JPS636680Y2 - - Google Patents
Info
- Publication number
- JPS636680Y2 JPS636680Y2 JP1980148093U JP14809380U JPS636680Y2 JP S636680 Y2 JPS636680 Y2 JP S636680Y2 JP 1980148093 U JP1980148093 U JP 1980148093U JP 14809380 U JP14809380 U JP 14809380U JP S636680 Y2 JPS636680 Y2 JP S636680Y2
- Authority
- JP
- Japan
- Prior art keywords
- container
- pressure vessel
- critical point
- gas
- jacket
- 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
Links
Landscapes
- Investigating Or Analysing Biological Materials (AREA)
- Sampling And Sample Adjustment (AREA)
- Drying Of Solid Materials (AREA)
Description
【考案の詳細な説明】
本考案は走査電子顕微鏡等の試料作成に用いる
臨界点乾燥装置に関する。[Detailed Description of the Invention] The present invention relates to a critical point drying device used for preparing samples for scanning electron microscopes and the like.
臨界点乾燥装置は適当な試薬により脱水,固定
更には置換処理された試料を圧力容器内に収納
し、この中に液体炭酸などの媒介溶剤を注入し、
該媒介溶剤を液相と気相の混合状態を経て気相に
移行するように加熱し、試料を乾燥する装置であ
る。斯かる装置においては媒介溶剤としての液化
ガス(液体炭酸など)を容易に注入するためには
圧力容器の温度を10℃前後又はそれ以下に保つ必
要がある。所が一度処理の終つた容器は40℃程度
の高温になつており連続処理を行うには強制的に
冷却しなければならない。このため従来は容器の
外にフアン等の空冷手段を設けたり、前記液化ガ
ス又はその蒸発ガスを直接容器内に注入し、この
ガスを急激に放出することによるガスの断熱膨脹
を利用して冷却が行われている。 In the critical point drying device, a sample that has been dehydrated, fixed, and replaced with an appropriate reagent is stored in a pressure vessel, into which a mediating solvent such as liquid carbonic acid is injected.
This device heats the mediating solvent so that it passes through a mixed state of a liquid phase and a gas phase and then changes to a gas phase, thereby drying the sample. In such a device, it is necessary to maintain the temperature of the pressure vessel at around 10° C. or lower in order to easily inject liquefied gas (liquid carbon dioxide, etc.) as a mediating solvent. However, once processing has been completed, the container reaches a high temperature of around 40°C, and must be forcibly cooled to allow continuous processing. For this reason, conventional methods have been to provide air cooling means such as a fan outside the container, or to inject the liquefied gas or its evaporated gas directly into the container, and to rapidly release the gas, thereby utilizing adiabatic expansion of the gas for cooling. is being carried out.
しかし乍ら、前者は冷却手段が大がかりで且
つ、あまり効率的でない。又、後者は試料を冷却
操作前に容器内に置くことができないので、冷却
後試料挿入のため容器蓋の開閉を行わねばならな
いが、このとき容器内が大気にさらされるため冷
却された容器内壁に最もきらわれる水分の露結が
生ずるのを防ぐことができない。もし試料を冷却
前に容器内に入れておくと、容器内ガスの断熱膨
脹による急激な低下、並びにガスの急激な流れに
より試料は損傷を受けることになる。 However, the former requires a large-scale cooling means and is not very efficient. In addition, in the latter case, the sample cannot be placed in the container before the cooling operation, so the container lid must be opened and closed to insert the sample after cooling, but at this time, the inside of the container is exposed to the atmosphere, so the inner wall of the cooled container It is not possible to prevent moisture condensation from occurring, which is the most hated thing in the world. If the sample is placed in the container before being cooled, the sample will be damaged by the rapid drop due to adiabatic expansion of the gas in the container and by the rapid flow of gas.
本考案は以上の欠点を解決するためのもので、
以下図面に基づいて詳述する。 This invention is intended to solve the above drawbacks.
The details will be explained below based on the drawings.
第1図は本考案の一実施例を示す図で1は圧力
容器で内部圧力が百数十気圧まで充分に耐えられ
るように頑強に造られている。該容器の上面は着
脱可能な蓋2であり、その中央部に内部を観察す
るための透明な窓3が設けてある。該容器の適所
には加熱ヒーター4が設けてあり容器を加熱して
内部に注入される媒介溶剤を加熱気化するために
使用される。5は媒介溶剤供給源、即ち例えば液
体炭酸のタンクであり、該液体炭酸は元栓6,導
入バルブ7を備えたパイプ8を通して容器1内に
導入される。圧力容器内での気化ガスはパイプ
9,排出バルブ10を介して外部に排出される。
11は容器1の外側に設けた槽で、容器を内槽に
して二重構造となつており、その間に空隙部を形
成し冷却ジヤケツト12を構成している。このジ
ヤケツトには導入バルブ13を有するパイプ14
が接続され、前記元栓6を介して液体炭酸のタン
ク5に接続される。これによりジヤケツト12内
には液体炭酸又はその気化ガスが冷媒として導入
される。15は排出用のパイプ、16は排出バル
ブである。 FIG. 1 is a diagram showing an embodiment of the present invention. Reference numeral 1 denotes a pressure vessel which is robustly constructed to withstand an internal pressure of more than 100 atmospheres. The upper surface of the container is a removable lid 2, and a transparent window 3 is provided in the center for observing the inside. A heater 4 is provided at a suitable location in the container and is used to heat the container and vaporize the mediator solvent injected into the container. Reference numeral 5 designates a source of mediating solvent, ie a tank of liquid carbonic acid, for example, which is introduced into the container 1 through a pipe 8 equipped with a tap 6 and an inlet valve 7. The vaporized gas within the pressure vessel is discharged to the outside via a pipe 9 and a discharge valve 10.
Reference numeral 11 denotes a tank provided outside the container 1, which has a double structure with the container serving as an inner tank, with a gap formed between them to form a cooling jacket 12. This jacket has a pipe 14 with an inlet valve 13.
is connected to the liquid carbon dioxide tank 5 via the main valve 6. As a result, liquid carbon dioxide or its vaporized gas is introduced into the jacket 12 as a refrigerant. 15 is a discharge pipe, and 16 is a discharge valve.
このような装置において、試料の乾燥処理を行
うには全てのバルブ及び元栓を閉じた状態で蓋2
を開け、容器1内に試料を収納する。次に元栓6
を開け、且つ、バルブ7,10を開け、容器内の
空気を炭酸ガスに置換する。然る後バルブ7と1
0を閉め、バルブ13及び16を開け、ジヤケツ
ト内にタンク5内の溶剤又はその蒸発ガスを流
し、容器1を予冷する。該容器が所定の温度(例
えば5℃)になつたらバルブ13及び16を閉
じ、今度はバルブ7及び10を開け容器1内に液
体炭酸を注入する。所定量(容器内の9割程度)
注入したら元栓6及びバルブ7を閉めヒーター4
により容器1を50℃前後に加熱する。この加熱に
より液体炭酸は蒸発していき、温度及び圧力が臨
界点以上に維持される。 In such a device, to dry the sample, close all valves and main valves and close the lid 2.
Open the container 1 and store the sample in the container 1. Next, the main valve 6
and valves 7 and 10 to replace the air in the container with carbon dioxide gas. After that, valves 7 and 1
0 is closed, valves 13 and 16 are opened, and the solvent in the tank 5 or its evaporated gas is allowed to flow into the jacket to pre-cool the container 1. When the container reaches a predetermined temperature (for example, 5° C.), valves 13 and 16 are closed, and valves 7 and 10 are then opened to inject liquid carbonic acid into container 1. Specified amount (approximately 90% of the contents in the container)
After injecting, close the main tap 6 and valve 7 and turn off the heater 4.
Heat container 1 to around 50°C. This heating causes the liquid carbonic acid to evaporate, maintaining the temperature and pressure above the critical point.
而して全ての液体炭酸を気化し、そのガスをバ
ルブ10を開いて排出しおわると試料の乾燥は終
了する。 When all of the liquid carbon dioxide is vaporized and the gas is discharged by opening the valve 10, the drying of the sample is completed.
以上の如き構成となせばジヤケツト12に冷媒
を流して容器1を冷却しており、且つ冷媒は乾燥
処理に使う媒介溶剤を用いているので構造は極め
て簡単、小型であり、又試料を容器内に収納した
状態で予冷でき、従つて容器壁に水分の露結は全
くなく満足な乾燥処理が行える。 With the above configuration, the container 1 is cooled by flowing a refrigerant into the jacket 12, and the refrigerant uses a mediating solvent used for drying processing, so the structure is extremely simple and compact, and the sample can be placed inside the container. The container can be pre-cooled while stored in the container, and therefore a satisfactory drying process can be performed without any moisture condensation on the container wall.
尚前記は本考案の一例であり色々と変更するこ
とができる。例えば、冷媒として乾燥処理用の液
化ガス、又はその蒸発ガスを用いたが、全く別個
の冷媒源を用いても良い。又冷却ジヤケツトは容
器を二重槽にする場合に限らず例えば第2図に示
す如く容器1に空洞又は穴を設けたものでも良
い。第2図中1a,1b,1c及び1dは容器壁
に対称的に設けられた空洞で、上下で相互に連絡
しておりこの中に冷媒が流される。4a,4bは
加熱用のヒーター、17a,17bは温度表示用
及び温度コントロール用のセンサーである。 Note that the above is an example of the present invention, and various modifications can be made. For example, although liquefied gas for drying processing or its evaporated gas is used as the refrigerant, a completely separate refrigerant source may be used. Further, the cooling jacket is not limited to the case where the container is a double tank, but may be one in which a cavity or hole is provided in the container 1 as shown in FIG. 2, for example. In FIG. 2, 1a, 1b, 1c and 1d are cavities symmetrically provided in the container wall, communicating with each other at the top and bottom, into which the refrigerant flows. 4a and 4b are heaters for heating, and 17a and 17b are sensors for temperature display and temperature control.
第1図は本考案の一実施例を示す図、第2図は
他の実施例を示す主部断面図である。
1……容器、2……蓋、3……窓、4……ヒー
ター、5……タンク、6……元栓、7,10,1
3及び16……バルブ、8,9,14及び15…
…パイプ、11……外槽、12……冷却ジヤケツ
ト。
FIG. 1 is a view showing one embodiment of the present invention, and FIG. 2 is a sectional view of the main part showing another embodiment. 1... Container, 2... Lid, 3... Window, 4... Heater, 5... Tank, 6... Main valve, 7, 10, 1
3 and 16... valves, 8, 9, 14 and 15...
...Pipe, 11...Outer tank, 12...Cooling jacket.
Claims (1)
試料を圧力容器内に収納し、液体炭酸や液体フ
レオンの媒介溶剤を注入し、該媒介溶剤を加熱
して液相から液相と気相の混合状態を経て気相
に移向せしめて前記試料を乾燥する装置におい
て、前記圧力容器に冷却ジヤケツトを設け、該
ジヤケツトに冷媒を供給する手段を設けてなる
臨界点乾燥装置。 2 前記ジヤケツトに供給される冷媒は、容器内
に注入される媒介溶剤、又はその蒸発気体であ
る実用新案登録請求の範囲第1項記載の臨界点
乾燥装置。 3 前記冷却ジヤケツトは、圧力容器に設けた穴
又は空洞である実用新案登録請求の範囲第1項
又は第2項記載の臨界点乾燥装置。 4 前記冷却ジヤケツトは容器内槽と外槽の二重
槽により形成される空間である実用新案登録請
求の範囲第1項又は第2項記載の臨界点乾燥装
置。[Scope of claims for utility model registration] 1. Dehydration using a reagent. The sample that has been fixed and replaced is stored in a pressure vessel, a mediating solvent such as liquid carbonic acid or liquid Freon is injected, and the mediating solvent is heated to change from a liquid phase to a mixed state of liquid and gas phases, and then to a gas phase. A critical point drying apparatus for drying the sample by transferring the pressure vessel to the pressure vessel, wherein the pressure vessel is provided with a cooling jacket, and a means for supplying a refrigerant to the jacket is provided. 2. The critical point drying apparatus according to claim 1, wherein the refrigerant supplied to the jacket is a medium solvent injected into the container or its evaporated gas. 3. The critical point drying apparatus according to claim 1 or 2, wherein the cooling jacket is a hole or cavity provided in a pressure vessel. 4. The critical point drying device according to claim 1 or 2, wherein the cooling jacket is a space formed by a double tank including an inner tank and an outer tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1980148093U JPS636680Y2 (en) | 1980-10-16 | 1980-10-16 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1980148093U JPS636680Y2 (en) | 1980-10-16 | 1980-10-16 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5770146U JPS5770146U (en) | 1982-04-27 |
JPS636680Y2 true JPS636680Y2 (en) | 1988-02-25 |
Family
ID=29507563
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1980148093U Expired JPS636680Y2 (en) | 1980-10-16 | 1980-10-16 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS636680Y2 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49109132A (en) * | 1973-02-19 | 1974-10-17 | ||
JPS5237446B2 (en) * | 1974-07-10 | 1977-09-22 | ||
JPS5331047A (en) * | 1976-09-01 | 1978-03-23 | Hitachi Ltd | Bearing for rotary machines |
JPS54124791A (en) * | 1978-03-20 | 1979-09-27 | Akashi Seisakusho Kk | Specimen freezer |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5237446U (en) * | 1975-09-09 | 1977-03-16 |
-
1980
- 1980-10-16 JP JP1980148093U patent/JPS636680Y2/ja not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49109132A (en) * | 1973-02-19 | 1974-10-17 | ||
JPS5237446B2 (en) * | 1974-07-10 | 1977-09-22 | ||
JPS5331047A (en) * | 1976-09-01 | 1978-03-23 | Hitachi Ltd | Bearing for rotary machines |
JPS54124791A (en) * | 1978-03-20 | 1979-09-27 | Akashi Seisakusho Kk | Specimen freezer |
Also Published As
Publication number | Publication date |
---|---|
JPS5770146U (en) | 1982-04-27 |
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