JPH0511219Y2 - - Google Patents
Info
- Publication number
- JPH0511219Y2 JPH0511219Y2 JP1990020782U JP2078290U JPH0511219Y2 JP H0511219 Y2 JPH0511219 Y2 JP H0511219Y2 JP 1990020782 U JP1990020782 U JP 1990020782U JP 2078290 U JP2078290 U JP 2078290U JP H0511219 Y2 JPH0511219 Y2 JP H0511219Y2
- Authority
- JP
- Japan
- Prior art keywords
- hollow conduit
- housing
- axis
- conduit
- coal
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/52—Adaptations of pipes or tubes
- B65G53/528—Flux combining or dividing arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K3/00—Feeding or distributing of lump or pulverulent fuel to combustion apparatus
- F23K3/02—Pneumatic feeding arrangements, i.e. by air blast
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- General Engineering & Computer Science (AREA)
- Air Transport Of Granular Materials (AREA)
- Combined Means For Separation Of Solids (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
Description
【考案の詳細な説明】
本考案は石炭流の分割装置に係り、さらに詳し
く言えば、石炭の大きな流れを複数の小さな流れ
に確実に分割する装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coal stream splitting device, and more particularly to a device for reliably splitting a large stream of coal into a plurality of smaller streams.
従来技術においては、気流輸送石炭の大きな流
れを小さな流れに満足のゆくように分割すること
は困難であるとされていた。石炭を搬送する管が
分割されているいわゆる空気力学流分割機を用い
る1つの方法がある。しかし、この方法は次の欠
点を有している。分割の精度が希望値よりも劣る
こと、安定性の問題があること、流速が浸食を生
じること、特に導管内における変化しやすい底流
量が沈澱物や閉塞物を生じることなどである。し
かしながら、別の高価な方法で、別個の小供給導
管を用いるものもある。最後に、L.G.Caldwell
著の“Some Developments in the Feeding of
Coal to Fluidized Bed Combustors”の著書に
おいては、石炭は区分室間に回転装置によつて分
配されうるが、しかし、そこから分配される石炭
は濃密状態である旨が述べられている。 In the prior art, it has been difficult to satisfactorily divide large streams of airborne coal into smaller streams. One method is to use so-called aerodynamic flow dividers, in which the tubes conveying the coal are divided. However, this method has the following drawbacks. The accuracy of the segmentation is less than desired, there are stability issues, flow rates can cause erosion, and variable bottom flows, especially in conduits, can create sediments and blockages. However, other expensive methods use separate small supply conduits. Finally, LGCardwell
Author “Some Developments in the Feeding of
In the book "Coal to Fluidized Bed Combustors" it is stated that coal can be distributed between the compartments by means of a rotating device, but that the coal distributed therefrom is in a dense state.
本考案者は、複数の区分室間に大きな流れを機
械的に均等に分割し、その後区分室の内容物を稀
薄状態で小導管にそれぞれ移動させることによつ
て、石炭流の分割が安定してかつ浸食を激減させ
る低速度でもつて小流間に均等かつ正確になされ
うることを見い出した。 The present inventor has determined that by mechanically evenly dividing a large flow between multiple compartments and then transferring the contents of the compartments in a dilute state to each of the smaller conduits, the division of the coal stream is stabilized. It has been found that it can be done evenly and accurately between small streams and at low velocities which greatly reduces erosion.
最適実施例においては、区分室への分配は、回
転子の回転軸からずれた出口を有する中空回転子
によつてなされる。 In the preferred embodiment, distribution to the compartments is provided by a hollow rotor having an outlet offset from the axis of rotation of the rotor.
次に、図面を参照して、本考案の最適実施例の
構成および動作について説明する。図面は本考案
の最適実施例である流れ分割機10を示す。 Next, the configuration and operation of the preferred embodiment of the present invention will be described with reference to the drawings. The drawings illustrate a flow divider 10 that is a preferred embodiment of the present invention.
流れ分割機10にはハウジング12が設けられ
ている。ハウジング12内に、プーリ16および
ベルト18をかいして駆動されるシヤフト14が
回転自在に装着されている。中空導管回転子20
がシヤフト14と一体に回転できるようにシヤフ
ト14に装着されていて、回転子20は入口端に
じようご22を支持し、下端部24がシヤフト1
4と同軸ではないが、壁26によつて区分室に分
割された下方環状体上を回転掃引するように配置
されるようにずらされている。1対の壁26によ
つて仕切られた各区分室から出口管28が延びて
いる。 Flow divider 10 is provided with a housing 12 . A shaft 14, which is driven by a pulley 16 and a belt 18, is rotatably mounted within the housing 12. Hollow conduit rotor 20
is mounted on the shaft 14 so as to be able to rotate together with the shaft 14, the rotor 20 supports a funnel 22 at the inlet end, and the lower end 24 is attached to the shaft 14.
4, but are offset so as to be arranged in a rotational sweep over a lower annulus divided into compartments by walls 26. An outlet tube 28 extends from each compartment separated by a pair of walls 26.
出口管28は直径が38.1〜50.8mm(1.5〜2″)で
あり、入口導管30は出口管28に所望の速度を
維持するのに十分な量の空気を供給できる寸法に
なつている。 The outlet tube 28 is 1.5" to 2" in diameter and the inlet conduit 30 is sized to supply a sufficient amount of air to the outlet tube 28 to maintain the desired velocity.
動作のさいには、十分な量の搬送空気が入口導
管30から注入されて出口管28内の流出空気速
度を12.2m/s(40t/s)に維持する。この空気
の量および速度は、前述したCaldwellの著書に
おける分割機から分配する濃密または非気送形体
に比較して、出口管28を通して石炭を稀薄(気
送)状態で搬送するのに十分なものである。 In operation, a sufficient amount of carrier air is injected through the inlet conduit 30 to maintain the exit air velocity in the outlet conduit 28 at 40 t/s. This air volume and velocity is sufficient to convey the coal through the outlet pipe 28 in a lean (pneumatic) condition compared to the dense or non-pneumatic configuration dispensed from the splitter in the Caldwell book discussed above. It is.
石炭はじようご22をかいしてクラツシヤ(図
示せず)から6.35mm(0.25″)の粒径で供給され
る。 Coal is fed through a funnel 22 from a crusher (not shown) in a particle size of 6.35 mm (0.25'').
回転子20が回転したとき、回転子20は壁2
6で仕切られた種々の区分室に等量の石炭を連続
的に堆積する。これらの区分室から、導管30か
らの搬送空気がハウジング12を通つて移動し、
出口管28を通して等量の石炭を移動させる。 When the rotor 20 rotates, the rotor 20 hits the wall 2
Equal amounts of coal are successively deposited in the various compartments separated by 6. From these compartments, conveyed air from conduit 30 travels through housing 12;
An equal amount of coal is transferred through outlet pipe 28.
図面は本考案の分割機の斜視図である。
10……分割機、12……ハウジング、14…
…シヤフト、16……プーリ、18……ベルト、
20……回転子、22……じようご、24……下
端部、26……壁、28……出口管、30……入
口導管。
The drawing is a perspective view of the dividing machine of the present invention. 10...Divider, 12...Housing, 14...
...Shaft, 16...Pulley, 18...Belt,
20... Rotor, 22... Funnel, 24... Lower end, 26... Wall, 28... Outlet pipe, 30... Inlet conduit.
Claims (1)
放射状に延びる壁を立設して各壁相互間と前記ハ
ウジングの側壁との間に上端が開口した複数の区
分室を形成し、前記ハウジング上部から前記軸線
に沿つて石炭を導入する中空導管を挿入し、当該
中空導管の下端出口は前記区分室の上方において
前記軸線から偏心して位置せしめ、前記ハウジン
グの底面から前記軸線に沿つて挿入した回転シヤ
フトの上端を前記中空導管に連結して前記中空導
管を前記軸線を中心として回転させ、前記ハウジ
ングにおける前記中空導管の下端出口よりも高い
位置に前記ハウジング内に搬送空気を強制的に導
入する搬送空気導管を接続し、前記中空導管の出
口から出た石炭を前記搬送空気で下方に吹き飛ば
しながら前記区分室内に落下させると共に前記搬
送空気によつて前記排出用導管から外部に排出す
るようにしてなる石炭流の分割装置。 Walls extending radially around the axis are erected on the inner bottom surface of the vertical cylindrical housing to form a plurality of compartments each having an open upper end between each wall and the side wall of the housing, A hollow conduit for introducing coal from the top along the axis is inserted, a lower end outlet of the hollow conduit is positioned eccentrically from the axis above the compartment, and the hollow conduit is inserted from the bottom of the housing along the axis. The upper end of the rotating shaft is connected to the hollow conduit to rotate the hollow conduit about the axis, and the conveying air is forcibly introduced into the housing at a position higher than the lower end outlet of the hollow conduit in the housing. A conveying air conduit is connected, and the coal coming out of the outlet of the hollow conduit is blown downward by the conveying air and falls into the compartment, and is also discharged to the outside from the discharge conduit by the conveying air. A coal flow splitting device.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US54468883A | 1983-10-24 | 1983-10-24 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02119429U JPH02119429U (en) | 1990-09-26 |
| JPH0511219Y2 true JPH0511219Y2 (en) | 1993-03-19 |
Family
ID=24173172
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22381384A Pending JPS60114622A (en) | 1983-10-24 | 1984-10-24 | Method and device for dividing coal flow |
| JP1990020782U Expired - Lifetime JPH0511219Y2 (en) | 1983-10-24 | 1990-03-01 |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22381384A Pending JPS60114622A (en) | 1983-10-24 | 1984-10-24 | Method and device for dividing coal flow |
Country Status (6)
| Country | Link |
|---|---|
| JP (2) | JPS60114622A (en) |
| AU (1) | AU3441884A (en) |
| DE (1) | DE3438950A1 (en) |
| FR (1) | FR2557269A1 (en) |
| GB (1) | GB2148226A (en) |
| SE (1) | SE8405281L (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE460617B (en) * | 1985-06-20 | 1989-10-30 | Asea Stal Ab | SET FOR DRYING, CRUSHING AND DISTRIBUTION OF SOLID BRAINSLE FOR SOLID BRAINS |
| DE102009008927A1 (en) * | 2009-02-13 | 2010-09-02 | Heinen-Köhl Tobacco GmbH | Device for selectively feeding a plurality of delivery lines with a bulk material |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB312474A (en) * | 1928-05-09 | 1929-05-30 | George Roscoe Alden | Improvements in or relating to distribution means for pulverulent material |
| GB1067191A (en) * | 1962-10-17 | 1967-05-03 | Koppers Co Inc | Improvements in or relating to injection of particulate material into furnaces |
| JPS5335351Y2 (en) * | 1976-01-23 | 1978-08-29 | ||
| DE2611358B2 (en) * | 1976-03-18 | 1979-10-04 | Amazonen-Werke H. Dreyer Gmbh & Co Kg, 4507 Hasbergen | Machine for the pneumatic discharge of granular material |
| US4313386A (en) * | 1979-11-01 | 1982-02-02 | The Keller Corporation | System for transport of mixtures of solid particulate fuel and air, and rotary distributor suitable for use therein |
| DE3039384A1 (en) * | 1980-10-18 | 1982-05-19 | Ruhrkohle Ag | DEVICE FOR BLOWING (ALPHA) -HALBHYDRATE AND / OR (BETA) -HALBHYDRATE |
| JPS5889523A (en) * | 1981-11-17 | 1983-05-27 | Sumitomo Metal Ind Ltd | Method and equipment for distributing powder |
| US4536121A (en) * | 1983-04-22 | 1985-08-20 | Foster Wheeler Energy Corporation | Divided rotary valve feeder |
-
1984
- 1984-10-17 AU AU34418/84A patent/AU3441884A/en not_active Abandoned
- 1984-10-18 GB GB08426342A patent/GB2148226A/en not_active Withdrawn
- 1984-10-22 SE SE8405281A patent/SE8405281L/en not_active Application Discontinuation
- 1984-10-24 JP JP22381384A patent/JPS60114622A/en active Pending
- 1984-10-24 DE DE19843438950 patent/DE3438950A1/en not_active Withdrawn
- 1984-10-24 FR FR8416295A patent/FR2557269A1/en not_active Withdrawn
-
1990
- 1990-03-01 JP JP1990020782U patent/JPH0511219Y2/ja not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| GB8426342D0 (en) | 1984-11-21 |
| SE8405281D0 (en) | 1984-10-22 |
| JPH02119429U (en) | 1990-09-26 |
| JPS60114622A (en) | 1985-06-21 |
| DE3438950A1 (en) | 1985-05-02 |
| AU3441884A (en) | 1985-05-02 |
| FR2557269A1 (en) | 1985-06-28 |
| SE8405281L (en) | 1985-04-25 |
| GB2148226A (en) | 1985-05-30 |
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