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JPH0727473A - Vacuum drying method - Google Patents

Vacuum drying method

Info

Publication number
JPH0727473A
JPH0727473A JP29770792A JP29770792A JPH0727473A JP H0727473 A JPH0727473 A JP H0727473A JP 29770792 A JP29770792 A JP 29770792A JP 29770792 A JP29770792 A JP 29770792A JP H0727473 A JPH0727473 A JP H0727473A
Authority
JP
Japan
Prior art keywords
drying chamber
dried
item
vacuum
drying
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
JP29770792A
Other languages
Japanese (ja)
Inventor
Akira Okashiro
晃 岡城
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.)
OKASHIRO KANAGATA KASEI KK
Original Assignee
OKASHIRO KANAGATA KASEI KK
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 OKASHIRO KANAGATA KASEI KK filed Critical OKASHIRO KANAGATA KASEI KK
Priority to JP29770792A priority Critical patent/JPH0727473A/en
Publication of JPH0727473A publication Critical patent/JPH0727473A/en
Pending legal-status Critical Current

Links

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  • Drying Of Solid Materials (AREA)
  • Cleaning Or Drying Semiconductors (AREA)

Abstract

PURPOSE:To improve the moisture removing precision by a method wherein a drying chamber is made of a radiant heat permeable material, and an item to be dried is heated by a radiant heat generator heater installed outside the drying chamber after the drying chamber is evacuated. CONSTITUTION:When an item 2 to be dried is placed in a drying chamber 3 and the pressure inside the drying chamber 3 is gradually reduced to a vacuum by a vacuum device 6, moisture attached on the surface of the item 2 immediately evaporates and is discharged outside the drying chamber 2 along with air to be discharged. Therefore, the item 2 is heated by a radiant heat generator heater 4 because the temperature of the item 2 may drop 20-30 deg.C below normal temperatures if it remains unheated. A work to carry the item 2 in and out from the drying chamber 3 and others are preferably made of a radiant heat permeable material. Then, the inside of the drying chamber 3 is returned to normal pressures while the item 2 is kept at around normal temperatures. Thereby, the moisture removing precision is improved because uneven drying parts and stains are not produced on the surface of the item 2.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、真空乾燥方法に関す
る。さらに詳しくは、光学レンズ,半導体ウエハ,配線
基板等からなる各種機器の比較的小型の部品部材の表面
に付着している水分を真空乾燥により除去する真空乾燥
方法において、その水分の除去精度に係る改良に関す
る。
FIELD OF THE INVENTION The present invention relates to a vacuum drying method. More specifically, in a vacuum drying method for removing moisture adhering to the surface of a relatively small component member of various equipment including an optical lens, a semiconductor wafer, a wiring board, etc. by vacuum drying, Regarding improvement.

【0002】[0002]

【従来の技術】一般に、前述のような各種機器の比較的
小型の部品部材について各種の加工が行われた後には、
フッ素系有機溶剤,塩素系有機溶剤等で加工表面を洗浄
することが行われてきていた。然しながら、環境破壊等
の理由から、フッ素系有機溶剤,塩素系有機溶剤等の使
用が規制されるようになり、代替え手段として水(超純
水)と水溶性洗剤,超音波等とによる水洗で洗浄が行わ
れることが多くなってきている。
2. Description of the Related Art Generally, after various processing is performed on relatively small component members of various kinds of equipment as described above,
It has been practiced to clean the processed surface with a fluorine-based organic solvent, a chlorine-based organic solvent, or the like. However, due to environmental damage, the use of fluorine-based organic solvents, chlorine-based organic solvents, etc. has come to be regulated. As an alternative, washing with water (ultra pure water), water-soluble detergent, ultrasonic waves, etc. Cleaning is often performed.

【0003】このような水洗による洗浄が行われると、
洗浄後に前記部品部材の表面に水分が付着残存してしま
い種々の不具合を生ずることになることから、付着して
いる水分を積極的に除去する処理が必要になる。また、
前記部品部材では大気中の水分が吸着しやすい性質のも
のがあり、精密な加工の前処理として表面に付着してい
る水分を除去する処理が必要になることがある。
When such washing with water is performed,
Since water adheres to and remains on the surface of the component member after cleaning and causes various problems, it is necessary to positively remove the adhered water. Also,
Some of the component members have a property of easily adsorbing moisture in the atmosphere, and thus a treatment for removing moisture adhering to the surface may be required as a pretreatment for precision processing.

【0004】従来、前記部品部材の表面に付着している
水分を除去する処理手段としては、真空乾燥方法が最も
好適なものとして着目されており、例えば特開平3−2
5283号公報に記載のものが知られている。
Conventionally, the vacuum drying method has been noted as the most suitable treatment means for removing the moisture adhering to the surface of the component member, and, for example, JP-A-3-2.
The one described in Japanese Patent No. 5283 is known.

【0005】この従来の真空乾燥方法は、図2に示すよ
うに、ベルトコンベア1に載って移動する前記部品部材
からなる被乾燥物2を収容する乾燥室3をベルトコンベ
ア1の上下から接離可能な2分割構造でしかもベルトコ
ンベア1と一体的に移動可能にしてなる連続乾燥型の装
置構成としてあり、被乾燥物2を乾燥室3の内部に収容
して、乾燥室3の内部を急速に減圧して真空にし、被乾
燥物2の表面に付着している水分を真空乾燥させて除去
し、水分の除去後に乾燥室3の内部を急速に常圧に復帰
させて被乾燥物2を乾燥室3から取出すものである。
In this conventional vacuum drying method, as shown in FIG. 2, a drying chamber 3 accommodating an article to be dried 2 composed of the above-mentioned component members mounted on a belt conveyor 1 is moved up and down from above and below the belt conveyor 1. It is a continuous drying type device configuration that has a possible two-part structure and is movable integrally with the belt conveyer 1. The material to be dried 2 is housed inside the drying chamber 3 and the inside of the drying chamber 3 is rapidly moved. The pressure is reduced to a vacuum, and the water adhering to the surface of the object to be dried 2 is vacuum dried to be removed. After the water is removed, the inside of the drying chamber 3 is rapidly returned to normal pressure to remove the object to be dried 2. It is taken out from the drying chamber 3.

【0006】このような従来の真空乾燥方法では、乾燥
室3の内部を急速に減圧するため、減圧の際に乾燥室3
の内壁やベルトコンベア1に付着している水分,ゴミ等
が飛散して被乾燥物2に付着してしまい、また乾燥室3
の内部を急速に常圧に復帰させるため、減圧により温度
低下していた被乾燥物2が急速な温度変化により結露が
生ずる。このため、水分の除去された被乾燥物2の表面
に乾燥ムラやシミが形成されてしまい、水分の除去精度
が低くなってしまうという問題点がある。
In such a conventional vacuum drying method, since the inside of the drying chamber 3 is rapidly depressurized, the drying chamber 3 is depressurized during depressurization.
Water, dust, and the like adhering to the inner wall of the conveyor and the belt conveyor 1 are scattered and adhere to the article to be dried 2, and the drying chamber 3
Since the inside of the product is rapidly returned to the normal pressure, dew condensation occurs on the material to be dried 2 whose temperature has been lowered by the pressure reduction due to the rapid temperature change. For this reason, there is a problem in that unevenness in drying and spots are formed on the surface of the article 2 to be dried from which the water has been removed, and the accuracy of removing the water becomes low.

【0007】[0007]

【発明が解決しようとする課題】本発明は、前述の問題
点を考慮してなされたもので、水分の除去精度の高い真
空乾燥方法を提供することを課題とする。
SUMMARY OF THE INVENTION The present invention has been made in consideration of the above problems, and an object of the present invention is to provide a vacuum drying method with high water removal accuracy.

【0008】[0008]

【課題を解決するための手段】前述の課題を解決するた
め、本発明に係る真空乾燥方法は、次のような手段を採
用する。
In order to solve the above problems, the vacuum drying method according to the present invention employs the following means.

【0009】即ち、請求項1では、被乾燥物を収容した
乾燥室の内部を真空にすることにより、被乾燥物の表面
に付着している水分を真空乾燥させて除去する真空乾燥
方法において、乾燥室を放射熱透過性の材質で形成して
おき、被乾燥物を収容した乾燥室の内部を徐々に減圧し
て真空とし、この減圧と同時進行してまたは乾燥室を真
空化した後に乾燥室の外部から被乾燥物に対して放射熱
を放射して被乾燥物を加熱し、被乾燥物が常温程度に加
熱された状態で乾燥室の内部を常圧に復帰させることを
特徴とする。
That is, according to the first aspect of the present invention, in the vacuum drying method, the inside of the drying chamber accommodating the material to be dried is evacuated to vacuum-dry the moisture adhering to the surface of the material to be dried. The drying chamber is made of a radiant heat permeable material, and the inside of the drying chamber containing the material to be dried is gradually decompressed to a vacuum, and drying is performed simultaneously with this decompression or after the drying chamber is evacuated. Radiation heat is radiated from the outside of the chamber to the object to be dried to heat the object to be dried, and the inside of the drying chamber is returned to normal pressure while the object to be dried is heated to about room temperature. .

【0010】また、請求項2では、請求項1の真空乾燥
方法において、乾燥室の内部を常圧に復帰させる際に、
乾燥室の内部に加熱された清浄な乾燥空気を少量づつ導
入し、乾燥室の内部を徐々に常圧に復帰させることを特
徴とする。
According to a second aspect of the present invention, in the vacuum drying method of the first aspect, when the inside of the drying chamber is returned to normal pressure,
It is characterized in that heated clean dry air is introduced little by little into the inside of the drying chamber to gradually return the inside of the drying chamber to normal pressure.

【0011】[0011]

【作用】前述の手段によると、請求項1では、乾燥室の
内部を徐々に減圧して真空化することから、減圧の際の
乾燥室の内部での水分,ゴミの飛散が防止さる。また、
乾燥室の内部に収容された被乾燥物を加熱して真空雰囲
気による温度低下を防止することから、常圧復帰の際の
結露が防止される。このため、水分の除去された被乾燥
物の表面に乾燥ムラやシミが形成されることがなくな
り、水分の除去精度の高い真空乾燥方法を提供するとい
う課題が解決されることになる。
According to the above-mentioned means, in the first aspect, the inside of the drying chamber is gradually depressurized to be evacuated, so that the scattering of water and dust inside the drying chamber during depressurization can be prevented. Also,
Since the material to be dried contained in the drying chamber is heated to prevent the temperature from decreasing due to the vacuum atmosphere, dew condensation at the time of returning to the normal pressure is prevented. Therefore, drying unevenness and spots are not formed on the surface of the dried object from which water is removed, and the problem of providing a vacuum drying method with high water removal accuracy is solved.

【0012】また、請求項2では、請求項1の作用にお
いて、加熱された清浄な空気を少量づつ乾燥室に導入し
て乾燥室の内部を徐々に常圧に復帰させるため、常圧復
帰の際の結露がより確実に防止されることになる。
According to the second aspect of the present invention, in the operation of the first aspect, the heated and clean air is introduced little by little into the drying chamber to gradually return the inside of the drying chamber to the normal pressure. Condensation at the time is more surely prevented.

【0013】[0013]

【実施例】以下、本発明に係る真空乾燥方法の実施例を
図1に基いて説明する。
EXAMPLE An example of the vacuum drying method according to the present invention will be described below with reference to FIG.

【0014】この実施例を実施するための装置構成は、
乾燥室3を放射熱透過性の材質で形成し、乾燥室3の外
側に放射熱発生加熱器4を設けたことが特徴となってい
る。即ち、放射熱発生加熱器4が赤外線発生型であれ
ば、乾燥室3をガラス等で形成することになる。
The apparatus configuration for carrying out this embodiment is as follows.
The drying chamber 3 is made of a radiant heat permeable material, and the radiant heat generating heater 4 is provided outside the drying chamber 3. That is, if the radiant heat generation heater 4 is an infrared ray generation type, the drying chamber 3 is formed of glass or the like.

【0015】さらに、この装置構成では、乾燥室3に通
気口5が設けられて真空装置6と給気装置7とが接続さ
れている。真空装置6は、乾燥室3の内部から脱気をし
て内部を減圧真空化するもので、真空ポンプ,減圧タン
ク等からなる。給気装置7は、乾燥室3の内部に加熱さ
れた清浄な乾燥空気を導入して真空化した内部を常圧に
復帰させるもので、ヒータ,フィルタ,コントロールバ
ルブ等からなる。
Further, in this device configuration, the drying chamber 3 is provided with the vent hole 5 and the vacuum device 6 and the air supply device 7 are connected to each other. The vacuum device 6 degasses the inside of the drying chamber 3 to decompress and evacuate the interior thereof, and includes a vacuum pump, a decompression tank, and the like. The air supply device 7 introduces heated clean dry air into the drying chamber 3 to restore the inside of the vacuum chamber to normal pressure, and includes a heater, a filter, a control valve, and the like.

【0016】このような装置構成を使用して実施するに
は、まず、図1(A)に示すように、乾燥室3の内部に
被乾燥物2を収容して、真空装置6により乾燥室3の内
部を徐々に減圧する。この徐々に減圧する手段として
は、真空装置6に複数基の真空ポンプを備えて運転基数
を徐々に増加するとか、コントロールバルブで脱気量を
少量づつにするとかが考えられる。
In order to carry out the operation using such an apparatus structure, first, as shown in FIG. 1 (A), the material to be dried 2 is housed inside the drying chamber 3, and the vacuum chamber 6 is used to dry the drying chamber. The pressure inside 3 is gradually reduced. As a means for gradually reducing the pressure, it is conceivable that the vacuum device 6 is provided with a plurality of vacuum pumps to gradually increase the number of operating units, or the control valve is used to gradually decrease the degassing amount.

【0017】このように乾燥室3の内部を徐々に減圧す
ると、乾燥室3の内部での圧力変動が少なく気流等が生
じないため、乾燥室3の内部の水分,ゴミ等の飛散が防
止されることになる。従って、この減圧速度は、乾燥室
3の内部の乾燥度合,清浄度合に影響されることにな
る。
When the inside of the drying chamber 3 is gradually decompressed in this manner, the pressure fluctuation inside the drying chamber 3 is small and the air flow is not generated, so that the scattering of water, dust and the like inside the drying chamber 3 is prevented. Will be. Therefore, this depressurization rate is affected by the dryness and cleanliness inside the drying chamber 3.

【0018】乾燥室3の内部が減圧され真空化される
と、被乾燥物2の表面に付着している水分は、直ちに蒸
発して脱気と共に乾燥室3の外部へ排出除去されること
になる。即ち、穀物乾燥等のように被乾燥物2の内部に
水分が含浸されているものを乾燥する場合には、被乾燥
物2に潜熱を加えなければならないが、前記部品部材の
ような被乾燥物2の表面に付着しているものを乾燥する
場合には、特別に潜熱を加える必要はない。従って、被
乾燥物2は、そのままでは真空雰囲気下で温度が低下す
ることになる(常温に対して20〜30℃)。
When the inside of the drying chamber 3 is decompressed and evacuated, the moisture adhering to the surface of the material to be dried 2 is immediately evaporated and discharged to the outside of the drying chamber 3 together with deaeration. Become. That is, when drying the material to be dried 2 in which water is impregnated such as grain drying, latent heat must be applied to the material to be dried 2, but the material to be dried such as the above-mentioned component member is dried. When drying the substance adhering to the surface of the object 2, it is not necessary to add latent heat. Therefore, the temperature of the material to be dried 2 will decrease in a vacuum atmosphere as it is (20 to 30 ° C. with respect to room temperature).

【0019】このように温度低下するまたは温度低下し
た被乾燥物2に対しては、放射熱発生加熱器4により加
熱を行う。即ち、乾燥室3の減圧と同時進行して加熱を
行うこともできるし、乾燥室3を減圧して真空化してか
ら加熱を行うこともできる。
The radiant heat generation heater 4 heats the material to be dried 2 whose temperature has been lowered or whose temperature has been lowered as described above. That is, heating can be performed simultaneously with the decompression of the drying chamber 3, or the drying chamber 3 can be decompressed and evacuated before heating.

【0020】放射熱発生加熱器4は、赤外線等のような
放射熱を放射し、乾燥室2を透過しさらに乾燥室3の内
部の真空域も通過した放射熱によって被乾燥物2を直接
加熱することになる。従って、この放射熱発生加熱器4
による加熱は、乾燥室3の外部から乾燥室2に順次熱伝
導させる加熱手段よりも熱効率が良好であり、乾燥室3
の内部に熱源を設けないため乾燥室3を小型化すること
ができる利点がある。なお、このような加熱をより有効
にするためには、放射熱を遮断することがないように、
被乾燥物2を乾燥室3に出入れするワーク等を放射熱透
過性の材料で形成するのが望ましい。
The radiant heat generating heater 4 radiates radiant heat such as infrared rays and directly heats the material to be dried 2 by the radiant heat passing through the drying chamber 2 and further passing through the vacuum region inside the drying chamber 3. Will be done. Therefore, this radiant heat generation heater 4
The heating by means of is superior in thermal efficiency to the heating means for sequentially conducting heat to the drying chamber 2 from the outside of the drying chamber 3.
Since there is no heat source provided inside, there is an advantage that the drying chamber 3 can be downsized. In order to make such heating more effective, so as not to block radiant heat,
It is desirable that a work or the like that puts the object to be dried 2 into and out of the drying chamber 3 is formed of a radiation heat permeable material.

【0021】この加熱は、被乾燥物2が常温程度に達
し、乾燥室3の内部が後述のように常圧に復帰するまで
継続される。なお、本発明者の実験では、加熱温度は常
温に対して5℃低くても不具合は生じなかった。また、
加熱の上限温度については、特に制限はなく、被乾燥物
2が変質,損傷しない程度まで可能である。
This heating is continued until the material to be dried 2 reaches about room temperature and the inside of the drying chamber 3 returns to normal pressure as described later. In the experiment conducted by the present inventor, no problem occurred even if the heating temperature was 5 ° C. lower than the room temperature. Also,
The upper limit temperature of heating is not particularly limited, and it is possible to the extent that the material to be dried 2 is not altered or damaged.

【0022】次に、被乾燥物2が常温程度まで加熱され
た状態を維持して、乾燥室3の内部を常圧に復帰させる
ことになる。この常圧への復帰は、急速に行っても差支
えない。
Next, the material to be dried 2 is maintained in a state of being heated to about room temperature, and the inside of the drying chamber 3 is returned to normal pressure. This return to normal pressure can be made rapidly.

【0023】乾燥室3の内部が常圧に復帰する際には、
従来例とは異なり被乾燥物2が常温程度まで加熱されて
いるため、被乾燥物2の急速な温度変化がなく結露が生
ずることがない。
When the inside of the drying chamber 3 returns to normal pressure,
Unlike the conventional example, since the material to be dried 2 is heated to about room temperature, there is no rapid temperature change in the material to be dried 2 and dew condensation does not occur.

【0024】なお、被乾燥物2が微小物で堆積,積層等
して真空乾燥する場合や凹凸部,複雑な形状部を有して
いる複雑構造物である場合には、前述の放射熱発生加熱
器4による加熱で被乾燥物2に加熱ムラが生ずることが
あるため、図1(B)に示すように、乾燥室3の内部に
給気装置7から加熱された清浄な乾燥空気を少量づつ導
入し、乾燥室3の内部を徐々に常圧に復帰させる。
When the object to be dried 2 is a minute object and is vacuum-dried by depositing or laminating it, or when it is a complex structure having irregularities and complicated shapes, the radiant heat generation described above is performed. Since heating unevenness may occur in the material to be dried 2 due to the heating by the heater 4, as shown in FIG. 1B, a small amount of clean dry air heated from the air supply device 7 is placed inside the drying chamber 3. Then, the inside of the drying chamber 3 is gradually returned to normal pressure.

【0025】このようにして乾燥室3の内部を徐々に常
圧に復帰させると、被乾燥物2の間や凹凸部等に加熱さ
れた空気が当触して加熱ムラが消失するため、結露が確
実に防止される。
When the inside of the drying chamber 3 is gradually returned to the normal pressure in this way, the heated air comes into contact with the space between the objects to be dried 2 and the uneven portion, and the uneven heating disappears. Is reliably prevented.

【0026】[0026]

【発明の効果】以上のように本発明に係る真空乾燥方法
は、請求項1では、乾燥室の内部を徐々に減圧して真空
化して水分,ゴミの飛散を防止し、被乾燥物を加熱して
真空雰囲気による温度低下を防止して結露を防止するこ
とから、水分の除去された被乾燥物の表面に乾燥ムラや
シミが形成されることがなくなるため、水分の除去精度
が高くなる効果がある。
As described above, in the vacuum drying method according to the present invention, in claim 1, the interior of the drying chamber is gradually decompressed to be vacuumed to prevent the scattering of water and dust and to heat the material to be dried. Since the temperature is prevented from lowering due to the vacuum atmosphere and dew condensation is prevented, unevenness in drying and stains are not formed on the surface of the dried material from which moisture has been removed, so that the accuracy of removing moisture is improved. There is.

【0027】さらに、請求項1では、被乾燥物の加熱を
放射熱により乾燥室の外部から行うため、熱効率が良好
で乾燥室周りの装置構成を小型化することができる効果
がある。
Further, according to the first aspect of the present invention, since the material to be dried is heated from the outside of the drying chamber by radiant heat, there is an effect that thermal efficiency is good and the device configuration around the drying chamber can be downsized.

【0028】さらに、請求項2では、請求項1の効果に
加えて、被乾燥物が微小物,複雑構造物である場合に、
加熱ムラを解消して結露を確実に防止することができる
効果がある。
Further, in addition to the effects of the first aspect, in the second aspect, when the material to be dried is a minute object or a complex structure,
There is an effect that uneven heating can be eliminated and dew condensation can be surely prevented.

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

【図1】本発明に係る真空乾燥方法の実施例を示すもの
で、(A),(B)の順に工程順を示してある。
FIG. 1 shows an embodiment of a vacuum drying method according to the present invention, in which the order of steps is shown in the order of (A) and (B).

【図2】従来例を示す装置構成の側面断面図である。FIG. 2 is a side sectional view of a device configuration showing a conventional example.

【符号の説明】[Explanation of symbols]

2 被乾燥物 3 乾燥室 4 放射熱発生加熱器 2 Drying object 3 Drying room 4 Radiant heat generation heater

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 被乾燥物を収容した乾燥室の内部を真空
にすることにより、被乾燥物の表面に付着している水分
を真空乾燥させて除去する真空乾燥方法において、乾燥
室を放射熱透過性の材質で形成しておき、被乾燥物を収
容した乾燥室の内部を徐々に減圧して真空とし、この減
圧と同時進行してまたは乾燥室を真空化した後に乾燥室
の外部から被乾燥物に対して放射熱を放射して被乾燥物
を加熱し、被乾燥物が常温程度に加熱された状態で乾燥
室の内部を常圧に復帰させることを特徴とする真空乾燥
方法。
1. A vacuum drying method for removing moisture adhering to the surface of an object to be dried by vacuuming the inside of the drying chamber containing the object to be dried by radiant heat. It is made of a permeable material, and the inside of the drying chamber containing the material to be dried is gradually depressurized to a vacuum, and simultaneously with this depressurization or after the drying chamber is evacuated, the drying chamber is covered from outside. A vacuum drying method, characterized in that radiant heat is radiated to a dried product to heat the dried product, and the inside of the drying chamber is returned to normal pressure while the dried product is heated to about room temperature.
【請求項2】 請求項1の真空乾燥方法において、乾燥
室の内部を常圧に復帰させる際に、乾燥室の内部に加熱
された清浄な乾燥空気を少量づつ導入し、乾燥室の内部
を徐々に常圧に復帰させることを特徴とする真空乾燥方
法。
2. The vacuum drying method according to claim 1, wherein when the inside of the drying chamber is returned to normal pressure, heated clean dry air is introduced little by little into the inside of the drying chamber. A vacuum drying method characterized by gradually returning to normal pressure.
JP29770792A 1992-10-09 1992-10-09 Vacuum drying method Pending JPH0727473A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29770792A JPH0727473A (en) 1992-10-09 1992-10-09 Vacuum drying method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29770792A JPH0727473A (en) 1992-10-09 1992-10-09 Vacuum drying method

Publications (1)

Publication Number Publication Date
JPH0727473A true JPH0727473A (en) 1995-01-27

Family

ID=17850127

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29770792A Pending JPH0727473A (en) 1992-10-09 1992-10-09 Vacuum drying method

Country Status (1)

Country Link
JP (1) JPH0727473A (en)

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