JPH0759281B2 - Thin film evaporator - Google Patents

Thin film evaporator

Info

Publication number
JPH0759281B2
JPH0759281B2 JP63240390A JP24039088A JPH0759281B2 JP H0759281 B2 JPH0759281 B2 JP H0759281B2 JP 63240390 A JP63240390 A JP 63240390A JP 24039088 A JP24039088 A JP 24039088A JP H0759281 B2 JPH0759281 B2 JP H0759281B2
Authority
JP
Japan
Prior art keywords
rotary shaft
evaporation
thin film
container body
bearing
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 - Fee Related
Application number
JP63240390A
Other languages
Japanese (ja)
Other versions
JPH0299101A (en
Inventor
忠成 山崎
裕利 半田
Original Assignee
神鋼パンテック株式会社
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 神鋼パンテック株式会社 filed Critical 神鋼パンテック株式会社
Priority to JP63240390A priority Critical patent/JPH0759281B2/en
Publication of JPH0299101A publication Critical patent/JPH0299101A/en
Publication of JPH0759281B2 publication Critical patent/JPH0759281B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、重合反応により生成した高分子樹脂の如き高
粘度液材料から残留するモノマー、溶剤等の揮発性成分
を蒸発除去して精製された蒸発処理液を得る等の目的に
使用される薄膜蒸発装置の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention is purified by evaporating and removing volatile components such as residual monomers and solvents from a high-viscosity liquid material such as a polymer resin produced by a polymerization reaction. The present invention relates to improvement of a thin film evaporation device used for the purpose of obtaining an evaporation treatment liquid.

〔従来の技術〕[Conventional technology]

第3図は、従来技術の強制攪拌薄膜化蒸発機の1例を示
す。
FIG. 3 shows an example of a prior art forced agitation thin film evaporator.

この装置は、中心縦軸線(X)のまわりに円形の密閉式
容器本体(1)の内周面(2)を外側のジャケット
(3)に熱媒ノズル(4)(5)を経て熱媒を通ずるこ
とにより加熱蒸発面とし、揮発性成分蒸気の蒸気出口ノ
ズル(6)を器外の凝縮器を経て真空化源(図示せず)
に接続することにより器内の減圧、真空化を可能とし、
中心縦軸線(X)上に回転軸(7)を容器本体上部を貫
通する上部のシール付軸受(8)と下部の器内軸受
(9)により回転支承して器外上部のモータ(図示せ
ず)により回転駆動されるようにし、器内の回転軸
(7)の上位に取付けた分散ユニット(10)により液材
料入口ノズル(11)から器内に供給される液材料を内周
面の全周に分散し、続いてその下位に取付けた薄膜化ユ
ニット(12)の攪拌翼(13)により下降する分散液材料
を加熱蒸発面上に薄膜状に展開させて揮発性成分の蒸発
の促進を図り、その蒸気を蒸気出口ノズル(6)から排
出し、一方蒸発を完了した蒸発処理液は容器本体下部の
処理液取出口(14)からギヤーポンプ(15)等の排出手
段により抜き出すようになっている。(16)は下部器内
軸受(9)を器内壁から支持するサポートで、器内を横
断する。
This device is configured such that the inner peripheral surface (2) of a circular closed container body (1) around the central longitudinal axis (X) is connected to the outer jacket (3) through the heat medium nozzles (4) and (5). A vaporization source (not shown) through a vapor outlet nozzle (6) for volatile component vapor through an external condenser through a vaporization nozzle as a heating evaporation surface.
By connecting to, it is possible to reduce the pressure and vacuum inside the container,
The rotary shaft (7) is rotatably supported by the upper sealed bearing (8) and the lower internal bearing (9) penetrating the upper part of the container main body on the central vertical axis (X) to support the motor (not shown) on the external upper part. No.), the liquid material supplied from the liquid material inlet nozzle (11) to the inside of the container by the dispersion unit (10) mounted above the rotary shaft (7) inside the container Disperse liquid material that is dispersed around the entire circumference and then descends by the stirring blade (13) of the thin film formation unit (12) installed in the lower part to spread it in a thin film on the heating evaporation surface to promote evaporation of volatile components. The vapor is discharged from the vapor outlet nozzle (6), while the vaporized treatment liquid that has completed evaporation is discharged from the treatment liquid outlet (14) at the bottom of the container body by a discharge means such as a gear pump (15). ing. Reference numeral (16) is a support for supporting the lower inner bearing (9) from the inner wall of the inner vessel and traverses the inner side of the vessel.

一般にこの種で薄膜蒸発装置は、減圧雰囲気のもとで液
静圧を薄膜化により小さくして蒸発を行わせるので蒸発
温度を低くでき、液材料の受ける熱影響を少なくし、ま
た薄膜の攪拌、掻下げ下方移送が攪拌翼により薄膜化に
伴ってなされるので、粘度の高い液材料も取扱える特長
を持つ。
Generally, in this type of thin-film evaporator, the static liquid pressure is reduced by thinning the film in a depressurized atmosphere to cause evaporation, so the evaporation temperature can be lowered, the thermal effect on the liquid material is reduced, and the thin film is agitated. Since the scraping and downward transfer is performed by the stirring blade as the film becomes thin, it has the feature that it can handle liquid materials with high viscosity.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかし。従来技術の薄膜蒸発装置は、液材料が高粘度化
するに伴って、次の諸困難があらわれる顕著化する。
However. In the conventional thin film evaporator, the following various problems are prominent as the liquid material becomes highly viscous.

すなわち、下部器内軸受(9)は半径方向に器内を横断
するサポート(16)により器内壁に支持されているの
で、器内壁面を伝って降下して来る高粘度の蒸発処理液
がサポートに付着堆積し、この堆積物が攪拌翼(13)に
接触するようになると、回転系の機械的なアンバランス
を生ずる原因となり、連続運転が不可能となる。
That is, since the lower vessel bearing (9) is supported on the vessel inner wall by the support (16) that traverses the vessel in the radial direction, the high viscosity evaporative treatment liquid that descends along the vessel inner wall surface is supported. If the deposit adheres to and is brought into contact with the stirring blade (13), it causes mechanical unbalance of the rotary system, and continuous operation becomes impossible.

また付着堆積の時間中の熱影響により質的変化した堆積
物が外れて蒸発処理液中に混入すると製品の品質低下を
招くことになる。
Further, if the deposits, which are qualitatively changed due to the heat effect during the deposition and deposition, come off and enter the evaporative treatment liquid, the quality of the product is deteriorated.

さらに薄膜化ユニット(12)により下方では蒸発処理液
は重力による自然流下によって処理液取出口(14)にま
で移動するが、その粘度が高くなると、自然流下では移
動が困難となり、容器本体内下部空間に蒸発処理液が滞
留し器内滞留時間が長くなり、その質的変化を来すこと
になる。
Furthermore, the evaporation treatment liquid moves downward to the treatment liquid outlet (14) by gravity flow due to the thinning unit (12), but when the viscosity becomes high, it becomes difficult to move under the natural flow, and the lower part inside the container body. The evaporative treatment liquid stays in the space, and the residence time in the vessel becomes long, which causes a qualitative change.

本発明は、薄膜蒸発装置の取扱液材料の高粘度化に伴う
これらの問題に総合的な解決を与えることを課題とす
る。
An object of the present invention is to provide a comprehensive solution to these problems associated with an increase in viscosity of a liquid material handled in a thin film evaporator.

〔課題を解決するための手段〕[Means for Solving the Problems]

前記課題を解決するため、本発明は、下部の回転軸は上
部の分散ユニットおよび薄膜ユニットの回転軸とは切り
離して別個に下部から駆動できるようにし、薄膜化蒸発
部の処理速度と蒸発処理液の器外抜出速度との引き継ぎ
連繋作動が釣り合いを保って行えるようにする。そし
て、下部の回転軸内に上部の回転軸の下部軸受を内臓状
態に設け、高粘度液との接触を避けるとともに下部軸受
の器内サポートを無くし付着堆積の問題に解決を与える
ものである。
In order to solve the above-mentioned problems, the present invention provides that the lower rotation shaft can be separately driven from the lower rotation shaft of the upper dispersion unit and the thin film unit, and can be driven separately from the lower rotation shaft. It is possible to maintain a balance in the take-up and connection operation with the withdrawal speed of. Then, the lower bearing of the upper rotary shaft is provided in the lower rotary shaft in a built-in state so as to avoid contact with the high-viscosity liquid and eliminate the internal support of the lower bearing to solve the problem of adhesion and deposition.

特に、本発明の特徴は、薄膜蒸発装置の高粘度液取扱の
問題の集中する下部の構造を根本的に変更し、薄膜化ユ
ニットに引き続いて、倒立円錐形に縮径した容器本体下
部において中心縦軸線のまわりに回転する掻下補助翼を
設け、また容器本体の下方延長筒部の部分内において中
心縦軸線のまわりに回転するスクリュー翼からなる排出
機構を設けて容器本体内下部において蒸発処理液の積極
的器外抜出を行い得るようにする。
In particular, the feature of the present invention is to fundamentally change the structure of the lower part where the problem of handling a high-viscosity liquid of a thin film evaporator is concentrated, and, following the thinning unit, the center of the lower part of the main body of the container which has been reduced in diameter to an inverted cone shape. An agitating auxiliary blade that rotates around the vertical axis is provided, and a discharge mechanism that consists of a screw blade that rotates around the central vertical axis is provided in the downward extension cylindrical portion of the container body, and evaporation processing is performed at the lower inside of the container body. Allow the liquid to be actively withdrawn.

これらを総合して、本発明の薄膜蒸発装置は、構成上に
おいては、中心縦軸線のまわりに円形の減圧可能な密閉
式容器本体の内周面を加熱蒸発面とし、中心縦軸線上に
上部回転軸とその下方に別個に駆動されて回転する下部
回転軸を設け、上部回転軸の下部軸受を下部回転軸内の
内蔵軸受とし、中心縦軸線上の上部回転軸に取付けられ
て回転する上位の分散ユニットにより液材料入口ノズル
から器内に供給された揮発性成分を含む液材料を内周面
の全周に一次的に分散し、続いて分散ユニットの下位の
上部回転軸上の薄膜化ユニットの攪拌翼により下降する
分散液材料を加熱蒸発面上に薄膜状に展開させて揮発性
成分の蒸発の促進を図り、蒸発処理液を容器本体下部の
処理液取出口から抜出すようにした強制薄膜化蒸発装置
において、 薄膜化ユニットに引き続いて、倒立円錐形に縮径した容
器本体下部の位置にある上部回転軸上に掻下補助翼を設
け、且つ処理液出口に直結するように、容器本体下方延
長筒部内の下部回転軸上にスクリュー翼排出機構を設け
たことを特徴とする。
In summary, the thin film evaporation apparatus of the present invention has a structure in which the inner peripheral surface of a circular depressurizable hermetic container body around the central vertical axis is the heating and evaporating surface, and the upper part on the central vertical axis. A rotating shaft and a lower rotating shaft that is separately driven to rotate are provided below the rotating shaft, and the lower bearing of the upper rotating shaft serves as a built-in bearing in the lower rotating shaft. The liquid unit containing the volatile components supplied from the liquid material inlet nozzle into the vessel by the dispersion unit is primarily dispersed over the entire circumference of the inner peripheral surface, and then a thin film is formed on the upper rotary shaft below the dispersion unit. The dispersion material descending by the stirring blade of the unit was spread in a thin film on the heating evaporation surface to promote the evaporation of volatile components, and the evaporation processing liquid was taken out from the processing liquid outlet at the bottom of the container body. Forced thin film evaporation Subsequent to the unit, a scraping auxiliary blade is provided on the upper rotating shaft located at the lower part of the container body that has been reduced in diameter to an inverted cone shape, and the lower part of the container body is extended downward so that it is directly connected to the processing solution outlet. A feature is that a screw blade discharging mechanism is provided on the shaft.

〔作 用〕[Work]

本発明の薄膜蒸発装置においては、薄膜化ユニットの攪
拌翼により薄膜状に展開され下方へ強制移送された蒸発
処理液は、高粘度であっても、薄膜化ユニットの下端に
達したのち滞留する暇なく直ちに掻下補助翼および回転
スクリュー翼に噛込まれて下方移送され器外に抜出され
る。
In the thin film evaporation apparatus of the present invention, the evaporation treatment liquid that is spread in a thin film by the stirring blades of the thinning unit and is forcedly transferred downwards stays after reaching the lower end of the thinning unit even if it has high viscosity. Immediately without any time, the blades are immediately bitten by the agitating auxiliary blades and the rotating screw blades, transferred downward, and taken out of the device.

液材料および蒸発処理液は、その処理全過程を通じて薄
膜化ユニットの攪拌翼、掻下補助翼およびスクリュー翼
によって強制移送され、その間に重力自然流下に依存す
る部分がないので、両軸の別個独立駆動により定量連繋
移送を行うことが可能となり、従って高粘度液を取扱う
場合にも、蒸発処理液の一時的滞留がなく質的変化物の
混入が起こらないので、蒸発処理液の品質は安定して良
品質のものが得られる。
The liquid material and the evaporation treatment liquid are forcibly transferred by the agitating blades, agitating auxiliary blades and screw blades of the thinning unit throughout the entire process, and there is no part dependent on gravity free flow between them, so both axes are independent. Since it is possible to transfer in a fixed amount by driving, even when handling a high viscosity liquid, the quality of the evaporation treatment liquid is stable because there is no temporary retention of the evaporation treatment liquid and mixing of qualitative changes does not occur. And good quality is obtained.

また上部回転軸の下部軸受をスクリュー翼の下部軸受内
に内蔵状態に設けることにより、従来技術の器内軸受サ
ポートが必要なく、蒸発処理液の付着堆積の原因が除か
れるので、これも蒸発処理液の良品質維持に寄与する。
In addition, by installing the lower bearing of the upper rotary shaft inside the lower bearing of the screw blade, the internal bearing support of the prior art is not required, and the cause of adhesion and deposition of the evaporative treatment liquid is eliminated. Contributes to maintaining good quality of liquid.

〔実施例〕〔Example〕

以下、本発明の薄膜蒸発装置を第1図および第2図の実
施例によりさらに具体的細部にわたって説明する。第1
図は、実施例装置の全体の縦断側面図、第2図はその要
部の下部回転軸まわりの部分の拡大縦断側面図を示す。
Hereinafter, the thin film evaporation apparatus of the present invention will be described in more detail with reference to the embodiments of FIGS. 1 and 2. First
FIG. 1 is a vertical sectional side view of the entire apparatus of the embodiment, and FIG. 2 is an enlarged vertical sectional side view of a portion around a lower rotary shaft of a main portion thereof.

この装置の強制薄膜化蒸発機としての基本的構成は第3
図の従来技術とほぼ同様であるから、均等部分には同一
符号を記入して指摘し、その説明を援用し、本発明の特
有部分とその関連について補足説明することとする。
The basic configuration of this device as a forced thinning evaporator is the third
Since it is almost the same as the prior art in the figure, the same parts are designated by the same reference numerals, the description thereof is cited, and a peculiar part of the present invention and its relation will be supplementarily explained.

この実施例の装置は、密閉式容器本体(1)の内周面
(2)が中心縦軸線(X)のまわりに円筒形で下部が倒
立円錐形に縮径しており、外側のジャケット(3)に熱
媒ノズル(4)(5)を経て熱媒を通ずることによりほ
ぼ全高にわたり加熱蒸発面および保温面となる。その器
内は、上部の揮発性成分の蒸気出口ノズル(6)を器外
の凝縮器を経て真空化源(図示せず)に接続することに
より減圧、真空化が可能である。
In the device of this embodiment, the inner peripheral surface (2) of the closed container body (1) is cylindrical around the central longitudinal axis (X) and the lower part is reduced to an inverted conical shape, and the outer jacket ( By passing the heat medium through the heat medium nozzles (4) and (5) to 3), it becomes a heating evaporation surface and a heat retaining surface over almost the entire height. The inside of the vessel can be depressurized and evacuated by connecting the vapor outlet nozzle (6) of the volatile component at the top through a condenser outside the vessel to a vacuum source (not shown).

本発明では、器内に上部回転軸(7A)が上部の頂壁貫通
部のシール付軸受(8)および下位の後述の内蔵軸受
(9A)(第2図参照)により中心縦軸線(X)上に支承
され、器外上部のモータ(図示せず)により回転駆動さ
れるようになっており、上部回転軸(7A)上には器内の
上位に分散ユニット(10)、その下位には攪拌翼(13)
を有する薄膜化ユニット(12)を取付け、さらにその下
位の容器本体円錐下部の高さには、後述目的の掻下補助
翼(17)を取付ける。
According to the present invention, the upper rotary shaft (7A) has a central longitudinal axis (X) in the container by means of a sealed bearing (8) at the top wall penetrating portion of the upper part and a lower built-in bearing (9A) described later (see FIG. 2). It is supported on the upper part and is driven to rotate by a motor (not shown) on the outside of the device. On the upper rotary shaft (7A), the dispersion unit (10) is located in the upper part of the device, and in the lower part of it. Stirrer (13)
The thinning unit (12) having the above is attached, and further, a lowering assisting blade (17), which will be described later, is attached to the lower part of the cone lower part of the container body.

材料入口ノズル(11)から器内に供給された揮発性成分
を含む液材料は回転する分散ユニット(10)により器内
周面の全周に分散されて降下し、続いて薄膜化ユニット
(12)の旋回する攪拌翼(13)により加熱蒸発面上に薄
膜状に展開されて揮発性成分の蒸発の促進が図られ、か
つ薄膜の掻下げ下方移送がなされる。かくして生じた揮
発性成分の蒸気は前記蒸気出口ノズル(6)から器外に
抜出され、蒸発処理液は最終的には後述の処理液取出口
(14A)から器外に抜出されることになる。
The liquid material containing a volatile component supplied from the material inlet nozzle (11) into the container is dispersed and lowered by the rotating dispersion unit (10) along the entire inner surface of the container, and then the thin film forming unit (12). (3) is swirled by the stirring blade (13), which is spread in a thin film on the heating and evaporating surface to promote the evaporation of the volatile component, and the thin film is scraped and transferred downward. The vapor of the volatile components thus generated is extracted from the vapor outlet nozzle (6) to the outside of the device, and the evaporated treatment liquid is finally extracted from the treatment liquid outlet (14A) to be described later. Become.

本発明により、器内の下部に上部回転軸(7A)の下方に
連接するが、別個に駆動されて回転するスリーブ状の下
部回転軸(18)を中心縦軸線(X)上に設け、この下部
回転軸(18)上に前記の掻下補助翼(17)の直下から容
器本体の下方延長筒部(1a)内にわたってスクリュー翼
(19)からなる排出機構を取付ける。
According to the present invention, a sleeve-shaped lower rotary shaft (18), which is connected to the lower part of the container under the upper rotary shaft (7A) but is driven separately, is provided on the central vertical axis (X). A discharge mechanism composed of a screw blade (19) is mounted on the lower rotary shaft (18) from immediately below the aiding assist blade (17) to the inside of the downward extension cylinder (1a) of the container body.

この下部回転軸(18)の支持駆動は、第2図に示すよう
に、容器本体下方延長筒部(1a)の下端に縦軸モータ
(20)を座板(21)を介して結合し、その上向突出の出
力軸(22)の上部に下部回転軸(18)の中空縮径下部を
ボルト(23)により一体に結合し、こうして下部回転軸
(18)をモータ(20)の軸受により中心縦軸線(X)上
にがっちりと回転支承する。そして出力軸(22)外周に
スタッフイングボックス(24)を設けて器内に向かって
シールし、処理液取出口(14A)は容器本体下方延長筒
部(1a)の下端から側方に導き出す。
This lower rotary shaft (18) is supported and driven by connecting a vertical axis motor (20) through a seat plate (21) to the lower end of the container main body lower extension cylinder part (1a) as shown in FIG. The hollow reduced diameter lower part of the lower rotary shaft (18) is integrally connected to the upper part of the upwardly projecting output shaft (22) by the bolt (23), and thus the lower rotary shaft (18) is connected by the bearing of the motor (20). Firmly support the rotation on the central vertical axis (X). Then, a stuffing box (24) is provided on the outer periphery of the output shaft (22) to seal the inside of the container, and the processing liquid outlet (14A) is guided laterally from the lower end of the container body lower extension cylinder (1a).

上部回転軸(7A)の下方支承は、下部回転軸(18)の中
空内にニードルローラベアリングの軸受(9A)を内蔵
し、中空内に挿入される上部回転軸(7A)の下方延長部
(7a)を支持するので、強固に支持され、従来技術のサ
ポート(16)は不要となる。下部回転軸(18)の上端で
下方延長部(7a)のまわりにオイルシール(25)を設
け、内蔵軸受(9A)を器内に向かってシールする。
The lower bearing of the upper rotary shaft (7A) has a needle roller bearing bearing (9A) built in the hollow of the lower rotary shaft (18), and the lower extension of the upper rotary shaft (7A) inserted in the hollow ( Since it supports 7a), it is firmly supported and the prior art support (16) is unnecessary. An oil seal (25) is provided around the lower extension (7a) at the upper end of the lower rotary shaft (18) to seal the internal bearing (9A) toward the inside of the device.

以上の構成とすることにより、揮発性成分を蒸発除去さ
れた蒸発処理液は、薄膜化ユニット(12)の攪拌翼(1
3)の下端に該当する容器本体(1)円筒部の下端に達
したのちは、掻下補助翼(17)の下方送りを受け、直ち
にスクリュー翼排出機構(19)に噛込まれその押出し作
用を受けて直結する処理液取出口(14A)から抜出され
る。すなわち材料入口ノズル(11)から供給された液材
料は、分散ユニット(10)、薄膜化ユニット(12)の攪
拌翼(13)、掻下補助翼(17)および排出機構のスクリ
ュー翼(19)から常に下方送液作用を受けることになる
ので、処理物質の器内滞留時間を適切に制御することが
できる。
With the above configuration, the evaporation treatment liquid from which the volatile components have been removed by evaporation is treated by the stirring blade (1) of the thinning unit (12).
After reaching the lower end of the cylindrical part of the container body (1) corresponding to the lower end of 3), it is fed downward by the assisting blade (17) for immediate downward action and is immediately bitten by the screw blade discharge mechanism (19) to push it out. It is withdrawn from the processing liquid outlet (14A) that is directly connected to it. That is, the liquid material supplied from the material inlet nozzle (11) is dispersed into the dispersion unit (10), the stirring blade (13) of the thinning unit (12), the assisting blade (17), and the screw blade (19) of the discharge mechanism. Therefore, since the liquid is always subjected to the downward liquid feeding action, the residence time of the substance to be treated in the container can be appropriately controlled.

また下部回転軸(18)内に上部回転軸(7A)の下部軸受
(9A)を内蔵させることにより、従来技術では蒸発処理
液の付着堆積の原因であったサポート(16)が存在せ
ず、付着堆積物による蒸発処理液の質の不良化が解消さ
れる。また両回転軸の回転数を個別に制御することがで
きるので、攪拌翼(13)先端周速とスクリュー翼(19)
の排出量との関係が最適となるように任意に両者関係を
設定できる。
In addition, by incorporating the lower bearing (9A) of the upper rotary shaft (7A) in the lower rotary shaft (18), the support (16), which was the cause of deposition and deposition of the evaporative treatment liquid in the prior art, does not exist, Deterioration of the quality of the evaporation treatment liquid due to the adhered deposit is eliminated. In addition, since the rotation speed of both rotary shafts can be controlled individually, the stirring blade (13) tip peripheral speed and screw blade (19)
The relationship between the two can be arbitrarily set so as to optimize the relationship with the emission amount.

〔発明の効果〕〔The invention's effect〕

以上のように、本発明の薄膜蒸発装置によると、集約し
て次の諸効果を実現することができる。
As described above, according to the thin film evaporation device of the present invention, the following various effects can be achieved collectively.

(I)蒸発処理液の自然流下部分をなくしたことによ
り、蒸発処理液の器内滞留時間を任意に制御することが
できる。
(I) Since the spontaneous flow-down portion of the evaporative treatment liquid is eliminated, the residence time of the evaporative treatment liquid in the container can be arbitrarily controlled.

(II)器内に付着堆積物が無くなることにより、装置の
連続運転が可能となる。
(II) The continuous operation of the device becomes possible by eliminating the deposits deposited in the device.

(III)蒸発処理液の下部軸受サポートへの付着が起こ
らないので、その品質の低下を防ぐことができる。
(III) Since the evaporation treatment liquid does not adhere to the lower bearing support, deterioration of the quality can be prevented.

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

第1図は、本発明の1実施例の薄膜蒸発装置の全体の縦
断側面図、第2図はその要部の下部回転軸まわりの部分
の拡大縦断側面図、第3図は従来技術の薄膜蒸発装置の
縦断側面図である。 (1)……容器本体、(1a)……下方延長筒部、(3)
……ジャケット、(4)(5)……熱媒ノズル、(6)
……蒸気出口ノズル、(7)……回転軸、(7A)……上
部回転軸、(7a)……下方延長部、(8)……上部シー
ル付軸受、(9)……器内軸受、(9A)……内蔵軸受、
(10)……分散ユニット、(11)……材料入口ノズル、
(12)……薄膜化ユニット、(13)……攪拌翼、(14)
(14A)……処理液取出口、(15)……ギヤーポンプ、
(16)……サポート、(17)……掻下補助翼、(18)…
…下部回転軸、(19)……スクリュー翼排出機構、(2
0)……縦軸モータ、(21)……座板、(22)……出力
軸、(23)……ボルト、(24)……スタッフイングボッ
クス、(25)……オイルシール。
FIG. 1 is a vertical sectional side view of an entire thin film evaporation apparatus according to an embodiment of the present invention, FIG. 2 is an enlarged vertical sectional side view of a portion around a lower rotation axis of a main portion thereof, and FIG. It is a vertical side view of an evaporator. (1) …… Container body, (1a) …… Downward extension cylinder, (3)
…… Jacket, (4) (5) …… Heat medium nozzle, (6)
...... Steam outlet nozzle, (7) …… Rotary shaft, (7A) …… Upper rotary shaft, (7a) …… Downward extension, (8) …… Upper sealed bearing, (9) …… Internal bearing , (9A) …… Built-in bearing,
(10) …… Dispersion unit, (11) …… Material inlet nozzle,
(12) …… Thin film unit, (13) …… Stirrer, (14)
(14A) …… Treatment liquid outlet, (15) …… Gear pump,
(16) …… Support, (17) …… Sucking aileron, (18)…
… Lower rotating shaft, (19)… Screw vane discharging mechanism, (2
0) …… Vertical motor, (21) …… Seat plate, (22) …… Output shaft, (23) …… Bolt, (24) …… Stuffing box, (25) …… Oil seal.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】中心縦軸線のまわりに円形の減圧可能な密
閉式容器本体の内周面を加熱蒸発面とし、中心縦軸線上
に上部回転軸とその下方に別個に駆動されて回転する下
部回転軸を設け、上部回転軸の下部軸受を下部回転軸内
の内蔵軸受とし、中心縦軸線上の上部回転軸に取付けら
れて回転する上位の分散ユニットにより液材料入口ノズ
ルから器内に供給された揮発性成分を含む液材料を内周
面の全周に一次的に分散し、続いて分散ユニットの下位
の上部回転軸上の薄膜化ユニットの攪拌翼により下降す
る分散液材料を加熱蒸発面上に薄膜状に展開させて揮発
性成分の蒸発の促進を図り、蒸発処理液を容器本体下部
の処理液取出口から抜出すようにした強制薄膜化蒸発装
置において、 薄膜化ユニットに引き続いて、倒立円錐形に縮径した容
器本体下部の位置にある上部回転軸上に掻下補助翼を設
け、且つ処理液出口に直結するように、容器本体下方延
長筒部内の下部回転軸上にスクリュー翼排出機構を設け
たことを特徴とする薄膜蒸発装置。
1. An inner peripheral surface of a circular depressurizable hermetic container body around a central vertical axis as a heating and evaporating surface, and an upper rotary shaft on the central vertical axis and a lower part which is separately driven and rotated below the rotary shaft. A rotary shaft is provided, the lower bearing of the upper rotary shaft is used as a built-in bearing in the lower rotary shaft, and it is supplied from the liquid material inlet nozzle into the container by the upper dispersion unit that is mounted and rotates on the upper rotary shaft on the central vertical axis. The liquid material containing volatile components is primarily dispersed all around the inner surface, and then the dispersion material descending by the stirring blade of the thinning unit on the upper rotary shaft below the dispersion unit is heated to the evaporation surface. In the forced thinning evaporation device that was developed in a thin film on the top to promote the evaporation of volatile components, and the evaporation processing liquid was drawn out from the processing liquid outlet at the bottom of the container body, following the thinning unit, An inverted cone-shaped container book A lower blade is provided on the upper rotary shaft at the lower part of the body, and a screw blade discharge mechanism is provided on the lower rotary shaft in the lower extension cylinder of the container body so as to be directly connected to the processing liquid outlet. Thin film evaporator.
JP63240390A 1988-09-26 1988-09-26 Thin film evaporator Expired - Fee Related JPH0759281B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63240390A JPH0759281B2 (en) 1988-09-26 1988-09-26 Thin film evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63240390A JPH0759281B2 (en) 1988-09-26 1988-09-26 Thin film evaporator

Publications (2)

Publication Number Publication Date
JPH0299101A JPH0299101A (en) 1990-04-11
JPH0759281B2 true JPH0759281B2 (en) 1995-06-28

Family

ID=17058769

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63240390A Expired - Fee Related JPH0759281B2 (en) 1988-09-26 1988-09-26 Thin film evaporator

Country Status (1)

Country Link
JP (1) JPH0759281B2 (en)

Also Published As

Publication number Publication date
JPH0299101A (en) 1990-04-11

Similar Documents

Publication Publication Date Title
JPH0360701A (en) Screw blade-type discharger for thin-film vaporizer
EP0384480B1 (en) Process for continously drying paste material for a high-density detergent
CN107405533B (en) Evaporation device
JPH0759281B2 (en) Thin film evaporator
US5425849A (en) Film-type evaporator
US4590686A (en) Drying plant for liquid or pasty products
KR900700778A (en) Method and apparatus for coating the inner cavity
CN212491598U (en) Film evaporator distributing device for treating high-viscosity materials
US3334680A (en) Rotary wiped film evaporator
GB740561A (en) Improvements relating to apparatus for distilling or evaporating liquids
US4812203A (en) Evaporator
WO2021119945A1 (en) Continuous evaporation and delivery apparatus for slurry
SU1457941A1 (en) Rotary apparatus for concentrating thermolabile solutions
JP2604010B2 (en) Coating device
JP3266299B2 (en) Thin film evaporator
CN212548340U (en) Distillation device for filtering chemical reagent
CN212141501U (en) Vacuum concentration device with stirring function
CN2511374Y (en) Evaporator
JPS63117038A (en) Horizontal reactor
JPH0647041B2 (en) Multipurpose heat transfer device
JPH0819241B2 (en) Continuous stirring device for viscous substances
US3878028A (en) Method and apparatus for distributing feed stock to dryer drum
CN111530107A (en) Film evaporator distributing device for treating high-viscosity materials
JPH0598032A (en) Preparation of solvent-free epoxy emulsion
JP2690983B2 (en) Centrifugal thin film evaporator

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees