JPH05277354A - Annular shaped fluidized bed device - Google Patents

Annular shaped fluidized bed device

Info

Publication number
JPH05277354A
JPH05277354A JP12100492A JP12100492A JPH05277354A JP H05277354 A JPH05277354 A JP H05277354A JP 12100492 A JP12100492 A JP 12100492A JP 12100492 A JP12100492 A JP 12100492A JP H05277354 A JPH05277354 A JP H05277354A
Authority
JP
Japan
Prior art keywords
fluidized bed
annular
plate
agitation
perforated plate
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.)
Pending
Application number
JP12100492A
Other languages
Japanese (ja)
Inventor
Isamu Maeda
勇 前田
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.)
KANKYO SOKEN CONSULTANT KK
Original Assignee
KANKYO SOKEN CONSULTANT 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 KANKYO SOKEN CONSULTANT KK filed Critical KANKYO SOKEN CONSULTANT KK
Priority to JP12100492A priority Critical patent/JPH05277354A/en
Publication of JPH05277354A publication Critical patent/JPH05277354A/en
Pending legal-status Critical Current

Links

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  • Drying Of Solid Materials (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

PURPOSE:To continuously preheat and dry without making an agglomerative powder and granular material lumpy. CONSTITUTION:An annular shaped fluidized bed is formed by providing a flow straightening conical body 6 at the center part of a perforated plate 5 in the circular fluidized bed device 4, the annular fluidized bed is provided with a separation weir 15 and an agitation mechanism composed of an agitation motor 8, a rotary shaft 9, a rotary arm 10 and an agitation flexible body 11 is mounted.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、粉粒体の予熱,乾燥,
焼成等を行う連続流動層装置に関するものである。
BACKGROUND OF THE INVENTION The present invention relates to preheating, drying, and
The present invention relates to a continuous fluidized bed apparatus that performs firing and the like.

【0002】[0002]

【従来の技術】従来の流動層装置は、断面円形または矩
形の流動層を形成し、粉粒体を回分式に供給し、乾燥後
は排出するいわゆるバッチ式のものである。また連続式
のものとしては、箱形の流動層を振動させて、粉粒体を
移動させるか、移送かん(レーキ)を流動層内に入れ
て、粉粒体を移動させ連続的に乾燥を行っているものが
ある。
2. Description of the Related Art A conventional fluidized bed apparatus is a so-called batch type apparatus in which a fluidized bed having a circular or rectangular cross section is formed, and the powdery or granular material is supplied batchwise and discharged after drying. As a continuous type, the box-shaped fluidized bed is vibrated to move the powder or granules, or a transfer can (rake) is placed in the fluidized bed to move the powder or granules for continuous drying. There is something you are doing.

【0003】[0003]

【発明が解決しようとする課題】従来の連続流動層装置
の振動式のものでは、粒度の大きい未乾燥のものが乾燥
物と混合して排出され不具合点があった。またレーキに
よる流動層内の粉粒体の移動はレーキ間内の粉粒体の撹
拌が充分行われないため、乾燥効率の低下や凝集性の粉
粒体では塊状物を形成するなどの不具合を生じている。
The vibration type of the conventional continuous fluidized bed apparatus has a problem in that the undried material having a large particle size is mixed with the dried material and discharged. In addition, the movement of the powder or granules in the fluidized bed due to the rake does not sufficiently agitate the powder or granules between the lakes, so there is a problem such as a decrease in drying efficiency or the formation of agglomerates with cohesive powder or granules. Has occurred.

【0004】本発明は、連続的に被乾燥粉粒体を流動層
装置に供給し、未乾燥物が乾燥物と混合して排出するこ
となく、完全に乾燥されたもののみを排出する。また凝
集性の粉粒体が塊状に凝集しないで、効率よく流動乾燥
させる装置を提供することを目的とする。
In the present invention, the powdery or granular material to be dried is continuously supplied to the fluidized bed apparatus, and the undried material is not mixed with the dried material and discharged, but only the completely dried material is discharged. Another object of the present invention is to provide an apparatus for efficiently fluidizing and drying the cohesive powdery particles without agglomerating in a lump.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に、本発明の流動層装置では、水平断面が円形で円形の
中心部に同心の上部円錐の円筒体を設置し、水平断面形
状が環状形の流動層を形成している。
In order to achieve the above object, in a fluidized bed apparatus of the present invention, a horizontal cross section is circular, and a concentric upper conical cylinder is installed at the center of the circle, and the horizontal cross section is An annular fluidized bed is formed.

【0006】また投入原料と乾燥排出原料の混合を防ぐ
ため、環状部の一部に分離堰を設け、この両側に投入口
と排出口を設けている。
Further, in order to prevent mixing of the charged raw material and the dry discharged raw material, a separation weir is provided in a part of the annular portion, and a charging port and a discharging port are provided on both sides thereof.

【0007】また凝集性の粉粒体が塊状となり、乾燥効
率の低下やその他のトラブルを生じないように円形中心
部に回転軸を持ち、それに固定された流動層の撹拌腕と
その腕に付設した撹拌可とう体からなる撹拌機構を設置
している。
[0007] Further, in order to prevent the cohesive powdery material from becoming a lump and causing a decrease in drying efficiency and other troubles, a rotating shaft is provided at the circular center portion, and the stirring arm of the fluidized bed fixed to it and the arm are attached to it. A stirring mechanism consisting of a stirrable flexible body is installed.

【0008】[0008]

【作用】上記のように構成された連続流動層装置におい
ては、投入された乾燥原料は、撹拌機構によって十分撹
拌されながら流動乾燥され、環状流動層部を移動しなが
ら完全に乾燥され排出口から排出される。
In the continuous fluidized bed apparatus constructed as described above, the introduced dry raw material is fluidized and dried while being sufficiently agitated by the agitating mechanism, and is completely dried while moving in the annular fluidized bed section and is discharged from the outlet. Is discharged.

【0009】また凝集性粉粒体も撹拌機構により、撹拌
流動するため凝集し、塊状となることなく十分乾燥され
ることになる。
Further, the aggregating powder and granules are agitated and flow by the agitation mechanism so that the agglomerates agglomerate and are sufficiently dried without forming an agglomerate.

【0010】[0010]

【実施例】実施例について図面を参照して説明すると、
図1は本発明の連続流動層装置の縦断面図である。本装
置は円筒と円錐部で構成され各部の水平断面は円形であ
る。
EXAMPLES Examples will be described with reference to the drawings.
FIG. 1 is a vertical sectional view of a continuous fluidized bed apparatus of the present invention. The device consists of a cylinder and a cone, and the horizontal cross section of each part is circular.

【0011】原料の供給機1は、流動層装置本体4の上
部に供給管2を介して連結し取り付けられている。流動
層装置本体4は、上部空間は自由空間3を形成し、上端
部に排気管14が取り付けられる。中間部に多孔板5が
取り付けられる。多孔板5の中心部には整流円錐体6が
取り付けられ、多孔板5の上部は環状流動床を形成し、
下部は熱風室7となる。
The raw material feeder 1 is connected and attached to the upper part of the fluidized bed apparatus main body 4 via a feed pipe 2. The fluidized bed apparatus body 4 has a free space 3 as an upper space, and an exhaust pipe 14 is attached to an upper end thereof. The perforated plate 5 is attached to the middle portion. A straightening cone 6 is attached to the center of the perforated plate 5, and the upper part of the perforated plate 5 forms an annular fluidized bed.
The lower part becomes the hot air chamber 7.

【0012】環状流動床上に形成される流動層を撹拌す
るため、本体4の上部中心に撹拌駆動機8を設置し、そ
れに連結する回転軸9に回転腕10を複数個取り付け、
回転腕10に撹拌可とう体11を複数個取り付けてい
る。撹拌可とう体11は鎖や弾性のある棒状の可とう性
の材料で構成される。
In order to stir the fluidized bed formed on the annular fluidized bed, a stirring drive machine 8 is installed at the center of the upper part of the main body 4, and a plurality of rotary arms 10 are attached to a rotary shaft 9 connected to it.
A plurality of stirring flexible bodies 11 are attached to the rotating arm 10. The agitating flexible body 11 is made of a chain or elastic rod-shaped flexible material.

【0013】環状流動床の端部には排出管12が取り付
けられ、排出機13に連結する。熱風室7には、熱風発
生器16が連結され、熱風を吹き込むための吹込ブロワ
ー17が熱風発生器に付設されている。
A discharge pipe 12 is attached to the end of the annular fluidized bed and is connected to a discharge machine 13. A hot air generator 16 is connected to the hot air chamber 7, and a blower blower 17 for blowing hot air is attached to the hot air generator.

【0014】図2は、投入原料と乾燥後の排出原料が混
合しないために設置した分離堰15と投入管2,排出管
14の位置関係を示す図である。
FIG. 2 is a diagram showing the positional relationship between the separation weir 15 and the charging pipe 2 and the discharging pipe 14 which are installed so that the charging raw material and the dried discharging raw material do not mix.

【0015】図3は、分離堰15と多孔板5,整流円錐
体6の高低関係を示す図である。
FIG. 3 is a view showing the height relationship between the separating weir 15, the perforated plate 5, and the rectifying cone 6.

【0016】図4は、撹拌駆動機8を本体4の下部に配
したときの構成を示す縦断面図である。
FIG. 4 is a vertical cross-sectional view showing the structure when the agitation drive machine 8 is arranged in the lower part of the main body 4.

【0017】[0017]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。
Since the present invention is constructed as described above, it has the following effects.

【0018】環状形の流動層を形成することにより、回
転式の撹拌を容易にし、凝集性粉粒体の塊状化を防止
し、撹拌による流動層の安定化,乾燥等の効率向上が計
られた。
By forming an annular fluidized bed, it is possible to facilitate rotary agitation, prevent agglomeration of agglomerate powders, and stabilize the fluidized bed by stirring and improve efficiency such as drying. It was

【0019】また環状形の流動層は分離堰15を設置
し、その両側に投入口と排出口が分離しているため、投
入された原料は撹拌乾燥されながら環状部を移動し排出
口に至るので、従来の流動層の如く未乾燥原料の一部が
排出口に奔流して乾燥原料と混合する等の不具合がなく
なった。
Further, the annular fluidized bed is provided with a separation weir 15, and the charging port and the discharging port are separated on both sides thereof, so that the charged raw material moves through the circular portion while being agitated and dried to reach the discharging port. Therefore, there is no problem such as the conventional fluidized bed in which a part of the undried raw material flows into the discharge port and is mixed with the dry raw material.

【0020】[0020]

【図面の簡単な説明】[Brief description of drawings]

【図1】環状形流動層装置の縦断面図である。FIG. 1 is a vertical sectional view of an annular fluidized bed apparatus.

【図2】分離堰と投入管,排出管の位置関係を示す図
(A〜A矢視図)である。
FIG. 2 is a diagram (A-A arrow view) showing a positional relationship between a separation weir, an input pipe, and a discharge pipe.

【図3】分離堰と多孔板・整流円錐体の高低関係を示す
図(B〜B矢視図)である。
FIG. 3 is a diagram (a view from BB arrow) showing a height relationship between a separation weir and a perforated plate / rectifying cone.

【図4】環状形流動層装置において撹拌駆動機を下部に
配したときの縦断面図である。
FIG. 4 is a vertical cross-sectional view of the annular fluidized bed apparatus when a stirring drive machine is arranged in the lower portion.

【符号の説明】[Explanation of symbols]

1.供給機 2.供給管 3.自由空間 4.流動層装置本体 5.多孔板 6.整流円錐体 7.熱風室 8.撹拌駆動機 9.回転軸 10.回転腕 11.撹拌可とう体 12.排出管 13.排出機 14.排気管 15.分離堰 16.熱風発生器 17.吸込ブロワー 1. Feeder 2. Supply pipe 3. Free space 4. Fluidized bed apparatus body 5. Perforated plate 6. Rectifying cone 7. Hot air chamber 8. Stirring drive 9. Rotating shaft 10. Rotating arm 11. Stirring flexible body 12. Discharge pipe 13. Ejector 14. Exhaust pipe 15. Separation weir 16. Hot air generator 17. Suction blower

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 水平断面円形の流動層装置本体(1)
の略中央部に水平に多孔板(5)を配し、その中心部に
円筒形の整流円錐体(6)を設置し、多孔板の環状形流
動床を形成し、その一部に分離堰(15)を設け、その
両側に投入管(2)排出管(12)を設けたことを特長
とする環状形流動層装置。
1. A fluidized bed apparatus body having a circular horizontal section (1)
A perforated plate (5) is horizontally arranged at the substantially central part of the plate, and a cylindrical rectifying cone (6) is installed in the central part of the plate to form an annular fluidized bed of the perforated plate, and a separation weir is partly formed on the plate. An annular fluidized bed apparatus characterized in that (15) is provided, and an input pipe (2) and an exhaust pipe (12) are provided on both sides thereof.
【請求項2】 撹拌駆動機(8),回転軸(9),回
転腕(10),撹拌可とう体(11)からなる流動層の
撹拌機構を取り付けた請求項1記載の環状形流層装置。
2. The annular flow bed according to claim 1, further comprising a stirring mechanism for the fluidized bed, which comprises an agitation drive machine (8), a rotating shaft (9), a rotating arm (10) and a stirring flexible body (11). apparatus.
JP12100492A 1992-03-30 1992-03-30 Annular shaped fluidized bed device Pending JPH05277354A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12100492A JPH05277354A (en) 1992-03-30 1992-03-30 Annular shaped fluidized bed device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12100492A JPH05277354A (en) 1992-03-30 1992-03-30 Annular shaped fluidized bed device

Publications (1)

Publication Number Publication Date
JPH05277354A true JPH05277354A (en) 1993-10-26

Family

ID=14800406

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12100492A Pending JPH05277354A (en) 1992-03-30 1992-03-30 Annular shaped fluidized bed device

Country Status (1)

Country Link
JP (1) JPH05277354A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003130545A (en) * 2001-10-17 2003-05-08 Tsukishima Kikai Co Ltd Fluidized-bed dryer and drying method
JP2007217600A (en) * 2006-02-17 2007-08-30 Mitsui Eng & Shipbuild Co Ltd Apparatus and method for producing gas hydrate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003130545A (en) * 2001-10-17 2003-05-08 Tsukishima Kikai Co Ltd Fluidized-bed dryer and drying method
JP2007217600A (en) * 2006-02-17 2007-08-30 Mitsui Eng & Shipbuild Co Ltd Apparatus and method for producing gas hydrate

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