JP2613736B2 - Screw feeder type powder cooler - Google Patents
Screw feeder type powder coolerInfo
- Publication number
- JP2613736B2 JP2613736B2 JP17391793A JP17391793A JP2613736B2 JP 2613736 B2 JP2613736 B2 JP 2613736B2 JP 17391793 A JP17391793 A JP 17391793A JP 17391793 A JP17391793 A JP 17391793A JP 2613736 B2 JP2613736 B2 JP 2613736B2
- Authority
- JP
- Japan
- Prior art keywords
- screw
- hollow
- powder
- cylinder
- blade
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Screw Conveyors (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、最近実用化されつつあ
る加圧流動床燃焼(以下、単にPFBCということもあ
る。)等による複合発電において、PFBCの燃焼ガス
をガスタービンに供給する際に、燃焼ガスから分離した
高温・高圧雰囲気の灰を連続的に冷却しながら取り出す
有圧灰排出系に係る。BACKGROUND OF THE INVENTION The present invention relates to a method for supplying PFBC combustion gas to a gas turbine in combined power generation by pressurized fluidized bed combustion (hereinafter, sometimes simply referred to as PFBC) which is being put into practical use recently. In addition, the present invention relates to a pressurized ash discharge system for taking out ash in a high temperature and high pressure atmosphere separated from combustion gas while continuously cooling it.
【0002】[0002]
【従来の技術】図6は第1の従来技術の例を示す図で、
実開昭55−122949号公報に記載された粒状物の
搬送装置の断面図である。図6において、101は筒
体、102は投入口、103は排出口、104は中空
軸、105はスクリュー羽根、106は外筒である。該
従来例においては、まず投入口102から投入された粒
状物は筒体101内に入る。筒体101の内部には、中
空内部に冷却液を流通させる中空軸104と、この中空
軸104の外周に装着されたスクリュー羽根105が回
転自在に挿設されている。また筒体101 外周には外
筒106が取り付けられ、両筒の間に冷却液を流通させ
得るように構成されている。2. Description of the Related Art FIG. 6 shows an example of a first prior art.
BRIEF DESCRIPTION OF THE DRAWINGS It is sectional drawing of the conveyance apparatus of the granular material described in Unexamined-Japanese-Patent No. 55-122949. In FIG. 6, 101 is a cylinder, 102 is an inlet, 103 is an outlet, 104 is a hollow shaft, 105 is a screw blade, and 106 is an outer cylinder. In the conventional example, first, the granular material supplied from the charging port 102 enters the cylindrical body 101. Inside the cylindrical body 101, a hollow shaft 104 for flowing a coolant through the hollow interior and a screw blade 105 mounted on the outer periphery of the hollow shaft 104 are rotatably inserted. An outer cylinder 106 is attached to the outer periphery of the cylinder 101 so that the coolant can flow between the two cylinders.
【0003】中空軸104内および筒体101と外筒1
06との間に冷却液を流通させ、中空軸104を回転さ
せることにより、投入口102から投入された粒状物は
筒体102内を回転しつつ周壁によって冷却され、温度
を低下されながらスクリュー羽根105によって排出口
103側に移動され、排出される。The inside of the hollow shaft 104, the cylindrical body 101 and the outer cylinder 1
06, and the hollow material 104 is rotated to rotate the hollow shaft 104, so that the granular material injected from the inlet 102 is cooled by the peripheral wall while rotating inside the cylindrical body 102, and the screw blade It is moved to the outlet 103 side by 105 and discharged.
【0004】また、第2の従来技術の例として、実開昭
59−108722号公報に記載された粉粒体輸送装置
のように、スクリューフィーダに加熱ジャケットを取り
付けて粉粒体を加熱することにより、排出口における粉
粒体の水分を一定にして灰の円滑な搬送を図るものがあ
る。[0004] As a second prior art example, a heating jacket is attached to a screw feeder to heat a granular material as in a granular material transporting apparatus described in Japanese Utility Model Laid-Open No. 59-108722. In some cases, the ash is smoothly transported while keeping the water content of the granular material at the discharge port constant.
【0005】更に又、第3の従来技術の例として、特表
平3−50577号公報に記載された、ねじコンベヤ付
き灰冷却器を備えた発電装置のように、冷却効率を上昇
させるために、スクリューフィーダ円筒内下部に流動化
装置を設けたものもある。[0005] Further, as a third prior art example, in order to increase the cooling efficiency, as in a power generator having an ash cooler with a screw conveyor described in Japanese Patent Publication No. 3-50577. In some cases, a fluidizing device is provided at the lower portion inside the screw feeder cylinder.
【0006】[0006]
【発明が解決しようとする課題】このように上記従来技
術においても、投入された粉粒状物を適宜熱交換させな
がら円滑に搬送させることが可能であった。しかしなが
ら例えば第1、第2の従来の技術においては、搬送され
る粉粒状物はスクリューフィーダ内に充満されることな
く、スクリュー下部に堆積する状態、すなわちスクリュ
ーの上部に空間を有した状態で搬送が行われるため、粉
粒状物出入口の差圧が変動するような系内において、ス
クリューフィーダの上流側のガスの流入、或いは下流側
ガスの逆流を防止させながらシール状態で灰のような粉
粒状物を搬送することができない。また搬送物がスクリ
ューの下部に堆積した状態にあることにより、熱交換部
との接触面積が減少し、装置自体が大型になるという不
具合を有するものであった。また第3の従来技術におい
ては、減圧灰搬出装置の次段に設置される形式のもので
あり、上記第1、第2の従来技術の場合と同様に、出入
口の差圧をシールする機能を有しないものである。As described above, also in the above-mentioned prior art, it was possible to smoothly transfer the supplied granular material while appropriately exchanging heat. However, for example, in the first and second conventional techniques, the conveyed powdery and granular materials are not filled in the screw feeder, but are deposited in a lower portion of the screw, that is, conveyed in a state having a space above the screw. Is performed, in a system where the differential pressure at the entrance and exit of the particulate matter fluctuates, the inflow of gas on the upstream side of the screw feeder or the backflow of downstream gas is prevented while preventing the Unable to transport objects. In addition, since the conveyed material is deposited on the lower portion of the screw, the contact area with the heat exchanging part is reduced, and the apparatus itself has a problem of being large. Further, in the third prior art, it is of a type that is installed at the next stage of the vacuum ash unloading device, and has a function of sealing the differential pressure between the entrance and the outlet, as in the first and second prior arts. It does not have.
【0007】本願発明はこのような現状に鑑みてなされ
たもので、簡潔な構成と低廉な製作コストとによって、
高温・高圧の系内において上流側から下流側への、或い
は逆に下流側から上流側へのガスの流通を遮断する機能
を有する粉粒体冷却搬送装置を提供することを目的とし
ている。[0007] The present invention has been made in view of such circumstances, and has a simple configuration and a low manufacturing cost.
It is an object of the present invention to provide a particulate cooling / transporting device having a function of blocking gas flow from an upstream side to a downstream side or vice versa in a high temperature / high pressure system.
【0008】上記の目的は、前記特許請求の範囲に記載
されたスクリューフィーダ型粉体冷却器によって達成さ
れる。すなわち、 傾斜して設置される円筒形状を有し、円筒下部の上面
に粉体投入口、円筒上部の下面に粉体送出口を備え、円
筒外殻をジャケット構造とし、円筒中心部のスクリュー
軸を中空構造とし、上記円筒外殻およびスクリュー軸内
に熱交換媒体を流通させてスクリューによって移動され
る粉体を冷却しながら搬送するスクリューフィーダ型冷
却器において、円筒外殻を耐圧構造とし、円筒内に両端
を耐圧シールされて支持された中空スクリュー軸と、該
中空スクリュー軸の下部の粉体入口側および上部の粉体
出口側に取り付けられた板状スクリュー羽根と、上記中
空スクリュー軸の中間部に前記各板状スクリュー羽根に
連続させて取り付けた、幅の狭い板或いは管状物によっ
てスクリュー羽根の先端部に相当する部分のみからなる
中空羽根部を形成してスクリュー軸に支持させ、スクリ
ュー軸の回転に伴って円筒外殻内壁の底部分の灰のみを
上方に押し上げ、押し上げられた灰がスクリュー羽根の
先端部に相当する部分とスクリュー軸との間に形成され
た空間部から溢れて円筒外殻内壁内を下部方向に滑り落
ち、再びスクリュー羽根の先端部に相当する部分によっ
て押し上げられるという動作を繰り返しながら次第に下
部方向から堆積し、スクリューフィーダ内の上記中空羽
根部を灰で充満させることにより、スクリューフィーダ
内に上流と下流の間のガスの流通を遮断する灰によるシ
ール部を形成させる中空スクリュー羽根とを有するスク
リューフィーダ型粉体冷却器。[0008] The above object is achieved by a screw feeder type powder cooler described in the claims. That is, it has a cylindrical shape installed at an angle, has a powder inlet on the upper surface of the lower part of the cylinder, a powder outlet on the lower surface of the upper part of the cylinder, has a cylindrical outer shell structure, and has a screw shaft at the center of the cylinder. In a screw feeder-type cooler that has a hollow structure and conveys a heat exchange medium through the cylindrical shell and the screw shaft while cooling the powder moved by the screw, the cylindrical shell has a pressure-resistant structure, A hollow screw shaft, both ends of which are pressure-tightly sealed and supported, a plate-like screw blade attached to a lower powder inlet side and an upper powder outlet side of the lower hollow screw shaft, and an intermediate portion of the hollow screw shaft A hollow blade consisting of only a portion corresponding to the tip end of a screw blade by a narrow plate or a tubular material, which is attached to each of the plate-shaped screw blades in a continuous manner. A part is formed and supported by the screw shaft, and only the ash of the bottom part of the inner wall of the cylindrical shell is pushed up with the rotation of the screw shaft, and the pushed up ash corresponds to the tip of the screw blade and the screw shaft. It gradually overflows from the space formed between it and slides down the inside of the cylindrical shell inner wall in the lower direction, and is gradually pushed up again by the portion corresponding to the tip of the screw blade, and gradually accumulates from the lower direction while repeating the operation. A screw feeder type powder cooling having a hollow screw blade that forms a seal portion with ash that blocks gas flow between upstream and downstream in the screw feeder by filling the hollow blade portion in the feeder with ash. vessel.
【0009】ジャケット構造の円筒外殻が両端部に直
接フランジを形成したものである記載のスクリューフ
ィーダ型粉体冷却器。 ジャケット構造の円筒外殻両端部と中空スクリュー軸
の両端に接続された從動軸を耐圧シールして支持する支
持部とを接続する接続部が、熱交換媒体の流路を有する
円筒とフランジからなるものであるまたは記載のス
クリューフィーダ型粉体冷却器。 中空スクリュー軸の中空部と両端の耐圧シールされた
支持部との間に位置する軸の外周に、中空スクリュー軸
の回転に基づいて円筒内の粉体を耐圧シール部側から円
筒中央部側に押し出す向きのスクリュー羽根を設けた
またはまたは記載のスクリューフィーダ型粉体冷却
器。 である。以下本発明の作用等について実施例に基づいて
説明する。The screw feeder type powder cooler according to the above description, wherein the cylindrical outer shell of the jacket structure has flanges formed directly at both ends. The connecting portion connecting the cylindrical outer shell both ends of the jacket structure and the supporting portion supporting the driven shafts connected to both ends of the hollow screw shaft by pressure-resistant sealing is formed from the cylinder having the heat exchange medium flow path and the flange. Or a screw feeder type powder cooler as described. On the outer periphery of the shaft located between the hollow portion of the hollow screw shaft and the support portion sealed at both ends, the powder in the cylinder is moved from the pressure-resistant seal portion side to the cylinder center portion side based on the rotation of the hollow screw shaft. A screw feeder-type powder cooler provided with or described with a screw blade in an extruding direction. It is. Hereinafter, the operation and the like of the present invention will be described based on examples.
【0010】[0010]
【実施例】図1〜5は本願発明に基づくスクリューフィ
ーダ型粉体冷却器の実施例を示す図で、図1はその一部
破断側面図、図2は板状羽根と中空スクリュー羽根とを
取り付けたスクリューの拡大図、図3は図2におけるa
・a線矢視断面図、図4は図2におけるb・b線矢視断
面図、図5は駆動軸端部の部分拡大図である。図1〜5
において、1は中空スクリュー軸、2,21はスクリュ
ー羽根、3は円筒外殻、4は粉体投入口、5は粉体送出
口、6,8,10は熱交換媒体入口、7,9,11は熱
交換媒体出口、12は水平レベル、13は板状スクリュ
ー羽根、14は中空スクリュー羽根、15は粉体のレベ
ル、16は円筒外殻内壁、17は支持金具、18はフラ
ンジ、19,20,22は熱交換媒体流路、23,24
は支持部、25は中空スクリュー羽根の領域、30はス
クリューフィーダである。1 to 5 show an embodiment of a screw feeder type powder cooler according to the present invention. FIG. 1 is a partially cutaway side view, and FIG. 2 shows a plate-like blade and a hollow screw blade. FIG. 3 is an enlarged view of the attached screw, and FIG.
FIG. 4 is a sectional view taken along line bb in FIG. 2, and FIG. 5 is a partially enlarged view of an end of the drive shaft. Figures 1-5
1, 1 is a hollow screw shaft, 2, 21 are screw blades, 3 is a cylindrical shell, 4 is a powder inlet, 5 is a powder outlet, 6, 8, and 10 are heat exchange medium inlets, 7, 9, and 9. 11 is a heat exchange medium outlet, 12 is a horizontal level, 13 is a plate screw blade, 14 is a hollow screw blade, 15 is a powder level, 16 is an inner wall of a cylindrical outer shell, 17 is a support bracket, 18 is a flange, 19 and 19, 20 and 22 are heat exchange medium channels, and 23 and 24
Is a support portion, 25 is a region of a hollow screw blade, and 30 is a screw feeder.
【0011】スクリューフィーダ30は投入される灰が
高温・高圧であるために、外側には内部に熱交換媒体流
路19を形成させたジャケット構造の耐圧型の円筒外殻
3を配し、中心部には内部に熱交換媒体を流通させ得る
流路22を有する中空スクリュー軸1を配設してあり、
該中空スクリュー軸1の外周部には円筒外殻3の内壁1
6にほぼ内接する高さのスクリュー羽根2が取り付けら
れている。The screw feeder 30 has a jacket-type pressure-resistant cylindrical outer shell 3 in which a heat exchange medium flow path 19 is formed inside, since the ash to be fed is at a high temperature and a high pressure. The portion is provided with a hollow screw shaft 1 having a channel 22 through which a heat exchange medium can flow,
The outer wall of the hollow screw shaft 1 has an inner wall 1
A screw blade 2 having a height substantially inscribed in 6 is attached.
【0012】円筒外殻3の下部および上部の両端部には
スクリュー羽根2を取り付けた中空スクリュー軸1を支
持し、或いは回転させるとともに高温・高圧に対処して
所定の強度を保持させた支持部23,24が設けられて
いる。円筒外殻3の下部の上面には粉体投入口4が設け
られ、また上部の下面には粉体送出口5が設けられてい
る。更に円筒外殻の下部および上部には円筒外殻3の熱
交換媒体流路19内に熱交換媒体を送入或いは送出させ
る熱交換媒体入口8或いは熱交換媒体出口9がそれぞれ
配設されている。また円筒外殻3の下部及び上部の各端
部には熱交換媒体流路20に熱交換媒体を送入、送出さ
せる熱交換媒体入口10,10′、出口11,11′が
配設されている。A hollow screw shaft 1 on which a screw blade 2 is mounted is supported or rotated at both lower and upper ends of a cylindrical outer shell 3 or a supporting portion which rotates and copes with high temperature and high pressure to maintain a predetermined strength. 23 and 24 are provided. A powder inlet 4 is provided on the upper surface of the lower portion of the cylindrical outer shell 3, and a powder outlet 5 is provided on the lower surface of the upper portion. Further, a heat exchange medium inlet 8 or a heat exchange medium outlet 9 for feeding or sending the heat exchange medium into or out of the heat exchange medium flow path 19 of the cylindrical outer shell 3 are provided at a lower portion and an upper portion of the cylindrical outer shell, respectively. . At the lower and upper ends of the cylindrical shell 3, heat exchange medium inlets 10 and 10 'and outlets 11 and 11' for supplying and exchanging the heat exchange medium to and from the heat exchange medium flow path 20 are provided. I have.
【0013】PFBC複合発電設備において、流動床ボ
イラから排出された燃焼ガスはセラミックフィルタ等の
高温脱塵装置において、燃焼ガス中から灰を分離し、清
浄化された燃焼ガスはガスタービンに送られて発電を行
い、他方、分離除去された灰は高温・高圧(約850〜
900℃,10気圧)の状態でスクリューフィーダ30
に送られる。In the PFBC combined cycle power generation system, the combustion gas discharged from the fluidized-bed boiler separates ash from the combustion gas in a high-temperature dust removing device such as a ceramic filter, and the purified combustion gas is sent to a gas turbine. The ash separated and removed is high temperature and high pressure (about 850
Screw feeder 30 at 900 ° C, 10 atm).
Sent to
【0014】スクリューフィーダ30の下部の上面に配
設された粉体投入口4を通じて流入した灰(以下、単に
粉体ということもある。)は、スクリューフィーダ30
内部に配設されたスクリューの回転に伴なってスクリュ
ーフィーダ30の上方に移動したのち、粉体送出口5を
経由して排出される。Ash (hereinafter, also simply referred to as powder) flowing through the powder inlet 4 disposed on the lower surface of the screw feeder 30 is fed to the screw feeder 30.
After being moved above the screw feeder 30 with the rotation of the screw disposed inside, it is discharged through the powder feed port 5.
【0015】その際、スクリューフィーダ30に送入さ
れ、排出される灰がほぼ大気圧に近い状態である場合、
スクリューフィーダ30が水平に配置され、かつスクリ
ュー羽根2が中空スクリュー軸1の全長にわたって板状
スクリュー羽根を取り付けた構造であっても、何ら不具
合を生じることはないが、PFBC排ガスのように高温
・高圧である場合には、スクリューフィーダ30の上流
側のガスがスクリューフィーダ30内を通過して一気に
下流側に流出し、下流側に配設された機器類が損傷され
る虞れがある。また、後流機器に散気等のために空気を
利用する場合にはスクリューフィーダ30でのシールが
完全でないことにより、上流側の高温脱塵装置からの灰
落下等に悪影響を及ぼす。At this time, when the ash which is fed into and discharged from the screw feeder 30 is almost at atmospheric pressure,
Even if the screw feeder 30 is arranged horizontally and the screw blade 2 has a structure in which the plate-shaped screw blade is attached to the entire length of the hollow screw shaft 1, there is no problem. When the pressure is high, the gas on the upstream side of the screw feeder 30 passes through the inside of the screw feeder 30 and flows out to the downstream side at once, and there is a possibility that the devices disposed on the downstream side may be damaged. Further, when air is used for air diffusion or the like in the downstream device, the seal in the screw feeder 30 is not perfect, which has an adverse effect on ash falling from the high-temperature dedusting device on the upstream side.
【0016】そのためスクリューフィーダ30内におい
て、送入された灰を利用してスクリューフィーダ30の
上流側と下流側とのガスの流通を遮断し、下流側機器か
らの空気の吹き上げを防止するとともにスクリューフィ
ーダ30内において高温のガスを下流側機器に損傷を与
えない温度まで灰とともに冷却する必要がある。[0016] Therefore, in the screw feeder 30, the gas flow between the upstream side and the downstream side of the screw feeder 30 is shut off by using the ash that has been fed, thereby preventing air from being blown up from downstream equipment and preventing the screw from being blown up. It is necessary to cool the hot gas together with the ash in the feeder 30 to a temperature that does not damage the downstream equipment.
【0017】本願は上記の目的を達成するために発明さ
れたもので、次のように構成されている。先ずスクリュ
ーフィーダ30全体を図1〜2に示すように、水平レベ
ル12に対して灰(粉体)の投入側が低く、灰(粉体)
の送出側が高くなるように傾斜させて設置する。それに
基づいて投入口から投入された灰は回転するスクリュー
羽根によって下部から上方に押し上げられ、順次円筒外
郭3の内部を充満させながらスクリューフィーダ30上
方に移動し、粉体送出口5から排出される。従ってスク
リューフィーダ30の上流側と下流側とはスクリューフ
ィーダ30内の粉体によって気体の流通を遮断され、上
流側の高温高圧ガスが下流側へ流出するのを抑止され
る。The present application was invented to achieve the above object, and has the following configuration. First, as shown in FIGS. 1 and 2, the ash (powder) input side of the entire screw feeder 30 is lower than the horizontal level 12, and the ash (powder)
It is installed so as to be inclined so that the sending side of is higher. On the basis of this, the ash supplied from the charging port is pushed upward from below by the rotating screw blades, moves upwards while gradually filling the inside of the cylindrical shell 3, and is discharged from the powder feed port 5. . Therefore, the gas flow between the upstream side and the downstream side of the screw feeder 30 is blocked by the powder in the screw feeder 30, and the upstream high-temperature and high-pressure gas is prevented from flowing out to the downstream side.
【0018】しかしながら本願発明者らの調査によれ
ば、スクリューフィーダ30を単に傾斜させたのみで
は、スクリューフィーダ30下部に堆積する灰の密度が
小さく、また充満している容積も小さいため、スクリュ
ーフィーダ30上流側の高温・高圧ガスはスクリュー羽
根2と円筒外殻3の内壁との間隙を通じて、ややもする
と下流側に漏洩し、下流側機器の流動化空気が逆流する
ことが明らかとなった。However, according to the investigation by the present inventors, simply tilting the screw feeder 30 results in a low density of ash deposited at the lower portion of the screw feeder 30 and a small volume of ash. It was found that the high-temperature high-pressure gas on the upstream side 30 leaked to the downstream side through the gap between the screw blade 2 and the inner wall of the cylindrical shell 3, and that the fluidized air of the downstream side device flowed back.
【0019】そこで本願発明者等は、スクリュー羽根2
の構造を、図2〜4に示すように、スクリューフィーダ
30の粉体投入口4側と粉体送出口5側に従来通りの板
状スクリュー羽根13を取り付け、粉体送出口5側近く
の両板状スクリュー羽根13の中間部に図3に示すよう
な中空スクリュー羽根14を取り付けた中空スクリュー
羽根の領域25を設けた。Therefore, the present inventors have proposed that the screw blade 2
As shown in FIGS. 2 to 4, a conventional plate-like screw blade 13 is attached to the powder feed port 4 side and powder feed port 5 side of the screw feeder 30 as shown in FIGS. A hollow screw blade region 25 to which the hollow screw blade 14 was attached as shown in FIG. 3 was provided in the middle of the two plate-shaped screw blades 13.
【0020】中空スクリュー羽根14は板状スクリュー
羽根13の先端部に相当する部分のみを形成させたもの
で、幅の細い板或いは管状物によってスクリュー羽根の
先端部のみを形成し、その両端はそれぞれ上流側或いは
下流側の板状スクリュー羽根13の先端部に接合されて
おり、全体は図に示すように複数の支持金具17によっ
て中空スクリュー軸1に強固に、かつ灰が中空スクリュ
ー軸1に沿って自在に流通し得るように十分な空間を設
けて取り付けられている。The hollow screw blade 14 is formed by forming only a portion corresponding to the tip portion of the plate-shaped screw blade 13. Only the tip portion of the screw blade is formed by a thin plate or a tubular material, and both ends thereof are respectively formed. It is joined to the tip of the upstream or downstream plate-like screw blade 13, and the whole is firmly attached to the hollow screw shaft 1 by a plurality of support fittings 17 as shown in FIG. It is installed with enough space to allow free circulation.
【0021】これによって、粉体投入口4から投入され
た灰は、まず下部の板状スクリュー羽根13によってス
クリューフィーダ30内を移動し中空スクリュー羽根1
4を取り付けた中空スクリュー羽根の領域25に至る。
該領域25においては中空スクリュー羽根14の先端部
に形成された幅の細い板或いは管状の羽根によって円筒
外郭内壁16の底部分の灰のみが上方に押し上げられ、
次に押し上げられた灰は中空スクリュー羽根14の中空
部分から溢れて円筒外郭内壁16内を下部方向に滑り落
ち、再び中空スクリュー羽根14によって押し上げられ
るという動作を繰返しながら次第に下部から堆積し、つ
いには図2に仮想線で示す粉体のレベル15を形成して
スクリューフィーダ30内の下部をやや圧密化させた灰
で充満させる。As a result, the ash supplied from the powder supply port 4 is first moved in the screw feeder 30 by the lower plate-like screw blade 13 and is fed into the hollow screw blade 1.
4 to the region 25 of the hollow screw blades.
In the region 25, only the ash at the bottom of the cylindrical outer wall 16 is pushed upward by a thin plate or a tubular blade formed at the tip of the hollow screw blade 14,
Next, the pushed-up ash overflows from the hollow portion of the hollow screw blade 14, slides down in the cylindrical outer inner wall 16 in the lower direction, and gradually accumulates from the lower portion while repeating the operation of being pushed up again by the hollow screw blade 14, and finally, A level 15 of the powder is formed as shown by the phantom line in FIG. 2 and the lower part in the screw feeder 30 is filled with the ash which is slightly compacted.
【0022】これによってスクリューフィーダ30の上
流側に配設された高温脱塵装置の逆洗等、灰の系内に急
激な圧力変動が生じた際にも、スクリューフィーダ30
内に圧密化して堆積した灰によってガスの流動が阻止さ
れ、スクリューフィーダ30下流側の機器類が高温のガ
スによって損傷されるのを防止すること、或いはスクリ
ューフィーダ30後流機器からの流動化空気の逆流を防
止することが可能になる。As a result, even when a rapid pressure fluctuation occurs in the ash system such as a backwash of a high-temperature dedusting device arranged on the upstream side of the screw feeder 30, the screw feeder 30 can be used.
The gas which is condensed and accumulated in the inside prevents the gas flow and prevents the equipment downstream of the screw feeder 30 from being damaged by the hot gas, or fluidized air from the downstream equipment of the screw feeder 30. Backflow can be prevented.
【0023】スクリューフィーダ30内の中空スクリュ
ー羽根の領域25よりも上方の粉体送出口側には板状ス
クリュー羽根13が取り付けられている。該板状スクリ
ュー羽根13によって、中空スクリュー羽根の領域25
よりも下部の粉体送入口側に配設された板状スクリュー
羽根13によって押し出され、中空スクリュー羽根の領
域25において堆積、圧密化され円筒内を充満させなが
ら押し上げられてきた粉体は粉体送出口5を通じて円滑
に排出され、スクリューフィーダ30内が灰によって閉
塞されるのを防止している。The plate-shaped screw blade 13 is mounted on the powder feed port side above the hollow screw blade region 25 in the screw feeder 30. By means of the plate-like screw blades 13, the region 25 of the hollow screw blades
The powder that has been extruded by the plate-shaped screw blades 13 disposed on the lower side of the powder inlet and is deposited and consolidated in the region 25 of the hollow screw blades and has been pushed up while filling the inside of the cylinder is powder. It is smoothly discharged through the delivery port 5 to prevent the inside of the screw feeder 30 from being blocked by ash.
【0024】図5に示すように、ジャケット構造の円筒
外殻3の端部にはフランジ18が一体に形成されてい
る。フランジ18の円筒外殻3側の側面の一部はジャケ
ットの熱交換媒体流路19の壁面の一部を構成してお
り、これによって高温の粉体がスクリューフィーダ30
内に投入された場合においても、フランジ18の温度が
異常に上昇することによってスクリューフィーダ30に
破損等の不具合が生じるのを防止し得る。As shown in FIG. 5, a flange 18 is integrally formed at an end of the cylindrical outer shell 3 having a jacket structure. A part of the side surface of the flange 18 on the side of the cylindrical outer shell 3 constitutes a part of the wall surface of the heat exchange medium flow path 19 of the jacket.
Even when the screw feeder 30 is inserted into the screw feeder 30, it is possible to prevent the screw feeder 30 from being damaged or the like due to an abnormal rise in the temperature of the flange 18.
【0025】ジャケット構造の円筒外殻の両端部と中空
スクリュー軸の両端を耐圧シールして支持する支持部と
を接続する接続部は、図5に示すように円筒部の内部に
熱交換媒体流路20を有し、その両端部にフランジを形
成し、該フランジの対面する側の一部を熱交換媒体流路
20の一部を構成するようにしていることにより、投入
される高温の粉体からの熱伝導によって、スクリューフ
ィーダ30の両端部に配設された支持部が焼損するのを
防止している。As shown in FIG. 5, a connecting portion for connecting the both ends of the outer shell of the jacket structure and the supporting portion for supporting both ends of the hollow screw shaft by pressure-tightly sealing the heat exchange medium flow inside the cylindrical portion. High temperature powder to be introduced by forming a flange at both ends thereof and forming a part of the opposite side of the flange as a part of the heat exchange medium flow path 20. The heat transfer from the body prevents the support portions provided at both ends of the screw feeder 30 from burning out.
【0026】また、ほぼ上記接続部の内側に位置した、
中空スクリュー軸の中空部と両端の耐圧シールされた支
持部との間に位置する軸の外周に、図5に示すようなス
クリュー羽根21を設けてある。該羽根21はスクリュ
ーフィーダ30下部の粉体投入口4側は、中空スクリュ
ー軸1に設けられた板状スクリュー羽根13と同一の向
きに、またスクリューフィーダ30上部の粉体送出口5
側は板状スクリュー羽根13と逆の向きに形成してあ
る。これに基づいてスクリューフィーダ30稼働時に、
スクリューフィーダ30内の両端部の粉体はスクリュー
羽根21によってスクリューフィーダ30の中央部側に
押し出され、両端支持部に粉体が侵入することによる焼
き付き等の不具合を生じるのを防止することが可能にな
る。[0026] Further, it is located substantially inside the connection portion.
A screw blade 21 as shown in FIG. 5 is provided on the outer periphery of the shaft located between the hollow portion of the hollow screw shaft and the support portions sealed at both ends with pressure resistance. The blade 21 has the powder feed port 4 at the lower part of the screw feeder 30 in the same direction as the plate-shaped screw blade 13 provided on the hollow screw shaft 1, and the powder feed port 5 at the upper part of the screw feeder 30.
The side is formed in a direction opposite to the plate-like screw blade 13. When the screw feeder 30 is operated based on this,
The powder at both ends in the screw feeder 30 is extruded toward the center part of the screw feeder 30 by the screw blades 21, and it is possible to prevent problems such as seizure caused by the powder entering the support at both ends. become.
【0027】[0027]
【発明の効果】 このように本願発明によれば、上記実施例において説
明したように、傾斜設置され、灰を搬送するスクリュー
羽根の出口部近くの板状スクリュー羽根の少し上流側に
中空スクリュー羽根を設けていることにより、スクリュ
ー羽根で送られてきた灰は、中空スクリュー羽根部で堆
積、圧密化されて、一時的に送られなくなるが、連続的
にスクリュー羽根が回転していてスクリューフィーダの
下方(上流側)から灰が供給されてくることにより、ス
クリューフィーダの入口側円筒内は灰で次第に満たさ
れ、円筒内を充満した形で出口側に送られ、ついには中
空スクリュー羽根部の空間部に圧密された灰を押し出
し、出口部へ送られて排出される。この時、円筒内は灰
で充満していることにより、出入口側で圧力変動が生じ
ても充満している灰によってガスシール状態にあるか
ら、ガスの吹き抜け、逆流は起こらない。As described above, according to the present invention, as described in the above-described embodiment, the hollow screw blade is provided at a position slightly upstream of the plate-shaped screw blade near the outlet of the screw blade that conveys the ash. As a result, the ash sent by the screw blades is deposited and compacted in the hollow screw blades and temporarily stopped being sent, but the screw blades are continuously rotating and the screw feeder As the ash is supplied from below (upstream side), the inside of the cylinder on the inlet side of the screw feeder is gradually filled with ash and sent to the outlet side with the inside of the cylinder filled, and finally the space of the hollow screw blade section The ash compacted in the section is extruded, sent to the outlet and discharged. At this time, since the inside of the cylinder is filled with the ash, even if the pressure fluctuates on the entrance / exit side, the gas is in a gas-sealed state due to the filled ash.
【0028】また円筒内に灰が充満していることによ
り、熱交換媒体が流通する中空スクリュー軸と円筒内面
における灰との接触面積が大きくなり、有効伝熱面積が
増加して、灰との熱交換能力が増大する。Further, since the cylinder is filled with ash, the contact area between the hollow screw shaft, through which the heat exchange medium flows, and the ash on the inner surface of the cylinder is increased, and the effective heat transfer area is increased. The heat exchange capacity increases.
【0029】ジャケット構造の円筒外殻の端部にフラ
ンジが一体に形成され、該フランジの円筒外殻側の側面
の一部はジャケットの熱交換媒体流路の壁面の一部を構
成していることにより、フランジの温度が異常に上昇し
てスクリューフィーダに破損等の不具合が生じるのを防
止し得る。A flange is integrally formed at an end of the cylindrical shell of the jacket structure, and a part of the side surface of the flange on the cylindrical shell side forms a part of a wall surface of the heat exchange medium flow path of the jacket. Thus, it is possible to prevent the temperature of the flange from rising abnormally and the screw feeder from being damaged or the like.
【0030】ジャケット構造の円筒外殻の両端部と支
持部との間の接続部を、円筒部の内部に熱交換媒体流路
を有し、その両端部にフランジを形成し、該フランジの
対面する側の一部を熱交換媒体流路の一部を構成するよ
うにしていることにより、投入される高温の粉体からの
熱伝導による支持部の焼損を防止し得る。A connecting portion between both ends of the cylindrical outer shell of the jacket structure and the support portion has a heat exchange medium flow path inside the cylindrical portion, and flanges are formed at both ends thereof. By making a part of the heat exchange medium flow path a part of the heat exchange medium flow path, it is possible to prevent burning of the support part due to heat conduction from the high-temperature powder to be supplied.
【0031】中空スクリュー軸の中空部とスクリュー
フィーダ両端の支持部との間に位置する軸の外周にスク
リュー羽根を設け、粉体投入口側は中空スクリュー軸に
設けられた板状スクリュー羽根と同一の向きに、また粉
体送出口側は板状スクリュー羽根と逆の向きに形成す
る。これによってスクリューフィーダ稼働時に両端支持
部近くの粉体をスクリューフィーダの中央部側に押し出
し、支持部が粉体の侵入によって焼き付き等を生じるの
を防止し得る。Screw blades are provided on the outer periphery of the shaft located between the hollow portion of the hollow screw shaft and the support portions at both ends of the screw feeder, and the powder inlet side is the same as the plate-shaped screw blade provided on the hollow screw shaft. And the powder outlet side is formed in the opposite direction to the plate-shaped screw blade. Thus, when the screw feeder is in operation, the powder near both ends of the support is pushed out toward the center of the screw feeder, so that the support can be prevented from burning due to intrusion of the powder.
【図1】本発明に基づく、スクリューフィーダ型粉体冷
却器の一部破断側面図である。FIG. 1 is a partially cutaway side view of a screw feeder type powder cooler according to the present invention.
【図2】板状羽根と中空スクリュー羽根とを取り付けた
スクリューの拡大図である。FIG. 2 is an enlarged view of a screw to which a plate-like blade and a hollow screw blade are attached.
【図3】図2におけるa・a線矢視断面図である。FIG. 3 is a sectional view taken along line aa in FIG. 2;
【図4】図2におけるb・b線矢視断面図である。FIG. 4 is a sectional view taken along line bb in FIG. 2;
【図5】駆動軸端部の部分拡大図である。FIG. 5 is a partially enlarged view of an end of a drive shaft.
【図6】第1の従来技術の例である。FIG. 6 is an example of the first prior art.
1 中空スクリュー軸 2,21 スクリュー羽根 3 円筒外殻 4 粉体投入口 5 粉体送出口 6,8,10 熱交換媒体入口 7,9,11 熱交換媒体出口 12 水平レベル 13 板状スクリュー羽根 14 中空スクリュー羽根 15 粉体のレベル 16 円筒外殻内壁 17 支持金具 18 フランジ 19,20,22 熱交換媒体流路 23,24 支持部 25 中空スクリュー羽根の領域 30 スクリューフィーダ 101 筒体 102 投入口 103 排出口 104 中空軸 105 スクリュー羽根 106 外筒 DESCRIPTION OF SYMBOLS 1 Hollow screw shaft 2, 21 Screw blade 3 Cylindrical shell 4 Powder inlet 5 Powder outlet 6, 8, 10 Heat exchange medium inlet 7, 9, 11 Heat exchange medium outlet 12 Horizontal level 13 Plate screw blade 14 Hollow screw blade 15 Powder level 16 Cylindrical shell inner wall 17 Support bracket 18 Flange 19, 20, 22 Heat exchange medium flow path 23, 24 Support section 25 Hollow screw blade area 30 Screw feeder 101 Cylindrical body 102 Input port 103 Discharge Outlet 104 Hollow shaft 105 Screw blade 106 Outer cylinder
Claims (4)
筒下部の上面に粉体投入口、円筒上部の下面に粉体送出
口を備え、円筒外殻をジャケット構造とし、円筒中心部
のスクリュー軸を中空構造とし、上記円筒外殻およびス
クリュー軸内に熱交換媒体を流通させてスクリューによ
って移動される粉体を冷却しながら搬送するスクリュー
フィーダ型冷却器において、 円筒外殻を耐圧構造とし、 円筒内に両端を耐圧シールされて支持された中空スクリ
ュー軸と、 該中空スクリュー軸の下部の粉体入口側および上部の粉
体出口側に取り付けられた板状スクリュー羽根と、 上記中空スクリュー軸の中間部に前記各板状スクリュー
羽根に連続させて取り付けた、幅の狭い板或いは管状物
によってスクリュー羽根の先端部に相当する部分のみか
らなる中空羽根部を形成してスクリュー軸に支持させ、
スクリュー軸の回転に伴って円筒外殻内壁の底部分の灰
のみを上方に押し上げ、押し上げられた灰がスクリュー
羽根の先端部に相当する部分とスクリュー軸との間に形
成された空間部から溢れて円筒外殻内壁内を下部方向に
滑り落ち、再びスクリュー羽根の先端部に相当する部分
によって押し上げられるという動作を繰り返しながら次
第に下部方向から堆積し、スクリューフィーダ内の上記
中空羽根部を灰で充満させることにより、スクリューフ
ィーダ内に上流と下流の間のガスの流通を遮断する灰に
よるシール部を形成させる中空スクリュー羽根とを有す
ることを特徴とするスクリューフィーダ型粉体冷却器。1. A cylinder having a cylindrical shape installed at an angle, a powder inlet on the upper surface of a lower portion of the cylinder, a powder outlet on a lower surface of the upper portion of the cylinder, a cylindrical outer shell having a jacket structure, and a central portion of the cylinder. A screw feeder-type cooler that has a screw shaft having a hollow structure and that conveys a heat exchange medium through the cylindrical shell and the screw shaft while cooling the powder moved by the screw, wherein the cylindrical shell has a pressure-resistant structure. A hollow screw shaft supported at both ends in a cylinder by pressure-sealing, a plate-like screw blade attached to a lower powder inlet side and an upper powder outlet side of the hollow screw shaft, and the hollow screw A narrow plate or tubular object attached to the middle of the shaft in succession to each of the plate screw blades
Only the part corresponding to the tip of the screw blade
Forming a hollow blade part consisting of and supporting it on the screw shaft,
Ash on the bottom of the inner wall of the cylindrical shell with the rotation of the screw shaft
Only the ash is pushed upwards,
Form between the portion corresponding to the tip of the blade and the screw shaft
Overflows from the formed space and the inside of the cylindrical shell inner wall in the downward direction
Sliding down again, the part corresponding to the tip of the screw blade again
While repeating the action of being pushed up by
First, deposits from the bottom direction, and the above in the screw feeder
Filling the hollow blades with ash allows the screw
Ash that blocks gas flow between upstream and downstream
A screw feeder-type powder cooler, comprising: a hollow screw blade for forming a seal portion formed by the screw feeder.
接フランジを形成したものである請求項1記載のスクリ
ューフィーダ型粉体冷却器。2. The screw feeder type powder cooler according to claim 1, wherein the cylindrical outer shell of the jacket structure has flanges directly formed at both ends.
スクリュー軸の両端を耐圧シールして支持する支持部と
を接続する接続部が熱交換媒体の流路を有する円筒とフ
ランジからなるものである請求項1または請求項2記載
のスクリューフィーダ型粉体冷却器。3. A connecting portion for connecting both ends of a cylindrical outer shell of a jacket structure and a supporting portion for supporting both ends of a hollow screw shaft by pressure-tight sealing, comprising a cylinder having a heat exchange medium flow path and a flange. The screw feeder type powder cooler according to claim 1 or claim 2.
シールされた支持部との間に位置する軸の外周に、中空
スクリュー軸の回転に基づいて円筒内の粉体を耐圧シー
ル部側から円筒中央部側に押し出す向きのスクリュー羽
根を設けたことを特徴とする請求項1または請求項2ま
たは請求項3記載のスクリューフィーダ型粉体冷却器。4. The powder in the cylinder is applied to the outer periphery of the shaft located between the hollow portion of the hollow screw shaft and the pressure-sealed support portions at both ends from the pressure-tight seal portion based on the rotation of the hollow screw shaft. 4. The screw feeder type powder cooler according to claim 1, wherein screw blades are provided in a direction toward the center of the cylinder so as to be pushed out.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17391793A JP2613736B2 (en) | 1993-07-14 | 1993-07-14 | Screw feeder type powder cooler |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17391793A JP2613736B2 (en) | 1993-07-14 | 1993-07-14 | Screw feeder type powder cooler |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0727492A JPH0727492A (en) | 1995-01-27 |
JP2613736B2 true JP2613736B2 (en) | 1997-05-28 |
Family
ID=15969478
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17391793A Expired - Fee Related JP2613736B2 (en) | 1993-07-14 | 1993-07-14 | Screw feeder type powder cooler |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2613736B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102147195A (en) * | 2011-05-17 | 2011-08-10 | 苏州钻石金属粉有限公司 | Powder cooler |
CN107857456A (en) * | 2017-12-13 | 2018-03-30 | 湖南海鑫环保科技有限公司 | Superposing type multi-stage multi-pipe pyrolyzing sludge advanced treatment device |
-
1993
- 1993-07-14 JP JP17391793A patent/JP2613736B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0727492A (en) | 1995-01-27 |
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