JP2002119882A - Cover gap adjustment device, and jet mill - Google Patents

Cover gap adjustment device, and jet mill

Info

Publication number
JP2002119882A
JP2002119882A JP2000316402A JP2000316402A JP2002119882A JP 2002119882 A JP2002119882 A JP 2002119882A JP 2000316402 A JP2000316402 A JP 2000316402A JP 2000316402 A JP2000316402 A JP 2000316402A JP 2002119882 A JP2002119882 A JP 2002119882A
Authority
JP
Japan
Prior art keywords
distance
powder
pressure air
plane
displacement
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.)
Pending
Application number
JP2000316402A
Other languages
Japanese (ja)
Inventor
Shinobu Endo
忍 遠藤
Keichi Takahashi
佳智 高橋
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.)
Bridgestone Corp
Original Assignee
Bridgestone Corp
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 Bridgestone Corp filed Critical Bridgestone Corp
Priority to JP2000316402A priority Critical patent/JP2002119882A/en
Publication of JP2002119882A publication Critical patent/JP2002119882A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an opposed-jet impact type jet mill having a cover gap (the gap between the lower end face of a classification rotor of a cover of the mill and the opening of a pulverized and classified powder conveyance means of a main body of the mill) adjustment device, which is capable of being used for pulverization, classification, etc., of a powder and easily performing adjustment of the above gap and also by which a pulverized and classified powder hardly contaminated with impurities can be obtained. SOLUTION: This mill is provided with: a cover 20 having a classification rotor 4 which is used for classifying a raw material powder pulverized with high-pressure gas streams opposed to each other and connected to a main body of the cover 20 in a upwardly and downwardly movable manner and provided at its lower end with a flat face 4f perpendicular to a rotary shaft 4b and also with an exposed flat face 4a that is positioned outside the main body of the cover 20 so as to be opposite and parallel to the face 4f; a pulverizer main body 10 having within it, a powder conveyance means 5 which is provided with an opening 5a that is formed opposite and parallel to the face 4f and used for introducing the powder classified with the rotor 4, and intended for conveying the power introduced through the opening 5a; and a displacement measurement means 30 for measuring the distance between the means 30 itself and the exposed flat face 4a and determining the difference of the measured distance from an initially set distance.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、粉体の微粉化・分
級等に用いられ、ギャップ調整の容易で不純物の混入が
少ない、対面衝突型の高圧気流式粉砕装置、及び該高圧
気流式粉砕装置のギャップを容易に調整することができ
る蓋体間隙調整装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high-pressure air-flow type pulverizer of a face-to-face collision type, which is used for pulverization and classification of powders, is easy to adjust a gap, and contains little impurities. The present invention relates to a cover gap adjusting device capable of easily adjusting a gap of the device.

【0002】[0002]

【従来の技術】対面衝突型の高圧気流式粉砕機は、微粉
化能(粉砕能)及び分級能を有し、従来より、各種分野
において広範に用いられており、例えば、これを用いて
セラミックス粉体を微粉化(粉砕)し、粉径分布の小さ
な微粉を得ることにより、高密度のセラミックス焼結体
を得ることができる。前記高圧気流式粉砕機は、一般
に、対向する高圧気流により粉砕された原料粉体を分級
する分級ロータと、該分級ロータにより分級した粉体を
開口部から導入し外部に搬送する粉体搬送手段とを備え
ている。前記分級ロータは、摩耗時のメインテナンスの
便宜等の理由から、装置本体に開閉可能に接続される蓋
体に備えられ、前記粉体搬送手段における前記開口部
は、該装置本体の内部に備えられており、使用時におい
ては、これらは前記装置本体の内部に収容され、該装置
本体の内部は蓋体により密閉される。
2. Description of the Related Art Face-to-face collision type high-pressure air-mills have a pulverizing ability (crushing ability) and a classifying ability and have been widely used in various fields. By pulverizing (pulverizing) the powder to obtain a fine powder having a small powder diameter distribution, a high-density ceramic sintered body can be obtained. In general, the high-pressure air-flow type pulverizer generally includes a classifying rotor for classifying raw material powder pulverized by an opposing high-pressure air flow, and powder conveying means for introducing the powder classified by the classifying rotor from an opening and conveying the powder to the outside. And The classifying rotor is provided on a lid that is openably and closably connected to the apparatus main body for reasons such as convenience of maintenance at the time of wear, and the opening in the powder conveying means is provided inside the apparatus main body. In use, they are housed inside the apparatus main body, and the inside of the apparatus main body is sealed by a lid.

【0003】前記高圧気流式粉砕機においては、原料粉
体が、対向する高圧気流により互いに強い衝撃力で衝突
し微粉化(粉砕)される。所定の粒径に微粉化(粉砕)
された原料粉体は、回転している分級ロータの外部に弾
き飛ばされず、該分級ロータの内部に侵入し通過し、前
記粉体搬送手段における開口部を通過して外部に搬送さ
れて分級される。前記原料粉体は、所定の粒径になるま
で、前記高圧気流により互いに衝突させられ、微粉化
(粉砕)される。前記高圧気流式粉砕機においては、以
上のプロセスにより、原料粉体の微粉化(粉砕)及び分
級が行なわれる。前記高圧気流式粉砕機においては、前
記分級ロータにより所定の粒径に微粉化(粉砕)された
微粉のみを外部に搬送して分級する必要があることか
ら、回転する前記分級ロータと、前記粉体搬送手段にお
ける前記開口部とが、互いに対向し近接して配置される
ことが必要とされ、該分級ロータと該開口部と間隙(ギ
ャップ)が僅か0.2mm程度になるように調整するこ
とが必要になる。
[0003] In the high-pressure air-flow type pulverizer, raw material powders collide with each other with a strong impact force by opposing high-pressure airflows to be pulverized (pulverized). Finely pulverized (crushed) to specified particle size
The raw material powder is not repelled to the outside of the rotating classifying rotor, enters and passes through the inside of the classifying rotor, passes through the opening in the powder conveying means, is conveyed to the outside, and is classified. You. The raw material powders are caused to collide with each other by the high-pressure airflow until they reach a predetermined particle size, and are pulverized (crushed). In the high-pressure air-flow type pulverizer, the pulverization (pulverization) and classification of the raw material powder are performed by the above processes. In the high-pressure air-flow type pulverizer, only the fine powder pulverized (pulverized) to a predetermined particle size by the classification rotor needs to be transported to the outside and classified. It is necessary that the openings of the body transporting means are opposed to and close to each other, and an adjustment is made so that the gap between the classifying rotor and the openings is only about 0.2 mm. Is required.

【0004】しかしながら、従来の高圧気流式粉砕機の
場合、この調整の作業が容易でなく、煩雑で不便である
という問題がある。即ち、従来の高圧気流式粉砕機にお
いては、微粉化(粉砕)処理を行う度に、あるいは前記
分級ロータのメインテナンスを行う度に前記蓋体を開閉
し、前記間隙の調整(ギャップ調整)を行わなくてはな
らなかった。そして、該間隙の調整(ギャップ調整)の
際には、前記蓋体を開けて前記分級ロータを露出させ、
該分級ロータの下端部と前記開口部との間に所定の厚み
の隙間ゲージを配置し、該分級ロータの取り付け部(前
記蓋体の内側)に適当なスペーサー等を脱着等してお
り、作業が極めて煩雑で不便であった。更に、該間隙の
調整(ギャップ調整)を行った後には、ゴミや埃塵等の
侵入による粒度分布の精度低下を防ぐために、前記高圧
気流式粉砕機を空運転させなければならなかった。
However, in the case of the conventional high-pressure air-flow type pulverizer, there is a problem that the operation of this adjustment is not easy, and is complicated and inconvenient. That is, in the conventional high-pressure air-flow type pulverizer, the lid is opened and closed each time the pulverization (pulverization) processing is performed or the maintenance of the classifying rotor is performed, and the gap is adjusted (gap adjustment). I had to. When adjusting the gap (gap adjustment), the lid is opened to expose the classifying rotor,
A gap gauge having a predetermined thickness is arranged between the lower end of the classifying rotor and the opening, and an appropriate spacer or the like is attached to or detached from a mounting portion (inside the lid) of the classifying rotor. Was very complicated and inconvenient. Further, after the gap is adjusted (gap adjustment), the high-pressure air-flow-type pulverizer must be run idle in order to prevent a decrease in the accuracy of the particle size distribution due to intrusion of dust and dirt.

【0005】[0005]

【発明が解決しようとする課題】本発明は、従来におけ
る前記諸問題を解決し、以下の目的を達成することを課
題とする。即ち、本発明は、粉体の微粉化・分級等に用
いられ、分級ロータのギャップ調整が容易で不純物の混
入が少ない、対面衝突型の高圧気流式粉砕装置、及び該
高圧気流式粉砕装置における分級ロータのギャップを容
易に調整することができる蓋体間隙調整装置を提供する
ことを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned conventional problems and achieve the following objects. That is, the present invention is used for pulverization / classification of powder, etc., in which the gap adjustment of the classifying rotor is easy and the amount of impurities is small, and the face-to-face collision type high-pressure airflow pulverizer and the high-pressure airflow pulverizer are used. It is an object of the present invention to provide a cover gap adjusting device capable of easily adjusting a gap of a classifying rotor.

【0006】[0006]

【課題を解決するための手段】前記課題を解決するため
の手段としては、以下の通りである。即ち、 <1> 回転軸に垂直な平面及び該平面に対し平行な露
出平面を有すると共に高圧気流により粉砕された粉体を
分級する分級ロータが昇降可能に接続された蓋体と、前
記平面に対し平行に対向配置されると共に該分級ロータ
により分級した粉体を導入する開口部を有し、該開口部
から導入された粉体を外部に搬送する粉体搬送手段が内
部に備えられた装置本体と、前記露出平面と間の距離を
測定し、初期設定距離に対する測定距離の変位を計測す
る変位計測手段と、を備えたことを特徴とする高圧気流
式粉砕装置である。 <2> 接続が螺合である前記<1>に記載の高圧気流
式粉砕装置である。 <3> 螺合が、1mm以下/360°の螺旋ピッチを
有する細目ネジで行われた前記<2>に記載の高圧気流
式粉砕装置である。 <4> 分級ロータが等間隔にかつ少なくとも3箇所で
蓋体に昇降可能に接続された前記<1>から<3>のい
ずれかに記載の高圧気流式粉砕装置である。 <5> 変位計測手段が高精度変位計である前記<1>
から<4>のいずれかに記載の高圧気流式粉砕装置であ
る。 <6> 変位計測手段が露出平面との距離を少なくとも
3箇所測定し、各箇所において予め設定した設定値に対
する前記距離の変位を計測する前記<1>から<5>の
いずれかに記載の高圧気流式粉砕装置である。 <7> 変位計測手段が、露出平面との距離を等間隔に
かつ少なくとも3箇所測定し、各箇所において予め設定
した設定値に対する前記距離の変位を計測する前記<1
>から<6>のいずれかに記載の高圧気流式粉砕装置で
ある。 <8> 変位計測手段が露出平面との距離を測定する箇
所が、分級ロータが蓋体に昇降可能に接続された箇所の
内の隣接する2箇所から略等距離に位置する前記<7>
に記載の高圧気流式粉砕装置である。 <9> 分級ロータにおける平面と、粉体搬送手段にお
ける開口部との間隙が0.2mm以下である前記<1>
から<8>のいずれかに記載の高圧気流式粉砕装置であ
る。 <10> 回転軸に垂直な平面及び該平面に対し平行な
露出平面を有すると共に高圧気流により粉砕された粉体
を分級する分級ロータが昇降可能に接続された蓋体と、
前記平面に対し平行に対向配置されると共に該分級ロー
タにより分級した粉体を導入する開口部を有し、該開口
部から導入された粉体を外部に搬送する粉体搬送手段が
内部に備えられた装置本体と、を備えてなる高圧気流式
粉砕装置に設けられ、前記平面と該開口部との間隙を調
整する蓋体間隙調整装置であって、前記露出平面と間の
距離を測定し、初期設定距離に対する測定距離の変位を
計測する変位計測手段を備えたことを特徴とする蓋体間
隙調整装置である。
Means for solving the above problems are as follows. That is, <1> a lid body having a plane perpendicular to the rotation axis and an exposed plane parallel to the plane, and a classifying rotor for classifying the powder pulverized by the high-pressure airflow connected so as to be able to move up and down; A device having an opening for introducing the powder classified by the classifying rotor and having a powder conveying means for conveying the powder introduced from the opening to the outside; A high-pressure air-flow type pulverizer comprising: a main body; and a displacement measuring means for measuring a distance between the exposed plane and measuring a displacement of a measured distance with respect to an initial set distance. <2> The high-pressure airflow pulverizer according to <1>, wherein the connection is screwed. <3> The high-pressure air-flow pulverizer according to <2>, wherein the screwing is performed with a fine screw having a helical pitch of 1 mm or less / 360 °. <4> The high-pressure air-flow pulverizer according to any one of <1> to <3>, wherein the classification rotors are connected to the lid at equal intervals and at least three places so as to be able to move up and down. <5> The above <1>, wherein the displacement measuring means is a high-precision displacement meter.
To the high-pressure airflow pulverizer according to any one of <1> to <4>. <6> The high voltage according to any one of <1> to <5>, wherein the displacement measuring unit measures a distance from the exposed plane at at least three places, and measures a displacement of the distance with respect to a preset set value at each place. It is a pneumatic crusher. <7> The displacement measuring means measures the distance from the exposed plane at equal intervals and at least three places, and measures the displacement of the distance with respect to a preset value at each place.
> The high-pressure air-flow-type pulverizer according to any one of <6> to <6>. <8> The place where the displacement measuring means measures the distance to the exposed plane is located at substantially the same distance from two adjacent places among the places where the classifying rotor is connected to the lid so as to be able to move up and down.
The high-pressure air-flow-type pulverizer described in 1 above. <9> The above <1>, wherein the gap between the plane of the classifying rotor and the opening of the powder conveying means is 0.2 mm or less.
To the high-pressure airflow pulverizer according to any one of <8> to <8>. <10> a lid having a plane perpendicular to the rotation axis and an exposed plane parallel to the plane, and a classifying rotor for classifying the powder pulverized by the high-pressure airflow connected to be vertically movable;
It has an opening for introducing the powder classified by the classifying rotor and is disposed parallel to the plane, and a powder conveying means for conveying the powder introduced from the opening to the outside is provided inside. Provided in a high-pressure air-flow-type pulverizing device comprising: a lid gap adjusting device for adjusting a gap between the flat surface and the opening portion, wherein a distance between the exposed flat surface is measured. And a displacement measuring means for measuring a displacement of a measured distance with respect to an initial set distance.

【0007】前記<1>に記載の高圧気流式粉砕装置
は、回転軸に垂直な平面及び該平面に対し平行な露出平
面を有すると共に高圧気流により粉砕された粉体を分級
する分級ロータが昇降可能に接続された蓋体と、前記平
面に対し平行に対向配置されると共に該分級ロータによ
り分級した粉体を導入する開口部を有し、該開口部から
導入された粉体を外部に搬送する粉体搬送手段が内部に
備えられた装置本体と、を備える。
The high-pressure air-flow type pulverizer according to the above <1> has a plane perpendicular to the rotation axis and an exposed plane parallel to the plane, and a classifying rotor for classifying the powder pulverized by the high-pressure air flow moves up and down. A lid, which is connected so as to be capable of being parallel to the plane, and has an opening for introducing the powder classified by the classifying rotor, and transports the powder introduced from the opening to the outside. And an apparatus main body in which a powder conveying means is provided.

【0008】この高圧気流式粉砕機においては、原料粉
体が、高圧気流により互いに強い衝撃力で衝突し微粉化
(粉砕)されて微粉となる。前記原料粉体は、所定の粒
径の微粉になるまで、前記高圧気流により互いに何度も
衝突させられ、微粉化(粉砕)される。前記分級ロータ
は回転しており、所定の粒径に微粉化(粉砕)された前
記原料粉体(微粉)は、前記高圧気流により上昇し、こ
の回転している分級ロータへと搬送される。該分級ロー
タへと搬送された前記微粉は、該分級ロータの内部に侵
入し該分級ロータを通過し、前記粉体搬送手段における
前記開口部を通過して分級されて外部に搬送される。一
方、所定の粒径に微粉化(粉砕)されていない前記原料
粉体は、この回転している前記分級ロータにより弾き飛
ばされ、所定の粒径になるまで微粉化(粉砕)される。
その結果、所定の粒径に分級され、粒度分布が一定の微
粉が得られる。
In this high-pressure air-flow type pulverizer, the raw material powders collide with each other with a high impact force due to the high-pressure air flow and are pulverized (pulverized) into fine powder. The raw material powders are caused to collide with each other many times by the high-pressure airflow until they become fine powder having a predetermined particle size, and are pulverized (crushed). The classifying rotor is rotating, and the raw material powder (fine powder) pulverized (crushed) to a predetermined particle size rises by the high-pressure airflow and is conveyed to the rotating classifying rotor. The fine powder conveyed to the classifying rotor enters the classifying rotor, passes through the classifying rotor, passes through the opening in the powder conveying means, is classified, and is conveyed to the outside. On the other hand, the raw material powder that has not been pulverized (pulverized) to a predetermined particle size is blown off by the rotating classifying rotor and pulverized (pulverized) until the particle diameter reaches a predetermined particle size.
As a result, a fine powder having a predetermined particle size and a uniform particle size distribution is obtained.

【0009】この高圧気流式粉砕機においては、前記蓋
体が、微粉化(粉砕)処理を行う度に、あるいは前記分
級ロータのメインテナンスを行う度に開閉される。この
とき、前記分級ロータと前記開口部との間隙(ギャッ
プ)を調整することが必要になるが、前記変位計測手段
を備えているので、該変位計測手段が、前記露出平面と
間の距離を測定し、初期設定距離に対する測定距離の変
位を計測し、その結果に基づいて、該変位が設定範囲に
なるように、前記蓋体に接続された前記分級ロータの位
置を動かして調整する。
In this high-pressure air-flow type pulverizer, the lid is opened and closed each time a pulverization (pulverization) process is performed or each time the classification rotor is maintained. At this time, it is necessary to adjust a gap (gap) between the classifying rotor and the opening. However, since the displacement measuring unit is provided, the displacement measuring unit sets a distance between the classifying rotor and the exposed plane. Measure and measure the displacement of the measured distance with respect to the initially set distance, and adjust the position of the classifying rotor connected to the lid body based on the result so that the displacement is within the set range.

【0010】前記変位計測手段の計測対象である、前記
分級ロータにおける露出平面と、前記分級ロータの回転
軸に垂直な前記平面と、該平面に対し対向配置される、
前記粉体搬送手段における開口部とは、互いに平行にな
っている。該平面と該開口部とが所定の大きさの間隙
(ギャップ)の時における前記変位計測手段の前記露出
平面に対する距離を予め初期設定距離として設定してお
く。前記変位計測手段が、測定時点での前記露出表面に
対する距離(測定距離)を測定し、該測定距離と前記初
期設定距離との変位を計測するので、該変位の値が設定
範囲になるように前記分級ロータの位置を動かして前記
接続状態を変位させて調整すると、前記平面と前記開口
部とが所定の大きさの間隙(ギャップ)に調整される。
[0010] An exposed plane of the classifying rotor, which is a measurement target of the displacement measuring means, a plane perpendicular to a rotation axis of the classifying rotor, and a plane opposed to the plane.
The openings in the powder conveying means are parallel to each other. A distance between the displacement measuring means and the exposed plane when the plane and the opening have a predetermined gap is previously set as an initial set distance. The displacement measuring means measures a distance (measurement distance) with respect to the exposed surface at the time of measurement, and measures a displacement between the measured distance and the initially set distance, so that the value of the displacement falls within a set range. When the position of the classifying rotor is moved and adjusted by displacing the connection state, the plane and the opening are adjusted to a predetermined gap.

【0011】この高圧気流式粉砕機においては、前記間
隙の調整(ギャップ調整)の際に、前記蓋体を開けて前
記分級ロータを露出させ、該分級ロータの下端部と前記
開口部との間に所定の厚みの隙間ゲージを配置し、該分
級ロータの取り付け部(前記蓋体の内側)に適当なスペ
ーサー等を脱着等する必要がなく、前記接続状態を調整
するだけで作業が完了するので、作業が極めて容易であ
り、不純物の混入が少ない。また、前記間隙の調整(ギ
ャップ調整)を行った後に、ゴミや埃塵等の侵入による
粒度分布の精度低下を防ぐための空運転の必要がない。
In this high-pressure air-flow type pulverizer, when adjusting the gap (gap adjustment), the lid is opened to expose the classification rotor, and the gap between the lower end of the classification rotor and the opening is adjusted. Since a gap gauge having a predetermined thickness is disposed on the mounting surface, there is no need to attach or detach an appropriate spacer or the like to or from the mounting portion (the inside of the lid) of the classifying rotor, and the work is completed only by adjusting the connection state. The operation is extremely easy and the contamination with impurities is small. Further, after the gap adjustment (gap adjustment) is performed, there is no need to perform idle operation for preventing a decrease in the accuracy of the particle size distribution due to intrusion of dust, dust, and the like.

【0012】前記<2>に記載の高圧気流式粉砕装置
は、前記<1>において、前記接続が螺合である。この
ため、前記間隙の調整(ギャップ調整)の際、該螺合状
態を変位させて、前記変位の値が設定範囲内になるよう
に前記分級ロータの位置を調整する。該螺合の場合、そ
の状態を連続的に変位させることができる。このため、
前記変位の値が設定範囲内になるように前記分級ロータ
の位置を微調整する際の作業が容易であり、調整の精度
も高い。
[0012] In the high-pressure air-flow type pulverizer according to <2>, in <1>, the connection is screwed. For this reason, when adjusting the gap (gap adjustment), the screwing state is displaced, and the position of the classifying rotor is adjusted so that the value of the displacement falls within a set range. In the case of the screw engagement, the state can be continuously displaced. For this reason,
The work of finely adjusting the position of the classifying rotor so that the displacement value falls within the set range is easy, and the adjustment accuracy is high.

【0013】前記<3>に記載の高圧気流式粉砕装置
は、前記<1>又は<2>において、前記螺合が、1m
m以下/360°の螺旋ピッチを有する細目ネジで行わ
れている。このため、前記間隙の調整(ギャップ調整)
の際、該細目ネジを動かして、前記変位の値が設定範囲
内になるように前記蓋体の位置を調整する。該細目ネジ
は、通常のネジよりも螺旋ピッチが1mm以下/360
°と極めて小さいため、一定の距離を上下動させるの
に、通常のネジよりも多くの回転が必要となる。このた
め、前記変位の値が設定範囲内になるように前記蓋体の
位置を微調整する際、通常のネジを用いた場合に比べて
極めて作業が容易であり、調整の精度も一層高い。
[0013] In the high-pressure air-flow pulverizer according to the above <3>, in the above <1> or <2>, the screw engagement may be 1 m.
It is performed with a fine thread having a helical pitch of less than m / 360 °. Therefore, adjustment of the gap (gap adjustment)
At this time, the position of the lid is adjusted by moving the fine screw so that the value of the displacement falls within a set range. The fine screw has a helical pitch of 1 mm or less / 360 times that of a normal screw.
Because of the extremely small angle of °, more vertical rotation than a normal screw is required to move up and down a certain distance. For this reason, when finely adjusting the position of the lid so that the value of the displacement falls within the set range, the operation is extremely easy as compared with the case where a normal screw is used, and the accuracy of the adjustment is even higher.

【0014】前記<4>に記載の高圧気流式粉砕装置に
おいては、前記<1>から<3>において、前記分級ロ
ータが等間隔にかつ少なくとも3箇所で蓋体に昇降可能
に接続されている。この場合、前記分級ロータが、接続
された少なくとも3箇所において昇降されてその位置が
調整される。少なくとも3点あれば一つの平面を特定す
ることができるので、前記変位の値が設定範囲内になる
ように、接続された少なくとも3箇所で前記分級ロータ
を昇降させることにより、調整が高精度で確実に行われ
る。
In the high-pressure air-flow pulverizer according to the above <4>, in the above <1> to <3>, the classifying rotors are connected to the lid at equal intervals and at least three places so as to be able to move up and down. . In this case, the classifying rotor is moved up and down at least at three connected positions to adjust its position. If at least three points, one plane can be specified, so that the classifying rotor is raised and lowered at least at three connected points so that the value of the displacement falls within the set range, so that the adjustment can be performed with high accuracy. It is done reliably.

【0015】前記<5>に記載の高圧気流式粉砕装置
は、前記<1>から<4>のいずれかにおいて、前記変
位計測手段が高精度変位計である。この場合、該高精度
変位計が、前記変位の値を精度良く、短時間で計測する
ので、更に調整の精度、効率に優れる。
[0015] In the high-pressure air-flow pulverizer according to <5>, in any one of <1> to <4>, the displacement measuring means is a high-precision displacement meter. In this case, since the high-precision displacement meter measures the value of the displacement with high accuracy in a short time, the accuracy and efficiency of the adjustment are further improved.

【0016】前記<6>に記載の高圧気流式粉砕装置
は、前記<1>から<5>のいずれかにおいて、前記変
位計測手段が露出平面との距離を少なくとも3箇所測定
し、各箇所において予め設定した初期設定距離に対する
前記測定距離の変位を計測する。少なくとも3点あれば
一つの平面を特定することができるので、この場合、前
記変位計測手段が計測した少なくとも3箇所における前
記変位の値を設定範囲内になるように前記分級ロータを
昇降させることにより、前記平面と前記開口部との間隙
(ギャップ)の調整がより高精度でより確実に行われ
る。
[0016] In the high-pressure air-flow type pulverizer according to <6>, in any one of <1> to <5>, the displacement measuring means measures a distance to an exposed plane at at least three places. The displacement of the measured distance with respect to a preset initial set distance is measured. One plane can be specified if there are at least three points. In this case, the classifying rotor is moved up and down so that the displacement values at at least three places measured by the displacement measuring means fall within a set range. The adjustment of the gap between the plane and the opening is performed with higher accuracy and more reliably.

【0017】前記<7>に記載の高圧気流式粉砕装置
は、前記<1>から<6>のいずれかにおいて、前記変
位計測手段が、露出平面との距離を等間隔にかつ少なく
とも3箇所測定し、各箇所において予め設定した初期設
定距離に対する前記測定距離の変位を計測する。この場
合、前記変位計測手段の計測を、前記露出表面において
等間隔に行うので、計測の誤差が少なく、調整の精度に
優れる。
In the high-pressure air-flow type pulverizer according to <7>, in any one of <1> to <6>, the displacement measuring means may measure a distance from an exposed plane at equal intervals and at least three places. Then, the displacement of the measurement distance with respect to the initially set distance set in advance at each location is measured. In this case, since the measurement by the displacement measuring means is performed at equal intervals on the exposed surface, the measurement error is small and the adjustment accuracy is excellent.

【0018】前記<8>に記載の高圧気流式粉砕装置
は、前記<7>において、前記変位計測手段が露出平面
との距離を測定する箇所が、分級ロータが蓋体に昇降可
能に接続された箇所の内の隣接する2箇所から略等距離
に位置する。この場合、前記変位計測手段の計測を、前
記露出表面において等間隔に、しかも隣接するネジ止め
箇所からも等間隔に行うので、計測の誤差が極めて少な
く、調整の精度に一層優れる。
[0018] In the high-pressure air-flow type pulverizer according to <8>, in the above <7>, a portion at which the displacement measuring means measures a distance from an exposed plane is connected to a classifier rotor such that the classifier rotor can move up and down. Are located at substantially equal distances from two adjacent locations. In this case, since the measurement by the displacement measuring means is performed at equal intervals on the exposed surface and also at equal intervals from adjacent screwed portions, the measurement error is extremely small, and the accuracy of adjustment is further improved.

【0019】前記<9>に記載の高圧気流式粉砕装置
は、前記<1>から<8>のいずれかにおいて、前記蓋
体における平面と、搬送手段における開口部との間隙が
0.2mm以下である。この場合、前記間隙(ギャッ
プ)が小さく、不純物が少なく、粒度分布が一定の微粉
が効率良く得られる。しかし、この場合、該間隙(ギャ
ップ)の調整に高精度が要求されるが、前記<1>から
<8>のいずれかに記載の高圧気流式粉砕装置であるの
で、容易に該調整が行われる。
[0019] In the high-pressure air-flow pulverizer according to <9>, in any one of <1> to <8>, a gap between a flat surface of the lid and an opening of the conveying means is 0.2 mm or less. It is. In this case, fine powder having a small gap, a small amount of impurities, and a uniform particle size distribution can be efficiently obtained. However, in this case, high precision is required for the adjustment of the gap. However, since the high-pressure air-flow-type pulverizer according to any one of <1> to <8>, the adjustment can be easily performed. Will be

【0020】前記<10>に記載の蓋体間隙調整装置
は、回転軸に垂直な平面及び該平面に対し平行な露出平
面を有すると共に高圧気流により粉砕された粉体を分級
する分級ロータが昇降可能に接続された蓋体と、前記平
面に対し平行に対向配置されると共に該分級ロータによ
り分級した粉体を導入する開口部を有し、該開口部から
導入された粉体を外部に搬送する粉体搬送手段が内部に
備えられた装置本体と、を備えてなる高圧気流式粉砕装
置に設けられる。この蓋体間隙調整装置は、前記露出平
面と間の距離(測定距離)を測定し、初期設定距離に対
する該測定距離の変位を計測する変位計測手段を備えて
いるので、前記変位の値を設定範囲内になるように前記
分級ロータを昇降させることにより、前記分級ロータの
前記平面と、前記開口部との間隙(ギャップ)の調整
が、精度良く行われる。
[0020] The lid gap adjusting device according to the above <10> has a classification rotor having a plane perpendicular to the rotation axis and an exposed plane parallel to the plane, and a classification rotor for classifying powder pulverized by a high-pressure airflow. A lid, which is connected so as to be capable of being parallel to the plane, and has an opening for introducing the powder classified by the classifying rotor, and transports the powder introduced from the opening to the outside. And a high-pressure air-flow type pulverizer comprising: Since the cover gap adjusting device includes a displacement measuring means for measuring a distance (measurement distance) from the exposed plane and measuring a displacement of the measurement distance with respect to an initial setting distance, the value of the displacement is set. By raising and lowering the classifying rotor so as to fall within the range, the gap between the plane of the classifying rotor and the opening is accurately adjusted.

【0021】[0021]

【発明の実施の形態】本発明の高圧気流式粉砕装置は、
蓋体と、装置本体と、変位計測手段とを備えてなり、必
要に応じて適宜選択したその他の手段を備えてなる。本
発明の蓋体間隙調整装置は、前記蓋体と前記装置本体と
を備える高圧気流式粉砕装置に設けられ、前記変位計測
手段を備えてなり、必要に応じて適宜選択したその他の
手段を備えてなる。以下、前記高圧気流式粉砕装置及び
前記蓋体間隙調整装置における、前記蓋体、前記装置本
体、前記変位計測手段、前記その他の手段について説明
する。
BEST MODE FOR CARRYING OUT THE INVENTION
It comprises a lid, a device body, and a displacement measuring means, and further comprises other means appropriately selected as needed. The cover gap adjusting device of the present invention is provided in a high-pressure air-flow pulverizing device including the cover and the device body, includes the displacement measuring unit, and includes other units appropriately selected as necessary. It becomes. Hereinafter, the lid, the apparatus main body, the displacement measuring means, and the other means in the high-pressure air-flow pulverizer and the lid gap adjusting device will be described.

【0022】前記蓋体としては、前記装置本体におけ
る、原料粉体を供給する開口を閉塞する機能を有する限
り、その材質、形状、構造、大きさ等については特に制
限はなく、目的に応じて公知の高圧気流式粉砕装置にお
けるものの中から適宜選択することができる。前記蓋体
には、分級ロータが回転可能に軸支され、かつ昇降可能
に接続されている。なお、該蓋体における前記分級ロー
タとの接続部分は、外部から不純物が侵入することがで
きないようにシールされる。
The material, shape, structure, size, and the like of the lid are not particularly limited as long as they have a function of closing the opening for supplying the raw material powder in the apparatus main body, and may be selected according to the purpose. It can be appropriately selected from those in a known high-pressure air-flow type pulverizer. The classification rotor is rotatably supported on the lid and is connected to the lid so as to be able to move up and down. The connecting portion of the lid with the classifying rotor is sealed so that impurities cannot enter from the outside.

【0023】前記分級ロータは、回転軸に垂直な平面及
び該平面に対し平行な露出平面を有すると共に高圧気流
により粉砕された原料粉体を分級する機能を有する限
り、特に制限はなく、目的に応じて、公知の高圧気流式
粉砕装置におけるものの中から適宜選択することができ
る。前記分級ロータは、回転軸に対してバランス調整さ
れているのが好ましい。前記バランス調整の方法として
は、特に制限はなく、公知のバランス調整方法が挙げら
れる。前記露出平面は、通常、前記蓋体における、前記
装置本体の内部に対向する側とは反対側に露出される平
面であり、その大きさ等については、特に制限はなく、
目的に応じて適宜選択することができる。
The classification rotor is not particularly limited as long as it has a plane perpendicular to the rotation axis and an exposed plane parallel to the plane, and has a function of classifying the raw material powder pulverized by the high-pressure airflow. Accordingly, it can be appropriately selected from those in a known high-pressure air-flow type pulverizer. It is preferable that the classifying rotor is adjusted in balance with respect to a rotation axis. The method of the balance adjustment is not particularly limited, and a known balance adjustment method can be used. The exposed plane is usually a plane exposed on a side of the lid opposite to a side facing the inside of the device main body, and the size and the like are not particularly limited.
It can be appropriately selected according to the purpose.

【0024】前記装置本体としては、内部で原料粉体を
微粉化(粉砕)することができる空間を有する限り、そ
の材質、形状、構造、大きさ等については特に制限はな
く、目的に応じて公知の高圧気流式粉砕装置におけるも
のの中から適宜選択することができる。
The material, shape, structure, size, etc. of the apparatus main body are not particularly limited as long as they have a space in which the raw material powder can be pulverized (crushed). It can be appropriately selected from those in a known high-pressure air-flow type pulverizer.

【0025】前記装置本体の内部表面は、摩耗防止の点
で、樹脂材料で被覆されているのが好ましく、高純度の
粉体が得られる点で、金属系不純物の含有量が少ない樹
脂材料で被覆されいるのがより好ましい。前記金属系不
純物としては、例えば、B、Na、Al、K、Cr、F
e、Ni、Cu、Zn、W等の金属系不純物が挙げられ
る。前記金属系不純物の含有量としては、10ppm以
下が好ましい。前記樹脂材料としては、例えば、ポリウ
レタンゴム、ポリアセタール樹脂、超高分子量ポリエチ
レン樹脂、ポリカーボネート、アクリル樹脂、シリコン
ゴム、塩化ビニル樹脂等が挙げられ、これらの中でも、
ポリウレタン樹脂、ポリアセタール樹脂等が好適に用い
られる。前記被覆の程度としては、特に制限はないが、
厚みで1〜15mm程度が好ましく、2〜10mm程度
がより好ましい。
The inner surface of the apparatus main body is preferably coated with a resin material from the viewpoint of preventing abrasion, and is made of a resin material having a low content of metallic impurities in that a high-purity powder is obtained. More preferably, it is coated. Examples of the metallic impurities include B, Na, Al, K, Cr, and F.
e, Ni, Cu, Zn, W, and other metal-based impurities. The content of the metallic impurities is preferably 10 ppm or less. Examples of the resin material include polyurethane rubber, polyacetal resin, ultrahigh molecular weight polyethylene resin, polycarbonate, acrylic resin, silicone rubber, and vinyl chloride resin.
Polyurethane resin, polyacetal resin and the like are preferably used. The degree of the coating is not particularly limited,
The thickness is preferably about 1 to 15 mm, more preferably about 2 to 10 mm.

【0026】前記装置本体には、粉体搬送手段が内部に
備えられている。前記粉体搬送手段は、前記平面に対し
平行に対向配置されると共に該分級ロータにより分級し
た粉体を導入する開口部を有し、該開口部から導入され
た粉体を外部に搬送することができる機能を有する限
り、特に制限はなく、目的に応じて、公知の高圧気流式
粉砕装置におけるものの中から適宜選択することができ
る。
The apparatus main body is provided with a powder conveying means inside. The powder conveying means has an opening arranged in parallel with the plane and opposed to the plane and for introducing the powder classified by the classifying rotor, and conveying the powder introduced from the opening to the outside. There is no particular limitation as long as it has the function of performing the above-mentioned operations, and it can be appropriately selected from those in a known high-pressure air-flow type pulverizer according to the purpose.

【0027】前記変位計測手段としては、前記露出平面
と間の距離(測定距離)を測定し、初期設定距離に対す
る該測定距離の変位を計測する機能を有する限り、特に
制限はなく、目的に応じて適宜選択することができ、例
えば、高精度変位計などが好適に挙げられる。該高精度
変位計としては、例えば、光学式(三角測距式)、レー
ザー透過型、渦電流式、超音波式、接触式、などの各種
方式のものであってもよいが、これらの中でも、高分解
能、高精度であり、センサヘッドが小型であり広い取付
スペースが必要なく、耐環境性に極めて優れる点で、渦
電流式の高精度変位計が好ましい。
The displacement measuring means is not particularly limited as long as it has a function of measuring a distance (measured distance) from the exposed plane and measuring a displacement of the measured distance from an initially set distance. For example, a high-precision displacement meter is preferably used. As the high-precision displacement meter, for example, various types such as an optical type (triangulation type), a laser transmission type, an eddy current type, an ultrasonic type, and a contact type may be used. An eddy-current-type high-precision displacement meter is preferable because it has high resolution, high accuracy, a small sensor head, does not require a wide mounting space, and is extremely excellent in environmental resistance.

【0028】前記変位計測手段の計測箇所としては、前
記分級ロータにおける前記露出平面上であればよく、1
箇所であってもよいし、2箇所以上であってもよい。後
者の場合、前記変位計測手段は、前記露出平面との距離
(測定距離)を各計測箇所において測定し、各計測箇所
において予め設定した初期設定距離に対する前記測定距
離の変位を計測する。
The measuring point of the displacement measuring means may be on the exposed plane of the classifying rotor.
Or two or more locations. In the latter case, the displacement measuring means measures a distance (measurement distance) from the exposed plane at each measurement point, and measures a displacement of the measurement distance with respect to an initial set distance preset at each measurement point.

【0029】これらの中でも、前記計測箇所としては、
高精度で確実に調整を行うことができる点で、3箇所以
上(少なくとも3箇所)であるのが好ましく、計測の誤
差が少なく、調整の精度に優れる点で、該計測箇所が互
いに等間隔に位置する3箇所以上(少なくとも3箇所)
であるのがより好ましい。また、該計測箇所としては、
計測誤差が極めて少なく、調整の精度に優れる点で、前
記分級ロータが前記蓋体に昇降可能に接続された箇所の
内の隣接する2箇所から略等距離に位置するのが好まし
い。
Among these, the measurement points include:
It is preferable that the number of measurement points is equal to or more than three (at least three) in that the adjustment can be performed with high accuracy, and the measurement points are equidistant from each other in that the measurement error is small and the adjustment accuracy is excellent. 3 or more locations (at least 3 locations)
Is more preferable. In addition, as the measurement location,
It is preferable that the classifying rotor is located at substantially the same distance from two adjacent places among the places that are connected to the lid so as to be able to move up and down in that the measurement error is extremely small and the adjustment accuracy is excellent.

【0030】本発明の高圧気流式粉砕装置においては、
前記分級ロータにおける前記平面と、前記粉体搬送手段
における前記開口部とが所定の大きさの間隙(ギャッ
プ)の時における前記変位計測手段の前記露出平面に対
する距離を予め初期設定距離として設定しておく。そし
て、前記変位計測手段が、前記露出表面に対する距離
(測定距離)を測定し、該測定距離と前記初期設定距離
との変位を計測する。該変位が設定範囲内(ゼロに近い
程好ましい)である場合には、前記分級ロータの位置を
昇降させて調整する必要がない。一方、該変位が設定範
囲内(ゼロに近い程好ましい)ではない場合には、該変
位の値が設定範囲内(ゼロに近い程好ましい)になるよ
うに前記分級ロータの位置を前記ネジを動かして昇降さ
せることにより調整する。前記変位が設定範囲内(ゼロ
に近い程好ましい)である場合には、前記平面と前記開
口部とが所定の大きさの間隙(ギャップ)に調整されて
いる。
In the high-pressure air-flow type pulverizer of the present invention,
The distance between the displacement measuring means and the exposed plane when the plane of the classifying rotor and the opening of the powder conveying means have a predetermined size is set as an initial setting distance in advance. deep. Then, the displacement measuring means measures a distance (measured distance) with respect to the exposed surface, and measures a displacement between the measured distance and the initially set distance. When the displacement is within the set range (preferably closer to zero), there is no need to adjust the position of the classifying rotor by moving it up and down. On the other hand, when the displacement is not within the set range (preferably closer to zero), the screw of the classification rotor is moved so that the value of the displacement is within the set range (preferably closer to zero). Adjust by raising and lowering. When the displacement is within a set range (preferably closer to zero), the plane and the opening are adjusted to have a predetermined gap.

【0031】前記間隙(ギャップ)の大きさとしては、
微粉化(粉砕)及び分級する原料粉体の種類、用途等に
応じて異なり、一概に規定することはできないが、0.
2mm以下が好ましく、0.07mm以下がより好まし
い。前記間隙(ギャップ)の大きさが、0.2mmを超
えると、前記分級ロータによる分級が不十分な粉体が該
間隙から侵入し、前記開口部を通過してしまうことがあ
り、均一な粒度分布の粉体が得られないことがある。な
お、前記間隙(ギャップ)の大きさは、通常、前記変位
の設定範囲とされる。
The size of the gap is as follows.
Although it depends on the type and use of the raw material powder to be pulverized (pulverized) and classified, it cannot be specified unconditionally.
It is preferably at most 2 mm, more preferably at most 0.07 mm. If the size of the gap (gap) exceeds 0.2 mm, powder that is insufficiently classified by the classification rotor may enter from the gap and pass through the opening, resulting in a uniform particle size. In some cases, a powder having a distribution may not be obtained. It should be noted that the size of the gap is usually set to the set range of the displacement.

【0032】前記分級ロータを前記蓋体に昇降可能に接
続するには、例えば、ネジ(ボルトも含む)等による螺
合、気圧式又は液圧式(水圧式、油圧式)シリンダーに
よる嵌合、ラックとピニオン等の歯車機構による歯合、
などを用いることができる。これらの中でも、ネジ(ボ
ルトも含む)等による螺合が好ましく、前記間隙の調整
が容易な点で細目ネジによる螺合がより好ましく、1m
m以下/360°の螺旋ピッチを有する細目ネジが更に
好ましく、0.8mm以下/360°の螺旋ピッチを有
する細目ネジによる螺合が特に好ましい。
To connect the classifying rotor to the lid so as to be able to move up and down, for example, screwing with screws (including bolts), fitting with a pneumatic or hydraulic (hydraulic, hydraulic) cylinder, racking Meshing with a gear mechanism such as a pinion and
Etc. can be used. Among these, screwing with screws (including bolts) is preferable, and screwing with fine screws is more preferable because the gap can be easily adjusted.
Fine screws having a helical pitch of not more than m / 360 ° are more preferable, and screwing with a fine screw having a helical pitch of not more than 0.8 mm / 360 ° is particularly preferable.

【0033】前記接続の位置としては、特に制限はな
く、目的に応じて適宜選択することができるが、該接続
が3箇所以上(少なくとも3箇所)で行われる場合に
は、等間隔に位置することが好ましい。
The position of the connection is not particularly limited and can be appropriately selected depending on the purpose. When the connection is made at three or more places (at least three places), the connection is made at equal intervals. Is preferred.

【0034】前記その他の手段としては、特に制限はな
く、目的に応じて適宜選択することができ、例えば、前
記装置本体の内部に原料粉体を供給する原料粉体供給手
段、前記装置本体の内部に高圧気流を供給し、該装置本
体の内部の原料粉体を粉砕させる高圧気流供給手段、前
記粉体搬送手段により外部に搬送され分級された微粉を
収容する微粉収容手段、などが好適に挙げられる。
The other means is not particularly limited and can be appropriately selected depending on the intended purpose. For example, a raw material powder supply means for supplying raw material powder into the apparatus main body, A high-pressure airflow supply means for supplying a high-pressure airflow inside and pulverizing the raw material powder inside the apparatus main body, a fine powder accommodating means for accommodating the classified fine powder conveyed to the outside by the powder conveyance means, and the like are preferably used. No.

【0035】前記高圧気流供給手段としては、特に制限
はなく、目的に応じて公知のものの中から適宜選択する
ことができ、例えば、高圧気流を対向させて噴射可能な
2つの高圧気流噴射バルブ、などが挙げられる。前記高
圧気流供給手段により供給される高圧気流の流速として
は、特に制限はなく、前記原料粉体の種類、量、目的等
に応じて適宜選択することができる。
The high-pressure air flow supply means is not particularly limited and can be appropriately selected from known ones according to the purpose. For example, two high-pressure air flow injection valves capable of injecting a high-pressure air flow in opposition are provided. And the like. The flow rate of the high-pressure airflow supplied by the high-pressure airflow supply means is not particularly limited, and can be appropriately selected according to the type, amount, purpose, and the like of the raw material powder.

【0036】なお、前記原料粉体としては、特に制限は
なく、目的に応じて適宜選択することができ、例えば、
炭化ケイ素粉体等のセラミック粉体、鉄等の金属単体粉
体やステンレス等の合金粉体等の金属粉体などの無機粉
体、熱硬化樹脂粉体、耐熱性樹脂粉体等の樹脂粉体など
の有機粉体、などが挙げられ、これらの中でも、炭化ケ
イ素粉体等のセラミック粉体が好ましい。
The raw material powder is not particularly limited and may be appropriately selected depending on the intended purpose.
Inorganic powders such as ceramic powders such as silicon carbide powders, simple metal powders such as iron, metal powders such as alloy powders such as stainless steel, and resin powders such as thermosetting resin powders and heat-resistant resin powders. And organic powders such as powders. Of these, ceramic powders such as silicon carbide powders are preferable.

【0037】[0037]

【実施例】以下、本発明の高圧気流式粉砕装置の一実施
例ついて図面を参照しながら説明する。図1は、本発明
の高圧気流式粉砕装置の一実施例を説明するための概略
説明図である。図1に示す高圧気流式粉砕装置1は、装
置本体10と蓋体20と変位計測手段30とを備える。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the high-pressure air-flow pulverizer of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic explanatory view for explaining one embodiment of a high-pressure air-flow type pulverizer of the present invention. The high-pressure air-flow type pulverizer 1 shown in FIG. 1 includes an apparatus main body 10, a lid 20, and a displacement measuring means 30.

【0038】装置本体10は、原料粉体供給手段2と、
高圧気流供給手段3と、粉体搬送手段5と、微粉収容器
6とを備える。
The apparatus main body 10 includes raw material powder supply means 2,
The apparatus includes a high-pressure air flow supply unit 3, a powder conveying unit 5, and a fine powder container 6.

【0039】原料粉体供給手段2は、原料粉体投入口2
aと、原料粉体導入路2bとを有してなる。原料粉体導
入路2bは、高圧気流粉砕装置1の内部に連通する筒体
であり、原料粉体投入口2aから投入された原料粉体を
高圧気流粉砕装置1の内部へと導入する。
The raw material powder supply means 2 includes a raw material powder input port 2
a and a raw material powder introduction path 2b. The raw material powder introduction path 2b is a cylindrical body that communicates with the inside of the high-pressure gas stream pulverizer 1, and introduces the raw material powder input from the material powder inlet 2a into the high-pressure air pulverizer 1.

【0040】高圧気流供給手段3は、装置本体10の内
部における、原料粉体導入路2bの開口部より下方に2
つ対向して設けられている。2つの高圧気流供給手段3
は、気体を同時に対向噴射し、高圧気流を、装置本体1
0の内部の底部から上方の蓋体20方向に生じさせるこ
とができるように設計されている。
The high-pressure air flow supply means 3 is located below the opening of the raw material powder introduction passage 2 b inside the apparatus main body 10.
Are provided facing each other. Two high-pressure airflow supply means 3
Simultaneously injects gas in opposite directions to generate high-pressure airflow
It is designed so that it can be generated in the direction of the upper lid 20 from the bottom inside the zero.

【0041】粉体搬送手段5は、装置本体10の内部に
おける、原料粉体導入路2bの開口部より上方に配置さ
れる。粉体搬送手段5は、分級ロータ4により分級した
粉体を導入する開口部5aと、開口部5aから導入され
た粉体を外部に搬送するための搬送路とを有する。開口
部5aは、分級ロータ4の下端面と対向する位置に設け
られ、その大きさは分級ロータ4の下端面に設けられた
開口の大きさとほぼ同等の大きさに設計されている。ま
た、前記搬送路の下流部分はサイロ様に設計されてお
り、微粉収容器6に向けて前記粉体を落下させることが
できるようになっている。
The powder conveying means 5 is disposed inside the apparatus main body 10 above the opening of the raw material powder introduction path 2b. The powder conveying means 5 has an opening 5a for introducing the powder classified by the classification rotor 4, and a conveying path for conveying the powder introduced from the opening 5a to the outside. The opening 5 a is provided at a position facing the lower end surface of the classification rotor 4, and the size thereof is designed to be substantially equal to the size of the opening provided at the lower end surface of the classification rotor 4. The downstream portion of the transport path is designed in a silo shape so that the powder can be dropped toward the fine powder container 6.

【0042】微粉収容器6は、開口部5aより粉体搬送
手段5に導入されると共に前記搬送路の下流部分から落
下される前記粉体を収容可能に設計された容器である。
The fine powder container 6 is a container designed to receive the powder introduced from the opening 5a into the powder conveying means 5 and dropped from the downstream portion of the conveying path.

【0043】蓋体20は、装置本体10の上方開口部に
開閉自在に装着されており、分級ロータ4を備える。
The lid 20 is attached to the upper opening of the apparatus main body 10 so as to be openable and closable, and includes the classification rotor 4.

【0044】分級ロータ4は、固定板4aと、回転軸4
bと、回転体4cと、棒状体(羽根ピン)4dと、棒状
体(羽根ピン)4dと着脱可能にネジ止めされた環状体
4eと、を備えている。
The classifying rotor 4 includes a stationary plate 4a and a rotating shaft 4
b, a rotating body 4c, a rod-shaped body (wing pin) 4d, and an annular body 4e which is detachably screwed to the rod-shaped body (wing pin) 4d.

【0045】固定板4aは、装置本体10の外部(蓋体
20の上方)に露出した状態で、かつ細目ネジである細
目アジャストボルト21により昇降可能に蓋体20に螺
合さている。
The fixing plate 4a is screwed to the lid 20 in a state of being exposed to the outside of the apparatus main body 10 (above the lid 20) and can be moved up and down by fine adjusting bolts 21 which are fine screws.

【0046】図2に示す通り、固定板4aは、円板状で
あり、その外周部から外方に向けて略等間隔に3箇所、
突出部が設けられている。前記突出部の上面は、固定板
4aの上面と平行な平面であり、これが前記露出平面と
して機能する。細目アジャストボルト21は、固定板4
aの外周縁部において、隣接する前記突出部から等距離
の位置に固定板4aを貫通した状態で3箇所設けられて
いる。細目アジャストボルト21の螺旋ピッチは、0.
75mm/360°である。
As shown in FIG. 2, the fixing plate 4a has a disk shape, and is provided at three locations at substantially equal intervals outward from the outer periphery.
A protrusion is provided. The upper surface of the protrusion is a plane parallel to the upper surface of the fixing plate 4a, and functions as the exposure plane. The fine adjustment bolt 21 is fixed to the fixing plate 4.
In the outer peripheral edge portion a, three portions are provided at positions equidistant from the adjacent protruding portions and penetrating the fixing plate 4a. The helical pitch of the fine adjustment bolt 21 is 0.1 mm.
75 mm / 360 °.

【0047】図3に示す通り、固定板4aを貫通した細
目アジャストボルト21には、ナット22及び23と、
固定板4aの位置を昇降可能な調整具24とが螺合され
ている。そして、ナット22は、固定板4aの上側に、
調整具24とナット23とは上からこの順に固定板4a
の下側に、それぞれ固定板4aを挟み込むようにして配
置されている。また、前記露出平面として機能する前記
突出部の上面には、変位計測手段30としての高精度変
位計が対向して配置されており、該高精度変位計によ
り、該露出平面の位置及びその設定値に対する変位が連
続して計測可能である。該高精度変位計は、蓋体20に
固定された取付具31に、ネジ止めされて設けられてい
る。
As shown in FIG. 3, nuts 22 and 23 are attached to the fine adjustment bolt 21 penetrating the fixing plate 4a.
An adjusting tool 24 that can move up and down the position of the fixing plate 4a is screwed. And the nut 22 is located above the fixing plate 4a.
The adjusting tool 24 and the nut 23 are fixed to the fixing plate 4a in this order from above.
Are arranged below the fixing plate 4 so as to sandwich the fixing plate 4a. In addition, a high-precision displacement meter as a displacement measuring means 30 is disposed on the upper surface of the projecting portion that functions as the exposure plane, and the position of the exposure plane and its setting are set by the high-precision displacement meter. The displacement with respect to the value can be measured continuously. The high-precision displacement meter is provided by being screwed to a fixture 31 fixed to the lid 20.

【0048】回転軸4bは、蓋体20を貫通した状態で
固定板4aに軸支されており、図示しない動力源により
速度可変自在に回転可能である。回転体4cは、円板状
部材であり、回転軸4bに対し垂直に固定され、回転軸
4bの回転に伴い同速で回転可能である。
The rotating shaft 4b is supported by the fixed plate 4a so as to penetrate the lid 20, and can be rotated at a variable speed by a power source (not shown). The rotating body 4c is a disc-shaped member, is fixed perpendicular to the rotating shaft 4b, and can rotate at the same speed as the rotating shaft 4b rotates.

【0049】棒状体(羽根ピン)4dは、円柱形状であ
り、その一端が回転体4cの外周縁部における同一円周
上に着脱可能に複数ネジ止めされている。環状体4e
は、回転体4cと略同径でその中心部に開口が設けられ
た円板状部材であり、棒状体(羽根ピン)4dにおける
前記一端とは反対側の他端と着脱可能にネジ止めされて
いる。なお、棒状体(羽根ピン)4dに摩耗等が生じた
場合には、棒状体(羽根ピン)4dは、回転体4cと環
状体4eとにネジ止めされているので、このネジとめを
解けば、容易に取り外すことができるので、摩耗時の取
り替えが容易である。
The rod (blade pin) 4d has a cylindrical shape, and one end thereof is detachably screwed on the same circumference at the outer peripheral edge of the rotating body 4c. Ring 4e
Is a disk-shaped member having substantially the same diameter as the rotating body 4c and having an opening at the center thereof, and is detachably screwed to the other end of the rod-shaped body (blade pin) 4d opposite to the one end. ing. When the rod-shaped body (wing pin) 4d is worn or the like, the rod-shaped body (wing pin) 4d is screwed to the rotating body 4c and the annular body 4e. , And can be easily removed, so that replacement when worn is easy.

【0050】分級ロータ4の下端面である平面4f(即
ち環状体4eの表面(開口面))と、開口部5aとの間
隙は、0.2mm以下である。この実施例では、後述す
る変位計測手段30における設定値は、0.2mm以下
とされている。
The gap between the flat surface 4f, which is the lower end surface of the classifying rotor 4 (ie, the surface (opening surface) of the annular body 4e), and the opening 5a is 0.2 mm or less. In this embodiment, the set value in the displacement measuring means 30 described later is set to 0.2 mm or less.

【0051】以下に、高圧気流式粉砕装置1の作用を説
明する。高圧気流式粉砕装置1においては、原料粉体供
給手段2の原料粉末投入口6から供給された原料粉体
が、原料粉体導入路2bを通って装置本体10の内部へ
導入される。なお、ここでの前記原料粉体は炭化ケイ素
粉体である。装置本体10の内部へ導入された原料粉体
は、原料粉体導入路2bより下方に、互いに対向して設
けられた高圧気流供給手段3から対向して供給される高
圧気流により、互いに強い衝撃力で衝突し合うことによ
り微粉化(粉砕)される。微粉化された粉体は、前記高
圧気流による上昇流により、上方で高速回転する分級ロ
ータ4へと搬送される。分級ロータ4の回転力により、
搬送されてきた粉体の内、所定の粒径にまで微粉化(粉
砕)されていない粉体は弾き飛ばされ、所定の粒径にま
で微粉化(粉砕)された粉体のみが分級ロータ4の内部
に侵入し分級ロータ4を通過する。分級ロータ4を通過
した粉体は、環状体4eの開口を通過し、開口部5aを
通過し、粉体搬送手段5により微粉収容器6内に搬送さ
れ、そこに収容される。
Hereinafter, the operation of the high-pressure air-flow type pulverizer 1 will be described. In the high-pressure air-flow-type pulverizer 1, the raw material powder supplied from the raw material powder inlet 6 of the raw material powder supply means 2 is introduced into the apparatus main body 10 through the raw material powder introduction path 2b. Here, the raw material powder is a silicon carbide powder. The raw material powder introduced into the inside of the apparatus main body 10 is strongly impacted by the high-pressure air flow supplied from the high-pressure air flow supply means 3 provided opposite to each other below the raw material powder introduction path 2b. It is pulverized (crushed) by colliding with each other by force. The pulverized powder is conveyed to the classifying rotor 4 rotating at a high speed at an upper position by the upward flow by the high-pressure air flow. By the torque of the classifying rotor 4,
Of the conveyed powders, powders that have not been pulverized (crushed) to a predetermined particle size are repelled, and only the powders that have been pulverized (pulverized) to a predetermined particle size are classified by the classification rotor 4. And passes through the classification rotor 4. The powder that has passed through the classifying rotor 4 passes through the opening of the annular body 4e, passes through the opening 5a, is transported by the powder transporting means 5 into the fine powder container 6, and is stored therein.

【0052】高圧気流式粉砕機1においては、分級ロー
タ4の下端面である平面4f(即ち環状体4eの表面
(開口面))と開口部5aとの間隙(ギャップ)は、以
下のように調整される。即ち、変位計測手段30が、対
向する突出部4gの前記露出平面と間の距離(測定距
離)を測定し、初期設定距離に対する前記測定距離の変
位を計測する。そして、変位計測手段30の計測結果に
基づき、該変位が設定範囲(ゼロに近い程好ましく、こ
の実施例では0.2mm以下である)になるように、蓋
体20に螺合された分級ロータ4の位置を、調整具24
を回転させて昇降させることにより調整する。
In the high-pressure air-flow type pulverizer 1, the gap between the flat surface 4f (ie, the surface (opening surface) of the annular body 4e), which is the lower end surface of the classifying rotor 4, and the opening 5a is as follows. Adjusted. That is, the displacement measuring means 30 measures the distance (measurement distance) between the opposing projection 4g and the exposed plane, and measures the displacement of the measurement distance with respect to the initially set distance. Then, based on the measurement result of the displacement measuring means 30, the classifying rotor screwed to the lid 20 such that the displacement is within a set range (preferably closer to zero, preferably 0.2 mm or less in this embodiment). 4 with the adjusting tool 24
Adjust by rotating and raising and lowering.

【0053】前記調整の原理は、以下の通りである。即
ち、変位計測手段30の計測対象である、分級ロータ4
の下端面である平面4fと、分級ロータの回転軸に垂直
な平面4fと、平面4fに対し対向配置される開口部5
aとは、互いに平行になっている。平面4fと開口部5
aとが所定の大きさの間隙(ギャップ)になっている時
の、変位計測手段30の前記露出平面に対する距離を初
期設定距離として予め設定しておく。そして、変位計測
手段30が、測定時点での前記露出表面に対する距離
(測定距離)を測定し、該測定距離と前記初期設定距離
との変位を計測し、該変位の値が設定範囲内(ゼロに近
い程好ましい)である0.2mm以下になるように分級
ロータ4の位置を昇降させることにより、平面4fと開
口部5aとが所定の大きさの間隙(ギャップ)に調整さ
れる。
The principle of the adjustment is as follows. That is, the classifying rotor 4 which is the measurement object of the displacement measuring means 30
4f, which is the lower end surface of the rotor, a plane 4f which is perpendicular to the rotation axis of the classifying rotor, and an opening 5 which is opposed to the plane 4f.
a are parallel to each other. Plane 4f and opening 5
The distance of the displacement measuring means 30 to the exposed plane when a is a gap having a predetermined size is previously set as an initial setting distance. Then, the displacement measuring means 30 measures a distance (measured distance) with respect to the exposed surface at the time of measurement, measures a displacement between the measured distance and the initially set distance, and sets a value of the displacement within a set range (zero). By raising and lowering the position of the classifying rotor 4 so as to be equal to or less than 0.2 mm, which is preferable to the above, the plane 4f and the opening 5a are adjusted to have a predetermined gap.

【0054】高圧気流式粉砕機1においては、前記間隙
の調整(ギャップ調整)の際に、蓋体20を開けて分級
ロータ4を露出させ、分級ロータ4の下端面である平面
4fと、平面4fに対し対向配置される開口部5aとの
間に所定の厚みの隙間ゲージを配置し、分級ロータ4の
取り付け部(前記蓋体20の内側)に適当なスペーサー
等を脱着等する必要がなく、調整具24を回転させて分
級ロータ4の位置を昇降させるだけで調整作業が完了す
るので、作業が極めて容易であり、不純物の混入が少な
い。また、前記間隙の調整(ギャップ調整)を行った後
に、ゴミや埃塵等の侵入による粒度分布の精度低下を防
ぐための空運転の必要もない。
In the high-pressure air-flow type pulverizer 1, when adjusting the gap (gap adjustment), the lid 20 is opened to expose the classifying rotor 4, and a flat surface 4f, which is the lower end surface of the classifying rotor 4, and a flat surface 4f. A gap gauge having a predetermined thickness is arranged between the opening 5a and the opening 5a opposed to the opening 4f, so that it is not necessary to attach or detach an appropriate spacer or the like to the attachment portion of the classification rotor 4 (inside the lid 20). Since the adjusting operation is completed only by rotating the adjusting tool 24 to raise and lower the position of the classifying rotor 4, the operation is extremely easy and the contamination of impurities is small. Further, after the gap adjustment (gap adjustment) is performed, there is no need to perform idle operation for preventing a decrease in the accuracy of the particle size distribution due to intrusion of dust and dirt.

【0055】[0055]

【発明の効果】本発明によると、粉体の微粉化・分級等
に用いられ、ギャップ調整の容易で不純物の混入が少な
い、対面衝突型の高圧気流式粉砕装置、及び該高圧気流
式粉砕装置のギャップを容易に調整することができる蓋
体隙間調整装置を提供することができる。
According to the present invention, a face-to-face collision type high-pressure air-flow-type pulverizer, which is used for pulverizing and classifying powders, is easy to adjust a gap, and contains little impurities, and the high-pressure air-flow-type pulverizer. Can be provided, which can easily adjust the gap of the cover.

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

【図1】図1は、本発明の高圧気流式粉砕装置の一実施
例を説明するための概略説明図である。
FIG. 1 is a schematic explanatory view for explaining one embodiment of a high-pressure air-flow type pulverizer of the present invention.

【図2】図2は、分級ロータにおける露出表面の概略説
明図である。
FIG. 2 is a schematic explanatory view of an exposed surface in a classifying rotor.

【図3】図3は、変位計測手段の拡大概略説明図であ
る。
FIG. 3 is an enlarged schematic explanatory view of a displacement measuring means.

【符号の説明】[Explanation of symbols]

1 高圧気流式粉砕装置 2 原料粉体供給手段 2a 原料粉体投入口 2b 原料粉体導入路 3 高圧気流供給手段 4 分級ロータ 4a 固定板 4b 回転軸 4c 回転体 4d 棒状体(羽根ピン) 4e 環状体 4f 平面 4g 突出部 5 粉体搬送手段 5a 開口部 6 微粉収容器 10 装置本体 20 蓋体 21 細目アジャストボルト 22 ナット 23 ナット 24 調整具 30 変位計測手段 31 取付具 DESCRIPTION OF SYMBOLS 1 High-pressure air-flow type pulverizer 2 Raw material powder supply means 2a Raw material powder input port 2b Raw material powder introduction path 3 High-pressure air flow supply means 4 Classification rotor 4a Fixed plate 4b Rotary shaft 4c Rotating body 4d Rod-shaped body (blade pin) 4e Ring Body 4f Flat surface 4g Projecting part 5 Powder conveying means 5a Opening 6 Fine powder container 10 Device main body 20 Lid 21 Fine adjusting bolt 22 Nut 23 Nut 24 Adjusting tool 30 Displacement measuring means 31 Mounting tool

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 回転軸に垂直な平面及び該平面に対し平
行な露出平面を有すると共に高圧気流により粉砕された
原料粉体を分級する分級ロータが昇降可能に接続された
蓋体と、 前記平面に対し平行に対向配置されると共に該分級ロー
タにより分級した粉体を導入する開口部を有し、該開口
部から導入された粉体を外部に搬送する粉体搬送手段が
内部に備えられた装置本体と、 前記露出平面と間の距離を測定し、初期設定距離に対す
る測定距離の変位を計測する変位計測手段と、 を備えたことを特徴とする高圧気流式粉砕装置。
1. A lid having a plane perpendicular to a rotation axis and an exposed plane parallel to the plane, and a classifier rotor for classifying raw material powder pulverized by a high-pressure air flow connected to the classifier so as to be able to move up and down. And an opening for introducing the powder classified by the classifying rotor, and a powder conveying means for conveying the powder introduced from the opening to the outside is provided inside. A high-pressure gas-flow-type pulverizer, comprising: an apparatus main body; and a displacement measuring unit that measures a distance between the exposed plane and a displacement of a measured distance with respect to an initially set distance.
【請求項2】 接続が螺合である請求項1に記載の高圧
気流式粉砕装置。
2. The high-pressure air-flow type pulverizer according to claim 1, wherein the connection is screwed.
【請求項3】 螺合が、1mm以下/360°の螺旋ピ
ッチを有する細目ネジで行われた請求項2に記載の高圧
気流式粉砕装置。
3. The high-pressure air-flow pulverizer according to claim 2, wherein the screwing is performed with a fine screw having a helical pitch of 1 mm or less / 360 °.
【請求項4】 分級ロータが等間隔にかつ少なくとも3
箇所で蓋体に昇降可能に接続された請求項1から3のい
ずれかに記載の高圧気流式粉砕装置。
4. Classification rotors are equally spaced and at least 3
The high-pressure air-flow type pulverizer according to any one of claims 1 to 3, wherein the high-pressure air pulverizer is connected to the lid so as to be able to move up and down.
【請求項5】 変位計測手段が高精度変位計である請求
項1から4のいずれかに記載の高圧気流式粉砕装置。
5. The high-pressure air-flow crusher according to claim 1, wherein the displacement measuring means is a high-precision displacement meter.
【請求項6】 変位計測手段が露出平面との距離を少な
くとも3箇所測定し、各箇所において予め設定した設定
値に対する前記距離の変位を計測する請求項1から5の
いずれかに記載の高圧気流式粉砕装置。
6. The high-pressure airflow according to claim 1, wherein the displacement measuring means measures a distance from the exposed plane at at least three places, and measures a displacement of the distance with respect to a preset value at each place. Type crusher.
【請求項7】 変位計測手段が、露出平面との距離を等
間隔にかつ少なくとも3箇所測定し、各箇所において予
め設定した設定値に対する前記距離の変位を計測する請
求項1から6のいずれかに記載の高圧気流式粉砕装置。
7. The displacement measuring device according to claim 1, wherein the displacement measuring means measures the distance from the exposed plane at equal intervals and at least three places, and measures the displacement of the distance with respect to a preset value at each place. 2. A high-pressure air-flow type pulverizer according to 1.
【請求項8】 変位計測手段が露出平面との距離を測定
する箇所が、分級ロータが蓋体に昇降可能に接続された
箇所の内の隣接する2箇所から略等距離に位置する請求
項7に記載の高圧気流式粉砕装置。
8. The position where the displacement measuring means measures the distance from the exposed plane is located at substantially the same distance from two adjacent positions where the classifying rotor is connected to the lid so as to be able to move up and down. 2. A high-pressure air-flow type pulverizer according to 1.
【請求項9】 分級ロータにおける平面と、粉体搬送手
段における開口部との間隙が0.2mm以下である請求
項1から8のいずれかに記載の高圧気流式粉砕装置。
9. The high-pressure air-flow pulverizer according to claim 1, wherein a gap between a plane of the classifying rotor and an opening of the powder conveying means is 0.2 mm or less.
【請求項10】 回転軸に垂直な平面及び該平面に対し
平行な露出平面を有すると共に高圧気流により粉砕され
た原料粉体を分級する分級ロータが昇降可能に接続され
た蓋体と、 前記平面に対し平行に対向配置されると共に該分級ロー
タにより分級した粉体を導入する開口部を有し、該開口
部から導入された粉体を外部に搬送する粉体搬送手段が
内部に備えられた装置本体と、 を備えてなる高圧気流式粉砕装置に設けられ、前記平面
と該開口部との間隙を調整する蓋体間隙調整装置であっ
て、 前記露出平面と間の距離を測定し、初期設定距離に対す
る測定距離の変位を計測する変位計測手段を備えたこと
を特徴とする蓋体間隙調整装置。
10. A lid having a plane perpendicular to a rotation axis and an exposed plane parallel to the plane, and a classifier rotor for classifying raw material powder pulverized by a high-pressure air flow, the lid being connected to be able to move up and down; And an opening for introducing the powder classified by the classifying rotor, and a powder conveying means for conveying the powder introduced from the opening to the outside is provided inside. An apparatus main body, provided in a high-pressure air-flow crushing apparatus comprising: a lid gap adjusting apparatus for adjusting a gap between the plane and the opening, measuring a distance between the exposed plane, A cover gap adjusting device comprising a displacement measuring means for measuring a displacement of a measurement distance with respect to a set distance.
JP2000316402A 2000-10-17 2000-10-17 Cover gap adjustment device, and jet mill Pending JP2002119882A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000316402A JP2002119882A (en) 2000-10-17 2000-10-17 Cover gap adjustment device, and jet mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000316402A JP2002119882A (en) 2000-10-17 2000-10-17 Cover gap adjustment device, and jet mill

Publications (1)

Publication Number Publication Date
JP2002119882A true JP2002119882A (en) 2002-04-23

Family

ID=18795356

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000316402A Pending JP2002119882A (en) 2000-10-17 2000-10-17 Cover gap adjustment device, and jet mill

Country Status (1)

Country Link
JP (1) JP2002119882A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007038109A (en) * 2005-08-02 2007-02-15 Bridgestone Corp Air flow type pulverizer
JP2011500310A (en) * 2007-10-09 2011-01-06 シービーピー・カーボン・インダストリーズ・インコーポレーテッド Method for classifying particles in pyrolyzed coal

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62151986U (en) * 1986-03-20 1987-09-26
JPH0383646U (en) * 1989-12-15 1991-08-26
JPH03275181A (en) * 1990-03-27 1991-12-05 Nippon Steel Chem Co Ltd Separator
JPH05146704A (en) * 1991-11-29 1993-06-15 Kurimoto Ltd Feed control method of particulate matter in crushing and classifying apparatus
JPH0871442A (en) * 1994-09-07 1996-03-19 Toshiba Corp Paper treating device
JPH08509415A (en) * 1993-04-27 1996-10-08 エフ エル スミス アンド コムパニー アクティーゼルスカブ Separators for sorting granular materials

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62151986U (en) * 1986-03-20 1987-09-26
JPH0383646U (en) * 1989-12-15 1991-08-26
JPH03275181A (en) * 1990-03-27 1991-12-05 Nippon Steel Chem Co Ltd Separator
JPH05146704A (en) * 1991-11-29 1993-06-15 Kurimoto Ltd Feed control method of particulate matter in crushing and classifying apparatus
JPH08509415A (en) * 1993-04-27 1996-10-08 エフ エル スミス アンド コムパニー アクティーゼルスカブ Separators for sorting granular materials
JPH0871442A (en) * 1994-09-07 1996-03-19 Toshiba Corp Paper treating device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007038109A (en) * 2005-08-02 2007-02-15 Bridgestone Corp Air flow type pulverizer
JP2011500310A (en) * 2007-10-09 2011-01-06 シービーピー・カーボン・インダストリーズ・インコーポレーテッド Method for classifying particles in pyrolyzed coal

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