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JPH0620483B2 - Thin film evaporative concentrator - Google Patents
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JPH0620483B2 - Thin film evaporative concentrator - Google Patents

Thin film evaporative concentrator

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Publication number
JPH0620483B2
JPH0620483B2 JP5386689A JP5386689A JPH0620483B2 JP H0620483 B2 JPH0620483 B2 JP H0620483B2 JP 5386689 A JP5386689 A JP 5386689A JP 5386689 A JP5386689 A JP 5386689A JP H0620483 B2 JPH0620483 B2 JP H0620483B2
Authority
JP
Japan
Prior art keywords
cylinder
shaft
thin
evaporative concentrator
thin film
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
JP5386689A
Other languages
Japanese (ja)
Other versions
JPH02233103A (en
Inventor
理文 井上
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.)
SAKURA SEISAKUSHO KK
Original Assignee
SAKURA SEISAKUSHO KK
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 SAKURA SEISAKUSHO KK filed Critical SAKURA SEISAKUSHO KK
Priority to JP5386689A priority Critical patent/JPH0620483B2/en
Publication of JPH02233103A publication Critical patent/JPH02233103A/en
Publication of JPH0620483B2 publication Critical patent/JPH0620483B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • 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> 開示技術は食品や医薬品、肥料等の製品を得るに際し、
高粘性の原料液を一方側から供給し、加熱作用により揮
発分を蒸発させ、撹拌ブレードにより撹拌混合作用を与
えて高度に濃縮させ、粉末化して製品として排出するこ
とができるようにした装置の構造技術分野に属する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The disclosed technology is used for obtaining products such as foods, pharmaceuticals and fertilizers.
A highly viscous raw material liquid is supplied from one side, the volatile components are evaporated by the heating action, the stirring blade gives the stirring and mixing action to highly concentrate, and the powdered product can be discharged as a product. Belongs to the field of structural technology.

<要旨の概要> 而して、この出願の発明は高粘性の原料液を供給し、濃
縮して製品として排出するプロセスに於て、被処理物の
原料液を薄膜式に形成させて加熱反応に加えて混合撹拌
作用を与えて蒸発作用を介し、濃縮プロセスを経て粉末
状態までに濃縮して製品として得ることが出来る薄膜式
蒸発濃縮装置であって、外側には熱交換用のジャケット
を装備すると共に、高粘性原料液等の被処理物の供給部
を一方側に、粉末の製品の排出部を他方側に有するシリ
ンダにシャフトが軸装され該シャフトにはその軸方向所
定間隔で所定段数複数の撹拌ブレードが周方向スイング
自在に設けられ、その先端をシリンダの内面へ微小クリ
アランスを介して近接させて、濃縮効果が高められるよ
うにされている薄膜式蒸発濃縮装置に関する発明であ
り、特に、上記シャフトに対する取合は撹拌ブレードの
基部をピンを介してブレードホルダにスイング自在に設
け、撹拌ブレードのシリンダ内面への稼動中の微小クリ
アランスを組付時に調整することが出来るシム等の調整
体が介装されている薄膜式蒸発濃縮装置に係る発明であ
る。
<Summary of summary> Therefore, the invention of this application, in the process of supplying a highly viscous raw material liquid, concentrating it and discharging it as a product, forms a raw material liquid of the object to be processed in a thin film type and heats it. In addition to this, it is a thin film evaporative concentrator that can be obtained as a product by concentrating to a powder state through a concentrating process by giving a mixing and stirring effect and evaporating, and equipped with a jacket for heat exchange on the outside. At the same time, a shaft is mounted on a cylinder having a supply part for the object to be treated such as a highly viscous raw material liquid on one side and a discharge part for the powder product on the other side, and the shaft has a predetermined number of stages at predetermined intervals in the axial direction. A plurality of stirring blades are provided so as to be swingable in the circumferential direction, and the tip thereof is brought close to the inner surface of the cylinder via a minute clearance, and is an invention relating to a thin-film type evaporative concentration apparatus in which the concentration effect is enhanced. In particular, for the attachment to the shaft, the base of the stirring blade is swingably provided on the blade holder via the pin, and the minute clearance during operation of the stirring blade to the inner surface of the cylinder can be adjusted during assembly, such as adjustment of shims. The invention relates to a thin-film type evaporative concentration apparatus in which a body is interposed.

<従来技術> 周知の如く、市民生活が向上すると、各種の製品が大
量、少量に取り扱われるようになり、したがって、これ
らの商品の安定供給が望まれると共に、その高精度の品
質が強く求められるようになってきている。
<Prior Art> As is well known, as the life of citizens is improved, various products are handled in large quantities and in small quantities. Therefore, stable supply of these products is desired, and high precision quality is strongly required. Is starting to appear.

これらの商品の中には農産物、海産物等の一次製品も多
いが、二次加工された食品、薬品、化粧品等の商品も各
種のものが流通している。
Many of these products are primary products such as agricultural products and marine products, but various products such as secondary processed foods, medicines, and cosmetics are also in circulation.

そして、これらの二次加工商品の中には、例えば、キャ
ンディやクリーム、薬品等の商品も多く、これらの中に
はゼリー状のものもあるが、果実、野菜ビューレ、た
れ、スープ等の液状品もあり、又、クリーム状のものも
あり、更には、顆粒状の樹脂製品や薬品等もあり、これ
らの特殊性状の製品の製造過程はコスト、及び、製品精
度の点から好ましくはその工数が少く、安易な取り扱い
処理が望まれている。
Among these secondary processed products, for example, there are many products such as candy, cream, and medicine, and there are also jelly-like products, but liquid products such as fruits, vegetable burets, sauces, and soups. There are products, creamy products, and granular resin products and chemicals. The manufacturing process of products with these special properties is preferable in terms of cost and product accuracy. However, there is a demand for easy handling.

而して、これに対処するに、物理化学的な熱交換を介し
熱反応を行う反応装置が開発されて採用され実用化され
ているが、例えば、第7、8図に示す様な境膜式熱交換
反応装置1にあっては外側に熱交換用のジャケット2を
有するドラムタイプのシリンダ3を設け、その前後端壁
面にベアリング5、メカニカルシール6を介してモータ
7に連結された軸8にシャフト9を一体的に設け、所定
数のブレード11、11…を径方向にスイング自在に設けて
シリンダ3の内周面にその遠心力により周方向スライド
自在に回転させるようにし、シリンダ3の一方側の供給
口12により所定の高粘性の原料液13を供給し、ブレード
11、11…により混合撹拌しながらその遠心力を介しシリ
ンダ3の内周面との間に薄膜状の境膜を形成させて、ジ
ャケット2に対する高温熱媒体15を供給口14より供給し
て物理化学的な熱交換を行って可及的速やかに熱反応を
行ってより更に高粘性にしたり、熱変成により顆粒状に
変化させてシリンダ3の他側に設けた排出口17より製品
18として取り出すようにしていた。
In order to deal with this, a reaction apparatus that performs a thermal reaction through physicochemical heat exchange has been developed, adopted, and put into practical use. For example, a boundary film as shown in FIGS. The heat exchange reaction apparatus 1 is provided with a drum type cylinder 3 having a jacket 2 for heat exchange on the outside, and a shaft 8 connected to a motor 7 via bearings 5 and mechanical seals 6 on the front and rear end wall surfaces thereof. Is integrally provided with a shaft 9, and a predetermined number of blades 11, 11 ... Are provided so as to be swingable in the radial direction so that the inner peripheral surface of the cylinder 3 can be slidably rotated in the circumferential direction by its centrifugal force. A predetermined high-viscosity raw material liquid 13 is supplied from the supply port 12 on one side, and a blade
A thin film boundary film is formed between the inner peripheral surface of the cylinder 3 and centrifugal force while mixing and stirring by 11, 11, ... Chemical heat exchange is carried out to cause a thermal reaction as quickly as possible to make it even more viscous, or it is converted into granules by thermal transformation and discharged from the outlet 17 provided on the other side of the cylinder 3.
I was going to take it out as 18.

<発明が解決しようとする課題> さりながら、かかる在来態様の境膜式熱交換反応装置1
では熱交換を行うジャケット2がシリンダ3の外側に1
ユニット設けられているために、製品によって迅速な熱
変化、例えば、高温熱媒体、低温熱媒体の切り換え、或
は、急激な熱勾配を有する熱交換が出来ないことから、
これらの熱履歴を有する製品が得られない欠点があり、
又、ロータが複段のブレード11、11…によるシリンダ3
の内周面に対する摺動であるために、連続的な反応がし
難いという難点があり、又、シリンダ3内部のロータの
構造が著しく複雑でブレート11とシリンダ3内周面との
取合いが極めて難しく、熟練を要するきらいがあり、初
期組み付け構造において煩瑣な作業を要し、結果的にコ
スト高になり、又、保守点検整備等のメンテナンスもし
難いというサービス性に劣る不都合さがあった。
<Problems to be Solved by the Invention> Incidentally, the conventional film-type heat exchange reaction device 1
Then, the jacket 2 for heat exchange is placed outside the cylinder 3.
Since the unit is provided, rapid heat change depending on the product, for example, switching between high-temperature heat medium and low-temperature heat medium, or heat exchange with a steep heat gradient cannot be performed,
There is a drawback that products with these heat history cannot be obtained,
Also, the rotor is a multi-stage blade 11, 11 ...
Since it slides on the inner peripheral surface of the cylinder, continuous reaction is difficult, and the structure of the rotor inside the cylinder 3 is remarkably complicated, so that the fitting between the plate 11 and the inner peripheral surface of the cylinder 3 is extremely difficult. It is difficult and requires skill and requires complicated work in the initial assembly structure, resulting in high cost and difficulty in maintenance such as maintenance and inspection.

そして、これらのネックにより製品コストに跳ね返る不
利点があり、又、ジャケット2による温度管理制御が極
めてデリケートで難しいという不具合があった。
These necks have the disadvantage that the product cost is repelled, and the temperature management control by the jacket 2 is extremely delicate and difficult.

これに対し、出願人等により鋭意開発研究がなされて第
9、10、11示すような薄膜式蒸発濃縮装置1′が開
発され、撹拌ブレード11′をシャフト9に対してブレー
ドホルダ10′を介して取付け、撹拌ブレード11′はブレ
ードホルダ10′に対しピン22で枢支し、該撹拌ブレード
11′をスイング自在にし、第11図に示す様に、その先
端がシリンダ3の内面に対し微小クリアランス21、21′
を形成することが出来るようにして、稼動中における装
置1′内を流過する被処理物を薄膜式に形成させてジャ
ケット2による加熱を介しての蒸発と加熱作用を向上さ
せると共に、混合撹拌作用をも効果的に付与するように
して濃縮効率が上げられるようにし、排出口17からの製
品18′については高濃縮の結果粉末状態とすることまで
出来るようになってきた。
On the other hand, the applicants conducted extensive research and development to develop a thin-film type evaporative concentrator 1'as shown in the ninth, tenth and eleventh aspects, in which a stirring blade 11 'was mounted on the shaft 9 via a blade holder 10'. The stirring blade 11 'is pivotally supported by the pin 22 with respect to the blade holder 10'.
11 'is allowed to swing, and as shown in FIG. 11, its tip is a minute clearance 21, 21' with respect to the inner surface of the cylinder 3.
Is formed so that the object to be processed flowing through the inside of the apparatus 1'in operation is formed in the form of a thin film to improve evaporation and heating action through heating by the jacket 2 and to perform mixing and stirring. It has also become possible to increase the concentration efficiency by effectively providing the action, and to make the product 18 'from the discharge port 17 into a powder state as a result of high concentration.

しかしながら、該種薄膜式蒸発濃縮装置1′において
は、前述境膜式濃縮装置の問題点は解決されるものの、
次のような新たな問題が生じてきた。即ち、供給される
被処理物に対する濃縮の度合は高ければ高い程当然のこ
とながら残渣量も減少し、当該残渣物の廃棄処理対策も
容易に行え、溶剤等の有効再利用等も促進される効果が
あるが、かかる効果は当然のことながら、高濃縮を図る
薄膜式の濃縮効率、即ち第11図に示す撹拌ブレード1
1′先端とシリンダ3内面との微小クリアランス21の設
計通りの形成が極めて重要にあずかってくることがわか
ってきた。
However, in the seed thin film type evaporative concentrator 1 ', although the problems of the boundary film type concentrator described above are solved,
The following new problems arose. That is, the higher the degree of concentration of the object to be supplied is, of course, the smaller the amount of the residue, the easier the disposal treatment of the residue, and the effective reuse of the solvent, etc. Although effective, such effect is, of course, a thin film concentration efficiency for high concentration, that is, the stirring blade 1 shown in FIG.
It has been found that the formation of the minute clearance 21 between the tip of the 1'and the inner surface of the cylinder 3 as designed is extremely important.

さりながら、当該薄膜式蒸発濃縮装置1′は機械加工が
なされ、又、特定部品も多い為にそれぞれの製作や組付
時の誤差が生じ、許容範囲を越えると、設計通りの高濃
縮が得られないという不具合があり、又、設計通りの微
小クリアランスを保持するには組付けやメンテナンスの
うえで高度の熟練を要し、装置の製作コストが高くつき
実稼動に徴し難いという不都合さが生じてきた。
By the way, the thin-film type evaporative concentrator 1'is machined, and since there are many specific parts, errors in manufacturing and assembling each occur, and if the allowable range is exceeded, high concentration as designed can be obtained. There is a problem that it can not be done, and in order to maintain the minute clearance as designed, a high level of skill is required in assembly and maintenance, the manufacturing cost of the device is high and it is difficult to put it into actual operation. Came.

<発明の目的> この出願の発明の目的は上述従来技術に基づく境膜式濃
縮装置等の問題点をクリアーした基本的な薄膜式蒸発濃
縮装置の問題点を解決すべき技術的課題とし、本来的な
薄膜式蒸発濃縮の利点をフルにいかすことが出来、設計
通りの濃縮粉末製品を得られるようにして化成品製造産
業における化学機械装置の利用分野に益する優れた薄膜
式蒸発濃縮装置を提供せんとするものである。
<Object of the invention> The object of the invention of this application is to solve the problems of the basic film-type concentrating device and the like based on the above-mentioned conventional technique and to solve the problems of the basic thin-film evaporating and concentrating device. It is possible to fully utilize the advantages of thin film evaporative concentration, and to obtain a concentrated powder product as designed, thus providing an excellent thin film evaporative concentration device that benefits the field of chemical mechanical equipment in the chemical product manufacturing industry. It is intended to be provided.

<課題を解決するための手段・作用> 上述目的に沿い先述特許請求の範囲を要旨とするこの発
明の構成は前述課題を解決するために、薄膜式蒸発濃縮
装置を作成するに際し、駆動装置に連結した回転軸に一
体延設するシャフトの軸方向所定部位に面取り部を形成
し、該面取り部にブレードホルダを所定の微小厚さのシ
ム等の調整体を介装してブレードホルダを取付けし、該
ブレードホルダにピンを介して撹拌ブレードをスイング
自在に枢支し、撹拌ブレードの先端をしてシリンダの内
面に設定微小クリアランスを形成させて所定の被処理物
を供給部より供給し、シリンダの外側のジャケットには
熱交換流体を供給して熱交換を行いながら被処理物を流
過させると、該被処理物はシリンダの内面に於て回転す
る撹拌ブレードによりシリンダ内面に薄膜式に流過して
加熱混合撹拌がなされて蒸発が促進されると共に、高濃
縮が行われて排出部近郊においては粉末化された製品と
されるようにした技術的手段を講じたものである。
<Means and Actions for Solving the Problem> In order to solve the above-mentioned problems, the structure of the present invention, which is based on the above-mentioned object, has a driving device at the time of producing a thin-film evaporation concentrating device. A chamfer is formed at a predetermined axial position of the shaft integrally extending to the connected rotating shaft, and the blade holder is attached to the chamfer with an adjusting body such as a shim having a predetermined small thickness interposed therebetween. , The stirring blade is swingably supported on the blade holder via a pin, the tip of the stirring blade is formed to form a set minute clearance on the inner surface of the cylinder, and a predetermined object to be processed is supplied from the supply unit, A heat exchange fluid is supplied to the jacket on the outside of the cylinder to allow the object to flow through while exchanging heat, and the object to be processed is rotated by the stirring blade on the inner surface of the cylinder. It is a thin film type and is heated and mixed with stirring to promote evaporation, and is highly concentrated to be a powdered product in the vicinity of the discharge area. Is.

<実施例> 次に、この出願と発明の実施例を第1乃至6図に基づい
て説明すれば以下の通りである。
<Embodiment> Next, an embodiment of the present application and invention will be described with reference to FIGS.

第1乃至3図に示す実施例に於て、10′はブレードホル
ダであり、撹拌ブレード11′をシャフト9にスイング自
在に取付けるものであり、該シャフト9の所定部位の軸
方向に沿って所定サイズのフラットな面取り部9′が形
成され、ブレードホルダ10′基部の座10″がボルト23に
より締結固定されるようにされており、ピン22を介し撹
拌ブレード11′がスイング自在に取付けられてその先端
とシリンダ3との間に前述した如く、稼動中における高
濃縮用の微小クリアランス21が△hだけ設計通りに形成
することが出来るようにされており、その際、シャフト
9の面取り9′の機械加工により、及び、ブレードホル
ダ10′の座10″の機械加工仕上げにより差が生じて微小
クリアランスにバラツキが生ずる虞があるためにこの出
願の発明においては、座10″のシャフト9の面取り部
9′に対するボルト23を介しての取合いにおいて、両者
の間に調整体としてのシム24を介装させて設計通りの微
小クリアランス21が△h形成することができるようにさ
れている。
In the embodiment shown in FIGS. 1 to 3, reference numeral 10 'is a blade holder for attaching a stirring blade 11' to the shaft 9 so as to be swingable, and to have a predetermined position along the axial direction of a predetermined portion of the shaft 9. A flat chamfer 9'of a size is formed, a seat 10 "at the base of the blade holder 10 'is fastened and fixed by a bolt 23, and a stirring blade 11' is swingably attached via a pin 22. As described above, the minute clearance 21 for high concentration during operation can be formed between the tip of the shaft 3 and the cylinder 3 as designed, and at this time, the chamfer 9'of the shaft 9 is formed. In the invention of this application, there is a possibility that a difference may occur due to the machining of the above and the machining finish of the seat 10 ″ of the blade holder 10 ′ to cause a variation in the minute clearance. In mounting the chamfered portion 9'of the shaft 9 "through the bolt 23, a small clearance 21 as designed can be formed by inserting a shim 24 as an adjusting body therebetween. Has been done.

尚、該調整体としてのシムは当該第3図に示す実施例の
如く1枚であっても良いが、予め厚みサイズの異なる数
種類のシム24を用意しておいて組付時の計測により設計
通りの微小クリアランス21△hが形成されるように選択
使用することは勿論のことであるが、第4図に示す様
に、厚みの異なるシム24′、24′、24′を複数枚合せて
選択して最適設計通りの微小クリアランス△hを形成す
ることが出来るようにすることは勿論のこと、又、第5
図に示す様に厚さの著しく薄いシムと厚さの著しく厚い
シムとを組合せるようにしても良く、更には第6図に示
す実施例の如く、ブレードホルダ10′の座10に予め厚
みの異なるものを用意してこれとシム24′との組合せ選
択により、撹拌ブレード11′とシリンダ3との内面との
間の微小クリアランス21△hを最適なものにするように
することが可能である。
The shim as the adjusting body may be one as in the embodiment shown in FIG. 3, but several kinds of shims 24 having different thickness sizes are prepared in advance and designed by measurement at the time of assembly. It is needless to say that the plurality of shims 24 ', 24', 24 'having different thicknesses are combined as shown in FIG. Of course, it is possible to select the minute clearance Δh as designed so as to form the minute clearance Δh.
As shown in the figure, a shim having a very small thickness and a shim having a very large thickness may be combined. Further, as in the embodiment shown in FIG. It is possible to optimize the micro clearance 21Δh between the stirring blade 11 'and the inner surface of the cylinder 3 by preparing different ones and selecting the combination of this and the shim 24'. is there.

このような調整体としてのシム24をシャフト9の面取り
部9′とブレードホルダ10′との座10″との間に介装し
て、ボルト23により締付けて該ブレードホルダ10′にピ
ン22を介して撹拌ブレード11′をスイング自在に取付け
ることにより、稼動中における撹拌ブレード11′の先端
とシリンダ3の内面との間の微小クリアランス21の△h
は設計通りの微小クリアランスに形成されて、供給口12
から供給される溶剤等の被処理物23はシリンダ3内の濃
縮処理部内に於て排出口17へ流過される間に流過する加
熱流体により加熱され、又、撹拌ブレード11′、11′…
により撹拌混合され、先端とシリンダ3の内面との間の
微小クリアランス21により蒸発作用を促進され、高濃縮
され、終期プロセスにおいては粉末化されて製品18′と
して取り出される。
A shim 24 as such an adjusting body is interposed between the chamfered portion 9'of the shaft 9 and the seat 10 "of the blade holder 10 ', and is tightened by a bolt 23 to attach the pin 22 to the blade holder 10'. The stirring blade 11 'is swingably attached via the above so that the minute clearance 21h between the tip of the stirring blade 11' and the inner surface of the cylinder 3 during operation can be reduced.
Is formed with a minute clearance as designed, and the supply port 12
An object to be treated 23 such as a solvent supplied from the inside is heated by a heating fluid flowing through the discharge port 17 in the concentrating treatment section in the cylinder 3, and is also stirred blades 11 ', 11'. …
Are agitated and mixed with each other, the evaporation action is promoted by the minute clearance 21 between the tip and the inner surface of the cylinder 3, the solution is highly concentrated, and in the final process, it is pulverized and taken out as a product 18 '.

又、蒸発分は蒸発口19から蒸発物20として排出されてい
く。このようにすることにより、例えば、被処理物とし
て自動車の塗装工程における廃棄溶剤の濃縮の比較を行
った実験データを次の表に示す。
Further, the evaporated portion is discharged from the evaporation port 19 as an evaporated material 20. By doing so, for example, the following table shows experimental data in which the concentration of the waste solvent in the painting process of the automobile as the object to be treated is compared.

当該比較表のデータに示す通り、従来態様に比しこの出
願の発明によれば、この程度に処理能力を有する場合に
おいて濃縮度は比較的に向上し、残渣量は200kgも減
少し、作業員も少なく悪臭もほとんどなく、安全に高能
率に作業が行え、回収溶剤も多くなり、コストダウンも
図れ、又、残渣は粉末化されているために、例えば、増
量材として売却することが出来、従来焼却処理しか行え
なかった残渣に対しても焼却費用がかかるどころか売却
利益が得られて経費的にもプラスすることが分る。
As shown in the data of the comparison table, according to the invention of this application, the concentration is relatively improved and the amount of residue is reduced by 200 kg in comparison with the conventional embodiment. There is little odor and there is almost no bad odor, work can be done safely and efficiently, the amount of recovered solvent increases, the cost can be reduced, and since the residue is powdered, it can be sold as a bulking material, for example. In addition to incurring incineration costs for residues that could only be incinerated in the past, profits can be obtained from the sale, which also adds to the cost.

尚、この発明の実施態様は上述実施例に限るものでない
ことは勿論であり、例えば、調整体としてはシムを厚さ
方向にテーパー状に形成する等種々の態様が採用可能で
ある。
It should be noted that the embodiment of the present invention is not limited to the above-described embodiment, and various embodiments such as forming a shim in a taper shape in the thickness direction can be adopted as the adjusting body.

<発明の効果> 以上、この出願の発明によれば、熱交換しながら供給さ
れた被処理物を高濃縮にさせて、溶剤分等を蒸発させて
粉末化させて製品として得られる薄膜式蒸発濃縮装置に
おいて、高濃縮プロセスにおける粉末化に極めて重要に
かかわりあいを有する撹拌ブレードの遠心力を介しての
シリンダ内面に対するスイング自在な先端微小クリアラ
ンスの形成が撹拌ブレードをブレードホルダを介してシ
ャフトに組付ける取合部に於てシム等の調整体を介装さ
せることにより、熟練を要することなく、撹拌ブレード
のシリンダ内面に対する稼動中の微小クリアランスを設
計通りに正確に形成し、設計通りの撹拌蒸発による高濃
縮を介しての粉末化が得られるという優れた効果が奏さ
れる。
<Effects of the Invention> As described above, according to the invention of this application, a thin film type evaporation obtained as a product by highly concentrating the object to be treated supplied while exchanging heat to evaporate the solvent component and the like to powder In the concentrator, the formation of a swingable tip micro clearance to the inner surface of the cylinder via the centrifugal force of the stirring blade, which is very importantly involved in pulverization in the high concentration process, attaches the stirring blade to the shaft via the blade holder. By inserting an adjusting body such as a shim in the joining part, it is possible to accurately form a minute clearance during operation with respect to the inner surface of the cylinder of the stirring blade as designed without the need for skill, and by stirring evaporation as designed. The excellent effect is obtained that powdering is achieved through high concentration.

したがって、供給する被処理物の溶剤分離効率が良く回
収しての再利用率が高くなり、それだけコストダウンが
図れ、残渣量が少なくなって確実に粉末化され、従来の
粘性の高い泥状の残渣ではなく、そのため焼却等せず、
増量材等として再利用出来、販売商品にさえ出来、焼却
に要する費用が削減されるばかりでなく利得にすらなる
という利点がある。
Therefore, the solvent separation efficiency of the workpiece to be supplied is improved and the reuse rate is increased, and the cost can be reduced accordingly, the amount of the residue is reduced, and the powder is reliably pulverized. It is not a residue, so it is not incinerated,
It has the advantages that it can be reused as a bulking material, can even be sold, and that not only the cost required for incineration can be reduced, but even gain can be achieved.

又、稼動中における撹拌ブレードのスイング自在な回転
に伴うシリンダ内面の微小クリアランスが常に安定して
得られるために、設計通りの薄膜式蒸発が行なわれて高
濃縮の粉末が得られて従来の粘性の高い残渣と異なり、
焼却等必要がなくなり、焼却費も削減され、むしろ、増
量材等として商品化して利得が得られて利益を生ずると
いう利点もある。
In addition, since the minute clearance on the inner surface of the cylinder due to the swinging rotation of the stirring blade during operation can always be stably obtained, thin film evaporation as designed is performed and highly concentrated powder is obtained, resulting in the conventional viscosity. Unlike high residue,
There is also the advantage that there is no need for incineration, the incineration cost is reduced, and rather, profit is obtained by commercializing it as an extender material and the like, and gaining profit.

又、シム等の調整体もブレードホルダとシャフトとの間
に介装することにより極めて微妙な微小クリアランスが
設計通りに形成することが出来るのみならず、稼動中に
おける微小クリアランスの変動もなく、安定した薄膜式
蒸発濃縮が行えるという効果もある。
Also, by inserting an adjusting body such as a shim between the blade holder and the shaft, not only a very delicate minute clearance can be formed as designed, but also the minute clearance does not fluctuate during operation and is stable. There is also an effect that the thin film type evaporation concentration can be performed.

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

第1乃至10図はこの出願の発明の実施例の説明図であ
り、第1図は1実施例の拡大横断面図、第2図は同部分
拡大側面図、第3図はブレードホルダとシャフトの取合
部分拡大断面図、第4、5、6図は他の実施例の第3図
相当拡大断面図、第9図は装置全体の縦断面図、第10
図は同横断面図、第7図は従来技術に基づく実施装置の
縦断面図、第8図は同横断面図、第11図は撹拌ブレー
ドとシリンダ内面の微小クリアランスの側面図である。 2……ジャケット、13……被処理物、 12……供給部、17……排出部、 18′……製品、 3……シリンダ、 10……シャフト、11′……撹拌ブレード、 1′……薄膜式蒸発濃縮装置、 21……微小クリアランス、14……調整体(シム)、 10′……ブレードホルダ、 9′……面取り部、
1 to 10 are explanatory views of an embodiment of the invention of this application, FIG. 1 is an enlarged cross-sectional view of one embodiment, FIG. 2 is an enlarged side view of the same, and FIG. 3 is a blade holder and a shaft. FIG. 4 is an enlarged cross-sectional view of another embodiment of the present invention, and FIG. 9 is a vertical cross-sectional view of the entire apparatus.
FIG. 7 is a horizontal cross-sectional view, FIG. 7 is a vertical cross-sectional view of an embodying device based on a conventional technique, FIG. 8 is a horizontal cross-sectional view of the same, and FIG. 11 is a side view of a minute clearance between a stirring blade and an inner surface of a cylinder. 2 …… Jacket, 13 …… Workpiece, 12 …… Supply part, 17 …… Discharge part, 18 ′ …… Product, 3 …… Cylinder, 10 …… Shaft, 11 ′ …… Stirring blade, 1 ′… … Thin film type evaporative concentrator, 21 …… Micro clearance, 14 …… Adjusting body (shim), 10 ′ …… Blade holder, 9 ′ …… Chamfer,

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】ジャケットを外装すると共に被処理物供給
部と製品排出部を有するシリンダに軸装したシャフトに
該シリンダ内面へ先端を近接する撹拌ブレードがスイン
グ自在に軸方向複数枢設されている薄膜式蒸発濃縮装置
において、上記シャフトと撹拌ブレードとの取合部に該
撹拌ブレードとシリンダ内面との間の稼動中の微小クリ
アランスを組付時に調整する調整体が介装されているこ
とを特徴とする薄膜式蒸発濃縮装置。
1. A plurality of agitating blades, each of which has its tip close to the inner surface of the cylinder, are pivotally mounted in a swingable manner on a shaft which is mounted on a cylinder having an outer surface of a jacket and an object supply portion and a product discharge portion. In the thin-film type evaporative concentrator, an adjusting body for adjusting a minute clearance during operation between the stirring blade and the inner surface of the cylinder at the time of assembly is interposed in the joint between the shaft and the stirring blade. Thin film evaporative concentrator.
【請求項2】上記調整体がシムであることを特徴とする
特許請求の範囲第1項記載の薄膜式蒸発濃縮装置。
2. The thin-film type evaporative concentrator according to claim 1, wherein the adjusting body is a shim.
【請求項3】上記シムがシャフトとブレードホルダとの
間に介装されていることを特徴とする特許請求の範囲第
2項記載の薄膜式蒸発濃縮装置。
3. The thin-film type evaporative concentrator according to claim 2, wherein the shim is interposed between the shaft and the blade holder.
【請求項4】上記シャフトのブレードホルダ取付部に面
取りが形成されていることを特徴とする特許請求の範囲
第3項記載の薄膜式蒸発濃縮装置。
4. A thin-film type evaporative concentrator according to claim 3, wherein a chamfer is formed on the blade holder mounting portion of the shaft.
JP5386689A 1989-03-08 1989-03-08 Thin film evaporative concentrator Expired - Lifetime JPH0620483B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5386689A JPH0620483B2 (en) 1989-03-08 1989-03-08 Thin film evaporative concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5386689A JPH0620483B2 (en) 1989-03-08 1989-03-08 Thin film evaporative concentrator

Publications (2)

Publication Number Publication Date
JPH02233103A JPH02233103A (en) 1990-09-14
JPH0620483B2 true JPH0620483B2 (en) 1994-03-23

Family

ID=12954691

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5386689A Expired - Lifetime JPH0620483B2 (en) 1989-03-08 1989-03-08 Thin film evaporative concentrator

Country Status (1)

Country Link
JP (1) JPH0620483B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5733647A (en) * 1992-11-05 1998-03-31 Polymer Innovations, Inc. Insole
JP6429270B2 (en) * 2014-10-08 2018-11-28 株式会社日立プラントメカニクス Horizontal centrifugal thin film evaporator

Also Published As

Publication number Publication date
JPH02233103A (en) 1990-09-14

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