JPS6369529A - Horizontal cylinder type agitating, crushing and drying device - Google Patents

Horizontal cylinder type agitating, crushing and drying device

Info

Publication number
JPS6369529A
JPS6369529A JP61211413A JP21141386A JPS6369529A JP S6369529 A JPS6369529 A JP S6369529A JP 61211413 A JP61211413 A JP 61211413A JP 21141386 A JP21141386 A JP 21141386A JP S6369529 A JPS6369529 A JP S6369529A
Authority
JP
Japan
Prior art keywords
stirring
stirring blade
crushing
horizontal cylindrical
blade
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.)
Granted
Application number
JP61211413A
Other languages
Japanese (ja)
Other versions
JPH0763600B2 (en
Inventor
Sumio Kawai
川合 純夫
Kimihiro Nonaka
公博 野中
Hiroshi Kojima
博 小島
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.)
Okawara Mfg Co Ltd
Original Assignee
Okawara Mfg Co 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 Okawara Mfg Co Ltd filed Critical Okawara Mfg Co Ltd
Priority to JP61211413A priority Critical patent/JPH0763600B2/en
Publication of JPS6369529A publication Critical patent/JPS6369529A/en
Publication of JPH0763600B2 publication Critical patent/JPH0763600B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/75Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with stirrers having planetary motion, i.e. rotating about their own axis and about a sun axis

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crushing And Grinding (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

PURPOSE:To prevent the deterioration of heat conductivity caused by the sticking of a material to a clearance part by restraining the clearance between the top end of heating agitator blades rotatably stretched to the inner wall part of a horizontal cylinder type vessel and inner wall of the vessel within 2mm. CONSTITUTION:The material stuck to the inner wall of the horizontal cylinder type vessel 1 is scraped off by the agitator blades 21 and agitator arms 22, and then mixed and crushed by mixing and crushing blades 18. And the clearances between an inner peripheral wall and the agitator blades 21 and between inner side walls and the agitator arms 22 are restrained in about 0.5-2mm to lessen the amount of the material stuck to the inner peripheral wall and inner side walls to reduce the resistance against heat conduction as small as possible. By constructing in such a way that the number of revolutions of the agitator blades 21 is able to be changed to max. 30r.p.m. according to the state of material, the fluctuation of the resistance against heat conduction in the interval between two scraping actions is negligible.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は真空下で材料を混合、攪拌、破砕、固液抽出、
液の濃縮反応、晶析、乾燥、造粒等の操作を回分式に行
なって取り出す横型円筒攪拌破砕乾燥装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is suitable for mixing, stirring, crushing, solid-liquid extraction, and
This invention relates to a horizontal cylindrical stirring, crushing and drying device that performs operations such as concentration reaction, crystallization, drying, and granulation of liquids in a batch manner.

〔従来技術とその問題点〕[Prior art and its problems]

円筒型攪拌破砕乾燥装置における伝熱効率は円筒内周壁
と攪拌翼先端および横型円筒の側面と摺接する攪拌アー
ム先端とのクリアランスは小さい程向上する。しかし、
製作精度、加熱時の膨張。
The heat transfer efficiency in a cylindrical stirring, crushing, and drying device improves as the clearance between the inner circumferential wall of the cylinder and the tip of the stirring blade and the tip of the stirring arm that makes sliding contact with the side surface of the horizontal cylinder decreases. but,
Manufacturing accuracy, expansion during heating.

材料の攪拌負荷に基づく変形などの問題により、大型装
置では一般に数■■、特に配慮のなされていない装置で
は10+s■以上のクリアランスがあり、その部分に停
滞する材料による伝熱抵抗の増大、その部分の過加熱が
起こることから加熱温度も下げなければならず、従って
渣力的制限も受けていた。
Due to problems such as deformation of the material due to the stirring load, large equipment generally has a clearance of several seconds, and equipment without special consideration has a clearance of 10+ seconds or more, and the material stagnates in that area, which increases heat transfer resistance and Since overheating of the parts occurs, the heating temperature must also be lowered, and therefore there are also pressure limitations.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上記従来のこの種円筒型攪拌破砕乾燥装置にお
ける問題点を解決するため、次のような知見を得た。す
なわちクリアラ〉′スは小さいことは理想的であるが、
実際の製作上及び装置運転上の容易さを考慮し、又材料
と板厚、加工精度と加熱能力、過加熱による部分的材料
損傷などを総合判断して前記攪拌翼、攪拌アームと円筒
容器の内壁とのクリアランスは0.5 mm〜2W會程
度が最も実際的であるという結論に至った。事実、液状
及びさらさらした粉粒状材料では3麿■以下ではほとん
ど前記クリアランス部の材料が伝熱抵抗になる影テは無
視できた。またペースト状材料ではクリアランスが大き
いと伝熱係数の低下が見られたが、これを掻き取り部先
端の角度及び掻き取り翼後部の形状によってはクリアラ
ンス部の材料の剥離がみられ、攪拌質の適正回転数の選
定により、クリアランス1層−であればクリアランス0
の理想状態に比べ、能力低下は約15%に過ぎなかった
In order to solve the problems in the above-mentioned conventional cylindrical stirring crushing drying apparatus, the present invention has obtained the following findings. In other words, although it is ideal that the clearance space is small,
The stirring blade, stirring arm, and cylindrical container are selected by taking into consideration the ease of actual manufacturing and equipment operation, and comprehensively judging the material and plate thickness, processing accuracy and heating capacity, partial material damage due to overheating, etc. It was concluded that the most practical clearance with the inner wall is approximately 0.5 mm to 2W. In fact, for liquid and free-flowing powder and granular materials, the heat transfer resistance of the material in the clearance area can be ignored at temperatures below 300 mm. In addition, with paste-like materials, a decrease in the heat transfer coefficient was observed when the clearance was large, but depending on the angle of the tip of the scraping part and the shape of the rear part of the scraping blade, peeling of the material in the clearance part was observed, resulting in a reduction in the agitating quality. By selecting the appropriate rotation speed, if the clearance is 1 layer - then the clearance will be 0.
Compared to the ideal state, the decline in performance was only about 15%.

以上の知見に基づいて本発明は攪拌翼先端および攪拌ア
ーム先端と横型円筒容器内v4壁とのクリアランスを2
」1以内望ましくは0.5履腸程度とする構成を採用し
、横型円筒容器内内周壁と攪拌質および攪拌アームとク
リアランス部分に付着する材料による伝熱効率の低下の
oT瞳性を著しく減少し1.乾燥装置の使方低下を可及
的に小さく止めることに成功した。
Based on the above findings, the present invention has been developed to increase the clearance between the tip of the stirring blade and the tip of the stirring arm and the V4 wall inside the horizontal cylindrical container by 2.
By adopting a configuration in which the diameter is less than 1, preferably about 0.5, the OT pupil effect, which is caused by the reduction in heat transfer efficiency due to materials adhering to the inner circumferential wall of the horizontal cylindrical container, the stirring material, the stirring arm, and the clearance part, is significantly reduced. 1. We succeeded in keeping the decrease in usage of the drying equipment as small as possible.

〔実施例の説明〕[Explanation of Examples]

以下2本発明装置の実施例について説明する。 Two embodiments of the apparatus of the present invention will be described below.

図面において。In the drawing.

1、横型円筒容器、第1図においてグはその傾斜角であ
る。
1. Horizontal cylindrical container. In Fig. 1, g is its inclination angle.

2:横型円筒容器lの支持軸3の軸受、3:横型円筒容
器lの容器中心軸線2Gに設けられた攪拌軸。
2: Bearing of the support shaft 3 of the horizontal cylindrical container l; 3: A stirring shaft provided on the container center axis 2G of the horizontal cylindrical container l.

4 : [Fff 21 c7)WIA’J21装m、
5:撹拌軸両側部に固定した攪拌アーム22の先端に攪
拌翼21を有し、破砕機6を内側に備えた回転機構。
4: [Fff 21 c7) WIA'J21 m,
5: A rotating mechanism having stirring blades 21 at the tips of stirring arms 22 fixed to both sides of the stirring shaft, and equipped with a crusher 6 inside.

6:破砕機で、破砕機軸15に混合破砕i18を増付け
る。この破砕Ja6は攪拌i21内側で自転して材料の
混合破砕を行なう。
6: In the crusher, add mixed crusher i18 to the crusher shaft 15. This crushing Ja6 rotates inside the stirring i21 to mix and crush the materials.

7:破砕機軸15の軸受で1回転機Jl!!5に取り付
けられる。
7: One rotation machine Jl with crusher shaft 15 bearing! ! It can be attached to 5.

8:破砕機軸15にとりつけられた伝動ブーリ−あるい
はギヤー、 9:伝動プーリーあるいはギヤー8.10の伝動手段、 10:破砕駆動装置12の駆動軸11に取り付けられた
伝動プーリーあるいはギヤー、 ll:前記した通り駆動軸 12:破砕機6の駆動装置 13:JQ拌アーム22内に設けられた空所で伝動プー
リーあるいはギヤー8,10、伝THJ機構9を収容し
、材料の侵入と、潤滑油の漏洩を防ぐため密封されてい
る。
8: Transmission pulley or gear attached to the crusher shaft 15, 9: Transmission pulley or gear 8.10 transmission means, 10: Transmission pulley or gear attached to the drive shaft 11 of the crusher drive device 12, ll: The above Drive shaft 12: Drive device 13 of crusher 6: Transmission pulley or gears 8, 10, and transmission THJ mechanism 9 are accommodated in the space provided in the JQ stirring arm 22 to prevent intrusion of materials and lubricating oil. Sealed to prevent leakage.

14:駆動軸11の軸受 15:前記した通り破砕機軸 16:破砕a6で混合破砕した各種の材料を造粒するた
めの媒剤を供給するための供給路である。しかしこの媒
剤供給は本発明の要旨とは直接関係ない。
14: Bearing of drive shaft 11 15: As described above, crusher shaft 16: Supply path for supplying a medium for granulating various materials mixed and crushed in crushing a6. However, this medium supply is not directly related to the gist of the present invention.

17:同じく媒剤ノズル管のノズル孔 18:破砕翼6の混合破砕質 18a:破砕板 19:媒剤のノズル管 20:横型円筒容器lの中心軸線 21:攪拌翼でその先端は回転方向に向けて僕状をなす
17: Similarly, nozzle hole of the medium nozzle pipe 18: Mixed crushed material 18a of the crushing blade 6: Crushing plate 19: Medium nozzle pipe 20: Central axis of horizontal cylindrical container l 21: Stirring blade whose tip is oriented in the direction of rotation write a servant letter to

21a二中空部 22:攪拌アーム 23:製品排出口 24:ナイフ つぎにその4I成作用について説明する。21a two hollow parts 22: Stirring arm 23: Product discharge port 24: Knife Next, the 4I formation process will be explained.

横型円筒容器l内に回転4I!msが配置される。Rotation 4I in horizontal cylindrical container l! ms is placed.

回転機構5は軸受2により攪拌軸3を中心として同心に
横型円筒容器1内で回転できるように設けられている。
The rotation mechanism 5 is provided so as to be able to rotate concentrically within the horizontal cylindrical container 1 about the stirring shaft 3 by means of a bearing 2.

この回転機構5は枠型形状からなっており、Wl拌gR
21と両側の攪拌アーム22とからなっていう、 (第
6図) 一方破砕橡6が撹拌翼21の内側で回転機構5に支持さ
れながら設けられる。この破砕機6は攪拌翼の回転と共
に公転するが、任意の回転数および回転方向で自転する
ように独自の駆e機構が設けられている。
This rotating mechanism 5 has a frame shape, and has a Wl stirring gR
21 and stirring arms 22 on both sides (FIG. 6). On the other hand, a crushing rod 6 is provided inside the stirring blade 21 and supported by the rotating mechanism 5. This crusher 6 revolves with the rotation of the stirring blades, and is provided with its own drive mechanism so that it can rotate at any rotational speed and direction.

一側の攪拌アーム22の内側には空所13が設けられ、
この中に伝動機構8.9.10が収容されている。
A space 13 is provided inside the stirring arm 22 on one side,
A transmission mechanism 8.9.10 is housed in this.

上記構造の装置において、横型円筒容器1の内周壁およ
び側壁に付着する材料は攪拌翼21及び撹拌アーム22
によって掻き取られ混合破砕質18により混合破砕され
る。しかも内周壁および内側壁と攪拌翼および攪拌アー
ムとのクリアランスは0.5 mm〜2mm程度とし内
周壁および内側壁に付着する材料をなるべく少なくり、
ai力伝熱抵抗とならないようにするのである。また攪
拌翼の回転数は材料の状態に応じて最高3 Or、p、
m、まで−ヒげられるようにしておけば、一度掻き取ら
れてから次にlllき増られる間の付着による伝熱抵抗
は無視少であった。
In the apparatus having the above structure, the material adhering to the inner peripheral wall and side wall of the horizontal cylindrical container 1 is the stirring blade 21 and the stirring arm 22.
The mixed crushed material 18 is used to scrape off and mix and crush the mixed crushed material 18. Moreover, the clearance between the inner peripheral wall and the inner wall and the stirring blade and the stirring arm is set to about 0.5 mm to 2 mm to minimize the amount of material adhering to the inner peripheral wall and the inner wall.
This is to prevent the AI force from becoming a resistance to heat transfer. In addition, the rotation speed of the stirring blade can be up to 3 Or, p,
If the coating was allowed to be scraped down to a depth of 1.5 m, the heat transfer resistance caused by the adhesion between being scraped off and then being thickened was negligible.

また第2図のようにナイフ24を攪拌質21に着脱自在
にとりつけると、模型円筒容器lの内壁に付着した材料
を一層精度よく掻き取ることができるのである。
Furthermore, if the knife 24 is detachably attached to the stirring medium 21 as shown in FIG. 2, the material adhering to the inner wall of the model cylindrical container l can be scraped off with even greater precision.

またこの攪拌翼21にはその中空部21’aに熱媒が流
入する機構になっており、攪拌翼からの伝熱も内周壁か
らの伝熱量の局〜埼を材料に笑えるようになっている。
In addition, the stirring blade 21 has a mechanism in which a heating medium flows into its hollow portion 21'a, so that the heat transfer from the stirring blade can be controlled by taking into account the amount of heat transferred from the inner circumferential wall. There is.

さらに攪拌翼は第5図■のように180°毎に2本設け
るのが一般的とされるが第5図■のように120’毎に
3本撹拌翼をとりつけてもよい。
Further, although it is generally said that two stirring blades are provided every 180° as shown in FIG. 5 (2), three stirring blades may be provided every 120° as shown in FIG.

また第2図に示すように攪拌翼21の先端は抵抗なく材
料を掻き取るように鋭角とし、かきとられた材料は抵抗
なく掘り起されるように内側は飛行機の翼状となってお
り、また周壁側は摩擦抵抗を小ざくすべく回転方向の反
対側にvk退角Oを設ける。1&遺角0は5°かそれ以
上内側に向う構造とするのである。
Furthermore, as shown in Figure 2, the tip of the stirring blade 21 has an acute angle so that it scrapes the material without resistance, and the inside is shaped like an airplane wing so that the scraped material can be dug up without resistance. On the peripheral wall side, a vk retraction angle O is provided on the opposite side of the rotation direction to reduce frictional resistance. The structure is such that angles 1 and 0 point inward by 5 degrees or more.

さらに攪拌アーム22についても横型円筒容器lの側壁
の材料を抵抗なく#4きとるように先端を鋭角とし、攪
拌アーム22の側面は容器lの側壁に対して後退角θ′
だけ回転方向と反対側内側に傾斜している。この後退角
θ′は1〜26が通常である。
Furthermore, the tip of the stirring arm 22 is made at an acute angle so that #4 can be scraped off the side wall material of the horizontal cylindrical container l without resistance, and the side surface of the stirring arm 22 is set at a receding angle θ' with respect to the side wall of the container l.
Only the side opposite to the direction of rotation is tilted inward. This receding angle θ' is usually 1 to 26.

また混合破砕質18は破砕機軸15に直角に取付けられ
る。また必要に応じて薄い破砕板18−aをとりつける
。 (第4図) さらにこの破砕板18aにひねりを4えると。
Further, the mixed crushed material 18 is attached at right angles to the crusher shaft 15. Further, a thin crushing plate 18-a is attached if necessary. (Fig. 4) Furthermore, if we add four twists to this crushing plate 18a.

材料の排出時、材料は排出口23への円滑な流れとなっ
て排出される。このひねりはあたかもスクリューコンベ
アーのスクリューのねじり方向に一致する。
When the material is discharged, the material flows smoothly into the discharge port 23 and is discharged. This twist corresponds to the twisting direction of the screw of a screw conveyor.

〔発明の効果〕〔Effect of the invention〕

攪拌翼21.攪拌アーム22を横型円筒容器lとのクリ
アランスを2i+■以下好ましくは0.5麿園程度とし
たので余り精度を要さないで製作できるにかかわらず、
その割りに伝熱効率は低下しない。
Stirring blade 21. Although the clearance between the stirring arm 22 and the horizontal cylindrical container l is set to 2i+■ or less, preferably about 0.5 mm, it can be manufactured without requiring much precision.
However, the heat transfer efficiency does not decrease.

したがって、全体的に経済的に効率のよい、攪拌破砕乾
f&装aが得られる。
Therefore, an overall economically efficient agitation crushing drying system is obtained.

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

第1図:本発明装置の断面図 第2図:攬袢運21の側面図 tjS3図:攪拌アーム22の平面図 第4図:混合破砕i18の正面図 第5図■■:攪拌児の取付は例を示す。 第6図二回転機構の正面図 1:横型円筒容器 2:軸受 3:攪拌軸 4:駆動?1訝 5:回転機構 6:破砕機 7:破砕機軸 8:伝動プーリーあるいはギヤー 9:伝動手段 10:伝動プーリーあるいはギヤー 11:!I動輪 12:駆動装置 13:空所 14:@1受 15:破砕機軸 16:供給路 17:ノズル孔 18:混合破砕χ 19:ノズル管 20:中心軸線 21:攪拌翼 22:攪拌アーム 23:製品排出口 24ニナ・fフ。 第3図 ■ 第2図 ■         ■ 第5図 第4図 第6図 昭和61年12月1日 Figure 1: Cross-sectional view of the device of the present invention Figure 2: Side view of 攬袢UN 21 tjS3 figure: Plan view of stirring arm 22 Figure 4: Front view of mixed crushing i18 Figure 5 ■■: Installation of the stirring element is shown as an example. Figure 6 Front view of two-rotation mechanism 1: Horizontal cylindrical container 2: Bearing 3: Stirring shaft 4: Drive? 1 doubt 5: Rotation mechanism 6: Crusher 7: Crusher shaft 8: Transmission pulley or gear 9: Transmission means 10: Transmission pulley or gear 11:! I-driving wheel 12: Drive device 13: Blank space 14: @1 Uke 15: Crusher shaft 16: Supply route 17: Nozzle hole 18: Mixed crushing χ 19: Nozzle pipe 20: Central axis line 21: Stirring blade 22: Stirring arm 23: Product discharge port 24 Nina f. Figure 3 ■ Figure 2 ■ ■ Figure 5 Figure 4 Figure 6 December 1, 1986

Claims (13)

【特許請求の範囲】[Claims] (1)取り扱うべき材料を受け入れるための壁加熱式横
型円筒容器と、その中心軸に対して同心に内周壁領域に
据えつけられ、容器の内側壁領域に延びた回転可能の加
熱攪拌翼と、前記容器の軸に対して偏心して回転可能に
据えつけられ、かつ前記攪拌翼と共に回転しながら自由
な回転方向でかつ撹拌翼とは異なる回転数で回転可能で
ある手段からなる混合破砕翼とで構成される円筒型攪拌
混合破砕加熱装置において 撹拌翼先端と、横型円筒容器内周壁とのクリアランスが
2mm以内望ましくは0.5mm程度とすることを特徴
とする横型円筒攪拌破砕乾燥装置。
(1) A wall-heated horizontal cylindrical container for receiving the material to be handled, and a rotatable heating stirring blade installed on the inner circumferential wall area concentrically with respect to the central axis and extending to the inner wall area of the container; A mixing and crushing blade comprising a means that is rotatably installed eccentrically with respect to the axis of the container and is rotatable in a free rotational direction and at a rotation speed different from that of the stirring blade while rotating together with the stirring blade. A horizontal cylindrical stirring, crushing and drying device comprising a cylindrical stirring, mixing, crushing and heating device, characterized in that the clearance between the tip of the stirring blade and the inner circumferential wall of the horizontal cylindrical container is within 2 mm, preferably about 0.5 mm.
(2)攪拌アームと横型円筒容器1の側面とのクリアラ
ンスが2mm以内望ましく0.5mm程度である特許請
求の範囲第1項記載の装置。
(2) The device according to claim 1, wherein the clearance between the stirring arm and the side surface of the horizontal cylindrical container 1 is within 2 mm, preferably about 0.5 mm.
(3)撹拌翼先端およびアームに掻き取りナイフを着脱
可能にした特許請求の範囲第1項、第2項のいづれか1
つに記載の装置。
(3) Any one of Claims 1 and 2, in which a scraping knife is removably attached to the tip of the stirring blade and the arm.
The device described in.
(4)攪拌翼の回転数が30r.p.m.以下で自由に
変更できる特許請求の範囲第1、2、3項のいづれか1
つに記載の装置。
(4) The rotation speed of the stirring blade is 30 r. p. m. Any one of claims 1, 2, and 3 that can be freely changed below.
The device described in.
(5)攪拌翼断面内部は中空になっており、加熱媒体を
通すことができる特許請求の範囲第1、2、3、4、項
のいづれか1つに記載の装置。
(5) The device according to any one of claims 1, 2, 3, and 4, wherein the inside of the stirring blade cross section is hollow and a heating medium can pass therethrough.
(6)攪拌翼は攪拌翼軸に180°毎に2本あるいは1
20°毎に3本放射状に取付けられた特許請求の範囲第
1〜5項のいづれか1つに記載の装置。
(6) There are two stirring blades or one stirring blade every 180° on the stirring blade axis.
6. A device according to any one of claims 1 to 5, which is arranged radially in three pieces at every 20°.
(7)攪拌翼の形状は回転方向先端が鋭くとがりかつ内
側は飛行機の翼状の流線形とした特許請求の範囲第1〜
6項のいづれか1つに記載の装置。
(7) The shape of the stirring blade is such that the tip in the direction of rotation is sharply pointed and the inside is streamlined like an airplane wing.
Apparatus according to any one of Clause 6.
(8)攪拌翼周壁側は第2図に示す如く後退角θを有し
、この角度5°と等しいかこれより大きくした特許請求
の範囲第1ないし7項のいづれか1つに記載の装置。
(8) The device according to any one of claims 1 to 7, wherein the stirring blade peripheral wall side has a receding angle θ as shown in FIG. 2, and this angle is equal to or larger than 5°.
(9)攪拌アームの形状は回転方向先端をするどく、横
型円筒容器1の内側面翼との対向面の回転方向反対側は
内側に傾斜する後退角θ′を有し、この後退角θ′は2
°前後である特許請求の範囲第1〜8項のいづれか1つ
に記載の装置。
(9) The shape of the stirring arm is such that the tip in the rotation direction is sharp, and the side opposite to the rotation direction of the inner surface of the horizontal cylindrical container 1 has a receding angle θ' that is inclined inward. 2
9. The device according to any one of claims 1 to 8, which is approximately .degree.
(10)撹拌翼の内側に設置され、自転する混合破砕機
は撹拌アーム内に内蔵される伝動機構を介して駆動され
る特許請求の範囲第1〜9項のいづれか1つに記載の装
置。
(10) The device according to any one of claims 1 to 9, wherein the rotating mixing and crushing machine is installed inside the stirring blade and is driven via a transmission mechanism built in the stirring arm.
(11)混合破砕機は破砕機軸15に直角に多数の混合
破砕質18を取り付けた特許請求の範囲第1〜10項の
いづれか1つに記載の装置。
(11) The mixing crusher is an apparatus according to any one of claims 1 to 10, wherein a large number of mixed crushed materials 18 are attached perpendicularly to the crusher shaft 15.
(12)混合破砕翼18に破砕板18cを取り付けた特
許請求の範囲第1〜10項のいづれか1つに記載の装置
(12) The device according to any one of claims 1 to 10, wherein a crushing plate 18c is attached to the mixing crushing blade 18.
(13)破砕板18aにひねりを加え内部の材料が破砕
されると同時に排出口方向に搬送するようにした特許請
求の範囲第1〜12項のいづれか1つに記載の装置。
(13) The device according to any one of claims 1 to 12, wherein the crushing plate 18a is twisted so that the material inside is crushed and conveyed toward the discharge port at the same time.
JP61211413A 1986-09-10 1986-09-10 Horizontal cylindrical stirring crushing drying device Expired - Lifetime JPH0763600B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61211413A JPH0763600B2 (en) 1986-09-10 1986-09-10 Horizontal cylindrical stirring crushing drying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61211413A JPH0763600B2 (en) 1986-09-10 1986-09-10 Horizontal cylindrical stirring crushing drying device

Publications (2)

Publication Number Publication Date
JPS6369529A true JPS6369529A (en) 1988-03-29
JPH0763600B2 JPH0763600B2 (en) 1995-07-12

Family

ID=16605544

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61211413A Expired - Lifetime JPH0763600B2 (en) 1986-09-10 1986-09-10 Horizontal cylindrical stirring crushing drying device

Country Status (1)

Country Link
JP (1) JPH0763600B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272139A (en) * 2005-03-29 2006-10-12 Toray Ind Inc Paste stirrer and production method of paste
CN115893413A (en) * 2023-02-13 2023-04-04 北京中欧普瑞科技有限公司 Activated carbon preparation equipment

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61181526A (en) * 1985-02-08 1986-08-14 Sukeyoshi Sano Braying device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61181526A (en) * 1985-02-08 1986-08-14 Sukeyoshi Sano Braying device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272139A (en) * 2005-03-29 2006-10-12 Toray Ind Inc Paste stirrer and production method of paste
CN115893413A (en) * 2023-02-13 2023-04-04 北京中欧普瑞科技有限公司 Activated carbon preparation equipment
CN115893413B (en) * 2023-02-13 2024-02-02 北京中欧普瑞科技有限公司 Activated carbon preparation equipment

Also Published As

Publication number Publication date
JPH0763600B2 (en) 1995-07-12

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