JPS60231887A - Disc shaped diffuser - Google Patents
Disc shaped diffuserInfo
- Publication number
- JPS60231887A JPS60231887A JP8556484A JP8556484A JPS60231887A JP S60231887 A JPS60231887 A JP S60231887A JP 8556484 A JP8556484 A JP 8556484A JP 8556484 A JP8556484 A JP 8556484A JP S60231887 A JPS60231887 A JP S60231887A
- Authority
- JP
- Japan
- Prior art keywords
- bagasse
- fibers
- disk
- rotating
- screws
- 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
Links
Landscapes
- Paper (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は砂糖きびの絞り粕(バガス)からパルプを作る
ときに用いるもので、バガスをこすったり、たたいたり
してビス(Pith)を分離し易くりるためのディスク
型デイビサに関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention is used to make pulp from sugarcane lees (bagasse), and involves separating pith by rubbing or pounding the bagasse. The present invention relates to a disc-type diviser for easy handling.
[従来の技術]
バガスパルプの品質眸、デイビシングの良し悪しで決ま
るといわれており、バガス繊維中に含まれるビスの割り
合いを少なくし且つビス中の繊維の割り合いを少なくす
ることによりバガスパルプの品質を高めることができる
ため、繊維中のビスを少なくし、ビス中の繊維を少なく
してこの割り合いを一定にして一定の品質にすることが
望まれる。[Prior art] It is said that the quality of bagasse pulp is determined by the quality of devising.The quality of bagasse pulp can be improved by reducing the proportion of bis contained in bagasse fibers and the proportion of fibers in bis. Therefore, it is desirable to reduce the amount of screws in the fibers and reduce the amount of fibers in the screws to keep this ratio constant and achieve a constant quality.
そこで、近年、バガスからパルプを作る場合に、バガス
をたたいて繊維をばらばらにし、繊維中のビスを繊維か
ら分離させて除去させるために脱ビス機としてディビサ
の使用が考えられバガスパルプの製造に使用されている
。Therefore, in recent years, when making pulp from bagasse, the use of Divisa as a devising machine has been considered in order to beat the bagasse to break up the fibers and separate and remove the screws in the fibers. It is used.
現存するディビサは、第1図に切断して示すような竪型
のハンマーミル型ディビサが主流を占めている。このハ
ンマーミル型゛ディピサは、ケーシングaの内側に筒形
のスクリーンbを配設し、該スクリーンbの内側に、上
下の軸受C1dに支持されたロータリーシャフトeをス
クリーンbの軸心位置に鉛直に配すと共に、該ロータリ
ーシャフトeの外周に、該外周部にハンマ−ナイフfを
有する円板を多段に配し、ロータリーシャフトeの上端
に設けた■ベルトプーリー〇に図示しない■ベルトを介
して回転動力を伝達することによりロータリーシャフト
eとともにハンマーナイフfが水平方向に回転するよう
にし、スクリーンbの内側ヘパガスを投入してハンマー
ナイフfを回転させることによって回転するハンマーナ
イフfで繊維がたたかれて分散させられると共に該ハン
マーナイフfとスクリーンbの間でバガス同士がこすら
れ(摩擦)で長繊維と短繊維にスクリーンbで分離され
るようにしである。The mainstream of existing divisers is the vertical hammer mill type diviser as shown in FIG. This hammer mill type dipisa has a cylindrical screen b arranged inside a casing a, and a rotary shaft e supported by upper and lower bearings C1d is placed inside the screen b and is vertically aligned with the axis of the screen b. At the same time, on the outer periphery of the rotary shaft e, disks having hammer knives f are arranged in multiple stages, and a belt (not shown) is connected to the By transmitting rotational power, the hammer knife f is rotated horizontally together with the rotary shaft e, and by injecting hepa gas inside the screen b and rotating the hammer knife f, the rotating hammer knife f causes the fibers to become loose. The bagasse is twisted and dispersed, and the bagasse is rubbed (friction) between the hammer knife f and the screen b so that it is separated into long fibers and short fibers by the screen b.
しかし、上記現存のハンマーミル型ディピザでは、ハン
マーナイフfの先端が長時間にわたる連続運転により摩
耗すると、繊維の砕ぎが不充分となり、繊維が長くなっ
て来る。繊維が良好に砕かれなくなると、ll維中のビ
ス含有−が増大して来る。ハンマーミル型ディピザは、
ハンマーナイフfが水平回転しながらバガスをたたき、
こする構造であるから、供給されるバガスの性状の変化
(たとえば、砂糖きび圧搾運転初期と後期でバガス長さ
と幅が変ること)によりアクセプトバガスのビス含有量
が増大し、パルプ品質の低下を起すという問題がある。However, in the existing hammer mill type dipizza, when the tip of the hammer knife f wears out due to continuous operation over a long period of time, the fibers are not crushed sufficiently and the fibers become long. If the fibers are not crushed well, the bis content in the fibers increases. Hammer mill type pizza is
The hammer knife f hits the bagasse while rotating horizontally,
Since it is a rubbing structure, changes in the properties of the supplied bagasse (for example, the length and width of the bagasse change between the early and late stages of sugar cane crushing operation) will increase the bis content of the accepted bagasse, causing a decline in pulp quality. There is a problem.
[発明が解決しようとする問題点]
本発明は、バガスをたたくこと(砕くこと)とこするこ
との両件用を確実に行って繊維に含まれるビスの割り合
いを少なくすると共にビス中の!1維の割り合いも少な
くしてこの割り合いを一定に維持できてバガスパルプ品
質を一定にしようとするものである。[Problems to be Solved by the Invention] The present invention reliably performs both beating (crushing) and rubbing the bagasse, thereby reducing the proportion of screws contained in the fibers, and reducing the proportion of screws contained in the fibers. The purpose is to reduce the proportion of 1 fiber and maintain this proportion constant, thereby making the quality of the bagasse pulp constant.
c問題点を解決するための手段]
本発明のディスク型ディビサは、固定円板と回転円板と
を鉛直方向に相対向させ、これら各円板の各対向面に、
耐摩耗性材料よりなるピラミッド型刃を多数突設させ、
且つ固定円板の刃と回転円板の刃との間に僅かな隙間を
形成させて、固定円板側から両回板間に送り出されるバ
ガスを回転円板の回転により刃によるたたきとこすり、
更にはバガス同士の摩擦力によってバガスrM雑を分散
させてビスを分離排除し易くし、前記の問題点を解決さ
せるようにする。Means for Solving the Problem c] The disc-type diviser of the present invention has a fixed disc and a rotating disc facing each other in the vertical direction, and on each opposing surface of each of these discs,
A large number of protruding pyramid-shaped blades made of wear-resistant material,
In addition, a slight gap is formed between the blade of the fixed disk and the blade of the rotating disk, and the bagasse sent from the fixed disk side between the two rotating disks is beaten and rubbed by the blade by the rotation of the rotating disk,
Furthermore, the bagasse rM miscellaneous particles are dispersed by the frictional force between the bagasse and the screws can be easily separated and removed, thereby solving the above-mentioned problems.
[実 施 例] 以下、本発明の実施例を図面を参照して説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.
実施例1
第2図乃至第4図は本発明の実施例を示すもので、ケー
シング1内に、固定円板2と回転円板3とを横方向から
相対向させて配置し、回転円板3は、ケーシング1を貫
通した回転軸4の一端に固定し、回転軸4の他端を連結
した或いは■ベルトを介したモータ5の駆動により回転
軸4を介して回転円板3が回転するようにし、一方、固
定円板2はバガスを搬送するスクリューコンベヤ6のケ
ーシング1の後方端に固定し、スクリューコンベヤ6で
搬送されるバガスが固定円板2の中心部の開口8を通り
円板2.3間に送出されるようにする。Embodiment 1 FIGS. 2 to 4 show an embodiment of the present invention, in which a fixed disk 2 and a rotating disk 3 are arranged laterally opposite each other in a casing 1, and the rotating disk 3 is fixed to one end of a rotating shaft 4 passing through the casing 1 and connected to the other end of the rotating shaft 4, or (2) the rotating disk 3 is rotated via the rotating shaft 4 by driving a motor 5 via a belt. On the other hand, the fixed disk 2 is fixed to the rear end of the casing 1 of the screw conveyor 6 that conveys the bagasse, and the bagasse conveyed by the screw conveyor 6 passes through the opening 8 in the center of the fixed disk 2 and passes through the disk. 2. Set it to be sent between 3 and 3.
上記固定円板2及び回転円板3の相対向する面には、第
3図及び第4図に示す如く多数のピラミッド型刃、すな
わち、先端が尖っている刃9を対摩耗性材で作って所要
の高さに突設させ、各円板における刃9の対峙間隔を所
定に保持させる。たとえば、刃9の高さを約3〜121
11゜刃9の対峙間隔を約5〜50+u+位とする。As shown in FIGS. 3 and 4, a large number of pyramid-shaped blades, that is, blades 9 with sharp tips, are formed from a wear-resistant material on opposing surfaces of the stationary disk 2 and the rotating disk 3. The blades 9 are made to protrude at a required height, and the spacing between the facing blades 9 on each disc is maintained at a predetermined value. For example, set the height of the blade 9 to about 3 to 121 cm.
The facing interval of the 11° blades 9 is approximately 5 to 50+u+.
上記固定円板2と一体にしたスクリューコンベヤ6のケ
ーシング7には、分配コンベヤ10から落下させられる
バガスを一定量供給できるよう分配コンベヤケーシング
11の下面との間に途中にビンフィーダ12を有するダ
クト13を配し、バガスフィードコンベヤ14により送
られて来たバガスが分配コンベヤ10からダクト13、
ピンフィーダ12を経てスクリューコンベヤ6に移され
、該スクリューコンベヤ6で固定円板2と回転円板3と
の間に供給されることにより、両回板2゜3の相対回転
によってバガス繊維がたたかれたり引き裂かれたりして
ビスが分離させられるようにする。The casing 7 of the screw conveyor 6 integrated with the fixed disk 2 has a duct having a bin feeder 12 in the middle between it and the lower surface of the distribution conveyor casing 11 so as to supply a certain amount of bagasse dropped from the distribution conveyor 10. 13, and the bagasse sent by the bagasse feed conveyor 14 is routed from the distribution conveyor 10 to the duct 13,
The bagasse fibers are transferred to the screw conveyor 6 via the pin feeder 12, and fed between the fixed disc 2 and the rotating disc 3 by the screw conveyor 6, whereby the bagasse fibers are separated by the relative rotation of both discs 2°3. Allow the screws to separate by being knocked or torn.
上記ケーシング1の下端はロータリーフィーダ15を介
して空気輸送管16に連絡し、固定円板2と回転円板3
の間から落下したものを、臼−タリーフィーダ15を経
て空気輸送管16に移すことにより、ブロワ17からの
圧送空気により輸送されて繊維分別室18内へ吹き飛ば
されるようにし1.[記1[分別室18内には、手前側
より長繊維集積部19、生繊維集積部20、ビス集積部
21を順に設置)、空気輸送管16から繊維分別室1B
内へ吹き出される繊維の比重差を利用して分別させるよ
うにし、長繊維集積部19及び生繊維集積部20のそれ
ぞれの下方に脱ビスバガス」ンベヤ22を設け、又、ビ
ス集積部21の下方にビスコンベヤ23を設ける。The lower end of the casing 1 is connected to an air transport pipe 16 via a rotary feeder 15, and has a fixed disk 2 and a rotating disk 3.
By transferring the material that has fallen from between the mill and tally feeder 15 to the air transport pipe 16, it is transported by compressed air from the blower 17 and blown into the fiber separation chamber 18.1. [Note 1 [The long fiber accumulating section 19, raw fiber accumulating section 20, and screw accumulating section 21 are installed in order from the front side in the sorting chamber 18], from the air transport pipe 16 to the fiber sorting chamber 1B.
The difference in specific gravity of the fibers blown into the interior is used to separate the fibers, and a devis bag gas conveyor 22 is provided below each of the long fiber accumulating section 19 and the raw fiber accumulating section 20, and below the bis accumulating section 21. A screw conveyor 23 is provided.
本発明のデイビサは、上記構成としであるので、繊維の
長さや幅の異なるバガスがフィードコンベヤ14により
分配コンベヤ10上に送り込まれると、分配コンベヤ1
0により均一に運ばれてダクト13より落下し、ピンフ
ィーダ12よりスクリューコンベヤ6に移される。スク
リューコンベヤ6上に落下たバガスは、スクリューコン
ベヤ6によりケーシング1内の固定円板2側へ供給され
る。固定円板2の軸心部の孔8から送り出されたバガス
は、モータ5により回転する回転円板3ど上記固定円板
2との間で各円板2.3の刃9によるたたきとこすりゃ
引き裂き作用を受けて繊維がばらばらに分散させられる
。この際、上記相対する両回板2,3間では、刃9の対
峙間隔が所定に定めであるので、バガス同士の摩擦も有
効に行われ、ビスは繊維から分離される。Since the diviser of the present invention has the above-described configuration, when bagasse with different fiber lengths and widths is fed onto the distribution conveyor 10 by the feed conveyor 14, the distribution conveyor 1
0 and falls through the duct 13, and is transferred from the pin feeder 12 to the screw conveyor 6. The bagasse that has fallen onto the screw conveyor 6 is supplied to the fixed disk 2 side inside the casing 1 by the screw conveyor 6. The bagasse sent out from the hole 8 in the axial center of the fixed disk 2 is passed between the rotary disk 3 rotated by the motor 5 and the fixed disk 2 by beating and scraping by the blades 9 of each disk 2.3. The fibers are dispersed as a result of the tearing action. At this time, since the opposing spacing of the blades 9 is set at a predetermined value between the two facing plates 2 and 3, friction between the bagasse is also effectively performed, and the screws are separated from the fibers.
分離されたビスは、バガス繊維とともにケーシング1内
より落下し、ロータリーフィーダ15によって空気輸送
管16内へ落下させられ、該空気輸送管16内をブロワ
11から吐出される空気によって圧送され、繊維分別室
18内に吹き込まれる。このとき繊維の比重差により軽
いものほど遠くへ飛ばされるため、重い長繊維は一番手
前の集積部19に落ち、最も軽いビスは一番遠い集積部
21に落ち、上記の中間の繊維は真中の集積部20に落
ちて自然に分別され、長繊維や生繊維にはビス含有量が
少なく、バガスパルプの品質を低下させることがなくな
る。The separated screws fall from the inside of the casing 1 together with the bagasse fibers, are dropped into the air transport pipe 16 by the rotary feeder 15, are fed under pressure through the air transport pipe 16 by the air discharged from the blower 11, and are separated into fibers. The air is blown into the chamber 18. At this time, due to the difference in the specific gravity of the fibers, the lighter the fibers are, the farther they are blown away, so the heavier long fibers fall to the nearest accumulation section 19, the lightest screws fall to the furthest accumulation section 21, and the above-mentioned intermediate fibers fall to the center. The long fibers and raw fibers fall into the collecting section 20 and are naturally separated, and the long fibers and raw fibers have a low bis content and do not deteriorate the quality of the bagasse pulp.
実施例2
第5図は本発明の他の実施例を示すもので、実施例1に
おける空気輸送管16を通して圧送し比重差によりビス
を分離させる方式に代え、スクリーンによりビスの分離
を行わせる場合を示したもので、篩24に、2段にスク
リーン25’、26を設け、下段のスクリーン26の目
よりも上段のスクリーン25の目の方を大きくし、且つ
全体を傾斜させ、ロータリーフィーダ15を経て落下し
たバガスを、先ず上段のスクリーン25で仕分番ノし、
該上段のスクリーン25の目を通過して落下した繊維を
下段のスクリーン26で仕分けし、該下段のスクリーン
26の目を通過したものをビスとして分離させるように
し、3つに分別された繊維を実施例1の場合と同様にコ
ンベヤ22.23で運び出すようにする。図中第2図と
同一の部分には同一の符号が付しである。Embodiment 2 FIG. 5 shows another embodiment of the present invention, in which the screws are separated by a screen instead of the method in Embodiment 1 in which the screws are separated by pressure feeding through the air transport pipe 16 and the difference in specific gravity is used. The sieve 24 is provided with screens 25' and 26 in two stages, the openings of the upper screen 25 are larger than those of the lower screen 26, and the whole is tilted, and the rotary feeder 15 is The bagasse that has fallen through the filter is first sorted and numbered on the upper screen 25.
The fibers that have passed through the holes of the upper screen 25 are sorted by the lower screen 26, and the fibers that have passed through the holes of the lower screen 26 are separated as screws, and the fibers are separated into three. As in the case of Embodiment 1, it is carried out on conveyors 22 and 23. In the figure, the same parts as in FIG. 2 are given the same reference numerals.
この実施例においても実施例1の場合と同様に良好なデ
ィビシングを行わせることができる。In this embodiment as well, good divising can be performed as in the case of the first embodiment.
[発明の効果]
以上述べた如く、本発明のディスク型ディビサによれば
、固定円板の刃に対し回転円板の刃が変位するので、バ
ガスl1ilfのたたき、こすりの内作用を良好に行う
ことができて繊維中のビスが分離し易い状態になり、繊
維のビス含有量を減少させ得られてバガスパルプ品質を
一定に維持させることができる。[Effects of the Invention] As described above, according to the disc-type diviser of the present invention, the blades of the rotating disc are displaced relative to the blades of the fixed disc, so that the internal action of pounding and scraping the bagasse l1ilf can be performed well. As a result, the bis in the fiber becomes easy to separate, the bis content of the fiber can be reduced, and the quality of the bagasse pulp can be maintained constant.
第1図は従来のディビサの切断斜視図、第2図は本発明
の一実施例を示す概略図、第3図は本発明の1イビサの
拡大図、第4図は第3図の■v矢視図、第5図は本発明
の他の実施例を示す概略図である。
1はケーシング、2は固定円板、3は回転円板、5はモ
ータ、6はスクリューコンベヤ、15はロータリーフィ
ーダ、18は繊維分別室、24は篩、25.26はスク
リーンを示す。Fig. 1 is a cutaway perspective view of a conventional Divisa, Fig. 2 is a schematic diagram showing an embodiment of the present invention, Fig. 3 is an enlarged view of one Ibiza of the present invention, and Fig. 4 is the ■v of Fig. 3. The arrow view and FIG. 5 are schematic diagrams showing another embodiment of the present invention. 1 is a casing, 2 is a fixed disk, 3 is a rotating disk, 5 is a motor, 6 is a screw conveyor, 15 is a rotary feeder, 18 is a fiber separation chamber, 24 is a sieve, and 25 and 26 are screens.
Claims (1)
転円板を相対向させ、上記固定円板と回転円板の各対向
面に、先端が尖った刃を多数突設し、且つ上記固定円板
の刃と回転円板の刃との間に僅かな隙間を保持させるよ
う固定円板と回転円板の間隔を定めたことを特徴とする
ディスク型デイピサ。1) A rotating disk rotated by a motor is opposed to a fixed disk, and a number of blades with sharp tips protrude from each opposing surface of the fixed disk and the rotating disk, and A disk-type dipisa characterized in that the distance between the fixed disk and the rotating disk is determined so as to maintain a small gap between the blade of the plate and the blade of the rotating disk.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8556484A JPS60231887A (en) | 1984-04-27 | 1984-04-27 | Disc shaped diffuser |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8556484A JPS60231887A (en) | 1984-04-27 | 1984-04-27 | Disc shaped diffuser |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60231887A true JPS60231887A (en) | 1985-11-18 |
Family
ID=13862304
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8556484A Pending JPS60231887A (en) | 1984-04-27 | 1984-04-27 | Disc shaped diffuser |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60231887A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008141464A1 (en) | 2007-05-23 | 2008-11-27 | Alberta Research Council Inc. | Decortication process |
-
1984
- 1984-04-27 JP JP8556484A patent/JPS60231887A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008141464A1 (en) | 2007-05-23 | 2008-11-27 | Alberta Research Council Inc. | Decortication process |
EP2152945A4 (en) * | 2007-05-23 | 2014-09-24 | Alberta Innovates Technology Futures | Decortication process |
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