JP4801484B2 - Vacuum drying equipment - Google Patents

Vacuum drying equipment Download PDF

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JP4801484B2
JP4801484B2 JP2006099919A JP2006099919A JP4801484B2 JP 4801484 B2 JP4801484 B2 JP 4801484B2 JP 2006099919 A JP2006099919 A JP 2006099919A JP 2006099919 A JP2006099919 A JP 2006099919A JP 4801484 B2 JP4801484 B2 JP 4801484B2
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drying
condensed water
storage tank
water level
valve
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JP2007271223A (en
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清登 小川
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Osaka Gas Co Ltd
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Osaka Gas Co Ltd
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Description

本発明は乾燥釜の内部を真空状態で加熱して被乾燥物を乾燥する真空乾燥装置関する。 The present invention relates to a vacuum drying apparatus for drying the heated in a vacuum material to be dried to the drying cauldron.

従来、残飯や保証期間の過ぎた食料品、食品工場における残滓物等の有機廃棄物を減量する手段として真空乾燥装置が利用されている。一般的な真空乾燥装置は、例えば特許文献1に示すように被乾燥物が投入される乾燥釜と、乾燥釜内を加熱する加熱手段と、乾燥釜内を真空引きする真空ポンプを備え、乾燥釜内を真空状態で加熱して乾燥釜内の被乾燥物を乾燥するものである。   Conventionally, a vacuum drying apparatus has been used as a means for reducing organic waste such as leftover food, food products that have passed the warranty period, and residue in food factories. For example, as shown in Patent Document 1, a general vacuum drying apparatus includes a drying kettle in which an object to be dried is charged, a heating means for heating the inside of the drying kettle, and a vacuum pump for evacuating the inside of the drying kettle. The inside of the kettle is heated in a vacuum state to dry the object to be dried in the drying kettle.

ところでこの種の真空乾燥装置の乾燥釜による乾燥運転を終了時点を決定する方式として、タイマーにより乾燥運転を終了するものがあるが、乾燥前の被乾燥物の含水率に違いがある場合、乾燥後の被乾燥物の含水率が不安定になり、十分に乾燥できなかったり、乾燥しすぎたりしてしまう。   By the way, as a method of determining the end point of the drying operation by the drying pot of this type of vacuum drying apparatus, there is one that ends the drying operation by a timer, but if there is a difference in the moisture content of the material to be dried before drying, the drying operation is performed. The moisture content of the later dried product becomes unstable, and cannot be sufficiently dried or dried too much.

また他の方式として、乾燥釜の重量を測定するロードセルを設け、被乾燥物の乾燥に伴う水分蒸発により乾燥釜の重量が所定量低下した場合に、十分に乾燥がなされたと判断して乾燥釜による乾燥運転を終了するもの等もあるが、このものも乾燥前の被乾燥物の含水率に違いがある場合には乾燥後の被乾燥物の含水率が定まらず、また乾燥釜の重量を測定するロードセルが必要であるためコストが高くなるという問題もある。
特開平11−337258号公報
As another method, a load cell for measuring the weight of the drying kettle is provided, and when the weight of the drying kettle is reduced by a predetermined amount due to water evaporation accompanying drying of the object to be dried, it is judged that the drying kettle has been sufficiently dried. However, if there is a difference in the moisture content of the material to be dried before drying, the moisture content of the material to be dried after drying will not be determined, and the weight of the drying kettle will be reduced. There is also a problem that the cost increases because a load cell to be measured is required.
JP-A-11-337258

本発明は上記従来の問題点に鑑みて発明したものであって、乾燥前の含水率に違いがある場合にも、被乾燥物を過不足なく確実に乾燥でき、しかも乾燥釜の重量を計測するロードセルのような高価な計器を設ける必要のない真空乾燥装置提供することを課題とするものである。 The present invention was invented in view of the above-mentioned conventional problems, and even when there is a difference in moisture content before drying, the object to be dried can be reliably dried without excess and deficiency, and the weight of the drying kettle is measured. It is an object of the present invention to provide a vacuum drying apparatus that does not require an expensive instrument such as a load cell.

上記課題を解決するために請求項1の乾燥装置は、被乾燥物2が投入される乾燥釜1と、乾燥釜1内を加熱する加熱手段と、乾燥釜1内を真空状態とする真空ポンプ8を備え、乾燥釜1内を真空状態で加熱して被乾燥物2を乾燥する真空乾燥装置において、乾燥釜1内で発生する水蒸気を凝縮する凝縮手段と、留部6を備え、貯留部6は、乾燥釜1内に連通すると共に凝縮手段で得られた凝縮水が流入するクッションタンク22と、クッションタンク22よりも下方に位置してクッションタンク22に連通路24を介して接続される貯留タンク23を備え、クッションタンク22の上部に前記真空ポンプ8を接続し、連通路24に連通バルブ25を設けると共に貯留タンク23の排水部30に排水バルブ34を設け、乾燥運転時において、連通バルブ25を開くと共に排水バルブ34を閉じてクッションタンク22内の凝縮水を連通路24を介して貯留タンク23に流入させて貯留する通常状態とし、この通常状態において貯留タンク内水位検知手段により貯留タンク23内の凝縮水の水位が所定水位以上となったことを検知した際に、連通バルブ25を閉じると共に排水バルブ34を開いて乾燥釜1内の真空状態を維持しつつ貯留タンク23内の凝縮水を排水部から排出する排水状態に切替え、この所定時間経過後に前記通常状態に復帰する真空乾燥装置であって、クッションタンク22内に流入した凝縮水を受けるカップ部26と、カップ部26内の凝縮水の水位を検知するカップ部26内水位検知手段と、一端をカップ部26の底部に接続すると共に他端を貯留タンク23の上部に接続した排出流路27と、排出流路27に設けた排出バルブ28と、制御装置を備え、制御装置が、乾燥運転時において所定時間t2毎にカップ部26内の凝縮水の水位が予め設定した所定水位以上であるか否かを判定し、カップ部26内の凝縮水の水位が予め設定した所定水位以上の場合には排出バルブ28を開いてカップ部26内の凝縮水を排出流路27を介して貯留タンク23に排出してカップ部26内を空とし、この後排出バルブ28を閉じてカップ部26内に凝縮水を貯留可能な状態とし、前記カップ部26内の凝縮水の水位が前記所定水位よりも低い場合には乾燥運転を終了するものであることを特徴とする。 In order to solve the above problems, a drying apparatus according to claim 1 includes a drying kettle 1 into which an object to be dried 2 is charged, a heating means for heating the inside of the drying kettle 1, and a vacuum pump for making the inside of the drying kettle 1 in a vacuum state. with 8, in a vacuum drying apparatus for drying objects to be dried 2 by heating in a vacuum drying cauldron 1, a condensing means for condensing the steam generated in the drying cauldron 1, it includes a savings engaging portion 6, the reservoir The part 6 communicates with the inside of the drying kettle 1 and receives a condensed tank 22 into which condensed water obtained by the condensing means flows, and is positioned below the cushion tank 22 and connected to the cushion tank 22 via a communication passage 24. A storage tank 23, the vacuum pump 8 is connected to the upper part of the cushion tank 22, a communication valve 25 is provided in the communication path 24, and a drainage valve 34 is provided in the drainage part 30 of the storage tank 23. While the passage valve 25 is opened and the drain valve 34 is closed, the condensed water in the cushion tank 22 flows into the storage tank 23 through the communication passage 24 and is stored, and in this normal state, the storage tank water level detection means When it is detected that the water level of the condensed water in the storage tank 23 is equal to or higher than the predetermined water level, the communication valve 25 is closed and the drain valve 34 is opened to maintain the vacuum state in the drying tank 1 while maintaining the vacuum state in the storage tank 23. A vacuum drying device that switches to a drainage state in which the condensed water is discharged from the drainage portion and returns to the normal state after the lapse of a predetermined time , a cup portion 26 that receives the condensed water flowing into the cushion tank 22 , and a cup portion a cup portion 26 in the water level detection means for detecting the water level of the condensed water in 26, store the other end with connecting one end to the bottom of the cup portion 26 tank 23 A discharge passage 27 connected to the upper, and the discharge valve 28 provided in the discharge passage 27, a control device, control device, the water level of the condensed water in the cup portion 26 every predetermined time t2 during the drying operation It is determined whether or not the water level is equal to or higher than a predetermined water level set in advance. If the water level of the condensed water in the cup portion 26 is higher than the predetermined water level set in advance, the discharge valve 28 is opened to discharge the condensed water in the cup portion 26. empty the cup portion 26 is discharged to the reservoir tank 23 through the passage 27, the condensed water and capable of storing state in the cup portion 26 closes the discharge valve 28 after this, condensation inside the cup portion 26 when the water level of the water is lower than the predetermined water level is characterized in that to terminate the drying operation.

上記構成により乾燥運転時において被乾燥物2の単位時間当たりの蒸発水の量が少なくなったことをカップ部26内の凝縮水の水位に基づいて判定して乾燥運転を終了でき、これにより被乾燥物2が十分に乾燥した時に乾燥釜1の乾燥運転を確実に終了できる。またこの場合、ロードセルのような構造が複雑で高価な計器を設けることなく乾燥運転の終了時点を決定できてコストを削減できる。また、通常状態と排水状態とに切替えて乾燥釜1内の真空状態を維持しつつ貯留タンク23内の凝縮水を排水できる真空乾燥装置において、乾燥運転を確実に終了でき、コストを削減できる。 With the above configuration, it is possible to determine that the amount of evaporated water per unit time of the object to be dried 2 has decreased during the drying operation based on the level of the condensed water in the cup portion 26, and thus the drying operation can be terminated. When the dried product 2 is sufficiently dried, the drying operation of the drying pot 1 can be surely terminated. In this case, the end point of the drying operation can be determined without providing a complicated and expensive instrument such as a load cell, and the cost can be reduced. Further, in the vacuum drying apparatus that can switch between the normal state and the drainage state and drain the condensed water in the storage tank 23 while maintaining the vacuum state in the drying kettle 1, the drying operation can be completed with certainty, and the cost can be reduced.

本発明乾燥装置では、乾燥釜に投入される被乾燥物の含水率に違いがある場合にも、被乾燥物を過不足なく確実に乾燥でき、また乾燥釜の重量を計測するロードセルのような高価な計器を設ける必要がなくてコストを削減できる。 In the drying apparatus of the present invention, even when there is a difference in the moisture content of the material to be dried, the material to be dried can be surely dried without excess or deficiency, and a load cell that measures the weight of the drying vessel is used. Therefore, it is not necessary to provide an expensive instrument and the cost can be reduced.

以下、本発明を添付図面に示す実施形態に基づいて説明する。   Hereinafter, the present invention will be described based on embodiments shown in the accompanying drawings.

図1は本発明の真空乾燥装置の全体のシステムを示すものである。真空乾燥装置の主体となる乾燥釜1は内部に収納した被乾燥物2を真空状態で加熱して乾燥するようになっている。乾燥釜1の周囲には乾燥釜1内を加熱する加熱手段として加熱ジャケット3を設けてあり、この加熱ジャケット3に温水、蒸気等の熱媒で熱を供給することで乾燥釜1の内壁を加熱できるようになっている。この熱媒が温水の場合、図1の矢印Aのように加熱ジャケット3に熱媒が入り、加熱ジャケット3から図1の矢印Bのように熱媒が出るように熱源機を介して循環するようになっている。また熱媒が蒸気の場合は、図1の矢印Bと逆方向に熱媒が加熱ジャケット3に入り、図1の矢印Aと逆方向に加熱ジャケット3から熱媒が出るようになっている。   FIG. 1 shows the entire system of the vacuum drying apparatus of the present invention. A drying pot 1 serving as a main body of a vacuum drying apparatus is configured to heat and dry an object to be dried 2 housed therein in a vacuum state. A heating jacket 3 is provided around the drying kettle 1 as a heating means for heating the inside of the drying kettle 1, and heat is supplied to the heating jacket 3 with a heating medium such as hot water or steam to thereby coat the inner wall of the drying kettle 1. It can be heated. When this heat medium is hot water, the heat medium enters the heating jacket 3 as indicated by an arrow A in FIG. 1, and circulates through the heat source unit such that the heat medium exits from the heating jacket 3 as indicated by an arrow B in FIG. It is like that. When the heat medium is steam, the heat medium enters the heating jacket 3 in the direction opposite to the arrow B in FIG. 1, and the heat medium exits from the heating jacket 3 in the direction opposite to the arrow A in FIG.

乾燥釜1内の空気は集塵器4、熱交換器5、貯留部6、逆止弁7を順に介して真空ポンプ8で吸引されて乾燥釜1内の真空状態が維持されるようになっている。またクーリングタワー9で冷却された冷却水が熱交換器5に循環させられて熱交換器5が冷却されるようになっている。真空ポンプ8を駆動して乾燥釜1内を真空引きしたとき乾燥釜1内が60〜100Torr程度に減圧されるようになっている。乾燥釜1の加熱により乾燥釜1内の被乾燥物2に含有した水が蒸発されて行き、真空ポンプ8の吸引により蒸発水含有排ガスは集塵器4を通り、熱交換器5で冷却凝縮されて気液分離され、凝縮水が貯留部6に溜まると共にドライ排ガスは大気に排気される。つまり本例ではクーリングタワー9と凝縮部となる熱交換器5とで乾燥時に乾燥釜1内で発生する水蒸気を凝縮する凝縮手段を構成している。なお貯留部6に一定量の凝縮水が溜まると装置外部に排水されるようになっている。   The air in the drying kettle 1 is sucked by the vacuum pump 8 through the dust collector 4, the heat exchanger 5, the storage unit 6, and the check valve 7 in order, so that the vacuum state in the drying kettle 1 is maintained. ing. The cooling water cooled by the cooling tower 9 is circulated through the heat exchanger 5 so that the heat exchanger 5 is cooled. When the vacuum pump 8 is driven and the inside of the drying pot 1 is evacuated, the inside of the drying pot 1 is decompressed to about 60 to 100 Torr. The water contained in the material to be dried 2 in the drying kettle 1 is evaporated by heating the drying kettle 1, and the exhaust gas containing evaporated water passes through the dust collector 4 by the suction of the vacuum pump 8 and is cooled and condensed by the heat exchanger 5. As a result, gas-liquid separation is performed, and condensed water accumulates in the reservoir 6 and dry exhaust gas is exhausted to the atmosphere. That is, in this example, the cooling tower 9 and the heat exchanger 5 serving as a condensing part constitute condensing means for condensing water vapor generated in the drying kettle 1 during drying. In addition, when a certain amount of condensed water accumulates in the reservoir 6, it is drained outside the apparatus.

乾燥釜1の上部には水分を含んだ有機廃棄物からなる被乾燥物2が投入される投入口10を設けてあり、投入口10は開閉自在な投入口蓋11にて気密的に閉塞されている。乾燥釜1内の上部には投入口10から投入した被乾燥物2を受けるホッパー12を設けてあり、ホッパー12の下端の出口には破砕機13を配置してある。破砕機13はモータにて回転駆動される一対の駆動軸14と、各駆動軸14に軸方向に複数枚並べるように装着した破砕刃15とで構成されている。   At the top of the drying kettle 1 is provided an inlet 10 into which an object to be dried 2 made of organic waste containing moisture is introduced. The inlet 10 is airtightly closed by an openable / closable inlet lid 11. Yes. A hopper 12 that receives an object to be dried 2 introduced from an inlet 10 is provided in the upper part of the drying pot 1, and a crusher 13 is disposed at the lower end of the hopper 12. The crusher 13 includes a pair of drive shafts 14 that are rotationally driven by a motor, and a crushing blade 15 that is mounted on each drive shaft 14 so as to be arranged in the axial direction.

乾燥釜1内の下部には攪拌機16を内装し、被乾燥物2を攪拌機16にて攪拌することにより乾燥を促進できるようになっている。攪拌機16はモータで駆動される攪拌軸17から羽根支持軸18を放射状に突設すると共に羽根支持軸18の先端に羽根19を装着してあり、攪拌軸17を回転駆動することで羽根19にて攪拌できるようになっている。乾燥釜1の底部には乾燥した乾燥物を排出する乾燥物排出部20を設けてある。   A stirrer 16 is provided in the lower part of the drying pot 1, and drying can be promoted by stirring the material to be dried 2 with the stirrer 16. The stirrer 16 has a blade support shaft 18 projecting radially from a stirring shaft 17 driven by a motor and a blade 19 attached to the tip of the blade support shaft 18. Can be stirred. A dry matter discharge unit 20 for discharging the dried product is provided at the bottom of the drying pot 1.

上記のように構成せる真空乾燥装置で水分を含んだ有機廃棄物からなる被乾燥物2を乾燥する場合バッチ式で次のように行う。投入口10から乾燥釜1内のホッパー12に被乾燥物2を投入し、投入口蓋11を閉じた状態で、乾燥釜1の加熱ジャケット3に熱媒を供給して乾燥釜1内を加熱すると共に真空ポンプ8を駆動して乾燥釜1内を真空引きし、破砕機13を駆動し、攪拌機16を駆動する。すると、ホッパー12に投入された被乾燥物2は破砕機13で破砕され乾燥釜1内の下部に供給される。乾燥釜1内の下部に落下した被乾燥物2は攪拌機16で攪拌されながら乾燥釜1の雰囲気で乾燥される。例えば含水率が60%から10%になるように乾燥される。この乾燥された乾燥物は細かな粒状となり、乾燥物が排出部20から排出され、これにより乾燥運転が終了する。   When drying the to-be-dried object 2 which consists of organic waste containing a water | moisture content with the vacuum drying apparatus comprised as mentioned above, it carries out as follows by a batch type. The material to be dried 2 is charged from the charging port 10 to the hopper 12 in the drying kettle 1, and the heating chamber 3 of the drying kettle 1 is supplied with a heating medium with the charging port lid 11 closed to heat the drying kettle 1. At the same time, the vacuum pump 8 is driven to evacuate the inside of the drying kettle 1, the crusher 13 is driven, and the stirrer 16 is driven. Then, the to-be-dried object 2 thrown into the hopper 12 is crushed by the crusher 13 and supplied to the lower part in the drying pot 1. The to-be-dried object 2 dropped to the lower part in the drying pot 1 is dried in the atmosphere of the drying pot 1 while being stirred by the stirrer 16. For example, it is dried so that the water content is 60% to 10%. The dried product is finely granulated, and the dried product is discharged from the discharge unit 20, thereby completing the drying operation.

ここで上記熱交換器5により得た凝縮水が流入する貯留部6の構造について詳述する。   Here, the structure of the reservoir 6 into which the condensed water obtained by the heat exchanger 5 flows will be described in detail.

図2に示すように貯留部6は、熱交換器5で得られた凝縮水が流入するクッションタンク22と、クッションタンク22の下方に位置してクッションタンク22に接続された貯留タンク23を備えており、クッションタンク22の上端部に前述の真空ポンプ8を接続している。   As shown in FIG. 2, the storage unit 6 includes a cushion tank 22 into which condensed water obtained by the heat exchanger 5 flows, and a storage tank 23 that is positioned below the cushion tank 22 and connected to the cushion tank 22. The above-described vacuum pump 8 is connected to the upper end portion of the cushion tank 22.

クッションタンク22の底部には下端を貯留タンク23の上端部に接続した連通路24の上端を接続している。連通路24には電磁開閉弁からなる連通バルブ25を設けてあり、連通バルブ25を開くことでクッションタンク22内に流入した凝縮水を連通路24を介して貯留タンク23に排出できる。クッションタンク22内の底部における連通路24とは別の箇所には熱交換器5側から流れ込んだ凝縮水を直接受けるカップ部26を設けてあり、カップ部26の底部には下端を貯留タンク23の上端部に接続した排出流路27の上端を接続している。排出流路27には電磁開閉弁からなる排出バルブ28を設けてあり、排出バルブ28を閉じることでカップ部26内に熱交換器5側から流入した凝縮水を貯留でき、また排出バルブ28を開くことでカップ部26内の凝縮水を排出流路27を介して貯留タンク23に流すことができる。またクッションタンク22にはカップ部26内の水位を検知するカップ部内水位検知手段としてカップ部26内の水位が予め設定した所定水位以上であるか否かを検知する水位センサ29を設けている。 The bottom end of the cushion tank 22 is connected to the upper end of the communication path 24 whose lower end is connected to the upper end of the storage tank 23. The communication passage 24 is provided with a communication valve 25 composed of an electromagnetic on-off valve. By opening the communication valve 25, the condensed water flowing into the cushion tank 22 can be discharged to the storage tank 23 via the communication passage 24. A cup portion 26 that directly receives condensed water flowing from the heat exchanger 5 side is provided at a location different from the communication passage 24 at the bottom portion in the cushion tank 22, and a lower end is provided at the bottom portion of the cup portion 26 at the storage tank 23. The upper end of the discharge flow path 27 connected to the upper end of each is connected. The discharge passage 27 is provided with a discharge valve 28 composed of an electromagnetic opening / closing valve. By closing the discharge valve 28, the condensed water flowing from the heat exchanger 5 side can be stored in the cup portion 26, and the discharge valve 28 is provided. By opening, the condensed water in the cup part 26 can be flowed to the storage tank 23 via the discharge flow path 27. Further, the cushion tank 22 is provided with a water level sensor 29 for detecting whether or not the water level in the cup part 26 is equal to or higher than a predetermined water level as a water level detecting means in the cup part for detecting the water level in the cup part 26.

一方、貯留タンク23の底部には貯留タンク23内の凝縮水を外部に排出する排水口からなる排水部30を設けてあり、排水部30には電磁開閉弁からなる排水バルブ34を設けている。貯留タンク23の上端部には貯留タンク23内を大気開放する開放口からなる大気開放部31を設けてあり、大気開放部31には電磁開閉弁からなる大気開放バルブ32を設けている。また貯留タンク23には貯留タンク23内に貯留された凝縮水の水位を検知する貯留タンク内水位検知手段として貯留タンク23内の水位が予め設定した所定水位以上であるか否かを検知する水位センサ33を設けている。 On the other hand, a drainage part 30 consisting of a drainage outlet for discharging condensed water in the storage tank 23 to the outside is provided at the bottom of the storage tank 23, and a drainage valve 34 consisting of an electromagnetic on-off valve is provided in the drainage part 30. . At the upper end of the storage tank 23 is provided an air release portion 31 that is an open port that opens the inside of the storage tank 23 to the atmosphere, and the air release portion 31 is provided with an air release valve 32 that is an electromagnetic on-off valve. Further, the storage tank 23 is a water level that detects whether or not the water level in the storage tank 23 is equal to or higher than a predetermined water level as a water level detection means in the storage tank that detects the water level of the condensed water stored in the storage tank 23. A sensor 33 is provided.

そして上記クッションタンク22の連通バルブ25及び排出バルブ28、貯留タンク23の排出バルブ28及び大気開放バルブ32は真空乾燥装置に設けた制御装置(図示せず)によって以下に示すように制御される。なお図3は乾燥運転時におけるタイムチャートである。   The communication valve 25 and the discharge valve 28 of the cushion tank 22 and the discharge valve 28 and the air release valve 32 of the storage tank 23 are controlled as shown below by a control device (not shown) provided in the vacuum drying device. FIG. 3 is a time chart during the drying operation.

制御装置は、加熱ジャケット3、真空ポンプ8、破砕機13、攪拌機16の夫々を駆動して乾燥釜1の乾燥運転を開始すると、連通バルブ25を開くと共に排出バルブ28、排水バルブ34、大気開放バルブ32を閉じた通常状態とする。これにより乾燥釜1内の空気はクッションタンク22を介して真空ポンプ8で吸引されて乾燥釜1内は真空状態となる。またこの時、乾燥釜1の乾燥運転時において熱交換器5で得られた凝縮水は、図2の白抜き矢印に示すようにクッションタンク22のカップ部26内に流れ込んでカップ部26に貯留され、カップ部26一杯に溜まった後はカップ部26から溢れ出て、クッションタンク22の底部から連通路24を介して貯留タンク23に流入して貯留される。なおこの通常状態では、連通バルブ25が開き、且つ排水バルブ34及び大気開放バルブ32が閉じた状態にあるため、貯留タンク23内も真空引きされて真空状態となる。   When the control device drives the heating jacket 3, the vacuum pump 8, the crusher 13, and the stirrer 16 to start the drying operation of the drying pot 1, the communication valve 25 is opened and the discharge valve 28, the drain valve 34, and the atmosphere are opened. The valve 32 is closed and in a normal state. As a result, the air in the drying kettle 1 is sucked by the vacuum pump 8 through the cushion tank 22 and the drying kettle 1 is in a vacuum state. At this time, the condensed water obtained by the heat exchanger 5 during the drying operation of the drying pot 1 flows into the cup portion 26 of the cushion tank 22 and is stored in the cup portion 26 as indicated by the white arrow in FIG. After the cup portion 26 is fully filled, the cup portion 26 overflows and flows into the storage tank 23 from the bottom of the cushion tank 22 via the communication path 24 and is stored. In this normal state, since the communication valve 25 is open and the drain valve 34 and the air release valve 32 are closed, the inside of the storage tank 23 is also evacuated to a vacuum state.

また制御装置は、上記乾燥釜1の乾燥運転時の通常状態において貯留タンク23の水位センサ33により貯留タンク23内の凝縮水の水位が所定水位以上となったことを検知した際には、連通バルブ25及び排出バルブ28を閉じ、この後、大気開放バルブ32を開き、さらにこの後、排水バルブ34を開いた排水状態とする。これにより乾燥釜1内の空気がクッションタンク22を介して真空ポンプ8で吸引されたままの状態(即ち乾燥釜1側が密閉状態にあり真空を維持した状態)で、貯留タンク23内が大気開放部31から大気開放されて貯留タンク23内の真空が破壊された後に貯留タンク23内に貯留された凝縮水が排水部30を介して外部に排水されて貯留タンク23内が空となる。なおこの時連通バルブ25が閉じた状態にあるため熱交換器5側からクッションタンク22内に流入した凝縮水はクッションタンク22内で一時的に貯留され、貯留タンク23側には流れない。そしてこの後、制御装置は所定時間が経過した時点で排水バルブ34及び大気開放バルブ32を閉じ、この後、連通バルブ25を開き、これにより前記通常状態に復帰する。即ち制御装置は上記通常状態と排水状態を交互に繰り返し行って乾燥運転を行う。   Further, when the control device detects that the water level of the condensed water in the storage tank 23 is equal to or higher than the predetermined water level by the water level sensor 33 of the storage tank 23 in the normal state during the drying operation of the drying pot 1, the communication device communicates. The valve 25 and the discharge valve 28 are closed, and then the atmosphere release valve 32 is opened. Thereafter, the drain valve 34 is opened, and the drainage state is set. As a result, the air in the drying tank 1 remains sucked by the vacuum pump 8 via the cushion tank 22 (that is, the drying tank 1 side is in a sealed state and the vacuum is maintained), and the storage tank 23 is opened to the atmosphere. The condensed water stored in the storage tank 23 after being released to the atmosphere from the section 31 and breaking the vacuum in the storage tank 23 is drained to the outside through the drainage section 30 and the storage tank 23 is emptied. At this time, since the communication valve 25 is closed, the condensed water flowing into the cushion tank 22 from the heat exchanger 5 side is temporarily stored in the cushion tank 22 and does not flow to the storage tank 23 side. Thereafter, the control device closes the drain valve 34 and the air release valve 32 when a predetermined time has elapsed, and then opens the communication valve 25, thereby returning to the normal state. That is, the control device performs the drying operation by alternately repeating the normal state and the drainage state.

また制御装置は、上記乾燥釜1の乾燥運転時おいて、凝縮水の所定時間当たりの発生量が予め設定した量よりも少なくなった場合に、加熱ジャケット3、真空ポンプ8、破砕機13、攪拌機16等の運転を停止して乾燥運転を終了する。 The control unit 35 also, the drying Oite during the drying operation of the kettle 1, when the generation amount per predetermined time of the condensed water becomes less than the amount set in advance, a heating jacket 3, the vacuum pump 8, crusher 13 Then, the operation of the stirrer 16 and the like is stopped and the drying operation is terminated.

具体的には、制御装置は、まず乾燥釜1の乾燥運転開始から所定時間t1(1〜2時間)が経過するまでの間は被乾燥物2の水が蒸発し難い初期期間として排出バルブ28を閉じた状態を維持する。なおこの初期期間終了時点において被乾燥物2から発生する凝縮水の単位時間あたりの量は、後述のように乾燥運転の終了を決定する時における所定時間t2あたりの凝縮水の発生量に見合った単位時間当たりの凝縮水の発生量よりも大きいものである。そしてこの初期期間が終えた時点から所定時間t2(30分)毎に水位センサ29によりカップ部26内の凝縮水の水位が予め設定した所定水位以上であるか否かを判定する。そしてこの判定により、カップ部26内の凝縮水の水位が予め設定した所定水位以上の場合には、排出バルブ28を開いてカップ部26内の凝縮水を排出流路27を介して貯留タンク23に流してカップ部26内を空とし、この後排出バルブ28を閉じてカップ部26内に凝縮水を貯留可能な状態とする。またこの判定により、カップ部26内の凝縮水の水位が所定水位よりも低い場合には、加熱ジャケット3や真空ポンプ8の運転を停止して乾燥運転を終了する。なお上記判定により、カップ部26内の凝縮水の水位が予め設定した所定水位以上であった場合に行う排出バルブ28の開動作は、真空乾燥装置が上記排水状態にあり排出バルブ28を閉じた状態にある時には無効とされ、次回判定時や次回通常状態復帰時に所定時間排出バルブ28を開くものとする。   Specifically, the control device first sets the discharge valve 28 as an initial period during which the water of the object to be dried 2 is difficult to evaporate until a predetermined time t1 (1 to 2 hours) elapses from the start of the drying operation of the drying pot 1. Keep closed. The amount of condensed water per unit time generated from the material to be dried 2 at the end of the initial period is commensurate with the amount of condensed water generated per predetermined time t2 when determining the end of the drying operation as described later. It is larger than the amount of condensed water generated per unit time. Then, the water level sensor 29 determines whether or not the water level of the condensed water in the cup portion 26 is equal to or higher than a predetermined water level set in advance by the water level sensor 29 every predetermined time t2 (30 minutes) from the end of the initial period. If it is determined that the water level of the condensed water in the cup portion 26 is equal to or higher than a predetermined water level set in advance, the discharge valve 28 is opened to allow the condensed water in the cup portion 26 to pass through the discharge passage 27 to the storage tank 23. Then, the cup portion 26 is emptied, and then the discharge valve 28 is closed so that condensed water can be stored in the cup portion 26. Moreover, when the water level of the condensed water in the cup part 26 is lower than a predetermined water level by this determination, the operation of the heating jacket 3 and the vacuum pump 8 is stopped and the drying operation is terminated. According to the above determination, the opening operation of the discharge valve 28 performed when the water level of the condensed water in the cup portion 26 is equal to or higher than a predetermined water level set in advance is that the vacuum drying device is in the drainage state and the discharge valve 28 is closed It is invalid when it is in the state, and the discharge valve 28 is opened for a predetermined time at the next determination or at the next normal state recovery.

このように本発明では制御装置により被乾燥物2の乾燥運転時において排出される凝縮水の所定時間当たりの排出量が予め設定した量よりも少なくなった場合に乾燥運転を終了するので、以下の効果が得られる。即ち、被乾燥物2を乾燥した場合、通常、単位時間当たりに被乾燥物2から蒸発する水の量は被乾燥物2の含水率が低くなる程少なくなるものであるため、該単位時間当たりの蒸発水の量が少なくなった場合には被乾燥物2が十分に乾燥したと判断できるものである。つまり本発明では上記のように乾燥運転時に凝縮手段にて得られる凝縮水の所定時間当たりの発生量が予め設定した量よりも少なくなった場合に乾燥運転を終了するので、乾燥釜1に投入される乾燥前の被乾燥物2の含水率に違いがある場合にも、被乾燥物2を乾燥しすぎることなく且つ十分に乾燥できる。また本発明では上記被乾燥物2の単位時間当たりの蒸発水の量が少なくなったことをカップ部26内の凝縮水の水位に基づいて判定でき、ロードセルのような構造が複雑で高価な計器を乾燥釜に設けることなく乾燥運転の終了時点を決定できてコストを削減できる。   Thus, in the present invention, the drying operation is terminated when the amount of condensed water discharged by the control device during the drying operation of the object to be dried 2 per predetermined time is less than the preset amount. The effect is obtained. That is, when the object to be dried 2 is dried, the amount of water evaporated from the object to be dried 2 per unit time usually decreases as the moisture content of the object to be dried 2 decreases. When the amount of evaporating water decreases, it can be determined that the material to be dried 2 is sufficiently dried. In other words, in the present invention, the drying operation is terminated when the amount of condensed water obtained by the condensing means during the drying operation per predetermined time is less than a preset amount. Even when there is a difference in the moisture content of the dried product 2 before drying, the dried product 2 can be sufficiently dried without being dried too much. Further, according to the present invention, it is possible to determine that the amount of evaporated water per unit time of the object to be dried 2 is reduced based on the water level of the condensed water in the cup portion 26, and the load cell-like structure is complicated and expensive. It is possible to determine the end point of the drying operation without providing the in the drying pot, and to reduce the cost.

本発明の真空乾燥装置の実施の形態の一例のシステム全体を示す概念図である。It is a conceptual diagram which shows the whole system of an example of embodiment of the vacuum drying apparatus of this invention. 同上の貯留部の説明図である。It is explanatory drawing of a storage part same as the above. 同上のタイムチャートである。It is a time chart same as the above.

符号の説明Explanation of symbols

1 乾燥釜
2 被乾燥物
8 真空ポンプ
22 クッションタンク
23 貯留タンク
24 連通路
25 連通バルブ
26 カップ部
27 排出流路
30 排水部
DESCRIPTION OF SYMBOLS 1 Drying pot 2 To-be-dried object 8 Vacuum pump 22 Cushion tank 23 Storage tank 24 Communication path 25 Communication valve 26 Cup part 27 Discharge flow path 30 Drain part

Claims (1)

被乾燥物が投入される乾燥釜と、乾燥釜内を加熱する加熱手段と、乾燥釜内を真空状態とする真空ポンプを備え、乾燥釜内を真空状態で加熱して被乾燥物を乾燥する真空乾燥装置において、
乾燥釜内で発生する水蒸気を凝縮する凝縮手段と、留部を備え、貯留部は、乾燥釜内に連通すると共に凝縮手段で得られた凝縮水が流入するクッションタンクと、クッションタンクよりも下方に位置してクッションタンクに連通路を介して接続される貯留タンクを備え、クッションタンクの上部に前記真空ポンプを接続し、連通路に連通バルブを設けると共に貯留タンクの排水部に排水バルブを設け、
乾燥運転時において、連通バルブを開くと共に排水バルブを閉じてクッションタンク内の凝縮水を連通路を介して貯留タンクに流入させて貯留する通常状態とし、この通常状態において貯留タンク内水位検知手段により貯留タンク内の凝縮水の水位が所定水位以上となったことを検知した際に、連通バルブを閉じると共に排水バルブを開いて乾燥釜内の真空状態を維持しつつ貯留タンク内の凝縮水を排水部から排出する排水状態に切替え、この所定時間経過後に前記通常状態に復帰する真空乾燥装置であって、
クッションタンク内に流入した凝縮水を受けるカップ部と、カップ部内の凝縮水の水位を検知するカップ部内水位検知手段と、一端をカップ部の底部に接続すると共に他端を貯留タンクの上部に接続した排出流路と、排出流路に設けた排出バルブと、制御装置を備え、制御装置が、乾燥運転時において所定時間毎にカップ部内の凝縮水の水位が予め設定した所定水位以上であるか否かを判定し、カップ部内の凝縮水の水位が予め設定した所定水位以上の場合には排出バルブを開いてカップ部内の凝縮水を排出流路を介して貯留タンクに排出してカップ部内を空とし、この後排出バルブを閉じてカップ部内に凝縮水を貯留可能な状態とし、前記カップ部内の凝縮水の水位が前記所定水位よりも低い場合には乾燥運転を終了するものである特徴とする真空乾燥装置
A drying kettle into which the material to be dried is put, a heating means for heating the inside of the drying kettle, and a vacuum pump for evacuating the inside of the drying kettle are provided. The inside of the drying kettle is heated in a vacuum state to dry the material to be dried. In vacuum drying equipment,
A condensing means for condensing the steam generated in the drying kiln, with a savings engaging portion, the reservoir portion, and a cushion tank condensate obtained by condensing means communicates with the drying kiln flows, than the cushion tank A storage tank that is located below and is connected to the cushion tank via a communication path is connected. The vacuum pump is connected to the upper part of the cushion tank, a communication valve is provided in the communication path, and a drain valve is provided in the drainage section of the storage tank. Provided,
During the drying operation, the communication valve is opened and the drain valve is closed so that the condensed water in the cushion tank flows into the storage tank through the communication path to be stored, and in this normal state, the storage tank water level detection means When it is detected that the water level of the condensed water in the storage tank has reached the specified level or higher, the condensate water in the storage tank is drained while closing the communication valve and opening the drain valve to maintain the vacuum state in the drying tank. A vacuum drying device that switches to a drained state that is discharged from the part and returns to the normal state after the predetermined time has elapsed,
A cup that receives the condensed water flowing into the cushion tank , a water level detecting means for detecting the level of condensed water in the cup , and one end connected to the bottom of the cup and the other connected to the top of the storage tank a discharge passage which is either a discharge valve provided in the discharge passage, a control device, control device, the water level of the condensed water in the cup portion every predetermined time during the drying operation is a predetermined level or more set in advance If the water level of the condensed water in the cup part is equal to or higher than a predetermined water level set in advance, the discharge valve is opened and the condensed water in the cup part is discharged to the storage tank via the discharge flow path, and the inside of the cup part is discharged. sky and then, the feature is intended Thereafter the condensed water and capable of storing state in the cup portion closes the discharge valve, when the water level of the condensed water in the cup portion is lower than the predetermined water level to end the drying operation That vacuum drying equipment.
JP2006099919A 2006-03-31 2006-03-31 Vacuum drying equipment Expired - Fee Related JP4801484B2 (en)

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