JPH0679101A - Continuous concentrator - Google Patents
Continuous concentratorInfo
- Publication number
- JPH0679101A JPH0679101A JP24426491A JP24426491A JPH0679101A JP H0679101 A JPH0679101 A JP H0679101A JP 24426491 A JP24426491 A JP 24426491A JP 24426491 A JP24426491 A JP 24426491A JP H0679101 A JPH0679101 A JP H0679101A
- Authority
- JP
- Japan
- Prior art keywords
- main body
- riser
- cylindrical rotor
- concentrated
- present
- 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
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、飲食品、化学薬品等の
濃縮技術において、被濃縮物の流動過程中に、熱交換を
行ない、連続して濃縮せしめるものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for concentrating foods and drinks, chemicals and the like, which allows heat to be exchanged during the flowing process of the substance to be concentrated to be continuously concentrated.
【０００２】従来飲食品や化学薬品等の濃縮、脱溶剤工
程には、種々の機械が使用されその熱交換器も色々使わ
れているが、何れも複雑な構造をとり、種々難点を有し
ていた。Conventionally, various machines have been used and various heat exchangers have been used for the steps of concentrating and removing solvents such as foods and drinks, chemicals, etc., but each has a complicated structure and has various difficulties. Was there.
【０００３】例えば特公昭２６−７８１１号公報に記載
されているものは、加熱管内に螺旋状長管を装置してお
り、その構造は複雑であり、機能も良好なものとはいえ
ない。For example, the one described in Japanese Examined Patent Publication No. 2681/1987 has a spiral long tube installed in a heating tube, its structure is complicated, and its function cannot be said to be good.
【０００４】[0004]
【発明が解決しようとする課題】そこで、本発明者は、
できるだけ簡易な構成で、しかも効率がよく、操作も容
易なものとし、特に短時間操作で連続加熱又は、冷却濃
縮せしめることを課題とし、その研究開発に努力した。Therefore, the inventor of the present invention
With the simplest possible structure, high efficiency, and easy operation, the subject was to continuously heat or cool and concentrate in a short time.
【０００５】[0005]
【発明を解決するための手段】本発明の濃縮機の外周
を、外筒スチームジャケットとし、その内方に適宜間隙
をおいて、内管スチームジャケットを設け、両筒の中間
の環状間隙を、被加工物（これを以下原液という）通路
とすると、ともに、その環状原液通路中に、本体の中央
に設けた回転軸に、円筒形ローター７に、上記内外両ス
チームジャケットに接するスクレッパーブレード及びミ
キシングブレードを取り付け、本体上方または側方別体
に設けた減圧または、常圧もしくわ加圧蒸発室に連結し
た連続濃縮機としたものである。The outer circumference of the concentrator of the present invention is an outer cylinder steam jacket, an inner tube steam jacket is provided with an appropriate gap inside thereof, and an annular gap in the middle of both cylinders is provided. When the workpiece (hereinafter referred to as "stock solution") passage is used, the rotary shaft provided in the center of the main body, the cylindrical rotor 7, the scraper blade and the mixing for contacting both the inner and outer steam jackets are provided in the annular stock solution passage. This is a continuous concentrator in which a blade is attached and is connected to a decompression provided at the upper part of the main body or a side separate body or a normal pressure or a pressure evaporation chamber.
【０００６】次に本発明を図面に記載した実施例につい
て、説明すると、図１に示すものは、本体１の外周に円
筒形外筒スチームジャケット４と、その内方に適宜の間
隙をおいて、内筒スチームジャケット５を設け、両筒の
中間の環状間隙２を被濃縮原液通路２とするとともに、
この環状原液通路中に、本体１の中央に設けた回転軸６
によって、回転される円筒形ローター７に、外筒スチー
ムジャケット４の内壁と、内筒スチームジャケット５の
外壁に接するスクレッパーブレード８及びミキシングブ
レード９を、図面に示すように、交互に、且つ、円筒形
ローター７に一定の角度（被濃縮物の種類、性状に応じ
その角度を異にするものを用意する）を保って図５、図
６の各Ｂに示すように取り付ける。The present invention will now be described with reference to the embodiments shown in the drawings. In the embodiment shown in FIG. 1, a cylindrical outer cylinder steam jacket 4 is provided on the outer periphery of a main body 1, and an appropriate gap is provided inside thereof. , An inner-cylinder steam jacket 5 is provided, and an annular gap 2 between the two cylinders is used as a concentrated liquid passage 2 to be concentrated,
A rotary shaft 6 provided at the center of the main body 1 in the annular stock solution passage.
The rotating cylindrical rotor 7 is provided with the inner wall of the outer cylinder steam jacket 4 and the scraper blades 8 and the mixing blades 9 in contact with the outer wall of the inner cylinder steam jacket 5 alternately and as shown in the drawing. The shaped rotor 7 is attached as shown in each of B of FIGS. 5 and 6 while keeping a certain angle (one having a different angle depending on the kind and property of the substance to be concentrated).
【０００７】なお、本発明の円筒形ローター７は、本体
中央に設けた回転軸６に、等間隔に支柱６′により４カ
所又は３カ所のように無理なく、安定して回転する様に
取り付けられる。The cylindrical rotor 7 of the present invention is mounted on the rotary shaft 6 provided at the center of the main body so that it can be stably rotated without difficulty at four or three places by means of columns 6'at equal intervals. To be
【０００８】また、本発明のスクレッパーブレードの材
質は、耐摩耗性の特殊プラスチックかニッケル合金で作
り、且つ、その基部にバネ反応式アッタチメント８′を
もって装着し、両側の内外両スチームジャケットに確実
に強固に圧接するようにする。Further, the material of the scraper blade of the present invention is made of wear-resistant special plastic or nickel alloy, and is attached with a spring reaction type attachment 8'on its base to surely attach it to both inner and outer steam jackets. Make sure to press firmly.
【０００９】一方本発明のミキシングブレード９は、材
質は金属または、硬質プラスチックをもって作られ、そ
の大きさ、形状、ローター７への取り付け角度は、被濃
縮物に応じて異にしたものを適宜使用する。そして、本
発明のローター７は、本機下方の減速機付きモーター１
８によって、急速に回転されるようにしてある。On the other hand, the mixing blade 9 of the present invention is made of metal or hard plastic, and its size, shape, and attachment angle to the rotor 7 differ depending on the substance to be concentrated. To do. The rotor 7 of the present invention is the motor 1 with a reduction gear under the main unit.
It is made to rotate rapidly by 8.
【００１０】なお、図面中３は、本体下方の原液入口で
あり、１０は、外筒スチームジャケット４の適所（図１
では上方）に設けたスチームの入口であり、１２は、内
筒スチームジャケット５のスチーム入口、１３は、内外
スチームジャケットのドレーン出口、１４は、加熱液２
は冷却液出口、１５は、その誘導管で、１６は減圧発生
室、１７は減圧発生室下方の原液の製品即ち濃縮物（濃
原液又は乾燥粉末）の取り出し口であり、ここに設けた
取り出し用ポンプ２０によって、取り出すものである。Reference numeral 3 in the drawing is a stock solution inlet at the bottom of the main body, and 10 is an appropriate position of the outer cylinder steam jacket 4 (see FIG. 1).
Is a steam inlet provided on the upper side), 12 is a steam inlet of the inner tubular steam jacket 5, 13 is a drain outlet of the inner and outer steam jackets, and 14 is a heating liquid 2.
Is a cooling liquid outlet, 15 is a guide tube thereof, 16 is a decompression generating chamber, 17 is an outlet for a product of the undiluted solution, that is, a concentrate (concentrated undiluted solution or dry powder) below the decompression generating chamber. It is taken out by the pump 20 for use.
【００１１】なお、減圧発生室上方には、蒸気排出管２
１があり、その先端にあるコンデンサー２２へ排出させ
るように成っている。またコンデンサー２２の下方に冷
却水入口２３があり、上方には冷却水出口２４が設けら
れている。Above the decompression chamber, the steam discharge pipe 2
1 and is designed to be discharged to the condenser 22 at the tip thereof. A cooling water inlet 23 is provided below the condenser 22 and a cooling water outlet 24 is provided above the condenser 22.
【００１２】以上、本発明の減圧発生室（コンデンサー
２２を含む）を図１として記載したが、ここに従来周知
の真空（減圧）発生装置を配置することも勿論可能であ
り、図１の記載に限定されるものではない。Although the depressurization generating chamber (including the condenser 22) of the present invention has been described above as FIG. 1, it is of course possible to dispose a heretofore known vacuum (decompression) generating device therein. It is not limited to.
【使用法と作用】次に本発明連続濃縮機の使用法と作用
を説明すると、第一実施例（図１）、第２実施例（図
３）は、ともに本体１の下方の、内外両スチームジャケ
ット４、５の間隙の原液通路２へその下方、原液入口３
から原液を適宜の圧力で送り込めば、その両側の内外ス
チームジャケットにより加熱（又は冷却）されて、高い
伝熱効果と、原液通路２中に設けられた、円筒形ロータ
ー７に取り付けられたスクレッパーブレード８及びミキ
シングブレード９により高い伝熱効果及び強力な機械的
撹拌が行なわれ、短時間に連続濃縮されて、上方の加熱
液（又は冷却液出口）１４より誘導管１５を介して、隣
接して設けた減圧発生室１６に移行し、ここで減圧乾燥
が進み、濃縮固体（粉末）として製品取り出し口１７か
ら適時取り出されるものである。[Usage and Action] Next, the use and action of the continuous concentrator of the present invention will be described. In both the first embodiment (FIG. 1) and the second embodiment (FIG. 3), both inside and outside of the main body 1 To the undiluted solution passage 2 in the gap between the steam jackets 4 and 5, below it, undiluted solution inlet 3
If the undiluted solution is fed at an appropriate pressure from the above, it is heated (or cooled) by the inner and outer steam jackets on both sides of the undiluted solution and has a high heat transfer effect and the scraper attached to the cylindrical rotor 7 provided in the undiluted solution passage 2. The blade 8 and the mixing blade 9 provide a high heat transfer effect and strong mechanical agitation, are continuously concentrated in a short time, and are adjacent from the upper heating liquid (or cooling liquid outlet) 14 via the induction pipe 15. It is transferred to the reduced pressure generating chamber 16 provided therein, where drying under reduced pressure proceeds, and it is taken out as a concentrated solid (powder) from the product taking-out port 17 at appropriate times.
【００１３】次に、第２実施例（図３）に示すものは、
図１の減圧発生室を常圧または加圧発生室１６′とした
もので、これを図面に基づいて説明すると、原液を本体
１の原液入口３から原液通路２に圧送せしめ、内外のス
チームジャケット４、５により加熱（又は冷却）せしめ
るとともに、両筒の中間の環状間隙２中に設けた円筒形
ローター７に取り付けられたスクレッパーブレード８及
びミキシングブレード９の回転により、図１の場合と同
様、原液は、高い伝熱効果及び強力な機械的撹拌によ
り、短時間に連続加熱され、上方の蒸発室１６′に常圧
又は加圧されて移送されて、原液中ベパーは上方のベパ
ー出口１１から外気中に放出され、濃縮された原液は本
機側方に設けた濃縮液出口１７より適時排出されるもの
である。Next, what is shown in the second embodiment (FIG. 3) is
The decompression generation chamber of FIG. 1 is a normal pressure or pressurization generation chamber 16 '. This will be described with reference to the drawings. The stock solution is pressure-fed from the stock solution inlet 3 of the main body 1 to the stock solution passage 2, and the steam jacket inside and outside By heating (or cooling) by 4, 5 and rotation of the scraper blade 8 and the mixing blade 9 attached to the cylindrical rotor 7 provided in the annular gap 2 in the middle of both cylinders, as in the case of FIG. The stock solution is continuously heated in a short time by a high heat transfer effect and strong mechanical agitation, and is transferred to the upper evaporation chamber 16 ′ under normal pressure or under pressure, and the vapor in the stock solution is discharged from the upper vapor outlet 11 of the upper part. The concentrated solution discharged into the outside air and concentrated is discharged from the concentrated solution outlet 17 provided on the side of this machine at appropriate times.
【００１４】[0014]
（実施例１）次に本発明の連続濃縮機の実施例を本機を
使用して実験したものとして記載する。 本発明の外筒スチームジャケットの内径２５０φ（２６
７．３ｍ／ｍ） 本発明の内筒スチームジャケットの外径２１８φ（４
２．０） 両筒の間隙 １６ｍ／ｍ 両スチームジャケットの長さ ３４０ｍ／ｍ 使用動力 １．５ｋｗ の大きさで伝熱面積 ０．５ｍ2の実験機を使用してキ
ャンデ材料として、砂糖６０％ 水飴４０％を溶解し、
濃縮実験を行なった。 操作条件として、 イ．スチーム圧力 ７／ｃｍ2Ｇ（１６９．６℃） ロ．真空度 ８０〜４０Ｔｏｒｒ ハ．蒸発室 濃縮液出口温度 １２０度〜１２５度 結果 上記の操作条件で３０ｍｉｎ間濃縮を行なった結果、 原液組成 １ｗｔ％（水分） 製品量 １００ｋｇ／３０ｍｉｎ＝２００ｋｇ／ｈｒ 蒸発量 ３２ｋｇ／３０ｍｉｎ＝６４ｋｇ／ｈｒ 従来法の濃縮テストとの比較をすると、（但し操作条件
は同様とする。）下表の通りである。なお、従来法とは
特許１８７６２２号の方法を云う。 (Example 1) Next, an example of the continuous concentrator of the present invention will be described as an experiment conducted using this machine. The outer diameter steam jacket of the present invention has an inner diameter of 250 φ (26
7.3 m / m) The outer diameter of the inner cylinder steam jacket of the present invention is 218φ (4
2.0) Gap between both cylinders 16 m / m Length of both steam jackets 340 m / m Power used 1.5 kw and heat transfer area 0.5 m 2 Using an experimental machine, sugar 60% was used as a candy material. Melt 40% starch syrup,
A concentration experiment was performed. The operating conditions are a. Steam pressure 7 / cm 2 G (169.6 ° C) b. Vacuum degree 80 to 40 Torr c. Evaporation chamber Concentrated liquid outlet temperature 120-125 ° Result As a result of concentration for 30 min under the above operating conditions, stock solution composition 1 wt% (water content) Product amount 100 kg / 30 min = 200 kg / hr Evaporation amount 32 kg / 30 min = 64 kg / hr A comparison with the conventional concentration test (however, the operating conditions are the same) is shown in the table below. The conventional method is the method of Japanese Patent No. 187622.
【００１５】（実施例２）実施例１と同じ実験機で行な
った。 キャンデー材料 砂糖 ４％ 水飴 ３５％ 全脂ミルク ４２％ その他 １９％ 上記の材料を配合溶解し、水分を２５％に調整し、濃縮
を行なった。 操作条件 イ．スチーム圧力 ４ｋｇ／ｃｍ2Ｇ（１５１．１℃） ロ．真空度 ２１０Ｔｏｒｒ ハ．蒸気室 濃縮液出口温度 １１５℃ 上記操作条件で、３０ｍｉｎ間濃縮を行なった結果、従
来製造不可能であった乳固形分の多いソフトキャンデー
の製造ができた。従来の方法では、形、色及び味が悪く
製品とならなかったが本発明で色も白色で風味のよい製
品が出来た。 結果 原液組成 ２５ｗｔ％（水分） 原液量 ６０ｋｇ／３０ｍｉｎ＝１２０ｋｇ／ｈｒ 製品組成 ５〜１１ｗｔ％（水分） 製品量 ２０ｋｇ／ｈｒ （注）従来のもの［特許第１８７６２２号］では、乳固
形分が多く、製品ができなかったが、本発明の連続濃縮
機では、可能となった。Example 2 The experiment was carried out in the same experimental machine as in Example 1. Candy material Sugar 4% Starch 35% Full fat milk 42% Others 19% The above ingredients were mixed and dissolved, the water content was adjusted to 25%, and the mixture was concentrated. Operating conditions a. Steam pressure 4 kg / cm 2 G (151.1 ° C) b. Vacuum degree 210 Torr c. Steam chamber Concentrated liquid outlet temperature: 115 ° C. Under the above operating conditions, concentration was carried out for 30 minutes. As a result, soft candy with a high milk solid content, which could not be produced conventionally, could be produced. According to the conventional method, a product having bad shape, color and taste was not obtained, but the present invention made a product having a white color and a good taste. Result Undiluted solution composition 25 wt% (water content) Undiluted solution quantity 60 kg / 30 min = 120 kg / hr Product composition 5-11 wt% (water content) Product quantity 20 kg / hr (Note) In the conventional one [Patent No. 187622], the milk solid content is large. The product could not be produced, but it became possible with the continuous concentrator of the present invention.
【００１６】（実施例３）本実施例は、本発明の連続濃
縮機を冷却濃縮機として使用した場合のものである。こ
の場合は、当然本発明中の熱交換機として外筒スチーム
ジャケット４及び内筒スチームジャケット５は冷却水に
おき替えるものである。実施機は、実施例１と同様の実
験機で内外のスチームジャケットには冷却水を導入した
ものである。 Ａ．原料 酵素糖化ブドー液を１０％（水分）以下に濃縮した濃縮
液を原液とした。 Ｂ．操作条件 原料ブドー糖液の温度 １１０℃ 冷却水条件 入口温度 １２℃ 出口温度 ４０℃ 撹拌条件 ３５〜４０ｎｐｍ Ｃ．結果 原料処理 １２８ｋｇ／ｈｒ処理 従来の冷却結晶機との比較をすると（横型撹拌機付外部
冷却水ジャケット） 従来品（上記）結晶機 処理能力 １５０ｋｇ／ｈｒｍ
2 実施例３ ２９６ｋｇ／ｈｒｍ2 （但し冷却水条件は同一とした）(Embodiment 3) In this embodiment, the continuous concentrator of the present invention is used as a cooling concentrator. In this case, the outer cylinder steam jacket 4 and the inner cylinder steam jacket 5 are naturally replaced with cooling water as the heat exchanger in the present invention. The embodying machine is the same experimental machine as that of the first embodiment, and cooling water is introduced into the inner and outer steam jackets. A. Raw material A concentrated solution obtained by concentrating the enzymatically saccharified Budo solution to 10% (water content) or less was used as a stock solution. B. Operating conditions Raw material Budo sugar temperature 110 ° C Cooling water condition Inlet temperature 12 ° C Outlet temperature 40 ° C Stirring condition 35-40npm C.I. Results Raw material treatment 128kg / hr treatment Comparison with conventional cooling crystallizer (external cooling water jacket with horizontal stirrer) Conventional product (above) Crystallizer processing capacity 150kg / hrm
2 Example 3 296 kg / hrm 2 (however, the cooling water conditions were the same)
【００１７】以上の結果 同一条件での能力は約５０％良く、しかも、品質に於て
も白色の非常に良好な製品が得られた。As a result of the above, an ability of about 50% was obtained under the same conditions, and a white product having a very good quality was obtained.
【００１８】[0018]
【発明の効果】本発明は、上述の構成と操作によって、
従来の加熱（または冷却）濃縮機と比べて下記の機能と
効果を有する。 イ．原液通過路の両側面を加熱（冷却）するので装置の
小型化が出来、且つ、熱効率も高い。 ロ．外筒スチームジャケットと内筒スチームジャケット
の間の原液通路中に設けた円筒形ローターに取り付けた
スクレッパーブレードとミキシングブレードが回転する
様になっているので伝熱効率と強力な撹拌効果が得ら
れ、且つ、被濃縮品の濃縮時間が短いので、その変質も
なく、形、色、味の優れた製品が得られる。 ハ．本発明の連続熱交換機は、濃縮加熱（又は冷却）混
合、晶折、殺菌、溶剤の回収等幅広い用途とその利用範
囲の拡大が出来飲食品、化学薬品等の連続濃縮機として
有効なものである。The present invention has the following features and operations.
It has the following functions and effects as compared with the conventional heating (or cooling) concentrator. I. Since both sides of the undiluted solution passage are heated (cooled), the device can be downsized and the thermal efficiency is high. B. Since the scraper blade and mixing blade attached to the cylindrical rotor provided in the stock solution passage between the outer cylinder steam jacket and the inner cylinder steam jacket are designed to rotate, heat transfer efficiency and a strong stirring effect are obtained, and Since the concentration time of the product to be concentrated is short, it is possible to obtain a product excellent in shape, color and taste without deterioration. C. INDUSTRIAL APPLICABILITY The continuous heat exchanger of the present invention is effective as a continuous concentrator for food and drink, chemicals, etc., which can be used for a wide range of applications such as concentrated heating (or cooling) mixing, crystallizing, sterilization, and solvent recovery, and its range of use can be expanded. is there.
【図１】本発明の一実施例で、減圧蒸発室を本体と別体
としたものの縦断面図。FIG. 1 is a vertical sectional view of an embodiment of the present invention in which a reduced pressure evaporation chamber is separated from a main body.
【図２】そのＸ−Ｘ線の横断面図。FIG. 2 is a cross-sectional view taken along the line XX.
【図３】本発明の蒸発室を本体上方に設け、常もしくは
加圧蒸発室とした縦断側面図。FIG. 3 is a vertical cross-sectional side view in which the evaporation chamber of the present invention is provided above the main body and used as a normal or pressurized evaporation chamber.
【図４】上記のＹ−Ｙ線の横断面図。FIG. 4 is a transverse sectional view taken along the line YY.
【図５】Ａは、本発明の内外のスチームジャケットの間
に設ける４点支柱に円筒形ローターの平面図。Ｂは、上
記Ａの円筒形ローターの展開図。FIG. 5A is a plan view of a cylindrical rotor on a four-point support provided between the inner and outer steam jackets of the present invention. B is a development view of the cylindrical rotor of A above.
【図６】Ａは、本発明の原液通路に設けた３点支柱の円
筒形ローター。Ｂは、上記６Ａの円筒形ローターの展開
図。FIG. 6A is a cylindrical rotor having a three-point support provided in the stock solution passage of the present invention. B is a development view of the cylindrical rotor of 6A.
１ 本体 ２ 原液通路 ３ 原液入口 ４ 外筒スチームジャケット ５ 内筒スチームジャケット ６ 回転軸 ６′ 回転軸支柱 ７ 円筒形ローター ８ スクレッパーブレード ９ ミキシングブレード １０ 外筒スチーム入口 １１ ベーパー出口 １２ 内筒スチーム入口 １３ 内外両筒のドレーン出口 １４ 加熱液（冷却液）出口 １５ 誘導管 １６ 減圧発生室 １６′ 常圧又は加圧発生室 １７ 製品取り出し口 １８ ローター回転モーター １９ 真空ポンプ ２０ 製品取り出し用ポンプ ２１ 蒸気排出管 ２２ コンデンサー ２３ 冷却水入口 ２４ 冷却水出口 1 Main Body 2 Undiluted Liquid Passage 3 Undiluted Liquid Inlet 4 Outer Cylinder Steam Jacket 5 Inner Cylinder Steam Jacket 6 Rotating Shaft 6'Rotating Shaft Support 7 Cylindrical Rotor 8 Scraper Blade 9 Mixing Blade 10 Outer Cylinder Steam Inlet 11 Vapor Outlet 12 Inner Cylinder Steam Inlet 13 Drain outlets for both inner and outer cylinders 14 Heating liquid (cooling liquid) outlet 15 Induction pipe 16 Decompression generation chamber 16 'Normal pressure or pressure generation chamber 17 Product outlet 18 Rotor rotation motor 19 Vacuum pump 20 Product retrieval pump 21 Steam exhaust pipe 22 condenser 23 cooling water inlet 24 cooling water outlet
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成５年８月３０日[Submission date] August 30, 1993
【手続補正１】[Procedure Amendment 1]
【補正対象書類名】図面[Document name to be corrected] Drawing
【補正対象項目名】全図[Correction target item name] All drawings
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【図１】 [Figure 1]
【図２】 [Fig. 2]
【図３】 [Figure 3]
【図４】 [Figure 4]
【図５】 [Figure 5]
【図６】 [Figure 6]
Claims (1)
し、内方に間隙をおいて、内筒スチームジャケットを設
け、両筒の中間の環状間隙を被加工物の通路とするとと
もに、この環状通路中に、本体中央に設けた回転軸に、
内外両スチームジャケットに接するスクレッパーブレー
ド及びミキシングブレードを取り付け、本体上方また
は、別に設けた減圧または、常圧もしくわ加圧蒸発室に
連結したことを特徴とする連続濃縮機。Claim: What is claimed is: 1. An outer cylinder steam jacket is provided on the outer periphery of a main body, an inner cylinder steam jacket is provided with a gap inward, and an annular gap in the middle of both cylinders is used as a passage for a workpiece. Inside, on the rotating shaft provided in the center of the main body,
A continuous concentrator, which is equipped with a scraper blade and a mixing blade in contact with both the inner and outer steam jackets and is connected to a reduced pressure or normal pressure or pressure evaporation chamber provided above the main body or separately.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3244264A JP2929400B2 (en) | 1991-08-30 | 1991-08-30 | Continuous concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3244264A JP2929400B2 (en) | 1991-08-30 | 1991-08-30 | Continuous concentrator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0679101A true JPH0679101A (en) | 1994-03-22 |
| JP2929400B2 JP2929400B2 (en) | 1999-08-03 |
Family
ID=17116168
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3244264A Expired - Fee Related JP2929400B2 (en) | 1991-08-30 | 1991-08-30 | Continuous concentrator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2929400B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013530835A (en) * | 2010-07-21 | 2013-08-01 | アクアバック・テクノロジーズ・インコーポレーテッド | Distillation equipment |
| KR20240019356A (en) | 2021-07-19 | 2024-02-14 | 가부시끼가이샤 도시바 | Information processing devices, information processing methods and recording media |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6447401A (en) * | 1987-08-13 | 1989-02-21 | Toshiba Corp | Centrifugal thin-film drier |
| JPH0243521A (en) * | 1988-08-03 | 1990-02-14 | Hitachi Ltd | Organic nonlinear optical element |
-
1991
- 1991-08-30 JP JP3244264A patent/JP2929400B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6447401A (en) * | 1987-08-13 | 1989-02-21 | Toshiba Corp | Centrifugal thin-film drier |
| JPH0243521A (en) * | 1988-08-03 | 1990-02-14 | Hitachi Ltd | Organic nonlinear optical element |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013530835A (en) * | 2010-07-21 | 2013-08-01 | アクアバック・テクノロジーズ・インコーポレーテッド | Distillation equipment |
| US9770676B2 (en) | 2010-07-21 | 2017-09-26 | Aquaback Technologies, Inc. | Distiller |
| KR20240019356A (en) | 2021-07-19 | 2024-02-14 | 가부시끼가이샤 도시바 | Information processing devices, information processing methods and recording media |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2929400B2 (en) | 1999-08-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0384480B1 (en) | Process for continously drying paste material for a high-density detergent | |
| RU96104259A (en) | THERMAL PROCESSING EXTRUDER FOR PRODUCING BIOPOLYMERS, AND ALSO THE EXTRUDING PROCESS OF BIOPOLYMERS WITH THERMAL PROCESSING | |
| JPH0679101A (en) | Continuous concentrator | |
| US2917372A (en) | Liquid-gas contact reactor | |
| CN211562939U (en) | Even heating and cooling reaction kettle | |
| WO2020158551A1 (en) | Organic sludge treatment facility and treatment method | |
| EA037138B1 (en) | Apparatus and method for enhancing phase contact and chemical reactions | |
| JP2005331210A5 (en) | ||
| GB1518468A (en) | Method and apparatus for manufacturing crystalline food products | |
| CN207384873U (en) | A kind of scraper evaporator device with screw conveyor | |
| KR20210122748A (en) | Crystallizer for extracting powder from sludge or liquid using centrifugal force | |
| US3769900A (en) | Processing of animal material compositions | |
| JPH0329377B2 (en) | ||
| JPS6226801B2 (en) | ||
| CN213133138U (en) | Evaporation reactor and lactide production system | |
| SU954095A1 (en) | Evaporation apparatus | |
| SU789087A1 (en) | Device for thermal and vacuum treatment of liquid foodstuffs | |
| CN219743929U (en) | Shell structure of evaporator | |
| JPH0351037Y2 (en) | ||
| JPH0531301A (en) | Continuous heat exchanger in heating concentrator | |
| JP3171614U (en) | Manufacturing system for recycled soy broth | |
| SU1463745A1 (en) | Mash-boiling apparatus of continuous action | |
| JPH03290164A (en) | Steam boiler for mashed soybean soup and continuous steaming system | |
| KR19980033439A (en) | Fermentation Dryer and Drying Method | |
| SU897197A2 (en) | Rotor film apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |