JPS626025Y2 - - Google Patents

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Publication number
JPS626025Y2
JPS626025Y2 JP1982106737U JP10673782U JPS626025Y2 JP S626025 Y2 JPS626025 Y2 JP S626025Y2 JP 1982106737 U JP1982106737 U JP 1982106737U JP 10673782 U JP10673782 U JP 10673782U JP S626025 Y2 JPS626025 Y2 JP S626025Y2
Authority
JP
Japan
Prior art keywords
charging
cooling chamber
hopper
cone
temperature
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
JP1982106737U
Other languages
Japanese (ja)
Other versions
JPS5911833U (en
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 filed Critical
Priority to JP10673782U priority Critical patent/JPS5911833U/en
Publication of JPS5911833U publication Critical patent/JPS5911833U/en
Application granted granted Critical
Publication of JPS626025Y2 publication Critical patent/JPS626025Y2/ja
Granted legal-status Critical Current

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  • Chutes (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
  • Auxiliary Methods And Devices For Loading And Unloading (AREA)
  • Feeding Of Articles To Conveyors (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Description

【考案の詳細な説明】 本考案は高温固体を対向流竪型冷却装置の冷却
室に分配装入する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for distributing high-temperature solids into the cooling chamber of a counterflow vertical cooling system.

高温固体と冷却ガスを冷却室内で対向流により
接触させ熱回収する対向流竪型冷却設備におい
て、処理能力を向上できるようにするためには、
冷却室の個数を増やすか、あるいは個数はそのま
まとし容積を増やすかのいずれかを選択しなけれ
ばならないが、前者の場合はコストの面で得策で
はないので、後者の方向で研究が進められてい
る。
In order to improve the processing capacity of counterflow vertical cooling equipment, which recovers heat by bringing high-temperature solids and cooling gas into contact with each other in a cooling chamber through counterflow,
A choice must be made to either increase the number of cooling chambers or to leave the number unchanged and increase the volume, but the former is not a good idea from a cost standpoint, so research is progressing in the latter direction. There is.

しかし、種々の粒度分布を有する高温固体を取
扱う対向流竪型冷却設備において冷却室の内径を
大きくしていくと、冷却室内で高温固体の粒度偏
析が助長され、その結果、高温固体の冷却が均一
に行われなくなるので、冷却ガスと高温固体との
間の熱伝達率が極端に低下するという問題があ
る。
However, in counter-flow vertical cooling equipment that handles high-temperature solids with various particle size distributions, increasing the internal diameter of the cooling chamber promotes particle size segregation of the high-temperature solids within the cooling chamber, and as a result, cooling of the high-temperature solids becomes difficult. Since the heat transfer is not carried out uniformly, there is a problem in that the heat transfer coefficient between the cooling gas and the high-temperature solid is extremely reduced.

本考案は上述の従来の問題点を解決することを
目的とするもので、高温固体の落下口と冷却室の
間に円錐体を配設し、該円錐体の外周に複数の集
合ホツパを配設し、該各集合ホツパの下部開口の
下方に装入ホツパを各々配設し、該各装入ホツパ
内に上記各下部開口の下方に位置するよう粒度偏
析防止金具を各々配置し、該各装入ホツパの下部
装入ノズルを前記冷却室と各々連絡せしめ、さら
に上記落下口と円錐体との間に、上記落下口を中
心として旋回する旋回シユートを配設したことを
特徴とする高温固体の分配装入装置、にかかるも
のである。
The purpose of this invention is to solve the above-mentioned conventional problems. A cone is disposed between the drop port for high-temperature solids and the cooling chamber, and a plurality of collecting hoppers are disposed around the outer circumference of the cone. A charging hopper is arranged below the lower opening of each collecting hopper, a particle size segregation prevention fitting is arranged in each charging hopper so as to be located below each lower opening, and each A high-temperature solid, characterized in that the lower charging nozzles of the charging hopper are connected to the cooling chamber, and a rotating chute that rotates around the dropping port is provided between the dropping port and the cone. This is related to the distribution and charging device.

以下本考案の実施例を図面により説明する。 Embodiments of the present invention will be described below with reference to the drawings.

第1図及び第2図は本考案について示すもの
で、高温固体の落下口1の真下に頂部が位置する
ようにして分配円錐体2を設け、該分配円錐体2
の外周に該分配円錐体2を四方から取囲むように
して4個の集合ホツパ3を配設している。また下
面に軸支した複数のローラ4を環状レール5に乗
せ転動させることにより落下口1を中心に、即ち
分配円錐体2を中心に回転し得るようにして落下
口1と分配円錐体2との間に設けた大径の歯車6
の中心部に旋回シユート7を設け、上記歯車6と
噛合する小径の歯車8に傘歯車9を介し旋回駆動
装置10を接続し、該駆動装置10により大径の
歯車6を回転させて落下口1を中心に旋回シユー
ト7を分配円錐体2上において一定の旋回速度で
連続的に旋回させたり、あるいは集合ホツパ3各
位置で任意の一定時間停止させるようにして間歇
的に旋回させ得るようにし、上記落下口1、旋回
シユート7、分配円錐体2及び集合ホツパ3を経
て集合ホツパ3の下部開口(装入口)11から落
下した高温固体12を受ける装入ホツパ13を上
部に備えた4本の装入ノズル14を冷却室15の
頂部に挿入している。16は装入ホツパ13に設
けた粒度偏析防止金具、17は冷却室15に設け
た冷却ガス出口である。
Figures 1 and 2 show the present invention, in which a distribution cone 2 is provided with its top located directly below the drop opening 1 for hot solids;
Four collecting hoppers 3 are arranged around the outer periphery of the distribution cone 2 so as to surround it from all sides. In addition, by rolling a plurality of rollers 4 supported on the lower surface on an annular rail 5, the rollers 4 can be rotated around the drop opening 1, that is, around the distribution cone 2. A large diameter gear 6 installed between
A swing chute 7 is provided at the center of the shaft, and a swing drive device 10 is connected via a bevel gear 9 to a small-diameter gear 8 that meshes with the gear 6, and the drive device 10 rotates the large-diameter gear 6 to open the drop opening. The chute 7 can be rotated continuously on the distribution cone 2 at a constant rotation speed, or can be rotated intermittently by stopping at each position of the collecting hopper 3 for an arbitrary fixed period of time. , four pipes each having a charging hopper 13 at the top for receiving the high-temperature solids 12 that have fallen from the lower opening (charging port) 11 of the collecting hopper 3 via the drop port 1, the rotating chute 7, the distribution cone 2, and the collecting hopper 3. A charging nozzle 14 is inserted into the top of the cooling chamber 15. Reference numeral 16 indicates a metal fitting for preventing grain size segregation provided in the charging hopper 13, and reference numeral 17 indicates a cooling gas outlet provided in the cooling chamber 15.

上記実施例において冷却室15に高温固体12
の装入を行う場合は、旋回シユート7を一定の回
転速度で旋回させつつ落下口1から旋回シユート
7に高温固体12を落下させるか、あるいは旋回
シユート7を集合ホツパ3各位置で任意の一定時
間停止させるようにして間歇的に旋回させつつ落
下口1から旋回シユート7に高温固体12を落下
させる。
In the above embodiment, the high temperature solid 12 is placed in the cooling chamber 15.
When charging, the high-temperature solids 12 are dropped from the drop port 1 into the rotating chute 7 while rotating the rotating chute 7 at a constant rotation speed, or the rotating chute 7 is rotated at an arbitrary constant speed at each position of the collecting hopper 3. The high-temperature solid 12 is dropped from the drop port 1 into the rotating chute 7 while being rotated intermittently so as to stop for a certain period of time.

旋回シユート7を一定速度で旋回させた場合に
おいて旋回シユート7から流出した高温固体12
は、分配円錐体2の表面を等分布で降下し、各集
合ホツパ3に等量の高温固体12が捕集される。
また旋回シユート7を間歇的に旋回させた場合に
おいて旋回シユート7から流出した高温固体12
は、分配円錐体2の表面を目的位置の集合ホツパ
3に向け降下し、各集合ホツパ3には同様に等量
の高温固体12が捕集される。
High-temperature solid 12 flowing out from the rotating chute 7 when the rotating chute 7 is rotated at a constant speed
descends in an even distribution over the surface of the distribution cone 2, and an equal amount of hot solid 12 is collected in each collecting hopper 3.
In addition, when the rotating chute 7 is rotated intermittently, the high temperature solid 12 flowing out from the rotating chute 7
is lowered with the surface of the distribution cone 2 toward the collecting hopper 3 at the target location, and each collecting hopper 3 similarly collects an equal amount of high-temperature solid 12.

集合ホツパ3に捕集された高温固体は下部開口
から直下の装入ホツパ13内へ落下する。すなわ
ち、旋回シユート7、分配円錐体2を半径方向下
方に降下した高温固体12は下部開口11により
直下方向に向きが変えられる。さらに、装入ホツ
パ13内の粒度偏析防止金具16により半径方向
に均一に分散せしめられより均一に装入ホツパ1
3内に装入される。さらに又、4つの装入ホツパ
13の各装入ノズル14から均等に冷却室15内
へ放出されるため、高温固体は略完全に冷却室1
5内へ均一装入される。
The high temperature solids collected in the collecting hopper 3 fall into the charging hopper 13 directly below from the lower opening. That is, the high-temperature solid 12 that has descended radially downward through the rotating chute 7 and the distribution cone 2 is turned directly downward by the lower opening 11. Furthermore, the particles are uniformly dispersed in the radial direction by the metal fitting 16 in the charging hopper 13 to prevent grain size segregation, and the grains are evenly distributed in the charging hopper 13.
3. Furthermore, since the charging nozzles 14 of the four charging hoppers 13 are evenly discharged into the cooling chamber 15, the high-temperature solids are almost completely discharged into the cooling chamber 15.
5 is charged uniformly.

冷却室15内に装入された高温固体12は冷却
室15の下部から順次切出されて冷却室15内を
降下し、冷却室15の下部から吹込まれ上昇する
冷却ガスと接触して冷却され、一方冷却ガスは高
温ガスとなり冷却ガス出口17から外部に取出さ
れる。
The high-temperature solid 12 charged into the cooling chamber 15 is sequentially cut out from the lower part of the cooling chamber 15, descends within the cooling chamber 15, and is cooled by contacting the cooling gas blown in from the lower part of the cooling chamber 15 and rising. On the other hand, the cooling gas becomes a high-temperature gas and is taken out from the cooling gas outlet 17.

以上のように本考案では、各装入ホツパ13に
高温固体12を均等に分配でき、従つて各装入ノ
ズル14から等量の高温固体12を冷却室15に
装入できるので、冷却室15内で高温固体12の
粒度偏析が助長されることはない。
As described above, in the present invention, the high-temperature solids 12 can be evenly distributed to each charging hopper 13, and therefore an equal amount of high-temperature solids 12 can be charged into the cooling chamber 15 from each charging nozzle 14. Particle size segregation of the high-temperature solid 12 within the temperature range is not promoted.

なお前記実施例では集合ホツパ及び装入ノズル
の個数をそれぞれ4個としたが、2個以上であれ
ばよく、その他本考案の要旨を逸脱しない範囲に
おいて種々の変更を加え実施できること等は勿論
である。
In the above embodiment, the number of collecting hoppers and charging nozzles was four each, but it is sufficient to have two or more, and it goes without saying that various changes can be made without departing from the gist of the present invention. be.

本考案によれば前述したように高温固体を旋回
シユートにより円錐体(分配円錐体)の表面を等
分布に、あるいは各集合ホツパに向け一定量づつ
降下させ、各集合ホツパに確実に等量の高温固体
を捕集せしめ得るようにし、各集合ホツパから各
装入ホツパへ装入する際粒度偏析防止金具により
分散させ、さらに複数の装入ノズルに高温固体を
均等に分配できるようにし、各装入ノズルが冷却
室内に等量の高温固体を装入できるようにしたの
で、種々の粒度分布を有する高温固体を大径の冷
却室に装入した場合に冷却室内で高温固体の粒度
偏析が助長されることをなくせ、従つて高温固体
の均一な冷却を行うことが可能になる、という優
れた効果を奏し得る。
According to the present invention, as mentioned above, high-temperature solids are distributed evenly on the surface of a cone (distribution cone) by a rotating chute, or are lowered by a fixed amount toward each collecting hopper, thereby ensuring that an equal amount is delivered to each collecting hopper. The high-temperature solids can be collected, dispersed by particle size segregation prevention fittings when charging from each collecting hopper to each charging hopper, and the high-temperature solids can be evenly distributed to multiple charging nozzles, so that each charging Since the inlet nozzle can charge the same amount of high-temperature solids into the cooling chamber, when high-temperature solids with various particle size distributions are charged into a large-diameter cooling chamber, particle size segregation of the high-temperature solids in the cooling chamber is promoted. Therefore, it is possible to achieve the excellent effect of making it possible to uniformly cool the high-temperature solid.

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

第1図及び第2図は本考案の実施例を示すもの
で、第1図は縦断面図、第2図は第1図の−
矢視図である。 1……落下口、2……分配円錐体、3……集合
ホツパ、7……旋回シユート、12……高温固
体、13……装入ホツパ、14……装入ノズル、
15……冷却室。
1 and 2 show an embodiment of the present invention, FIG. 1 is a longitudinal sectional view, and FIG. 2 is a -
It is an arrow view. 1... Falling port, 2... Distribution cone, 3... Collection hopper, 7... Rotating chute, 12... High temperature solid, 13... Charging hopper, 14... Charging nozzle,
15...Cooling room.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 高温固体の落下口と冷却室の間に円錐体を配設
し、該円錐体の外周に複数の集合ホツパを配設
し、該各集合ホツパの下部開口の下方に装入ホツ
パを各々配設し、該各装入ホツパ内に上記各下部
開口の下方に位置するよう粒度偏析防止金具を
各々配置し、該各装入ホツパの下部装入ノズルを
前記冷却室と各々連絡せしめ、さらに上記落下口
と円錐体との間に、上記落下口を中心として旋回
する旋回シユートを配設したことを特徴とする高
温固体の分配装入装置。
A cone is disposed between the high-temperature solids fall port and the cooling chamber, a plurality of collecting hoppers are disposed around the outer periphery of the cone, and a charging hopper is disposed below the lower opening of each collecting hopper. Particle size segregation prevention fittings are arranged in each charging hopper so as to be located below each of the lower openings, the lower charging nozzle of each charging hopper is connected to the cooling chamber, and the lower charging nozzle of each charging hopper is connected to the cooling chamber, and A distributing and charging device for high-temperature solids, characterized in that a rotating chute that rotates around the drop port is disposed between the port and the cone.
JP10673782U 1982-07-14 1982-07-14 Distributing and charging equipment for high temperature solids Granted JPS5911833U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10673782U JPS5911833U (en) 1982-07-14 1982-07-14 Distributing and charging equipment for high temperature solids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10673782U JPS5911833U (en) 1982-07-14 1982-07-14 Distributing and charging equipment for high temperature solids

Publications (2)

Publication Number Publication Date
JPS5911833U JPS5911833U (en) 1984-01-25
JPS626025Y2 true JPS626025Y2 (en) 1987-02-12

Family

ID=30249656

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10673782U Granted JPS5911833U (en) 1982-07-14 1982-07-14 Distributing and charging equipment for high temperature solids

Country Status (1)

Country Link
JP (1) JPS5911833U (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2754048B2 (en) * 1989-07-10 1998-05-20 大和製衡株式会社 Article supply device in combination scale
DK176326B1 (en) * 2003-05-14 2007-08-13 Smidth As F L Device for dividing a stream of particulate or powdered material into partial streams
PL3096101T3 (en) * 2015-05-20 2018-09-28 Primetals Technologies Austria GmbH Cooling device for cooling bulk material
WO2018121733A1 (en) * 2016-12-29 2018-07-05 Primetals Technologies Austria GmbH Cooling of bulk material
CN110678711B (en) * 2016-12-29 2022-03-01 首要金属科技奥地利有限责任公司 Cooling of bulk material
DE102018117351B4 (en) * 2018-07-18 2020-11-05 Fette Compacting Gmbh Soft of a tablet drain of a tablet press

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5053948A (en) * 1973-09-13 1975-05-13
JPS5169055A (en) * 1974-12-06 1976-06-15 Toshihiko Satake Kokusono bunsansochi

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5225814Y2 (en) * 1972-11-28 1977-06-11

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5053948A (en) * 1973-09-13 1975-05-13
JPS5169055A (en) * 1974-12-06 1976-06-15 Toshihiko Satake Kokusono bunsansochi

Also Published As

Publication number Publication date
JPS5911833U (en) 1984-01-25

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