part 9 Radial direction part 11 Solid fuel fall pipe 11B-1 Protrusion part 12 Solid fuel fall pipe 13 Resistance part 14 Damper member 15 Control board 16 Lid Wall 17 Cylinder Wall 18 Furnace Main Body 19 Furnace 20 Furnace Lid 21 Top Plate 23 Fluid Fuel Supply Port (Burner)
25 Drop opening 43 Injector M Raw material S Solid fuel

Claims (8)

竪型の炉本体の上部で該炉本体の鉛直中心線に対して半径方向に延び半径方向中央域に落下開口が形成された環板状の炉床を有し、該炉床と、炉床外周縁位置で上方に延びる筒壁と、該筒壁の上端を塞ぐ蓋壁とで囲まれた空間により予熱空間を形成し、上記炉床の落下開口内縁から垂下する炉本体内に焼成空間を形成し、上記蓋壁が半径方向外側領域部をなす環状の天板部と該天板部より半径方向内側領域部をなす炉蓋部とを有し、炉外にて上記蓋壁の上方位置に配設された原料貯留槽が、槽底から垂下する複数の原料供給管を経て、天板部の原料供給口に接続され、炉外に設けられた燃料供給装置が蓋壁の燃料供給口に接続されている竪型焼成炉装置において、
燃料供給装置は、流体燃料供給装置と固体燃料供給装置とを有し、流体燃料供給装置は蓋壁中央部の炉蓋部に形成された流体燃料供給口に接続され、固体燃料供給装置は、固体燃料供給源から延びる圧送管の圧送方向複数位置に該圧送管から垂下する固体燃料落下管を有し、圧送方向下流端側位置の固体燃料落下管が、上記炉蓋部の固体燃料供給口に接続され、他の各固体燃料落下管は原料貯留槽内に突入配置され、下端開口が原料貯留槽内で対応する原料供給管の上端開口の上方に位置していることを特徴とする竪型焼成炉装置。
An annular plate-shaped hearth extending in the radial direction with respect to the vertical center line of the furnace main body at the upper part of the vertical furnace main body and having a drop opening formed in the central area in the radial direction. A preheating space is formed by a space surrounded by a cylindrical wall extending upward at the outer peripheral edge position and a lid wall that closes the upper end of the cylindrical wall, and a firing space is formed in the furnace body that hangs down from the inner edge of the drop opening of the hearth. And an annular top plate portion in which the lid wall forms a radially outer region portion and a furnace lid portion that forms a radially inner region portion from the top plate portion, and is located above the lid wall outside the furnace. The raw material storage tank disposed in the tank is connected to the raw material supply port of the top plate through a plurality of raw material supply pipes hanging from the bottom of the tank, and the fuel supply device provided outside the furnace is connected to the fuel supply port of the lid wall In the vertical firing furnace device connected to
The fuel supply device includes a fluid fuel supply device and a solid fuel supply device, the fluid fuel supply device is connected to a fluid fuel supply port formed in a furnace lid portion at the center of the lid wall, and the solid fuel supply device is A solid fuel dropping pipe suspended from the pumping pipe is provided at a plurality of positions in the pumping direction of the pumping pipe extending from the solid fuel supply source, and the solid fuel dropping pipe at the downstream end side in the pumping direction is a solid fuel supply port of the furnace lid portion. The other solid fuel dropping pipes are plunged into the raw material storage tank, and the lower end opening is located above the upper end opening of the corresponding raw material supply pipe in the raw material storage tank. Mold firing furnace device.
原料供給管は炉本体の鉛直中心線まわりの周方向の複数位置に設けられ、圧送管は上記原料供給管の上方位置で上記周方向に延びる周回部と、該圧送管の下流端側で半径内方に向って、炉蓋部の固体燃料供給口に接続されている固体燃料落下管に至る半径方向部と、上記周回部上流端と固体燃料供給源とを接続する圧送上流部とを有していることとする請求項1に記載の竪型焼成炉装置。   The raw material supply pipes are provided at a plurality of positions in the circumferential direction around the vertical center line of the furnace main body, and the pressure feed pipe has a circular portion extending in the circumferential direction above the raw material supply pipe and a radius at the downstream end side of the pressure feed pipe. Inwardly, it has a radial direction part that reaches the solid fuel drop pipe connected to the solid fuel supply port of the furnace lid part, and a pumping upstream part that connects the upstream end of the circulating part and the solid fuel supply source. The vertical firing furnace apparatus according to claim 1, wherein the vertical firing furnace apparatus is provided. 原料貯留槽内に突入せる固体燃料落下管は下端開口もしくはその直上位置で半径外方に突出するフランジ状の抵抗部を有していることとする請求項1又は請求項2に記載の竪型焼成炉装置。   3. The saddle type according to claim 1 or 2, wherein the solid fuel dropping pipe to be plunged into the raw material storage tank has a flange-shaped resistance portion projecting radially outward at a lower end opening or a position immediately above the lower end opening. Firing furnace equipment. 圧送方向下流端側位置の固体燃料落下管の下端開口が、流体燃料供給口を有するインジェクタに接続され、該インジェクタで固体燃料と流体燃料が混合されて炉内に噴射されるようになっていることとする請求項1ないし請求項3のうちの一つに記載の竪型焼成炉装置。   The lower end opening of the solid fuel dropping pipe at the downstream end side in the pumping direction is connected to an injector having a fluid fuel supply port, and the solid fuel and the fluid fuel are mixed and injected into the furnace by the injector. A vertical firing furnace apparatus according to any one of claims 1 to 3. 固体燃料落下管の下端開口は、インジェクタの噴射方向を中心線とする円周に対して接線方向に開口していることとする請求項3に記載の竪型焼成炉装置。   The vertical firing furnace device according to claim 3, wherein the lower end opening of the solid fuel dropping pipe is opened in a tangential direction with respect to a circumference having the injection direction of the injector as a center line. 圧送管は、周回部における固体燃料落下管の上端開口位置にて、圧送される固体燃料の流れに対して抵抗を与えると共に上記状端開口への固体燃料の落下を促進せしめる落下促進装置を有していることとする請求項1又は請求項2に記載の竪型焼成炉装置。   The pressure feed pipe has a drop promoting device that provides resistance to the flow of the solid fuel to be pumped at the upper end opening position of the solid fuel drop pipe in the circulation portion and promotes the fall of the solid fuel to the end opening. The vertical firing furnace apparatus according to claim 1 or 2, wherein the vertical firing furnace apparatus is provided. 落下促進装置は、周回部における各固体燃料落下管の上端開口の下流側縁部に位置して設けられたダンパ部材により構成され、該ダンパ部材は閉位置では上記上端開口を閉じ、開位置では、周回部管内の下層流に対して抵抗を与え上層流の流れを許容するように位置し、上記各ダンパ部材のうち選定されたダンパ部材が順次開位置にもたらされ他のダンパ部材が閉位置にあることとする請求項6に記載の竪型焼成炉装置。   The fall accelerating device is constituted by a damper member provided at the downstream edge of the upper end opening of each solid fuel dropping pipe in the circulating portion, and the damper member closes the upper end opening in the closed position and in the open position. The damper member is positioned so as to provide resistance to the lower layer flow in the circulation pipe and allow the upper layer flow, and the selected damper member among the damper members is sequentially brought into the open position, and the other damper members are closed. The vertical firing furnace device according to claim 6, wherein the vertical firing furnace device is located. 炉本体は、外部から受けた空気を炉本体内で上方に向け吹き上げる空気吹上げ装置を有していることとする請求項1に記載の竪型焼成炉装置。   The vertical furnace according to claim 1, wherein the furnace body has an air blowing device for blowing air received from the outside upward in the furnace body.
JP2008034948A 2008-02-15 2008-02-15 Vertical firing furnace Expired - Fee Related JP5436784B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013148258A (en) * 2012-01-19 2013-08-01 Chisaki:Kk Vertical kiln
JP2013190148A (en) * 2012-03-13 2013-09-26 Chisaki:Kk Vertical kiln
CN103423991A (en) * 2012-05-18 2013-12-04 中国有色(沈阳)冶金机械有限公司 Feeding cart of magnesium smelting operation unit

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08337447A (en) * 1995-06-09 1996-12-24 Chisaki:Kk Vertical type firing furnace
JP2007139343A (en) * 2005-11-21 2007-06-07 Chisaki:Kk Vertical kiln

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08337447A (en) * 1995-06-09 1996-12-24 Chisaki:Kk Vertical type firing furnace
JP2007139343A (en) * 2005-11-21 2007-06-07 Chisaki:Kk Vertical kiln

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013148258A (en) * 2012-01-19 2013-08-01 Chisaki:Kk Vertical kiln
JP2013190148A (en) * 2012-03-13 2013-09-26 Chisaki:Kk Vertical kiln
CN103423991A (en) * 2012-05-18 2013-12-04 中国有色(沈阳)冶金机械有限公司 Feeding cart of magnesium smelting operation unit
CN103423991B (en) * 2012-05-18 2015-02-04 中国有色(沈阳)冶金机械有限公司 Feeding cart of magnesium smelting operation unit

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