JPS59191880A - Vacuum freezing drier - Google Patents

Vacuum freezing drier

Info

Publication number
JPS59191880A
JPS59191880A JP6535883A JP6535883A JPS59191880A JP S59191880 A JPS59191880 A JP S59191880A JP 6535883 A JP6535883 A JP 6535883A JP 6535883 A JP6535883 A JP 6535883A JP S59191880 A JPS59191880 A JP S59191880A
Authority
JP
Japan
Prior art keywords
heat
heating
cooling
cold trap
heater
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.)
Pending
Application number
JP6535883A
Other languages
Japanese (ja)
Inventor
健治 戸草
文雄 原田
元博 伊藤
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP6535883A priority Critical patent/JPS59191880A/en
Publication of JPS59191880A publication Critical patent/JPS59191880A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は真空凍結乾燥機に係り、特に昇華熱補給の熱源
を冷凍機の排熱を利用することにより経済曲を同上させ
た装置に関するものである。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a vacuum freeze dryer, and more particularly to a device that achieves economical performance by using waste heat of a refrigerator as a heat source for sublimation heat supplementation. be.

〔従来技術〕[Prior art]

真空凍結乾燥機に係る従来技術を第1図、第2図により
説明する。
A conventional technique related to a vacuum freeze dryer will be explained with reference to FIGS. 1 and 2.

第1図の場合、寸ず最初に被乾燥物10は、乾燥棚9の
ヒに置かれて予備凍結しなければならない。この予備凍
結蝶、王縮機1.1jpf縮器2、膨張弁5、冷却コイ
ル12によりなる冷凍サイクルにより乾燥棚9を冷却す
ることによシ行われる。一般的には、この時の凍結温度
は−40’C以下で釣る。
In the case of FIG. 1, the material to be dried 10 must first be placed on the drying rack 9 and pre-frozen. This is carried out by cooling the drying shelf 9 through a refrigeration cycle consisting of the pre-freezing butterfly, the compressor 1.1jpf compressor 2, the expansion valve 5, and the cooling coil 12. Generally, the freezing temperature at this time is -40'C or lower.

凍結が完了すると、次に′電磁弁4を閉じて、電磁弁6
を開き、冷凍サイクルを切換えてコールドトラップ13
を冷41する。コールドトラップが十分冷却された後真
空ポンプ14を運転開始する。
When freezing is completed, close solenoid valve 4 and close solenoid valve 6.
Open the cold trap 13 and switch the refrigeration cycle.
Cool for 41 minutes. After the cold trap has been sufficiently cooled, the vacuum pump 14 is started.

凍結乾燥庫8の内部が高真窒しくなると被乾燥物10内
の夢結している水分は昇華をはじめる。昇華した水分は
大部分がコールドトラップ13において捕集される。被
乾燥vlJ10内の水分が昇華を継続するためには、昇
華熱に相当する熱を加える必要があり、加熱ヒータ11
はこのために乾燥棚9の中に組込まれており、温度調節
器(図示せず)により被乾沫物10の温度を適招に保つ
ように制(財)される。
When the inside of the freeze-drying chamber 8 becomes very cold, the moisture in the material to be dried 10 begins to sublimate. Most of the sublimated water is collected in the cold trap 13. In order to continue subliming the moisture in the dried vlJ 10, it is necessary to apply heat equivalent to the heat of sublimation, and the heating heater 11
is incorporated into the drying rack 9 for this purpose, and is controlled by a temperature regulator (not shown) to maintain the temperature of the drying material 10 at a suitable level.

しかるにこの昇華熱は非常に大きく、コールドトラップ
の冷却熱竜に匹敵する容量が必要であり、運転経費がか
さむという欠点がある。
However, this heat of sublimation is extremely large, requiring a capacity comparable to that of a cold trap's cooling heat dragon, which has the disadvantage of increasing operating costs.

第2図の場合、乾燥棚9の加熱冷却に際し、冷却コイル
12を冷却熱交換器20に、加熱コイル11を加熱熱交
換器21に設け、循環ポンプ22は同じである。このた
め前記のものと同様、運転経費がかさむという欠点があ
る。
In the case of FIG. 2, when heating and cooling the drying rack 9, the cooling coil 12 is provided in the cooling heat exchanger 20, the heating coil 11 is provided in the heating heat exchanger 21, and the circulation pump 22 is the same. Therefore, like the above-mentioned one, it has the disadvantage of high operating costs.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、大容量のヒータを使用せずに乾燥棚を
加熱することにある。
An object of the present invention is to heat a drying rack without using a large-capacity heater.

〔発明の概要〕[Summary of the invention]

被乾燥物の昇華潜熱が、コールドトラップの冷却熱量と
バランスするというヒントから、このコールドトラップ
を冷却する冷凍機の排熱を利用することを思いついた。
Based on the hint that the latent heat of sublimation of the material to be dried is balanced with the cooling heat of the cold trap, we came up with the idea of using the exhaust heat of the refrigerator that cools the cold trap.

しかし、冷凍機の吐出ガスをこのまま加熱に利用するこ
とは圧縮機の人力、及びコールドトラップ等への熱損失
分だけ加熱量が太きいため、これを適正量に制間して使
用することとした。
However, if the discharged gas of the refrigerator is used as it is for heating, the amount of heating will be large due to the human power of the compressor and the heat loss to cold traps, etc., so it is necessary to limit the amount of heat used. did.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例を第3図により説明する。従来
技術の第2図における加熱ヒータ11の代りに、加熱コ
イル19を設けてあり、真空乾燥運転時に、これに冷凍
サイクルのホットガスを流すように構成しである。
An embodiment of the present invention will be described below with reference to FIG. In place of the heater 11 in FIG. 2 of the prior art, a heating coil 19 is provided, and hot gas from the refrigeration cycle is passed through this during vacuum drying operation.

乾燥工程において、コールドトラップ13が十分冷却さ
れた後、X全運転が始まると冷凍サイクルの冷媒の流れ
は、電磁弁18を閉じて、電磁弁17を開くことにより
高湛高王の吐出ガス(一般的に100C程度)は、まず
補助冷却器+5に入り、ここでファン16の回転数変化
等の制量により、高子圧力の最適温度まで冷却する。次
にこの冷媒ガスが加熱熱交換器21内の加熱コイル19
に流入し、ここで循環ポンプ22、三方弁23、を介し
て循環する熱媒体に熱を与えて凝縮液化する。この凝縮
過程における冷媒の温度で、熱媒体を加熱すれば、熱媒
体の過熱劣化を未然に防止することもできる。
In the drying process, after the cold trap 13 has been sufficiently cooled and full operation begins, the flow of the refrigerant in the refrigeration cycle is controlled by closing the solenoid valve 18 and opening the solenoid valve 17. (generally about 100C) first enters the auxiliary cooler +5, where it is cooled down to the optimum temperature for the high pressure by controlling the rotation speed of the fan 16, etc. Next, this refrigerant gas is transferred to the heating coil 19 in the heating heat exchanger 21.
Here, heat is applied to the heat medium circulating through the circulation pump 22 and the three-way valve 23, and the heat medium is condensed and liquefied. If the heat medium is heated at the temperature of the refrigerant in this condensation process, overheating deterioration of the heat medium can also be prevented.

次に液化した冷媒は、電磁弁6、膨張弁7を通ってコー
ルドトラップ13内にて蒸発冷却して、再び圧縮機1に
戻る。
Next, the liquefied refrigerant passes through the electromagnetic valve 6 and the expansion valve 7, is evaporated and cooled in the cold trap 13, and returns to the compressor 1 again.

冷凍機のヒートポンプ熱量は過熱分(補助冷却器15で
除去した熱量)を除くとほとんど蒸発熱量と等しいため
、冷凍サイクルはバランスし、乾燥棚9の加熱熱欧は十
分に供給される。
Since the heat pump heat amount of the refrigerator is almost equal to the evaporation heat amount, excluding the superheat amount (the heat amount removed by the auxiliary cooler 15), the refrigeration cycle is balanced and the heating heat of the drying rack 9 is sufficiently supplied.

第4図においてけ乾燥棚9の冷却時Vこ、冷却コイル1
2に直接市媒ガスを通じて冷却し、加熱時には加熱熱交
換器21で加熱された熱媒体を1川じて加熱する以外、
r’!”73図の場合と同様の動作をする本発明の一実
施例1である。
In FIG. 4, when cooling the drying rack 9, the cooling coil 1
2, and when heating, the heat medium heated by the heating heat exchanger 21 is heated as a single stream.
r'! This is a first embodiment of the present invention that operates in the same way as the case shown in FIG. 73.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、被乾燥物の昇華熱に相当する熱量を冷
凍機の排熱を利用するようにしたため、別のヒータ熱−
二を8歎とせず、経済的である。
According to the present invention, since the waste heat of the refrigerator is used to generate heat equivalent to the heat of sublimation of the material to be dried,
It's economical and doesn't mean 2 is 8.

さらに耐凍機の吐出ガスを予備冷却して加熱量の適正化
を図ると同時に、熱媒体の高温加熱による劣化を防止す
ることができるという効果がある
Furthermore, it has the effect of pre-cooling the discharge gas of the freezer to optimize the amount of heating, and at the same time, preventing deterioration of the heat medium due to high-temperature heating.

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

?p1図、第2図は従来の真空凍結乾燥機のサイクル系
統図、第3図第4図は本発明による真空凍結乾燥機によ
るサイクル系統図を示す。 1・・・圧縮機 2・・・凝縮器 4.6.17.18
・・・電磁弁 5,7・・・膨張弁 8・・・凍結乾燥
庫 9・・・乾燥棚 10・・・被乾燥物 11・・・
加熱ヒータ 12・・・冷却コイル 13・・・コール
ドトラップ 14・・・真空ポンプ 15・・・補助冷
却器 19・・・加熱コイル 20・・・冷却熱交換器
 21・・・加熱熱交換器22・・・循環ポンプ 23
・・・三方弁蓼1m 茅zfJ 第う団
? Figures p1 and 2 are cycle diagrams of a conventional vacuum freeze dryer, and Figures 3 and 4 are cycle diagrams of a vacuum freeze dryer according to the present invention. 1... Compressor 2... Condenser 4.6.17.18
... Solenoid valve 5,7... Expansion valve 8... Freeze drying chamber 9... Drying shelf 10... Material to be dried 11...
Heater 12... Cooling coil 13... Cold trap 14... Vacuum pump 15... Auxiliary cooler 19... Heating coil 20... Cooling heat exchanger 21... Heating heat exchanger 22 ...Circulation pump 23
...Mikata Bento 1m KayazfJ 1st group

Claims (1)

【特許請求の範囲】[Claims] 凍結用冷却詣、加熱器、コールドトラップを、真空容器
に収納すると共に冷却6金冷凍サイクルと接続した真空
凍結乾燥機において、前記加熱器に冷凍機の吐出ガス冷
媒にて加熱した熱媒体を流入可能に接続したことを特徴
とする真空凍結乾燥機。
In a vacuum freeze dryer in which a cooling device for freezing, a heater, and a cold trap are housed in a vacuum container and connected to a cooling 6K refrigeration cycle, a heat medium heated by the discharge gas refrigerant of the refrigerator is flowed into the heater. A vacuum freeze dryer characterized in that it can be connected.
JP6535883A 1983-04-15 1983-04-15 Vacuum freezing drier Pending JPS59191880A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6535883A JPS59191880A (en) 1983-04-15 1983-04-15 Vacuum freezing drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6535883A JPS59191880A (en) 1983-04-15 1983-04-15 Vacuum freezing drier

Publications (1)

Publication Number Publication Date
JPS59191880A true JPS59191880A (en) 1984-10-31

Family

ID=13284651

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6535883A Pending JPS59191880A (en) 1983-04-15 1983-04-15 Vacuum freezing drier

Country Status (1)

Country Link
JP (1) JPS59191880A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6031305A (en) * 1996-07-26 2000-02-29 Nippon Seiki Co., Ltd. Stepping motor with rotor and stator having related axial width

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6031305A (en) * 1996-07-26 2000-02-29 Nippon Seiki Co., Ltd. Stepping motor with rotor and stator having related axial width

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