JPS6039108Y2 - Powder classification device - Google Patents

Powder classification device

Info

Publication number
JPS6039108Y2
JPS6039108Y2 JP8330182U JP8330182U JPS6039108Y2 JP S6039108 Y2 JPS6039108 Y2 JP S6039108Y2 JP 8330182 U JP8330182 U JP 8330182U JP 8330182 U JP8330182 U JP 8330182U JP S6039108 Y2 JPS6039108 Y2 JP S6039108Y2
Authority
JP
Japan
Prior art keywords
classification
opening
wind
air
sieve
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
JP8330182U
Other languages
Japanese (ja)
Other versions
JPS58186882U (en
Inventor
修 丸子
Original Assignee
株式会社細川粉体工学研究所
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 株式会社細川粉体工学研究所 filed Critical 株式会社細川粉体工学研究所
Priority to JP8330182U priority Critical patent/JPS6039108Y2/en
Publication of JPS58186882U publication Critical patent/JPS58186882U/en
Application granted granted Critical
Publication of JPS6039108Y2 publication Critical patent/JPS6039108Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は分級羽根車と環状の風篩部材とを具備させた粉
粒体の分級装置に関するものである。
[Detailed Description of the Invention] The present invention relates to an apparatus for classifying powder and granular materials, which is equipped with a classification impeller and an annular wind sieve member.

従来、分級羽根車を具備し、゛該分級羽根車を回転させ
ることによって粉粒体に遠心力を付与させ、該遠心力と
気流に伴う求心力との作用力差を以って粉粒体を微粉と
粗粉とに選別させ、微粉は空気と共に分級羽根車内を通
過させて機外に、粗粉は下方の排出口に向けて下降させ
る形式の分級装置においては、第1図に示すように分級
羽根車3の下方に下方小径の開口部9を有する円錐環状
の風篩部材7を配設させ、降下する粗粉に対して導入空
気流(以下風篩気流eと云う)を以って、風篩作用を付
与させ、当該分級装置の分級精度を向上させるべく方法
が用いられていた。
Conventionally, a classification impeller is provided, and by rotating the classification impeller, a centrifugal force is applied to the powder and granules, and the difference between the centrifugal force and the centripetal force accompanying the airflow is used to separate the powder and granules. In a classification device that separates fine powder and coarse powder, the fine powder passes through a classification impeller together with air to the outside of the machine, and the coarse powder descends toward the discharge port below, as shown in Figure 1. A conical annular wind sieve member 7 having a small-diameter downward opening 9 is disposed below the classification impeller 3, and an introduced air flow (hereinafter referred to as wind sieve air flow e) is used to filter the falling coarse powder. A method has been used to improve the classification accuracy of the classification device by imparting a wind sieving effect.

しかしながら、該風篩部材7では風篩気流eを降下粒子
に対して有効に付与できる作用域がほぼ一平面上のみと
言う非常に狭い範囲に限られており、しかも、該風篩気
流eに対する粒子は高速度の旋回状態にあるため、該風
篩気流eによる風篩作用を受けにくく、したがって、該
粒子への分散効果も不充分となり、多分に微粉が粗粉中
に混在した状態のまま排出されるものであった。
However, in the wind sieve member 7, the area of action in which the wind sieve airflow e can be effectively applied to the falling particles is limited to a very narrow range, approximately only on one plane. Since the particles are in a high-velocity swirling state, they are not easily affected by the wind sieving action of the air sieve e, and therefore the dispersion effect on the particles is insufficient, and the fine powder remains mixed in the coarse powder. It was something that would be discharged.

また、風篩部材7を通過した粗粉粒子は該粒子自身の持
つ旋回エネルギーにより、さらに風篩気流eの旋回力に
も助長され、該粒子は本体1の下方内壁面11に沿って
旋回しながら下降するため、該内壁面11を不要に磨耗
させ易いと云う問題もあった。
Further, the coarse powder particles that have passed through the wind sieve member 7 are further encouraged by the swirling force of the wind sieve air flow e due to the swirling energy of the particles themselves, and the particles swirl along the lower inner wall surface 11 of the main body 1. There is also the problem that the inner wall surface 11 tends to be worn out unnecessarily because the inner wall surface 11 is moved downward.

こうしたことに鑑み、本考案は前記風篩部材7における
風篩作用を良好なものとし、より高い分級精度を得るこ
とと、前記内壁面11の早期の磨耗を防止することとを
目的とするものであり、本体1内上部に配設された分級
羽根車3の下方に上端を本体1側に保持させた下方小径
の開口部9を持つ円錐環状の風篩リング7と、空気導入
口1゜とを有する分級装置において、前記開口部9に対
し適当な長さ1を有する整流板8を下方に向けて配設さ
せたものであり、以下実施例を以って説明する。
In view of the above, the present invention aims to improve the wind sieving action of the wind sieve member 7, obtain higher classification accuracy, and prevent early wear of the inner wall surface 11. Below the classification impeller 3 disposed in the upper part of the main body 1, there is a conical ring-shaped wind sieve ring 7 having an opening 9 with a small diameter at the lower end whose upper end is held on the main body 1 side, and an air inlet 1°. In this classification device, a rectifying plate 8 having an appropriate length 1 is disposed downwardly relative to the opening 9, and will be described below with reference to an embodiment.

第2図、及び第3図において、分級機の本体1内には上
部に分級羽根車3を、その下方には下方小径の開口部9
を持つ円錐環状の風篩リング7上端を本体1側に保持さ
せて配設したおり、さらに、その下方には空気導入口1
0が設けられている。
2 and 3, inside the main body 1 of the classifier, there is a classification impeller 3 at the top, and a small diameter opening 9 below it.
The upper end of the conical air sieve ring 7 is held on the main body 1 side, and an air inlet 1 is provided below it.
0 is set.

そして、本体1の上部には前記分級羽根車3の内部に連
通ずる排気口6が、下部には排出口5が具備されており
、排気口6には図示省略のサイクロン、バッグフィルタ
ー等の捕集機が接続される。
The upper part of the main body 1 is provided with an exhaust port 6 that communicates with the inside of the classification impeller 3, and the lower part is provided with an exhaust port 5. The collector is connected.

搬送管4は、粉粒体材料(以下単に原料Pと云う)を空
気と共に分級室2内に供給するためのもので、下方より
開口部9を貫通して配設されているが、原料が分級室2
への供給方法、及び構造は特に限定されるものではなく
、原料Pと空気とをそれぞれ別々に送り込む樹皮であっ
てもよい。
The conveying pipe 4 is for supplying a powder material (hereinafter simply referred to as raw material P) into the classification chamber 2 together with air, and is disposed through the opening 9 from below. Classification room 2
The feeding method and structure are not particularly limited, and it may be a bark that feeds the raw material P and air separately.

ところで、前記風篩リング7の下端、即ち開口部9と同
径で適当な長さ1を有する円筒部材8が連続して配設さ
れている。
By the way, a cylindrical member 8 having the same diameter as the lower end of the wind sieve ring 7, that is, the opening 9, and a suitable length 1 is continuously disposed.

なお、この円筒部材8の適当な長さ1については、実際
上の寸法として、必ずしも限定されるものではなく、た
とえば該円筒部材8の配設に伴う圧力損失の面に関連す
る本体1機胴の径と開口部9の大きさ、及び導入される
空気量と当該装置による所望の分級粒子径、その他の諸
条件に合わせ適時設定されるものである。
Note that the appropriate length 1 of this cylindrical member 8 is not necessarily limited as a practical dimension; The size of the opening 9, the amount of air introduced, the desired particle size classified by the device, and other conditions are set appropriately.

以上のような樹皮において、搬送管4により空気と共に
分級室2内に送り込まれた原料Pは分級羽根車3の回転
に伴う旋回気流rにより、あるいは該分級羽根車3との
衝突により分散化され分級選別の作用を受ける。
In the above-mentioned bark, the raw material P sent into the classification chamber 2 along with air through the conveyance pipe 4 is dispersed by the swirling airflow r accompanying the rotation of the classification impeller 3 or by collision with the classification impeller 3. It is subjected to the action of classification and selection.

つまり、原料Pは分級羽根車3による遠心力Fと、該分
級羽根車3を通過し排気口6に向う流出気流jによる求
心力にとの両作用力の差によって分級、選別がなされ、
その結果、気流jの影響をより受は易い微粉は該気流j
と共に排気口6より排出、捕集機で捕集される。
In other words, the raw material P is classified and sorted by the difference between the centrifugal force F by the classification impeller 3 and the centripetal force by the outflow air J passing through the classification impeller 3 and toward the exhaust port 6.
As a result, fine powder that is more susceptible to the influence of airflow j
It is also discharged from the exhaust port 6 and collected by a collector.

他方、遠心力Fの影響にまさる粗粉は前記旋回気流rと
共に旋回しながら壁面に沿って下降し風篩リング7を経
て開口部9に到るが、該開口部9においては、下方の空
気導入口10より導入され分級室2内に流入する空気流
、即ち風篩気流eによって分散と選別の作用が付加され
るわけであり、これにより粗粉中に付着し、あるいは凝
集により混在していた微粉粒子を粗粉粒子と分離させ再
度分級室2内へ返送させるものである。
On the other hand, the coarse powder that overcomes the influence of the centrifugal force F descends along the wall surface while swirling with the swirling air flow r, passes through the air sieve ring 7, and reaches the opening 9. In the opening 9, the air below The air flow introduced from the inlet 10 and flowing into the classification chamber 2, that is, the air sieve air flow e, adds dispersion and sorting effects, and this causes particles to adhere to the coarse powder or to be mixed together due to agglomeration. The fine powder particles are separated from the coarse particles and returned to the classification chamber 2 again.

ところで1、本願の要点である該開口部9における円筒
部材8の配設によって風篩気流eは該円筒部材8の適当
な長さlの区間全域にわたって降下粒子との接触を持つ
ことができるため風篩気流eによる風篩の作用域がほぼ
一平面上のみに限られていた従来に比べ該粒子にとって
は風篩選別の機会は格段に増加されるに到り、確実で良
好な風篩効果が得られるわけである。
By the way, 1. By arranging the cylindrical member 8 in the opening 9, which is the main point of the present application, the wind sieve airflow e can come into contact with the falling particles over the entire section of the cylindrical member 8 having an appropriate length l. Compared to the past, where the area of action of the wind sieve by the wind sieve air current e was limited to almost only one plane, the opportunities for wind sieving for these particles have been greatly increased, and a reliable and good wind sieving effect can be achieved. is obtained.

また、該円筒部材8は開口部9に到る降下粒子に対しそ
の旋回力を弱めさせ、後の風篩気流eによる風篩作用を
付与させ易いと云う面もあるほか、その配設によって開
口部9における風篩選別の作用位置を従来より下降に移
行させることになり、当該風篩作用後の粗粉粒子による
本体1の下方内壁面11の不要な磨耗を大幅に減少させ
ることができるものである。
In addition, the cylindrical member 8 has the advantage that it weakens the swirling force of the falling particles that reach the opening 9, making it easier to apply the wind sieving action by the subsequent wind sieving air flow e, and also because of its arrangement, The operating position of the air sieve sorting in the section 9 is shifted downward from the conventional position, and unnecessary wear of the lower inner wall surface 11 of the main body 1 due to coarse particles after the air sieve action can be significantly reduced. It is.

こうして開口部9における粗粉中の微粉は分離され分級
室2に返還され、再度分級羽根車3により分級選別され
て排気口6より、他方粗粉は開口部9及び円筒部材8を
通過、下降して排出口5より、それぞれ機外に排出、捕
集されるわけである。
In this way, the fine powder from the coarse powder in the opening 9 is separated and returned to the classification chamber 2, and is classified and sorted again by the classification impeller 3 through the exhaust port 6.On the other hand, the coarse powder passes through the opening 9 and the cylindrical member 8 and descends. Then, they are discharged and collected outside the machine from the discharge port 5, respectively.

以上のように、風篩選別部としての前記開口部9におけ
る円筒部材8の付設により、開口部9を通過する際、降
下粒子と風篩気流eとの接触の機会、即ち風篩作用域の
増大により確実、かつ良好な風篩効果が得られ、分級装
置として最も重要な分級精度の向上と性能の維持が計ら
れ、しかも簡単な構造と効率よい前記風篩効果に伴う所
要空気量の減少により経済的にも有利であるなど本考案
の効果は顕著である。
As described above, by providing the cylindrical member 8 in the opening 9 as a wind sieve sorting part, when passing through the opening 9, there is an opportunity for the falling particles to come into contact with the wind sieve air flow e, that is, in the wind sieve action area. By increasing the size, a reliable and good wind sieving effect can be obtained, improving the classification accuracy and maintaining performance, which is the most important for a classification device, and reducing the amount of air required due to the simple structure and efficient wind sieving effect. The effects of the present invention are remarkable, such as being economically advantageous.

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

第1図は従来例の概略図、第2図は本実施例の要部断面
図である。 図において1・・・・・・本体、2・・・・・・分級室
、3・・・・・・分級羽根車、4・・・・・・搬送管、
5・・・・・・排出口、6・・・・・・排気口、7・・
・・・・風篩リング、8・・・・・・円筒部材、9・・
・・・・開口部、10・・・・・・空気導入口、11・
・・・・・内壁面、e・・・・・・風篩気流、j・・・
・・・流出気流、r・・・・・・旋回気流、F・・・・
・・遠心力、K・・・・・・求心力である。
FIG. 1 is a schematic diagram of a conventional example, and FIG. 2 is a sectional view of a main part of this embodiment. In the figure, 1... Main body, 2... Classifying chamber, 3... Classifying impeller, 4... Conveying pipe,
5...Exhaust port, 6...Exhaust port, 7...
...Wind sieve ring, 8...Cylindrical member, 9...
...Opening, 10...Air inlet, 11.
...Inner wall surface, e...Wind sieve air flow, j...
...Outflow airflow, r...Swirling airflow, F...
...Centrifugal force, K...Centripetal force.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 本体1内上部に分級羽根車3を配し、下方に上端を本体
1側に保持させた下方小径の開口部9を持つ円錐環状の
風篩リング7と、空気導入口10とを有する分級装置に
おいて、前記開口部9に対し該開口部9と同径で適当な
長さ1を有する円筒部材8を下方に連続させて配設した
ことを特徴とする粉粒体の分級装置。
A classification device having a classification impeller 3 arranged in the upper part of the main body 1, a conical ring-shaped wind sieve ring 7 having a lower small diameter opening 9 whose upper end is held on the main body 1 side below, and an air inlet 10. In the apparatus for classifying powder and granular materials, a cylindrical member 8 having the same diameter as the opening 9 and an appropriate length 1 is disposed continuously below the opening 9.
JP8330182U 1982-06-03 1982-06-03 Powder classification device Expired JPS6039108Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8330182U JPS6039108Y2 (en) 1982-06-03 1982-06-03 Powder classification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8330182U JPS6039108Y2 (en) 1982-06-03 1982-06-03 Powder classification device

Publications (2)

Publication Number Publication Date
JPS58186882U JPS58186882U (en) 1983-12-12
JPS6039108Y2 true JPS6039108Y2 (en) 1985-11-22

Family

ID=30092317

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8330182U Expired JPS6039108Y2 (en) 1982-06-03 1982-06-03 Powder classification device

Country Status (1)

Country Link
JP (1) JPS6039108Y2 (en)

Also Published As

Publication number Publication date
JPS58186882U (en) 1983-12-12

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