JPH0325217B2 - - Google Patents

Info

Publication number
JPH0325217B2
JPH0325217B2 JP58100285A JP10028583A JPH0325217B2 JP H0325217 B2 JPH0325217 B2 JP H0325217B2 JP 58100285 A JP58100285 A JP 58100285A JP 10028583 A JP10028583 A JP 10028583A JP H0325217 B2 JPH0325217 B2 JP H0325217B2
Authority
JP
Japan
Prior art keywords
gas
granular material
annular member
rotating
rotating frame
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 - Lifetime
Application number
JP58100285A
Other languages
Japanese (ja)
Other versions
JPS59225732A (en
Inventor
Susumu Kamikawa
Masahiko Kobayashi
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP10028583A priority Critical patent/JPS59225732A/en
Publication of JPS59225732A publication Critical patent/JPS59225732A/en
Publication of JPH0325217B2 publication Critical patent/JPH0325217B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/02Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • F26B3/08Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Furnace Details (AREA)

Description

【発明の詳細な説明】 本発明は粒塊状材料を処理する装置に関し、
種々の鉱石、金属化合物等の加熱、乾燥、冷却等
の処理に有利に使用できる装置に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for processing granular material;
The present invention relates to an apparatus that can be advantageously used for heating, drying, cooling, etc. processing of various ores, metal compounds, etc.

本発明の説明に当つてはこれらの粒塊状材料の
うち特にピツチコークスの冷却に関連して以下に
説明する。
The present invention will be described below with particular reference to the cooling of pitch coke among these granular materials.

セメント、コークス、焼結鉱のように、一旦焼
成した後、冷却を要する粒塊状材料の処理には歩
留りの向上、顕熱の回収に有利な乾式処理装置が
採用されており、粉状材料には流動層、塊状材料
にはシヤフト炉ないし円形グレード装置が一般に
使用されている。
Dry processing equipment, which is advantageous in improving yields and recovering sensible heat, is used to process granular materials that require cooling after being fired, such as cement, coke, and sintered ore. For bulk materials, a shaft furnace or circular grade equipment is generally used.

しかし、実用上、流動層、シヤフト炉には適性
粒度範囲が存在し、流動層では一般に6mm以下、
シヤフト炉では逆に10mm以上が好ましく、又粒度
分布範囲も狭い。これらの適性領域を外れると、
圧力損失が増加し、大幅にランニングコストが悪
化するばかりでなく、均一な冷却が得られない、
設備費が増加し、経済性が悪化する等の不具合点
が発生し、実用上極めて不利である。ピツチコー
クスを冷却する場合には、銘柄により平均粒径1
mmの粉粒状のものから15〜20mmまでの塊を取り扱
う必要があり、流動層とシヤフト炉では前記適性
粒度範囲確保のため、流動層とシヤフト炉の両者
共必要となり、片方が片方に対し遊休設備となる
ため、経済性が非常に悪くなる。
However, in practice, there is an appropriate particle size range for fluidized beds and shaft furnaces.
On the other hand, in a shaft furnace, the diameter is preferably 10 mm or more, and the particle size distribution range is also narrow. If you go outside these appropriate areas,
Not only does pressure loss increase and running costs deteriorate significantly, but uniform cooling cannot be achieved.
This is extremely disadvantageous in practice, as it causes problems such as increased equipment costs and worsened economic efficiency. When cooling pitch coke, depending on the brand, the average particle size is 1
It is necessary to handle lumps ranging from millimeters in size to 15 to 20 mm, and in order to ensure the appropriate particle size range, both a fluidized bed and a shaft furnace are required, and one is idle compared to the other. Since it is a piece of equipment, the economic efficiency is very poor.

一方、円形グレード装置は適用粒度範囲が前記
2者に比べ柔軟である。第1図に円形グレード装
置の代表断面図を示す。1は外側環状部材、2は
外側環状部材1から間隔をおいて設けられた内側
環状部材、3は回転枠である。回転枠3下端には
ガス透過性のグレードを有す回転格子4が回転枠
3に傾動可能に取付けられ処理粒塊状材料を支持
する。この格子4を通過するガスを包封するため
回転枠3の上方に静止状に上方フツド5、下方に
静止状に風箱6を設置し、且つ上方フツド5と回
転枠3との間及び回転枠3と風箱6との間に液体
含有トラフ7と、液体含有トラフ7内の液中に延
びるシールプレート8とによつて構成するシール
機構を備えている。又回転枠3は回転枠3下部に
取り付けられた車輪9により水平環状軌道10上
で支持され移動するが、この間格子4上に層状に
堆積した処理粒塊状材料11にガス18を通過せ
しめることによつて冷却等の処理を行う。以上の
ことから円形グレード装置においては格子4上の
粒塊状材料11の層高を低くすることにより粒塊
状の材料を扱う場合においても圧力損失を低く抑
えることができるわけである。このように、ピツ
チコークスのような塊を扱う場合には、格子4を
通過するガス流速を速くし、コンパクトな設備を
提供できるが、粉状材料を扱う場合には、ガス流
速を粉状材料の流動化速度以下にすることが制限
条件となるため、設備としては格子面積を大きく
とらざるを得なくなり、結果的に設備費が大幅に
増加する。又、外側、内側環状部材1,2を高く
し、ガス流速を上げ、全体を流動化させようとす
るならば、流動化面積が大きいこと、又粒度偏析
等により層の一部が吹き抜けるチヤネリングの発
生が生じるため未冷却部が発生し、実用上円形グ
レード装置を流動層として扱うのは困難である。
On the other hand, the applicable particle size range of the circular grading device is more flexible than those of the above two methods. Figure 1 shows a representative cross-sectional view of a circular grade device. 1 is an outer annular member, 2 is an inner annular member provided at a distance from the outer annular member 1, and 3 is a rotating frame. At the lower end of the rotating frame 3, a rotating grating 4 having a gas permeable grade is tiltably attached to the rotating frame 3 and supports the treated granular material. In order to seal the gas passing through the grid 4, an upper hood 5 is installed stationary above the rotating frame 3, and a wind box 6 is installed stationary below. A sealing mechanism is provided between the frame 3 and the wind box 6, which includes a liquid-containing trough 7 and a seal plate 8 extending into the liquid in the liquid-containing trough 7. The rotating frame 3 is supported and moved on a horizontal annular track 10 by wheels 9 attached to the lower part of the rotating frame 3. During this time, the gas 18 is passed through the treated granular material 11 deposited in layers on the grid 4. Thereafter, processing such as cooling is performed. From the above, in the circular grading device, by lowering the layer height of the granular material 11 on the grid 4, pressure loss can be kept low even when handling granular material. In this way, when handling lumps such as pitchcoke, the gas flow rate passing through the grid 4 can be increased and compact equipment can be provided, but when handling powdered materials, the gas flow rate can be adjusted to Since the limiting condition is to keep the fluidization speed below the fluidization speed, the equipment must have a large grid area, resulting in a significant increase in equipment costs. In addition, if you try to increase the height of the outer and inner annular members 1 and 2 to increase the gas flow rate and fluidize the entire body, the fluidization area must be large, and channeling, where part of the layer blows through due to particle size segregation, etc. As a result, uncooled parts occur, making it difficult to treat a circular grading device as a fluidized bed in practice.

本発明は、前記欠点により従来実用上処理不能
とされていた幅広い粒度構成を有す粒塊状材料を
経済的に処理し得る装置を提供するものである。
The present invention provides an apparatus capable of economically processing granular material having a wide range of particle size configurations, which has heretofore been considered practically unprocessable due to the above-mentioned drawbacks.

即ち本発明は、粒塊状材料を加熱、乾燥、冷却
等により処理する装置において、回転枠上部の上
部環状部材及び下部環状部材間に、下端にガス透
過性グレードを有する回転格子を有し、両端をガ
スタイトに固設した独立の中空円筒もしくは角筒
の粒塊状材料保持筒を複数列配設してなり、下方
に配置された風箱より処理媒体ガスを前記回転格
子を介して粒塊状保持筒に供給し得るようにして
なることを特徴とする粒塊状材料処理装置に関す
るものである。
That is, the present invention provides an apparatus for processing granular material by heating, drying, cooling, etc., which has a rotating grating having a gas permeability grade at the lower end between an upper annular member and a lower annular member at the upper part of the rotating frame, and A plurality of rows of independent hollow or rectangular granular material holding cylinders are arranged in a gas-tight manner, and the processing medium gas is passed through the rotating lattice from the wind box located below to the granular material holding cylinders. The present invention relates to a granular material processing apparatus characterized in that it is configured to be able to supply granular material.

第2図は本発明装置の一実施例を示す図、第3
図は第2図のA−A断面図、第4図は第2図のB
−B断面図である。
FIG. 2 is a diagram showing an embodiment of the device of the present invention, and FIG.
The figure is a sectional view taken along line A-A in Figure 2, and Figure 4 is B in Figure 2.
-B sectional view.

第2〜4図において、第1図と同一符号は第1
図と同一部位を示し、12は上部環状部材、13
は下部環状部材、14は回転枠を示す。この上下
環状部材12,13の間にあり、両端をガスタイ
トに上下環状部材12,13に固定して円環状複
数列且つ独立した中空円筒状もしくは角形状の粒
塊状材料保持筒15を設置する。又個々の保持筒
15下端にはガス透過性のグレードを有する回転
格子16が傾動可能に回転枠14に取付けられ
る。処理粒塊状材料11は各々の保持筒15内で
格子16上に層状に堆積され保持されながら、回
転枠14下部に取付けた車輪9が水平円環状に施
設された軌道10上で回転枠14を支持しながら
移動することにより移送される。17aは上部シ
ール機構で、上部架構30aに懸架されたフツド
5の下端部5a及び同フツド5に固着されたシー
ルプレート8aと上部環状部材12に取付けられ
た液体含有トラフ7aとで構成されている。17
bは下部シール機構で、回転枠14に固着された
シールプレート8bと風箱6の側周に固着された
液体含有トラフ7bとで構成されている。処理媒
体であるガス18は、風箱6、保持筒15及びフ
ツド5と上記上部及び下部シール機構17a,1
7bとによつて包封され、風箱6から格子16及
び保持筒15内を通過することによつて粒塊状材
料を加熱あるいは冷却等により処理する。なお、
シール機構17は加圧装置19を配設した加圧用
ガス配管20によつて相互に連結されている。
In Figures 2 to 4, the same reference numerals as in Figure 1 indicate
The same parts as in the figure are shown, 12 is an upper annular member, 13
14 indicates a lower annular member, and 14 indicates a rotating frame. Between the upper and lower annular members 12 and 13, a plurality of rows of independent hollow cylindrical or angular granular material holding cylinders 15 are installed with both ends fixed to the upper and lower annular members 12 and 13 in a gas-tight manner. Further, at the lower end of each holding cylinder 15, a rotating grating 16 having a gas permeable grade is attached to the rotating frame 14 so as to be tiltable. The treated granular material 11 is deposited and held in layers on a grid 16 in each holding cylinder 15, while wheels 9 attached to the lower part of the rotating frame 14 move the rotating frame 14 on a horizontal annular track 10. It is transported by moving while supporting it. Reference numeral 17a denotes an upper sealing mechanism, which is composed of a lower end 5a of the hood 5 suspended on the upper frame 30a, a seal plate 8a fixed to the hood 5, and a liquid-containing trough 7a attached to the upper annular member 12. . 17
Reference numeral b denotes a lower seal mechanism, which is composed of a seal plate 8b fixed to the rotating frame 14 and a liquid-containing trough 7b fixed to the side circumference of the wind box 6. The gas 18, which is a processing medium, is supplied to the wind box 6, the holding cylinder 15, the hood 5, and the upper and lower sealing mechanisms 17a, 1.
7b, and passes through the grid 16 and the holding cylinder 15 from the wind box 6 to process the granular material by heating or cooling. In addition,
The sealing mechanisms 17 are interconnected by a pressurizing gas pipe 20 in which a pressurizing device 19 is provided.

このように、本発明装置によれば、粒塊状材料
11を多数の保持筒15内で保持することによつ
て、粒塊状材料を小分割に分離して移送、処理す
ることができる。このことは、個々のグレード1
6面積が小さくなることにより、粒径状材料を処
理する場合、ガス18の吹き抜けを防止すること
ができ、個々の保持筒15を独立した流動層とし
て取り扱うことができるため、ガス流速を増加で
きる。又塊状材料を処理する場合は、個々の保持
筒15内で静止した固定充てん層として取り扱う
ことができる。更に粉粒状材料と塊状材料が混合
した材料においても、保持筒15内で塊状材料が
下層に堆積し、塊状材料層上に粉粒状材料が流動
層を形成するため、粉状、塊状にとらわれること
なく、適性ガス流速で処理することができる。
As described above, according to the apparatus of the present invention, by holding the granular material 11 in a large number of holding cylinders 15, the granular material can be separated into small parts and transported and processed. This means that individual Grade 1
6 By reducing the area, when processing granular materials, it is possible to prevent the gas 18 from blowing through, and each holding cylinder 15 can be treated as an independent fluidized bed, so the gas flow rate can be increased. . Furthermore, when processing bulk material, it can be handled as a stationary fixed packed layer within each holding cylinder 15. Furthermore, even in the case of a material that is a mixture of powdery material and lumpy material, the lumpy material is deposited in the lower layer within the holding cylinder 15 and the powdery granular material forms a fluidized bed on the lumpy material layer, so that it is not trapped in the powdery or lumpy state. The process can be performed at an appropriate gas flow rate.

以上述べたごとく、本発明装置によれば、従来
実用上困難とされていた粉状材料と塊状材料の同
時処理が可能となるばかりでなく、ガス流速を最
適速度に選択できることによる冷却面積の減少に
よつてコンパクトな設備を提供することができ、
設備費上極めて有利となる。
As described above, according to the apparatus of the present invention, it is not only possible to simultaneously process powdered materials and bulk materials, which was conventionally considered difficult in practice, but also to reduce the cooling area by selecting the optimum gas flow rate. can provide compact equipment,
This is extremely advantageous in terms of equipment costs.

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

第1図は円形グレード装置の代表断面図を示
し、第2図は本発明装置の一実施例を示す代表断
面図であり、第3図及び第4図はそれぞれ第2図
のA−A断面及びB−B断面を示す図である。
FIG. 1 shows a representative sectional view of a circular grade device, FIG. 2 shows a representative sectional view of an embodiment of the device of the present invention, and FIGS. and a diagram showing a BB cross section.

Claims (1)

【特許請求の範囲】[Claims] 1 粒塊状材料を加熱、乾燥、冷却等により処理
する装置において、回転枠上部の上部環状部材及
び下部環状部材間に、下端にガス透過性グレード
を有する回転格子を有し、両端をガスタイトに固
設した独立の中空円筒もしくは角筒の粒塊状保持
筒を複数配設してなり、下方に設置された風箱よ
り処理媒体ガスを前記回転格子を介して粒塊状保
持筒に供給し得るようにしてなることを特徴とす
る粒塊状材料処理装置。
1. In an apparatus that processes granular materials by heating, drying, cooling, etc., a rotating grating having a gas permeability grade at the lower end is provided between the upper annular member and the lower annular member at the top of the rotating frame, and both ends are fixed in a gas-tight manner. A plurality of independent hollow cylindrical or rectangular granule holding cylinders are arranged, and the processing medium gas can be supplied to the granular holding cylinders from a wind box installed below through the rotating lattice. A granular material processing device characterized by:
JP10028583A 1983-06-07 1983-06-07 Apparatus for treating particulate lumpy material Granted JPS59225732A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10028583A JPS59225732A (en) 1983-06-07 1983-06-07 Apparatus for treating particulate lumpy material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10028583A JPS59225732A (en) 1983-06-07 1983-06-07 Apparatus for treating particulate lumpy material

Publications (2)

Publication Number Publication Date
JPS59225732A JPS59225732A (en) 1984-12-18
JPH0325217B2 true JPH0325217B2 (en) 1991-04-05

Family

ID=14269915

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10028583A Granted JPS59225732A (en) 1983-06-07 1983-06-07 Apparatus for treating particulate lumpy material

Country Status (1)

Country Link
JP (1) JPS59225732A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104697358B (en) * 2013-12-05 2018-04-20 北新集团建材股份有限公司 A kind of vertical powder cooler

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5629668U (en) * 1979-08-10 1981-03-20

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5629668U (en) * 1979-08-10 1981-03-20

Also Published As

Publication number Publication date
JPS59225732A (en) 1984-12-18

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