JP2877799B1 - Particle classifier - Google Patents

Particle classifier

Info

Publication number
JP2877799B1
JP2877799B1 JP7155498A JP7155498A JP2877799B1 JP 2877799 B1 JP2877799 B1 JP 2877799B1 JP 7155498 A JP7155498 A JP 7155498A JP 7155498 A JP7155498 A JP 7155498A JP 2877799 B1 JP2877799 B1 JP 2877799B1
Authority
JP
Japan
Prior art keywords
flat plate
particles
angle
fine particles
particle
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 - Fee Related
Application number
JP7155498A
Other languages
Japanese (ja)
Other versions
JPH11267593A (en
Inventor
一博 小泉
直人 渡邉
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP7155498A priority Critical patent/JP2877799B1/en
Application granted granted Critical
Publication of JP2877799B1 publication Critical patent/JP2877799B1/en
Publication of JPH11267593A publication Critical patent/JPH11267593A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

【要約】 【課題】高温粒子をも能率的に分級することができる耐
久性に優れた粒子の分級装置を提供する。 【解決手段】斜め方向に延びる多数の傾斜溝2を備えた
耐熱材料製の平板1を水平面から傾斜角αを持たせて設
置する。平板1の上部には粒子の投入部6を設け、また
その下部には粗大粒子の回収部7と、傾斜溝2に沿って
落下する微細粒子の回収部8とを設ける。平板2を利用
した分級ができるので、900 〜1000℃の高温の粒子をも
連続的かつ能率的に分級することができる。
An object of the present invention is to provide a highly durable particle classifier capable of efficiently classifying high-temperature particles. A flat plate (1) made of a heat-resistant material having a large number of inclined grooves (2) extending in an oblique direction is installed at an inclination angle (α) from a horizontal plane. An upper part of the flat plate 1 is provided with a particle input section 6, and a lower part thereof is provided with a coarse particle recovery section 7 and a fine particle recovery section 8 which falls along the inclined groove 2. Since classification using the flat plate 2 can be performed, particles having a high temperature of 900 to 1000 ° C. can be continuously and efficiently classified.

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】本発明は粒子の分級装置に関
するものであり、特に通常の分級装置を使用できない高
温粒子の分級に適した粒子の分級装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for classifying particles, and more particularly to an apparatus for classifying particles suitable for classifying high-temperature particles which cannot be used with ordinary classifiers.

【0002】[0002]

【従来の技術】例えば流動焼却炉の内部に焼却灰の造粒
物を投入して造粒焼結灰を製造する場合には、粒径が5m
m 程度の造粒焼結灰を平均粒径が0.3 〜0.4mm の流動媒
体から900 〜1000℃の高温状態で分離し、流動媒体は炉
内に返送することが好ましい。粗大粒子と微細粒子との
混合物を分級するには通常は篩が用いられるが、篩のメ
ッシュを耐熱金属製としてもこのような高温の粒子を接
触させると短時間で損傷されてしまうため、高温粒子の
分級ができなかった。また空気分級は高温粒子に対して
も使用可能であるが、処理能力が非常に低いことや、空
気により粒子が冷却されるため熱ロスが大きくなる問題
があった。
2. Description of the Related Art For example, when granulated incinerated ash is put into a fluidized incinerator to produce granulated sintered ash, the particle size is 5 m.
It is preferable that the granulated sintered ash of about m is separated from a fluid medium having an average particle diameter of 0.3 to 0.4 mm at a high temperature of 900 to 1000 ° C., and the fluid medium is returned to the furnace. A sieve is usually used to classify a mixture of coarse particles and fine particles, but even if the mesh of the sieve is made of a refractory metal, if such high-temperature particles are brought into contact, they will be damaged in a short time. Particles could not be classified. Although air classification can be used for high-temperature particles, there are problems that the processing capacity is very low and that heat loss is increased because the particles are cooled by air.

【0003】[0003]

【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、従来の篩が使用できないような高温
粒子をも能率的に分級することができる耐久性に優れた
粒子の分級装置を提供するためになされたものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems and classifies high-temperature particles which cannot be used by conventional sieves efficiently and has excellent durability. It was made to provide a device.

【0004】[0004]

【課題を解決するための手段】上記の課題を解決するた
めになされた粒子の分級装置は、斜め方向に延びる多数
の傾斜溝を備えた平板を水平面から下向きに傾斜させて
設置し、その上部には粒子の投入部を設け、またその下
部には投入部の直下に落下する粗大粒子の回収部と、傾
斜溝に沿って落下する微細粒子の回収部とを設けたこと
を特徴とするものである。
In order to solve the above-mentioned problem, a particle classifying apparatus is provided in which a flat plate having a large number of inclined grooves extending in an oblique direction is installed so as to be inclined downward from a horizontal plane, and the upper part thereof is provided. Is provided with a particle input section, and a recovery section for coarse particles falling directly below the input section and a recovery section for fine particles falling along the inclined groove are provided below the input section. It is.

【0005】粗大粒子の回収部と微細粒子の回収部との
間に、分離ゲートを設けることが好ましく、平板の上面
に、平板側に微細粒子の通過を妨げない隙間を備えたガ
ードを設けることが好ましい。また、水平面に対する平
板の傾斜角を、分級する粒子の安息角の大きいものの角
度よりも12.5〜17.5°大きい値とし、平板の傾斜溝が水
平面に対してなす溝角度を、分級する粒子の安息角の大
きいものの角度よりも20〜25°大きい値としておくこと
が好ましい。
[0005] It is preferable to provide a separation gate between the collecting section for the coarse particles and the collecting section for the fine particles, and to provide a guard provided on the upper surface of the flat plate with a gap on the flat plate side which does not hinder the passage of the fine particles. Is preferred. Further, the inclination angle of the flat plate with respect to the horizontal plane is set to a value that is larger than the angle of repose of the particles to be classified by 12.5 to 17.5 °, and the groove angle formed by the inclined groove of the flat plate with respect to the horizontal plane, the repose angle of the particles to be classified Is preferably set to a value 20 to 25 ° larger than the angle of the object having the larger value.

【0006】本発明の粒子の分級装置は、平板の表面に
沿って粒子を落下させ、微細粒子は傾斜溝により斜め方
向に落下するが、粗大粒子は傾斜溝を乗り越えながら垂
直に落下することを利用して、分級を行う。このため平
板をセラミックス等の耐熱材料で構成しておけば、900
〜1000℃の高温の粒子を連続的かつ能率的に分級するこ
とができる。
[0006] The particle classification apparatus of the present invention is designed to drop particles along the surface of a flat plate, and to cause fine particles to fall obliquely by the inclined grooves, but coarse particles to fall vertically while climbing over the inclined grooves. Use and classify. Therefore, if the flat plate is made of a heat-resistant material such as ceramics, 900
High temperature particles of ~ 1000 ° C can be classified continuously and efficiently.

【0007】[0007]

【発明の実施の形態】以下に本発明の好ましい実施の形
態を示す。図1は本発明の分級装置の斜視図、図2はそ
の正面図、図3はその側面図である。これらの図におい
て、1はセラミック等の耐熱材料よりなる平板であり、
その表面には斜め方向に延びる多数の傾斜溝2が形成さ
れている。傾斜溝2は例えば図4(A) に示すように平板
1の表面に凸条3を張り付けることにより形成しても、
図4(B) に示すように高さの異なる多数枚の薄板4を積
層することにより形成しても、図4(C) に示すように平
板1の表面にスリット5を刻むことにより形成してもよ
い。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below. FIG. 1 is a perspective view of a classification device of the present invention, FIG. 2 is a front view thereof, and FIG. 3 is a side view thereof. In these figures, 1 is a flat plate made of a heat-resistant material such as ceramic,
A large number of inclined grooves 2 extending in an oblique direction are formed on the surface. Even if the inclined groove 2 is formed by attaching a ridge 3 to the surface of the flat plate 1 as shown in FIG.
As shown in FIG. 4 (B), even when formed by laminating many thin plates 4 having different heights, they are formed by cutting slits 5 in the surface of the flat plate 1 as shown in FIG. 4 (C). You may.

【0008】傾斜溝2の深さは分級しようとする粒子中
の微細粒子の直径よりも大きく、粗大粒子の直径よりも
小さいものとする。以下の例では、平均粒径が5mm 程度
で安息角37.5°の粗大粒子と、平均粒径が0.3 〜0.4mm
で安息角35°の微細粒子との分級を、傾斜溝2の深さと
幅がともに2mm の平板1を用いて行った。
It is assumed that the depth of the inclined groove 2 is larger than the diameter of the fine particles in the particles to be classified and smaller than the diameter of the coarse particles. In the example below, coarse particles with an average particle size of about 5 mm and a repose angle of 37.5 °, and an average particle size of 0.3 to 0.4 mm
The classification with fine particles having an angle of repose of 35 ° was performed using a flat plate 1 in which both the depth and width of the inclined groove 2 were 2 mm.

【0009】このような傾斜溝2を持つ平板1は、図3
に示すように水平面から下向きに傾斜させて設置され
る。その傾斜角αは45〜60°程度とし、後記する実施例
のデータでは50〜55°が最適であり、安息角の大きい粗
大粒子の安息角よりも12.5〜17.5°大きな値であった。
しかしこの傾斜角αは適宜設定することができる。また
平板の傾斜溝が水平面に対してなす溝角度βは55〜65°
程度とし、後記する実施例のデータでは57.5〜62.5°が
最適であり、粗大粒子の安息角よりも20〜25°大きな値
であった。しかしこれらの角度は分級しようとする粒子
の安息角に左右されるものであるから、粒子の種類によ
って決定すべきである。
The flat plate 1 having such an inclined groove 2 is shown in FIG.
As shown in the figure, it is installed inclined downward from the horizontal plane. The inclination angle α is about 45 to 60 °, and in the data of the examples described later, the optimum is 50 to 55 °, which is 12.5 to 17.5 ° larger than the repose angle of coarse particles having a large repose angle.
However, the inclination angle α can be set as appropriate. In addition, the angle β of the inclined groove of the flat plate with respect to the horizontal plane is 55 to 65 °
57.5 to 62.5 ° was optimal in the data of Examples described later, and was a value 20 to 25 ° larger than the angle of repose of the coarse particles. However, since these angles depend on the angle of repose of the particles to be classified, they should be determined according to the type of the particles.

【0010】この平板1の上部の片側には粒子の投入部
6が設けられ、粗大粒子と微細粒子とが混合している粒
子が投入される。微細粒子は平板1の傾斜溝2に入り込
むため傾斜溝2に沿って斜め方向に落下するが、粗大粒
子は傾斜溝2よりも大きいために傾斜溝2を乗り越えな
がら垂直に落下しこれによって分級が行われる。また平
板1の下部には、投入部6の直下に落下する粗大粒子の
回収部7と、傾斜溝2に沿って落下する微細粒子の回収
部8とを設けてある。なお、それらの間には分離ゲート
9を設けておくことが好ましい。
On one side of the upper part of the flat plate 1, a particle input section 6 is provided, and particles in which coarse particles and fine particles are mixed are input. The fine particles fall into the inclined groove 2 of the flat plate 1 and fall obliquely along the inclined groove 2, but the coarse particles fall vertically while climbing over the inclined groove 2 because they are larger than the inclined groove 2. Done. At the lower part of the flat plate 1, there are provided a collecting section 7 for coarse particles falling just below the input section 6 and a collecting section 8 for fine particles falling along the inclined groove 2. It is preferable to provide an isolation gate 9 between them.

【0011】しかしこのような傾斜溝2を設けただけで
は、粗大粒子の一部が傾斜溝2の側面に衝突して飛び跳
ね、微細粒子の回収部8に入り込む恐れがある。そこで
分離ゲート9の上方に平板1側に微細粒子の通過を妨げ
ない隙間10を備えたガード11を設け、飛び跳ねた粗
大粒子がガード11を乗り越えて微細粒子の回収部8に
入り込むことを防止することが好ましい。図1と図2で
はガード11は垂直に示されているが、傾斜溝2と直行
する方向に傾けてもよい。
However, if only such an inclined groove 2 is provided, a part of the coarse particles may collide with the side surface of the inclined groove 2 and jump off, and may enter the collecting section 8 for the fine particles. Therefore, a guard 11 having a gap 10 which does not hinder the passage of the fine particles is provided above the separation gate 9 on the side of the flat plate 1 to prevent the jumping coarse particles from climbing over the guard 11 and entering the collection part 8 of the fine particles. Is preferred. Although the guard 11 is shown vertically in FIGS. 1 and 2, the guard 11 may be inclined in a direction perpendicular to the inclined groove 2.

【0012】上記のとおり、本発明の分級装置は平板1
を利用して粒子の分級を行うので、平板1を耐熱材料製
としておけば900 〜1000℃の高温の粒子を連続的かつ能
率的に分級することができる。次の本発明の実施例を示
す。
As described above, the classification device of the present invention uses the flat plate 1
When the flat plate 1 is made of a heat resistant material, particles having a high temperature of 900 to 1000 ° C. can be continuously and efficiently classified. The following examples of the present invention are shown.

【0013】[0013]

【実施例】図1に示される形状の分級装置を用い、傾斜
角α、溝角度β、分離ゲート9の幅A、ガード11の隙
間10の高さH等を種々変更して混入率(粗大粒子の回
収部7への微細粒子の混入率及び微細粒子の回収部8へ
の粗大粒子の混入率)を試験した。試験に用いた粒子
は、平均粒径が5mm で安息角37.5°の造粒焼結灰5kg を
平均粒径が0.3 〜0.4mm で安息角35°の硅砂10kgと混合
したものであり、傾斜溝2の幅と深さはそれぞれ2mm と
した。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Using a classifier having the shape shown in FIG. 1, the inclination angle α, groove angle β, width A of the separation gate 9 and height H of the gap 10 of the guard 11 are variously changed, and the mixing ratio (coarse) The mixing ratio of the fine particles into the collecting portion 7 of the particles and the mixing ratio of the coarse particles into the collecting portion 8 of the fine particles were tested. The particles used in the test consisted of 5 kg of granulated sintered ash having an average particle size of 5 mm and a repose angle of 37.5 ° mixed with 10 kg of silica sand having an average particle size of 0.3 to 0.4 mm and a repose angle of 35 °. The width and depth of 2 were each 2 mm.

【0014】図5は傾斜角αと混入率との関係を示すグ
ラフである。ただし溝角度βは60°とし、分離ゲート9
の幅Aは250mm とした。図示のとおり、傾斜角αが45°
未満では流れが悪く分級できず、傾斜角αが60°を越え
ると微細粒子も傾斜溝2を乗り越えて粗大粒子の回収部
7に落下してしまうため、微細粒子の混入率が高くなっ
た。この例では、傾斜角αを50〜55°としたときに最も
好ましい結果が得られた。
FIG. 5 is a graph showing the relationship between the inclination angle α and the mixing ratio. However, the groove angle β is 60 ° and the separation gate 9
Has a width A of 250 mm. As shown, the inclination angle α is 45 °
If the inclination angle α exceeds 60 °, the fine particles climb over the inclined groove 2 and fall into the collecting part 7 for coarse particles, so that the mixing ratio of the fine particles increases. In this example, the most preferable result was obtained when the inclination angle α was 50 to 55 °.

【0015】図6は溝角度βと混入率との関係を示すグ
ラフである。ただし傾斜角αは52.5°とし分離ゲート9
の幅Aは200mm とした。図示のとおり、溝角度βを57.5
〜62.5°としたときに最も好ましい結果が得られた。
FIG. 6 is a graph showing the relationship between the groove angle β and the mixing ratio. However, the inclination angle α is 52.5 ° and the separation gate 9
Has a width A of 200 mm. As shown, the groove angle β is 57.5
The most favorable results were obtained when the angle was set to 662.5 °.

【0016】図7は分離ゲート9の幅Aと混入率との関
係を示すグラフである。ただし傾斜角αは52.5°とし、
溝角度βは60°とした。分離ゲート9の幅Aを狭くする
と微細粒子の回収部8への粗大粒子の混入率が増加し、
逆に分離ゲート9の幅Aを広くすると粗大粒子の回収部
7への微細粒子の混入率が増加する。従って分級の目的
に応じて分離ゲート9の幅Aを調節することが好まし
い。
FIG. 7 is a graph showing the relationship between the width A of the separation gate 9 and the mixing ratio. However, the inclination angle α is 52.5 °,
The groove angle β was 60 °. When the width A of the separation gate 9 is reduced, the mixing ratio of coarse particles into the collection unit 8 of fine particles increases,
Conversely, when the width A of the separation gate 9 is increased, the mixing ratio of the fine particles into the collection unit 7 for the coarse particles increases. Therefore, it is preferable to adjust the width A of the separation gate 9 according to the purpose of classification.

【0017】図8は、平板1の縦方向の長さLと混入率
との関係を示すグラフである。ただし傾斜角αは52.5
°、溝角度βは60°、分離ゲート9の幅Aは100mmとし
た。長さLを大きくすれば粗大粒子の回収部7への微細
粒子の混入率は低下するが、完全に0とすることはでき
なかった。
FIG. 8 is a graph showing the relationship between the longitudinal length L of the flat plate 1 and the mixing ratio. However, the inclination angle α is 52.5
°, the groove angle β was 60 °, and the width A of the separation gate 9 was 100 mm. When the length L is increased, the mixing ratio of the fine particles into the collection part 7 of the coarse particles is reduced, but it cannot be completely reduced to zero.

【0018】図9は、分離ゲート9の隙間10の高さH
と混入率との関係を示すグラフである。ただし傾斜角α
は52.5°、溝角度βは60°、分離ゲート9の幅Aは100m
m 、平板1の縦方向の長さLは1200mmとした。分離ゲー
ト9を設けることにより微細粒子の回収部8への粗大粒
子の混入率は大幅に改善された。しかし微細粒子の一部
も分離ゲート9に衝突してしまうため、粗大粒子の回収
部7への微細粒子の混入率が若干多くなっている。
FIG. 9 shows the height H of the gap 10 of the separation gate 9.
6 is a graph showing the relationship between the ratio and the mixing ratio. Where inclination angle α
Is 52.5 °, the groove angle β is 60 °, and the width A of the separation gate 9 is 100 m.
m, and the length L in the vertical direction of the flat plate 1 was 1200 mm. By providing the separation gate 9, the mixing ratio of the coarse particles into the collection part 8 of the fine particles was greatly improved. However, since a part of the fine particles also collides with the separation gate 9, the mixing ratio of the fine particles into the collection part 7 of the coarse particles is slightly increased.

【0019】図10は、投入部6の幅Bと混入率との関
係を示すグラフである。ただし傾斜角αは52.5°、溝角
度βは60°、分離ゲート9の幅Aは100mm 、平板1の縦
方向の長さLは1200mm、隙間10の高さHは2mm とし
た。投入部6の幅Bを適当に選択することにより、粗大
粒子の回収部7への微細粒子の混入率及び微細粒子の回
収部8への粗大粒子の混入率をともに1.7 〜1.8 %の低
レベルに抑えられることが確認された。
FIG. 10 is a graph showing the relationship between the width B of the charging section 6 and the mixing ratio. However, the inclination angle α was 52.5 °, the groove angle β was 60 °, the width A of the separation gate 9 was 100 mm, the longitudinal length L of the flat plate 1 was 1200 mm, and the height H of the gap 10 was 2 mm. By appropriately selecting the width B of the charging section 6, the mixing ratio of fine particles to the collecting section 7 for coarse particles and the mixing rate of coarse particles to the collecting section 8 for fine particles are both low levels of 1.7 to 1.8%. It was confirmed that it could be suppressed.

【0020】[0020]

【発明の効果】以上に説明したように、本発明の粒子の
分級装置は傾斜溝を設けた平板を利用して粗大粒子と微
細粒子との分級ができる。このため、平板を耐熱材料で
構成しておけば、900 〜1000℃の高温の粒子をも連続的
かつ能率的に分級することができる利点がある。
As described above, the particle classification apparatus of the present invention can classify coarse particles and fine particles using a flat plate provided with inclined grooves. Therefore, if the flat plate is made of a heat-resistant material, there is an advantage that particles having a high temperature of 900 to 1000 ° C. can be continuously and efficiently classified.

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

【図1】本発明の分級装置の斜視図である。FIG. 1 is a perspective view of a classification device of the present invention.

【図2】本発明の分級装置の正面図である。FIG. 2 is a front view of the classification device of the present invention.

【図3】本発明の分級装置の側面図である。FIG. 3 is a side view of the classification device of the present invention.

【図4】平板の断面図である。FIG. 4 is a sectional view of a flat plate.

【図5】傾斜角αと混入率との関係を示すグラフであ
る。
FIG. 5 is a graph showing the relationship between the inclination angle α and the mixing ratio.

【図6】溝角度βと混入率との関係を示すグラフであ
る。
FIG. 6 is a graph showing a relationship between a groove angle β and a mixing ratio.

【図7】分離ゲートの幅Aと混入率との関係を示すグラ
フである。
FIG. 7 is a graph showing a relationship between a separation gate width A and a mixing ratio.

【図8】平板の縦方向の長さLと混入率との関係を示す
グラフである。
FIG. 8 is a graph showing the relationship between the length L of the flat plate in the vertical direction and the mixing ratio.

【図9】分離ゲートの隙間の高さHと混入率との関係を
示すグラフである。
FIG. 9 is a graph showing the relationship between the height H of the gap of the separation gate and the mixing ratio.

【図10】投入部の幅Bと混入率との関係を示すグラフ
である。
FIG. 10 is a graph showing the relationship between the width B of the charging section and the mixing ratio.

【符号の説明】[Explanation of symbols]

1 平板、2 傾斜溝、3 凸条、4 薄板、5 スリ
ット、6 粒子の投入部、7 粗大粒子の回収部、8
微細粒子の回収部、9 分離ゲート、10 隙間、11
ガード、α 傾斜角、β 溝角度、A 分離ゲートの
幅、B 投入部の幅、H 分離ゲートの隙間の高さ、L
平板の縦方向の長さ
Reference Signs List 1 flat plate, 2 inclined grooves, 3 ridges, 4 thin plates, 5 slits, 6 particle input section, 7 coarse particle recovery section, 8
Collection unit for fine particles, 9 separation gate, 10 gap, 11
Guard, α inclination angle, β groove angle, A separation gate width, B input part width, H separation gate clearance height, L
Vertical length of flat plate

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 斜め方向に延びる多数の傾斜溝を備えた
平板を水平面から下向きに傾斜させて設置し、その上部
には粒子の投入部を設け、またその下部には投入部の直
下に落下する粗大粒子の回収部と、傾斜溝に沿って落下
する微細粒子の回収部とを設けたことを特徴とする粒子
の分級装置。
1. A flat plate provided with a large number of inclined grooves extending in an oblique direction is installed so as to be inclined downward from a horizontal plane, an input portion for particles is provided at an upper portion thereof, and a drop portion directly below the input portion is provided at a lower portion thereof. A particle classification device, comprising: a collection section for coarse particles to be collected; and a collection section for fine particles falling along an inclined groove.
【請求項2】 粗大粒子の回収部と微細粒子の回収部と
の間に、分離ゲートを設けた請求項1に記載の粒子の分
級装置。
2. The particle classification apparatus according to claim 1, wherein a separation gate is provided between the collection section for the coarse particles and the collection section for the fine particles.
【請求項3】 平板の上面に、平板側に微細粒子の通過
を妨げない隙間を備えたガードを設けた請求項1又は2
に記載の粒子の分級装置。
3. A guard provided on the upper surface of the flat plate with a gap on the side of the flat plate that does not hinder the passage of fine particles.
3. The particle classification device according to 1.).
【請求項4】 水平面に対する平板の傾斜角を、分級す
る粒子の安息角の大きいものの角度よりも12.5〜17.5°
大きい値とした請求項1〜3の何れかに記載の粒子の分
級装置。
4. The angle of inclination of the flat plate with respect to the horizontal plane is 12.5 to 17.5 ° larger than the angle of the particle having a large angle of repose.
The particle classification apparatus according to any one of claims 1 to 3, wherein the apparatus has a large value.
【請求項5】 平板の傾斜溝が水平面に対してなす溝角
度を、分級する粒子の安息角の大きいものの角度よりも
20〜25°大きい値とした請求項1〜4の何れかに記載の
粒子の分級装置。
5. The angle of a groove formed by an inclined groove of a flat plate with respect to a horizontal plane is larger than that of a particle having a large angle of repose of particles to be classified.
The particle classification device according to any one of claims 1 to 4, wherein the value is set to a value larger by 20 to 25 °.
JP7155498A 1998-03-20 1998-03-20 Particle classifier Expired - Fee Related JP2877799B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7155498A JP2877799B1 (en) 1998-03-20 1998-03-20 Particle classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7155498A JP2877799B1 (en) 1998-03-20 1998-03-20 Particle classifier

Publications (2)

Publication Number Publication Date
JP2877799B1 true JP2877799B1 (en) 1999-03-31
JPH11267593A JPH11267593A (en) 1999-10-05

Family

ID=13464076

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7155498A Expired - Fee Related JP2877799B1 (en) 1998-03-20 1998-03-20 Particle classifier

Country Status (1)

Country Link
JP (1) JP2877799B1 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6670822B2 (en) * 2015-02-24 2020-03-25 住友精化株式会社 Water absorbent resin production equipment
KR101791671B1 (en) * 2015-12-31 2017-11-20 주식회사 큐리오시스 Apparatus of Sorting and Aligning Micro-particles, and Method thereof

Also Published As

Publication number Publication date
JPH11267593A (en) 1999-10-05

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