JPH02233103A - Thin membrane type evaporative concentration apparatus - Google Patents
Thin membrane type evaporative concentration apparatusInfo
- Publication number
- JPH02233103A JPH02233103A JP5386689A JP5386689A JPH02233103A JP H02233103 A JPH02233103 A JP H02233103A JP 5386689 A JP5386689 A JP 5386689A JP 5386689 A JP5386689 A JP 5386689A JP H02233103 A JPH02233103 A JP H02233103A
- Authority
- JP
- Japan
- Prior art keywords
- cylinder
- shaft
- thin film
- stirring
- stirring blade
- 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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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
【発明の詳細な説明】
く産業上の利用分野〉
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、攪拌ブレードにより攪拌混合作用を与
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 Application Fields The disclosed technology is applicable to obtaining products such as foods, medicines, fertilizers, etc.
This equipment is capable of supplying a highly viscous raw material liquid from one side, evaporating the volatile matter through heating action, giving a stirring and mixing action using a stirring blade to highly concentrate, powdering, and discharging as a product. Belongs to the structural technology field.
〈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で、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攪拌
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攪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攪拌ブレードの基
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
、攪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VcMに係る発明であ
る。<Summary> The invention of this application is a process in which a highly viscous raw material liquid is supplied, concentrated, and discharged as a product, in which the raw material liquid of the object to be processed is formed into a thin film and subjected to a heating reaction. It is a thin film type evaporation concentrator that can obtain a product by applying a mixing and stirring action in addition to the evaporation process and concentrating it to a powder state through a concentration process, and is equipped with a jacket for heat exchange on the outside. At the same time, a shaft is mounted on a cylinder that has a supply section for a processed material such as a highly viscous raw material liquid on one side and a discharge section for a powdered product on the other side, and the shaft has a predetermined number of stages arranged at predetermined intervals in the axial direction. This invention relates to a thin film type evaporation concentrator in which a plurality of stirring blades are provided so as to be able to freely swing in the circumferential direction, and the tips thereof are brought close to the inner surface of a cylinder through a minute clearance to enhance the concentration effect, and in particular, The shaft is connected to the base of the stirring blade via a pin so that it can swing freely to the blade holder, and an adjustment body such as a shim is used to adjust the minute clearance of the stirring blade to the inner surface of the cylinder during operation during assembly. This invention relates to a thin film type evaporative concentration VcM in which a 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 people's lives improve, various products are handled in large quantities and small quantities.Therefore, a stable supply of these products is desired, and high-precision quality is also strongly required. It's starting to look like this.
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、二次加工ざれた食品、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 include primary products such as agricultural products and marine products, but a variety of secondary processed products such as foods, medicines, and cosmetics are also distributed.
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、野菜ピューレ、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, there are many products such as candies, creams, and medicines, and some of these products are in the form of jelly, but there are also liquid products such as fruits, vegetable purees, sauces, and soups. There are also products in the form of creams, resin products in the form of granules, chemicals, etc. The manufacturing process for these products with special properties is preferably reduced in man-hours in terms of cost and product accuracy. There is a desire for easy handling and less waste.
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ざれて採用ざれ実用化ざれ
ているが、例えば、第7、8図に示す様な境模式熱交換
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に連結ざれた軸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・・・により混合潰拌しながら
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1
5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。To deal with this, reaction devices that perform thermal reactions through physicochemical heat exchange have been developed, adopted, and put into practical use. The heat exchange reactor 1 is equipped with a drum-type cylinder 3 having a heat exchange jacket 2 on the outside, bearings 5 on the front and rear end walls, and a shaft 8 connected to a motor 7 via a mechanical seal 6. A shaft 9 is integrally provided, and a predetermined number of blades 11, 11, . A predetermined high-viscosity raw material liquid 13 is supplied through the supply port 12 on one side of the cylinder 3, and while being mixed and crushed by the blades 11, 11, etc., a thin film is formed between it and the inner peripheral surface of the cylinder 3 through the centrifugal force. The high temperature heat medium 1 is applied to the jacket 2 by forming a film of
5 is supplied from the supply port 14 and subjected to physicochemical heat exchange to carry out a thermal reaction as soon as possible to make it even more viscous, or to change it into granules through thermal transformation and transfer it to the other side of the cylinder 3. The product 18 was taken out from a discharge port 17 provided.
〈発明が解決しようとする課題〉
きりながら、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、ロー夕が複段のブレード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プレート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
がおり、初期組み付け製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。<Problem to be solved by the invention> While cutting, the membrane heat exchange reactor 1 of the conventional mode
In this case, the jacket 2 for heat exchange is placed on the outside of the cylinder 3.
Because the unit is installed, rapid heat changes depending on the product, such as switching between high-temperature heat medium and low-temperature heat medium, or heat exchange with a sudden thermal gradient, are not possible.
There is a drawback that products with these thermal histories cannot be obtained,
In addition, since the rotor slides against the inner circumferential surface of the cylinder 3 using multiple stages of blades 11, 11, etc., there is a problem in that it is difficult to perform a continuous reaction. The structure is extremely complicated, with plate 11 and cylinder 3.
It is extremely difficult to connect to the inner circumferential surface, requires great skill, and requires complicated work during initial assembly and manufacturing.
As a result, the cost is high, and maintenance such as maintenance, inspection, etc. is difficult, resulting in poor serviceability.
そして、これらのネックにより製品コストに跳杓返る不
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 bottlenecks have the disadvantage of increasing product costs, and the temperature 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
発ざれ、攪拌ブレード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、攪拌ブレード11′
はブレードホルダ10’ に対しピン22で枢支し、
該攪拌ブレード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、混合攪拌作用をも効
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。In response to this, the applicant and others have carried out intensive research and development, and have developed a thin film type evaporation concentrator 1' as shown in Nos. 9, 10, and 11. Attach the stirring blade 11'
is pivoted to the blade holder 10' by a pin 22,
The stirring blade 11' is made swingable so that its tip can form minute clearances 21, 21' with the inner surface of the cylinder 3, as shown in FIG. The material to be processed is formed into a thin film to improve the evaporation and heating effect through heating by the jacket 2, and the mixing and stirring effect is also effectively imparted to improve the concentration efficiency. The product 18' from the outlet 17 can now be made into a powder as a result of high concentration.
しかしながら、核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。However, although the nuclide thin film type evaporative concentrator 1' solves the problems of the film type concentrator described above, the following new problems have arisen.
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から残漬量も減少し、当該残漬物
の廃棄処理対策も容易に行え、溶剤等の有効再利用等も
促進される効果がおるが、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
す攪拌ブレード11′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。In other words, the higher the degree of concentration of the supplied material to be treated, the less the amount of leftover residue, which makes it easier to dispose of the leftover waste, and promotes the effective reuse of solvents, etc. Naturally, this effect is due to the concentration efficiency of the thin film type that achieves high concentration, that is, the formation of the minute clearance 21 between the tip of the stirring blade 11' and the inner surface of the cylinder 3 as shown in FIG. 11 as designed. It has become clear that the world plays an extremely important role.
きりながら、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。However, since the thin film evaporation concentrator 1' is machined and has many specific parts, errors may occur during manufacture and assembly of each part, and if the tolerance is exceeded, it may not be possible to achieve the high concentration as designed. In addition, maintaining the minute clearance as designed requires a high degree of skill in assembly and maintenance, resulting in the inconvenience of high production costs and difficulty in actual operation. It's here.
〈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。<Purpose of the Invention> The purpose of the invention of this application is to solve the technical problem of a basic thin film type evaporation concentrator that overcomes the problems of the film type concentrator etc. based on the above-mentioned prior art. We have developed an excellent thin-film evaporative concentrator that can fully utilize the advantages of conventional thin-film evaporative concentrators and obtain concentrated powder products as designed, thereby benefiting the application of chemical and mechanical equipment in the chemical manufacturing industry. This is what we intend to provide.
く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
休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
ブレードホルダにビンを介して攪拌ブレードをスイング
自在に枢支し、攪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で回転す
る攪拌ブレードによりシリンダ内面に薄膜式に流過して
加熱混合攪拌がなされて蒸発が促進ざれると共に、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
ざれるようにした技術的手段を講じたものである。In order to solve the above-mentioned problems, the structure of the present invention, which is based on the above-mentioned object and the gist of the above-mentioned patent claims, is to solve the above-mentioned problems. A chamfered portion is formed at a predetermined axial portion of the shaft that is extended from the connected rotating shaft, and the blade holder is attached to the chamfered portion by interposing an adjusting body such as a shim with a predetermined minute thickness. A stirring blade is swingably supported on the blade holder via a bottle, the tip of the stirring blade is made to form a set minute clearance on the inner surface of the cylinder, and a predetermined material to be processed is supplied from the supply section, and the cylinder is moved into the cylinder. When a heat exchange fluid is supplied to the outer jacket of the cylinder and the material to be processed is passed through while exchanging heat, the material to be processed is flowed in a thin film form on the inner surface of the cylinder by a stirring blade rotating on the inner surface of the cylinder. Technical measures have been taken to promote evaporation by heating, mixing, and stirring, and to achieve high concentration so that the powdered product is discarded near the discharge section.
〈実施例〉
次に、この出願の発明の実施例を第1乃至6図に基づい
て説明すれば以下の通りである。<Example> Next, an example of the invention of this application will be described below based on FIGS. 1 to 6.
第1乃至3図に示す実施例に於で、10′ はブレ−ド
ホルダであり、攪拌ブレード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
′が形成ざれ、ブレードホルダ10’基部の座10’が
ボルト23により締結固定ざれるようにされており、ビ
ン22を介し攪拌ブレード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Δh
だけ設計通りに形成することが出来るようにざれており
、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
る虞がお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2
4を介装させて設計通りの微小クリアランス21がΔh
形成することができるようにざれている。In the embodiment shown in FIGS. 1 to 3, reference numeral 10' denotes a blade holder, which attaches the stirring blade 11' to the shaft 9 in a freely swingable manner, and mounts the stirring blade 11' along the axial direction of a predetermined portion of the shaft 9. Flat chamfered portion 9 of predetermined size
' is formed, and the seat 10' at the base of the blade holder 10' is fastened and fixed with a bolt 23, and the agitating blade 11' is swingably attached via a bottle 22, and its tip is connected to the cylinder 3. In the meantime, as mentioned above,
The micro clearance 21 for high concentration during operation is Δh
However, by machining the chamfer 9' of the shaft 9,
Furthermore, since there is a possibility that the machining finish of the seat 10' of the blade holder 10' may vary, resulting in slight variations in the clearance, in the invention of this application, the seat 10'
When the chamfered portion 9' of the shaft 9 is attached to the chamfered portion 9' of the shaft 9 via the bolt 23, a shim 2 is inserted between the two as an adjusting body.
4 is inserted, the minute clearance 21 as designed is Δh
It is roughened so that it can be formed.
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を用怠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21Δhが形成ざれるように
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
Δh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図に示す様に厚ざの若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、攪拌ブレード11′
とシリンダ3との内面との間の微小クリアランス21Δ
hを最適なものにするようにすることが可能である。Incidentally, the shim serving as the adjusting body may be one piece as in the embodiment shown in FIG. Of course, it is necessary to select and use shims so that the minute clearance 21Δh as designed is not formed, but as shown in FIG. Of course, it is possible to form a minute clearance Δh according to the optimal design by combining a thin shim with a very thick shim as shown in Fig. 5. Furthermore, as in the embodiment shown in FIG. 6, the seat 10' of the blade holder 10' may have different thicknesses, and by selecting a combination of this and the shim 24', the agitating blade 11'
Minute clearance 21Δ between and the inner surface of cylinder 3
It is possible to try to make h optimal.
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を介して攪拌ブレード11′をス
イング自在に取付けることにより、稼動中における攪拌
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Δhは設計通りの微小クリアランス
に形成ざれて、供給口12から供給ざれる溶剤等の被処
理物23はシリンダ3内の濃縮処理部内に於で排出口1
7へ流過される間に流過する加熱流体により加熱ざれ、
又、攪拌ブレード11’ 、11’・・・により攪拌混
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、高濃縮ざれ、終期
プロセスにおいては粉末化ざれて製品18′ として取
り出ざれる。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 the bolt 23 is tightened to attach the pin 22 to the blade holder 10'. By attaching the agitating blade 11' so that it can swing freely through the agitator blade 11', the minute clearance 21 Δh between the tip of the agitating blade 11' and the inner surface of the cylinder 3 during operation is formed to the designed minute clearance, and the supply port is closed. The material to be treated 23 such as a solvent supplied from the cylinder 3 is discharged from the discharge port 1 in the concentration processing section in the cylinder 3.
7 is heated by the heating fluid flowing through it,
In addition, the stirring blades 11', 11', etc. stir and mix the mixture, and the minute clearance 21 between the tip and the inner surface of the cylinder 3 promotes evaporation, resulting in highly concentrated scum, and in the final process, the product is powdered. 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 matter is discharged from the evaporation port 19 as evaporated matter 20. In this way, for example, the following table shows experimental data comparing the concentration of waste solvents used in the painting process of automobiles as objects to be treated.
廃棄溶剤の高濃度比較表
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がるどころか売
却利益が得られて経費的にもプラスすることが分る。Comparison Table of High Concentration of Waste Solvents As shown in the data in the comparison table, compared to the conventional embodiment, according to the invention of this application, when the processing capacity is at this level, the degree of concentration is relatively improved, and the amount of residue is reduced. 200 kg is reduced, there are fewer workers and there is almost no odor, work can be carried out safely and efficiently, more solvent is collected, costs can be reduced, and since the residue is powdered, for example,
It can be sold as bulking material, and even for residues that could only be incinerated in the past, instead of incurring incineration costs, it can be seen that profits from the sale can be made, which is beneficial in terms of costs.
尚、この発明の実!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
方向にテーバー状に形成する等種々の態様が採用可能で
ある。The fruit of this invention! It goes without saying that the mode is not limited to the above-mentioned embodiment, and various modes can be adopted, such as forming a shim into a tapered shape in the thickness direction as the adjusting body.
く発明の効果〉
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攪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
ンスの形成が攪拌ブレードをブレードホルダを介してシ
ャフ1〜に組付ける取合部に於で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、攪拌ブレー
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、設計通りの攪拌蒸発による高
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, the supplied material is highly concentrated while exchanging heat, and the solvent etc. are evaporated and powdered to obtain a product by thin film evaporation. In a concentrator, the formation of a minute clearance at the tip of the stirring blade, which can swing freely against the inner surface of the cylinder through the centrifugal force of the stirring blade, which is extremely important for powderization in the high concentration process, moves the stirring blade to the shaft 1 through the blade holder. By interposing an adjustment body such as a shim in the fitting part to be assembled, it is possible to accurately form the minute clearance between the stirring blade and the inner surface of the cylinder during operation as designed, without requiring any skill, and to achieve stirring as designed. The excellent effect of obtaining powder through high concentration through evaporation is achieved.
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、残清但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1qにすらな
るという利点がある。Therefore, the solvent separation efficiency of the supplied material to be processed is high, and the rate of recovery and reuse is high, leading to cost reductions. It is not a residue, so it is not incinerated, etc.
It has the advantage that it can be reused as bulking material, etc., or even made into a commercial product, which not only reduces the cost of incineration but also increases the profit by 1q.
又、稼動中における攪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
溌縮の粉末が1qられて従来の粘性の高い残漬と異なり
、焼却等必要がなくなり、焼却費も削減ざれ、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, because the minute clearance on the inner surface of the cylinder due to the freely swingable rotation of the stirring blade during operation is always stably obtained, thin-film evaporation is performed as designed, and 1q of highly compressed powder is produced compared to the conventional method. Unlike highly viscous residue, there is no need for incineration, reducing incineration costs;
There is also the advantage that profits can be generated by commercializing it as a bulking material or the like.
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。In addition, by interposing an adjustment body such as a shim between the blade holder and the shaft, not only can extremely delicate micro-clearances be formed as designed, but also the micro-clearances do not fluctuate during operation, making it stable. Another advantage is that thin-film evaporation concentration can be performed.
第1乃至10図はこの出願の発明の実施例の説明図でお
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図は攪拌ブレー
ドとシリンダ内而の微小クリアランスの側面図でおる。
第3図
第4図
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′ ・・・攪拌ブレード、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、第5図
第
図1 to 10 are explanatory diagrams of embodiments of the invention of this application, in which FIG. 1 is an enlarged cross-sectional view of one embodiment, FIG. 2 is an enlarged side view of the same part, and FIG. 3 is a blade holder and shaft. Figures 4, 5, and 6 are enlarged sectional views corresponding to Figure 3 of other embodiments, Figure 9 is a longitudinal sectional view of the entire device, and Figure 10 is an enlarged sectional view of the joint part.
7 is a longitudinal sectional view of the implementation device based on the prior art, FIG. 8 is a lateral sectional view of the same, and FIG. 11 is a side view of the minute clearance between the stirring blade and the inside of the cylinder. Figure 3 Figure 4 2...Jacket, 13...Workpiece, 12.
... Supply section, 17... Discharge section, 18'... Product, 3... Cylinder, 10... Shaft,
11'... Stirring blade, 1'... Thin film evaporation concentrator, 21... Minute clearance, 14... Regulator (shim), 10'... Blade holder, 9'... Chamfering Section, Figure 5
Claims (4)
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攪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、上記シャフトと攪拌ブレードとの取合部に該攪拌
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 thin film in which a plurality of stirring blades, each having a tip close to the inner surface of the cylinder, are swingably pivoted in the axial direction on a shaft that is equipped with a jacket and is attached to a cylinder that has a processing material supply section and a product discharge section. In the type evaporation concentrator, an adjustment body is installed at the joint between the shaft and the stirring blade to adjust a minute clearance during operation between the stirring blade and the inner surface of the cylinder during assembly. Thin film evaporation concentration equipment.
求の範囲第1項記載の薄膜式蒸発濃縮装置。(2) The thin film evaporation concentration device according to claim 1, wherein the regulator is a shim.
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 evaporation concentration device according to claim 2, wherein the shim is interposed between the shaft and the blade holder.
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) The thin film evaporation concentration device according to claim 3, wherein a chamfer is formed on the blade holder attachment portion of the shaft.
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 true JPH02233103A (en) | 1990-09-14 |
| JPH0620483B2 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) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5733647A (en) * | 1992-11-05 | 1998-03-31 | Polymer Innovations, Inc. | Insole |
| JP2016073947A (en) * | 2014-10-08 | 2016-05-12 | 株式会社日立プラントメカニクス | Horizontal centrifugal thin film evaporator |
-
1989
- 1989-03-08 JP JP5386689A patent/JPH0620483B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5733647A (en) * | 1992-11-05 | 1998-03-31 | Polymer Innovations, Inc. | Insole |
| JP2016073947A (en) * | 2014-10-08 | 2016-05-12 | 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 |
|---|---|
| JPH0620483B2 (en) | 1994-03-23 |
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