JPS6138394B2 - - Google Patents

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Publication number
JPS6138394B2
JPS6138394B2 JP11228178A JP11228178A JPS6138394B2 JP S6138394 B2 JPS6138394 B2 JP S6138394B2 JP 11228178 A JP11228178 A JP 11228178A JP 11228178 A JP11228178 A JP 11228178A JP S6138394 B2 JPS6138394 B2 JP S6138394B2
Authority
JP
Japan
Prior art keywords
powder
fixed ventilation
ventilation plate
movable grate
resistor
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
Application number
JP11228178A
Other languages
Japanese (ja)
Other versions
JPS5541310A (en
Inventor
Hayato Yokota
Shoichi Hanawa
Hiroshi Yoshioka
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP11228178A priority Critical patent/JPS5541310A/en
Publication of JPS5541310A publication Critical patent/JPS5541310A/en
Publication of JPS6138394B2 publication Critical patent/JPS6138394B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 この発明は焼塊の冷却移送またはペレツト等の
加熱移送装置に係り、特に製紙用ライム焼塊の冷
却に好適な粉粒体の熱交換移送装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for cooling and transferring baked ingots or heating for transferring pellets, etc., and more particularly to a heat exchange transfer apparatus for powder and granular materials suitable for cooling lime ingots for paper making.

従来の粉粒体熱交換移送装置、特に焼塊の冷却
装置は第1図に示す如くロータリーキルン1等の
焼塊製造設備において焼成された粉粒体が熱交換
移送装置の粉粒体投入口2から多数の通気孔を有
する固定通気板3と可動グレート3′で形成する
火格子上に供給され、可動グレート3′の往復運
動により粉粒体投入口2から排出口4へ層を形成
して搬送される。この間に固定通気板3、可動グ
レート3′上の粉粒体は冷却空気室5に吹き込ま
れた空気によつて冷却され、一方冷却によつて予
熱された空気はロータリーキルン1等に回収され
燃料節減に役立てる。冷却された粉粒体は出口6
から排出され次のプロセスへ送られると同時に、
冷却中に冷却空気室5に落下した細粒の粉粒体は
コンベア7により粉粒体排出口12から排出され
る。ここにおいて粉粒体を層に形成して搬送する
ためには固定通気板3および可動グレート3′の
いづれも、その断面形状が粉粒体の移送方向に対
して傾斜が急で、反対方向の傾斜がゆるやかな山
形状に曲成してある。これにより駆動装置10、
連結棒9により駆動される可動グレート3′が粉
粒体の移送方向に移動する場合には可動グレート
3′の急傾斜面で粉粒体を第1図の右から左へ押
し、その前方に位置する固定通気板3のゆるい傾
斜面を乗り越えさせる。反対に可動グレート3′
が移送方向と逆に第1図の左から右へ後退する場
合には後方に位置する固定通気板3の急傾斜面が
粉粒体が逆流するのを防止する。つまり上記した
粉粒体の冷却装置を初めとして、粉粒体の熱交換
装置にはこれら粉粒体を効率良く移送するために
可動グレート3′、固定通気板3を第1図に示す
様に山形状に曲成する必要がある。
As shown in FIG. 1, in a conventional powder heat exchange transfer device, particularly a baked ingot cooling device, the powder and granule fired in a baked ingot manufacturing equipment such as a rotary kiln 1 are transferred to a powder inlet 2 of the heat exchange transfer device. The powder is supplied onto a grate formed by a fixed ventilation plate 3 having a large number of ventilation holes and a movable grate 3', and a layer is formed from the powder inlet 2 to the outlet 4 by the reciprocating movement of the movable grate 3'. transported. During this time, the powder and granules on the fixed ventilation plate 3 and the movable grate 3' are cooled by the air blown into the cooling air chamber 5, while the air preheated by cooling is collected into the rotary kiln 1 etc. to save fuel. Useful for. The cooled powder and granules are sent to outlet 6.
At the same time as it is discharged from and sent to the next process,
The fine particles that have fallen into the cooling air chamber 5 during cooling are discharged from the powder discharge port 12 by the conveyor 7. In order to transport the powder and granular material in a layered manner, both the fixed ventilation plate 3 and the movable grate 3' have a cross-sectional shape that has a steep slope with respect to the transport direction of the powder and granular material, and The slope is curved into a gentle mountain shape. As a result, the drive device 10,
When the movable grate 3' driven by the connecting rod 9 moves in the direction of conveying the powder, the steeply inclined surface of the movable grate 3' pushes the powder from right to left in Fig. 1, and the powder is pushed forward. It is made to climb over the gently sloped surface of the fixed ventilation plate 3 located there. On the contrary, movable grate 3'
When the powder moves backward from left to right in FIG. 1 in the opposite direction to the transport direction, the steeply inclined surface of the fixed ventilation plate 3 located at the rear prevents the powder from flowing backward. In other words, in addition to the above-mentioned cooling device for powder and granular materials, the heat exchange device for powder and granular materials includes a movable grate 3' and a fixed ventilation plate 3, as shown in Fig. 1, in order to efficiently transfer the powder and granular material. It is necessary to curve it into a mountain shape.

しかし石灰焼成用キルン等の小型熱交換移送装
置の如き小型のプロセスにおいては、装置の大き
さ、輸送能力、配置等に種々の制約があり、装置
設計上具備すべきものとされる要求事項を満足さ
せ得るような可動グレート3′および固定通気板
3の配置が非常に困難であつた。さらに固定通気
板3の形状を上記の如き山形状に曲成するため、
固定通気板3の製作費が高価となり、特に小型の
装置においては経済的に大きな不利益があつた。
However, in small processes such as compact heat exchange transfer equipment such as lime kilns, there are various restrictions on equipment size, transportation capacity, layout, etc., and it is difficult to satisfy the requirements that should be met in equipment design. It was very difficult to arrange the movable grate 3' and the fixed ventilation plate 3 in such a way that the movable grate 3' and the fixed ventilation plate 3 could be arranged. Furthermore, in order to curve the shape of the fixed ventilation plate 3 into the above-mentioned mountain shape,
The production cost of the fixed ventilation plate 3 is high, which is a big economic disadvantage, especially in small-sized devices.

この発明の目的は上記した従来技術の欠点をな
くし、粉粒体の冷却効果を低下させることなく粉
粒体の移送を良好に行え、かつ小型の装置にも十
分実施可能で、しかも安価な粉粒体熱交換移送装
置を提供することにある。
The purpose of the present invention is to eliminate the drawbacks of the prior art described above, to be able to transfer powder and granules well without reducing the cooling effect of powder and granules, to be able to implement the powder and granules sufficiently in small-sized equipment, and to produce inexpensive powder. An object of the present invention is to provide a granular heat exchange transfer device.

本発明は前述の目的を達成するために、固定通
気板を平板部と、この平板部の粉粒体移送側にほ
ぼ垂直面を有する抵抗体によつて構成したもので
ある。
In order to achieve the above-mentioned object, the present invention comprises a fixed ventilation plate including a flat plate part and a resistor having a substantially perpendicular surface on the powder transport side of the flat plate part.

以下この発明の実施例を添付図面を用いて説明
する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

従来の固定通気板は第1図に示す様に、山形状
に曲成された固定通気板3であつたが、本発明の
固定通気板3は第2図に示すように平板部3a
と、この平板部3aの粉粒体移送側にほぼ垂直面
11aを有する抵抗体11によつて構成したもの
である。
The conventional fixed ventilation plate was a fixed ventilation plate 3 bent into a mountain shape as shown in FIG. 1, but the fixed ventilation plate 3 of the present invention has a flat plate portion 3a as shown in FIG.
The resistor 11 has a substantially vertical surface 11a on the powder transfer side of the flat plate portion 3a.

第2図の抵抗体11は断面形状の直角三角形で
粉粒体の移送方向側に直角もしくはこれに近い垂
直面11aとなつている。
The resistor 11 shown in FIG. 2 has a right-angled triangular cross-sectional shape, and has a vertical surface 11a that is perpendicular to or nearly perpendicular to the direction in which the granular material is transported.

以上の水平部3aと抵抗体11を有する固定通
気板13においては、可動グレート3′が粉粒体
の移送方向に前進している場合には、可動グレー
ト3′の急傾斜面に押されて固定通気板13の平
板部3aに位置する粉粒体は前進し、抵抗体11
の緩傾斜面11bを越えて前方へ移動する。反対
に可動グレート3′が後退する場合には抵抗体1
1の垂直面11aの抵抗によりほとんど逆戻りし
ない。この様に本発明の固定通気板13を平板部
3aと抵抗体11によつて構成することにより粉
粒体の移送方向はほぼ一方向になり移送能力を高
めることができる。
In the fixed ventilation plate 13 having the above horizontal portion 3a and the resistor 11, when the movable grate 3' is moving forward in the direction of transporting the powder or granular material, the movable grate 3' is pushed by the steep slope of the movable grate 3'. The powder and granules located on the flat plate portion 3a of the fixed ventilation plate 13 move forward, and the resistor 11
move forward over the gently sloped surface 11b. On the other hand, when the movable grate 3' moves back, the resistor 1
Due to the resistance of the vertical surface 11a of 1, there is almost no reversal. By constructing the fixed ventilation plate 13 of the present invention by the flat plate portion 3a and the resistor 11 in this manner, the powder and granular material can be transported in almost one direction, thereby increasing the transporting capacity.

また、平板部3a、可動グレート3′上の粉粒
体層厚は固定通気板13がほぼ平面形状であるた
めに均一化され、熱交換率を高くすることができ
る。なお、粉粒体投入口2から投入された粉粒体
は、往復運動をする可動グレート3′によつて粉
粒体室8内で火格子床面上に一定の層厚を形成し
て撹拌されながら排出口4へ向けて移送される。
この際、可動グレート3′は可変速の駆動装置1
0により連結棒9によつて連結され、往復運動が
与えられる。この間に冷却空気室5からは空気ま
たはガスが可動グレート3′、固定通気板13の
平板部3aの通気孔を通して送入され粉粒体を冷
却または加熱して熱交換を行う。この熱交換時
に、通気孔または平板部3aと可動グレート3′
の間隙から洩出した粉粒体の細粒はコンベア7等
の排出装置によつて粉粒体排出口12から排出さ
れる。
Further, the thickness of the powder layer on the flat plate portion 3a and the movable grate 3' is made uniform because the fixed ventilation plate 13 has a substantially planar shape, and the heat exchange rate can be increased. The powder and granules inputted from the powder and granule inlet 2 are stirred by forming a constant layer thickness on the grate floor surface in the powder and granule chamber 8 by a reciprocating movable grate 3'. It is transferred toward the discharge port 4 while being
At this time, the movable grate 3' is moved by the variable speed drive device 1.
0 is connected by a connecting rod 9 to provide reciprocating motion. During this time, air or gas is introduced from the cooling air chamber 5 through the movable grate 3' and the ventilation holes in the flat plate portion 3a of the fixed ventilation plate 13, thereby cooling or heating the powder and granules for heat exchange. During this heat exchange, the ventilation hole or flat plate part 3a and the movable grate 3'
The fine powder particles leaking from the gap are discharged from the powder discharge port 12 by a discharge device such as a conveyor 7.

第3図はこの発明の第2の実施例を示し、第1
の実施例において示した断面形状が直角三角形の
抵抗体11の形状に変更を加えたものである。こ
の実施例における固定通気板23は平板部3aと
抵抗体111によつて形成し、この抵抗体111
は頭頂部が半円形に成形して粉粒体が乗り越え易
いようにしたものである。
FIG. 3 shows a second embodiment of the invention;
This is a modification of the shape of the resistor 11 whose cross-sectional shape is a right triangle shown in the embodiment. The fixed ventilation plate 23 in this embodiment is formed by a flat plate portion 3a and a resistor 111.
The top of the head is shaped into a semicircle to make it easier for the powder to cross over.

第4図は第3の実施例を示し、前記第2の実施
例と同様に固定通気板33は平板部3aと抵抗体
112によつて形成し、抵抗体112の粉粒体移
送側に垂直面112aを形成し、粉粒体の逆流を
防止したものである。
FIG. 4 shows a third embodiment, in which a fixed ventilation plate 33 is formed by a flat plate portion 3a and a resistor 112, and is perpendicular to the powder transfer side of the resistor 112, as in the second embodiment. A surface 112a is formed to prevent the powder from flowing backward.

第5図は固定通気板43を平板部3aと抵抗体
113によつて形成し、抵抗体113の粉粒体移
送側に垂直面113aを形成したものである。
In FIG. 5, a fixed ventilation plate 43 is formed by a flat plate portion 3a and a resistor 113, and a vertical surface 113a is formed on the powder transfer side of the resistor 113.

この発明によれば固定通気板を平板部と抵抗体
によつて構成することによつて粉粒体を良好に移
送および熱交換することができる。
According to this invention, by constructing the fixed ventilation plate by the flat plate portion and the resistor, it is possible to transfer and heat exchange the powder and granular material favorably.

また、固定通気板を平板部と抵抗体によつて作
るので、製作費を安価に押えることができ、特に
経済的に不利であつた小型の装置に対しても実施
可能であり、装置の保守、点検も容易になる。
In addition, since the fixed ventilation plate is made of a flat plate part and a resistor, manufacturing costs can be kept low, and it can be implemented even for small equipment, which was economically disadvantageous, and maintenance of the equipment can be reduced. , inspection becomes easier.

さらに粉粒体の層高を均一にすることができ熱
交換の能力を一層良好に発揮することができる。
Furthermore, the layer height of the powder and granules can be made uniform, and the heat exchange ability can be exhibited even better.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の粉粒体熱交換移送装置側断面
図、第2図はこの発明に係る粉粒体熱交換移送装
置の側断面図、第3図は第2の実施例を示す抵抗
体を中心とした固定通気板の側断面部分図、第4
図は第3の実施例を示す固定通気板の側断面部分
図、第5図は第4の実施例を示す固定通気板の側
断面部分図である。 3,23,33,43……固定通気板、3……
可動グレート、3a……平板部、9……連結棒、
10……駆動装置、11,111,112,11
3……抵抗体、11a,111a,112a,1
13a……垂直面。
FIG. 1 is a side sectional view of a conventional powder heat exchange transfer device, FIG. 2 is a side sectional view of a powder heat exchange transfer device according to the present invention, and FIG. 3 is a resistor showing a second embodiment. Partial side cross-sectional view of the fixed ventilation plate centered on 4th
The figure is a partial side sectional view of a fixed ventilation plate showing a third embodiment, and FIG. 5 is a partial side sectional view of a fixed ventilation plate showing a fourth embodiment. 3, 23, 33, 43...Fixed ventilation plate, 3...
Movable grate, 3a... flat plate part, 9... connecting rod,
10... Drive device, 11, 111, 112, 11
3...Resistor, 11a, 111a, 112a, 1
13a... Vertical surface.

Claims (1)

【特許請求の範囲】[Claims] 1 多数の通気孔を有し、固定通気板と可動グレ
ートによつて移送装置を形成し、可動グレートの
往復運動により粉粒体を移送しつつ熱交換を行な
うものにおいて、前記固定通気板を平板部と、こ
の平板部の粉粒体移送側にほぼ垂直面を有する抵
抗体とによつて構成したことを特徴とする粉粒体
熱交換移送装置。
1. In a device having a large number of ventilation holes, in which a fixed ventilation plate and a movable grate form a transfer device, and heat exchange is performed while transferring powder and granular material by reciprocating motion of the movable grate, the fixed ventilation plate is replaced with a flat plate. What is claimed is: 1. A heat exchange and transfer device for powder and granular material, comprising a resistor having a substantially perpendicular surface on the powder and granule transfer side of the flat plate section.
JP11228178A 1978-09-14 1978-09-14 Heat exchanging and transferring device for pulverized substance Granted JPS5541310A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11228178A JPS5541310A (en) 1978-09-14 1978-09-14 Heat exchanging and transferring device for pulverized substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11228178A JPS5541310A (en) 1978-09-14 1978-09-14 Heat exchanging and transferring device for pulverized substance

Publications (2)

Publication Number Publication Date
JPS5541310A JPS5541310A (en) 1980-03-24
JPS6138394B2 true JPS6138394B2 (en) 1986-08-29

Family

ID=14582763

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11228178A Granted JPS5541310A (en) 1978-09-14 1978-09-14 Heat exchanging and transferring device for pulverized substance

Country Status (1)

Country Link
JP (1) JPS5541310A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3217969A1 (en) * 1982-05-13 1983-11-17 Claudius Peters Ag, 2000 Hamburg DEVICE FOR DISCHARGING RUST DIAGNOSIS
JPS63153293A (en) * 1986-12-17 1988-06-25 Chugoku Denka Kogyo Kk Surface treatment of work
JPH0532538Y2 (en) * 1990-03-15 1993-08-19
DE10117226A1 (en) * 2001-04-06 2002-10-10 Bmh Claudius Peters Gmbh Cooling grate for bulk goods
EP2843342B2 (en) 2013-08-27 2019-07-03 Alite GmbH Clinker cooler

Also Published As

Publication number Publication date
JPS5541310A (en) 1980-03-24

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