JP2916699B2 - Vacuum steam generator - Google Patents

Vacuum steam generator

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Publication number
JP2916699B2
JP2916699B2 JP2157834A JP15783490A JP2916699B2 JP 2916699 B2 JP2916699 B2 JP 2916699B2 JP 2157834 A JP2157834 A JP 2157834A JP 15783490 A JP15783490 A JP 15783490A JP 2916699 B2 JP2916699 B2 JP 2916699B2
Authority
JP
Japan
Prior art keywords
vacuum
steam
vacuum steam
vessel
evaporation
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
JP2157834A
Other languages
Japanese (ja)
Other versions
JPH0448102A (en
Inventor
良康 藤原
雅克 岡本
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 JP2157834A priority Critical patent/JP2916699B2/en
Publication of JPH0448102A publication Critical patent/JPH0448102A/en
Application granted granted Critical
Publication of JP2916699B2 publication Critical patent/JP2916699B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は被加熱物を100℃以下程度の比較的低温度で
処理するための真空蒸気発生装置に関する。
Description: TECHNICAL FIELD The present invention relates to a vacuum steam generator for processing an object to be heated at a relatively low temperature of about 100 ° C. or less.

化学や食品あるいは紙パルプや繊維工場等において
は、加熱対象物によって100℃以下の比較的低温で処理
しなければならない場合が多々ある。またこれら工場に
おいては100℃以下程度の温排水が多量に発生するため
に、この温排水の一部を利用して上記処理を行なってい
た。
In chemicals, foods, paper pulp, textile factories, and the like, it is often necessary to treat at a relatively low temperature of 100 ° C. or less depending on an object to be heated. In addition, since a large amount of hot wastewater of about 100 ° C. or less is generated in these factories, the above treatment is performed using a part of the hot wastewater.

しかしながら温水加熱は、温水の保有する顕熱のみを
利用するためにその熱容量は小さく、また境膜伝熱係数
も小さいために加熱効率が低く、生産効率を高めること
ができなかった。
However, hot water heating uses only sensible heat possessed by hot water, so its heat capacity is small, and its heat transfer coefficient is also small, so its heating efficiency is low and its production efficiency cannot be increased.

従来技術 従来は、実開昭63−80401号公報に示されているよう
な技術が用いられていた。これは、蒸発容器に温水流入
管と出口復水排出管を接続し、出口腹水排出管にスチー
ムトラップと真空ポンプを接続し、蒸発容器内を所望の
真空度に制御する真空度制御弁を設けて、大気圧以下の
所望の真空蒸気を発生し、蒸発容器の上部に配した熱交
換器へ真空蒸気を自然循環により供給することにより、
100℃以下の比較的低温で蒸気加熱するものである。
2. Description of the Related Art Conventionally, a technique as disclosed in Japanese Utility Model Application Laid-Open No. 63-80401 has been used. In this method, a hot water inflow pipe and an outlet condensate discharge pipe are connected to the evaporation vessel, a steam trap and a vacuum pump are connected to the outlet ascites discharge pipe, and a vacuum control valve is provided to control the inside of the evaporation vessel to a desired degree of vacuum. Thus, by generating a desired vacuum steam below the atmospheric pressure and supplying the vacuum steam to a heat exchanger disposed at the top of the evaporation vessel by natural circulation,
Steam heating at a relatively low temperature of 100 ° C or less.

蒸気の保有する熱容量は温水に比較して大きいため
に、加熱効率を高めて生産効率を向上することができ
る。
Since the heat capacity of the steam is larger than that of the hot water, the heating efficiency can be increased and the production efficiency can be improved.

本発明が解決しようとする課題 しかし、上記従来技術においては、熱交換器の負荷が
小さなものに限られてしまい、工場における実際の使用
箇所も限定されたものとなってしまう問題があった。こ
れは、熱交換器を蒸発容器の上部に配して、発生せしめ
た真空蒸気を自然循環によって熱交換器に供給するため
である。
Problems to be Solved by the Present Invention However, in the above-mentioned prior art, there is a problem that the load on the heat exchanger is limited to a small one, and the actual use place in the factory is also limited. This is because the heat exchanger is arranged at the upper part of the evaporating vessel, and the generated vacuum steam is supplied to the heat exchanger by natural circulation.

上記工場において多量に発生する100℃以下程度の温
排水の大部分は回収効率が低いために回収されることな
く棄てられており、ごく一部が上記のように温水加熱に
用いられたり、真空蒸気加熱に用いられているのみであ
る。
Most of the hot wastewater of about 100 ° C or less generated in the above factories is discarded without being collected due to low recovery efficiency, and only a small part is used for hot water heating as described above or vacuum It is only used for steam heating.

従って本発明の技術的課題は、多量に棄てられていた
温排水を再利用すると共に熱交換器の負荷が大きなもの
でも使用することのできる真空蒸気発生装置を得ること
である。
SUMMARY OF THE INVENTION Accordingly, it is an object of the present invention to provide a vacuum steam generator capable of reusing a large amount of discarded hot waste water and using a heat exchanger having a large load.

課題を解決する為の手段 上記の課題を解決するために講じた本発明の技術手段
は、温排水の流入する蒸発容器と、該蒸発容器を所望の
真空度に維持する減圧手段を接続し、上記蒸発容器で温
排水の再蒸発により発生した真空蒸気を利用するものに
おいて、蒸発容器の真空蒸気取出口と減圧手段を真空蒸
気使用装置を介して配置したものである。
Means for solving the problem The technical means of the present invention taken in order to solve the above-mentioned problems, an evaporation vessel into which warm wastewater flows, and a decompression means for maintaining the evaporation vessel at a desired degree of vacuum are connected, In the above-mentioned evaporating container utilizing vacuum steam generated by re-evaporation of hot waste water, a vacuum steam outlet and a pressure reducing means of the evaporating container are arranged via a vacuum steam using device.

また、蒸発容器と別途設けた減圧手段とを管を介して
接続したり、あるいは、蒸発容器と真空蒸気使用装置の
間に更に減圧手段を配置するものである。
In addition, the evaporating vessel is connected to a separately provided depressurizing means via a pipe, or a depressurizing means is further arranged between the evaporating vessel and the apparatus using vacuum steam.

作用 真空蒸気使用装置を介して蒸発容器の真空蒸気取出口
と減圧手段を配したことにより、蒸発容器内で発生した
真空蒸気は真空蒸気使用装置を経て減圧手段に強制的に
吸引され循環する。
Function By arranging the vacuum steam outlet of the evaporating vessel and the pressure reducing means via the vacuum steam using apparatus, the vacuum steam generated in the evaporation vessel is forcibly sucked and circulated to the pressure reducing means via the vacuum steam using apparatus.

発明の効果 真空蒸気を蒸気使用装置へ強制的に循環することによ
り、負荷の大きな蒸気使用装置でも多量の真空蒸気を供
給するとができ、従来は棄てていた多量の温排水を有効
に再利用することができる。
Effect of the Invention By forcibly circulating vacuum steam to the steam-using device, a large amount of vacuum steam can be supplied even to a steam-using device having a large load, and a large amount of warm wastewater that has been conventionally discarded can be effectively reused. be able to.

実施例 上記の技術的手段の具体例を示す実施例を説明する。
(第1図乃至第4図参照) 第1実施例(第1図参照) 蒸発容器1と真空蒸気使用装置2と減圧手段としての
真空ポンプ30で真空蒸気発生装置を構成する。蒸発容器
1に温排水導入管3を接続すると共に、上部の真空蒸気
取出口4と真空蒸気使用装置2を接続する。真空蒸気使
用装置2は内部を真空蒸気がコイル状に通過して被加熱
物(図示せず)を加熱処理する。被加熱物は被加熱物入
口5から流入し、被加熱物出口6から排出される。真空
蒸気使用装置2の出口側は復水排出管7で真空ポンプ30
のエゼクタ8と接続する。真空ポンプ30はエゼクタ8と
給水タンク9と循環ポンプ10、及びこれらを接続する循
環路11より成る。エゼクタ8内にノズル12を設けて循環
路11と接続すると共にディフューザ13と給水タンク9を
接続する。給水タンク9には、冷却水を供給するための
冷却水供給管14をコントロール弁15を介して接続すると
共に、タンク9内の水位を検出するための水位センサー
16,17、及び水温を検出するための水温センサー18を取
り付ける。給水タンク9の下部と循環ポンプ10を循環路
11で接続する。循環ポンプ10とノズル12の間に水位セン
サー16,17からの信号により開閉する弁19を設けた排水
路20を分岐する。
Embodiment An embodiment showing a specific example of the above technical means will be described.
(See FIGS. 1 to 4) First Embodiment (See FIG. 1) A vacuum steam generator is constituted by an evaporating vessel 1, a vacuum steam using device 2, and a vacuum pump 30 as a pressure reducing means. The hot water drainage pipe 3 is connected to the evaporating vessel 1, and the upper vacuum steam outlet 4 is connected to the vacuum steamer 2. The vacuum steam application device 2 heats an object to be heated (not shown) by passing the vacuum steam inside in a coil shape. The heated object flows into the heated object inlet 5 and is discharged from the heated object outlet 6. The outlet side of the apparatus 2 using the vacuum steam is a condensate discharge pipe 7 and a vacuum pump 30.
Connected to the ejector 8 of the. The vacuum pump 30 includes the ejector 8, the water supply tank 9, the circulation pump 10, and the circulation path 11 connecting these. A nozzle 12 is provided in the ejector 8 to connect to the circulation path 11 and connect the diffuser 13 to the water supply tank 9. A cooling water supply pipe 14 for supplying cooling water is connected to the water supply tank 9 through a control valve 15, and a water level sensor for detecting a water level in the tank 9 is provided.
16, 17 and a water temperature sensor 18 for detecting the water temperature are attached. The lower part of the water supply tank 9 and the circulation pump 10
Connect with 11. A drainage path 20 provided between the circulation pump 10 and the nozzle 12 and provided with a valve 19 that opens and closes based on signals from water level sensors 16 and 17 is branched.

真空ポンプ30のエゼクタ8に、蒸発容器1内と連通し
た連通管23の一端を接続する。連通管23は蒸発容器1内
の温排水の液位を所定値に維持すると共に、蒸発容器1
内を真空ポンプ30で生じる真空度に維持する。
One end of a communication pipe 23 communicating with the inside of the evaporation container 1 is connected to the ejector 8 of the vacuum pump 30. The communication pipe 23 maintains the liquid level of the hot waste water in the evaporation container 1 at a predetermined value, and
The inside is maintained at a degree of vacuum generated by the vacuum pump 30.

参照番号31は水位センサー16,17や水温センサー18か
らの信号に基づいてそれぞれの弁に開閉指令を発するコ
ントロール部である。
Reference numeral 31 denotes a control unit that issues an open / close command to each valve based on signals from the water level sensors 16, 17 and the water temperature sensor 18.

作用は以下の通りである。 The operation is as follows.

温排水導入管3から流入してきた温排水は蒸発容器1
内に溜まる。蒸発容器1は連通管23で真空ポンプ30と接
続されているために真空ポンプ30で発生する真空度に維
持される。従って蒸発容器1内の温排水は100℃以下の
比較的低温で再蒸発する。真空ポンプ30で発生する真空
度は、ノズル12を通過する流体の温度における飽和圧力
となるために、流体温度を冷却水供給管14に設けたコン
トロール弁15で制御することにより適宜設定できる。
The hot waste water flowing from the hot waste water introduction pipe 3
Accumulate inside. Since the evaporating vessel 1 is connected to the vacuum pump 30 through the communication pipe 23, the degree of vacuum generated by the vacuum pump 30 is maintained. Therefore, the warm waste water in the evaporation container 1 re-evaporates at a relatively low temperature of 100 ° C. or less. The degree of vacuum generated by the vacuum pump 30 becomes a saturation pressure at the temperature of the fluid passing through the nozzle 12, and can be appropriately set by controlling the fluid temperature with a control valve 15 provided in the cooling water supply pipe 14.

蒸発容器1内で発生した真空蒸気は、真空蒸気取出口
4を経て蒸気使用装置2へ至り被加熱物を加熱する。加
熱により再度復水化した復水は復水排出管7を通ってエ
ゼクタ8へ吸引される。従って、従来棄てられることの
多かった温排水から発生した真空蒸気は強制的に循環さ
れ、負荷の大きな蒸気使用装置であっても充分に加熱処
理することができる。
Vacuum steam generated in the evaporation container 1 reaches the steam use device 2 through the vacuum steam outlet 4 to heat the object to be heated. The condensate condensed again by heating is sucked into the ejector 8 through the condensate discharge pipe 7. Therefore, the vacuum steam generated from the warm wastewater which has been frequently discarded is forcibly circulated, so that even a heavy-load steam-using device can be sufficiently heated.

吸引された復水は給水タンク9、循環ポンプ10を循環
すると共に、余剰水は排水路20より系外に排除される。
The sucked condensed water circulates through the water supply tank 9 and the circulation pump 10, and excess water is discharged out of the system through the drainage channel 20.

第2実施例(第2図参照) 本実施例は第1実施例に圧力調整弁25と別途設けた真
空ポンプ26を追加したものであり、同一部材には同一符
号を付し、真空蒸気発生装置としての詳細な説明は省略
する。
Second Embodiment (see FIG. 2) This embodiment is obtained by adding a vacuum pump 26 provided separately from the pressure regulating valve 25 to the first embodiment. A detailed description of the device will be omitted.

真空蒸気取出口4と真空蒸気使用装置2の間に圧力調
整弁25を設ける。圧力調整弁25は、真空蒸気使用装置2
への供給圧力を所定値に維持することにより被加熱物の
加熱温度をさらに精度良く一定に維持する。また本実施
例においては、蒸発容器1内を所望の真空度に維持する
ために真空ポンプ30とは別の真空ポンプ26を設けたこと
により、真空ポンプ30の運転能力は小さなものですみラ
ンニングコストの低減を計ることができる。
A pressure regulating valve 25 is provided between the vacuum steam outlet 4 and the vacuum steam using device 2. The pressure regulating valve 25 is a device using vacuum steam 2
By maintaining the supply pressure to the heater at a predetermined value, the heating temperature of the object to be heated is maintained more accurately and constantly. Further, in this embodiment, since the vacuum pump 30 is provided separately from the vacuum pump 30 in order to maintain the inside of the evaporating vessel 1 at a desired degree of vacuum, the operating capacity of the vacuum pump 30 is small and the running cost is low. Can be reduced.

第3実施例(第3図参照) 本実施例は第2実施例に補助蒸気供給管27と更なる減
圧手段としての蒸気エゼクタ28を追加したものであり、
上記実施例と同一の部材には同一の符号を付し、詳細な
説明は省略する。
Third Embodiment (see FIG. 3) This embodiment is obtained by adding an auxiliary steam supply pipe 27 and a steam ejector 28 as a further pressure reducing means to the second embodiment.
The same members as those in the above embodiment are denoted by the same reference numerals, and detailed description will be omitted.

補助蒸気供給管27から供給される補助蒸気により、蒸
発容器1内で発生した真空蒸気は蒸気エゼクタ28に吸引
され、混合される。混合された蒸気は圧力調整弁25を経
て真空蒸気使用装置2に供給され被加熱物を加熱処理す
る。補助蒸気を供給することにより、さらに加熱能力を
高めることができる。
By the auxiliary steam supplied from the auxiliary steam supply pipe 27, the vacuum steam generated in the evaporation container 1 is sucked by the steam ejector 28 and mixed. The mixed steam is supplied to the vacuum steam using device 2 via the pressure regulating valve 25, and heats the object to be heated. By supplying the auxiliary steam, the heating capacity can be further increased.

第4実施例(第4図参照) 本実施例は補助蒸気供給管27に圧力コントロール弁34
を設けると共に、更なる減圧手段としての蒸気エゼクタ
28と真空蒸気使用装置2の間に圧力センサー29を設け圧
力コントローラ35を介して圧力コントロール弁34を操作
して供給蒸気圧力を制御することにより、さらに精度良
く被加熱物の加熱温度を制御するようにしたものであ
る。
Fourth Embodiment (See FIG. 4) In this embodiment, a pressure control valve 34 is connected to the auxiliary steam supply pipe 27.
And a steam ejector as a further decompression means
A pressure sensor 29 is provided between the apparatus 28 and the apparatus 2 using vacuum steam, and the pressure control valve 34 is operated via a pressure controller 35 to control the supply steam pressure, thereby controlling the heating temperature of the object to be heated with higher accuracy. It is like that.

【図面の簡単な説明】[Brief description of the drawings]

第1図は本発明の真空蒸気発生装置の実施例を示す系統
図、第2図、第3図、第4図は他の実施例を示す系統図
である。 1:蒸発容器、2:真空蒸気使用装置 3:温水導入管、4:真空蒸気取出口 8:エゼクタ、12:ノズル 14:冷却水供給管、23:連通管 25:圧力調整弁、27:補助蒸気供給管 28:蒸気エゼクタ、29:圧力センサー 26,30:真空ポンプ、31:コントロール部 34:圧力コントロール弁
FIG. 1 is a system diagram showing an embodiment of a vacuum steam generator according to the present invention, and FIGS. 2, 3, and 4 are system diagrams showing another embodiment. 1: Evaporation vessel, 2: Vacuum steam device 3: Hot water inlet pipe, 4: Vacuum steam outlet 8: Ejector, 12: Nozzle 14: Cooling water supply pipe, 23: Communication pipe 25: Pressure regulating valve, 27: Auxiliary Steam supply pipe 28: Steam ejector, 29: Pressure sensor 26, 30: Vacuum pump, 31: Control unit 34: Pressure control valve

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】温排水の流入する蒸発容器と、該蒸発容器
を所望の真空度に維持する減圧手段を接続し、上記蒸発
容器で温排水の再蒸発により発生した真空蒸気を利用す
るものにおいて、蒸発容器の真空蒸気取出口と減圧手段
を真空蒸気使用装置を介して配置したことを特徴とする
真空蒸気発生装置。
An evaporating vessel into which hot waste water flows, and a pressure reducing means for maintaining the evaporating vessel at a desired degree of vacuum are connected, and a vacuum steam generated by re-evaporation of the hot waste water in the evaporating vessel is used. A vacuum steam generator, wherein a vacuum steam outlet and a pressure reducing means of an evaporation container are arranged via a vacuum steam using device.
【請求項2】蒸発容器内部と別途設けた減圧手段とを管
を介して接続した特許請求の範囲第1項記載の真空蒸気
発生装置。
2. The vacuum steam generator according to claim 1, wherein the inside of the evaporation vessel and a separately provided pressure reducing means are connected via a pipe.
【請求項3】蒸発容器と真空蒸気使用装置の間に更に減
圧手段を配置した特許請求の範囲第1項記載の真空蒸気
発生装置。
3. The vacuum steam generator according to claim 1, further comprising a pressure reducing means disposed between the evaporating vessel and the apparatus using the vacuum steam.
【請求項4】蒸発容器内部と別途設けた減圧手段とを管
を介して接続すると共に、蒸発容器と真空蒸気使用装置
の間に更に減圧手段を配置した特許請求の範囲第1項記
載の真空蒸気発生装置。
4. The vacuum system according to claim 1, wherein the inside of the evaporation vessel is connected to a separately provided decompression means via a pipe, and the decompression means is further disposed between the evaporation vessel and the apparatus using the vacuum steam. Steam generator.
JP2157834A 1990-06-15 1990-06-15 Vacuum steam generator Expired - Fee Related JP2916699B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2157834A JP2916699B2 (en) 1990-06-15 1990-06-15 Vacuum steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2157834A JP2916699B2 (en) 1990-06-15 1990-06-15 Vacuum steam generator

Publications (2)

Publication Number Publication Date
JPH0448102A JPH0448102A (en) 1992-02-18
JP2916699B2 true JP2916699B2 (en) 1999-07-05

Family

ID=15658354

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2157834A Expired - Fee Related JP2916699B2 (en) 1990-06-15 1990-06-15 Vacuum steam generator

Country Status (1)

Country Link
JP (1) JP2916699B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5312884B2 (en) * 2008-09-12 2013-10-09 株式会社テイエルブイ Vapor compression refrigerator
KR100898380B1 (en) * 2008-11-13 2009-05-18 영일펌프테크(주) Apparatus for recovering vent steam and drain

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS602111B2 (en) * 1980-12-26 1985-01-19 アルプス電気株式会社 Aerosol spray device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS602111U (en) * 1983-06-16 1985-01-09 三菱重工業株式会社 Steam generator blow-water heat recovery device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS602111B2 (en) * 1980-12-26 1985-01-19 アルプス電気株式会社 Aerosol spray device

Also Published As

Publication number Publication date
JPH0448102A (en) 1992-02-18

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