JPS61107082A - Drier - Google Patents
DrierInfo
- Publication number
- JPS61107082A JPS61107082A JP22783984A JP22783984A JPS61107082A JP S61107082 A JPS61107082 A JP S61107082A JP 22783984 A JP22783984 A JP 22783984A JP 22783984 A JP22783984 A JP 22783984A JP S61107082 A JPS61107082 A JP S61107082A
- Authority
- JP
- Japan
- Prior art keywords
- drying
- vacuum
- container
- type
- ribbon
- 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
Links
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- Drying Of Solid Materials (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)
本発明は真空状態で粉粒体全力ロ熱乾燥する装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to an apparatus for drying powder and granular materials under full blast heat in a vacuum state.
(従来の技術)
粉粒体の攪拌、混合、乾燥装置としては大別して容器回
転型と固定容器混合型の2種がある。(Prior Art) Apparatuses for stirring, mixing, and drying powder and granular materials can be roughly divided into two types: a rotating container type and a fixed container mixing type.
第2図は容器回転型の代表としてV型混合機1全示すも
のであり、上部2ケ所の装入口2より材料装入全行い、
交錯部5より排出する方式であるが、粘着性や加熱する
と軟化浴融性′?c有するものには適用困難であるため
、固定容器混合型が多用されている。Figure 2 shows the entire V-type mixer 1 as a representative of the container rotating type, and all materials are charged from the two charging ports 2 at the top.
The method is to discharge from the intersecting part 5, but the softening bath may be sticky or meltable when heated. Since it is difficult to apply to those with c.c., a fixed container mixing type is often used.
第3図はナラター型ミキサーと呼ばれている ′もの
であり、容器1の内部に設置されたスクリュー4が自転
公転を行いつつ粉粒体全混合する方式であるが、外壁面
に加熱手段(例えば高温熱媒油が流れるジャケット)全
設け、且つ真空状態に保持する真空乾燥器に利用するこ
とも可能である。然し乍ら自転軸と公転軸の二軸シール
が難しく高真空下で運転することは無理が有る。なお、
図中、5は排出口である。Figure 3 shows a so-called narrator type mixer, in which a screw 4 installed inside the container 1 rotates around its axis and mixes all the powder and granules. For example, it is also possible to use it in a vacuum dryer that is completely equipped with a jacket (for example, a jacket through which high-temperature heat transfer oil flows) and is maintained in a vacuum state. However, it is difficult to seal the two shafts of rotation and revolution, making it impossible to operate under high vacuum. In addition,
In the figure, 5 is a discharge port.
又第4図は容器1内部中心にスクリュー4を設けたファ
ウンテンミキサーであるが壁面加熱方式で真空乾燥機に
使う場合、内壁面に粘着するような物質には伝熱が悪く
適用するには大型化する欠点がある。Fig. 4 shows a fountain mixer with a screw 4 installed in the center of the container 1, but when using the wall heating method in a vacuum dryer, heat transfer is poor and the mixer is too large to be applied to materials that stick to the inner wall. There are drawbacks to becoming
(発明が解決しようとする問題点)
発明者らは1000〜2000 ppmの内部水分を含
むポリエステル樹脂ベレットヲ残存水分10 ppm以
下に乾燥する装置について検討した結果、通常の大気圧
下での加熱乾燥では加水分解による重合度低下が大きく
実用的でない事より、真空下で加熱乾燥する装置につい
て鋭X研究に努めた。ポリエステルは約110℃の結晶
化温度を有するため、加熱して行くとこの付近で粘着性
が現われ、加熱面に付層する事より、1トール付近の高
真空に維持し、ペレツ)’(f−壁面に付層させる事な
く且つ、器内に停滞部分全作らない高効率X空乾燥装置
の開発ケ目的とするものである。(Problems to be Solved by the Invention) The inventors investigated an apparatus for drying polyester resin pellets containing internal moisture of 1,000 to 2,000 ppm to a residual moisture of 10 ppm or less, and found that heating drying under normal atmospheric pressure does not Since the degree of polymerization decreases significantly due to hydrolysis, making it impractical, we conducted extensive research into a device that heats and dries under vacuum. Polyester has a crystallization temperature of about 110°C, so when it is heated, it becomes sticky around this point, and by attaching a layer to the heated surface, it is maintained at a high vacuum of around 1 Torr and pellets are formed. - The purpose is to develop a highly efficient X-air drying device that does not create a layer on the wall and does not create any stagnation inside the container.
(問題点全解決するための手段)
本発明は、円錐型の竪型固定容器の、内部中心にリボン
型攪拌羽根を設置した事で回転軸からのリーク防止全可
能にし、高真空保持を容易にした事及びペレットの動き
が周壁面全上昇し、内部中心を下降することになり、熱
交換が効率良く行なわれ、更に壁面への付着や停滞部全
解消したことケ特徴とするものである。(Means for solving all problems) The present invention has a ribbon-type stirring blade installed in the center of the interior of a conical vertical fixed container, making it possible to completely prevent leakage from the rotating shaft and easily maintaining a high vacuum. This is characterized by the fact that the pellets move all the way up on the peripheral wall and down at the center of the inside, which allows for efficient heat exchange, and also completely eliminates adhesion to the wall and stagnation. .
すなわち本発明は粉粒体’(rX空状態下で71fl熱
乾燥する装置において、本体を竪型円錐形状とし、内部
に複数のリボン状撹拌羽根會設けlてなることを特徴と
する乾燥装置でおる。That is, the present invention relates to a drying apparatus for thermally drying 71 fl of powder or granular material (r is.
本発明は、粉粒体の混合装置、乾燥装置として有利に適
用することができる。The present invention can be advantageously applied as a mixing device and a drying device for powder and granular materials.
以下、本発明の一夾施態様全第1図に従って詳述する。Hereinafter, one embodiment of the present invention will be described in detail with reference to FIG.
第1図はポリエステルペレットの真空乾燥装置に適用し
た例を示すものである。第1図において、1は竪型円錐
状の乾燥機本体、2は攪拌用の軸であり、これにリボン
状の攪拌羽根3が固定されている。なお、この攪拌軸2
は上下にスライドしうるように設けることが好ましい。FIG. 1 shows an example in which the present invention is applied to a vacuum drying apparatus for polyester pellets. In FIG. 1, 1 is a vertical conical dryer main body, 2 is a stirring shaft, and a ribbon-shaped stirring blade 3 is fixed to this. Note that this stirring shaft 2
It is preferable to provide it so that it can slide up and down.
4は加熱媒体が流れるジャケットであり、入口ノズル5
、出口ノズル6ケ有する。7は原料ペレットの装入口、
8は製品排出用弁であり、弁体9全エアシリンダ11で
駆動する機構になっている。又弁棒12からの漏れ防止
のため金属ベロー10でシールしている。13は真空弁
、14は真空発生源(図示してない)に続いている排気
口、15.18Fiシ一ル機構16は攪拌用′電動機1
7を支持する架台である。4 is a jacket through which the heating medium flows, and an inlet nozzle 5
, has 6 outlet nozzles. 7 is a charging port for raw material pellets;
Reference numeral 8 denotes a product discharge valve, and the valve body 9 is entirely driven by an air cylinder 11. Further, to prevent leakage from the valve stem 12, it is sealed with a metal bellows 10. 13 is a vacuum valve, 14 is an exhaust port connected to a vacuum source (not shown), and 15.18 Fi seal mechanism 16 is an electric motor 1 for stirring.
This is a pedestal that supports 7.
(作用)
原料ペレットは装入ロアより乾燥機1の中に投入される
。乾燥機1は予じめカロ熱媒体全入ロノズル5より出口
ノズル6へ流して所定温度に加熱しておき、攪拌羽根5
も電動機17で所定回転数で回転しておく。(Operation) Raw material pellets are charged into the dryer 1 from the charging lower. The dryer 1 is heated in advance to a predetermined temperature by flowing the heat medium from the fully filled nozzle 5 to the outlet nozzle 6, and then the stirring blade 5
The motor 17 also rotates at a predetermined rotation speed.
排出弁8も閉状態にしておき、原料投入が終ったのち、
装入ロア全閉じたのち、約1トールの真空に吸引し所定
時間攪拌混合して乾燥させる。The discharge valve 8 is also kept closed, and after the raw materials have been input,
After the charging lower is completely closed, the mixture is vacuumed to about 1 Torr and stirred and mixed for a predetermined period of time to dry.
乾燥終了后系内全大気圧に開放し下部の製品排出弁8を
開けて系外の製品タンク(図示してない)に回収する。After drying, the system is released to full atmospheric pressure, the product discharge valve 8 at the bottom is opened, and the product is collected in a tank (not shown) outside the system.
(効果〕
竪型円錐状の混合槽の中にリボン状の攪拌羽根を配設し
た効果として
fil lJn熱壁面への原料の付着防止が図れ、熱
伝達率が同上する。(Effects) As an effect of arranging the ribbon-shaped stirring blades in the vertical conical mixing tank, it is possible to prevent the raw materials from adhering to the heating wall surface, and the heat transfer coefficient is increased.
(2) 原料σ壁面を上昇し、中心部全降下する流動
様式となり、上に行くほど断面積が増加するため、半径
方向の粒子混合が促進され、従来のファウンテン式より
熱伝達率が飛躍的に大きくなる。(2) The flow pattern is such that the raw material σ rises up the wall surface and descends completely at the center, and the cross-sectional area increases as it goes up, promoting particle mixing in the radial direction and dramatically increasing the heat transfer coefficient compared to the conventional fountain type. becomes larger.
(3) 層内に動きの悪い停滞部が存在しなくなり、
製品の品質にバラつきが無い。(3) There are no sluggish areas within the layer,
There is no variation in product quality.
(41円錐状であるため製品の排出が容易であり、多種
類の原料全処理する時、異種製品間の汚染が起らない。(41) Because of its conical shape, it is easy to discharge the product, and there is no contamination between different types of products when processing all kinds of raw materials.
(5) ナラター型に比べ一軸シールであり、真壁保
持は通常のメカニカルシールで充分対応できる。(5) Compared to the Narrator type, this is a uniaxial seal, and regular mechanical seals can be used to maintain true walls.
(6)攪拌軸を上下に移動することでリボン羽根と壁面
との隙間調整が簡単容易に行える。(6) By moving the stirring shaft up and down, the gap between the ribbon blade and the wall surface can be easily adjusted.
従って極めて付N性の強いものでも処理でき、応用分野
が拡大される。Therefore, even materials with extremely strong N-binding properties can be processed, expanding the field of application.
第1図は本発明装置の一実施態様金示す概略図、第2図
〜第4図は従来の各種乾燥装置を示す概略図である。
復代理人 内 1) 明
復代理人 萩 原 亮 −
特開昭G1−107082(3)
第2図
第3図FIG. 1 is a schematic diagram showing one embodiment of the apparatus of the present invention, and FIGS. 2 to 4 are schematic diagrams showing various conventional drying apparatuses. Sub-Agent 1) Meifu Agent Ryo Hagiwara - JP-A-1-107082 (3) Figure 2 Figure 3
Claims (1)
を竪型円錐形状とし、内部に複数のリボン状攪拌羽根を
設けてなることを特徴とする乾燥装置。What is claimed is: 1. A drying device for heating and drying powder and granular materials under vacuum conditions, characterized in that the main body has a vertical conical shape, and a plurality of ribbon-shaped stirring blades are provided inside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22783984A JPS61107082A (en) | 1984-10-31 | 1984-10-31 | Drier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22783984A JPS61107082A (en) | 1984-10-31 | 1984-10-31 | Drier |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61107082A true JPS61107082A (en) | 1986-05-24 |
JPH0231303B2 JPH0231303B2 (en) | 1990-07-12 |
Family
ID=16867171
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22783984A Granted JPS61107082A (en) | 1984-10-31 | 1984-10-31 | Drier |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61107082A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0319501U (en) * | 1989-07-05 | 1991-02-26 | ||
JP2011075193A (en) * | 2009-09-30 | 2011-04-14 | Kumeta Seisakusho:Kk | Drying device |
CN104930847A (en) * | 2015-07-15 | 2015-09-23 | 南京高捷轻工设备有限公司 | Wet solid material feeding device with pre-drying function and pre-drying feeding method thereof |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001249491A (en) * | 2001-02-19 | 2001-09-14 | Nippon Zeon Co Ltd | Toner and method of manufacturing the same |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60159578A (en) * | 1984-01-30 | 1985-08-21 | 東レ株式会社 | Vacuum drier and method of operating said drier |
-
1984
- 1984-10-31 JP JP22783984A patent/JPS61107082A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60159578A (en) * | 1984-01-30 | 1985-08-21 | 東レ株式会社 | Vacuum drier and method of operating said drier |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0319501U (en) * | 1989-07-05 | 1991-02-26 | ||
JP2011075193A (en) * | 2009-09-30 | 2011-04-14 | Kumeta Seisakusho:Kk | Drying device |
CN104930847A (en) * | 2015-07-15 | 2015-09-23 | 南京高捷轻工设备有限公司 | Wet solid material feeding device with pre-drying function and pre-drying feeding method thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH0231303B2 (en) | 1990-07-12 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
EXPY | Cancellation because of completion of term |