JP6100084B2 - Evaporative concentration apparatus and cleaning method thereof - Google Patents

Evaporative concentration apparatus and cleaning method thereof Download PDF

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JP6100084B2
JP6100084B2 JP2013101027A JP2013101027A JP6100084B2 JP 6100084 B2 JP6100084 B2 JP 6100084B2 JP 2013101027 A JP2013101027 A JP 2013101027A JP 2013101027 A JP2013101027 A JP 2013101027A JP 6100084 B2 JP6100084 B2 JP 6100084B2
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heat transfer
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evaporator
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condensed water
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JP2014221441A (en
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恵理 鈴木
恵理 鈴木
智裕 井上
智裕 井上
西村 靖史
靖史 西村
利幸 辻本
利幸 辻本
晃平 山田
晃平 山田
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Sasakura Engineering Co Ltd
Suntory Holdings Ltd
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Suntory Holdings Ltd
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Description

本発明は、液体を蒸発濃縮する蒸発濃縮装置およびその洗浄方法に関し、更に詳しくは、食品用の液体を濃縮するのに好適な蒸発濃縮装置およびその洗浄方法に関する。   The present invention relates to an evaporation concentration apparatus for evaporating and concentrating a liquid and a cleaning method thereof, and more particularly to an evaporation concentration apparatus suitable for concentrating a liquid for food and a cleaning method thereof.

液体を蒸発濃縮する蒸発濃縮装置として、例えば、特許文献1には、下部に濃縮処理される廃液等の被処理液が貯留される密閉型の蒸発器内の上部に、複数の伝熱管を設け、各伝熱管の外表面に、循環ポンプによって供給される被処理液を散布ノズルで散布することによって蒸発させ、発生した蒸気を、蒸気エゼクターで圧縮して昇温し、この昇温した蒸気を、ダクトを介して前記各伝熱管内に供給することによって、各伝熱管の外表面に散布される被処理液を加熱、蒸発させるようにした蒸発濃縮装置が開示されている。 As an evaporative concentration apparatus for evaporating and concentrating a liquid, for example, in Patent Document 1, a plurality of heat transfer tubes are provided in an upper part of a hermetic evaporator in which a liquid to be treated such as a waste liquid to be concentrated is stored in a lower part. The liquid to be treated supplied by a circulation pump is sprayed on the outer surface of each heat transfer tube by a spray nozzle, and the generated steam is heated by compressing it with a steam ejector. An evaporative concentration apparatus is disclosed in which the liquid to be treated sprayed on the outer surface of each heat transfer tube is heated and evaporated by supplying the heat transfer tube through the duct.

特開平7−24202号公報Japanese Patent Laid-Open No. 7-24202

かかる蒸発濃縮装置によって濃縮処理される被処理液が廃液である場合、廃液には、種々の金属成分が含有されていることがあり、時間の経過に伴って次第に、伝熱管の外表面にスケールとして付着し、伝熱効率が低下することになる。   When the liquid to be processed to be concentrated by the evaporative concentration apparatus is a waste liquid, the waste liquid may contain various metal components, and gradually scales on the outer surface of the heat transfer tube as time passes. As a result, the heat transfer efficiency decreases.

このため、従来では、定期的に人手によって装置を開放し、ジェットノズルからの高圧洗浄液を装置内部の伝熱管外表面などに噴射して洗浄するようにしている。   For this reason, conventionally, the apparatus is periodically opened manually and the high-pressure cleaning liquid from the jet nozzle is sprayed onto the outer surface of the heat transfer tube inside the apparatus for cleaning.

被処理液が、廃液ではなく、例えば、お茶、コーヒー、スープエキス等の食品用の液体である場合には、衛生上、各部に付着した残渣等を取除いて常に清潔に保つと共に、残渣等による変質や味の劣化等を防止するために、頻繁に洗浄する必要がある。更に、被処理液を加熱する伝熱管の外表面のみならず、その内部の洗浄も行えるようにすることが好ましい。   If the liquid to be treated is not a waste liquid but a liquid for food such as tea, coffee, soup extract, etc. It is necessary to wash frequently in order to prevent deterioration or deterioration of taste due to. Furthermore, it is preferable that not only the outer surface of the heat transfer tube for heating the liquid to be treated but also the inside thereof can be cleaned.

しかしながら、上述のように、定期的に人手によって装置を開放して高圧洗浄液を噴射して洗浄する従来の蒸発濃縮装置では、かかる頻繁な洗浄や伝熱管内部の洗浄は困難である。   However, as described above, in the conventional evaporative concentration apparatus in which the apparatus is periodically opened manually and the high pressure cleaning liquid is sprayed for cleaning, it is difficult to perform such frequent cleaning or cleaning of the inside of the heat transfer tube.

本発明は、上述のような点に鑑みてなされたものであって、伝熱管内部の洗浄を行えるようにし、更には、各部を容易に洗浄できるようにすることを目的とする。   The present invention has been made in view of the above points, and it is an object of the present invention to allow the inside of a heat transfer tube to be cleaned, and to easily clean each part.

本発明では、上記目的を達成するために、次のように構成している。   In order to achieve the above object, the present invention is configured as follows.

(1)本発明の蒸発濃縮装置は、被処理液を大気圧以下の減圧状態で蒸発させる蒸発器を備える蒸発濃縮装置であって、前記蒸発器内には、被処理液を加熱する複数の伝熱管が配置され、前記蒸発器の底部に貯留される被処理液を、前記蒸発器の上部に戻して、前記伝熱管の外表面に供給する循環手段と、蒸気が供給される前記伝熱管内で生成される凝縮水を排出する凝縮水ポンプと、前記伝熱管内に洗浄液を供給する洗浄液供給管路と、前記凝縮水ポンプの吐出側の排出経路を分岐して前記伝熱管に接続する分岐経路とを備え、前記凝縮水ポンプから前記凝縮水が吐出されるときには、吐出される前記凝縮水を、前記排出経路を介して排出し、前記凝縮水ポンプから前記洗浄液が吐出されるときには、吐出される前記洗浄液を、前記分岐経路を介して前記伝熱管内に導入することにより、前記洗浄液を、前記凝縮水ポンプと前記伝熱管との間で循環させるものである(1) An evaporation concentrating apparatus of the present invention is an evaporation concentrating apparatus including an evaporator that evaporates a liquid to be processed in a reduced pressure state equal to or lower than an atmospheric pressure, and includes a plurality of heating liquids in the evaporator. Circulating means in which a heat transfer tube is disposed and the liquid to be treated stored in the bottom of the evaporator is returned to the top of the evaporator and supplied to the outer surface of the heat transfer tube, and the heat transfer to which steam is supplied A condensed water pump that discharges condensed water generated in the pipe, a cleaning liquid supply pipe that supplies cleaning liquid into the heat transfer pipe, and a discharge path on the discharge side of the condensed water pump are branched and connected to the heat transfer pipe. A branch path, and when the condensed water is discharged from the condensed water pump, the discharged condensed water is discharged through the discharge path, and when the cleaning liquid is discharged from the condensed water pump, The cleaning liquid to be discharged is By introducing into the heat transfer tube through, the washing solution, in which is circulated between the heat transfer tube and the condensed water pump.

本発明の蒸発濃縮装置によると、複数の伝熱管内で生成される凝縮水を排出する凝縮水ポンプの吐出側の排出経路を分岐して、凝縮水ポンプからの水を前記伝熱管内へ導入する分岐経路を設けているので、伝熱管内からの水を凝縮水ポンプによって分岐経路を介して再び伝熱管内に戻すことができる。これによって、洗浄液を、伝熱管と凝縮ポンプとの間で循環させて伝熱管の内部を洗浄することが可能となる。   According to the evaporative concentration apparatus of the present invention, the discharge path on the discharge side of the condensed water pump that discharges the condensed water generated in the plurality of heat transfer tubes is branched, and the water from the condensed water pump is introduced into the heat transfer tubes. Therefore, the water from the heat transfer tube can be returned to the heat transfer tube again through the branch route by the condensed water pump. Accordingly, the cleaning liquid can be circulated between the heat transfer tube and the condensing pump to clean the inside of the heat transfer tube.

(2)本発明の蒸発濃縮装置の好ましい実施態様では、前記蒸発器内には、該蒸発器の内面および前記伝熱管の外表面に洗浄液を噴射する噴射器が設けられる。   (2) In a preferred embodiment of the evaporation concentrator of the present invention, an injector for injecting a cleaning liquid onto the inner surface of the evaporator and the outer surface of the heat transfer tube is provided in the evaporator.

この実施態様によると、蒸発器内には噴射器を設けているので、噴射器から蒸発器の内面および伝熱管の外表面に対して洗浄液を噴射して容易に洗浄することができる。   According to this embodiment, since the injector is provided in the evaporator, the cleaning liquid can be easily sprayed from the injector to the inner surface of the evaporator and the outer surface of the heat transfer tube.

(3)本発明の蒸発濃縮装置は、被処理液を大気圧以下の減圧状態で蒸発させる蒸発器を備える蒸発濃縮装置であって、前記蒸発器内には、被処理液を加熱する複数の伝熱管が配置され、前記蒸発器の底部に貯留される被処理液を、前記蒸発器の上部に戻して、前記伝熱管の外表面に供給する循環手段と、蒸気が供給される前記伝熱管内で生成される凝縮水を排出する凝縮水ポンプと、前記蒸発器で発生する蒸気を圧縮して前記伝熱管内に供給する圧縮機とを備え、前記凝縮水ポンプの吐出側の排出経路を分岐して、該凝縮水ポンプから吐出される水を前記伝熱管内に導入する分岐経路を設け、前記蒸発器から前記圧縮機に至る管路内には、洗浄液を前記管路内に噴射する噴射器が設けられ、前記圧縮機から前記伝熱管に至る管路の途中には、開閉弁が設けられる。 (3) evaporation equipment of the present invention is an evaporative concentration apparatus comprising an evaporator for evaporating the liquid to be treated in the following reduced pressure atmosphere, inside the evaporator, a plurality of heating the liquid to be treated The heat transfer tube is disposed, circulating means for returning the liquid to be treated stored at the bottom of the evaporator to the top of the evaporator and supplying it to the outer surface of the heat transfer tube, and the heat transfer supplied to the steam. A discharge path on the discharge side of the condensed water pump, comprising: a condensed water pump that discharges condensed water generated in the heat pipe; and a compressor that compresses steam generated in the evaporator and supplies the compressed steam to the heat transfer pipe. And a branch path for introducing water discharged from the condensate pump into the heat transfer pipe is provided, and cleaning liquid is injected into the pipe from the evaporator to the compressor. In the middle of the pipe line from the compressor to the heat transfer pipe Off valve is provided.

本発明によると、圧縮機から伝熱管に至る管路の途中の開閉弁を閉じて、蒸発器から圧縮機に至る管路内の噴射器から洗浄液を噴射することによって、蒸発器から開閉弁に至る管路内および圧縮機を洗浄することができる。 According to the present invention , the on-off valve in the middle of the pipe line from the compressor to the heat transfer pipe is closed, and the cleaning liquid is injected from the injector in the pipe line from the evaporator to the compressor, so that the evaporator changes from the evaporator to the on-off valve. The entire pipeline and the compressor can be cleaned.

(4)本発明の蒸発濃縮装置の更に他の実施態様では、前記被処理液が、食品用の液体である。   (4) In still another embodiment of the evaporative concentration apparatus of the present invention, the liquid to be treated is a liquid for food.

この実施態様によると、伝熱管の内部を洗浄できると共に、噴射器によって蒸発器内部や管路を容易に洗浄できるので、衛生上、常に清潔に保つために頻繁な洗浄が要求される食品用の液体の濃縮に好適である。   According to this embodiment, the inside of the heat transfer tube can be washed, and the inside of the evaporator and the pipe line can be easily washed by the injector. Therefore, for foods that require frequent washing in order to keep it hygienic all the time. Suitable for liquid concentration.

(5)本発明の蒸発濃縮装置の洗浄方法は、本発明に係る蒸発濃縮装置の洗浄方法であって、前記凝縮水ポンプの吐出側を、前記排出経路から前記分岐経路に切替え、前記洗浄を、前記凝縮水ポンプと前記伝熱管との間で循環させるものである。 (5) cleaning method of evaporation apparatus of the present invention is a cleaning method of evaporation apparatus according to the present invention, the discharge side of the condensed water pump, switching from the discharge route to the branch path, the washing liquid Is circulated between the condensate pump and the heat transfer tube.

本発明の蒸発濃縮装置の洗浄方法によると、伝熱管の内部を、洗浄液によって洗浄することができる。   According to the cleaning method of the evaporative concentration apparatus of the present invention, the inside of the heat transfer tube can be cleaned with the cleaning liquid.

本発明によれば、洗浄液を、伝熱管と凝縮ポンプとの間で循環させることによって、伝熱管の内部を洗浄することが可能となる。   According to the present invention, the inside of the heat transfer tube can be cleaned by circulating the cleaning liquid between the heat transfer tube and the condensation pump.

図1は本発明の一実施形態の蒸発濃縮装置の構成図である。FIG. 1 is a configuration diagram of an evaporative concentration apparatus according to an embodiment of the present invention. 図2は本発明の他の実施形態の蒸発濃縮装置の構成図である。FIG. 2 is a configuration diagram of an evaporative concentration apparatus according to another embodiment of the present invention.

以下、図面によって本発明の実施形態について詳細に説明する。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

図1は、本発明の一実施形態に係る蒸発濃縮装置の構成図である。   FIG. 1 is a configuration diagram of an evaporative concentration apparatus according to an embodiment of the present invention.

この実施形態の蒸発濃縮装置は、被処理液として、食品用の液体、例えばお茶、コーヒー、果汁、牛乳、ジャムやスープ等を蒸発濃縮するものであり、密閉型の蒸発器1を備えている。   The evaporative concentration apparatus of this embodiment is a device for evaporating and concentrating a liquid for food such as tea, coffee, fruit juice, milk, jam or soup as a liquid to be treated, and includes a sealed evaporator 1. .

この蒸発器1は、全体として縦長の直方体形状であって、底部が四角錐形状をなしている。   The evaporator 1 has a vertically long rectangular parallelepiped shape as a whole, and the bottom portion has a quadrangular pyramid shape.

この蒸発器1の四角錐状の底部は、被処理液を貯留する液溜部18となっており、その上部には、左右一対のヘッダー2,3が設けられると共に、両ヘッダー2,3の間を繋ぐ複数本の伝熱管4が水平方向に設けられる。また、両ヘッダー2,3の内、一方の入口側のヘッダー2内には、入口室2aと折り返し室2bとを区画する仕切り板2cが設けられ、他方の出口側のヘッダー3内には、折り返し室3aと出口室3bとを区画する仕切り板3cが設けられる。   The bottom portion of the square pyramid of the evaporator 1 is a liquid reservoir 18 for storing the liquid to be treated. A pair of left and right headers 2 and 3 are provided on the top, and both the headers 2 and 3 are provided. A plurality of heat transfer tubes 4 connecting them are provided in the horizontal direction. In addition, a partition plate 2c that partitions the inlet chamber 2a and the folding chamber 2b is provided in the header 2 on one inlet side of the headers 2 and 3, and in the header 3 on the other outlet side, A partition plate 3c that partitions the folding chamber 3a and the outlet chamber 3b is provided.

この出口側のヘッダー3の折り返し室3aの下部には、伝熱管4を流下して溜まった凝縮液を排出するための排出経路としての排出管路27が接続され、この排出管路27の途中に凝縮水ポンプ11が設けられている。出口側のヘッダー3の折り返し室3aと凝縮水ポンプ27との間の排出管路27には、後述の洗浄時以外の濃縮処理時には、開放されている第1開閉弁28が設けられている。また、凝縮水ポンプ11の吐出側の排出管路27には、凝縮水の排水時に開放される第3開閉弁37が設けられている。   A discharge pipe 27 serving as a discharge path for discharging the condensate accumulated by flowing down the heat transfer pipe 4 is connected to the lower part of the folding chamber 3 a of the header 3 on the outlet side. A condensate pump 11 is provided. A discharge opening 27 between the return chamber 3a of the header 3 on the outlet side and the condensed water pump 27 is provided with a first on-off valve 28 that is opened during a concentration process other than the cleaning described later. The discharge pipe 27 on the discharge side of the condensed water pump 11 is provided with a third on-off valve 37 that is opened when condensed water is drained.

出口側のヘッダー3上部の出口室3bには、蒸発器1内を大気圧以下に減圧するための真空ポンプ10が接続される。   A vacuum pump 10 for reducing the inside of the evaporator 1 to atmospheric pressure or less is connected to the outlet chamber 3b above the header 3 on the outlet side.

液溜部18の被処理液は、循環ポンプ5によって循環管路6を介して、蒸発器1内の上部に設けた散布ノズル7に供給され、この散布ノズル7から各伝熱管4の外表面に向かって散布した後、蒸発器1内の液溜部18に流下するという循環を行うように構成している。循環管路6の途中には、濃縮した被処理液を排出するための排出管路8が接続される。蒸発器1には、原液としての被処理液を供給するための原液供給管路23が接続される。   The liquid to be treated in the liquid reservoir 18 is supplied to the spray nozzle 7 provided in the upper part of the evaporator 1 by the circulation pump 5 through the circulation pipe 6, and the outer surface of each heat transfer tube 4 from the spray nozzle 7. Then, the liquid is circulated to the liquid reservoir 18 in the evaporator 1 after being sprayed. In the middle of the circulation line 6, a discharge line 8 for discharging the concentrated liquid to be processed is connected. The evaporator 1 is connected to a stock solution supply line 23 for supplying a liquid to be treated as a stock solution.

循環ポンプ5、循環管路6及び散布ノズル7によって、液溜部18に貯留される被処理液を、蒸発器1上部の散布ノズル7から伝熱管4の外表面に供給するように循環させる循環手段が構成される。   Circulation by which the liquid to be treated stored in the liquid reservoir 18 is circulated by the circulation pump 5, the circulation pipe 6 and the spray nozzle 7 so as to be supplied from the spray nozzle 7 above the evaporator 1 to the outer surface of the heat transfer pipe 4. Means are configured.

蒸発器1の上部は、蒸気管路19を介してブロワー等の圧縮機9に接続されており、蒸発器1からの蒸気は、圧縮機9によって圧縮され、蒸気管路20を介して入口側のヘッダー2に供給される。蒸気管路20には、後述の洗浄時以外は開放される開閉弁としての仕切り弁26が設けられている。なお、圧縮機9に代えて蒸気エゼクターで圧縮してもよい。   The upper part of the evaporator 1 is connected to a compressor 9 such as a blower via a steam line 19, and the steam from the evaporator 1 is compressed by the compressor 9 and is input to the inlet side via a steam line 20. To the header 2. The steam line 20 is provided with a gate valve 26 as an on-off valve that is opened except during the later-described cleaning. In addition, it may replace with the compressor 9 and may compress with a steam ejector.

この実施形態の蒸発濃縮装置は、上述のように、食品用の液体を濃縮するものであって、サニタリー仕様となっている。すなわち、この実施形態では、蒸発器1は、ステンレス鋼からなると共に、洗浄効果を高めるために、蒸発器1の内面の角部は、Rを取って曲面とし、更に、蒸発器の内面には、バフ研磨を施している。また、主要な管路は、ステンレス製のサニタリー配管で構成されている。   The evaporative concentration apparatus of this embodiment concentrates a liquid for food as described above, and has a sanitary specification. That is, in this embodiment, the evaporator 1 is made of stainless steel, and in order to enhance the cleaning effect, the corners of the inner surface of the evaporator 1 are rounded and curved, and further, Buffing is applied. The main pipeline is composed of sanitary piping made of stainless steel.

次に、後述の洗浄のための構成を除く上記蒸発濃縮装置による被処理液の濃縮処理について説明する。   Next, the concentration process of the liquid to be processed by the above evaporative concentration apparatus excluding the configuration for cleaning described later will be described.

この被処理液の濃縮処理では、蒸発器1内を真空ポンプ10によって減圧すると共に、原液供給管路23から被処理液を蒸発器1内の液溜部18に供給する。更に、蒸気供給管路25を介して高圧蒸気を駆動用の蒸気として入口側のヘッダー2に供給すると共に、循環ポンプ5を駆動して液溜部18内の被処理液を、蒸発器1内の上部の散布ノズル7に供給して各伝熱管4の外表面に散布する。   In the concentration process of the liquid to be processed, the inside of the evaporator 1 is decompressed by the vacuum pump 10 and the liquid to be processed is supplied from the stock solution supply line 23 to the liquid reservoir 18 in the evaporator 1. Further, high-pressure steam is supplied to the header 2 on the inlet side as driving steam through the steam supply line 25, and the circulating pump 5 is driven so that the liquid to be processed in the liquid reservoir 18 is fed into the evaporator 1. Is supplied to the spray nozzle 7 at the top of the heat transfer tube 4 and sprayed on the outer surface of each heat transfer tube 4.

散布された被処理液は、蒸発器1内の下部の液溜部18に流下する一方、各伝熱管4の外表面で加熱されて蒸発し、発生した蒸気は、蒸気管路19から圧縮機9に吸引、圧縮された後、入口側のヘッダー2を介して蒸発器1における各伝熱管4内に導かれて、当該各伝熱管4の外表面に散布される被処理液を加熱するための熱源として利用される。各伝熱管4内で生成して出口側のヘッダー3の折り返し室3aの下部に溜まった凝縮液は、排出管路27を介して凝縮水ポンプ11によって系外へ排出される。液溜部18には、蒸発濃縮による減量分の原液が供給される。   The sprayed liquid to be treated flows down to the lower liquid reservoir 18 in the evaporator 1, and is heated and evaporated on the outer surface of each heat transfer tube 4. The generated steam is sent from the steam line 19 to the compressor. In order to heat the liquid to be treated which is sucked and compressed into 9 and then introduced into each heat transfer tube 4 in the evaporator 1 through the header 2 on the inlet side and sprayed on the outer surface of each heat transfer tube 4. Used as a heat source. Condensate produced in each heat transfer tube 4 and accumulated in the lower portion of the folding chamber 3a of the header 3 on the outlet side is discharged out of the system by the condensed water pump 11 through the discharge pipe 27. The liquid reservoir 18 is supplied with a reduced amount of stock solution by evaporation and concentration.

この実施形態では、食品用の液体、例えば、お茶やコーヒー等の被処理液を、濃縮するので、各部を容易に洗浄できるように、次のように構成している。   In this embodiment, a liquid for food, for example, a liquid to be treated such as tea or coffee is concentrated, so that each part can be easily washed as follows.

先ず、複数の伝熱管4の内部を洗浄できるようにするために、凝縮水ポンプ11の吐出側の排出管路27を分岐して出口側のヘッダー3の出口室3bに接続する分岐経路としての分岐管路29を設けており、凝縮水ポンプ11からの水を、出口室3bに接続された上部の伝熱管4に導入できるようにしている。この分岐管路29には、濃縮処理時には閉止され、伝熱管4内部の洗浄時に開放される第4開閉弁36が設けられている。   First, in order to be able to clean the inside of the plurality of heat transfer tubes 4, the discharge side discharge pipe 27 of the condensed water pump 11 is branched and connected to the outlet chamber 3b of the header 3 on the outlet side. A branch pipe 29 is provided so that water from the condensed water pump 11 can be introduced into the upper heat transfer pipe 4 connected to the outlet chamber 3b. The branch pipe 29 is provided with a fourth on-off valve 36 that is closed during the concentration process and opened during cleaning of the heat transfer pipe 4.

また、凝縮水ポンプ11の吸込み側の排出管路27と入口側のヘッダー2の入口室2aとを接続するバイパス管路30が設けられ、このバイパス管路30には、濃縮処理時には閉止され、伝熱管4の内部の洗浄時に開放される第2開閉弁31が設けられる。   In addition, a bypass line 30 is provided to connect the suction side discharge line 27 of the condensed water pump 11 and the inlet chamber 2a of the header 2 on the inlet side, and this bypass line 30 is closed during the concentration process, A second on-off valve 31 is provided that is opened when the inside of the heat transfer tube 4 is cleaned.

伝熱管4の内部の洗浄時には、濃縮処理時に開放されている第1開閉弁28を閉止する一方、バイパス管路30の第2開閉弁31を開放する。また、凝縮水ポンプ11の吐出側の分岐管路29の第4開閉弁36を開放する。このとき、凝縮水ポンプ11の吐出側の排出管路27の第3開閉弁37は閉止されている。   When cleaning the inside of the heat transfer pipe 4, the first on-off valve 28 opened at the time of the concentration process is closed, while the second on-off valve 31 of the bypass pipe line 30 is opened. Further, the fourth on-off valve 36 of the branch pipe 29 on the discharge side of the condensed water pump 11 is opened. At this time, the third on-off valve 37 of the discharge pipe 27 on the discharge side of the condensed water pump 11 is closed.

更に、圧縮機9から入口側のヘッダー2に蒸気を供給するための蒸気管路20に設けられている仕切り弁26を閉止する。   Furthermore, the gate valve 26 provided in the steam line 20 for supplying steam from the compressor 9 to the header 2 on the inlet side is closed.

これによって、伝熱管4の内部の洗浄時には、凝縮水ポンプ11の吐出側から分岐管路29を介して出口側のヘッダー3の出口室3bに至り、蒸気の供給方向とは逆に、上方の伝熱管4から下方の伝熱管4に至り、入口側のヘッダー2の入口室2aを介して凝縮水ポンプ11の吸込み側に戻るという循環経路が構成される。   Thereby, at the time of cleaning the inside of the heat transfer pipe 4, the discharge side of the condensed water pump 11 reaches the outlet chamber 3 b of the header 3 on the outlet side via the branch pipe 29, and the upper direction is opposite to the steam supply direction. A circulation path is formed from the heat transfer tube 4 to the lower heat transfer tube 4 and returning to the suction side of the condensed water pump 11 through the inlet chamber 2a of the header 2 on the inlet side.

伝熱管4の内部の洗浄時には、先ず、前記循環経路内を洗浄液で満たす。この実施形態では、例えば、出口側のヘッダー3bの出口室3bには、循環経路内に供給される洗浄液の供給量を検出する検出手段として、レベルスイッチが設けられている。このレベルスイッチによって、伝熱管4を含む循環経路が略満水となって所定の液面レベルに達したことが検出されるまで、入口側のヘッダー2の入口室2aへ図示しない洗浄液供給管路を介して洗浄液を供給する。   When cleaning the inside of the heat transfer tube 4, first, the inside of the circulation path is filled with a cleaning liquid. In this embodiment, for example, a level switch is provided in the outlet chamber 3b of the header 3b on the outlet side as detection means for detecting the supply amount of the cleaning liquid supplied into the circulation path. Until this level switch detects that the circulation path including the heat transfer pipe 4 is substantially full and reaches a predetermined liquid level, the cleaning liquid supply pipe (not shown) is connected to the inlet chamber 2a of the header 2 on the inlet side. Supply the cleaning liquid.

このように循環経路を洗浄液で満たした後、凝縮水ポンプ11を駆動し、洗浄液を、伝熱管4を含む前記循環経路で循環させ、これによって、両ヘッダー2,3の内部および伝熱管4の内部を洗浄する。   After filling the circulation path with the cleaning liquid in this way, the condensate pump 11 is driven, and the cleaning liquid is circulated through the circulation path including the heat transfer tubes 4, thereby the inside of the headers 2 and 3 and the heat transfer tubes 4. Clean inside.

なお、入口側のヘッダー2の入口室2aと凝縮水ポンプ11の吸込み側とを接続するバイパス管路30を設けて、洗浄時の循環経路を構成するのは、出口側のヘッダー3の折り返し室3aと凝縮水ポンプ11の吸込み側とを接続する排出管路27を用いて洗浄時の循環経路を構成すると、前記折り返し室3aと前記入口室2aとを接続する下方の伝熱管4内に洗浄液を供給できないからである。   The bypass pipe 30 that connects the inlet chamber 2a of the header 2 on the inlet side and the suction side of the condensate pump 11 to provide a circulation path for cleaning is the folding chamber of the header 3 on the outlet side. When a circulation path for cleaning is configured using the discharge pipe 27 that connects 3a and the suction side of the condensed water pump 11, the cleaning liquid is placed in the lower heat transfer pipe 4 that connects the folding chamber 3a and the inlet chamber 2a. It is because it cannot supply.

以上のような伝熱管4の内部の洗浄は、上述の各開閉弁26,28,31,36等を自動弁で構成し、次のように図示しない制御装置によって自動制御するようにしてもよい。   For cleaning the inside of the heat transfer tube 4 as described above, the above-described on-off valves 26, 28, 31, 36, etc. may be constituted by automatic valves and automatically controlled by a control device (not shown) as follows. .

すなわち、濃縮処理が終了した後、伝熱管4の洗浄時には、制御装置は、凝縮水ポンプ11の吸込み側の第1開閉弁28を閉止する一方、バイパス管路30の第2開閉弁31を開放する。また、制御装置は、凝縮水ポンプ11の吐出側の分岐管路29の第4開閉弁36を開放し、更に、圧縮機9から入口側のヘッダー2に蒸気を供給するための蒸気管路20の仕切り弁26を閉止する。   That is, after the concentration process is completed, when the heat transfer pipe 4 is cleaned, the control device closes the first on-off valve 28 on the suction side of the condensed water pump 11 and opens the second on-off valve 31 of the bypass pipe 30. To do. Further, the control device opens the fourth on-off valve 36 of the branch pipe 29 on the discharge side of the condensed water pump 11, and further supplies the steam from the compressor 9 to the header 2 on the inlet side. The gate valve 26 is closed.

次に、入口側のヘッダー2の入口室2aへ図示しない洗浄液供給管路の開閉弁を開放して洗浄液の供給を開始し、上述のレベルスイッチによって、伝熱管4を含む循環経路が略満水となったことが検出されるまで、洗浄液を供給する。その後、制御装置は、凝縮水ポンプ11の駆動を開始し、両ヘッダー2,3の内部および伝熱管4の内部を一定期間に亘って洗浄する。   Next, an opening / closing valve of a cleaning liquid supply pipe (not shown) is opened to the inlet chamber 2a of the header 2 on the inlet side to start supplying the cleaning liquid. By the above-described level switch, the circulation path including the heat transfer pipe 4 is substantially full. The cleaning solution is supplied until it is detected that this has occurred. Thereafter, the control device starts driving the condensed water pump 11 and cleans the inside of both headers 2 and 3 and the inside of the heat transfer tube 4 over a certain period.

この実施形態では、蒸発器1の内部を洗浄できるようにするために、蒸発器1の内部には、各伝熱管4の両端を支持する管板等を含む各内面を洗浄する複数の第1洗浄ノズル32が設けられると共に、各伝熱管4の外表面を洗浄する複数の第2洗浄ノズル33が設けられている。伝熱管4の外表面を洗浄する第2洗浄ノズル33は、伝熱管4の上方位置に限らず、伝熱管4の側方位置に設けて上下の伝熱管4の間に洗浄液を噴射できるようにしてもよい。   In this embodiment, in order to be able to clean the inside of the evaporator 1, the inside of the evaporator 1 includes a plurality of first surfaces for cleaning each inner surface including tube plates and the like that support both ends of each heat transfer tube 4. A cleaning nozzle 32 is provided, and a plurality of second cleaning nozzles 33 for cleaning the outer surface of each heat transfer tube 4 are provided. The second cleaning nozzle 33 for cleaning the outer surface of the heat transfer tube 4 is not limited to the position above the heat transfer tube 4, and is provided at a side position of the heat transfer tube 4 so that the cleaning liquid can be injected between the upper and lower heat transfer tubes 4. May be.

洗浄時には、噴射器としての各洗浄ノズル32,33に、第1洗浄液供給管路34を介して洗浄ポンプ35から洗浄液が供給され、蒸発器1内の各部に洗浄液を噴射して洗浄する。   At the time of cleaning, the cleaning liquid is supplied from the cleaning pump 35 to the cleaning nozzles 32 and 33 as the injectors via the first cleaning liquid supply pipe 34, and the cleaning liquid is sprayed to the respective parts in the evaporator 1 for cleaning.

洗浄液は、洗浄ポンプ35の吸込み側から分岐された洗浄液供給管路45を介して蒸発器1に供給できるように構成されている。洗浄時には、被処理液に代えて、蒸発器1の液溜部18へ洗浄液を供給し、この洗浄液を循環ポンプ5によって蒸発器1上部の散布ノズル7から伝熱管4の外表面に散布して伝熱管4の外表面を洗浄することができる。   The cleaning liquid can be supplied to the evaporator 1 through a cleaning liquid supply pipe 45 branched from the suction side of the cleaning pump 35. At the time of cleaning, the cleaning liquid is supplied to the liquid reservoir 18 of the evaporator 1 instead of the liquid to be treated, and this cleaning liquid is sprayed from the spray nozzle 7 above the evaporator 1 onto the outer surface of the heat transfer tube 4 by the circulation pump 5. The outer surface of the heat transfer tube 4 can be cleaned.

また、この実施形態では、蒸発器1の上部と圧縮機9とを接続する蒸気管路19内には、該蒸気管路19内に洗浄液を噴射する複数の第3洗浄ノズル36が適宜の間隔で設けられている。圧縮機9と入口側のヘッダー2の入口室2aとの間の蒸気管路20は、上述のように仕切り弁26が設けられており、洗浄時には、この仕切り弁26が閉止される。   Further, in this embodiment, a plurality of third cleaning nozzles 36 for injecting a cleaning liquid into the steam pipe 19 are arranged at appropriate intervals in the steam pipe 19 connecting the upper part of the evaporator 1 and the compressor 9. Is provided. The steam pipe 20 between the compressor 9 and the inlet chamber 2a of the header 2 on the inlet side is provided with the gate valve 26 as described above, and the gate valve 26 is closed during cleaning.

この状態で、噴射器としての各第3洗浄ノズル36には、第2洗浄液供給管路40を介して洗浄ポンプ35から洗浄液が供給され、各第3洗浄ノズル36から蒸気管路19内へ洗浄液が噴射されて洗浄される。このとき、蒸気管路19内の洗浄液は、仕切り弁26までの蒸気管路20内に満たされることになり、圧縮機9の内部にも洗浄液が溜まり、洗浄される。   In this state, the cleaning liquid is supplied from the cleaning pump 35 to the third cleaning nozzles 36 as the injectors via the second cleaning liquid supply pipes 40, and the cleaning liquid is supplied from the third cleaning nozzles 36 into the steam pipes 19. Is sprayed and washed. At this time, the cleaning liquid in the steam line 19 is filled in the steam line 20 up to the gate valve 26, and the cleaning liquid is accumulated in the compressor 9 and cleaned.

上述の各洗浄ノズル32,33,36の個数、噴射角度あるいは配置は、各部を効果的に洗浄できるように適宜選択することができる。   The number, the spray angle, or the arrangement of each of the cleaning nozzles 32, 33, and 36 can be selected as appropriate so that each part can be cleaned effectively.

なお、洗浄液は、洗浄剤や殺菌剤などが含まれる洗浄液であってもよいし、濯ぎのための清水などであってもよい。   The cleaning liquid may be a cleaning liquid containing a cleaning agent or a bactericidal agent, or may be clean water for rinsing.

以上のように、この実施形態の蒸発濃縮装置では、洗浄時には、伝熱管4と凝縮水ポンプ11との間の循環経路で洗浄液を循環させて伝熱管4の内部を洗浄することができる一方、蒸発器1の内面および伝熱管4の外表面に第1,第2洗浄ノズル32,33から洗浄液を噴射して洗浄することができ、更に、蒸発器1の上部から仕切り弁26までの蒸気管路19,20内に第3洗浄ノズル36から洗浄液を噴射して各蒸気管路19,20および圧縮機9内部を洗浄することができる。   As described above, in the evaporative concentration apparatus of this embodiment, at the time of cleaning, the cleaning liquid can be circulated in the circulation path between the heat transfer tube 4 and the condensed water pump 11 to clean the inside of the heat transfer tube 4, Cleaning can be performed by spraying the cleaning liquid from the first and second cleaning nozzles 32, 33 onto the inner surface of the evaporator 1 and the outer surface of the heat transfer tube 4, and further, the steam tube from the upper portion of the evaporator 1 to the gate valve 26. The cleaning liquid can be sprayed from the third cleaning nozzle 36 into the passages 19 and 20 to clean the inside of the steam pipes 19 and 20 and the compressor 9.

このように伝熱管4の内部を含む蒸発濃縮装置の各部を容易に洗浄することが可能となり、衛生上、常に清潔に保つことが要求される食品用の液体の濃縮に好適である。   Thus, each part of the evaporative concentration apparatus including the inside of the heat transfer tube 4 can be easily washed, which is suitable for the concentration of food liquids that are required to be kept clean for hygiene purposes.

食品用の液体の蒸発濃縮処理では、食品用の液体の加熱および蒸発を伴うので、蒸発濃縮装置における滞留時間が長くなると、色、味、香りといった品質に影響があるので、滞留時間を短くすることが求められる。   Evaporation and concentration of food liquids involves heating and evaporation of food liquids, so increasing the residence time in the evaporative concentration device affects the quality such as color, taste, and aroma. Is required.

更に、この実施形態では、循環ポンプ5として、容積式ポンプを用いており、この容積式ポンプは、従来の渦流ポンプに比べて、NPSH(正味吸込みヘッド)が小さいために、蒸発器1内の液溜部18に貯留される被処理液の水位を低く設定することが可能となる、すなわち、保有液量を少なくできるので、蒸発濃縮装置における被処理液の滞留時間を、従来に比べて短くすることができる。   Further, in this embodiment, a positive displacement pump is used as the circulation pump 5, and this positive displacement pump has a smaller NPSH (net suction head) than a conventional vortex pump. The water level of the liquid to be treated stored in the liquid reservoir 18 can be set low, that is, the amount of liquid retained can be reduced, so that the residence time of the liquid to be treated in the evaporative concentration apparatus is shorter than that of the prior art. can do.

しかも、蒸発器1の底部は、下方に向かって水平断面積が小さくなるコーン状、この実施形態では、四角錐状であるので、蒸発器1内の底部に貯留される被処理液の保有液量を更に少なくすることができ、蒸発濃縮処理における被処理液の滞留時間を、一層短くすることができる。   Moreover, the bottom of the evaporator 1 has a cone shape in which the horizontal cross-sectional area decreases downward, and in this embodiment is a quadrangular pyramid, so that the liquid to be treated is stored in the bottom of the evaporator 1. The amount can be further reduced, and the residence time of the liquid to be treated in the evaporation concentration process can be further shortened.

また、この実施形態の蒸発濃縮装置は、被処理液から発生する蒸気を、圧縮機9で圧縮、昇温することによって、伝熱管4で被処理液を加熱、蒸発させるための熱源として利用する、すなわち、被処理液から発生する蒸気の熱を回収して熱源として利用するので、蒸気圧縮式でない濃縮装置に比べてエネルギー効率が高いものとなる。   Moreover, the evaporation concentrator of this embodiment is used as a heat source for heating and evaporating the liquid to be processed by the heat transfer tube 4 by compressing and raising the temperature of the vapor generated from the liquid to be processed by the compressor 9. That is, since the heat of the steam generated from the liquid to be treated is recovered and used as a heat source, the energy efficiency is higher than that of a concentration apparatus that is not a vapor compression type.

上述の実施形態では、洗浄ポンプ35によって洗浄液を各部に供給して洗浄したけれども、本発明の他の実施形態として、図2に示すように洗浄ポンプ35を省略し、循環ポンプ5によって各部に洗浄液を供給するようにしてもよい。   In the above embodiment, the cleaning liquid is supplied to each part by the cleaning pump 35 and cleaning is performed. However, as another embodiment of the present invention, the cleaning pump 35 is omitted as shown in FIG. May be supplied.

図2において、被処理液の原液を供給する原液供給管路23aは、蒸発器1に接続され、この原液供給管路23aは、洗浄液を供給する洗浄液供給管路を兼用し、あるいは、破線で示すように洗浄液供給管路と合流している。   In FIG. 2, a stock solution supply line 23a for supplying a stock solution to be treated is connected to the evaporator 1, and this stock solution supply line 23a also serves as a cleaning solution supply line for supplying a cleaning solution, or is indicated by a broken line. As shown, it merges with the cleaning liquid supply conduit.

また、循環ポンプ5から蒸発器1内の上部に設けた散布ノズル7に至る循環管路6aは、その途中で蒸発器1内部の各洗浄ノズル32,33に洗浄液を供給する第1洗浄液供給管路34aと、蒸発器1から圧縮機9へ至る蒸気管路19内の各洗浄ノズル36に洗浄液を供給する第2洗浄液供給管路40aとに分岐している。各洗浄液供給管路34a,40aには、洗浄時に開放される第5,第6開閉弁42,43が設けられている。その他の構成は、上述の実施形態と同様である。   A circulation pipe 6a from the circulation pump 5 to the spray nozzle 7 provided in the upper part in the evaporator 1 is provided with a first cleaning liquid supply pipe for supplying a cleaning liquid to the cleaning nozzles 32 and 33 in the evaporator 1 in the middle. The passage 34a is branched into a second cleaning liquid supply pipe 40a for supplying a cleaning liquid to each cleaning nozzle 36 in the steam pipe 19 from the evaporator 1 to the compressor 9. The cleaning liquid supply pipes 34a and 40a are provided with fifth and sixth on-off valves 42 and 43 that are opened during cleaning. Other configurations are the same as those of the above-described embodiment.

この実施形態では、蒸発器1等の洗浄時には、第1,第2洗浄液供給管路34a,40aの各開閉弁42,43を開放し、洗浄液の供給を兼ねる原液供給管路23aから洗浄液を供給すると共に、循環ポンプ5を駆動する。これによって、洗浄液は、循環管路6a及び第1洗浄液供給管路34aを介して蒸発器1内部の散布ノズル7及び各洗浄ノズル32,33に供給され、蒸発器1の内部が洗浄される一方、循環管路6a及び第2洗浄液供給管路40aを介して蒸気管路19内の各洗浄ノズル36に供給され、蒸気管路19内および圧縮機9が洗浄される。   In this embodiment, when the evaporator 1 or the like is cleaned, the on-off valves 42 and 43 of the first and second cleaning liquid supply lines 34a and 40a are opened, and the cleaning liquid is supplied from the raw liquid supply line 23a that also serves as the supply of the cleaning liquid. At the same time, the circulation pump 5 is driven. Accordingly, the cleaning liquid is supplied to the spray nozzle 7 and the cleaning nozzles 32 and 33 in the evaporator 1 through the circulation line 6a and the first cleaning liquid supply line 34a, and the inside of the evaporator 1 is cleaned. Then, the gas is supplied to each cleaning nozzle 36 in the steam line 19 through the circulation line 6a and the second cleaning liquid supply line 40a, and the inside of the steam line 19 and the compressor 9 are cleaned.

このように洗浄ポンプ35を設けることなく、循環ポンプ5によって各ノズル7,32,33,36に洗浄液を供給して各部を洗浄することができる。   Thus, without providing the cleaning pump 35, the circulation pump 5 can supply the cleaning liquid to the nozzles 7, 32, 33, and 36 to clean each part.

上述の実施形態では、食品用の液体の濃縮に適用して説明したけれども、本発明は、食品用の液体に限らず、例えば、医薬品や化学薬品用の液体や廃液などの液体の濃縮にも適用できるものである。   In the above-described embodiment, the present invention is applied to the concentration of a liquid for food. However, the present invention is not limited to a liquid for food. Applicable.

1 蒸発器
2,3 ヘッダー
4 伝熱管
5 循環ポンプ
6,6a 循環管路
7 散布ノズル
9 圧縮機
18 液溜部
29 分岐管路
32,33,36 洗浄ノズル(噴射器)
35 洗浄ポンプ
DESCRIPTION OF SYMBOLS 1 Evaporator 2, 3 Header 4 Heat transfer pipe 5 Circulation pump 6, 6a Circulation pipe line 7 Spray nozzle 9 Compressor 18 Liquid storage part 29 Branch pipe lines 32, 33, 36 Cleaning nozzle (injector)
35 Washing pump

Claims (5)

被処理液を大気圧以下の減圧状態で蒸発させる蒸発器を備える蒸発濃縮装置であって、
前記蒸発器内には、被処理液を加熱する複数の伝熱管が配置され、
前記蒸発器の底部に貯留される被処理液を、前記蒸発器の上部に戻して、前記伝熱管の外表面に供給する循環手段と、
蒸気が供給される前記伝熱管内で生成される凝縮水を排出する凝縮水ポンプと
前記伝熱管内に洗浄液を供給する洗浄液供給管路と、
前記凝縮水ポンプの吐出側の排出経路を分岐して前記伝熱管に接続する分岐経路とを備え、
前記凝縮水ポンプから前記凝縮水が吐出されるときには、吐出される前記凝縮水を、前記排出経路を介して排出し、前記凝縮水ポンプから前記洗浄液が吐出されるときには、吐出される前記洗浄液を、前記分岐経路を介して前記伝熱管内に導入することにより、前記洗浄液を、前記凝縮水ポンプと前記伝熱管との間で循環させる、
ことを特徴とする蒸発濃縮装置。
An evaporative concentration apparatus comprising an evaporator for evaporating a liquid to be treated in a reduced pressure state below atmospheric pressure,
In the evaporator, a plurality of heat transfer tubes for heating the liquid to be processed are arranged,
Circulation means for returning the liquid to be treated stored at the bottom of the evaporator to the top of the evaporator and supplying it to the outer surface of the heat transfer tube;
A condensed water pump for discharging condensed water generated in the heat transfer pipe to which steam is supplied ;
A cleaning liquid supply pipe for supplying a cleaning liquid into the heat transfer pipe;
A branch path for branching a discharge path on the discharge side of the condensed water pump and connecting to the heat transfer pipe,
When the condensed water is discharged from the condensed water pump, the discharged condensed water is discharged through the discharge path, and when the cleaning liquid is discharged from the condensed water pump, the discharged cleaning liquid is discharged. The cleaning liquid is circulated between the condensate pump and the heat transfer pipe by introducing it into the heat transfer pipe through the branch path .
An evaporative concentration apparatus characterized by that.
前記蒸発器内には、該蒸発器の内面および前記伝熱管の外表面に洗浄液を噴射する噴射器が設けられる、
請求項1に記載の蒸発濃縮装置。
In the evaporator, an injector for injecting a cleaning liquid onto the inner surface of the evaporator and the outer surface of the heat transfer tube is provided.
The evaporative concentration apparatus according to claim 1.
被処理液を大気圧以下の減圧状態で蒸発させる蒸発器を備える蒸発濃縮装置であって、
前記蒸発器内には、被処理液を加熱する複数の伝熱管が配置され、
前記蒸発器の底部に貯留される被処理液を、前記蒸発器の上部に戻して、前記伝熱管の外表面に供給する循環手段と、
蒸気が供給される前記伝熱管内で生成される凝縮水を排出する凝縮水ポンプと、
前記蒸発器で発生する蒸気を圧縮して前記伝熱管内に供給する圧縮機とを備え、
前記凝縮水ポンプの吐出側の排出経路を分岐して、該凝縮水ポンプから吐出される水を前記伝熱管内に導入する分岐経路を設け、
前記蒸発器から前記圧縮機に至る管路内には、洗浄を前記管路内に噴射する噴射器が設けられ、
前記圧縮機から前記伝熱管に至る管路の途中には、開閉弁が設けられる、
ことを特徴とする蒸発濃縮装置。
An evaporative concentration apparatus comprising an evaporator for evaporating a liquid to be treated in a reduced pressure state below atmospheric pressure,
In the evaporator, a plurality of heat transfer tubes for heating the liquid to be processed are arranged,
Circulation means for returning the liquid to be treated stored at the bottom of the evaporator to the top of the evaporator and supplying it to the outer surface of the heat transfer tube;
A condensed water pump for discharging condensed water generated in the heat transfer pipe to which steam is supplied;
A compressor that compresses the steam generated in the evaporator and supplies the steam into the heat transfer tube,
Branching the discharge path on the discharge side of the condensed water pump, providing a branch path for introducing water discharged from the condensed water pump into the heat transfer pipe,
Wherein the evaporator conduit leading to the compressor from the injector for injecting cleaning liquid into the conduit is provided,
In the middle of the pipeline from the compressor to the heat transfer tube, an on-off valve is provided.
An evaporative concentration apparatus characterized by that .
前記被処理液が、食品用の液体である、
請求項1ないし3のいずれかに記載の蒸発濃縮装置。
The liquid to be treated is a liquid for food.
The evaporative concentration apparatus according to any one of claims 1 to 3.
請求項1に記載の蒸発濃縮装置の洗浄方法であって、
前記凝縮水ポンプの吐出側を、前記排出経路から前記分岐経路に切替え、前記洗浄を、前記凝縮水ポンプと前記伝熱管との間で循環させる、
ことを特徴とする蒸発濃縮装置の洗浄方法。
A method for cleaning an evaporation concentrator according to claim 1,
Wherein the discharge side of the condensate pump, switching from the discharge route to the branch path, the cleaning liquid is circulated between the heat transfer tube and the condensed water pump,
A method for cleaning an evaporative concentration apparatus.
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