JP3510010B2 - Vacuum steam heating device - Google Patents

Vacuum steam heating device

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Publication number
JP3510010B2
JP3510010B2 JP20146095A JP20146095A JP3510010B2 JP 3510010 B2 JP3510010 B2 JP 3510010B2 JP 20146095 A JP20146095 A JP 20146095A JP 20146095 A JP20146095 A JP 20146095A JP 3510010 B2 JP3510010 B2 JP 3510010B2
Authority
JP
Japan
Prior art keywords
steam
vacuum
waste water
vessel
hot waste
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP20146095A
Other languages
Japanese (ja)
Other versions
JPH0926103A (en
Inventor
学 太田垣
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tlv Co Ltd
Original Assignee
Tlv Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tlv Co Ltd filed Critical Tlv Co Ltd
Priority to JP20146095A priority Critical patent/JP3510010B2/en
Publication of JPH0926103A publication Critical patent/JPH0926103A/en
Application granted granted Critical
Publication of JP3510010B2 publication Critical patent/JP3510010B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は被加熱物を100度C以
下程度の低温蒸気で加熱処理する場合に適した真空蒸気
加熱装置に関する。具体的には各種化学反応に用いられ
る反応釜や食品の蒸溜装置、濃縮装置、あるいは、医療
品の殺菌装置等の蒸気加熱に用いるものである。 【0002】 【従来技術】従来の真空蒸気加熱装置としては、例えば
特開平4−48102号公報に示されたものが用いられ
ていた。これは、温排水が流入して再蒸発する蒸発容器
と、蒸発容器の再蒸発蒸気取出口と減圧手段とを真空蒸
気加熱器を介して接続して、温排水の再蒸発により発生
した真空蒸気を加熱器で使用するものであり、従来廃棄
されていた多量の温排水を有効に再利用することができ
るものである。 【0003】 【本発明が解決しようとする課題】上記従来の真空蒸気
加熱装置では、流入してくる温排水の量が少ない場合
に、再蒸発の蒸気量が少なくなり真空蒸気加熱器で充分
な加熱を行えなくなる問題があった。これは、蒸発容器
から直接に温排水を真空ポンプで吸引するために、流入
した温排水が直ちに真空ポンプに吸引されてしまうと共
に、蒸発容器上部の比較的高温の再蒸発し易い温排水が
優先的に吸引されてしまい、再蒸発蒸気量が少なくなっ
てしまうためである。 【0004】従って本発明の技術的課題は、蒸発容器に
流入してくる温排水の量が少ない場合であっても、充分
な量の再蒸発蒸気を発生することのできる真空蒸気加熱
装置を得ることである。 【0005】 【課題を解決する為の手段】本発明の真空蒸気加熱装置
の構成は次の通りである。温排水が流入して再蒸発する
蒸発容器と、該蒸発容器の再蒸発蒸気取出口と減圧手段
とを真空蒸気加熱器を介して接続したものにおいて、蒸
発容器の上下部を連通する連通管を取り付けて、該連通
管上にスチ―ムトラップを配置し、該スチ―ムトラップ
の出口側を減圧手段と接続したものである。 【0006】 【作用】蒸発容器で再蒸発した蒸気は、真空蒸気加熱器
を経て減圧手段に吸引されることにより、加熱器で被加
熱物を蒸気加熱する。真空蒸気加熱器は減圧手段と接続
されているために、真空蒸気加熱器内は大気圧以下の真
空状態となり、100度C以下の低温蒸気で被加熱物を
加熱することができる。被加熱物を加熱したことにより
凝縮した真空蒸気の凝縮水すなわち復水は減圧手段に吸
引され、系外へ排除される。 【0007】スチ―ムトラップとは、液体すなわち温排
水は出口側へ排出するが、気体すなわち再蒸発蒸気は排
出しない自動弁の一種である。蒸発容器の上下部を連通
する連通管を取り付け、この連通管上にスチ―ムトラッ
プを配置したことにより、蒸発容器に流入してきた温排
水はスチ―ムトラップを介して減圧手段に吸引されるこ
とになり、スチ―ムトラップの配置位置を適宜選定する
ことにより蒸発容器内に必要な温排水量を確保すること
ができると共に、スチ―ムトラップを経て減圧手段に吸
引される温排水は蒸発容器の下部から優先的に吸引され
るために、比較的高温の温排水が上部に滞留することと
なって、再蒸発蒸気をより多く発生することができる。 【0008】 【実施例】図示の実施例を詳細に説明する。温排水流入
管5と接続した蒸発容器1と、真空蒸気加熱器2と、蒸
発容器1と真空蒸気加熱器2とを連通する真空蒸気管6
と、真空蒸気管6の下端部を接続した減圧手段3とで真
空蒸気加熱装置を構成する。 【0009】蒸発容器1にバルブ7を介して温排水流入
管5を接続する。蒸発容器1の再蒸発蒸気取出口8に真
空蒸気管6を接続する。蒸発容器1の上部と下部を連通
する連通管9を取り付けて、その上方部に管10を介し
てスチ―ムトラップ11を配置する。スチ―ムトラップ
11の出口側は管12により減圧手段3と接続する。ス
チ―ムトラップ11と並行してバイパスバルブ13を取
り付ける。スチ―ムトラップ11は温排水は出口側に排
出するが、再蒸発蒸気は排出しない自動弁の一種であ
る。 【0010】真空蒸気管6に圧力調整弁15を介して真
空蒸気加熱器2と接続し、その下端部を減圧手段3と接
続する。真空蒸気加熱器2には、被加熱物供給管16と
被加熱物取出管17を接続する。 【0011】減圧手段3は、ノズルを内蔵したエゼクタ
―20とタンク21と循環ポンプ22、及び、これらを
接続する循環路23から成るエゼクタ―式真空ポンプで
構成する。タンク21の下部と循環ポンプ22の吸込み
口側を接続し循環ポンプ22の吐出口側をエゼクタ―2
0と接続する。減圧手段としてのエゼクタ―式真空ポン
プ3はタンク21内の流体すなわち水等を循環ポンプ2
2で循環してエゼクタ―20内のノズル部へ通過させる
ことにより、エゼクタ―20で吸引力を生じるものであ
る。循環ポンプ22の吐出口と接続する循環路23に弁
25を介して余剰水排出通路26を接続する。タンク2
1の上部には冷却水補給管27を冷却水制御弁28を介
して接続する。 【0012】次に作用を説明する。バイパスバルブ13
を開弁すると共に、エゼクタ―式真空ポンプ3を駆動し
てエゼクタ―20で吸引力を発生させ、蒸発容器1内、
及び、真空蒸気管6内を所定の真空状態とする。所定の
真空状態となった時点でバイパスバルブ13は閉弁して
おく。バルブ7を開弁して、温排水流入管5から温排水
を蒸発容器1内へ流下させる。蒸発容器1内の温排水が
再蒸発し、その再蒸発蒸気が真空蒸気管6から圧力調整
弁15を介して真空加熱器2へ供給され、内部の被加熱
物を低温の真空蒸気で加熱する。被加熱物を加熱した蒸
気は凝縮して復水となりにエゼクタ―式真空ポンプ3の
エゼクタ―20へ吸引されタンク21に至る。 【0013】蒸発容器1内に溜った温排水の内、上面部
の温排水は再蒸発するが、下部の温排水は連通管9を通
りスチ―ムトラップ11からエゼクタ―20に吸引され
る。従って、温排水流入管5から流下してくる温排水の
量が少なくて、蒸発容器1内の上下部で温排水の温度差
が生じた場合であっても、スチ―ムトラップ11からは
下部の低温の温排水が優先的に排出され、蒸発容器1内
での再蒸発蒸気量を確保することができる。 【0014】 【発明の効果】本発明によれば、スチ―ムトラップを介
して温排水を吸引手段で吸引すると共に、蒸発容器下部
の比較的低温の温排水を優先的に吸引することにより、
蒸発容器に流入してくる温排水の量が少ない場合であっ
ても、より多くの再蒸発蒸気を確保することができ、真
空蒸気加熱器で充分な加熱を行うことができる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vacuum steam heating apparatus suitable for heating an object to be heated with a low-temperature steam of about 100 ° C. or less. Specifically, it is used for steam heating in a reaction pot used for various chemical reactions, a distilling device for food, a concentrating device, or a sterilizing device for medical products. 2. Description of the Related Art As a conventional vacuum steam heating device, for example, a device disclosed in Japanese Patent Application Laid-Open No. 4-48102 has been used. This is because the evaporating vessel into which the hot waste water flows in and re-evaporates, the re-evaporating steam outlet of the evaporating vessel and the pressure reducing means are connected via a vacuum steam heater, and the vacuum steam generated by the re-evaporation of the hot waste water is connected. Is used in a heater, and a large amount of hot wastewater that has been conventionally discarded can be effectively reused. [0003] In the above-mentioned conventional vacuum steam heating apparatus, when the amount of hot water discharged is small, the amount of steam for re-evaporation is small, and the vacuum steam heater is sufficient. There was a problem that heating could not be performed. This is because the hot drainage is directly sucked into the vacuum pump because the hot drainage is sucked directly from the evaporation container by the vacuum pump, and the relatively high temperature hot drainage at the top of the evaporation container that is easy to re-evaporate has priority. This is due to the fact that it is sucked in tentatively and the amount of re-evaporated steam is reduced. Accordingly, a technical problem of the present invention is to provide a vacuum steam heating device capable of generating a sufficient amount of re-evaporated steam even when the amount of hot waste water flowing into an evaporation vessel is small. That is. [0005] The structure of the vacuum steam heating apparatus of the present invention is as follows. An evaporating vessel into which hot waste water flows in and re-evaporated, and a communication pipe connecting the upper and lower portions of the evaporating vessel with a re-evaporating steam outlet of the evaporating vessel and a pressure reducing means connected via a vacuum steam heater. A steam trap is mounted on the communication pipe, and the outlet side of the steam trap is connected to a pressure reducing means. The vapor re-evaporated in the evaporating vessel is sucked by the pressure reducing means through the vacuum vapor heater, so that the object to be heated is heated by the heater. Since the vacuum steam heater is connected to the pressure reducing means, the inside of the vacuum steam heater is in a vacuum state at atmospheric pressure or lower, and the object to be heated can be heated with low-temperature steam at 100 ° C. or lower. The condensed water of the vacuum vapor condensed by heating the object to be heated, that is, condensed water, is sucked by the decompression means and discharged to the outside of the system. [0007] A steam trap is a type of automatic valve that discharges liquid, that is, hot waste water, to the outlet side, but does not discharge gas, that is, re-evaporated steam. By installing a communication pipe that communicates the upper and lower parts of the evaporation vessel, and arranging a steam trap on this communication pipe, the hot waste water that has flowed into the evaporation vessel is sucked into the pressure reducing means via the steam trap. Therefore, by appropriately selecting the position of the steam trap, it is possible to secure the necessary amount of hot waste water in the evaporating vessel, and the hot waste water sucked into the pressure reducing means via the steam trap is given priority from the bottom of the evaporating vessel. As a result, the relatively high-temperature hot waste water stays in the upper portion, so that more reevaporated steam can be generated. An embodiment shown in the drawings will be described in detail. An evaporating vessel 1 connected to the warm drainage inflow pipe 5, a vacuum steam heater 2, and a vacuum steam pipe 6 for communicating the evaporating vessel 1 with the vacuum steam heater 2.
And the pressure reducing means 3 connected to the lower end of the vacuum steam pipe 6 constitute a vacuum steam heating device. A hot waste water inflow pipe 5 is connected to the evaporating vessel 1 via a valve 7. A vacuum steam pipe 6 is connected to a re-evaporation steam outlet 8 of the evaporation vessel 1. A communication pipe 9 that connects the upper part and the lower part of the evaporating vessel 1 is attached, and a steam trap 11 is disposed above the evaporating vessel 1 via a pipe 10. The outlet side of the steam trap 11 is connected to the pressure reducing means 3 by a pipe 12. A bypass valve 13 is attached in parallel with the steam trap 11. The steam trap 11 is a type of automatic valve that discharges hot waste water to the outlet side but does not discharge reevaporation steam. [0010] The vacuum steam pipe 6 is connected to the vacuum steam heater 2 via a pressure regulating valve 15, and the lower end thereof is connected to the pressure reducing means 3. The heated object supply pipe 16 and the heated object removal pipe 17 are connected to the vacuum steam heater 2. The pressure reducing means 3 comprises an ejector-type vacuum pump comprising an ejector 20 having a built-in nozzle, a tank 21, a circulation pump 22, and a circulation path 23 connecting these. The lower part of the tank 21 is connected to the suction port side of the circulation pump 22 and the discharge port side of the circulation pump 22 is connected to the ejector 2.
Connect to 0. The ejector-type vacuum pump 3 as a pressure reducing means circulates the fluid in the tank 21, that is, water, etc.
The suction force is generated in the ejector 20 by circulating in the nozzle 2 and passing through the nozzle portion in the ejector 20. A surplus water discharge passage 26 is connected via a valve 25 to a circulation passage 23 connected to a discharge port of the circulation pump 22. Tank 2
A cooling water supply pipe 27 is connected to the upper part of the cooling water supply pipe 1 via a cooling water control valve 28. Next, the operation will be described. Bypass valve 13
Is opened, and the ejector-type vacuum pump 3 is driven to generate a suction force by the ejector 20.
Then, the inside of the vacuum steam pipe 6 is brought into a predetermined vacuum state. When a predetermined vacuum state is reached, the bypass valve 13 is closed. The valve 7 is opened, and the hot waste water flows down from the hot waste water inflow pipe 5 into the evaporation vessel 1. The hot wastewater in the evaporation vessel 1 is re-evaporated, and the re-evaporated steam is supplied from the vacuum steam pipe 6 to the vacuum heater 2 via the pressure regulating valve 15 to heat the object to be heated with low-temperature vacuum steam. . The steam that has heated the object to be heated is condensed and condensed to be condensed, and is sucked by the ejector 20 of the ejector type vacuum pump 3 to reach the tank 21. [0013] Of the hot waste water stored in the evaporating vessel 1, the hot waste water on the upper surface is re-evaporated, but the hot waste water on the lower part is sucked from the steam trap 11 to the ejector 20 through the communication pipe 9. Therefore, even if the amount of hot waste water flowing down from the hot waste water inflow pipe 5 is small and a difference in temperature of the hot waste water occurs between the upper and lower portions in the evaporating vessel 1, the lower portion of the steam trap 11 can be used. Low-temperature hot wastewater is preferentially discharged, and the amount of re-evaporated steam in the evaporation container 1 can be secured. According to the present invention, the hot waste water is sucked by the suction means through the steam trap, and the relatively low-temperature hot waste water at the lower part of the evaporator is preferentially sucked.
Even when the amount of hot wastewater flowing into the evaporation container is small, more re-evaporated steam can be secured, and sufficient heating can be performed by the vacuum steam heater.

【図面の簡単な説明】 【図1】本発明の真空蒸気加熱装置の実施例を示す構成
図である。 【符号の説明】 1 蒸発容器 2 真空蒸気加熱器 3 減圧手段 5 温排水流入管 6 真空蒸気管 8 再蒸発蒸気取出口 9 連通管 11 スチ―ムトラップ 20 エゼクタ― 21 タンク 22 循環ポンプ
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a configuration diagram showing an embodiment of a vacuum steam heating device of the present invention. [Description of Signs] 1 Evaporation vessel 2 Vacuum steam heater 3 Decompression means 5 Hot drainage inlet pipe 6 Vacuum steam pipe 8 Re-evaporation steam outlet 9 Communication pipe 11 Steam trap 20 Ejector 21 Tank 22 Circulation pump

Claims (1)

(57)【特許請求の範囲】 【請求項1】 温排水が流入して再蒸発する蒸発容器
と、該蒸発容器の再蒸発蒸気取出口と減圧手段とを真空
蒸気加熱器を介して接続したものにおいて、蒸発容器の
上下部を連通する連通管を取り付けて、該連通管上にス
チ―ムトラップを配置し、該スチ―ムトラップの出口側
を減圧手段と接続したことを特徴とする真空蒸気加熱装
置。
(57) [Claims 1] An evaporating vessel into which hot waste water flows and re-evaporates, and a re-evaporating steam outlet of the evaporating vessel and a pressure reducing means are connected via a vacuum steam heater. Vacuum steam heating, characterized in that a communication pipe connecting the upper and lower portions of the evaporation vessel is attached, a steam trap is arranged on the communication pipe, and an outlet side of the steam trap is connected to a pressure reducing means. apparatus.
JP20146095A 1995-07-14 1995-07-14 Vacuum steam heating device Expired - Fee Related JP3510010B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20146095A JP3510010B2 (en) 1995-07-14 1995-07-14 Vacuum steam heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20146095A JP3510010B2 (en) 1995-07-14 1995-07-14 Vacuum steam heating device

Publications (2)

Publication Number Publication Date
JPH0926103A JPH0926103A (en) 1997-01-28
JP3510010B2 true JP3510010B2 (en) 2004-03-22

Family

ID=16441464

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20146095A Expired - Fee Related JP3510010B2 (en) 1995-07-14 1995-07-14 Vacuum steam heating device

Country Status (1)

Country Link
JP (1) JP3510010B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007017036A (en) * 2005-07-06 2007-01-25 Miura Co Ltd System for effectively using energy
JP2007247970A (en) * 2006-03-16 2007-09-27 Tlv Co Ltd Wastewater treatment equipment
JP5306750B2 (en) * 2008-09-12 2013-10-02 株式会社テイエルブイ Vapor compression refrigerator
JP5306751B2 (en) * 2008-09-12 2013-10-02 株式会社テイエルブイ Vapor compression refrigerator

Also Published As

Publication number Publication date
JPH0926103A (en) 1997-01-28

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