JPS5951355B2 - Classifier - Google Patents

Classifier

Info

Publication number
JPS5951355B2
JPS5951355B2 JP14580278A JP14580278A JPS5951355B2 JP S5951355 B2 JPS5951355 B2 JP S5951355B2 JP 14580278 A JP14580278 A JP 14580278A JP 14580278 A JP14580278 A JP 14580278A JP S5951355 B2 JPS5951355 B2 JP S5951355B2
Authority
JP
Japan
Prior art keywords
classification
classifier
impeller
classification impeller
particles
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
JP14580278A
Other languages
Japanese (ja)
Other versions
JPS5573376A (en
Inventor
益男 細川
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.)
Hosokawa Funtai Kogaku Kenkyusho KK
Original Assignee
Hosokawa Funtai Kogaku Kenkyusho 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 Hosokawa Funtai Kogaku Kenkyusho KK filed Critical Hosokawa Funtai Kogaku Kenkyusho KK
Priority to JP14580278A priority Critical patent/JPS5951355B2/en
Priority to GB7940364A priority patent/GB2041251B/en
Priority to CA340,474A priority patent/CA1126215A/en
Priority to DE2947310A priority patent/DE2947310C2/en
Priority to FR7928997A priority patent/FR2442083A1/en
Priority to US06/098,275 priority patent/US4260478A/en
Publication of JPS5573376A publication Critical patent/JPS5573376A/en
Publication of JPS5951355B2 publication Critical patent/JPS5951355B2/en
Expired legal-status Critical Current

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  • Combined Means For Separation Of Solids (AREA)

Description

【発明の詳細な説明】 本発明は粉粒体を気流にのせ遠心力と求心力を同時に作
用させ所望の粒径域で選別する分級装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a classifying device for sorting powder particles into a desired particle size range by applying centrifugal force and centripetal force simultaneously to the particles in an air flow.

従来よりこの種の分級装置には各種のものがあるが、一
般には被選別材料(以下単に材料という)を気流ととも
に分級機内に導入させ、該分級機内で回転する分級羽根
車によつて遠心力を付与させる一方気流の流れを該分級
羽根車の内部を経由して機外に排出させるよう構成して
いるため気流中の材料は同時に付与される遠心力と求心
力の作用差により分離、選別されるものがある。そして
この種の分級機においては材料がよく分散されているこ
とが望ましい。しかし従来のものではこの分散効果が充
分でな<、材料中の凝集した微粉粒子の一部は単粒子に
分散されないで粗粉域に送られるおそれがあつた。そし
てその結果として粗粉中に微粉が混入するという問題が
あり、それは微粉の回収率及び分級効率の低下という面
に現われていた。そこで本発明は材料粒子の分散を効果
的に促進させ、次工程の分級作用を効率よく行なわせ、
微粉回収率及び分級効率を向上させることを目的とする
ものである。次に本発明の構成を実施例により説明する
。1は分級機本体であり、その機胴内上部には回転軸3
により回転可能に支持された回転外周面が逆円錐状を形
成する分級羽根車2と、該分級羽根車2を包囲し、該分
級羽根車2と適当な間隔を有し、かつ分級羽根車2の回
転方向下手側に向つてスリット状に開口させた流入口1
5を具備する通気部材7を配設させ、分級機本体1の機
胴内壁面14との間に気室8を形成させるとともに該気
室8に連通して2次気体入口9を配設している。
Conventionally, there are various types of classification devices of this type, but in general, the material to be sorted (hereinafter simply referred to as material) is introduced into the classifier along with an airflow, and centrifugal force is applied by a classification impeller rotating inside the classifier. The material in the airflow is separated and sorted by the difference between the centrifugal force and the centripetal force, which are applied at the same time. There are things to do. In this type of classifier, it is desirable that the material be well dispersed. However, in the conventional method, this dispersion effect was not sufficient, and there was a risk that some of the aggregated fine powder particles in the material would not be dispersed into single particles and would be sent to the coarse powder region. As a result, there is a problem that fine powder is mixed into coarse powder, which is manifested in a decrease in the recovery rate and classification efficiency of fine powder. Therefore, the present invention effectively promotes the dispersion of material particles and efficiently performs the classification action in the next step.
The purpose is to improve the fine powder recovery rate and classification efficiency. Next, the configuration of the present invention will be explained using examples. 1 is the main body of the classifier, and the rotating shaft 3 is located in the upper part of the body of the machine.
a classification impeller 2 whose rotating outer peripheral surface forms an inverted conical shape and is rotatably supported by a classification impeller 2; An inlet 1 having a slit-like opening toward the lower side in the rotational direction.
5 is disposed, an air chamber 8 is formed between it and the body inner wall surface 14 of the classifier main body 1, and a secondary gas inlet 9 is disposed in communication with the air chamber 8. ing.

なお本実施例では気室8を隔壁11により仕切り、気室
Ba、8bとしこれに対処してそれぞれに2次気、体入
口9a、9bを具備させているが、とくに二室に限定す
るものではない。以上の機胴内上部の構造に対し、下部
には気流にのせて材料を導入させる吹込管4と、選別さ
れた粗粉側粒子を機外に取出すための粗粉排出口6と、
粗粉側に移行するフ材料の風篩を目的とする気体を導入
するための3次気体入口10と前記案内羽根7と連続し
て配設され風篩部を形成する風篩リング13が設けられ
ている。12は吹込管4の開口で、該開口12は前記分
級羽根車2と同心で対向しており、かつ、クその位置は
条件に応じ分級羽根車2との間隔、および風篩リング1
3の下端部との間隔を調節可能にすべく構成されている
In this embodiment, the air chamber 8 is partitioned by a partition wall 11 into air chambers Ba and 8b, each of which is provided with a secondary air inlet and a body inlet 9a and 9b, but this is particularly limited to two chambers. isn't it. In contrast to the above structure of the upper part of the inside of the machine body, the lower part includes a blowing pipe 4 for introducing the material along with the airflow, and a coarse powder outlet 6 for taking out the sorted coarse powder side particles to the outside of the machine.
A tertiary gas inlet 10 for introducing gas for the purpose of wind sieving the material transferred to the coarse powder side and a wind sieve ring 13 which is disposed continuously with the guide vanes 7 and forms a wind sieve part are provided. It is being Reference numeral 12 denotes an opening of the blowing pipe 4. The opening 12 is concentrically opposed to the classification impeller 2, and its position is determined according to the distance from the classification impeller 2 and the wind sieve ring 1.
3 is configured to allow adjustment of the distance from the lower end.

なお本実施例では吹込管4に敢合する調節筒16により
前記間隔は調節可能に構成されているが、該調節筒16
を吹込管4内に可動可能に畝合させることによつては機
外よりの調節を行うことができる。また風篩リング13
を脱着式として適当内径のものにすることもできる。ま
た本実施例では分級羽根車2を回転時にその外周面が逆
円錐状を形成するような構造にしており、これに伴い通
気部材7も分級羽根車2に沿つた形状をなしているが分
級羽根車2に他の形状のものを用いたり、通気部材7を
円筒状に設けても本発明を実施できる。また前記2次気
体入口9a,9b及び3次気体体入口10は前記分級羽
根車2の回転方向に合せ、かつ分級機本体1の機胴に対
し接線方向に向けて開口されており、通気部材7及び風
篩リング13を通過する気流の流れを均一にし安定させ
るものであるがとくに開口方向を限定されるものではな
い。なお本実施例において通気部材7は平板羽根状の部
材を一定の間隙を保持させ、かつ分級羽根車2の回転方
向下手側に向つて傾斜させるとともに隣接するそれぞれ
の端部が重なるように配設して構成しているが、このほ
かにも前記羽根状部材を流線に沿つた曲面状に形成した
もの、あるいは分級羽根車2の回転方向に傾斜して穿孔
されたパンチプレートなどでも適用可能である。要は分
級羽根車2の回転方向下手側に向つて傾斜、あるいは通
気部材7の内周面接線方向に近い方向に比較的小孔の開
口が該通気部材7の内周面に沿つて均一に分布して配設
されたものであればよい。なお前記微粉排出口5は図示
省略のサイタロンコレクタ一、パックプール.タ一など
の捕集器を介して図示省略の風車に連通される。以上の
ような構成において気流と共に吹込管4から分級機本体
1内に搬送された材料は搬送気流と分級羽根車2の回転
(方向は図中矢印に示す).に伴う旋回気流による攪拌
作用を受けて分散、単粒子化されるとともに分級羽根車
2の回転に伴う遠心力Fと該分級羽根車2の中心部に向
う気流jによる求心力Kを同時に受けるが、該分級羽根
車2の回転速度と分級羽根車2の中心部に向う気流4速
度を所定の値になるように調節することによつて所望の
選別作用を材料粒子に付与させ、該選別作用によつて求
心力Kの方が大きい微粉側粒子は分級羽根車2の中心部
に気流jと共に吸引、微粉排出口5より機外に搬出され
たのち前記捕集器によつて気体と分離、捕集される。
In this embodiment, the above-mentioned interval is configured to be adjustable by an adjustment cylinder 16 that fits into the blow pipe 4; however, the adjustment cylinder 16
Adjustment from outside the machine can be made by movably fitting into the blow tube 4. Also, wind sieve ring 13
It is also possible to make it a removable type with an appropriate inner diameter. Furthermore, in this embodiment, the classification impeller 2 is structured so that its outer peripheral surface forms an inverted conical shape when rotating, and accordingly, the ventilation member 7 also has a shape that follows the classification impeller 2. The present invention can be practiced even if the impeller 2 has a different shape or the ventilation member 7 is provided in a cylindrical shape. Further, the secondary gas inlets 9a, 9b and the tertiary gas inlet 10 are opened in accordance with the rotating direction of the classification impeller 2 and in a tangential direction to the body of the classifier main body 1, and are opened as ventilation members. 7 and the air sieve ring 13 to make the flow uniform and stable, but the opening direction is not particularly limited. In this embodiment, the ventilation member 7 is a flat blade-like member that maintains a constant gap, is inclined toward the lower side in the rotational direction of the classification impeller 2, and is arranged so that adjacent ends thereof overlap. However, it is also possible to use a blade-like member formed into a curved surface along a streamline, or a punch plate with holes tilted in the rotation direction of the classification impeller 2. It is. The point is that the openings of the small holes are relatively uniform along the inner peripheral surface of the ventilation member 7 at an angle toward the downstream side in the rotational direction of the classification impeller 2, or in a direction close to the inner peripheral surface line of the ventilation member 7. It is sufficient if they are distributed and arranged. The fine powder discharge port 5 is connected to a Cytalon collector, a pack pool, etc. (not shown). It is communicated with a windmill (not shown) via a collector such as a turbine. In the above configuration, the material is transported from the blowing pipe 4 into the classifier main body 1 along with the airflow due to the rotation of the transporting airflow and the classification impeller 2 (the direction is shown by the arrow in the figure). It is dispersed and made into single particles under the agitation effect of the swirling airflow associated with it, and is simultaneously subjected to the centrifugal force F caused by the rotation of the classification impeller 2 and the centripetal force K due to the airflow j directed toward the center of the classification impeller 2. By adjusting the rotational speed of the classification impeller 2 and the speed of the airflow toward the center of the classification impeller 2 to predetermined values, a desired sorting effect is imparted to the material particles, and the sorting effect is applied to the material particles. Therefore, the fine particles for which the centripetal force K is larger are sucked into the center of the classification impeller 2 along with the air flow J, and after being carried out of the machine from the fine powder outlet 5, they are separated from the gas and collected by the collector. be done.

他方、遠心力Fが大きい粗粉粒子は、回転外周囲に移行
し、前記通気部材7によつて形成される内周壁部に到達
する。ここで本発明の要件である通気部材7の配設によ
り、前記搬送気流により搬送された材料は該搬送気流と
分級羽根車2の回転に伴う旋回気流に加えて2次気体入
口9a,9bから導入され、通気部材7に具備された流
入口15より該通気部材7の内周面に沿つて吹き込む流
入気流1によつてその分散作用を著しく高められ、急速
に分散されたのち、再び前記分級羽根車2外周部に搬送
され選別が行われる。つまり該流入口15を通過する流
入気流1はきわめて高速度化されており、しかも全周か
ら均一に吹き込むため、あたかも高速度で流れる気膜を
形成したような状態になり、従来の搬送気流及び分級羽
根車2の回転に伴う旋回気流との合流に際しては著しい
攪拌作用が発生し、そのため気流中の材料はきわめて効
率よく分散、単粒子化される。そしてこのようなくり返
し選別作用を付与されたのち、なお粗粉域にある材料は
通気部材7の内壁面に沿つて下降するが前記風篩リング
13を通過するに際し3次気体入口10より導入された
上昇気流eによる風篩と、これにともなう分散作用と選
別作用を受け粗粉側粒子中になお付着、混在する微粉粒
子は分離され、前記搬送気流により搬送、再度選別作用
を付与されたのち分級羽根車2を通して微粉排出口5か
ら、粗粉粒子は風篩リング13を通過、落下して粗粉排
出口6から、それぞれ機外に排出、捕集される。このよ
うにして本実施例による分級装置に供給された材料は、
分散作用と選別作用とをくり返し付与されることによつ
て、一粒子にとつて見れば多くの分級の機会を与えられ
、分級性能が高められる。以上のように本発明によれば
粗粉側粒子中に微粉粒子が付着、凝集した状態で機胴内
を下降、あるいは粗粉中に混入する度合がきわめて減少
されることによつて微粉の回収率及び分級効率を向上さ
せること、また粗粉を製品として回収する場合、高品質
のものが得られること、効果的な分散作用と効率よい分
級作用によつて分級能力を一段と向上させることができ
るなど、本発明は工業上きわめて有用で゛ある。
On the other hand, coarse particles with a large centrifugal force F move to the outer circumference of the rotation and reach the inner circumferential wall formed by the ventilation member 7. Here, by providing the ventilation member 7, which is a requirement of the present invention, the material transported by the transport airflow is transferred from the secondary gas inlets 9a and 9b in addition to the transport airflow and the swirling airflow caused by the rotation of the classification impeller 2. The dispersion effect of the inflow air 1 blown along the inner circumferential surface of the ventilation member 7 from the inflow port 15 provided in the ventilation member 7 is greatly enhanced, and after being rapidly dispersed, the classification is performed again. It is transported to the outer circumference of the impeller 2 and sorted. In other words, the inflow airflow 1 passing through the inflow port 15 has an extremely high velocity and is uniformly blown from all around the circumference, so that it appears to form a gas film flowing at high speed, unlike the conventional conveying airflow. When the airflow merges with the swirling airflow caused by the rotation of the classification impeller 2, a significant agitation effect occurs, so that the material in the airflow is extremely efficiently dispersed and made into single particles. After being subjected to such repeated sorting actions, the material still in the coarse powder region descends along the inner wall surface of the ventilation member 7, but as it passes through the air sieve ring 13, it is introduced from the tertiary gas inlet 10. The fine powder particles that are still adhered to or intermixed with the coarse particles are separated by the wind sieving caused by the rising air current e and the accompanying dispersion and sorting effects, and are transported by the conveying air flow and subjected to the sorting effect again. Coarse particles pass through the classification impeller 2, pass through the wind sieve ring 13, fall, and are discharged and collected from the coarse powder outlet 6 to the outside of the machine. The material thus supplied to the classifier according to this example is
By repeatedly applying the dispersing action and the sorting action, many opportunities for classification are given to one particle, and the classification performance is improved. As described above, according to the present invention, the degree of fine powder particles adhering to the coarse powder side particles, descending in the machine body in an agglomerated state, or being mixed into the coarse powder is extremely reduced, so that fine powder can be recovered. In addition, when recovering coarse powder as a product, high quality can be obtained, and the classification ability can be further improved through effective dispersion and efficient classification. The present invention is extremely useful industrially.

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

第1図は本発明の実施例を示す要部断面図、第2図は第
1図A−A断面図、第3図は第2図B部拡大図である。 図において、1 ・・・・・・分級機本体、2 ・・・
・・・分級羽根車、4・・・・・・吹込管、5 ・・・
・・・微粉排出口、6・・・・・・粗粉排出口、7 ・
・・・・・通気部材、8 ・・・・・・気室、9 ・・
・・・・ 2次気体入口、14・・・・・・内壁面、1
5・・・・・・流入口である。
1 is a sectional view of a main part showing an embodiment of the present invention, FIG. 2 is a sectional view taken along line AA in FIG. 1, and FIG. 3 is an enlarged view of a portion B in FIG. 2. In the figure, 1... the main body of the classifier, 2...
...Classifying impeller, 4...Blowing pipe, 5...
... Fine powder discharge port, 6 ... Coarse powder discharge port, 7 ・
...Ventilation member, 8 ...Air chamber, 9 ...
...Secondary gas inlet, 14...Inner wall surface, 1
5...Inflow port.

Claims (1)

【特許請求の範囲】[Claims] 1 気流にのせて被選別材料を搬入させる吹込管4と、
微粉排出口5及び粗排出口6を有する分級機本体1と、
該分級機本体1内に設けられた分級羽根車2とよりなり
、該分級羽根車2を回転させ、選別した微分粒子は該分
級羽根車2の肉側に吸引し前記微粉排出口5より、粗粉
粒子は前記粗粉排出口6より、それぞれ排出すべく構成
された分級装置において、前記分級機本体1内に分級羽
根車2を包囲し、該分級羽根車2と適当な間隔を有し、
該分級羽根車2の回転方向下手側に向つて開口させた多
数の流入口15を具備する通気部材7を配設させ、該通
気部材7によつて前記分級機本体1内壁面14との間に
気室8を形成させるとともに該気室8に連通させて2次
気体入口9を配設したことを特徴とする分級装置。
1. A blowing pipe 4 that carries in the material to be sorted on an air current;
a classifier main body 1 having a fine powder outlet 5 and a coarse outlet 6;
It consists of a classification impeller 2 provided in the classifier main body 1, the classification impeller 2 is rotated, the sorted differential particles are sucked into the meat side of the classification impeller 2, and the fine powder is discharged from the fine powder outlet 5. In a classifier configured to discharge the coarse powder particles from the coarse powder discharge ports 6, the classifier body 1 surrounds a classification impeller 2, and is spaced from the classification impeller 2 at an appropriate distance. ,
A ventilation member 7 having a large number of inlets 15 opened toward the downstream side in the rotational direction of the classification impeller 2 is disposed, and the ventilation member 7 allows the air flow between the inner wall surface 14 of the classifier main body 1 and A classification device characterized in that an air chamber 8 is formed in the air chamber 8, and a secondary gas inlet 9 is provided in communication with the air chamber 8.
JP14580278A 1978-11-24 1978-11-24 Classifier Expired JPS5951355B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP14580278A JPS5951355B2 (en) 1978-11-24 1978-11-24 Classifier
GB7940364A GB2041251B (en) 1978-11-24 1979-11-22 Pneumatic classifier
CA340,474A CA1126215A (en) 1978-11-24 1979-11-23 Cyclone separator with stator-fan arrangement about the vortex finder
DE2947310A DE2947310C2 (en) 1978-11-24 1979-11-23 Through air sifter
FR7928997A FR2442083A1 (en) 1978-11-24 1979-11-23 APPARATUS FOR SORTING PARTICLES
US06/098,275 US4260478A (en) 1978-11-24 1979-11-28 Apparatus for classifying particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14580278A JPS5951355B2 (en) 1978-11-24 1978-11-24 Classifier

Publications (2)

Publication Number Publication Date
JPS5573376A JPS5573376A (en) 1980-06-03
JPS5951355B2 true JPS5951355B2 (en) 1984-12-13

Family

ID=15393482

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14580278A Expired JPS5951355B2 (en) 1978-11-24 1978-11-24 Classifier

Country Status (1)

Country Link
JP (1) JPS5951355B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE68986T1 (en) * 1987-07-03 1991-11-15 Ciba Geigy Ag SPRAY DRYERS FOR THE PRODUCTION OF POWDERS, AGGLOMERATES OR THE LIKE.

Also Published As

Publication number Publication date
JPS5573376A (en) 1980-06-03

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