JPS6311588Y2 - - Google Patents

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Publication number
JPS6311588Y2
JPS6311588Y2 JP13796183U JP13796183U JPS6311588Y2 JP S6311588 Y2 JPS6311588 Y2 JP S6311588Y2 JP 13796183 U JP13796183 U JP 13796183U JP 13796183 U JP13796183 U JP 13796183U JP S6311588 Y2 JPS6311588 Y2 JP S6311588Y2
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JP
Japan
Prior art keywords
blades
drying
horizontal
vertical
stirring
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
Application number
JP13796183U
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Japanese (ja)
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JPS6043991U (en
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Priority to JP13796183U priority Critical patent/JPS6043991U/en
Publication of JPS6043991U publication Critical patent/JPS6043991U/en
Application granted granted Critical
Publication of JPS6311588Y2 publication Critical patent/JPS6311588Y2/ja
Granted legal-status Critical Current

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Description

【考案の詳細な説明】 この考案は、合成樹脂チツプや、その他の粉粒
体などの材料を乾燥するために使用する乾燥装置
に関する。
[Detailed Description of the Invention] This invention relates to a drying device used for drying materials such as synthetic resin chips and other powder and granular materials.

ポリエステル樹脂を一例にすれば、このポリエ
ステルの製造プロセス及び成形プロセスにおい
て、重合したチツプは水分を含んでいるため乾燥
しなければならない。しかし、このチツプは非結
晶状態であるから、そのまま加熱しても、該チツ
プは融着し団子状になつて固つてしまい取り扱え
なくなる。逆に、該チツプを乾燥せずに成形する
と、含有水分が加水分解し物性が極度に低下して
しまう。
Taking polyester resin as an example, during the manufacturing and molding processes of polyester, polymerized chips must be dried because they contain water. However, since these chips are in a non-crystalline state, even if they are heated as they are, the chips will fuse and become lump-like and solid, making them impossible to handle. On the other hand, if the chips are molded without drying, the water content will be hydrolyzed and the physical properties will be extremely deteriorated.

従つて、このポリエステル樹脂の製造ないし成
形プロセスでは、ポリエステルチツプを融着しな
いように加熱して、一定レベル以上の結晶化度を
もたせると共に、含有水分を除去させる乾燥を行
わねばならない。
Therefore, in the manufacturing or molding process of this polyester resin, it is necessary to heat the polyester chips so as not to fuse them, to give them a certain level of crystallinity or higher, and to dry them to remove the moisture content.

従来、原料メーカーにおいては、大容量の真空
式ロータリードライヤーを使用して、前記結晶化
と乾燥操作をバツチ方式で行つていた。しかる
に、これによれば、バツチ処理時間が長く、ロス
時間が大きかつた。また、大きな設備と動力源な
どのエネルギー消費を必要とした。一方、原料メ
ーカー側だけでなく、原料加工者側でも、原料は
結晶化されたものに限られ不便であつた。
Conventionally, raw material manufacturers have performed the crystallization and drying operations in batches using large-capacity vacuum rotary dryers. However, according to this method, the batch processing time was long and the loss time was large. It also required energy consumption such as large equipment and power sources. On the other hand, raw materials are limited to crystallized ones, which is inconvenient not only for raw material manufacturers but also for raw material processors.

この考案は、撹拌羽根を内装した乾燥容器内に
加熱手段よりの熱を送風機により送風して材料を
撹拌する乾燥装置において、前記撹拌羽根は回転
軸線に対して略平行な縦羽根と略垂直な横羽根と
の多数個の組合せからなると共に、これら撹拌羽
根の適数個には材料が当る面を水平方向または垂
直方向に対し角度をもつ傾斜面とし、さらに前記
横羽根の傾斜面は材料を上昇方向に掬い上げて撹
拌し、縦羽根の傾斜面は回転軸線方向に集合させ
て撹拌すべく配設することによつて、上記不都合
や不便を解消するだけでなく、乾燥すべき材料の
付着や変形をなくし、物性に対応できるものを提
供するにある。
This invention is based on a drying device that stirs the material by blowing heat from a heating means into a drying container equipped with stirring blades using a blower. It consists of a large number of combinations with horizontal blades, and a suitable number of these stirring blades have surfaces that the material comes into contact with are sloped surfaces that are at an angle with respect to the horizontal or vertical direction, and furthermore, the sloped surfaces of the horizontal blades are such that the material is By scooping up and stirring in the upward direction, and arranging the vertical blades so that the inclined surfaces gather in the direction of the axis of rotation for stirring, the above-mentioned inconveniences and inconveniences are not only eliminated, but also the material to be dried is prevented from adhering to the material. The objective is to provide a product that eliminates deformation and deformation and can respond to physical properties.

この考案の一実施例を第1図乃至第6図に基づ
いて以下に説明する。
An embodiment of this invention will be described below based on FIGS. 1 to 6.

1はポリエステルチツプ等の材料を結晶化する
と共に乾燥したり、或いはその他の材料を乾燥だ
けする乾燥容器であつて、基台2上に固定した下
部容器1aと、この下部容器1a上に立設した上
部容器1bとからなり、上部容器1bの円周近く
の上面には上部に材料投入口3aを形成した材料
供給ホツパー3が立設してある。この材料供給ホ
ツパー3として、この実施例ではサイクロンを設
けているが、これに限定されるものではない。3
bは排気筒である。
1 is a drying container for crystallizing and drying materials such as polyester chips, or simply drying other materials, and includes a lower container 1a fixed on a base 2, and a lower container 1a erected on top of this lower container 1a. A material supply hopper 3 having a material input port 3a formed in the upper part thereof is erected on the upper surface near the circumference of the upper container 1b. Although a cyclone is provided as the material supply hopper 3 in this embodiment, it is not limited to this. 3
b is an exhaust stack.

4は蒸気ヒータ5と電気ヒータ6とからなる加
熱手段であつて、これで発生させた熱は、その前
部に接続した送風機7により熱風管8を介して下
部容器1a側部より送り込むようにしてある。下
部容器1a内には前記熱風を分散するために漏斗
状の多孔板9が配設してある。
4 is a heating means consisting of a steam heater 5 and an electric heater 6, and the heat generated by this is sent from the side of the lower container 1a through a hot air pipe 8 by a blower 7 connected to the front part thereof. There is. A funnel-shaped perforated plate 9 is provided in the lower container 1a to disperse the hot air.

前記上部容器1bの上面の一部には排気管10
が設けてあり、この排気管10の先端は集塵装置
(この実施例ではバツクフイルター)11に接続
されている。集塵装置11の上部には連通管12
を介してダクト13が左方向から右方向に向け横
設され、該ダクト13の先端は、風量調整弁1
4、短管15、サクシヨンフイルター16を介し
て前記送風機7の吸気口と接続してある。17は
送風機7の駆動モータである。従つて、加熱手段
4よりの熱は、送風機7の送風により、熱風管
8、乾燥容器1、排気管10、集塵装置11、連
通管12、ダクト13、短管15、サクシヨンフ
イルター16を順次通つてから送風機7の吸気口
に送り込まれ循環する。このように熱風を循環さ
せて再利用を図る構成とすれば、熱風供給エネル
ギーの節約が達成できる。
An exhaust pipe 10 is provided on a part of the upper surface of the upper container 1b.
The tip of this exhaust pipe 10 is connected to a dust collector 11 (back filter in this embodiment). A communication pipe 12 is installed at the top of the dust collector 11.
A duct 13 is installed horizontally from the left to the right through the airflow control valve 1.
4. It is connected to the air intake port of the blower 7 via a short pipe 15 and a suction filter 16. 17 is a drive motor for the blower 7. Therefore, the heat from the heating means 4 is transferred to the hot air pipe 8, the drying container 1, the exhaust pipe 10, the dust collector 11, the communication pipe 12, the duct 13, the short pipe 15, and the suction filter 16 by the air blowing from the blower 7. After passing through the air one after another, it is fed into the air intake port of the blower 7 and circulated. If the configuration is such that the hot air is circulated and reused, it is possible to save energy for supplying the hot air.

前記乾燥容器1内には、撹拌羽根の回転軸22
線に対して略平行な縦羽根と略垂直な横羽根との
多数個の組合せからなる撹拌羽根20が取り付け
られており、これら撹拌羽根20の適数個には材
料が当る面を水平方向または垂直方向に対し角度
をもつ傾斜面イとしている。この傾斜面イは、こ
の実施例では第5図又は第6図の如き傾斜をもた
せると共に、該傾斜面イの両端に補強板ロを形成
し、断面が三角形又は略半円形となし、この補強
板ロで傾斜面イの補強を行つている。しかし、こ
の補強板ロはないものでもよい。
Inside the drying container 1, there is a rotating shaft 22 of a stirring blade.
Stirring blades 20 consisting of a large number of combinations of vertical blades that are approximately parallel to the line and horizontal blades that are approximately perpendicular to the line are attached, and a suitable number of these stirring blades 20 have a surface that touches the material horizontally or The surface is inclined at an angle to the vertical direction. In this embodiment, this inclined surface A has an inclination as shown in FIG. Reinforcement of the sloped surface A is being carried out using plate rotors. However, this reinforcing plate B may be omitted.

前述の撹拌羽根20を詳しく説明すれば、第4
図示の如く、モータにより駆動される鎖伝動機構
21により回転される回転軸18と連結した撹拌
羽根の回転軸22の非対称位置に取り付けてあ
り、この撹拌羽根20は、長さを異ならし、かつ
断面を第5図の如く三角形とした横羽根a,b,
c,d,e,fと、前記aとbの先端間に連結し
た断面が第6図の如く略半円形とした縦羽根m
と、前記c中央近くに立設した断面を前記mと同
形状とした縦羽根nと、平板状の水平羽根o,p
と、平板の二重板からなる水平羽根q,rと、螺
旋状の羽根S,S1,S2とからなつている。
To explain the above-mentioned stirring blade 20 in detail, the fourth
As shown in the figure, the stirring blades 20 are attached at an asymmetrical position on a rotating shaft 22 connected to a rotating shaft 18 rotated by a chain transmission mechanism 21 driven by a motor, and the stirring blades 20 have different lengths and Horizontal blades a, b, with triangular cross sections as shown in Figure 5,
c, d, e, f, and a vertical blade m whose cross section connected between the tips of a and b is approximately semicircular as shown in FIG.
, a vertical blade n whose cross section is the same shape as the m, and flat horizontal blades o and p, which are installed near the center of the c.
, horizontal blades q and r made of double flat plates, and spiral blades S, S 1 and S 2 .

しかも、前記横羽根a〜fの傾斜面イは材料を
上昇方向に掬い上げて撹拌し、縦羽根m,nの傾
斜面イは撹拌羽根の回転軸22線方向に集合させ
て撹拌するように配設してある。螺旋状の羽根
S,S1,S2は乾燥容器1の出口1c近くの材料を
上昇方向に掬い上げて撹拌する。従つて、前記横
羽根a〜fの傾斜面イと螺旋状の羽根S,S1,S2
とが相俟つて、出口1c近くの材料の閉塞を防止
すると共に、材料を上昇させて撹拌する。上昇さ
れた材料は縦羽根m,nの傾斜面イの作用により
上方中央に集合させられ、次いで下方に移動され
てから再度上方へ移動される。このように材料が
対流されるため均一な撹拌、乾燥が行われる。
Moreover, the inclined surfaces A of the horizontal blades a to f scoop up the material in the upward direction and stir it, and the inclined surfaces A of the vertical blades m and n gather the material in the direction of the axis of rotation 22 of the stirring blades and stir it. It is arranged. The spiral blades S, S 1 and S 2 scoop up the material near the outlet 1c of the drying container 1 in the upward direction and stir it. Therefore, the inclined surfaces A of the horizontal blades a to f and the spiral blades S, S 1 , S 2
Together, this prevents the material near the outlet 1c from clogging, and raises and stirs the material. The lifted material is gathered at the upper center by the action of the inclined surfaces A of the vertical blades m and n, then moved downward, and then moved upward again. Since the material is convected in this way, uniform stirring and drying are performed.

また、乾燥容器1内の漏斗状の多孔板9に対応
する横羽根d,e,fの外端は何れも同多孔板9
内壁に接近させており、これで多孔板9に対する
材料の付着を防止している。
Further, the outer ends of the horizontal blades d, e, and f corresponding to the funnel-shaped perforated plate 9 in the drying container 1 are all connected to the same perforated plate 9.
It is placed close to the inner wall, thereby preventing material from adhering to the perforated plate 9.

なお、前記撹拌羽根20は、第7図示の如き構
成にすることもできる。このものは、撹拌羽根の
回転軸22の左右両側の非対称位置に、断面が第
5図の如く三角形で回転軸22線に対して略垂直
の長い横羽根tと、短い横羽根uとを段違いに横
設する一方、この両横羽根t,uの先端には、断
面を第6図の如く略半円形とした折曲げ状の縦羽
根x,yの上部を連結すると共に、両縦羽根x,
yの最下端部とそれより少し上方とを断面が第5
図の如く三角形とした横羽根w,vを連結してな
るものである。この場合の縦羽根x,yも乾燥容
器1下部の多孔板9内壁に接近させ、多孔板9に
材料が付着するのを防止している。
Note that the stirring blade 20 can also be configured as shown in FIG. 7. This device has a long horizontal blade t, which has a triangular cross section and is approximately perpendicular to the rotation axis 22 line, and a short horizontal blade u, which have a triangular cross section and are approximately perpendicular to the line of the rotation axis 22, and a short horizontal blade u, which are disposed asymmetrically on both the left and right sides of the rotating shaft 22 of the stirring blade, as shown in FIG. At the same time, the tops of bent vertical blades x, y whose cross sections are approximately semicircular as shown in FIG. 6 are connected to the tips of both horizontal blades t and u, and both vertical blades x ,
The cross section of the lowest end of y and a little above it is the 5th
It is made by connecting triangular horizontal blades w and v as shown in the figure. In this case, the vertical blades x and y are also brought close to the inner wall of the perforated plate 9 at the bottom of the drying container 1 to prevent material from adhering to the perforated plate 9.

なお、前記横羽根vはないものも実施できる。 Incidentally, a structure without the horizontal blade v can also be implemented.

縦羽根m,n,x,yは図示の形状に限定され
るものではなく、回転軸線に対して傾斜している
場合も含む。また、横羽根a〜f,t,u,v,
wも図示のものに限らず、回転軸線に対して勾配
をもつもの、或いは彎曲しているものも含む。
The vertical blades m, n, x, and y are not limited to the illustrated shape, and may also be inclined with respect to the axis of rotation. Also, the horizontal blades a to f, t, u, v,
w is not limited to the one shown in the drawings, but also includes one having an inclination with respect to the axis of rotation, or one having a curve.

前記第4図と第7図に示した撹拌羽根20の構
成によれば、材料に対して圧縮やせん断力が加わ
らないため、材料が団子状になるのを防止する
し、また材料を乾燥容器1に充填した状態でも全
ての部分が運動し、さらに撹拌羽根の縦羽根と横
羽根との交差部においても抵抗が少ない利点があ
る。
According to the configuration of the stirring blade 20 shown in FIGS. 4 and 7, no compression or shearing force is applied to the material, which prevents the material from forming into lumps, and also prevents the material from forming in a drying container. Even when the stirring blade is filled to 100%, all parts move, and furthermore, there is an advantage that there is little resistance at the intersection between the vertical blade and the horizontal blade of the stirring blade.

前記加熱手段4は、温度制御装置23によつて
複数段階以上に温度調節ができるようにしてあ
る。24は温度計である。かかる構成によれば、
急速昇温を避けることができるから、特に大容量
の場合に発生する材料の融着時の撹拌羽根との共
回り現象を避けることができる。また材料の粘性
などの物性の違いに応じて適温の熱風を供給でき
る。
The temperature of the heating means 4 can be adjusted in multiple stages or more by a temperature control device 23. 24 is a thermometer. According to such a configuration,
Since rapid temperature rise can be avoided, it is possible to avoid the co-rotation phenomenon with the stirring blade when the materials are fused, which occurs particularly in the case of a large capacity. In addition, hot air at an appropriate temperature can be supplied depending on the physical properties such as viscosity of the material.

なお、前記鎖伝動機構21はスプロケツト2
5,26とローラーチエン27と駆動源とからな
つており、28は減速機である。
Note that the chain transmission mechanism 21 is connected to the sprocket 2.
5, 26, a roller chain 27, and a drive source, and 28 is a speed reducer.

30は蒸気用パイプ、31はバルブ、32はス
トレーナ、34は電磁弁、35は材料供給ホツパ
ー3下部に取り付けた自動ゲートバルブ、36は
リミツトスイツチ、37,38は掃除口扉、39
はレベル窓、40はレベル計、41はスライドダ
ンバー、42は材料取出し口で、これに次工程の
成形機や本乾燥機などが接続される。43は端子
ボツクス、44はダイヤフラム弁、45は電磁
弁、46はアキユームレータ、47は点検口扉、
48は集塵装置の外装ケース、49はエアフイル
ター、50はダストホース、51は粉塵排出口、
52はフイルターバツグ、53はチエンカバーで
ある。
30 is a steam pipe, 31 is a valve, 32 is a strainer, 34 is a solenoid valve, 35 is an automatic gate valve attached to the bottom of the material supply hopper 3, 36 is a limit switch, 37 and 38 are cleaning ports, 39
4 is a level window, 40 is a level meter, 41 is a slide damper, and 42 is a material outlet, to which a molding machine, main dryer, etc. for the next process are connected. 43 is a terminal box, 44 is a diaphragm valve, 45 is a solenoid valve, 46 is an accumulator, 47 is an inspection door,
48 is the outer case of the dust collector, 49 is the air filter, 50 is the dust hose, 51 is the dust outlet,
52 is a filter bag, and 53 is a chain cover.

なお、加熱手段4は実施例のものに限らず任意
である。
Incidentally, the heating means 4 is not limited to the one in the embodiment, but is arbitrary.

この撹拌羽根20は前記実施例で示した乾燥容
器1にしか採用できないものではなく、あらゆる
乾燥容器に適用できる。あるいは撹拌槽などにも
適用できる。
This stirring blade 20 is not applicable only to the drying container 1 shown in the above embodiment, but can be applied to any drying container. Alternatively, it can also be applied to a stirring tank.

この実施例の作用を、材料としてポリエステル
チツプの結晶化及び乾燥操作工程を例として以下
に説明する。
The operation of this embodiment will be explained below by taking as an example the crystallization and drying process of polyester chips as the material.

乾燥容器1内の撹拌羽根20を鎖伝動機構21
を介して回転させながら、ポリエステルチツプを
材料供給ホツパー3の材料投入口3aから供給
し、その下部の自動ゲートバルブ35の開放によ
り所定量を乾燥容器1内に送り込み、そこで同材
料を撹拌羽根20で撹拌する。
The stirring blade 20 inside the drying container 1 is connected to a chain transmission mechanism 21.
The polyester chips are supplied from the material input port 3a of the material supply hopper 3 while being rotated through the material supply hopper 3, and a predetermined amount is fed into the drying container 1 by opening the automatic gate valve 35 at the bottom thereof, where the same material is passed through the stirring blade 20. Stir with

一方、加熱手段4の熱は、送風機7によつて、
熱風として乾燥容器1下側部より多孔板9を介し
て乾燥室内の材料と接触する。従つて、乾燥容器
1の乾燥室では前記撹拌羽根20のうち横羽根a
〜f……が材料を上昇方向に掬い上げると共に、
縦羽根m,n……は回転軸線方向に集合させて撹
拌すると同時に、これら撹拌羽根の適数個には材
料が当る面を水平方向または垂直方向に対し角度
をもつ傾斜面イとしていることから、材料に対す
るせん断力と圧縮力をなくし、材料の付着や変形
あるいは団塊の発生もなく、材料の撹拌が均一に
行われ、材料(ポリエステルチツプ)の結晶化が
均一に行われると共に水分も除去され、所望のポ
リエステルチツプが得られる。
On the other hand, the heat from the heating means 4 is transferred by the blower 7.
The hot air comes into contact with the material inside the drying chamber from the lower side of the drying container 1 through the perforated plate 9. Therefore, in the drying chamber of the drying container 1, the horizontal blade a of the stirring blades 20
~f... scoops up the material in the upward direction, and
The vertical blades m, n... are assembled in the direction of the axis of rotation for stirring, and at the same time, a suitable number of these stirring blades have surfaces on which the material comes into contact with inclined surfaces that are angled with respect to the horizontal or vertical direction. , the shearing force and compressive force on the material are eliminated, there is no adhesion or deformation of the material, or the formation of lumps, the material is uniformly stirred, the material (polyester chips) is uniformly crystallized, and water is also removed. , the desired polyester chips are obtained.

タイマーに設定した時間が経過すると、スライ
ドダンバー41が自動的に開いて、結晶化と乾燥
が処理された材料が材料取出し口42より、次工
程の合成樹脂用成形機や本乾燥機などに排出され
る。
When the time set on the timer has elapsed, the slide damper 41 automatically opens and the crystallized and dried material is discharged from the material outlet 42 to the next process, such as a synthetic resin molding machine or main dryer. be done.

次いで、上記排出時間を設定したタイマーのタ
イムアツプに連動して、前記スライドダンバー4
1が閉じ、材料供給ホツパー3の自動ゲートバル
ブ35が開くと、それに連動して材料投入口3a
より新規材料が乾燥容器1内に所定量供給され、
次サイクルの結晶化と乾燥処理が行なわれる。
Next, in conjunction with the time up of the timer that has set the ejection time, the slide damper 4
1 is closed and the automatic gate valve 35 of the material supply hopper 3 is opened, the material input port 3a is
A predetermined amount of new material is supplied into the drying container 1,
The next cycle of crystallization and drying is carried out.

なお、乾燥容器1内で材料と熱交換した空気
は、排気管10を経て集塵装置11で清浄され、
該清浄空気は連通管12、ダクト13、サクシヨ
ンフイルター16を経て前記送風機7の吸込口に
送り込んで循環利用する。かかる構成によれば、
前述した如く、循環利用される空気は余熱がある
ので、熱風エネルギーの節約が達成できる利点が
ある。
The air that has exchanged heat with the material in the drying container 1 passes through the exhaust pipe 10 and is purified by the dust collector 11.
The clean air is sent to the suction port of the blower 7 through the communication pipe 12, duct 13, and suction filter 16 for circulation. According to such a configuration,
As mentioned above, since the air that is recycled has residual heat, it has the advantage of saving hot air energy.

第8図は、こ乾燥装置を公知の真空式ロータリ
ードライヤと接続した応用例を示す。
FIG. 8 shows an application example in which this drying device is connected to a known vacuum type rotary dryer.

このものは、フレコン60内の材料を材料供給
ホツパー3に送り込んでから、一定量を空気動力
源63の圧送空気により輸送管65を介してサイ
クロン66、乾燥容器1内に輸送し、該乾燥容器
1で材料を結晶化ないし乾燥する。処理済の材料
は、スライドバルブ68を開放し、切替バルブ6
4の開操作によつて輸送管651へ空気動力源6
3の圧送空気を送り込んで、サイクロン69を経
て貯蔵タンク70に貯蔵する。その場合に、サイ
クロン66,69の排気口661,691から排出
される空気は、集塵装置72に供給されてから、
クーラー73で冷却され空気動力源63の吸込口
に送り込まれ再度循環して利用される。
In this system, the material in the flexible container 60 is fed into the material supply hopper 3, and then a certain amount is transported via the transport pipe 65 to the cyclone 66 and into the drying container 1 using compressed air from the air power source 63. 1. Crystallize or dry the material. To remove the processed material, open the slide valve 68 and transfer the material to the switching valve 6.
The air power source 6 is connected to the transport pipe 65 1 by the opening operation of 4.
The compressed air of No. 3 is sent in, passes through a cyclone 69, and is stored in a storage tank 70. In that case, the air discharged from the exhaust ports 66 1 and 69 1 of the cyclones 66 and 69 is supplied to the dust collector 72 and then
The air is cooled by the cooler 73, fed into the suction port of the air power source 63, and circulated again for use.

前記貯蔵タンク70の下部は輸送管652及び
供給器82を介して公知の真空式ロータリードラ
イヤー74に接続されている。そして、輸送管6
2の中途には空気動力源75よりの圧送空気を
供給する空気輸送管76が接続されている。従つ
て、貯蔵タンク70内の処理済の材料は、バルブ
71の開放により輸送管652を介して真空式ロ
ータリードライヤー74に送り込まれ、このドラ
イヤー74でも乾燥を行う。ここで乾燥処理済の
材料は、排出口77より空気動力源75の圧送空
気によりサイクロン79を経て製品貯蔵タンク8
0へ送り込まれる。この製品貯蔵タンク80より
製品をフレコンなどの収納容器81に収納する。
サイクロン79と供給器82の排気口791,8
1は、排気管83,84を介して集塵装置72
と接続すると共に、該集塵装置72の排気口72
をクーラー85を介して前記空気動力源75の
吸込口と接続しており、使用済の空気を循環して
再利用するようにしている。86はドライエアー
供給管である。
The lower part of the storage tank 70 is connected to a known vacuum rotary dryer 74 via a transport pipe 65 2 and a feeder 82 . And transport pipe 6
An air transport pipe 76 for supplying pressurized air from an air power source 75 is connected to the middle of the air pump 5 2 . Therefore, the treated material in the storage tank 70 is sent to the vacuum rotary dryer 74 via the transport pipe 65 2 by opening the valve 71, and is also dried in this dryer 74. Here, the dried material is transferred from a discharge port 77 to a product storage tank 8 via a cyclone 79 by compressed air from an air power source 75.
sent to 0. The product is stored from this product storage tank 80 in a storage container 81 such as a flexible container.
Exhaust ports 79 1 , 8 of cyclone 79 and feeder 82
2 1 is connected to the dust collector 72 via exhaust pipes 83 and 84.
and the exhaust port 72 of the dust collector 72.
1 is connected to the suction port of the air power source 75 via a cooler 85, and used air is circulated and reused. 86 is a dry air supply pipe.

この考案は、以上の構成からなるものであり、
撹拌羽根を内装した乾燥容器内に加熱手段の熱を
送風機により送風して材料を撹拌する乾燥装置に
おいて、前記撹拌羽根は回転軸線に対して略平行
な縦羽根と略垂直な横羽根との多数個の組合せか
らなると共に、これら撹拌羽根の適数個には材料
が当る面を水平方向または垂直方向に対し角度を
もつ傾斜面としているから、材料に対するせん断
力と圧縮力がなくなり、材料の団塊の発生を防ぐ
と共に、撹拌羽根に材料が付着したり変形したり
することがなくなる。
This idea consists of the above structure,
In a drying device that stirs the material by blowing heat from a heating means with an air blower into a drying container equipped with a stirring blade, the stirring blade has a plurality of vertical blades substantially parallel to the axis of rotation and horizontal blades substantially perpendicular to the axis of rotation. In addition, since an appropriate number of these stirring blades have surfaces in contact with the material that are inclined at an angle to the horizontal or vertical direction, the shearing force and compressive force on the material are eliminated, and the material becomes lumpy. This also prevents material from adhering to or deforming the stirring blade.

また、前記横羽根の傾斜面は材料を上昇方向に
掬い上げて撹拌し、縦羽根の傾斜面は材料を回転
軸線方向に集合して撹拌するように配設してなる
から、材料が乾燥容器の下方(出口)から上方
へ、上方から上方中央へ、上方中央から下方へと
対流させられるため、均一に撹拌される。
In addition, the sloped surface of the horizontal blade is arranged to scoop up and stir the material in the upward direction, and the sloped surface of the vertical blade is arranged so as to collect and stir the material in the direction of the rotation axis. Convection flows from the bottom (outlet) to the top, from the top to the top center, and from the top center to bottom, so that the mixture is uniformly stirred.

かくして、この考案は、撹拌羽根を縦羽根と横
羽根とで構成すると共に、特殊な傾斜面をもつよ
うに形成していることから、材料の撹拌、乾燥が
均一に行われ、材料の結晶化や乾燥の処理時間が
短時間に行える。すなわち、ポリエステルチツプ
の結晶化処理について例示すると、従来の真空式
ロータリードライヤーによれば、処理量1トン/
1バツチで、結晶化時間だけで約12時間を要した
が、この考案によれば、同一処理量で15分ないし
60分で結晶化が完了した実験結果が得られた。
Thus, in this invention, the stirring blade is composed of vertical blades and horizontal blades, and is formed with a special inclined surface, so that the stirring and drying of the material is performed uniformly, and the crystallization of the material is prevented. and drying process time can be shortened. That is, to give an example of the crystallization treatment of polyester chips, according to a conventional vacuum rotary dryer, the throughput is 1 ton/
One batch required about 12 hours just for crystallization, but according to this idea, it took about 15 minutes or less for the same amount of processing.
Experimental results showed that crystallization was completed in 60 minutes.

本案品は構造が簡単で、従来の真空式ロータリ
ードライヤーの如き大規模なスペースをとらない
ので、原料加工者側で本案品を据え付ければ、非
結晶状態の材料を自前で結晶化することができ
る。
This product has a simple structure and does not take up as much space as conventional vacuum rotary dryers, so if raw material processors install this product, they can crystallize amorphous materials on their own. can.

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

図は何れもこの考案の実施例を示し、第1図は
正面図、第2図は平面図、第3図は右側面図、第
4図は撹拌羽根の斜視図、第5図と第6図は撹拌
羽根の断面図、第7図は撹拌羽根の変形例の斜視
図、第8図は本案品の応用例を示すフローチヤー
トである。 1……乾燥容器、4……加熱手段、7……送風
機、20……撹拌羽根、22……撹拌羽根の回転
軸、23……温度制御装置、イ……傾斜面、a,
b,c,d,f,t,u,v,w……横羽根、
m,n,x,y……縦羽根。
The figures all show examples of this invention; Fig. 1 is a front view, Fig. 2 is a plan view, Fig. 3 is a right side view, Fig. 4 is a perspective view of the stirring blade, and Figs. 5 and 6. The figure is a sectional view of a stirring blade, FIG. 7 is a perspective view of a modified example of the stirring blade, and FIG. 8 is a flowchart showing an example of application of the present product. DESCRIPTION OF SYMBOLS 1... Drying container, 4... Heating means, 7... Air blower, 20... Stirring blade, 22... Rotating shaft of stirring blade, 23... Temperature control device, A... Inclined surface, a,
b, c, d, f, t, u, v, w...horizontal blade,
m, n, x, y...vertical blades.

Claims (1)

【実用新案登録請求の範囲】 (1) 撹拌羽根を内装した乾燥容器内に加熱手段の
熱を送風機により送風して材料を撹拌する乾燥
装置において、前記撹拌羽根は回転軸線に対し
て略平行な縦羽根と略垂直な横羽根との多数個
の組合せからなると共に、これら撹拌羽根の適
数個には材料が当る面を水平方向または垂直方
向に対し角度をもつ傾斜面とし、さらに前記横
羽根の傾斜面は材料を上昇方向に掬い上げて撹
拌し、縦羽根の傾斜面は回転軸線方向に集合さ
せて撹拌すべく配設してあることを特徴とする
乾燥装置。 (2) 前記加熱手段は温度制御装置により調節でき
るようにしてある実用新案登録請求の範囲第(1)
項記載の乾燥装置。 (3) 前記送風機で送られた熱風は使用後に同送風
機に循環させ再利用できるようにしてある実用
新案登録請求の範囲第(1)項または第(2)項記載の
乾燥装置。
[Claims for Utility Model Registration] (1) In a drying device that stirs the material by blowing heat from a heating means into a drying container equipped with a stirring blade using an air blower, the stirring blade is substantially parallel to the axis of rotation. It consists of a large number of combinations of vertical blades and approximately vertical horizontal blades, and a suitable number of these stirring blades have surfaces that contact the material with inclined surfaces that are angled with respect to the horizontal or vertical direction, and furthermore, the horizontal blades A drying device characterized in that the inclined surfaces of the vertical blades are arranged to scoop up and stir the material in an upward direction, and the inclined surfaces of the vertical blades are arranged to aggregate and stir the material in the direction of the rotation axis. (2) Utility model registration claim No. (1), wherein the heating means is adjustable by a temperature control device.
Drying equipment as described in section. (3) The drying device according to claim 1 or 2, wherein the hot air sent by the blower is circulated through the blower after use so that it can be reused.
JP13796183U 1983-09-05 1983-09-05 drying equipment Granted JPS6043991U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13796183U JPS6043991U (en) 1983-09-05 1983-09-05 drying equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13796183U JPS6043991U (en) 1983-09-05 1983-09-05 drying equipment

Publications (2)

Publication Number Publication Date
JPS6043991U JPS6043991U (en) 1985-03-28
JPS6311588Y2 true JPS6311588Y2 (en) 1988-04-04

Family

ID=30309707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13796183U Granted JPS6043991U (en) 1983-09-05 1983-09-05 drying equipment

Country Status (1)

Country Link
JP (1) JPS6043991U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103162523A (en) * 2013-04-14 2013-06-19 江苏吉能达建材设备有限公司 Material scattering device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103162523A (en) * 2013-04-14 2013-06-19 江苏吉能达建材设备有限公司 Material scattering device

Also Published As

Publication number Publication date
JPS6043991U (en) 1985-03-28

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