JPH0619342B2 - Vacuum drying tester - Google Patents
Vacuum drying testerInfo
- Publication number
- JPH0619342B2 JPH0619342B2 JP60109582A JP10958285A JPH0619342B2 JP H0619342 B2 JPH0619342 B2 JP H0619342B2 JP 60109582 A JP60109582 A JP 60109582A JP 10958285 A JP10958285 A JP 10958285A JP H0619342 B2 JPH0619342 B2 JP H0619342B2
- Authority
- JP
- Japan
- Prior art keywords
- drying
- vacuum
- plate
- medium
- heating
- 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
Links
- 238000001291 vacuum drying Methods 0.000 title claims description 22
- 238000001035 drying Methods 0.000 claims description 39
- 238000010438 heat treatment Methods 0.000 claims description 26
- 238000001816 cooling Methods 0.000 claims description 13
- 239000002826 coolant Substances 0.000 claims description 12
- 239000000498 cooling water Substances 0.000 claims description 7
- 239000002994 raw material Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- 230000008569 process Effects 0.000 claims description 6
- 239000002002 slurry Substances 0.000 claims description 6
- 239000004744 fabric Substances 0.000 claims description 5
- 229920002994 synthetic fiber Polymers 0.000 claims description 5
- 239000012209 synthetic fiber Substances 0.000 claims description 5
- 235000013305 food Nutrition 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- 239000006072 paste Substances 0.000 description 6
- 239000010409 thin film Substances 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 241000287828 Gallus gallus Species 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 235000014347 soups Nutrition 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 238000010411 cooking Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000006694 eating habits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 235000021067 refined food Nutrition 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 238000005092 sublimation method Methods 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Freezing, Cooling And Drying Of Foods (AREA)
- Testing Resistance To Weather, Investigating Materials By Mechanical Methods (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は真空乾燥試験機に関するものであり、更に詳し
くは本格操業に先立って真空乾燥条件を選定するため、
液状、スラリー状もしくはペースト状に調合された比較
的少量の原材料に試験的な真空乾燥処理を施すための真
空乾燥試験機に関するものである。TECHNICAL FIELD The present invention relates to a vacuum drying tester, and more specifically, for selecting vacuum drying conditions prior to full-scale operation,
The present invention relates to a vacuum drying tester for performing a trial vacuum drying treatment on a relatively small amount of raw materials prepared in a liquid, slurry or paste form.
従来の技術 近年、食生活の多様化に伴って数多くの種類の加工食品
材料やインスタント食品が市販されている。このような
食品加工分野に於いては、消費者が製品を調理素材とし
て使用する場合の溶解生と即席性を所定の水準に維持す
ると共に、最終製品に品質の低下と成分の変質を伴わな
い復元性を付与する目的で、各種の常圧乾燥装置や真空
乾燥装置が使用されている。このような乾燥装置のなか
でも調理素材たる製品の溶解性を良好な水準に維持する
ことが比較的容易である点に着目され、真空乾燥装置の
使用分野が急速に増大しつつある。汎用の真空乾燥装置
としては、噴霧乾燥機や凍結乾燥機が知られているが、
前者は乾燥コストが安価である反面、製品の溶解性と品
質の保持性能あるいは成分変化の防止性能が幾分劣り、
後者は氷結・昇華行程を採用していることに起因して構
造の複雑化や乾燥コストの高騰という問題点を付随せし
めている。ここに於いて、上記噴霧乾燥機や凍結乾燥機
に認められている実用上の問題点の解決手段として、真
空ベルト乾燥機の開発が要請されるに至った。真空ベル
ト乾燥機は、真空容器内に加熱ゾーンとベルト搬送装置
を設け、液状、スラリー状、もしくはペースト状に調合
された食品材料を無端搬送ベルト上に薄膜状に供給し、
該無端搬送ベルトの回転によって食品材料を加熱ゾーン
に導き、比較的低温の乾燥条件下で真空乾燥を施すよう
に構成されている。この際、ベルト上に薄膜状を呈して
載置された食品材料には内部に含有されている水分の激
しい蒸発現象が生起して、食品材料は膨脹化しながら内
部に多数の通気孔を形成し、多孔質の中間製品としてク
ラッシャーに送り出される。2. Description of the Related Art In recent years, many kinds of processed food materials and instant foods have been marketed with the diversification of eating habits. In such a food processing field, the consumer maintains the solubility and immediacy when using the product as a cooking ingredient at a predetermined level, and the final product is free from deterioration of quality and deterioration of ingredients. Various atmospheric dryers and vacuum dryers are used for the purpose of imparting restoration properties. Focusing on the fact that it is relatively easy to maintain the solubility of a product as a cooking ingredient at a good level among such dryers, the fields of use of vacuum dryers are rapidly increasing. Spray dryers and freeze dryers are known as general-purpose vacuum dryers.
The former has a low drying cost, but the solubility and quality retention performance of the product or the component change prevention performance is somewhat inferior.
The latter is accompanied by the problems of complicated structure and soaring drying cost due to the adoption of freezing and sublimation processes. Here, the development of a vacuum belt dryer has been demanded as a means for solving the practical problems recognized in the spray dryer and the freeze dryer. The vacuum belt dryer is provided with a heating zone and a belt transfer device in a vacuum container, and supplies a food material prepared in a liquid form, a slurry form, or a paste form in a thin film form on an endless transfer belt,
The rotation of the endless conveyor belt guides the food material to the heating zone, and vacuum drying is performed under relatively low temperature drying conditions. At this time, the food material placed in a thin film on the belt undergoes a rapid evaporation phenomenon of the water contained therein, and the food material expands and forms a large number of vent holes inside. , Sent to the crusher as a porous intermediate product.
発明が解決しようとする問題点 以上の説明から理解し得る如く、真空ベルト乾燥機は、
品質の保持性能、成分変化の防止性能、あるいは乾燥コ
ストの低減性に於いて、公知の噴霧乾燥機や凍結乾燥機
を大幅に上廻る性能を発揮することができるが、真空乾
燥処理を施すべき食品材料の多様化に対応するために
は、乾燥条件の選択性能を更に強化する必要がある。一
方、このような真空ベルト乾燥機に於いては、本格的な
操業の開始に先立って食品材料の特性に適合した最適の
乾燥条件を見出す必要があり、このため比較的少量の資
料について温度ならびに時間を変化せしめながら乾燥テ
ストを実行し実際の真空乾燥行程に適応可能な乾燥時間
ならびに乾燥温度のデータを取得している。Problems to be Solved by the Invention As can be understood from the above description, the vacuum belt dryer is
In terms of quality retention performance, component change prevention performance, and drying cost reduction performance, it is possible to exhibit performance far exceeding that of known spray dryers and freeze dryers, but vacuum drying should be performed. In order to cope with the diversification of food materials, it is necessary to further enhance the selection performance of drying conditions. On the other hand, in such a vacuum belt dryer, it is necessary to find the optimum drying conditions that match the characteristics of food materials before starting full-scale operation. The drying test is executed while changing the time, and the data of the drying time and the drying temperature applicable to the actual vacuum drying process are acquired.
しかしながら、実際の真空乾燥行程に設置されている真
空ベルト乾燥機は試料を乾燥条件の異なる炉が連設され
た中を走行させるものであるため、各炉の乾燥条件をこ
まかく任意に調整することは困難であった。However, since the vacuum belt dryer installed in the actual vacuum drying process runs the sample in a series of furnaces with different drying conditions, the drying conditions of each furnace should be carefully and arbitrarily adjusted. Was difficult.
本発明の主要な目的は、実際の生産ラインに設置されて
いる大型の真空ベルト乾燥機を乾燥条件の選定手段とし
てプレパイロット段階にそのまま転用した場合に認めら
れる上記の如き問題点を解消し得る真空乾燥試験機を提
供することにある。The main object of the present invention is to eliminate the above-mentioned problems observed when a large vacuum belt dryer installed in an actual production line is diverted to the pre-pilot stage as a means for selecting drying conditions. It is to provide a vacuum drying tester.
問題点を解決するための手段 斯かる目的に鑑みて本発明は、液状、スラリー状、もし
くはペースト状に調合された原材料の真空乾燥条件を設
定するための試験機であって、真空容器(1)内に挿
入、引出し自在に架装された合成繊維布製の乾燥棚
(2)と、該乾燥棚(2)の下方に配設されている加熱
兼冷却プレート(3)と、上記プレート(3)に接続さ
れ、系外から導入された蒸気により前記プレート(3)
内に供給する加熱媒体を生成する第1の熱交換器(10)
と、上記プレート(3)に接続され、チラーユニット
(9)から送出された冷却水により、前記プレート
(3)内に供給する冷却媒体を生成する第2の熱交換器
(11)と、上記プレート(3)に接続され、上記第1及
び第2の熱交換器(10)(11)より導入する加熱媒体も
しくは冷却媒体を調整してプレート(3)の温度と作動
時間を制御するシーケンス機能を有する乾燥時間および
乾燥温度制御装置(4)により構成され作動媒体の温度
を時間と共に変化させ静止した状態の試料に大型の真空
乾燥機中で試料を走行してテストした場合と同等の条件
を再現して、真空乾燥処理を施す真空乾燥試験機を要旨
とするものである。Means for Solving the Problems In view of such an object, the present invention is a tester for setting vacuum drying conditions of raw materials prepared in a liquid form, a slurry form, or a paste form, and a vacuum container (1 ), A drying rack (2) made of a synthetic fiber cloth that is freely inserted into and pulled out from the inside, a heating / cooling plate (3) disposed below the drying rack (2), and the plate (3). ) Connected to the plate (3) by steam introduced from outside the system.
A first heat exchanger (10) for generating a heating medium to be supplied into
A second heat exchanger (11) which is connected to the plate (3) and generates a cooling medium to be supplied into the plate (3) by the cooling water sent from the chiller unit (9); Sequence function that is connected to the plate (3) and controls the heating medium or cooling medium introduced from the first and second heat exchangers (10) and (11) to control the temperature and operating time of the plate (3) A drying time and a drying temperature control device (4) having a temperature of the working medium is changed with time, and a sample in a stationary state is run under the same conditions as in the case where the sample is run and tested in a large vacuum dryer. The gist is a vacuum drying tester that reproduces and performs a vacuum drying process.
作用 乾燥時間および乾燥温度の制御装置(4)を操作して真
空容器(1)内に配置されている加熱兼冷却プレート
(3)内に導入される作動媒体の温度を試料の種類に応
じて時間の経過と共に変化させ、比較的少量の静止した
状態の試料に真空乾燥処理を施すことによって、実際の
操作時に必要なデータを取得する。Action The temperature of the working medium introduced into the heating / cooling plate (3) arranged in the vacuum container (1) by operating the controller for the drying time and the drying temperature (4) is changed according to the type of sample. The data necessary for the actual operation is acquired by subjecting a relatively small amount of the stationary sample to a vacuum drying treatment which is changed with the passage of time.
実施例 第1図は本発明装置の全体構造を例示する一部分を断面
にした正面図である。図示するように真空容器(1)内
には、合成繊維製の編織布を支持枠に張設してなる乾燥
棚(2)が挿入・引出し自在に架装されており、また該
乾燥棚の下方には、真空乾燥を施すべき液状、スラリー
状、もしくはペースト状に調合された原材料に加熱・冷
却媒体を作用させるための加熱兼冷却プレート(3)が
配設されている。加熱兼冷却プレート(3)は、前記原
材料の特性に応じて乾燥条件、即ち、原材料の加熱温度
や冷却温度あるいは乾燥時間を自由に変更し得ることが
必要であり、このため加熱兼冷却プレート(3)には、
その内部に導入される加熱媒体もしくは冷却媒体の温度
ならびに該加熱媒体もしくは冷却媒体の作動時間を制御
するためのシーケンスリレーを内蔵したパネルが制御装
置(4)として接続されている。Embodiment FIG. 1 is a front view with a part in section illustrating the overall structure of the device of the present invention. As shown in the figure, in the vacuum container (1), a drying rack (2) formed by stretching a synthetic fiber knitted fabric on a support frame is mounted so that it can be inserted and pulled out. A heating / cooling plate (3) for causing a heating / cooling medium to act on raw materials prepared in a liquid form, a slurry form, or a paste form to be vacuum-dried is disposed below. The heating / cooling plate (3) needs to be able to freely change the drying conditions, that is, the heating temperature, the cooling temperature or the drying time of the raw material according to the characteristics of the raw material. In 3),
A panel having a sequence relay for controlling the temperature of the heating medium or the cooling medium introduced therein and the operating time of the heating medium or the cooling medium is connected as a control device (4).
真空容器(1)には、真空乾燥シシテムの構成部材とし
て、常法に従って真空発生装置(5)と、加熱兼冷却プ
レート(3)に加熱媒体または冷却媒体を循環させる、
図中太線で示す媒体循環用配管(20)とが接続されてお
る。上記媒体循環用配管(20)には、系外から導入され
た蒸気と配管(20)内を循環する媒体との間で熱交換機
能を生起させて加熱媒体を得るための第1のチューブ
式、もしくはプレート式熱交換器(10)と、冷却水タン
ク(6)、空冷式チラー(7)、冷却水の循環ポンプ
(8)からなるチラーユニット(9)により生起された
冷却水と配管(20)内を循環する媒体との間で熱交換機
能を生起させて冷却媒体を得るための第2のチューブ
式、もしくはプレート式熱交換器(11)と、該媒体循環
用配管(20)内で媒体を循環させる循環ポンプ(12)を
設ける。In the vacuum container (1), a heating medium or a cooling medium is circulated through a vacuum generator (5) and a heating / cooling plate (3) as a component of a vacuum drying system according to a conventional method.
It is connected to the medium circulation pipe (20) indicated by the thick line in the figure. In the medium circulation pipe (20), a first tube type for producing a heating medium by causing a heat exchange function between the steam introduced from outside the system and the medium circulating in the pipe (20) Alternatively, the cooling water and piping generated by the chiller unit (9) including the plate heat exchanger (10), the cooling water tank (6), the air cooling chiller (7), and the cooling water circulation pump (8) ( 20) A second tube type or plate type heat exchanger (11) for producing a cooling medium by causing a heat exchange function with a medium circulating in the medium, and a medium circulation pipe (20) A circulation pump (12) for circulating the medium is provided.
なお、図中 で示す配管は蒸気配管(21)であり、 で示す配管は冷却水配管(22)である。(23)は蒸気配
管(21)に設けた電磁弁であり、(24)は冷却水配管
(22)に設けた電磁弁であって、上記電磁弁(23)(2
4)をパネル制御装置(4)で選択的に開閉制御するこ
とにより、媒体循環用配管(20)中に加熱媒体、あるい
は、冷却媒体を生起させ、加熱兼冷却プレート(3)を
加熱、または冷却する。In the figure The pipe shown by is the steam pipe (21), The pipe shown by is the cooling water pipe (22). (23) is a solenoid valve provided in the steam pipe (21), (24) is a solenoid valve provided in the cooling water pipe (22), and the solenoid valve (23) (2
By selectively controlling opening and closing of 4) by the panel control device (4), a heating medium or a cooling medium is generated in the medium circulation pipe (20) to heat the heating / cooling plate (3), or Cooling.
真空発生装置(5)を作動することによって、試料の乾
燥時に真空容器(1)の内部は、10Torr前後の真空度
を保持し得るように構成されている。一方、真空容器
(1)には、エアー加圧により熱水の循環を促進する膨
脹タンク(13)と、液状、スラリー状、もしくはペース
ト状に調合された試料の供給装置(14)が付設さてい
る。該試料供給装置(14)は、真空容器(1)内で加熱
兼冷却プレート(3)の上方に架装されている合成繊維
布製の乾燥棚(2)の上面に、テスト対象品たる比較的
少量の試料を薄膜状に供給するための吐出ノズル機構で
あって、第1の実施態様に従えば、手動ハンドル(15)
またはモータ(図示省略)によって回転するリードスク
リュー(16)、該リードスクリューと螺子係合しその軸
線方向に沿って前後進するスライドブラケット(19)、
該スライドブラケットに固着された試料吐出ノズル(1
7)、ならびに原料タンク(18)から構成されている。
また、第2の実施態様に従えば、前記スライドブラケッ
ト(19)は、リードスクリュー(16)の軸線方向に沿っ
て前後進しながら首振り運動または回転運動を行い試料
の延展機能を促進する。乾燥棚(2)は、合成繊維糸条
の編織布を適当な支持枠(図示省略)に張設することに
よって形成された織目もしくは編目付きの通気性試料載
置面を有する薄膜状部材であって、強度や摩擦係数、あ
るいは耐熱性等の一般的な特性の外に真空乾燥を施され
た後の試料の剥離性を向上せしめ、また織目や編目を通
して加熱媒体もしくは冷却媒体の持つ熱エネルギーを試
料に効率良く伝達するため、例えばポリエステルのマル
チフィラメントヤーンの織成布にシリコンやポリテトラ
フルオルエチレン等の樹脂で表面処理を施すことによっ
て製作される。By operating the vacuum generator (5), the inside of the vacuum container (1) can be maintained at a vacuum degree of about 10 Torr when the sample is dried. On the other hand, the vacuum container (1) is provided with an expansion tank (13) that promotes circulation of hot water by air pressurization, and a device (14) for supplying a sample prepared in a liquid, slurry or paste form. There is. The sample supply device (14) is a synthetic fiber cloth drying rack (2) mounted above the heating / cooling plate (3) in the vacuum container (1), and is a comparative object to be tested. A discharge nozzle mechanism for supplying a small amount of sample in a thin film form, and according to the first embodiment, a manual handle (15).
Alternatively, a lead screw (16) rotated by a motor (not shown), a slide bracket (19) screw-engaged with the lead screw and moving forward and backward along the axial direction thereof,
Sample discharge nozzle (1
7) and the raw material tank (18).
Further, according to the second embodiment, the slide bracket (19) performs a swinging motion or a rotating motion while moving forward and backward along the axial direction of the lead screw (16) to promote the spreading function of the sample. The drying shelf (2) is a thin film member having a breathable sample mounting surface with a weave or stitches formed by stretching a knitted fabric of synthetic fiber yarn on an appropriate support frame (not shown). Therefore, in addition to general properties such as strength, friction coefficient, heat resistance, etc., it improves the peelability of the sample after vacuum drying, and the heat of the heating medium or cooling medium through the weave and the stitches. In order to efficiently transfer energy to the sample, it is produced, for example, by subjecting a woven fabric of polyester multifilament yarn to a surface treatment with a resin such as silicone or polytetrafluoroethylene.
真空容器(1)の端壁部分は、公知の蓋およびヒンジ機
構によって開閉自在に支持されており、真空乾燥を施さ
れた試料は、真空容器(1)内を真空状態から大気圧開
放状態に切替えた後、前記蓋を開くことによって乾燥棚
(2)上に載置されたままの状態で真空容器(1)内か
ら引出すことができる。The end wall portion of the vacuum container (1) is openably and closably supported by a well-known lid and hinge mechanism, and the sample dried under vacuum is changed from a vacuum state in the vacuum container (1) to an atmospheric pressure released state. After switching, by opening the lid, the lid can be pulled out from the vacuum container (1) while being placed on the drying shelf (2).
以下、未乾燥状態に於ける重量が60gであるチキンス
ープの例示に基づいて本発明装置の使用例を説明する。Hereinafter, a usage example of the device of the present invention will be described based on an example of chicken soup having a weight of 60 g in an undried state.
真空容器(1)の内部に乾燥棚(2)を架装した後、密
閉された真空容器(1)内を真空発生装置(5)の起動
により約10Torrの真空度に維持した。この状態で試料
供給装置(14)を起動し、前記チキンスープのペースト
状原液を乾燥棚(2)上に薄膜状に延展載置して試料供
給装置(14)の送りを停止し試料を静止し、次いで乾燥
時間および乾燥温度の制御装置(4)のシーケンス機能
を利用して、第1及び第2の熱交換器(10)(11)から
加熱兼冷却プレート(3)内に導入される加熱媒体もし
くは冷却媒体を経時的に切換え、例えば第2図に示す実
施例によれば先ず150℃で14分間、続いて140℃で14分
間、120℃で9分間、及び40℃で4分間プレート(3)
の温度を保持した加熱特性を設定し、真空乾燥試験を実
施した。このようにして真空乾燥処理を施されたチキン
スープは、30gの乾燥重量を有する多孔質ケーキに生成
されており、真空容器(1)を開くことによって乾燥棚
(2)上に載置されたままの状態で取出された。得られ
た試料はこの後常法に従って顆粒状に微粉化され、後続
の品質テスト行程へ送出された。After the drying shelf (2) was mounted inside the vacuum container (1), the sealed vacuum container (1) was maintained at a vacuum degree of about 10 Torr by activating the vacuum generator (5). In this state, the sample supply device (14) is activated, the paste stock solution of chicken soup is spread and placed on the drying shelf (2) in a thin film state, the feeding of the sample supply device (14) is stopped, and the sample is stopped. Then, it is introduced into the heating and cooling plate (3) from the first and second heat exchangers (10) and (11) by utilizing the sequence function of the controller for controlling the drying time and the drying temperature (4). The heating or cooling medium is switched over time, for example according to the embodiment shown in FIG. 2, the plate is first at 150 ° C. for 14 minutes, then 140 ° C. for 14 minutes, 120 ° C. for 9 minutes, and 40 ° C. for 4 minutes. (3)
The vacuum drying test was carried out by setting the heating characteristics with the temperature maintained. The chicken soup thus vacuum-dried is formed into a porous cake having a dry weight of 30 g, and placed on the drying shelf (2) by opening the vacuum container (1). It was taken out as it was. The obtained sample was then pulverized into granules according to a conventional method and sent to the subsequent quality test process.
発明の効果 以上の説明から理解し得る如く、本発明装置は、本格操
業に先行するテスト過程で比較的少量の試料について真
空乾燥条件を選定する場合、真空容器の乾燥条件を経時
的に切換えて設定し、テストするので、実際の生産工程
に配置されている異なった乾燥条件の区画を複数段連設
内蔵した大型の真空乾燥機を用いてテストした場合と同
等の条件を再現することが出来、さらに乾燥条件の設
定、変更は極めて簡単容易である。よって本発明によれ
ば、少量の試料によるテスト結果から本格操業で必要と
する真空乾燥データを適確に選定することができる。EFFECTS OF THE INVENTION As can be understood from the above description, in the apparatus of the present invention, when vacuum drying conditions are selected for a relatively small amount of sample in the test process prior to full-scale operation, the drying conditions of the vacuum container are changed over time. Since it is set and tested, it is possible to reproduce the same conditions as when testing using a large vacuum dryer that has multiple built-in sections with different drying conditions arranged in the actual production process. Moreover, it is extremely easy and easy to set and change the drying conditions. Therefore, according to the present invention, the vacuum drying data required for full-scale operation can be accurately selected from the test results of a small amount of sample.
第1図は本発明装置の全体構造を例示する一部分を断面
にした正面図であり、第2図は本発明装置によるテスト
の一例を示す直交座標線図である。 (1)……真空容器、(2)……乾燥棚、 (3)……加熱兼冷却プレート、 (4)……乾燥時間および乾燥温度の制御装置。FIG. 1 is a front view with a partial cross section illustrating the overall structure of the device of the present invention, and FIG. 2 is an orthogonal coordinate diagram showing an example of a test by the device of the present invention. (1) ... vacuum container, (2) ... drying rack, (3) ... heating and cooling plate, (4) ... control device for drying time and drying temperature.
Claims (1)
調合された原材料の真空乾燥条件を設定するための試験
機であって、 真空容器内に挿入、引出し自在に架装された合成繊維布
製の乾燥棚と、 該乾燥棚の下方に配設されている加熱兼冷却プレート
と、 上記プレートに接続され、系外から導入された蒸気によ
り前記プレート内に供給する加熱媒体を生成する第1の
熱交換器と、 上記プレートに接続され、チラーユニットから送出され
た冷却水により、前記プレート内に供給する冷却媒体を
生成する第2の熱交換器と、 上記プレートに接続され、上記第1及び第2の熱交換器
より導入する加熱媒体もしくは冷却媒体を調整してプレ
ートの温度と作動時間を制御するシーケンス機能を有す
る乾燥時間および乾燥温度制御装置により構成され、作
動媒体の温度を時間と共に変化させ静止した状態の試料
に真空乾燥処理を施すことを特徴とする真空乾燥試験
機。1. A tester for setting vacuum drying conditions of raw materials prepared in a liquid state, a slurry state, or a paste state, which is made of a synthetic fiber cloth that can be inserted into and pulled out from a vacuum container. A drying shelf, a heating / cooling plate disposed below the drying shelf, and a first heat which is connected to the plate and generates a heating medium to be supplied into the plate by steam introduced from outside the system. A second heat exchanger which is connected to the exchanger and which produces cooling medium supplied into the plate by cooling water sent from the chiller unit; 2 is composed of a drying time and drying temperature control device having a sequence function for controlling the temperature and operating time of the plate by adjusting the heating medium or cooling medium introduced from the heat exchanger. Vacuum drying tester and characterized by applying vacuum drying process to a sample of a stationary state by changing the temperature of the working medium over time.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60109582A JPH0619342B2 (en) | 1985-05-21 | 1985-05-21 | Vacuum drying tester |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60109582A JPH0619342B2 (en) | 1985-05-21 | 1985-05-21 | Vacuum drying tester |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61266956A JPS61266956A (en) | 1986-11-26 |
| JPH0619342B2 true JPH0619342B2 (en) | 1994-03-16 |
Family
ID=14513922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60109582A Expired - Lifetime JPH0619342B2 (en) | 1985-05-21 | 1985-05-21 | Vacuum drying tester |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0619342B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103263062B (en) * | 2013-04-28 | 2014-10-22 | 沈阳农业大学 | Perforating machine for refrigerated berries and production process of dried berries |
| CN114963702B (en) * | 2022-06-02 | 2023-05-23 | 武汉市依翎针织有限责任公司 | Dryer for textile processing production |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5835725B2 (en) * | 1975-07-31 | 1983-08-04 | 荏原インフイルコ株式会社 | lokadatsu suisouchi |
| JPS5935242A (en) * | 1982-08-20 | 1984-02-25 | Nec Corp | Switching control system |
-
1985
- 1985-05-21 JP JP60109582A patent/JPH0619342B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61266956A (en) | 1986-11-26 |
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