JP3318682B2 - Granulator - Google Patents

Granulator

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Publication number
JP3318682B2
JP3318682B2 JP12847293A JP12847293A JP3318682B2 JP 3318682 B2 JP3318682 B2 JP 3318682B2 JP 12847293 A JP12847293 A JP 12847293A JP 12847293 A JP12847293 A JP 12847293A JP 3318682 B2 JP3318682 B2 JP 3318682B2
Authority
JP
Japan
Prior art keywords
rotary
discharge port
drum
rotary drum
rotating
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
JP12847293A
Other languages
Japanese (ja)
Other versions
JPH06315619A (en
Inventor
俊典 杉橋
孝治 三宅
Original Assignee
光洋機械産業株式会社
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 光洋機械産業株式会社 filed Critical 光洋機械産業株式会社
Priority to JP12847293A priority Critical patent/JP3318682B2/en
Publication of JPH06315619A publication Critical patent/JPH06315619A/en
Application granted granted Critical
Publication of JP3318682B2 publication Critical patent/JP3318682B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】この発明は、主として焼却灰、土
砂、鋳造廃砂などの粉粒物を所要の粒径に造粒せしめる
装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for granulating powdery particles such as incinerated ash, earth and sand, and foundry sand to a required particle size.

【0002】[0002]

【従来の技術】一般に、この種の造粒装置は、水平また
は排出口側を下向きに若干傾斜せしめた円筒状回転ドラ
ムを回転させ、回転ドラムの一端より粉粒物原料を供給
すると共に、適宜水や各種エマルジョンなどの結合剤や
パウダ−を加え、回転ドラムの回転に伴う粉粒体の転動
によって凝集・造粒を行わしめるものである。そして、
かかる原料粉粒体の転動は、回転ドラム内面と粉粒体と
の間の摩擦力により、回転ドラムの回転に伴う円弧状上
昇運動と、重力による下降によって生じるものである。
このため、原料粉粒体と回転ドラム内面との相対的摩擦
抵抗が小さい場合、例えば、回転ドラム内面を平滑状に
形成せしめた場合には、回転ドラムの摩擦による粉粒体
持ち上げ力が不足して比較的低い位置までしか上昇せ
ず、しかも、滑りを生じて転動が不十分となりやすいの
みならず、回転ドラム内周面に付着成長しやすく、確実
なる造粒化は期待しえないものであった。
2. Description of the Related Art Generally, a granulating apparatus of this kind rotates a cylindrical rotary drum whose horizontal or discharge port side is slightly inclined downward, feeds powdery material from one end of the rotary drum, and appropriately controls the rotation. Binders and powders such as water and various emulsions are added, and agglomeration and granulation are performed by the rolling of the powder and granules accompanying the rotation of the rotating drum. And
The rolling of the raw material particles is caused by an ascending movement caused by the rotation of the rotating drum and a descent by gravity due to a frictional force between the inner surface of the rotating drum and the granular material.
For this reason, when the relative frictional resistance between the raw material powder and the inner surface of the rotating drum is small, for example, when the inner surface of the rotating drum is formed to be smooth, the lifting force of the powder due to the friction of the rotating drum is insufficient. Not only does it rise only to a relatively low position, but it also tends to cause slippage and insufficient rolling, and also tends to adhere and grow on the inner peripheral surface of the rotating drum, so that reliable granulation cannot be expected. Met.

【0003】かかる従来の問題点を解決するものとし
て、回転ドラム内にスクレ−パを取付けた造粒装置が提
案されている。かかる造粒装置は、原料の粉粒体を回転
ドラム内面に沿って掻き上げ、その転動を確実に行わし
めることが出来る反面、摩擦抵抗が大きくて回転ドラム
の駆動動力が大となりやすいのみならず、造粒中にスク
レ−パから凝集・造粒化しつつある粉粒体が落下し、安
定造粒に悪影響を及ぼすものとなっていた。
In order to solve such a conventional problem, there has been proposed a granulating apparatus in which a scraper is mounted in a rotating drum. Such a granulating device can scrape up the powdery material of the raw material along the inner surface of the rotating drum and surely perform the rolling, but on the other hand, if the frictional resistance is large and the driving power of the rotating drum is likely to be large, However, during granulation, the agglomerates and granules falling from the scraper fell, which had an adverse effect on stable granulation.

【0004】[0004]

【発明が解決しようとする課題】この発明は、従来の問
題点を一挙に解決しようとするもので、原料の粉粒体と
回転ドラム内面との摩擦力のみならず、往復作動自在な
回転スクレ−パの掻き上げ作用により粉粒体間の摩擦力
を有効に利用して転動運動を行わしめ、所望の粒径に均
一に、しかも確実に造粒せしめることが出来る造粒装置
を提供するにある。
SUMMARY OF THE INVENTION The present invention is intended to solve the conventional problems at a glance, and not only the frictional force between the raw material powder and the inner surface of the rotary drum, but also a reciprocally operable rotary screen. -To provide a granulating device capable of performing rolling motion by effectively utilizing the frictional force between powder and granules by the scraping action of the powder and uniformly and surely granulating to a desired particle size. It is in.

【0005】[0005]

【課題が解決するための手段】即ち、この発明は、回転
ドラム2a・2b・2cの基端部に原料供給フィ−ダ−
9、同他端部に排出口4が各々形成されると共に、回転
ドラム2a・2b・2c内には該排出口4を介して液体
噴出パイプ12・パウダ−供給フィ−ダ−13及び往復
作動自在な回転スクレ−パ15が各々挿着され、かつ、
回転ドラム2a・2b・2cはその排出口4側を上向き
に傾斜支持せしめるべく基端側に傾斜角度調整自在な昇
降手段5が設けられた構成よりなる。
That is, according to the present invention, a material supply feeder is provided at the base end of the rotary drums 2a, 2b and 2c.
9. A discharge port 4 is formed at the other end, and a liquid ejection pipe 12, a powder-supply feeder 13, and a reciprocating operation are provided in the rotary drums 2a, 2b, and 2c via the discharge port 4. A free rotating scraper 15 is inserted into each, and
The rotary drums 2a, 2b, 2c are configured such that a lifting / lowering means 5 capable of adjusting the tilt angle is provided on the base end side so as to tilt and support the discharge port 4 upward.

【0006】[0006]

【作用】昇降手段5により回転ドラム2a・2b・2c
の傾斜を適正に調整したのち、回転ドラム2a・2b・
2cを回転作動せしめると共に、回転スクレ−パ15を
回転・往復作動せしめ、回転ドラム2a・2b・2c内
に供給フィ−ダ−9を介して所要の原料粉粒体Aを供給
すると共に、液体噴出パイプ12及び供給フィ−ダ−1
3を介して水や各種エマルジョンなどの結合剤Bと所要
のパウダ−Cを供給する。そして、回転ドラム2a・2
b・2cの傾斜化により、原料の粉粒体Aを滞留せしめ
つつ回転ドラム内面との摩擦力、及び粉粒体間の摩擦力
を利用し、回転スクレ−パ15の回転・往復作動とも相
まって転動運動を確実に行わしめ、所望の粒径に均一
に、しかも確実に造粒せしめることが出来る。
The rotary drums 2a, 2b, 2c are moved by the lifting means 5.
Of the rotating drums 2a, 2b,
2c, the rotating scraper 15 is rotated and reciprocated, and the required raw material particles A are supplied into the rotating drums 2a, 2b, 2c via the supply feeder 9, and the liquid Ejection pipe 12 and supply feeder-1
3, a binder B such as water or various emulsions and a required powder C are supplied. And the rotating drums 2a and 2
The inclination of b · 2c makes use of the frictional force with the inner surface of the rotating drum and the frictional force between the particles while retaining the powdery material A of the raw material, and the rotation and reciprocating operation of the rotary scraper 15 are combined. The rolling motion can be surely performed, and the desired particle size can be uniformly and reliably granulated.

【0007】[0007]

【実施例】以下に、この発明を図面に示す一実施例につ
いて説明する。1は細長な方形体状のフレ−ム、2aは
該フレ−ム1上に傾動架台3を介して傾斜状に配設され
た円筒状の回転ドラムで、該回転ドラム2aはその一端
部に形成された排出口4側を高くして上向きに設定する
ものとされている。5は上記回転ドラム2aを調整自在
に傾斜支持せしめるべく傾動架台3に装着された両側一
対の油圧シリンダ、6は歯車機構7を介して回転ドラム
2aを回転作動せしめるべくその基端側に配設されたモ
−タ、8は回転ドラム2aのほぼ中位に配設された両側
一対の支持ロ−ラ、9は回転ドラム2aの基端部に固着
された閉塞蓋体10を挿通して配設された原料粉粒体A
の供給フィ−ダ−、11は該供給フィ−ダ−9を作動せ
しめるモ−タ、12・13は回転ドラム2aの排出口4
を介して回転ドラム2内に挿着された長尺状の結合剤B
用液体噴出パイプと短尺状のパウダ−C用供給フィ−ダ
−、14は該供給フィ−ダ−13を作動せしめるモ−
タ、15は回転ドラム2aの中心線に沿って回転自在に
配設された回転スクレ−パで、該回転スクレ−パ15は
その長手方向に往復作動自在とされている。その他、D
は生成粒子を示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. Reference numeral 1 denotes an elongated rectangular frame, and 2a denotes a cylindrical rotary drum which is disposed on the frame 1 via a tilting base 3 in an inclined manner. The rotary drum 2a is provided at one end thereof. The formed discharge port 4 side is set high and set upward. Reference numeral 5 denotes a pair of hydraulic cylinders mounted on the tilting gantry 3 for tiltably supporting the rotary drum 2a in an adjustable manner. Reference numeral 6 denotes a hydraulic cylinder provided at a base end thereof for rotating the rotary drum 2a via a gear mechanism 7. The motor 8 is a pair of support rollers disposed on the both sides of the rotary drum 2a at a substantially middle position, and the motor 9 is provided by inserting a closing lid 10 fixed to the base end of the rotary drum 2a. Raw material powder A provided
Are feed motors 11 for operating the feed feeder 9, and 12 and 13 are discharge ports 4 of the rotary drum 2a.
Binder B inserted into the rotary drum 2 through the
The liquid ejecting pipe and the short feeder for powder C are provided with a motor for operating the feeder 13.
The rotary scraper 15 is rotatably disposed along the center line of the rotary drum 2a, and the rotary scraper 15 is reciprocally movable in its longitudinal direction. Other, D
Indicates product particles.

【0008】次に、上述の如く構成された実施例による
焼却灰Aの造粒作動について説明する。まず、油圧シリ
ンダ5を適宜昇降作動せしめて回転ドラム2aの傾斜角
度を適正に調整したのち、モ−タ6を起動せしめ、回転
ドラム2aを回転せしめると共に、回転スクレ−パ15
を回転作動せしめつつ往復作動せしめる。そして、供給
フィダ−9より焼却灰Aを、また、液体噴出パイプ12
より水などの結合剤Bを回転ドラム2a内に供給すると
共に、必要に応じて供給フィ−ダ−13より所要のパウ
ダ−Cを供給する。供給された焼却灰Aは、回転スクレ
−パ15により掻き上げられながら結合剤Bにより加湿
されつつ回転ドラム2aの回転作動によりその基端側よ
り排出口4側に向けて転動し、次第に凝集・造粒化せし
められる。このさい、傾斜する回転ドラム2aの排出口
4側が高く設定、即ち、加湿焼却灰Aの転動が昇り勾配
となるため、原料の焼却灰Aを滞留せしめつつ回転ドラ
ム内面との摩擦力、及び焼却灰A間の摩擦力により転動
運動を確実に行わしめることが出来、回転スクレ−パ1
5の回転・往復作動とも相まって造粒効果を一層増大せ
しめうる。
Next, the granulating operation of the incinerated ash A according to the embodiment configured as described above will be described. First, the hydraulic cylinder 5 is moved up and down as appropriate to properly adjust the inclination angle of the rotary drum 2a. Then, the motor 6 is started to rotate the rotary drum 2a, and the rotary scraper 15 is rotated.
Is operated reciprocally while rotating. Then, the incineration ash A is supplied from the supply feeder 9 and the liquid ejection pipe 12
A binder B such as water is supplied into the rotary drum 2a, and a required powder C is supplied from a supply feeder 13 as needed. The supplied incineration ash A rolls from its base end toward the discharge port 4 side by the rotation of the rotary drum 2a while being humidified by the binder B while being scraped up by the rotary scraper 15, and gradually aggregates.・ It is granulated. At this time, the discharge port 4 side of the inclined rotary drum 2a is set high, that is, since the rolling of the humidified incineration ash A has an ascending gradient, the frictional force with the inner surface of the rotating drum while retaining the incineration ash A of the raw material, and The rolling motion can be reliably performed by the frictional force between the incineration ash A, and the rotary scraper 1
The granulation effect can be further increased in combination with the rotation / reciprocation operation of No. 5.

【0009】凝集・造粒化して生成された粒子Dは、焼
却灰Aの継続的な供給により次第に排出口4方向に押圧
されてせり上がりつつ更に転動する。このさい、生成粒
子Dの水分量が多い場合には、供給フィ−ダ−13より
所要のパウダ−Cを回転ドラム2a内に供給し、粒子D
にまぶすことにより水分調整を行うと良い。水分調整の
完了した粒子Dは、排出口4を通って外方へ排出され
る。以下、同様にして焼却灰Aを連続的に造粒せしめ
る。
The particles D produced by the agglomeration / granulation are further pressed and gradually rolled in the direction of the discharge port 4 by the continuous supply of the incineration ash A, and further roll. At this time, when the water content of the produced particles D is large, the required powder C is supplied from the supply feeder 13 into the rotating drum 2a, and the particles D are supplied.
It is good to adjust the water content by dusting. The particles D whose water content has been adjusted are discharged outward through the discharge port 4. Hereinafter, incineration ash A is continuously granulated in the same manner.

【0010】なお、上記実施例は焼却灰Aへの適用例を
示したが、これに限定されるものでなく、土砂や鋳造廃
砂などの粒状物の造粒にも適用することが出来る。ま
た、回転ドラム2aの形状は円筒状とされているが、図
4に示す略鼓形状の回転ドラム2b、あるいは、図5に
示す略太鼓形状の回転ドラム2cなど所要の形状に形成
せしめても良く、また、回転ドラム2aは油圧シリンダ
5により傾斜支持するものとされているが、エアシリン
ダ等、他の公知の昇降手段を採用してもよいものであ
る。さらに、粉粒体Aの造粒効果をよりアップせしめる
ため、昇降手段を小ストロ−クでもって連続的に昇降作
動せしめ、回転ドラム2a・2b・2cを揺動せしめつ
つ回転作動せしめるようにしてもよく、また、場合によ
っては公知の揺動機構を付設せしめてよいものである。
Although the above-described embodiment shows an example of application to incineration ash A, the present invention is not limited to this and can also be applied to granulation of granular materials such as earth and sand and casting waste sand. Further, although the shape of the rotary drum 2a is cylindrical, the rotary drum 2a may be formed into a required shape such as the substantially drum-shaped rotary drum 2b shown in FIG. 4 or the substantially drum-shaped rotary drum 2c shown in FIG. Although the rotary drum 2a is inclined and supported by the hydraulic cylinder 5, other known lifting means such as an air cylinder may be employed. Further, in order to further enhance the granulation effect of the powder A, the lifting means is continuously moved up and down with a small stroke, and the rotating drums 2a, 2b and 2c are rotated while being rocked. Alternatively, a known swing mechanism may be additionally provided in some cases.

【0011】[0011]

【発明の効果】この発明によれば以上の次第で、回転ド
ラム2a・2b・2cの基端部に原料供給フィ−ダ−
9、同他端部に排出口4が各々形成されると共に、回転
ドラム2a・2b・2c内には該排出口4を介して液体
噴出パイプ12・パウダ−供給フィ−ダ−13及び往復
作動自在な回転スクレ−パ15が各々挿着され、かつ、
回転ドラム2a・2b・2cはその排出口4側を上向き
に傾斜支持せしめるべく基端側に傾斜角度調整自在な昇
降手段5が設けられているから、昇降手段5により回転
ドラム2a・2b・2cを適正に傾斜支持せしめつつ回
転作動せしめると共に、回転スクレ−パ15を回転・往
復作動せしめつつ、回転ドラム2a・2b・2c内に供
給フィ−ダ−9を介して所要の原料粉粒体Aを供給する
とともに、液体噴出パイプ12及び供給フィ−ダ−13
を介して水などの結合剤Bと所要のパウダ−Cを供給
し、原料の粉粒体Aを滞留せしめつつ回転ドラム内面と
の摩擦力、及び粉粒体間の摩擦力を利用し、回転スクレ
−パ15の回転・往復作動とも相まって転動運動を確実
に行わしめ、所望の粒径に均一に、しかも確実に造粒せ
しめることが出来るものである。
According to the present invention, as described above, the raw material supply feeder is provided at the base end of the rotary drums 2a, 2b, 2c.
9. A discharge port 4 is formed at the other end, and a liquid ejection pipe 12, a powder-supply feeder 13, and a reciprocating operation are provided in the rotary drums 2a, 2b, and 2c via the discharge port 4. A free rotating scraper 15 is inserted into each, and
The rotary drums 2a, 2b, and 2c are provided with lift means 5 capable of adjusting the tilt angle on the base end side so as to tilt and support the discharge port 4 side upward. The rotation of the rotary scraper 15 while rotating and reciprocating the rotary scraper 15 while properly tilting and supporting the raw material particles A in the rotary drums 2a, 2b and 2c via the supply feeder 9 is performed. And the liquid ejection pipe 12 and the supply feeder 13
A binder B such as water and a required powder C are supplied through the hopper, and the frictional force with the inner surface of the rotating drum and the frictional force between the powdery particles are utilized while retaining the powdery material A as a raw material. The rolling motion is surely performed in combination with the rotation and reciprocating operation of the scraper 15, so that the granules can be uniformly and reliably granulated to a desired particle size.

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

【図1】この発明の一実施例を示す縦断面図である。FIG. 1 is a longitudinal sectional view showing one embodiment of the present invention.

【図2】同左側面図である。FIG. 2 is a left side view of the same.

【図3】図1のl−l線に沿う断面図である。FIG. 3 is a cross-sectional view taken along line 1-1 of FIG. 1;

【図4】回転ドラムbを示す半截断面図である。FIG. 4 is a half sectional view showing a rotary drum b.

【図5】回転ドラムcを示す半截断面図である。FIG. 5 is a half sectional view showing a rotary drum c.

【符号の説明】[Explanation of symbols]

2a・2b・2c 回転ドラム 5 油圧シリンダ 9 供給フィ−ダ− 12 液体噴出パイプ 13 供給フィ−ダ− 14 回転スクレ−パ 2a, 2b, 2c Rotary drum 5 Hydraulic cylinder 9 Supply feeder 12 Liquid ejection pipe 13 Supply feeder 14 Rotary scraper

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭53−43975(JP,A) 特開 昭59−222218(JP,A) 特開 昭58−189028(JP,A) 実公 昭38−620(JP,Y1) (58)調査した分野(Int.Cl.7,DB名) B01J 2/12 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-53-43975 (JP, A) JP-A-59-222218 (JP, A) JP-A-58-1889028 (JP, A) 620 (JP, Y1) (58) Field surveyed (Int. Cl. 7 , DB name) B01J 2/12

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 回転ドラム2a・2b・2cの基端部に
原料供給フィ−ダ−9、同他端部に排出口4が各々形成
されると共に、回転ドラム2a・2b・2c内には該排
出口4を介して液体噴出パイプ12・パウダ−供給フィ
−ダ−13及び往復作動自在な回転スクレ−パ15が各
々挿着され、かつ、回転ドラム2a・2b・2cはその
排出口4側を上向きに傾斜支持せしめるべく基端側に傾
斜角度調整自在な昇降手段5が設けられてなることを特
徴とする造粒装置。
1. A raw material supply feeder 9 is formed at a base end of the rotating drums 2a, 2b and 2c, and a discharge port 4 is formed at the other end of the rotating drums 2a, 2b and 2c. A liquid ejection pipe 12, a powder supply feeder 13, and a reciprocally movable rotary scraper 15 are respectively inserted through the discharge port 4, and the rotary drums 2a, 2b, 2c are connected to the discharge port 4. A granulating apparatus characterized in that an elevation means 5 capable of adjusting the inclination angle is provided on the base end side so that the side can be inclined upwardly.
JP12847293A 1993-05-04 1993-05-04 Granulator Expired - Fee Related JP3318682B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12847293A JP3318682B2 (en) 1993-05-04 1993-05-04 Granulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12847293A JP3318682B2 (en) 1993-05-04 1993-05-04 Granulator

Publications (2)

Publication Number Publication Date
JPH06315619A JPH06315619A (en) 1994-11-15
JP3318682B2 true JP3318682B2 (en) 2002-08-26

Family

ID=14985580

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12847293A Expired - Fee Related JP3318682B2 (en) 1993-05-04 1993-05-04 Granulator

Country Status (1)

Country Link
JP (1) JP3318682B2 (en)

Cited By (1)

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Publication number Priority date Publication date Assignee Title
CN103143294A (en) * 2013-03-14 2013-06-12 南通贝特医药机械有限公司 Novel granulating and material transferring machine

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JP2006167715A (en) * 2004-11-18 2006-06-29 Kitagawa Iron Works Co Ltd Apparatus and method for granulating material
JP5165943B2 (en) * 2007-07-09 2013-03-21 大同特殊鋼株式会社 Granulated product sizing equipment for metal-containing by-products

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103143294A (en) * 2013-03-14 2013-06-12 南通贝特医药机械有限公司 Novel granulating and material transferring machine

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