JP2007309614A - Superheated steam drying apparatus - Google Patents

Superheated steam drying apparatus Download PDF

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JP2007309614A
JP2007309614A JP2006141116A JP2006141116A JP2007309614A JP 2007309614 A JP2007309614 A JP 2007309614A JP 2006141116 A JP2006141116 A JP 2006141116A JP 2006141116 A JP2006141116 A JP 2006141116A JP 2007309614 A JP2007309614 A JP 2007309614A
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drying
superheated steam
steam
dried
unit
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JP4909640B2 (en
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Gentaro Nemoto
源太郎 根本
Yoshimitsu Amano
善光 天野
Hiroyuki Miyoshi
啓之 三好
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OGAWARA KAKOKI KK
OOGAWARA KAKOKI KK
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OOGAWARA KAKOKI KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a superheated steam drying apparatus capable of carrying out drying of various types of objects to be dried, and capable of efficiently carrying out drying. <P>SOLUTION: The superheated steam drying apparatus 1 is provided with a steam supplying part 8 supplying steam, a circulation fan (a circulating means) 7 circulating the steam, and a heater (a superheating part) 5 superheating the steam. They are each connected by a communication pipe 12 to form a closed circuit, a drying part 2 is provided in the closed circuit, and a housing part 3 is provided for housing the objects to be dried and composed such that it is movable between a drying part 2 interior and exterior. In the housing part 3, at a first position with at least one part of its body outside the drying part, the objects to be dried are housed, and at a second position with its body moved from the first position into the drying part 2 interior, the superheated steam introduced into the drying part 2 is introduced into the body to dry the objects to be dried. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、被乾燥物を常圧過熱水蒸気の閉回路系において、回分式で連続的に乾燥させる過熱水蒸気乾燥装置に関する。   The present invention relates to a superheated steam drying apparatus for continuously drying an object to be dried in a batch circuit system in a closed circuit system of atmospheric superheated steam.

従来、原料又は残渣物等の被乾燥物の乾燥方法としては、外気を導入し加熱昇温させ熱風とし、この熱によって被乾燥物の水分を気化蒸発させる熱風乾燥法が主に用いられてきた。熱風乾燥法とは、被乾燥物から熱風中に水分を移動させ乾燥させる方法であり、公害防止や熱の有効利用のため、熱交換器によって冷却して除湿し再加熱する技術を使ったり、熱風を循環させ一部を加熱吸気、一部を排気することが多い。   Conventionally, as a method for drying a material to be dried such as a raw material or a residue, a hot air drying method in which outside air is introduced and heated to raise the temperature to hot air, and the moisture of the material to be dried is vaporized and evaporated by this heat has been mainly used. . The hot air drying method is a method of moving moisture from the material to be dried into the hot air and drying it, and in order to prevent pollution and effectively use heat, use a technology that cools, dehumidifies and reheats with a heat exchanger, In many cases, hot air is circulated, and a part is heated and sucked, and a part is exhausted.

しかしながら、熱風乾燥法は、多量に発生する排ガスの臭気処理が困難であった。また、熱風乾燥法は、被乾燥物の品質が熱によって変性するのを防止するため、乾燥工程において初期に高温とし、後期は80℃程度の低温とすることが一般的であるが、乾燥は被乾燥物の表面から進み、表面に固い乾燥皮質が形成されるので、内部の乾燥は阻害されてしまい、被乾燥物の品質低下が生じる。更に、熱風乾燥法は、乾燥における水分の蒸発時には湿球温度以上に被乾燥物の温度が上昇しないので、完全な殺菌、滅菌は行われないという問題があった。   However, the hot air drying method has been difficult to treat odor of exhaust gas generated in large quantities. The hot air drying method generally uses a high temperature at the initial stage in the drying process and a low temperature of about 80 ° C. in the latter stage in order to prevent the quality of the material to be dried from being denatured by heat. Since it progresses from the surface of the object to be dried and a hard dry cortex is formed on the surface, the internal drying is inhibited and the quality of the object to be dried is reduced. Furthermore, the hot-air drying method has a problem that the temperature of the material to be dried does not rise above the wet bulb temperature when water is evaporated during drying, and thus, complete sterilization and sterilization are not performed.

一方、高温(400〜600℃)で、且つ高湿度熱風で乾燥する高温高湿乾燥法は、従来の熱風乾燥法と比較して、連続で、被乾燥物を多量に乾燥できるだけでなく、過熱水蒸気雰囲気に近い高温高湿熱風を用いることにより、乾燥速度が速く、乾燥装置を小型化することができる。   On the other hand, the high-temperature and high-humidity drying method, which is dried at a high temperature (400 to 600 ° C.) and with high-humidity hot air, can continuously dry a large amount of the object to be dried, compared with the conventional hot-air drying method, and can also be overheated. By using high-temperature, high-humidity hot air close to a water vapor atmosphere, the drying speed is fast and the drying apparatus can be miniaturized.

しかしながら、高温高湿乾燥法は、被乾燥物の表面には固い乾燥皮質が出来てしまい、表面の酸化等もあわせて被乾燥物の品質低下が生じるだけでなく、乾燥における水分の蒸発時には湿球温度以上に被乾燥物の温度が上昇しないので、完全な殺菌、滅菌をすることができないという問題点があった。また、高温高湿乾燥方法は、乾燥工程の運転開始時と終了時に、被乾燥物の変性が発生しやすいという問題点があった。更に、高温高湿乾燥方法は、半閉回路乾燥であるため、乾燥器内へ空気の流入による被乾燥物の酸化や排ガスの臭気処理をすることが困難であった。   However, the high-temperature and high-humidity drying method produces a hard dry cortex on the surface of the material to be dried, which not only causes deterioration of the quality of the material to be dried together with oxidation of the surface, but also causes moisture to evaporate during drying. Since the temperature of the object to be dried does not rise above the bulb temperature, there has been a problem that complete sterilization and sterilization cannot be performed. Further, the high temperature and high humidity drying method has a problem that the material to be dried tends to be denatured at the start and end of the operation of the drying process. Furthermore, since the high-temperature and high-humidity drying method is semi-closed circuit drying, it is difficult to oxidize the object to be dried and to treat the exhaust gas odor by inflow of air into the dryer.

そこで、被乾燥物から発生する臭気を乾燥装置外部に排出させることなく、被乾燥物の品質を維持しつつ、被乾燥物の殺菌、滅菌が行え、被乾燥物内部まで乾燥することができ、更には省エネルギーで低ランニングコストである連続式常圧過熱水蒸気乾燥方法及び装置が開示されている(特許文献1)。
特開2002−62044号公報
Therefore, without discharging the odor generated from the object to be dried to the outside of the drying apparatus, while maintaining the quality of the object to be dried, the object to be dried can be sterilized and sterilized, and the inside of the object to be dried can be dried. Furthermore, a continuous atmospheric pressure superheated steam drying method and apparatus that are energy saving and low running cost are disclosed (Patent Document 1).
JP 2002-62044 A

しかしながら、特許文献1によると、被乾燥物は、投入ホッパーから投入され、乾燥処理が終了すると、出口チャンバーから排出される構造となっており、大塊は小塊とされた乾燥品として排出されるものである。このため、特定の被乾燥物には使用できるが、種々の被乾燥物に使用することができなかった。このため、種々の被乾燥物に使用し、効率よく乾燥できる装置が望まれている。   However, according to Patent Document 1, the material to be dried is input from the input hopper and is discharged from the exit chamber when the drying process is completed, and the large mass is discharged as a dry product made into a small mass. Is. For this reason, although it can use for a specific to-be-dried material, it could not be used for various to-be-dried materials. For this reason, the apparatus which can be used for various to-be-dried objects and can dry efficiently is desired.

また、装置内に対象物を設置してから装置を立ち上げるため、水蒸気が湿った状態で被乾燥物と触れ、その表面における凝縮量が多くなる。さらに、製品の取り出し毎に装置内部を空気と置換するため、装置の再立ち上げに時間がかかるという問題もあった。   In addition, since the apparatus is started up after the object is installed in the apparatus, the amount of condensation on the surface of the apparatus increases due to contact with the object to be dried in a state where the water vapor is wet. Furthermore, since the inside of the apparatus is replaced with air each time a product is taken out, there is a problem that it takes time to restart the apparatus.

本発明の課題は、種々の被乾燥物を乾燥処理することができ、効率よく乾燥処理を行える過熱水蒸気乾燥装置を提供することにある。   The subject of this invention is providing the superheated steam drying apparatus which can dry-process various to-be-dried objects and can perform a drying process efficiently.

上記課題を解決するため、本発明によれば、過熱水蒸気を供給する過熱水蒸気供給手段と、過熱水蒸気を導入することにより、過熱水蒸気雰囲気下で被乾燥物を乾燥させるための乾燥部と、被乾燥物を収納し乾燥部内外に移動可能に構成され、その本体の少なくとも一部が乾燥部外とされる第一位置において、被乾燥物を収納し、第一位置よりもその本体が乾燥部内に移動した第二位置において、乾燥部に導入された過熱水蒸気をその本体内に導入して収納された被乾燥物を乾燥させる収納部と、を備える過熱水蒸気乾燥装置が提供される。   In order to solve the above problems, according to the present invention, a superheated steam supply means for supplying superheated steam, a drying section for drying a material to be dried in a superheated steam atmosphere by introducing superheated steam, It is configured to store dry matter and be movable inside and outside the drying unit, and stores the material to be dried at a first position where at least a part of the main body is outside the drying unit. A superheated steam drying apparatus is provided that includes, in a second position moved to, a storage unit that introduces superheated steam introduced into the drying unit into the main body and dries the material to be dried.

本発明の過熱水蒸気乾燥装置において、より具体的には、収納部は、乾燥部に導入された過熱水蒸気を本体内に導入する水蒸気導入口と、本体内に導入された過熱水蒸気を排出する水蒸気排出口とを備え、収納部が第一位置において、水蒸気導入口及び水蒸気排出口が閉状態とされて、乾燥部に導入された過熱水蒸気は、収納部に導入されずに乾燥部から排出され、収納部が第二位置において、水蒸気導入口及び水蒸気排出口が開状態とされて、乾燥部に導入された過熱水蒸気は、収納部に導入されたのち、乾燥部から排出される構成を採用することができる。   In the superheated steam drying apparatus of the present invention, more specifically, the storage unit includes a steam inlet for introducing the superheated steam introduced into the drying unit into the main body, and a steam for discharging the superheated steam introduced into the main body. The superheated steam introduced into the drying section is discharged from the drying section without being introduced into the storage section when the storage section is in the first position and the steam inlet and the steam outlet are closed. When the storage unit is in the second position, the steam inlet and the steam outlet are opened, and the superheated steam introduced into the drying unit is introduced into the storage unit and then discharged from the drying unit. can do.

また、乾燥部又は収納部の少なくともいずれか一方に、過熱水蒸気の循環経路部と非循環経路部とを仕切る仕切り部が形成され、収納部が第一位置において、水蒸気導入口及び水蒸気排出口が仕切り部によって乾燥部の非循環経路部側に位置して閉状態とされ、収納部が第二位置において水蒸気導入口及び水蒸気排出口が仕切り部によって乾燥部の循環経路部側に位置して開状態とされるように構成することができる。   Further, at least one of the drying part and the storage part is formed with a partition part for partitioning the circulation path part of the superheated steam and the non-circulation path part, and when the storage part is at the first position, the steam introduction port and the steam discharge port are provided. The partition portion is positioned on the non-circulation path section side of the drying section to be closed, and the storage section is in the second position and the water vapor inlet and the water vapor discharge port are positioned on the circulation path section side of the drying section by the partition section and opened. It can be configured to be in a state.

収納部は、その移動方向に対して平行な周面部に水蒸気導入口及び水蒸気排出口が形成された構成とするとよい。そして、乾燥部に、過熱水蒸気を導入する乾燥部水蒸気導入口、及び過熱水蒸気を排出する乾燥部水蒸気排出口が設けられ、収納部が第二位置において、収納部の水蒸気導入口、水蒸気排出口、乾燥部の乾燥部水蒸気導入口、及び乾燥部水蒸気排出口が直線状に配置されるように構成することができる。   The storage section may have a structure in which a water vapor inlet and a water vapor outlet are formed in a peripheral surface parallel to the moving direction. The drying section is provided with a drying section steam inlet for introducing superheated steam and a drying section steam outlet for discharging superheated steam, and when the storage section is at the second position, the steam inlet, steam outlet of the storage section The drying unit water vapor inlet and the drying unit water vapor outlet of the drying unit can be arranged in a straight line.

さらに収納部は、第一位置において開閉可能な開閉部が設けられ、該開閉部を開閉して、被乾燥物の出し入れを行うようにすることができる。   Further, the storage unit is provided with an openable / closable portion that can be opened and closed at the first position.

過熱水蒸気供給手段は、乾燥部へ導入されて排出された過熱水蒸気を再び乾燥部へと循環する循環手段、水蒸気を供給する蒸気供給部、水蒸気及び過熱水蒸気を過熱する過熱部が設けられている構成とすることができる。   The superheated steam supply means is provided with a circulation means for circulating the superheated steam introduced and discharged to the drying section to the drying section again, a steam supply section for supplying steam, and a superheat section for superheating the steam and superheated steam. It can be configured.

さらに、本発明の過熱水蒸気乾燥装置において、収納部に収納されて乾燥処理される被乾燥物の水分蒸発に伴う余剰水蒸気を排出する余剰水蒸気排出手段を備える構成とすることができる。   Furthermore, the superheated steam drying apparatus of the present invention can be configured to include surplus steam discharging means for discharging surplus steam accompanying the evaporation of moisture of the material to be dried that is stored in the storage unit and dried.

また、乾燥部内の圧力を検知する圧力検知手段と、該圧力検知手段による圧力検知結果に基づいて、乾燥部内の圧力を調整する圧力調整手段とを備える構成とすることもできる。   Moreover, it can also be set as the structure provided with the pressure detection means which detects the pressure in a drying part, and the pressure adjustment means which adjusts the pressure in a drying part based on the pressure detection result by this pressure detection means.

本発明の過熱水蒸気乾燥装置は、被乾燥物(対象物)を乾燥させる収納部を乾燥部の内外に移動可能に構成され、過熱水蒸気をバイパスさせて循環させておくことができる。このため、乾燥処理前に予め過熱水蒸気を循環させた状態で装置を立ち上げることができ、また装置内を空気に置換することなく対象物の仕込みや取り出しを行うことができる。したがって短時間にて乾燥処理を行うことができる。また対象物の仕込み、取り出し時の作業が容易である。そして、前もって過熱水蒸気を循環させておくため、水蒸気が乾いた状態で対象物と接触させることができ、対象物への水分の影響を最小限にすることができる。また、食品や食品廃棄物等に対しては、乾燥とともに殺菌を行うことができる。   The superheated steam drying apparatus of the present invention is configured so that a storage section for drying an object to be dried (object) can be moved in and out of the drying section, and can circulate by bypassing the superheated steam. For this reason, the apparatus can be started up in a state in which superheated steam is circulated in advance before the drying process, and an object can be charged and taken out without replacing the inside of the apparatus with air. Therefore, the drying process can be performed in a short time. Moreover, the work at the time of preparation and removal of the object is easy. Since the superheated steam is circulated in advance, the steam can be brought into contact with the object in a dry state, and the influence of moisture on the object can be minimized. In addition, food and food waste can be sterilized with drying.

以下、図面を参照しつつ本発明の実施の形態について説明する。本発明は、以下の実施形態に限定されるものではなく、発明の範囲を逸脱しない限りにおいて、変更、修正、改良を加え得るものである。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. The present invention is not limited to the following embodiments, and changes, modifications, and improvements can be added without departing from the scope of the invention.

図1に本発明の過熱水蒸気乾燥装置1を示す。過熱水蒸気乾燥装置1は、水蒸気を供給する蒸気供給部8、水蒸気を循環させる循環ファン(循環手段)7、水蒸気を過熱するヒータ(過熱部)5が設けられている。蒸気供給部8、循環ファン7、ヒータ5は、過熱水蒸気供給手段を構成する。   FIG. 1 shows a superheated steam dryer 1 of the present invention. The superheated steam drying apparatus 1 is provided with a steam supply unit 8 that supplies water vapor, a circulation fan (circulation means) 7 that circulates water vapor, and a heater (superheater) 5 that superheats water vapor. The steam supply unit 8, the circulation fan 7, and the heater 5 constitute superheated steam supply means.

蒸気供給部8、循環ファン7、ヒータ5は、流通管12によって各々が接続されて閉回路が形成され、その閉回路内に乾燥部2が設けられている。乾燥部2は、過熱水蒸気供給手段から過熱水蒸気を導入することにより、過熱水蒸気雰囲気下で被乾燥物(対象物)を乾燥・殺菌する。さらに、被乾燥物を収納し乾燥部2内外に移動可能に構成された収納部3が設けられている。図1に示すように、収納部3は、その本体の少なくとも一部が乾燥部2外とされる第一位置において、被乾燥物(対象物)を収納し、第一位置よりもその本体が乾燥部2内に移動した第二位置(図3(b)参照)において、乾燥部2に導入された過熱水蒸気をその本体内に導入して収納された被乾燥物を乾燥させる。   The steam supply unit 8, the circulation fan 7, and the heater 5 are connected by a circulation pipe 12 to form a closed circuit, and the drying unit 2 is provided in the closed circuit. The drying unit 2 dries and sterilizes an object to be dried (object) in an atmosphere of superheated steam by introducing superheated steam from the superheated steam supply means. Furthermore, a storage unit 3 configured to store an object to be dried and move inside and outside the drying unit 2 is provided. As shown in FIG. 1, the storage unit 3 stores an object to be dried (target object) at a first position where at least a part of the main body is outside the drying unit 2, and the main body is positioned more than the first position. At the second position (see FIG. 3B) that has moved into the drying unit 2, the superheated steam introduced into the drying unit 2 is introduced into the main body to dry the material to be dried.

そして収納部3は、乾燥部2に導入された過熱水蒸気を本体内に導入する水蒸気導入口31と、本体内に導入された過熱水蒸気を排出する水蒸気排出口32とを備え、収納部3が第一位置において、水蒸気導入口31及び水蒸気排出口32が閉状態とされて、乾燥部2に導入された過熱水蒸気は、収納部3に導入されずに乾燥部2から排出され、収納部3が第二位置において、水蒸気導入口31及び水蒸気排出口32が開状態とされて、乾燥部2に導入された過熱水蒸気は、収納部3に導入されたのち、乾燥部2から排出される。このような構成により、収納部3を移動させることにより、収納部3内に過熱水蒸気を導入して、収納部3内の被乾燥物を乾燥させることができる。   The storage unit 3 includes a water vapor inlet 31 for introducing the superheated steam introduced into the drying unit 2 into the main body, and a water vapor discharge port 32 for discharging the superheated steam introduced into the main body. In the first position, the water vapor inlet 31 and the water vapor outlet 32 are closed, and the superheated steam introduced into the drying unit 2 is discharged from the drying unit 2 without being introduced into the storage unit 3, and is stored in the storage unit 3. However, in the second position, the steam inlet 31 and the steam outlet 32 are opened, and the superheated steam introduced into the drying unit 2 is introduced into the storage unit 3 and then discharged from the drying unit 2. With such a configuration, by moving the storage unit 3, it is possible to introduce superheated steam into the storage unit 3 and dry the object to be dried in the storage unit 3.

より具体的には、収納部3は、過熱水蒸気の循環経路部23と非循環経路部24とを仕切る仕切り部25が形成され、乾燥部2には、乾燥部水蒸気導入口21、及び乾燥部水蒸気排出口22が設けられている。   More specifically, the storage unit 3 is formed with a partition 25 that partitions the superheated steam circulation path 23 and the non-circulation path 24, and the drying unit 2 includes a drying unit steam inlet 21 and a drying unit. A water vapor outlet 22 is provided.

収納部3は、円筒状に形成され、水蒸気導入口31及び水蒸気排出口32が移動方向に対して平行な周面部(円筒部)33に形成されている。さらに収納部3は、第一位置において開閉可能な開閉部34が設けられている。開閉部34は、前面扉として形成されており、開閉部34を開閉して、被乾燥物の出し入れを行うことができる。   The accommodating part 3 is formed in a cylindrical shape, and the water vapor inlet 31 and the water vapor outlet 32 are formed in a peripheral surface part (cylindrical part) 33 parallel to the moving direction. Furthermore, the storage part 3 is provided with an opening / closing part 34 that can be opened and closed at the first position. The opening / closing part 34 is formed as a front door, and the opening / closing part 34 can be opened and closed so that an object to be dried can be taken in and out.

このような構成により、収納部3が第一位置において、水蒸気導入口31及び水蒸気排出口32が仕切り部25によって乾燥部2の非循環経路部24に位置して閉状態とされる。また収納部3が第二位置において、水蒸気導入口31及び水蒸気排出口32が仕切り部25によって乾燥部2の循環経路部23に位置して開状態とされ、収納部3の水蒸気導入口31、水蒸気排出口32、乾燥部水蒸気導入口21、及び乾燥部水蒸気排出口22が直線状に配置されて、収納部3に過熱水蒸気を導入して被乾燥物を乾燥・殺菌することができる。被乾燥物を乾燥処理した過熱水蒸気は、排出口32から排出される。   With such a configuration, when the storage unit 3 is in the first position, the water vapor inlet 31 and the water vapor outlet 32 are positioned in the non-circulation path 24 of the drying unit 2 by the partition unit 25 and are closed. Further, when the storage unit 3 is in the second position, the water vapor introduction port 31 and the water vapor discharge port 32 are opened by being positioned in the circulation path unit 23 of the drying unit 2 by the partition unit 25, and the water vapor introduction port 31 of the storage unit 3, The water vapor discharge port 32, the drying unit water vapor introduction port 21, and the drying unit water vapor discharge port 22 are arranged in a straight line, and superheated water vapor can be introduced into the storage unit 3 to dry and sterilize the material to be dried. The superheated steam obtained by drying the material to be dried is discharged from the discharge port 32.

さらに、過熱水蒸気乾燥装置1は、前述の過熱水蒸気を導入するために水蒸気を供給する蒸気供給部8、被乾燥物の水分蒸発に伴う余剰水蒸気を排出する余剰水蒸気排出手段9、乾燥部2内に図示されない圧力検知手段を備える。   Further, the superheated steam drying apparatus 1 includes a steam supply unit 8 for supplying steam for introducing the above-described superheated steam, surplus steam discharge means 9 for discharging surplus steam accompanying moisture evaporation of the object to be dried, Includes pressure detection means not shown in FIG.

図2を用いて、過熱水蒸気乾燥装置1の動作原理を説明する。蒸気供給部8、循環ファン7、ヒータ5は、流通管12によって各々が接続されて閉回路が形成され、その閉回路内に乾燥部2が設けられている。また蒸気供給部8には、蒸気弁が設けられ、蒸気弁を開として水蒸気を装置内に導入することができ、ヒータ5によって水蒸気を過熱することができる。このような構成により、過熱水蒸気が閉回路内を循環し、収納部3に収納された被乾燥物を乾燥・殺菌処理することができる。また余剰水蒸気排出手段9は、電磁弁が設けられ、被乾燥物の水分蒸発に伴う余剰水蒸気を排出することができる。蒸気供給部8と余剰水蒸気排出手段9によって、閉回路内の過熱水蒸気が適度となるように調整することができる。   The operation principle of the superheated steam dryer 1 will be described with reference to FIG. The steam supply unit 8, the circulation fan 7, and the heater 5 are connected by a circulation pipe 12 to form a closed circuit, and the drying unit 2 is provided in the closed circuit. The steam supply unit 8 is provided with a steam valve, and the steam valve can be opened to introduce water vapor into the apparatus, and the water vapor can be superheated by the heater 5. With such a configuration, the superheated steam circulates in the closed circuit, and the object to be dried stored in the storage unit 3 can be dried and sterilized. The surplus water vapor discharge means 9 is provided with a solenoid valve, and can discharge surplus water vapor accompanying water evaporation of the material to be dried. The steam supply unit 8 and the surplus steam discharge means 9 can be adjusted so that the superheated steam in the closed circuit becomes appropriate.

本発明の過熱水蒸気乾燥装置1による乾燥方法は、被乾燥物を過熱水蒸気(100〜400℃)の閉回路系において回分式で連続的に乾燥させることが主な特徴であり、乾燥部2の循環経路部内の空気を過熱水蒸気に十分に置換した後、収納部3を乾燥部2内にスライドさせることにより、被乾燥物を乾燥部2内に導入し、乾燥部2内の過熱水蒸気雰囲気を一定条件に維持するように過熱水蒸気を循環させながら、回分式で連続的に被乾燥物の乾燥を行うことができる。また収納部3を乾燥部2外の方向にスライドさせることにより、過熱水蒸気雰囲気を開放することなく過熱水蒸気を循環させた状態で、乾燥処理後の被乾燥物を取り出すことができる。   The drying method by the superheated steam drying apparatus 1 of the present invention is mainly characterized in that an object to be dried is continuously dried in a batch system in a closed circuit system of superheated steam (100 to 400 ° C.). After sufficiently replacing the air in the circulation path with superheated steam, the storage unit 3 is slid into the drying unit 2 to introduce the material to be dried into the drying unit 2, and the superheated steam atmosphere in the drying unit 2 is changed. The product to be dried can be continuously dried batchwise while circulating the superheated steam so as to maintain a constant condition. In addition, by sliding the storage unit 3 in the direction outside the drying unit 2, the material to be dried after the drying process can be taken out in a state where the superheated steam is circulated without opening the superheated steam atmosphere.

過熱水蒸気による乾燥方法とは、飽和水蒸気温度以上の高い温度の乾燥能力を有した蒸気(ドライスチーム)による乾燥方法である。水蒸気は100℃未満では飽和水蒸気であり乾燥能力を持たないが、100℃以上になると乾燥能力を有するようになり、温度を上げる程、乾燥速度は高まるため、物品を乾燥させ易くなる。ここで、過熱水蒸気とは、100℃で蒸発した飽和水蒸気を常圧のまま、100℃以上に過熱した水蒸気である。   The drying method using superheated steam is a drying method using steam (dry steam) having a drying ability at a temperature higher than the saturated steam temperature. Water vapor is saturated water vapor at less than 100 ° C. and does not have a drying ability. However, when it reaches 100 ° C. or higher, it has a drying ability. The higher the temperature, the higher the drying speed, and the easier it is to dry the article. Here, the superheated steam is steam that has been heated to 100 ° C. or more while maintaining saturated steam evaporated at 100 ° C. at normal pressure.

過熱水蒸気による乾燥の特徴は、乾燥部2内を水蒸気で満たしたまま乾燥を行えるため、被乾燥物の酸化や被乾燥物表面の硬化による皮質の形成が無く、品物が予熱された水分蒸発期間での品温がほぼ100℃に保持されるので、殺菌、滅菌、酵素失活も被乾燥物の内部まで行うことができる。   The feature of drying with superheated steam is that the drying part 2 can be dried while being filled with water vapor, so there is no formation of cortex due to oxidation of the material to be dried or hardening of the surface of the material to be dried, and the moisture evaporation period in which the product is preheated Since the product temperature is maintained at approximately 100 ° C., sterilization, sterilization, and enzyme deactivation can be performed up to the inside of the object to be dried.

本発明の過熱水蒸気装置1は、熱媒体ガスが閉回路であるため、被乾燥物から発生する臭気の乾燥装置外部への排出を防止又は抑制することができ、過熱水蒸気を用いることにより、被乾燥物の品質を維持しつつ、被乾燥物の殺菌、滅菌が行え、被乾燥物内部まで乾燥することができ、更には省エネルギーで低ランニングコストである。   In the superheated steam device 1 of the present invention, since the heating medium gas is a closed circuit, it is possible to prevent or suppress the discharge of odor generated from the material to be dried to the outside of the drying device. While maintaining the quality of the dried product, the material to be dried can be sterilized and sterilized, and the inside of the material to be dried can be dried. Further, energy saving and low running cost are achieved.

本発明における乾燥処理では、ほぼ100%の過熱水蒸気が常圧で占有する雰囲気下で、被乾燥物を連続的に乾燥させることが重要である。尚、常圧過熱水蒸気に占有された雰囲気は、空気分圧がほぼ「ゼロ」であり、空気がほとんど介在しないため、ほぼ「無酸素状態」を呈する。このような雰囲気を乾燥部2内に一定の条件で維持し、継続的に無酸素状態を維持するためには、乾燥部2内を微小プラス圧とすることが重要である。   In the drying treatment in the present invention, it is important to continuously dry the material to be dried in an atmosphere in which almost 100% of superheated steam is occupied at normal pressure. Note that the atmosphere occupied by the normal pressure superheated steam has almost zero air partial pressure, and almost no air is present. In order to maintain such an atmosphere in the drying unit 2 under certain conditions and maintain an oxygen-free state continuously, it is important that the drying unit 2 has a minute positive pressure.

このため、本発明では、乾燥に使用された過熱水蒸気を、電気ヒータ5で再過熱して乾燥部2内に再循環させたり、余剰な水蒸気を排出することが好ましい。   For this reason, in this invention, it is preferable to reheat the superheated steam used for drying by the electric heater 5, and to recirculate it in the drying part 2, or to discharge | emit excess steam.

尚、本発明では、乾燥部2内に、水蒸気を直接導入してもよいが、熱風と噴霧水から過熱水蒸気を発生させるように構成することもできる。   In the present invention, water vapor may be directly introduced into the drying unit 2, but it is also possible to generate superheated steam from hot air and spray water.

また、本発明の乾燥処理において、熱媒体ガスの過熱水蒸気を閉回路式で行うことが重要である。これにより、乾燥処理中、乾燥部2内への空気の流入や乾燥部2外への排ガスの流出がないため、酸素による被乾燥物の酸化が生じることがなく、乾燥部2から発生した臭気を抑制することができるため、環境改善に貢献することができる。   In the drying process of the present invention, it is important to perform the superheated steam of the heat medium gas in a closed circuit system. As a result, there is no inflow of air into the drying unit 2 or outflow of exhaust gas to the outside of the drying unit 2 during the drying process, so that the object to be dried is not oxidized by oxygen, and the odor generated from the drying unit 2 Therefore, it is possible to contribute to environmental improvement.

乾燥処理について、図3(a)、図3(b)、図4(a)及び図4(b)を用いてさらに説明する。まず被乾燥物を収納部3に収納するために、図3(a)、図4(a)に示すように、収納部3の本体の一部が乾燥部2外とされる第一位置にする。この第一位置において、収納部3の水蒸気導入口31及び水蒸気排出口32は、乾燥部2の非循環経路部24に位置し、乾燥部2に導入された過熱水蒸気は、収納部3には導入されず、バイパス循環する状態となる。このように収納部3をスライドして引き出した状態で、各バルブを閉めて循環ファン7とヒータ5を起動する。そして、蒸気弁(図2参照)を開いて、循環経路内に水蒸気を導入する。水蒸気がヒータ5によって過熱され、循環ファン7によって循環されて、循環経路部内が過熱水蒸気によって置換されると、蒸気弁を閉じる。   The drying process will be further described with reference to FIGS. 3A, 3B, 4A, and 4B. First, in order to store an object to be dried in the storage unit 3, as shown in FIGS. 3A and 4A, a part of the main body of the storage unit 3 is at a first position where it is outside the drying unit 2. To do. In this first position, the water vapor inlet 31 and the water vapor outlet 32 of the storage unit 3 are located in the non-circulation path unit 24 of the drying unit 2, and the superheated steam introduced into the drying unit 2 is stored in the storage unit 3. It is not introduced and is in a state of bypass circulation. With the storage part 3 slid out in this way, the valves are closed and the circulation fan 7 and the heater 5 are started. Then, the steam valve (see FIG. 2) is opened to introduce water vapor into the circulation path. When the steam is superheated by the heater 5 and circulated by the circulation fan 7, and the inside of the circulation path is replaced by the superheated steam, the steam valve is closed.

次に、引き出されている収納部3の移動方向外側に設けられた開閉部34を図1に示すように開状態として、被乾燥物(対象物)を収納する。被乾燥物を収納すると、図3(b)及び図4(b)に示すように、第一位置よりも収納部3の本体が乾燥部2内とされる第二位置にする。この状態において、水蒸気導入口31及び水蒸気排出口32が仕切り部25によって乾燥部2の循環経路部23に位置し、収納部3の水蒸気導入口31、水蒸気排出口32、乾燥部水蒸気導入口21、及び乾燥部水蒸気排出口22が直線状に配置されて、収納部3に過熱水蒸気を導入して被乾燥物を乾燥させることができる。   Next, the opening / closing part 34 provided on the outer side in the moving direction of the storage part 3 that is pulled out is opened as shown in FIG. 1 to store an object to be dried (object). When the object to be dried is stored, the main body of the storage unit 3 is set to the second position in the drying unit 2 rather than the first position, as shown in FIGS. 3 (b) and 4 (b). In this state, the water vapor introduction port 31 and the water vapor discharge port 32 are located in the circulation path portion 23 of the drying unit 2 by the partition portion 25, and the water vapor introduction port 31, the water vapor discharge port 32, and the drying unit water vapor introduction port 21 of the storage unit 3. And the drying part water vapor | steam discharge port 22 is arrange | positioned linearly, superheated steam can be introduce | transduced into the accommodating part 3, and a to-be-dried object can be dried.

水蒸気導入口31、水蒸気排出口32、乾燥部水蒸気導入口21、及び乾燥部水蒸気排出口22が直線状に配置されていることから、過熱水蒸気を効率よく循環させることができる。また、収容部3に、過熱水蒸気の循環経路部23と非循環経路部24とを仕切る仕切り部25が形成されていることから、収納部3を第一位置と第二位置に移動させることにより、水蒸気導入口31及び水蒸気排出口32に特別な開閉装置を設置しなくても、これらを閉状態と開状態にすることができる。なお、仕切り部25は、乾燥部2に形成することもできる。   Since the steam inlet 31, the steam outlet 32, the drying part steam inlet 21, and the drying part steam outlet 22 are arranged in a straight line, the superheated steam can be circulated efficiently. Moreover, since the partition part 25 which partitions the circulation path part 23 and the non-circulation path part 24 of superheated steam is formed in the accommodating part 3, by moving the accommodating part 3 to a 1st position and a 2nd position Even if a special opening / closing device is not installed at the water vapor inlet 31 and the water vapor outlet 32, they can be in a closed state and an open state. In addition, the partition part 25 can also be formed in the drying part 2.

被乾燥物の水分が少ない場合は、蒸気弁を開けて、循環経路内に水蒸気を追加するとよい。また過熱水蒸気乾燥装置1は、乾燥部2内の圧力を検知する圧力検知手段と、圧力検知結果に基づいて乾燥部2内の圧力を調整する圧力調整手段を備え、圧力が上昇した場合には、電磁弁を開状態として、圧力が一定となるように制御する。   When the moisture of the material to be dried is low, it is preferable to open the steam valve and add water vapor in the circulation path. Moreover, the superheated steam drying apparatus 1 includes a pressure detection unit that detects the pressure in the drying unit 2 and a pressure adjustment unit that adjusts the pressure in the drying unit 2 based on the pressure detection result. Then, the solenoid valve is opened, and the pressure is controlled to be constant.

被乾燥物の乾燥処理が終了すれば、収納部3をスライドさせて引き出し、開閉部34を開けて被乾燥物を取り出すことができる。過熱水蒸気を循環経路内に保持した状態で、被乾燥物の取り出し、仕込みを行うことができる。   When the drying process of the object to be dried is completed, the storage unit 3 can be slid and pulled out, and the opening / closing part 34 can be opened to take out the object to be dried. With the superheated steam held in the circulation path, the material to be dried can be taken out and charged.

図5を用いて、本発明の第二の実施の形態について説明する。本実施の形態においては、過熱水蒸気の通流方向に対して略垂直となるように、収納部3内に被乾燥物を載置する棚段41が設けられている。棚段41は、収納部3に複数設けることもできる。このように構成することにより、過熱水蒸気の循環によって、被乾燥物を効果的に乾燥させることができる。これにより、粉状や小塊の被乾燥物を乾燥処理することも可能である。   The second embodiment of the present invention will be described with reference to FIG. In the present embodiment, a shelf 41 for placing an object to be dried is provided in the storage unit 3 so as to be substantially perpendicular to the flowing direction of superheated steam. A plurality of shelves 41 may be provided in the storage unit 3. By comprising in this way, a to-be-dried object can be effectively dried by circulation of superheated steam. Thereby, it is also possible to dry-process a powdery or small lump to-be-dried material.

図6を用いて、本発明の第三の実施の形態について説明する。本実施の形態においては、円筒状に形成された収納部3の内側に、収納部3と同心となる円筒状の回転ドラム42が備えられている。回転ドラム42内に被乾燥物を導入して、回転ドラムを回転させつつ、過熱水蒸気を循環させて、被乾燥物を効果的に乾燥させることができる。   A third embodiment of the present invention will be described with reference to FIG. In the present embodiment, a cylindrical rotating drum 42 that is concentric with the storage portion 3 is provided inside the storage portion 3 that is formed in a cylindrical shape. The material to be dried can be effectively dried by introducing the material to be dried into the rotating drum 42 and circulating the superheated steam while rotating the rotating drum.

以上のように、収納部3の内部構造を変えることにより、被乾燥物(対象物)に応じて、棚段式、攪拌式などの方式を採用することが可能である。これにより種々の被乾燥物の乾燥処理を行うことができる。   As described above, by changing the internal structure of the storage unit 3, it is possible to adopt a system such as a shelf type or a stirring type according to an object to be dried (object). Thereby, various drying objects can be dried.

本発明の過熱水蒸気乾燥装置は、食料、肥料、燃料等の種々の被乾燥物の乾燥装置として用いることが可能である。また、食品の乾燥・殺菌、食品廃棄物等の未利用資源の再利用化、電子部品、ガラス製品などの乾燥・殺菌に利用することができる。   The superheated steam drying apparatus of the present invention can be used as a drying apparatus for various objects to be dried such as food, fertilizer and fuel. It can also be used for drying and sterilizing food, reusing unused resources such as food waste, and drying and sterilizing electronic parts and glass products.

本発明の過熱水蒸気乾燥装置の第一の実施の形態を示す構成図である。It is a block diagram which shows 1st embodiment of the superheated steam drying apparatus of this invention. 過熱水蒸気乾燥装置の原理図である。It is a principle diagram of a superheated steam dryer. 第一位置における動作を示す概略構成図である。It is a schematic block diagram which shows the operation | movement in a 1st position. 第二位置における動作を示す概略構成図である。It is a schematic block diagram which shows the operation | movement in a 2nd position. 第一位置における要部を示す模式図である。It is a schematic diagram which shows the principal part in a 1st position. 第二位置における要部を示す模式図である。It is a schematic diagram which shows the principal part in a 2nd position. 本発明の過熱水蒸気乾燥装置の第二の実施の形態を示す構成図である。It is a block diagram which shows 2nd embodiment of the superheated steam dryer of this invention. 本発明の過熱水蒸気乾燥装置の第三の実施の形態を示す構成図である。It is a block diagram which shows 3rd embodiment of the superheated steam drying apparatus of this invention.

符号の説明Explanation of symbols

1:過熱水蒸気乾燥装置、2:乾燥部、3:収納部、5:ヒータ、7:循環ファン、8:蒸気供給部、9:余剰水蒸気排出手段、12:流通管、21:乾燥部水蒸気導入口、22:乾燥部水蒸気排出口、23:循環経路部、24:非循環経路部、25:仕切り部、31:水蒸気導入口、32:水蒸気排出口、33:周面部、34:開閉部、41:棚段、42:回転ドラム 1: Superheated steam dryer, 2: Drying unit, 3: Storage unit, 5: Heater, 7: Circulation fan, 8: Steam supply unit, 9: Excess water vapor discharge means, 12: Distribution pipe, 21: Drying unit water vapor introduction Mouth, 22: Drying section steam outlet, 23: Circulating path section, 24: Non-circulating path section, 25: Partition section, 31: Steam inlet, 32: Steam outlet, 33: Circumferential section, 34: Opening / closing section, 41: shelf, 42: rotating drum

Claims (11)

過熱水蒸気を供給する過熱水蒸気供給手段と、
前記過熱水蒸気を導入することにより、過熱水蒸気雰囲気下で被乾燥物を乾燥させるための乾燥部と、
前記被乾燥物を収納し前記乾燥部内外に移動可能に構成され、その本体の少なくとも一部が前記乾燥部外とされる第一位置において、前記被乾燥物を収納し、前記第一位置よりもその本体が前記乾燥部内に移動した第二位置において、前記乾燥部に導入された前記過熱水蒸気をその本体内に導入して収納された前記被乾燥物を乾燥させる収納部と、
を備える過熱水蒸気乾燥装置。
Superheated steam supply means for supplying superheated steam;
By introducing the superheated steam, a drying section for drying the material to be dried in a superheated steam atmosphere;
In the first position where the object to be dried is stored and movable inside and outside the drying unit, and at least a part of the main body is outside the drying unit, the object to be dried is stored in the first position. In the second position where the main body has moved into the drying section, a storage section for introducing the superheated steam introduced into the drying section into the main body and drying the material to be dried,
A superheated steam drying device.
前記収納部は、前記乾燥部に導入された前記過熱水蒸気を前記本体内に導入する水蒸気導入口と、前記本体内に導入された前記過熱水蒸気を排出する水蒸気排出口とを備え、
前記収納部が前記第一位置において、前記水蒸気導入口及び前記水蒸気排出口が閉状態とされて、前記乾燥部に導入された前記過熱水蒸気は、前記収納部に導入されずに前記乾燥部から排出され、前記収納部が前記第二位置において、前記水蒸気導入口及び前記水蒸気排出口が開状態とされて、前記乾燥部に導入された前記過熱水蒸気は、前記収納部に導入されたのち、前記乾燥部から排出される請求項1に記載の過熱水蒸気乾燥装置。
The storage unit includes a steam inlet for introducing the superheated steam introduced into the drying unit into the main body, and a water vapor outlet for discharging the superheated steam introduced into the main body,
When the storage unit is in the first position, the steam inlet and the steam outlet are closed, and the superheated steam introduced into the drying unit is not introduced into the storage unit from the drying unit. The superheated steam introduced into the drying section is introduced into the storage section after being discharged and the storage section is in the second position, the steam inlet and the steam outlet are opened, and the drying section is introduced. The superheated steam dryer according to claim 1 discharged from the drying section.
前記乾燥部又は前記収納部の少なくともいずれか一方に、前記過熱水蒸気の循環経路部と非循環経路部とを仕切る仕切り部が形成され、
前記収納部が前記第一位置において、前記水蒸気導入口及び前記水蒸気排出口が前記仕切り部によって前記乾燥部の前記非循環経路部側に位置して閉状態とされ、前記収納部が前記第二位置において前記水蒸気導入口及び前記水蒸気排出口が前記仕切り部によって前記乾燥部の前記循環経路部側に位置して開状態とされるように構成された請求項2に記載の過熱水蒸気乾燥装置。
At least one of the drying unit or the storage unit is formed with a partition that partitions the superheated steam circulation path part and the non-circulation path part,
When the storage part is in the first position, the water vapor inlet and the water vapor outlet are closed by the partition part on the non-circulation path part side of the drying part, and the storage part is in the second position. The superheated steam drying device according to claim 2, wherein the steam inlet and the steam outlet are opened at a position on the circulation path portion side of the drying portion by the partition portion.
前記収納部は、その移動方向に対して平行な周面部に前記水蒸気導入口及び前記水蒸気排出口が形成された請求項3に記載の過熱水蒸気乾燥装置。   The superheated steam drying device according to claim 3, wherein the storage portion is formed with the steam inlet and the steam outlet on a peripheral surface parallel to a moving direction thereof. 前記乾燥部に、前記過熱水蒸気を導入する乾燥部水蒸気導入口、及び前記過熱水蒸気を排出する乾燥部水蒸気排出口が設けられ、
前記収納部が前記第二位置において、前記収納部の前記水蒸気導入口、前記水蒸気排出口、前記乾燥部の前記乾燥部水蒸気導入口、及び前記乾燥部水蒸気排出口が直線状に配置される請求項2ないし4のいずれか1項に記載の過熱水蒸気乾燥装置。
The drying unit is provided with a drying unit steam inlet for introducing the superheated steam, and a drying unit steam outlet for discharging the superheated steam,
The water vapor inlet, the water vapor outlet, the drying part water vapor inlet of the drying part, and the drying part water vapor outlet are arranged in a straight line when the storage part is in the second position. Item 5. The superheated steam drying apparatus according to any one of Items 2 to 4.
前記収納部は、前記第一位置において開閉可能な開閉部が設けられ、該開閉部を開閉して、前記被乾燥物の出し入れを行う請求項1ないし5のいずれか1項に記載の過熱水蒸気乾燥装置。   The superheated steam according to any one of claims 1 to 5, wherein the storage portion is provided with an opening / closing portion that can be opened and closed at the first position, and the opening / closing portion is opened and closed to allow the material to be dried to be taken in and out. Drying equipment. 前記過熱水蒸気供給手段は、前記乾燥部へ導入されて排出された前記過熱水蒸気を再び前記乾燥部へと循環する循環手段が設けられている請求項1ないし6のいずれか1項に記載の過熱水蒸気乾燥装置。   The superheated steam supply means according to any one of claims 1 to 6, wherein the superheated steam supply means is provided with a circulation means for circulating the superheated steam introduced and discharged to the drying section to the drying section again. Steam dryer. 前記過熱水蒸気供給手段は、水蒸気を供給する蒸気供給部が設けられている請求項1ないし7のいずれか1項に記載の過熱水蒸気乾燥装置。   The superheated steam drying device according to any one of claims 1 to 7, wherein the superheated steam supply means is provided with a steam supply unit for supplying steam. 前記過熱水蒸気供給手段は、前記水蒸気及び前記過熱水蒸気を過熱する過熱部が設けられている請求項8に記載の過熱水蒸気乾燥装置。   The superheated steam drying apparatus according to claim 8, wherein the superheated steam supply means is provided with a superheater that superheats the steam and the superheated steam. 前記収納部に収納されて乾燥処理される前記被乾燥物の水分蒸発に伴う余剰水蒸気を排出する余剰水蒸気排出手段を備える請求項1ないし9のいずれか1項に記載の過熱水蒸気乾燥装置。   The superheated steam drying apparatus according to any one of claims 1 to 9, further comprising surplus steam discharging means for discharging surplus steam accompanying the evaporation of moisture of the material to be dried which is stored in the storage unit and dried. 前記乾燥部内の圧力を検知する圧力検知手段と、
該圧力検知手段による圧力検知結果に基づいて、前記乾燥部内の圧力を調整する圧力調整手段とを備える請求項1ないし10のいずれか1項に記載の過熱水蒸気乾燥装置。
Pressure detecting means for detecting the pressure in the drying section;
The superheated steam drying apparatus according to any one of claims 1 to 10, further comprising: a pressure adjusting unit that adjusts a pressure in the drying unit based on a pressure detection result by the pressure detecting unit.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014070886A (en) * 2012-10-02 2014-04-21 Okawara Mfg Co Ltd Dehydration and concentration method and dehydration and concentration device
CN106895669A (en) * 2015-12-18 2017-06-27 无锡市金义博仪器科技有限公司 A kind of pipe drying device

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Publication number Priority date Publication date Assignee Title
JPS6115074A (en) * 1984-07-02 1986-01-23 金子農機株式会社 Sample cereal drier
JP2002027958A (en) * 2000-07-11 2002-01-29 Johnson Boiler Kk Apparatus for drying and sterilizing powdery or granular material
JP2002333103A (en) * 2001-05-10 2002-11-22 Katsumi Shibata Generating method of superheated steam and equipment therefor

Patent Citations (3)

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Publication number Priority date Publication date Assignee Title
JPS6115074A (en) * 1984-07-02 1986-01-23 金子農機株式会社 Sample cereal drier
JP2002027958A (en) * 2000-07-11 2002-01-29 Johnson Boiler Kk Apparatus for drying and sterilizing powdery or granular material
JP2002333103A (en) * 2001-05-10 2002-11-22 Katsumi Shibata Generating method of superheated steam and equipment therefor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014070886A (en) * 2012-10-02 2014-04-21 Okawara Mfg Co Ltd Dehydration and concentration method and dehydration and concentration device
CN106895669A (en) * 2015-12-18 2017-06-27 无锡市金义博仪器科技有限公司 A kind of pipe drying device

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