JPH0416697B2 - - Google Patents

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Publication number
JPH0416697B2
JPH0416697B2 JP58013380A JP1338083A JPH0416697B2 JP H0416697 B2 JPH0416697 B2 JP H0416697B2 JP 58013380 A JP58013380 A JP 58013380A JP 1338083 A JP1338083 A JP 1338083A JP H0416697 B2 JPH0416697 B2 JP H0416697B2
Authority
JP
Japan
Prior art keywords
drying
dried
pipe
hot air
air
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 - Lifetime
Application number
JP58013380A
Other languages
Japanese (ja)
Other versions
JPS59138878A (en
Inventor
Sadaaki Tanaka
Tsutomu Oono
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.)
Matsui Mfg Co Ltd
Original Assignee
Matsui 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 Matsui Mfg Co Ltd filed Critical Matsui Mfg Co Ltd
Priority to JP1338083A priority Critical patent/JPS59138878A/en
Publication of JPS59138878A publication Critical patent/JPS59138878A/en
Publication of JPH0416697B2 publication Critical patent/JPH0416697B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、例えば合成樹脂材料などの粉粒体
等(被乾燥物又は材料ともいう)を合成樹脂成形
機などに供給する前に該粉粒体等を乾燥する装置
に関する。
Detailed Description of the Invention [Industrial Field of Application] This invention provides a method for drying powder or granular materials such as synthetic resin materials (also referred to as materials to be dried) before supplying them to a synthetic resin molding machine or the like. This invention relates to a device for drying granules, etc.

〔従来の技術〕[Conventional technology]

従来、この種の粉粒体等の乾燥装置としては、 (イ) 実公昭36−6981号公報、(ロ) 特開昭53−
71362号公報に示されているように、駆動源によ
り回転される回転軸の等配位置に2つ以上の乾燥
室を回転自在に設けるとともに、各乾燥室の下端
近傍には熱風受口を形成し、この熱風受口の対応
個所には熱源と接続した送風管を固設し、各乾燥
室の回転につれて各乾燥室の熱風受口が順次に前
記送風管に連通され、各乾燥室に供給された被乾
燥物を下方から上方に向けた熱風により流動乾燥
し、乾燥室の上方から被乾燥物を供給し乾燥室の
下部から取り出すようにしたものが知られてい
る。
Conventionally, this type of drying apparatus for powder and granular materials has been disclosed in (a) Japanese Utility Model Publication No. 6981-1981, and (b) Japanese Unexamined Patent Application Publication No. 1983-1989.
As shown in Publication No. 71362, two or more drying chambers are rotatably provided at equidistant positions on a rotating shaft rotated by a drive source, and a hot air receptacle is formed near the bottom end of each drying chamber. A blower pipe connected to a heat source is fixed at the corresponding location of this hot air inlet, and as each drying room rotates, the hot air inlet of each drying room is sequentially communicated with the blower pipe, and the hot air is supplied to each drying room. There is a known method in which the dried material is fluidized and dried by hot air directed from below upward, and the dried material is supplied from the upper part of the drying chamber and taken out from the lower part of the drying chamber.

(ハ) また、特公昭42−1833号公報に示すよう
に、区画された複数の乾燥室へ異なる温度の熱風
を供給して被乾燥物を所望の乾燥温度に乾燥する
構成とするとともに、各乾燥室には被乾燥物の投
入及び取出し用バツチを設け流動乾燥するように
してなるものも知られている。
(c) As shown in Japanese Patent Publication No. 42-1833, a structure is adopted in which hot air of different temperatures is supplied to a plurality of divided drying chambers to dry the material to be dried to a desired drying temperature, and each It is also known that a drying chamber is provided with a batch for loading and unloading the material to be dried, thereby allowing fluidized drying.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかるに、(1) 上記従来例(イ)、(ロ)のものは、乾
燥室の上部のホツパーから被乾燥物を供給し、乾
燥済被乾燥物は乾燥室の下部から自重により排出
するものであるため、排出時に被乾燥物が乾燥室
内に残留する場合があつて、材料替えなどの際に
はその都度清掃しなければならなかつた。
However, (1) In the conventional examples (a) and (b) above, the material to be dried is supplied from the hopper at the top of the drying chamber, and the dried material is discharged from the bottom of the drying chamber by its own weight. Therefore, the material to be dried may remain in the drying chamber when it is discharged, and the drying chamber must be cleaned every time the material is changed.

また、従来例(ハ)のものは、各乾燥室に設けたバ
ツチより被乾燥物を供給し取り出す構成であるた
め、同一個所から被乾燥物の供給と排出ができる
利点はあるものの、前記と同様に被乾燥物が乾燥
室内に残留して排出し難く清掃が面倒であつた。
In addition, in the conventional example (c), the material to be dried is supplied and taken out from batches provided in each drying chamber, so although it has the advantage of being able to supply and discharge the material to be dried from the same location, Similarly, the material to be dried remains in the drying chamber and is difficult to discharge, making cleaning difficult.

(2) 従来例(イ)、(ロ)のものでは、各乾燥室には所望
する一定の乾燥温度の熱風を供給するものである
ため、乾燥温度の異なる2つ以上の被乾燥物を乾
燥したり、或いは単一の被乾燥物でも乾燥温度を
変えて乾燥することはできないという問題点があ
つた。
(2) In conventional examples (a) and (b), each drying chamber is supplied with hot air at a desired constant drying temperature, so two or more items to be dried with different drying temperatures can be dried. There is a problem that even a single object to be dried cannot be dried by changing the drying temperature.

この発明は、上記従来例(イ)、(ロ)、(ハ)の問題点を
ことごとく解消しようとするものであつて、乾燥
済材料の排出時に乾燥室内に該材料が残留するの
を防止すると共に、材料替え時などにおいて乾燥
室内の清掃を不要とするだけでなく、異なる乾燥
温度で乾燥することにより、被乾燥物を適切な温
度で加熱して乾燥効率を向上するとともに乾燥時
間の短縮化を図るものを提供するものである。
This invention aims to solve all of the problems of the conventional examples (a), (b), and (c) above, and prevents the dried material from remaining in the drying chamber when the material is discharged. In addition, not only does it eliminate the need to clean the drying chamber when changing materials, but by drying at different drying temperatures, the material to be dried is heated at an appropriate temperature, improving drying efficiency and shortening drying time. The aim is to provide something that helps people achieve their goals.

〔課題を解決するための手段〕[Means to solve the problem]

上記課題を解決するため、この発明は、駆動源
により回転される回転軸の等配位置に2つ以上の
乾燥筒を回転自在に設けるとともに、各乾燥筒の
下端近傍には熱風受口を形成し、この熱風受口の
対応個所には熱源と接続した送風管を固設し、各
乾燥筒の回転につれ各乾燥筒の熱風受口が順次に
前記送風管に連通され、前記送風管は2つ以上の
乾燥室に同時に連通するように設けるとともに、
その送風管に供給する熱風には温度差を設け、各
乾燥室に供給された被乾燥物を下方から上方に向
けた熱風により流動乾燥するようにしてなる粉粒
体等の乾燥装置であつて、 前記乾燥筒の少なくとも1つの材料入口の上流
側には搬送管を設け、この搬送管には切替弁を介
して材料供給管と乾燥済材料排出管とを接続し、
乾燥筒内への被乾燥物の供給は前記材料供給管を
介して空気源の気力により行うとともに、乾燥済
みの被乾燥物の排出は乾燥済材料排出管を介して
空気源の吸引力により排出するようにする一方、
上記搬送管と連通した乾燥筒内には該搬送管を上
下動自在に嵌挿するとともに、搬送管の下端外周
には蓋体を設け、同乾燥筒と短管との間にはフイ
ルターを挾着してなることを特徴とする構成を採
用したものである。
In order to solve the above problems, the present invention rotatably provides two or more drying cylinders at equidistant positions on a rotating shaft rotated by a drive source, and forms a hot air receptacle near the lower end of each drying cylinder. However, a blower pipe connected to a heat source is fixed at a corresponding location of the hot air inlet, and as each drying tube rotates, the hot air inlet of each drying tube is sequentially communicated with the blower tube, and the blower tube is connected to the blower tube. It is installed so that it communicates with two or more drying chambers at the same time, and
A drying device for powder and granular materials, etc., which sets a temperature difference in the hot air supplied to the blower pipes, and fluidizes and dries the material to be dried supplied to each drying chamber by the hot air directed from the bottom to the top. , a conveying pipe is provided upstream of at least one material inlet of the drying cylinder, and a material supply pipe and a dried material discharge pipe are connected to this transport pipe via a switching valve,
The materials to be dried are supplied into the drying cylinder through the material supply pipe using the air force of the air source, and the dried materials are discharged through the dried material discharge pipe using the suction force of the air source. On the other hand,
The conveying tube is inserted into the drying tube that communicates with the conveying tube so as to be able to move up and down, and a lid is provided on the outer periphery of the lower end of the conveying tube, and a filter is inserted between the drying tube and the short tube. It adopts a structure characterized by the fact that it is worn over the body.

少なくとも1つ以上の乾燥室には、前記熱源の
使用後の排熱を空気源に戻して循環使用するよう
に構成することもできる。
At least one or more drying chambers may be configured so that exhaust heat after use of the heat source is returned to the air source for circulation.

〔作用〕[Effect]

(1) 乾燥筒が、被乾燥物の仕込位置に来たとき
に、該乾燥筒内に被乾燥物が供給され所定量が
充填される。この乾燥筒内への被乾燥物の供給
は、切替弁を開弁して、空気源の気力により材
料供給管を経て搬送管から供給される (2) 仕込を終了した乾燥筒の乾燥室は、次に複数
の乾燥位置に1こまづつ回転されて行く。この
乾燥位置では熱源からの熱風が下方から上方に
向けて流動状態で乾燥されるため、通常の加熱
温度より高温処理または低温(冷却)処理して
も粉粒体が団魂や付着を生じることもない。
(1) When the drying cylinder comes to the position where the material to be dried is placed, the material to be dried is supplied into the drying cylinder and filled to a predetermined amount. The material to be dried is supplied into the drying cylinder by opening the switching valve and using the energy of the air source to supply the material from the conveying pipe via the material supply pipe (2) Once the drying process has been completed, the drying chamber of the drying cylinder is , and then rotated one frame at a time to a plurality of drying positions. In this drying position, the hot air from the heat source is dried in a flowing state from the bottom to the top, so even if processed at a higher temperature than the normal heating temperature or at a lower temperature (cooling), the powder and granules will not form lumps or stick to each other. Nor.

そこで、この流動乾燥をしながら、複数の乾
燥室のそれぞれの乾燥温度が異なるように、送
風管からの熱風に温度差を設けるようにしてい
るため、所望の加熱温度を選択することによ
り、乾燥温度の異なる2つ以上の被乾燥物を乾
燥することができる。また、例えば、第1乾燥
室では110℃、第2乾燥室では150℃、第3乾燥
室では100℃の如く、当該樹脂材料の通常の乾
燥温度で乾燥してから、その通常の乾燥温度よ
りも高い温度で乾燥させた後に、通常の乾燥温
度又はそれより少し低温の冷却温度に戻す工程
を採ることもできる。さらには、乾燥温度の異
なる材料を、それぞれ所望温度の乾燥室に供給
して、乾燥しつつ混合することにより混合材料
を得るようにすることもできる。
Therefore, while performing this fluidized drying, we create temperature differences in the hot air from the blast pipes so that the drying temperatures in each of the multiple drying chambers are different, so by selecting the desired heating temperature, drying Two or more objects to be dried at different temperatures can be dried. Furthermore, after drying at the normal drying temperature of the resin material, such as 110°C in the first drying room, 150°C in the second drying room, and 100°C in the third drying room, It is also possible to adopt a step of drying at a high temperature and then returning the temperature to a normal drying temperature or a slightly lower cooling temperature. Furthermore, it is also possible to obtain a mixed material by supplying materials having different drying temperatures to drying chambers each having a desired temperature and mixing them while drying.

(3) 乾燥筒内の乾燥室で所望水分率まで乾燥され
た被乾燥物は、取出位置の材料排出部から排出
される。このとき、搬送管を下動して蓋体とフ
イルター間に収容されている被乾燥物を、空気
源の吸引力により搬送管の材料入口から開弁し
ている切替弁を経て系外に排出する。これによ
り乾燥室内への残材が完全に除去される。一
方、乾燥室内で熱交換を終えた加熱空気は、材
料中から除湿した水分とともに系外に排出され
るか、フイルターなどでの適宜処理を施してか
ら空気源に戻して循環使用することができる。
(3) The material to be dried that has been dried to a desired moisture content in the drying chamber in the drying cylinder is discharged from the material discharge section at the take-out position. At this time, the material to be dried stored between the lid and the filter is moved down the transport pipe and discharged from the system through the switching valve that is opened from the material inlet of the transport pipe using the suction force of the air source. do. This completely removes any remaining material in the drying chamber. On the other hand, the heated air that has undergone heat exchange in the drying room can be discharged to the outside of the system along with the moisture that has been dehumidified from the material, or it can be appropriately treated with a filter, etc., and then returned to the air source for circulation. .

〔実施例〕〔Example〕

この発明の一実施例を第1図ないし第4図に基
づいて以下に説明する。
An embodiment of the present invention will be described below with reference to FIGS. 1 to 4.

1は架台で、この架台1の上部と下部には取付
板2,2aが水平に固定されており、この上下両
取付板2,2aの中心部には、取付板2上に載置
された駆動源3により駆動される回転軸4が、軸
受5,5を介して回転自在に支承されている。上
下取付板2,2a間の上部と下部とには、粉粒体
等の被乾燥物を収納して乾燥するための乾燥室9
を形成した乾燥筒81〜84の支持板6,6aが、
回転軸4に回転自在に軸支されている。
Reference numeral 1 denotes a pedestal, and mounting plates 2 and 2a are fixed horizontally to the upper and lower parts of the pedestal 1. At the center of both the upper and lower mounting plates 2 and 2a, there is a mount plate placed on the mounting plate 2. A rotating shaft 4 driven by a drive source 3 is rotatably supported via bearings 5, 5. A drying chamber 9 is provided at the upper and lower portions between the upper and lower mounting plates 2 and 2a for storing and drying materials to be dried such as powder and granules.
The support plates 6, 6a of the drying tubes 8 1 to 8 4 formed with
It is rotatably supported on a rotating shaft 4.

この支持板6,6aの同一円周上の等配位置に
は4個の貫通孔7が穿設され、垂直線上にある上
下1対の貫通孔7,7には強化ガラスや金属製等
の同一形状からなる乾燥筒81,82,83,84
4個等配位置に嵌め込まれている。各乾燥筒81
〜84の上下両端と取付板2,2aとの間には短
管10が取付けられており、各短管10は支持板
6,6a対面側にフランジ10aを形成するとと
もに、取付板2,2a対面側にはリング体11を
外嵌めし、リング体11一端とフランジ10aと
の間にはコイルバネ12を巻装している。従つ
て、対向した上下一対の短管10,10同士のコ
イルバネ12,12の弾発力により、各乾燥筒8
〜84を挾持するとともに、短管10のリング体
11を常時取付板2,2aに密着させ、しかも各
リング体11の端面11aが取付板2,2a対面
部に摺接しながら回転される。13はパツキンで
ある。
Four through holes 7 are bored at equal positions on the same circumference of the support plates 6, 6a, and a pair of upper and lower through holes 7, 7 on the vertical line are filled with reinforced glass, metal, etc. Four drying tubes 8 1 , 8 2 , 8 3 , and 8 4 having the same shape are fitted in equidistant positions. Each drying cylinder 8 1
Short pipes 10 are installed between the upper and lower ends of ~8 4 and the mounting plates 2, 2a, and each short pipe 10 forms a flange 10a on the opposite side of the support plates 6, 6a, and the mounting plates 2, A ring body 11 is externally fitted on the side facing 2a, and a coil spring 12 is wound between one end of the ring body 11 and the flange 10a. Therefore, each drying cylinder 8
1 to 8 4 are held, and the ring body 11 of the short pipe 10 is kept in close contact with the mounting plates 2, 2a at all times, and the end surface 11a of each ring body 11 is rotated while slidingly contacting the facing portion of the mounting plates 2, 2a. . 13 is Patsukin.

各乾燥筒81〜84の乾燥室9の下端近傍、つま
り実施例では短管10下端部には熱風受口14が
形成れている。これら熱風受口14…14の少な
くとも2つ以上の対応個所(実施例では4個所)
には、送風管15…15が取付板2aに取付けて
あり、該送風管15下端には接続管16が連結し
てある。各接続管16の先端は、バルブV1、V2
を介して熱源17に接続され、この熱源17の先
方には架台1下端部に固定した空気源18が接続
してある。
A hot air inlet 14 is formed near the lower end of the drying chamber 9 of each drying cylinder 8 1 to 8 4 , that is, in the lower end of the short tube 10 in the embodiment. At least two or more locations corresponding to these hot air outlets 14...14 (four locations in the example)
, air pipes 15...15 are attached to the mounting plate 2a, and a connecting pipe 16 is connected to the lower end of the air pipes 15. The tip of each connecting pipe 16 has valves V 1 and V 2 .
The air source 18 is connected to a heat source 17 via a heat source 17, and an air source 18 fixed to the lower end of the frame 1 is connected to the other side of the heat source 17.

上記取付板2には乾燥筒81上端に連結した短
管10に連通したフード28が接続され、このフ
ード28及び乾燥筒81〜84が少なくとも1つの
材料入口8の上流側には搬送管19を設け、この
搬送管19には切替弁20を介して材料供給管2
1と乾燥済み材料を排出する乾燥済材料排出管2
2とが連結されている。
A hood 28 communicating with the short pipe 10 connected to the upper end of the drying tube 8 1 is connected to the mounting plate 2, and the hood 28 and the drying tubes 8 1 to 8 4 are connected to the upstream side of at least one material inlet 8. A pipe 19 is provided, and a material supply pipe 2 is connected to this transport pipe 19 via a switching valve 20.
1 and a dried material discharge pipe 2 for discharging the dried material.
2 are connected.

乾燥筒81〜84…内への被乾燥物の供給は前記
材料供給管21を介して空気源の気力により行う
とともに、乾燥済みの被乾燥物の排出は乾燥済材
料排出管22を介して空気源の吸引力により排出
するようにする。一方、上記搬送管19と連通し
た乾燥筒81…内には該搬送管19をシリンダー
装置などで上下動動自在に嵌挿するとともに、搬
送管19の下端外周には蓋体35を設け、該蓋体
35の搬送管19下端接続部下面にはテーパー3
6を形成する一方、同乾燥筒81と短管10との
間には断面皿形状フイルター13を挾着してい
る。このような構成によれば、乾燥済み材料を乾
燥済材料排出管22より排出する場合に、蓋体3
5を下動できるため乾燥室9内の被乾燥物が残る
ことなく全量排出でき、特に乾燥室9の断面積が
大きい場合には有効である。そのほか、蓋体35
をフイルター33に近傍させたときに、両者3
5,33間に収容されている被乾燥物は蓋体35
のテーパー36とフイルタ33の凹部33aとの
間の隙間へ移動するから、被乾燥物のかみ込みが
解消でき、従つて清掃も容易である利点がある。
なお、短管10に送風管15の役割を持たせるよ
うに設計変更できる。
The material to be dried is supplied into the drying cylinders 8 1 to 8 4 by the air force of the air source through the material supply pipe 21, and the dried material is discharged through the dried material discharge pipe 22. and discharge by the suction force of the air source. On the other hand, the conveying tube 19 is fitted into the drying tube 8 1 communicating with the conveying tube 19 so as to be vertically movable by means of a cylinder device, and a lid 35 is provided on the outer periphery of the lower end of the conveying tube 19. A taper 3 is provided on the lower surface of the lid body 35 where the lower end of the transport pipe 19 is connected.
6, and a filter 13 having a dish-shaped cross section is clamped between the drying tube 81 and the short tube 10. According to such a configuration, when the dried material is discharged from the dried material discharge pipe 22, the lid body 3
5 can be moved downward, so that all the material to be dried in the drying chamber 9 can be discharged without remaining, which is particularly effective when the cross-sectional area of the drying chamber 9 is large. In addition, the lid body 35
When 3 is placed near the filter 33, both 3
The material to be dried stored between 5 and 33 is covered by the lid 35.
Since the drying material moves into the gap between the taper 36 and the recess 33a of the filter 33, it is possible to prevent the material to be dried from being caught in the drying material, which has the advantage of being easy to clean.
Note that the design can be changed so that the short pipe 10 has the role of the blower pipe 15.

送風管15は実施例の如く熱風受口14と同数
設けられるが、2つ以上なら任意に選定できる。
Although the number of blower pipes 15 is the same as the number of hot air outlets 14 as in the embodiment, two or more can be arbitrarily selected.

各熱風受口14を回転しながら順次に送風管1
5に連通させる方法としては、図示しないがシリ
ンダ装置によつて送風管15を上下動させて行つ
てもよく、その構造を問わない。
While rotating each hot air outlet 14, the blower pipe 1 is
Although not shown, the method for communicating with the air pipe 5 may be to move the air pipe 15 up and down using a cylinder device, and the structure thereof is not limited.

乾燥筒82、83、84上端に連結した短管10,
10,10には、排気管23が連通され同排気管
23は1つの排気口23aより排気されるように
してある。
Short pipes 10 connected to the upper ends of the drying tubes 8 2 , 8 3 , 8 4 ,
10, 10 are connected to an exhaust pipe 23, and the exhaust pipe 23 is configured to be exhausted from one exhaust port 23a.

そして、この排気口23aよりの排気は直ちに
外部に排出させてもよいが、この実施例では第3
図示の如く接続管24を連結し、該接続管24は
フイルター25、外気取入調節部28及びバルブ
V4を介して空気源18に接続する一方、バルブ
V4の後方位置には今1つの接続管27をバルブ
V3を介して乾燥筒81下方の接続管16に連結し
ている。各乾燥筒82〜84に通された熱風は、排
気管23、接続管24、空気源18を経て熱源1
7まで循環させ、熱源の熱効率を高めるようにし
ている。
The exhaust from this exhaust port 23a may be immediately discharged to the outside, but in this embodiment, the third
A connecting pipe 24 is connected as shown in the figure, and the connecting pipe 24 includes a filter 25, an outside air intake adjustment section 28, and a valve.
Connect to air source 18 via V 4 while valve
There is now one connecting pipe 27 in the rear position of V 4 as a valve.
It is connected to the connecting pipe 16 below the drying cylinder 8 1 via V 3 . The hot air passed through each of the drying tubes 8 2 to 8 4 passes through the exhaust pipe 23 , the connecting pipe 24 , and the air source 18 to the heat source 1 .
7 to increase the thermal efficiency of the heat source.

上部支持板6の外周部にはリードスイツチ28
の感知部材28aを取付ける一方、架台1内側に
は90゜間隔をおいてスイツチブラケツト28
b4個を取付け、各乾燥室9(乾燥筒8)を回転
したときに、感知部材28aがスイツチブラケツ
ト28bに嵌合すると、該乾燥室9が位置決めさ
れる。この位置決めは順次に周期的に行われる。
つまり、各乾燥室9を回転すると、各乾燥室9の
熱風受口14が順次に(この実施例では90゜ごと
に)各送風管15に周期的に連通される。各乾燥
室9に供給された粉粒体を下流から上流に向けた
熱風により流動乾燥するようにしている。
A reed switch 28 is installed on the outer periphery of the upper support plate 6.
The sensing member 28a is installed, while the switch bracket 28 is installed at a 90° interval inside the pedestal 1.
When the four drying chambers 9 (drying tubes 8) are rotated and the sensing member 28a is fitted into the switch bracket 28b, the drying chamber 9 is positioned. This positioning is performed sequentially and periodically.
That is, when each drying chamber 9 is rotated, the hot air inlet 14 of each drying chamber 9 is periodically communicated with each blast pipe 15 sequentially (every 90 degrees in this embodiment). The powder and granular material supplied to each drying chamber 9 is fluidized and dried by hot air directed from downstream to upstream.

なお、30は乾燥筒82,83,84に収容した
被乾燥物が排気管23へ飛び出すのを防止するフ
イルター、31はキー、32は光電管または近傍
スイツチ等のレベル計であつて、材料のレベル量
を検知する。33は多層からなる焼結フイルタ
ー、34はナツトである。
In addition, 30 is a filter that prevents the materials to be dried stored in the drying tubes 8 2 , 8 3 , 8 4 from jumping out into the exhaust pipe 23, 31 is a key, and 32 is a level meter such as a phototube or a nearby switch. Detects the level amount of material. 33 is a multilayer sintered filter, and 34 is a nut.

また、前記送風管15は2つ以上の乾燥室9…
9に送風するように設けるとともに、その送風管
15に供給する熱風には温度差を設けてある。こ
れにより、既述したように、乾燥温度の異なる2
つ以上の材料を乾燥できるほか、乾燥しようとす
る樹脂材料の通常の乾燥温度よりも高い温度で乾
燥させた後、通常の乾燥温度程度の冷却温度に戻
すことにより、材料がより一層短時間で乾燥でき
るなどの利点がある。
Further, the air pipe 15 is connected to two or more drying chambers 9...
The hot air supplied to the blast pipe 15 is provided with a temperature difference. As a result, as mentioned above, two
In addition to drying more than one material, the material can be dried in a shorter time by drying at a temperature higher than the normal drying temperature of the resin material to be dried and then cooling it back to the normal drying temperature. It has the advantage of being dry.

この実施例の乾燥筒8つまり乾燥室9は4つ設
けているが、2つ以上なら任意採用できる。
Although four drying tubes 8, that is, four drying chambers 9 are provided in this embodiment, two or more can be arbitrarily employed.

前記空気源18は小容量のもので熱源17の送
風のみを行わせ、材料の供給と排出は別設の空気
源によつて行うような構成もできる。
The air source 18 may have a small capacity and only blow air from the heat source 17, and the supply and discharge of materials may be performed by a separate air source.

なお、この実施例の乾燥装置は架台1に固定す
る構成としたが、成形機に直接載架する構成もと
り得る。
Note that although the drying device in this embodiment is configured to be fixed to the pedestal 1, it may also be configured to be directly mounted on the molding machine.

この実施例の作用を第3図に基づいて以下に説
明すると、今、乾燥筒81へ材料を供給した場合、
バルブV1に閉、バルブV2は開で乾燥筒82,83
4に熱源17の熱風を送り込み乾燥中であり、
その使用済み熱風はフイルター25を通つてから
バルブV4が閉じているため一時滞留し、バルブ
V3は開である。
The operation of this embodiment will be explained below based on FIG. 3. If material is now supplied to the drying cylinder 81 ,
Valve V 1 is closed, valve V 2 is open and drying tubes 8 2 , 8 3 ,
8 4 is being dried by sending hot air from heat source 17,
Since the used hot air passes through the filter 25 and valve V 4 is closed, it temporarily stagnates and passes through the valve.
V 3 is open.

次に、乾燥筒81へ材料が供給し終わると、該
乾燥筒81の乾燥室9でも熱風乾燥が開始される。
すなわち、このときバルブV1はレベル計と連動
して開となり、熱源17よりの加熱空気が空気源
18で同乾燥筒81内に送風され同乾燥室9内の
粉粒体を乾燥させる。一方、バルブV2も開弁中
で乾燥筒82,83,84の粉粒体も乾燥され、該
乾燥筒82,83,84内で使用済の熱風は、バル
ブV4が開、バルブV3が閉となつているため、空
気源18を経て熱源17に通され再利用される。
Next, when the material is completely supplied to the drying tube 8 1 , hot air drying is also started in the drying chamber 9 of the drying tube 8 1 .
That is, at this time, the valve V 1 is opened in conjunction with the level meter, and heated air from the heat source 17 is blown into the drying cylinder 8 1 by the air source 18 to dry the powder and granular material in the drying chamber 9 . On the other hand, the valve V 2 is also open, and the powder and granules in the drying cylinders 8 2 , 8 3 , 8 4 are also dried, and the hot air used in the drying cylinders 8 2 , 8 3 , 8 4 is transferred to the valve V 4 . is open and valve V3 is closed, the air is passed through the air source 18 to the heat source 17 and reused.

乾燥筒81内で粉粒体が所定水分まで完全に乾
燥し終わると、バルブV1は開、バルブV2は閉、
バルブV3は閉、バルブV4は開となるため、同図
での乾燥筒81内の粉粒体だけが、バルブV1と接
続した接続管16及び送風管15を介して空気源
18と熱源17とによる熱風で搬送管19及び乾
燥済材料排出管22より系外に排出される。この
排出された乾燥済の粉粒体は成形機(図示せず)
などに送り込まれる。乾燥筒82,83,84も前
記乾燥筒81と同位置に来たときに、前記と同様
の作用が行われる。
When the powder and granules are completely dried to a predetermined moisture content in the drying cylinder 8 1 , the valve V 1 is opened, the valve V 2 is closed,
Since the valve V 3 is closed and the valve V 4 is open, only the powder inside the drying tube 8 1 in the figure is sent to the air source 18 via the connecting pipe 16 and the blower pipe 15 connected to the valve V 1 . The heated air generated by the heat source 17 is discharged out of the system through the conveying pipe 19 and the dried material discharge pipe 22. This discharged dried powder is transferred to a molding machine (not shown).
etc. will be sent to. When the drying tubes 8 2 , 8 3 , and 8 4 also come to the same position as the drying tube 8 1 , the same effect as described above is performed.

なお、実施例において、熱源17よりの加熱空
気を空気源18で各乾燥室9に送り込んで乾燥し
た後に排出される熱風を再循環させる場合に、そ
の循環ラインには、冷却器と除湿ユニツトとを取
り付けるとか、別説の空気源と連結した予備ヒー
タの予熱源を取り付け、予熱源の予備熱を少なく
とも1つ以上の乾燥室9に供給するとか、その他
種々設計変更することができる。
In addition, in the embodiment, when the heated air from the heat source 17 is sent into each drying chamber 9 by the air source 18 and the hot air discharged after drying is recirculated, the circulation line is equipped with a cooler and a dehumidifying unit. Various other design changes can be made, such as attaching a preheating source for a preheater connected to an air source described elsewhere, and supplying preliminary heat from the preheating source to at least one or more drying chambers 9.

〔発明の効果〕〔Effect of the invention〕

この発明によれば、(1) 乾燥筒の少なくとも1
つの材料入口の上流側には搬送管を設け、この搬
送管には切替弁20を介して材料供給管21と乾
燥済材料排出管とを接続し、乾燥筒内への被乾燥
物の供給は前記材料供給管を介して空気源の気力
により行うとともに、乾燥済みの被乾燥物の排出
は乾燥済材料排出管を介して空気源の吸引力によ
り排出するようにしているから、切替弁を切り替
えるだけで、空気源の気力により、各乾燥筒内へ
被乾燥物が自動的に連続して供給できるととも
に、同乾燥筒内での乾燥済材料の排出も同様に自
動的に連続して行える。
According to this invention, (1) at least one of the drying tubes
A transport pipe is provided upstream of the two material inlets, and a material supply pipe 21 and a dried material discharge pipe are connected to this transport pipe via a switching valve 20, and the material to be dried is supplied into the drying cylinder. This is done by the air force of the air source through the material supply pipe, and the dried material is discharged by the suction force of the air source through the dried material discharge pipe, so the switching valve is switched. With this, the material to be dried can be automatically and continuously supplied into each drying cylinder by the energy of the air source, and the dried material can also be automatically and continuously discharged from the drying cylinders.

(2) しかも、搬送管と連通した乾燥筒内には該
搬送管を上下動自在に嵌挿するとともに、搬送管
の下端外周には蓋体を設け、同乾燥筒と短管との
間にはフイルターを挾着してなることから、乾燥
済材料の排出時には、搬送管の蓋体を材料の嵩に
応じて適宜上下動することにより、当該乾燥室内
の材料が残留することがなく完全に排出され、材
料替えの際などにおいて乾燥室内の清掃が不要と
なる顕著な効果がある。
(2) Moreover, the conveying tube is inserted into the drying tube that communicates with the conveying tube so that it can move up and down, and a lid is provided on the outer periphery of the lower end of the conveying tube, and a lid is provided between the drying tube and the short tube. Since the drying chamber is equipped with a filter, when discharging the dried material, the lid of the conveying pipe can be moved up and down as appropriate depending on the volume of the material, so that no material remains in the drying chamber and is completely removed. This has the remarkable effect of eliminating the need to clean the inside of the drying chamber when changing materials.

(3) さらに、複数の乾燥室を一こまづつ回転し
て、乾燥位置において被乾燥物を乾燥室の下方か
ら上方に向けていわゆる流動乾燥する構成を採り
ながら、送風管は2つ以上の乾燥室に送風するよ
うに設けてその送風管に供給する熱風には温度差
を設けてあることから、従来例(イ),(ロ)のものに比
べ、本発明は、乾燥処理中に被乾燥物たる粉粒体
が団魂を形成したり、付着したりすることがない
のは勿論のこと、所望の加熱温度を選択すること
により、乾燥温度の異なる2つ以上の被乾燥物を
乾燥することができる。また、例えば、第1乾燥
室では110℃、第2乾燥室では150℃、第3乾燥室
では100℃の如く、当該樹脂材料の通常の乾燥温
度で乾燥してから、その通常の乾燥温度よりも高
い温度で乾燥させた後に、通常の乾燥温度又はそ
れより少し低温の冷却温度に戻す工程を採ること
もできる。さらには、乾燥温度の異なる粉粒体等
を、それぞれ所望温度の乾燥室に供給して、乾燥
しつつ混合することにより混合材料を得るように
することもできる。
(3) Furthermore, while the plurality of drying chambers are rotated one by one and the material to be dried is dried in a so-called fluidized manner from the bottom of the drying chamber to the top at the drying position, the air pipes are connected to two or more drying chambers. Compared to the conventional examples (a) and (b), the present invention has a temperature difference in the hot air supplied to the blower pipe, so that the drying material is not heated during the drying process. It goes without saying that the powder particles do not form clusters or stick together, and by selecting the desired heating temperature, two or more objects to be dried with different drying temperatures can be dried. I can do it. Furthermore, after drying at the normal drying temperature of the resin material, such as 110°C in the first drying room, 150°C in the second drying room, and 100°C in the third drying room, It is also possible to adopt a step of drying at a high temperature and then returning the temperature to a normal drying temperature or a slightly lower cooling temperature. Furthermore, it is also possible to obtain a mixed material by supplying powder or granules having different drying temperatures to drying chambers each having a desired temperature and mixing them while drying.

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

図はいずれもこの発明の一実施例を示す。第1
図は縦断面図、第2図は平面図、第3図はフロー
シート図、第4図は乾燥筒及び短管の一部の拡大
縦断面図である。 3…駆動源、81,82,83,84…乾燥筒、9
…乾燥室、14…熱風受口、15…送風管、17
…熱源、18…空気源、19…搬送管、20…切
替弁、21…材料供給管、22…乾燥済材料排出
管、23…排気管。
Each figure shows an embodiment of the present invention. 1st
2 is a plan view, FIG. 3 is a flow sheet diagram, and FIG. 4 is an enlarged longitudinal sectional view of a part of the drying tube and short tube. 3... Drive source, 8 1 , 8 2 , 8 3 , 8 4 ... Drying cylinder, 9
...Drying room, 14...Hot air inlet, 15...Air pipe, 17
... heat source, 18 ... air source, 19 ... conveyance pipe, 20 ... switching valve, 21 ... material supply pipe, 22 ... dried material discharge pipe, 23 ... exhaust pipe.

Claims (1)

【特許請求の範囲】 1 駆動源3により回転される回転軸4の等配位
置に2つ以上の乾燥筒81,82…を回転自在に設
けるとともに、各乾燥筒81,82…の下端近傍に
は熱風受口14を形成し、この熱風受口14の対
応個所には熱源17と接続した送風管15を固設
し、各乾燥筒81,82…の回転につれ各乾燥筒8
,82…の熱風受口14が順次に前記送風管15
に連通され、前記送風管15…は2つ以上の乾燥
筒81,82…に同時に連通するように設けるとと
もに、その送風管15…に供給する熱風には温度
差を設け、各乾燥筒9に供給された被乾燥物を下
方から上方に向けた熱風により流動乾燥するよう
にしてなる粉粒体等の乾燥装置であつて、 前記乾燥筒81,82…の少なくとも1つの材料
入口8の上流側には搬送管19を設け、この搬送
管19には切替弁20を介して材料供給管21と
乾燥済材料排出管22とを接続し、乾燥筒81
2…内への被乾燥物の供給は前記材料供給管2
1を介して空気源の気力により行うとともに、乾
燥済みの被乾燥物の排出は乾燥済材料排出管22
を介して空気源の吸引力により排出するようにす
る一方、 上記搬送管19と連通した乾燥筒81…内には
該搬送管19を上下動自在に嵌挿するとともに、
搬送管19の下端外周には蓋体35を設け、同乾
燥筒81…と短管10との間にはフイルター33
を挾着してなることを特徴とする粉粒体等の乾燥
装置。
[Scope of Claims] 1. Two or more drying tubes 8 1 , 8 2 . A hot air socket 14 is formed near the lower end of the cylinder, and a blow pipe 15 connected to a heat source 17 is fixed at a corresponding position of the hot air socket 14. As each drying cylinder 8 1 , 8 2 . Tube 8
The hot air inlets 14 of 1 , 8 2 . . .
The blast pipes 15 are provided so as to communicate simultaneously with two or more drying tubes 8 1 , 8 2 . A drying device for powder and granular materials, etc., configured to fluidize and dry the material to be dried supplied to the drying cylinders 8 1 , 8 2 . . . by means of hot air directed upward from below. A conveying pipe 19 is provided on the upstream side of the drying cylinder 8 , and a material supply pipe 21 and a dried material discharge pipe 22 are connected to this transport pipe 19 via a switching valve 20 .
8 2 The material to be dried is supplied into the material supply pipe 2.
1, and the dried material is discharged through the dried material discharge pipe 22.
The drying cylinder 8 1 communicates with the conveying pipe 19, and the conveying pipe 19 is inserted into the drying cylinder 8 1 so as to be vertically movable.
A lid 35 is provided on the outer periphery of the lower end of the conveying pipe 19, and a filter 33 is provided between the drying cylinder 8 1 and the short pipe 10.
A drying device for powder and granular materials, etc., characterized in that it is made by clamping .
JP1338083A 1983-01-29 1983-01-29 Drier for powdered and granular body Granted JPS59138878A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1338083A JPS59138878A (en) 1983-01-29 1983-01-29 Drier for powdered and granular body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1338083A JPS59138878A (en) 1983-01-29 1983-01-29 Drier for powdered and granular body

Publications (2)

Publication Number Publication Date
JPS59138878A JPS59138878A (en) 1984-08-09
JPH0416697B2 true JPH0416697B2 (en) 1992-03-24

Family

ID=11831486

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1338083A Granted JPS59138878A (en) 1983-01-29 1983-01-29 Drier for powdered and granular body

Country Status (1)

Country Link
JP (1) JPS59138878A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5371362A (en) * 1976-12-08 1978-06-24 Matsui Osamu Method of drying synthetic resin

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5371362A (en) * 1976-12-08 1978-06-24 Matsui Osamu Method of drying synthetic resin

Also Published As

Publication number Publication date
JPS59138878A (en) 1984-08-09

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