JPS6023867B2 - Classifier using alternating electric field - Google Patents

Classifier using alternating electric field

Info

Publication number
JPS6023867B2
JPS6023867B2 JP6633579A JP6633579A JPS6023867B2 JP S6023867 B2 JPS6023867 B2 JP S6023867B2 JP 6633579 A JP6633579 A JP 6633579A JP 6633579 A JP6633579 A JP 6633579A JP S6023867 B2 JPS6023867 B2 JP S6023867B2
Authority
JP
Japan
Prior art keywords
inner cylinder
powder
housing
electric field
alternating electric
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
JP6633579A
Other languages
Japanese (ja)
Other versions
JPS55157361A (en
Inventor
博 杉本
賢二 尾崎
滋 庵原
敏彦 黒崎
武司 鈴木
三樹雄 村尾
克実 清水
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP6633579A priority Critical patent/JPS6023867B2/en
Publication of JPS55157361A publication Critical patent/JPS55157361A/en
Publication of JPS6023867B2 publication Critical patent/JPS6023867B2/en
Expired legal-status Critical Current

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  • Combined Means For Separation Of Solids (AREA)
  • Electrostatic Separation (AREA)
  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】 本発明は、粉粒体原料を風力あるいはふるい絹を用いて
分級する分級装置に関し、もっと詳しくはハウジング内
に導入された分級されるべき粉粒体を交番電界内に導い
て風力あるいはふるい絹を用いて分級する分級方法およ
び装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a classification device for classifying powder and granular raw materials using wind power or sieve silk, and more specifically, the present invention relates to a classification device for classifying powder and granular raw materials using wind power or sieve silk, and more specifically, the present invention relates to a classification device that classifies powder and granular materials by using wind power or sieve silk, and more specifically, the present invention relates to a classification device that classifies powder and granular raw materials by using wind power or sieve silk, and more specifically, by classifying powder and granular materials introduced into a housing and to be classified into an alternating electric field. This invention relates to a classification method and apparatus for classifying using guided wind or sieving silk.

従釆から風力あるいはふるい網を用いた分級装置におい
ては、分級されるべき粉粒体原料がファンデルワールス
力、静電引力および付着水などによって凝集し、そのた
め粗粉として排出されしまう場合がある。また風力を用
いた分級装置においては分級装置の分級空間を形成する
ハウジング内で粉粒体原料濃度が増大した場合には、そ
の分級空間内に粉粒体の分布密度の著しい粗密を生じ、
分布密度の密な空間にある粉粒体は徴粉を含んだまま塊
状となって沈降し、粗粉として排出される。本発明の主
な目的は、分級効率の向上した風力あるいはふるい網を
用いた分級方法および装置を提供することである。
In a classification device that uses wind power or a sieve screen, the granular material to be classified may aggregate due to van der Waals force, electrostatic attraction, adhering water, etc., and therefore be discharged as coarse powder. . In addition, in a classifier using wind power, when the concentration of powder raw material increases in the housing that forms the classification space of the classifier, the distribution density of the powder becomes extremely dense within the classification space.
Powder in a space with a dense distribution density settles out as a lump while containing characteristic powder, and is discharged as coarse powder. The main object of the present invention is to provide a classification method and apparatus using wind power or a sieve net with improved classification efficiency.

本発明は、上下に延びる筒状ハウジングー内に、そのハ
ウジング1と同軸に内筒3が設けられ、内筒3の上部は
上方に先細状となっており、内筒3の下部は下方に先細
状となっており、この内筒3上部の上方には、粉粒体を
導入するショート2の下端部が臨み、内筒3下部の下方
には、ハウジング側方から気体を送入する送入口4が設
けられ、ハウジング1の送入口4よりも下方には粗粉排
出口6が設けられ、前記内筒3は、複数の導電性分割部
分14〜18が電気絶縁物20を介して上下に配置され
て構成され、各分割部分14〜18には相順が下から上
に順次定められた3相以上の交流電源21が接続され、
ハウジングー内で内筒3との闇の空間には、下から上に
順次定められた進行波交番電界が形成されることを特徴
とする交番電界を用いた分級装置である。
In the present invention, an inner cylinder 3 is provided in a vertically extending cylindrical housing coaxially with the housing 1, the upper part of the inner cylinder 3 is tapered upward, and the lower part of the inner cylinder 3 is tapered downward. Above the upper part of the inner cylinder 3, the lower end of the short 2 for introducing powder and granules faces, and below the lower part of the inner cylinder 3 is an inlet port for introducing gas from the side of the housing. 4 is provided, and a coarse powder discharge port 6 is provided below the inlet port 4 of the housing 1, and the inner cylinder 3 has a plurality of conductive divided portions 14 to 18 arranged vertically through an electrical insulator 20. An AC power source 21 having three or more phases whose phase order is sequentially determined from bottom to top is connected to each divided portion 14 to 18,
This is a classification device using an alternating electric field, characterized in that a traveling wave alternating electric field is formed sequentially from the bottom to the top in the dark space between the inner cylinder 3 and the housing.

第1図は本発明の一実施例の全体の系統図である。FIG. 1 is an overall system diagram of an embodiment of the present invention.

上下に延びる筒状のハウジング1の上部には分級される
べき粉粒体原料が送入されるシュート2が設けられる。
これによって粉粒体原料がハウジングーの上方から投入
される。ハウジングー内では、シュート2から投入され
た粉粒体の分散を促進するための内筒3が設けられてお
り、この内筒3はハウジング1と同軸に上下に延び、上
下両端は先細状の円錐に形成される。ハウジング1の下
部には空気送入口4が設けられ、ここから空気が矢符に
ように導入される。/・ゥジングーの下部に設けられた
粗粉排出口6から排出された粗粉は、粉砕機7に導かれ
て粉砕され、再びシュート2に導かれる。ハウジング1
内で分級された徴粉は、シュート8からサイクロン9に
導かれる。このサイクロン9によって微粉が橘集される
。サイクロン9の下部にはフラップダンパ11が設けら
れる。導電性ハウジング1内の内筒3が上下に6個の導
電‘性分割部分14〜19に分割される。
A chute 2 is provided at the top of the vertically extending cylindrical housing 1, into which powdered raw material to be classified is fed.
As a result, the powder raw material is introduced from above into the housing. Inside the housing, an inner cylinder 3 is provided to promote the dispersion of the powder and granules introduced from the chute 2. This inner cylinder 3 extends vertically coaxially with the housing 1, and has tapered conical ends at both upper and lower ends. is formed. An air inlet 4 is provided at the bottom of the housing 1, from which air is introduced as shown by the arrow. The coarse powder discharged from the coarse powder discharge port 6 provided at the bottom of the ujingu is guided to the crusher 7, crushed, and guided to the chute 2 again. Housing 1
The powder classified inside is led to a cyclone 9 through a chute 8. This cyclone 9 collects fine powder. A flap damper 11 is provided at the bottom of the cyclone 9. The inner cylinder 3 within the conductive housing 1 is vertically divided into six conductive divided parts 14 to 19.

それらの分割部分14〜19の間には電気絶縁物20が
介在される。相対的に上方の分割部分14,15,16
は、相対的に下方の分割部分17,18,19と電気的
にそれぞれ接続されており、それらの共通接続された分
割部分16,19:15,18;14,17は、3相以
上の交流電源(この実施例では3相)21の各相u,v
,wにそれぞれ接続される。このようにしてハウジング
1内で内筒3との間の空間に形成される交番電界は、相
順が下から上に順次定められた3相の進行波交番電界と
なる。これによってシュート2から送入された徴粉体は
、相順方向すなわち下から上に向けて電界強度に依存し
た静電力を受ける。そのため粉粒体の自然落下終末速度
が電界の強度に依存して変化し、これによって分級粒度
を制御することが可能である。ハウジングーと内筒3と
は、電気絶縁性の支持部材12によって/・ゥジングー
内に支持される。
An electrical insulator 20 is interposed between the divided portions 14-19. Relatively upper divided portions 14, 15, 16
are electrically connected to relatively lower divided portions 17, 18, and 19, respectively, and those commonly connected divided portions 16, 19: 15, 18; 14, 17 are Each phase u, v of the power supply (three phases in this example) 21
, w, respectively. The alternating electric field thus formed within the housing 1 in the space between it and the inner cylinder 3 becomes a three-phase traveling wave alternating electric field whose phase order is determined from bottom to top. As a result, the powder introduced from the chute 2 is subjected to an electrostatic force that depends on the electric field strength in the phase direction, that is, from the bottom to the top. Therefore, the final velocity of natural fall of the powder changes depending on the strength of the electric field, and it is thereby possible to control the classified particle size. The housing and the inner tube 3 are supported within the housing by an electrically insulating support member 12.

この支持部材12は、空気送入口4からの空気の上昇お
よび粉粒体の流れを妨げないように周方向に間隔をあげ
て配置されている。電源21の周波数はたとえば50〜
60HZであり「その電界強度は、たとえば実効値飢v
/cmである。シュート2から投入される原料は、交番
電界により誘電分極を生じる。
The support members 12 are arranged at intervals in the circumferential direction so as not to impede the rise of air from the air inlet 4 and the flow of powder and granular material. The frequency of the power supply 21 is, for example, 50~
60Hz, and the electric field strength is, for example, the effective value starvation.
/cm. The raw material introduced from the chute 2 undergoes dielectric polarization due to the alternating electric field.

各分極に必要な時間はたとえば1/100頂砂以下で非
常に短く、交流電源13の周波数がたとえば前述のよう
に50〜60HZとしたときにおいては、分極に要する
時間を無視でき、粉粒体原料は交流電源と同一周波数お
よび位相で分極を繰返す。したがって交流電界と分極電
荷によって生じる静電力によって、粉粒体は、電気力線
に沿ってその両端が、それぞれ近い方の電極への引力を
受ける。また粉粒体は一般に完全な球ではなく、球以外
の各種の形状を有し、したがって、交番電界の方向と分
極電荷の分布によっては回転モーメントを受ける。これ
らの静電力によって、凝集粉粒体は分裂し、分裂後は互
いに異符号に帯電している。シュート2から投入される
粉粒体が予め帯電している場合を含めて、帯電している
粉粒体は交番電界によって振動する。
The time required for each polarization is very short, for example, 1/100 or less, and when the frequency of the AC power source 13 is, for example, 50 to 60Hz as described above, the time required for polarization can be ignored, and the powder The raw material is repeatedly polarized at the same frequency and phase as the AC power source. Therefore, due to the electrostatic force generated by the alternating electric field and the polarized charges, both ends of the granular material are attracted to the electrodes closer to each other along the lines of electric force. Furthermore, powder and granules are generally not perfect spheres, but have various shapes other than spheres, and are therefore subject to rotational moment depending on the direction of the alternating electric field and the distribution of polarized charges. These electrostatic forces cause the aggregated powder particles to split, and after the split, they are charged with opposite signs. The charged powder and granules are vibrated by the alternating electric field, including the case where the powder and granules introduced from the chute 2 are charged in advance.

この粉粒体の振動は、その粉粒体の質量、帯電している
電荷量および形状によって異なり、各粉粒体に固有な振
幅および位相で振動を生じ、この粉粒体の振動の周波数
は交流電源21の周波数と同一である。また空気送入口
4からは、空気が上向きに流入する。
The vibration of this granular material varies depending on the mass, amount of charge, and shape of the granular material, and vibrations occur with an amplitude and phase unique to each granular material, and the frequency of the vibration of this granular material is The frequency is the same as the frequency of the AC power supply 21. Furthermore, air flows upward from the air inlet 4.

これによってシュート2からハウジング1内に投入され
た粉粒体は複雑な運動を行うことになる。したがってハ
ウジング1内において粉粒体が分していた徴粉が個別に
分裂する。またハウジング1内において粉粒体の分布密
度が均一になり、粉粒体が塊状になって落下することが
防止される。したがって徴粉は確実にダクトからサイク
ロン9に導かれて瓶集され、粗粉のみが粗粉排出口6か
ら粉砕機7に導出される。従来では粗粉排出口6からの
粗粉には凝集徴粉が混ざっており、したがって粉砕機7
に供給される粉粒体循環量が増加し、作業能率が低下す
る。
As a result, the powder and granules introduced into the housing 1 from the chute 2 undergo complicated movements. Therefore, the powder particles that have been separated within the housing 1 are individually separated. Moreover, the distribution density of the powder and granules becomes uniform within the housing 1, and the powder and granules are prevented from falling in the form of lumps. Therefore, the fine powder is reliably led from the duct to the cyclone 9 and collected in the bottle, and only the coarse powder is led out from the coarse powder outlet 6 to the crusher 7. Conventionally, the coarse powder from the coarse powder outlet 6 contains agglomerated powder, and therefore
The amount of circulating powder and granules supplied to the machine increases, and work efficiency decreases.

また粉砕機7内において粗粉のほかに徴粉が含まれてい
るので、その粕粉と粉砕機7内の粉砕媒体との衝撃力が
徴粉によって弱められ、粉砕効率が低下することとなっ
た。本発明によれば、狙粉排出口6からの粗粉には微粉
が含まれていないので、粉砕機7を含む系全体としての
粉砕能力が向上し、また粉砕機7における粉砕効率の低
下が防止される。以上のように本発明によれば、分級装
置内に交番電界を形成するようにしたので、分級される
べき粉粒体の凝集徴粉が分散される。
In addition, since the pulverizer 7 contains coarse powder as well as coarse powder, the impact force between the lees powder and the grinding media in the pulverizer 7 is weakened by the coarse powder, reducing the pulverization efficiency. Ta. According to the present invention, since the coarse powder from the target powder outlet 6 does not contain fine powder, the pulverizing capacity of the entire system including the pulverizer 7 is improved, and the reduction in pulverizing efficiency in the pulverizer 7 is prevented. Prevented. As described above, according to the present invention, since an alternating electric field is formed in the classifier, agglomerated particles of the powder to be classified are dispersed.

また分級装置内に投入された粉粒体が交番電界によって
騒乱され、粉粒体の分布密度が均一となる。そのため分
級効率が向上される。また交流電源を用いるので粉粒体
原料全体としては一極性の電荷が増加することが防止さ
れ、したがって分級装置の後段の機器における粉粒体の
ハンドリングに際し、静電気に起因した障害が生じない
。また、交番電界を形成するための電力消費が非常に少
なくてすむ。また3相以上の交流電源が下から上に順次
定められた進行波交番電界が形成され、粉粒体には上向
きの静電力が作用し、したがって分級を効率よく行なう
ことができる。この電界は、ハウジングーと内筒3との
間の空間に形成され、この空間には、分割部分14〜1
8と電気絶縁物が突出しておらず、したがって粉粒体が
円滑に振動、分級されることができ、粉粒体が付着など
することがない。
Further, the powder and granules introduced into the classifier are disturbed by the alternating electric field, and the distribution density of the powder and granules becomes uniform. Therefore, classification efficiency is improved. In addition, since an AC power source is used, unipolar charges are prevented from increasing in the powder raw material as a whole, and therefore, problems due to static electricity do not occur when handling the powder in equipment downstream of the classifier. Further, the power consumption for forming the alternating electric field is extremely low. In addition, a traveling wave alternating electric field is formed in which three or more phases of alternating current power are sequentially determined from bottom to top, and an upward electrostatic force acts on the powder, so that classification can be carried out efficiently. This electric field is formed in the space between the housing and the inner cylinder 3, and in this space there are divided parts 14 to 1.
8 and the electrical insulator do not protrude, so that the powder and granules can be smoothly vibrated and classified, and the powder and granules do not stick together.

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

第1図は本発明の一実施例を示す断面図である。 1……ハウジング、2……シュート、3……内筒、21
・・・・・・3相交流電源。 第1図
FIG. 1 is a sectional view showing one embodiment of the present invention. 1...Housing, 2...Chute, 3...Inner cylinder, 21
...3-phase AC power supply. Figure 1

Claims (1)

【特許請求の範囲】[Claims] 1 上下に延びる筒状ハウジング1内に、そのハウジン
グ1と同軸に内筒3が設けられ、内筒3の上部は上方に
先細状となつており、内筒3の下部は下方に先細状とな
つており、この内筒3上部の上方には、粉粒体を導入す
るシユート2の下端部が臨み、内筒3下部の下方には、
ハウジング側方から気体を送入する送入口4が設けられ
、ハウジング1の送入口4よりも下方には粗粉排出口6
が設けられ、前記内筒3は、複数の導電性分割部分14
〜18が電気絶縁物20を介して上下に配置されて構成
され、各分割部分14〜18には相順が下から上に順次
定められた3相以上の交流電源21が接続され、ハウジ
ング1内で内筒3との間の空間には、下から上に順次定
められた進行波交番電界が形成されることを特徴とする
交番電界を用いた分級装置。
1 An inner cylinder 3 is provided coaxially with the housing 1 in a cylindrical housing 1 extending vertically, the upper part of the inner cylinder 3 is tapered upward, and the lower part of the inner cylinder 3 is tapered downward. Above the upper part of this inner cylinder 3, the lower end of the chute 2 for introducing powder and granules faces, and below the lower part of the inner cylinder 3,
An inlet 4 for introducing gas from the side of the housing is provided, and a coarse powder outlet 6 is provided below the inlet 4 of the housing 1.
is provided, and the inner cylinder 3 has a plurality of electrically conductive divided portions 14.
- 18 are arranged vertically with an electrical insulator 20 interposed between them, and each divided part 14 - 18 is connected to an AC power supply 21 having three or more phases whose phase order is determined from bottom to top. A classification device using an alternating electric field, characterized in that a traveling wave alternating electric field is formed in the space between the inner cylinder 3 and the inner cylinder 3.
JP6633579A 1979-05-28 1979-05-28 Classifier using alternating electric field Expired JPS6023867B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6633579A JPS6023867B2 (en) 1979-05-28 1979-05-28 Classifier using alternating electric field

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6633579A JPS6023867B2 (en) 1979-05-28 1979-05-28 Classifier using alternating electric field

Publications (2)

Publication Number Publication Date
JPS55157361A JPS55157361A (en) 1980-12-08
JPS6023867B2 true JPS6023867B2 (en) 1985-06-10

Family

ID=13312873

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6633579A Expired JPS6023867B2 (en) 1979-05-28 1979-05-28 Classifier using alternating electric field

Country Status (1)

Country Link
JP (1) JPS6023867B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57119882A (en) * 1981-01-20 1982-07-26 Kobe Steel Ltd Classifier for powdered body
JPS57136980A (en) * 1981-02-17 1982-08-24 Kawasaki Heavy Ind Ltd Method and device for dispersing coagulated powdered and granular body

Also Published As

Publication number Publication date
JPS55157361A (en) 1980-12-08

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