JP2954367B2 - Equipment for drying goods - Google Patents
Equipment for drying goodsInfo
- Publication number
- JP2954367B2 JP2954367B2 JP41314090A JP41314090A JP2954367B2 JP 2954367 B2 JP2954367 B2 JP 2954367B2 JP 41314090 A JP41314090 A JP 41314090A JP 41314090 A JP41314090 A JP 41314090A JP 2954367 B2 JP2954367 B2 JP 2954367B2
- Authority
- JP
- Japan
- Prior art keywords
- drying
- steam
- article
- chamber
- superheated steam
- 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 - Fee Related
Links
- 238000001035 drying Methods 0.000 title claims description 42
- 229920006395 saturated elastomer Polymers 0.000 claims description 11
- 238000010793 Steam injection (oil industry) Methods 0.000 claims description 2
- 239000011521 glass Substances 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000005406 washing Methods 0.000 description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- AJDIZQLSFPQPEY-UHFFFAOYSA-N 1,1,2-Trichlorotrifluoroethane Chemical compound FC(F)(Cl)C(F)(Cl)Cl AJDIZQLSFPQPEY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 2
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 2
- 238000004506 ultrasonic cleaning Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000007601 warm air drying Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Coating Apparatus (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、物品を飽和水蒸気によ
って予備加熱した後、過熱水蒸気によって乾燥する物品
の乾燥装置に関する。The present invention relates, after preheated by saturated steam articles relates dry 燥装 location of the article to dry by superheated steam.
【0002】[0002]
【従来の技術】精密部品などの洗浄乾燥方法として、従
来、フロン113、トリクロロエチレン等の不燃性溶剤
による洗浄乾燥方法が行なわれている。この方法は、ま
ず物品を洗浄液に浸漬して超音波洗浄を行なった後、冷
フロンによる冷シャワーを行ない、次に飽和フロン蒸気
によって仕上乾燥を行ない、更に風乾によって仕上乾燥
を行なうものであり、上記不燃性溶剤による低い表面張
力と少ない蒸発潜熱のため良質の乾燥品が得られてい
た。2. Description of the Related Art As a method for washing and drying precision parts and the like, a washing and drying method using a nonflammable solvent such as chlorofluorocarbon 113 and trichloroethylene has been used. In this method, the article is first immersed in a cleaning liquid and subjected to ultrasonic cleaning, followed by performing a cold shower with cold Freon, then performing finish drying with saturated Freon vapor, and further performing finish drying by air drying. Good quality dried products have been obtained due to the low surface tension and low latent heat of vaporization of the nonflammable solvent.
【0003】また、水系の洗浄乾燥方法も知られてお
り、この場合は、アルキルベンゼンスルフォン酸ソーダ
(ABS系活性剤)等の薬品によって洗浄した後リンス
し、次いで超純水による洗浄を行ない、イソプロパノー
ル、アセトン等で水と置換し、温風乾燥によって仕上乾
燥を行なっていた。また、物品の洗浄後、過熱蒸気によ
って乾燥を行なう方法も提案されている。[0003] An aqueous washing and drying method is also known. In this case, washing with a chemical such as sodium alkylbenzenesulfonate (ABS-based activator), rinsing, washing with ultrapure water, and isopropanol are then performed. , Acetone, etc., and finish drying by warm air drying. Further, a method has been proposed in which the article is washed and then dried with superheated steam.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、これら
従来の洗浄乾燥方法にあっては、フロン113やトリク
ロロエチレン等の不燃性溶剤が環境への影響からその使
用が制限されているという問題がある。また、水系の場
合には乾燥方法に適切なものがなく、可燃性溶剤である
イソプロパノール、アセトン等によって水と置換し、空
気または窒素ガス、炭酸ガス等の温風で乾燥している
が、連続操作・運転の場合には、装置が複雑となり、安
全性および性能の点で問題があった。However, in these conventional washing and drying methods, there is a problem that the use of nonflammable solvents such as Freon 113 and trichloroethylene is restricted due to the influence on the environment. In the case of water-based systems, there is no suitable drying method, and water is replaced with flammable solvents such as isopropanol and acetone, and dried with warm air such as air or nitrogen gas or carbon dioxide gas. In the case of operation and operation, the device becomes complicated, and there are problems in terms of safety and performance.
【0005】また、洗浄した物品を過熱蒸気によって乾
燥する方法では、乾燥に要する時間を短かくすることが
でき、また、低酸素による品質保持を図ることができる
が、温度の低い物品を過熱蒸気中に入れると、物品の表
面にウォーターマーク(水滴のあとが斑点状に残ったも
の、水紋ともいう)ができるという問題があるため好ま
しくない。[0005] In the method of drying the washed articles with superheated steam, the time required for drying can be shortened and the quality can be maintained by low oxygen. It is not preferable to put it inside because there is a problem that a watermark (a spot left behind a water drop, also referred to as a water mark) is formed on the surface of the article.
【0006】[0006]
【課題を解決するための手段】そこで本発明者らは、上
記した従来の問題に鑑みて鋭意検討を行なった結果、本
発明に到達した。 The present inventors have made intensive studies in view of the above-mentioned conventional problems, and as a result, have reached the present invention .
【0007】即ち、本発明によれば、物品を予備加熱す
るための飽和水蒸気噴出口を有する予熱室と、予備加熱
された物品を乾燥するための過熱水蒸気噴射ノズルを有
する乾燥室と、該予熱室で噴出された飽和水蒸気を外気
とともに吸引して排気する第一排気手段と、該乾燥室で
噴射された過熱水蒸気を循環して前記過熱水蒸気噴射ノ
ズルに供給する循環手段と、該乾燥室よりの水蒸気を外
気とともに吸引して排気する第二排気手段とを備えたこ
とを特徴とする物品の乾燥装置が提供される。 That is , according to the present invention, a preheating chamber having a saturated steam jet port for preheating an article, a drying chamber having a superheated steam jet nozzle for drying a preheated article, A first exhaust unit that sucks and exhausts the saturated steam ejected in the chamber together with the outside air, a circulation unit that circulates the superheated steam injected in the drying chamber and supplies the superheated steam to the superheated steam injection nozzle, And a second exhaust means for sucking and exhausting the water vapor together with the outside air.
【0008】[0008]
【作用】本発明は、飽和水蒸気によって物品を予備加熱
した後、過熱水蒸気(ドライスチーム、乾き蒸気とも呼
ばれ、飽和蒸気温度よりも高い温度の蒸気をいう。)を
使用することにより物品を乾燥させることに特徴があ
る。According to the present invention, the article is preheated with saturated steam and then dried by using superheated steam (also referred to as dry steam or dry steam, which is steam having a temperature higher than the saturated steam temperature). There is a feature in making it work.
【0009】物品を乾燥する場合、温度の低い物品を熱
風空気中や過熱水蒸気中に入れると、該物品の表面にウ
ォーターマーク(水滴のあとが斑点状に残ったもの、水
紋ともいう)ができるので好ましくない。これに対し
て、本発明のように物品を飽和水蒸気で予備加熱した
後、過熱蒸気で急速に乾燥させると、ウォーターマーク
の発生を防止し、物品を効率よく、良好に乾燥すること
ができる。In the case of drying an article, if a low-temperature article is put in hot air or superheated steam, a water mark (a spot left behind a water droplet, also called a water mark) is formed on the surface of the article. It is not preferable because it can be done. On the other hand, when the article is preheated with saturated steam and then rapidly dried with superheated steam as in the present invention, the generation of watermarks can be prevented, and the article can be efficiently and well dried.
【0010】過熱水蒸気の温度としては特に限定されな
いが、大気圧下において130〜800℃、好ましくは
250〜450℃である。乾燥する物品としては、ガラ
ス管、セラミックス、形状の複雑な精密部品等に対して
特に効果がある。本発明の乾燥装置による乾燥中の物品
の移動はタクト方式とし、所定のタクト距離を、所定の
タクトタイムで、バッチ方式で連続的に移動することが
できる。[0010] The temperature of the superheated steam is not particularly limited, but it is 130 to 800 ° C, preferably 250 to 450 ° C under atmospheric pressure. The articles to be dried are particularly effective for glass tubes, ceramics, precision parts having complicated shapes, and the like. The movement of the article during drying by the drying apparatus of the present invention is performed in a tact system, and can be continuously moved in a batch system at a predetermined tact distance at a predetermined tact time.
【0011】[0011]
【実施例】以下、本発明を図示の実施例により更に詳細
に説明するが、本発明はこれらの実施例に限られるもの
ではない。第1図は本発明の物品の乾燥装置の一実施例
の概要図である。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail with reference to the illustrated embodiments, but the present invention is not limited to these embodiments. FIG. 1 is a schematic view of an embodiment of an article drying apparatus according to the present invention.
【0012】この乾燥装置は、乾燥室1の前後に予熱室
2と後室3及び予熱室2の前に吸引フード14を有し、
被乾燥物である物品4がコンベア5により、予熱室2→
乾燥室1→後室3と搬送されるようになっている。ま
た、蒸発器6が設置されており、純水が送入されて蒸発
され、予熱室2の上部に設けられた噴出ノズル9から予
熱室2へ噴出され、また乾燥室1からの過熱蒸気ととも
に循環され、蒸気加熱器15で再加熱された蒸気は、乾
燥室1の上部に設けられた噴射ノズル8より乾燥室1へ
噴射されるようになっている。This drying apparatus has a preheating chamber 2, a rear chamber 3 before and after the drying chamber 1, and a suction hood 14 in front of the preheating chamber 2.
The article 4 to be dried is conveyed by the conveyor 5 to the preheating chamber 2 →
The drying chamber 1 is transferred to the rear chamber 3. In addition, an evaporator 6 is provided, and pure water is sent in and evaporated, and is ejected from an ejection nozzle 9 provided at an upper portion of the preheating chamber 2 to the preheating chamber 2, and together with superheated steam from the drying chamber 1. The steam circulated and reheated by the steam heater 15 is injected into the drying chamber 1 from an injection nozzle 8 provided at the upper part of the drying chamber 1.
【0013】次に、上記装置の操作について説明する。
被乾燥物としてガラス管を用い、まず乾燥の前段階とし
て中性洗剤による超音波洗浄を行ない、更に純水によっ
てリンス(すすぎ洗い)を行なう。次に、上記の前処理
を行なったガラス管4の入った容器10をコンベア5に
載せて予熱室2に送入する。予熱室2では蒸発器6から
送られてきた、100℃、1気圧の飽和水蒸気を噴出口
9からガラス管4に噴射して予熱した。余分な蒸気は吸
引フード14より排気ファン20で排出される。なお、
予熱室2の下部からはドレン液が排出される。Next, the operation of the above device will be described.
A glass tube is used as an object to be dried. First, ultrasonic cleaning with a neutral detergent is performed as a pre-drying step, followed by rinsing with pure water. Next, the container 10 containing the glass tube 4 that has been subjected to the above pretreatment is placed on the conveyor 5 and sent into the preheating chamber 2. In the preheating chamber 2, saturated steam at 100 ° C. and 1 atm, which was sent from the evaporator 6, was injected from the ejection port 9 into the glass tube 4 for preheating. Excess steam is discharged from the suction hood 14 by the exhaust fan 20. In addition,
The drain liquid is discharged from a lower part of the preheating chamber 2.
【0014】予熱室2は板や扉あるいはカーテン等の遮
断扉12によって外気と、遮断扉13によって乾燥室1
とそれぞれ遮断されている。次いでガラス部品4を乾燥
室1に送入する。乾燥室1では、大気圧下で100℃、
1気圧の蒸気を大気圧下、蒸気過熱器15によって30
0℃まで過熱した過熱水蒸気を作製し、噴射ノズル8よ
りガラス管4に噴射した。過熱水蒸気出口16の蒸気温
度は被乾燥物の乾燥状態により変化するが、蒸気は蒸発
器6からの蒸気と合わせて循環使用する。尚、乾燥室1
の下部からはドレン液が排出される。循環蒸気は蒸気過
熱器15により所定の温度、この例では300℃まで過
熱され、噴射ノズル8より噴射される。なお、18はブ
ロアを示す。The preheating chamber 2 is connected to the outside air by a shut-off door 12 such as a plate, a door or a curtain, and the drying chamber 1 is shut by a shut-off door 13.
And each is shut off. Next, the glass component 4 is sent into the drying chamber 1. In the drying chamber 1, at 100 ° C. under atmospheric pressure,
The steam of 1 atm.
Superheated steam heated to 0 ° C. was produced, and injected from the injection nozzle 8 to the glass tube 4. Although the steam temperature at the superheated steam outlet 16 changes depending on the drying state of the material to be dried, the steam is circulated and used together with the steam from the evaporator 6. In addition, drying room 1
The drain liquid is discharged from the lower part of the. The circulating steam is superheated by the steam superheater 15 to a predetermined temperature, in this example, 300 ° C., and is injected from the injection nozzle 8. Reference numeral 18 denotes a blower.
【0015】次いで、乾燥室1において所定時間(この
例では3.5分間)乾燥されたガラス管4を後室3に移
送する。後室3は、遮断扉22によって外気と遮断して
あり、漏洩してくる蒸気等を排出するための換気口23
を設けてある。また、乾燥室1との境には遮断扉24が
設けてあり、これらの扉22,24は前記の扉12,1
3と同様にガラス管4の入室および出室時にのみ開閉す
るようになっている。また、乾燥室1側から換気口23
の間の壁および天井に結露するのを防ぐためヒーター2
1を設け、壁面温度を100℃以上に保つようにする。
以上のようにしてガラス管4の乾燥をタクトタイム(乾
燥間隔)3.5分で行なったところ、良好な乾燥を行な
うことができた。Next, the glass tube 4 dried for a predetermined time (3.5 minutes in this example) in the drying chamber 1 is transferred to the rear chamber 3. The rear room 3 is shut off from the outside air by a shutoff door 22, and is provided with a ventilation port 23 for discharging leaking steam and the like.
Is provided. Further, at the boundary with the drying chamber 1, a shut-off door 24 is provided, and these doors 22 and 24 are connected to the doors 12 and 1.
Like the glass tube 3, the glass tube 4 can be opened and closed only when the glass tube 4 enters and leaves the room. In addition, the ventilation opening 23
Heater 2 to prevent condensation on walls and ceiling between
1 to keep the wall temperature at 100 ° C. or higher.
As described above, when the glass tube 4 was dried at a tact time (drying interval) of 3.5 minutes, good drying could be performed.
【0016】[0016]
【発明の効果】以上説明したように、本発明の物品の乾
燥装置によれば、被乾燥物品を、飽和水蒸気によって予
備加熱した後、過熱水蒸気によって乾燥するので、物品
の表面にウォーターマークの発生する恐れがなく物品を
効率よく、良好な乾燥を行なうことができる。As described above, the dryness of the article of the present invention can be improved.
According to 燥装 location, to be dried article was preheated by saturated steam, since the drying by superheated steam, efficiently there is no fear articles which generation of water marks on the surface of the article, to perform a good drying Can be.
【図1】本発明の物品の乾燥装置の一実施例の概要図で
ある。FIG. 1 is a schematic view of an embodiment of an apparatus for drying articles according to the present invention.
1 乾燥室 2 予熱室 3 後室 4 物品 5 コンベア 6 蒸発器 7 サイクロン 8 噴射ノズル 9 噴出ノズル 10 容器 15 蒸気過熱器 21 ヒーター DESCRIPTION OF SYMBOLS 1 Drying room 2 Preheating room 3 Back room 4 Article 5 Conveyor 6 Evaporator 7 Cyclone 8 Injection nozzle 9 Ejection nozzle 10 Container 15 Steam superheater 21 Heater
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F26B 9/00 F26B 15/00 F26B 15/18 F26B 15/22 F26B 21/00 ──────────────────────────────────────────────────続 き Continuation of front page (58) Field surveyed (Int. Cl. 6 , DB name) F26B 9/00 F26B 15/00 F26B 15/18 F26B 15/22 F26B 21/00
Claims (1)
出口を有する予熱室と、予備加熱された物品を乾燥する
ための過熱水蒸気噴射ノズルを有する乾燥室と、該予熱
室で噴出された飽和水蒸気を外気とともに吸引して排気
する第一排気手段と、該乾燥室で噴射された過熱水蒸気
を循環して前記過熱水蒸気噴射ノズルに供給する循環手
段と、該乾燥室よりの水蒸気を外気とともに吸引して排
気する第二排気手段とを備えたことを特徴とする物品の
乾燥装置。1. A preheating chamber having a saturated steam jet port for preheating an article, a drying chamber having a superheated steam jet nozzle for drying a preheated article, and a saturated jet spouted from the preheating chamber. First exhaust means for sucking and exhausting steam together with outside air, circulating means for circulating superheated steam injected in the drying chamber and supplying it to the superheated steam injection nozzle, and sucking steam from the drying chamber together with outside air And a second exhaust means for exhausting the air.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP41314090A JP2954367B2 (en) | 1990-12-22 | 1990-12-22 | Equipment for drying goods |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP41314090A JP2954367B2 (en) | 1990-12-22 | 1990-12-22 | Equipment for drying goods |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04222383A JPH04222383A (en) | 1992-08-12 |
| JP2954367B2 true JP2954367B2 (en) | 1999-09-27 |
Family
ID=18521835
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP41314090A Expired - Fee Related JP2954367B2 (en) | 1990-12-22 | 1990-12-22 | Equipment for drying goods |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2954367B2 (en) |
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| JP4980331B2 (en) * | 2008-01-31 | 2012-07-18 | 富士電機株式会社 | Heat treatment device with superheated steam |
| JP4961004B2 (en) * | 2009-10-06 | 2012-06-27 | 関東自動車工業株式会社 | Superheated steam dryer and production line |
| JP5599221B2 (en) * | 2010-04-28 | 2014-10-01 | 日立造船株式会社 | Method for forming buffer layer in dye-sensitized solar cell |
| US20140319241A1 (en) * | 2013-04-30 | 2014-10-30 | Armstrong World Industries, Inc. | System and method for humidifying a system for applying a coating to a workpiece |
| KR102257673B1 (en) * | 2014-05-15 | 2021-05-28 | 삼성에스디아이 주식회사 | Apparatus for drying electrode plate and method for drying the same |
| JP2016198255A (en) * | 2015-04-09 | 2016-12-01 | シブヤマシナリー株式会社 | Heat treatment device |
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| KR101996370B1 (en) * | 2018-10-17 | 2019-07-05 | 서영파일테크 주식회사 | Floating process of tension material |
-
1990
- 1990-12-22 JP JP41314090A patent/JP2954367B2/en not_active Expired - Fee Related
Cited By (1)
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| CN109631550A (en) * | 2018-10-29 | 2019-04-16 | 湖北万硕新型材料有限公司 | A kind of porcelain tendre molding apparatus for baking |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04222383A (en) | 1992-08-12 |
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