JPH0448102A - Vacuum steam generator - Google Patents

Vacuum steam generator

Info

Publication number
JPH0448102A
JPH0448102A JP15783490A JP15783490A JPH0448102A JP H0448102 A JPH0448102 A JP H0448102A JP 15783490 A JP15783490 A JP 15783490A JP 15783490 A JP15783490 A JP 15783490A JP H0448102 A JPH0448102 A JP H0448102A
Authority
JP
Japan
Prior art keywords
steam
vacuum
vacuum steam
unit
vessel
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.)
Granted
Application number
JP15783490A
Other languages
Japanese (ja)
Other versions
JP2916699B2 (en
Inventor
Yoshiyasu Fujiwara
良康 藤原
Masakatsu Okamoto
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)

Abstract

PURPOSE:To use even if load of a heat exchanger is large and to effectively reuse a large quantity of hot drain water by arranging the vacuum steam outlet of a steam vessel and pressure reducing means through a vacuum steam using unit, and forcibly circulating vacuum steam to the using unit. CONSTITUTION:A vacuum steam generator is composed of a steam vessel 1, a vacuum steam using unit 2 and a vacuum pump 30 as pressure reducing means. Hot drain water fed from a hot drain water inlet tube 3 is stored in the vessel 1, and vacuum steam generated in the vessel 1 is fed to the unit 2 through a vacuum steam outlet 4 to heat a matter to be heated. Condensed water again condensed by heating is sucked to an ejector 8 through a condensed water drain tube 7. Accordingly, the steam is forcibly circulated, and sufficiently heat treated even in the unit 2 having large load to enhance effective utility of the heat.

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。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a vacuum steam generator for treating objects 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。
In chemical, food, paper, pulp and textile factories, etc.
Depending on the object to be heated, it is often necessary to process the object at a relatively low temperature of 100° C. or lower.

またこれら工場においては100’C以下程度の温排水
か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 addition, since these factories generate a large amount of heated waste water of about 100'C or less, a portion of this heated waste water is used for the above-mentioned treatment.

しかしながら温水加熱は、温水の保有する顕然のみを利
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か低く、生産効率を高めることが
できなかった。
However, since hot water heating utilizes only the heat contained in hot water, its heat capacity is small, and the film heat transfer coefficient is also small, resulting in low heating efficiency and has not been able to increase production efficiency.

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、出口復水排出管にス
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。
Prior Art Conventionally, a technique as disclosed in Japanese Utility Model Application Laid-Open No. 63-80401 has been used. This connects a hot water inflow pipe and an outlet condensate discharge pipe to the evaporation vessel, connects a steam trap and a vacuum pump to the outlet condensate discharge pipe, and installs a vacuum level control valve that controls the inside of the evaporation vessel to the desired degree of vacuum. The system generates the desired vacuum steam at a pressure below atmospheric pressure, and supplies the vacuum steam through natural circulation to a heat exchanger placed at the top of the evaporation vessel, thereby heating the steam at a relatively low temperature of 100°C or less. be.

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 steam is larger than that of hot water,
Production efficiency can be improved by increasing heating efficiency.

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
ざ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、発生ぜしめた
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 conventional technology, there was a problem in that the load on the heat exchanger was limited to small items, and the actual locations in the factory where it was used were also limited. . This is because the heat exchanger is disposed above the evaporation vessel and the generated vacuum steam is supplied to the heat exchanger through 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
く棄てられてあり、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 heated waste water below 100℃ generated in large quantities in the above factories is discarded without being recovered due to low recovery efficiency, and only a small portion is used for hot water heating as mentioned above or 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。
Therefore, the technical problem of the present invention is to obtain a vacuum steam generator that can reuse a large amount of discarded heated waste water and can be used even if the load on the heat exchanger is large.

課題を解決する為の手段 上記課題を解決する為に講じた本発明の技術的手段は、
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と、上記蒸発装置で温排水の再蒸
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
を介して配したものである。
Means for solving the problems The technical means of the present invention taken to solve the above problems are as follows:
An evaporation vessel into which heated wastewater flows, a decompression means for maintaining the evaporation vessel at a desired degree of vacuum, and a vacuum steam intake of the evaporation vessel in the evaporator that utilizes the vacuum steam generated by re-evaporation of the heated wastewater. The outlet and pressure reduction means are arranged via a vacuum steam using device.

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。
By arranging the vacuum vapor outlet of the evaporation container and the depressurizing means through the vacuum steam using device, the vacuum vapor generated in the evaporating container is forcibly sucked into the depressurizing means via the vacuum steam using device and circulated.

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
することができ、従来は棄てていた多量の温排水を有効
に再利用することかできる。
Effects of the invention By forcibly circulating vacuum steam to steam-using equipment, a large amount of vacuum steam can be supplied even to steam-using equipment with a large load, and a large amount of heated wastewater that was conventionally discarded can be effectively reused. I can do something.

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は内部を真空蒸気か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人
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3
0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イフユーザ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 illustrating a specific example of the above technical means will be described. (
(See FIGS. 1 to 4) First Embodiment (See FIG. 1) A vacuum steam generation device is constituted by an evaporation container 1, a vacuum steam usage device 2, and a vacuum pump 30 as a pressure reducing means. A heated waste water introduction pipe 3 is connected to the evaporation container 1, and a vacuum steam outlet 4 in the upper part is connected to the vacuum steam usage device 2. The vacuum steam using device 2 heats an object to be heated (not shown) by passing vacuum steam in a coil shape inside the device. The object to be heated flows in from the object to be heated 5 and is discharged from the outlet 6 for the object to be heated. The outlet side of the vacuum steam usage device 2 is a condensate discharge pipe 7 connected to a vacuum pump 3.
0 ejector 8. The vacuum pump 30 includes an ejector 8, a water tank 9, a circulation pump 10, and a circulation path 11 connecting these. A nozzle 12 is provided in the ejector 8 and connected to the circulation path 11, and also connects the diffuser 13 and the water tank 9. A cooling water supply pipe 14 for supplying cooling water is connected to a control valve 15 in the water supply tank 9.
At the same time, water level sensors 16 and 17 for detecting the water level in the tank 9 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 are connected by a circulation path 11. A drainage channel 20 is branched between the circulation pump 10 and the nozzle 12 and is provided with a valve 19 that opens and closes according to signals from water level sensors 16 and 17.

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 heated wastewater inside the evaporation container 1 at a predetermined value, and also maintains the inside of the evaporation container 1 at the 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 is a control unit that issues opening/closing commands to the respective valves 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 action 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て発生する真空度
に維持される。従って蒸発容器1内の温排水は100’
C以下の比較的低温で再蒸発する。真空ポンプ30て発
生する真空度は、ノズル12を通過する流体の温度にあ
ける飽和圧力となるために、流体温度を冷却水供給管1
4に設けたコントロール弁15で制wJスることにより
適宜設定できる。
The heated waste water flowing in from the heated waste water introduction pipe 3 is collected in the evaporation container 1. Since the evaporation container 1 is connected to a vacuum pump 30 through a communication pipe 23, the degree of vacuum generated by the vacuum pump 30 is maintained. Therefore, the heated waste water in the evaporation container 1 is 100'
It reevaporates at relatively low temperatures below C. 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.
It can be set appropriately by controlling wJ with a control valve 15 provided at 4.

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。
The vacuum vapor generated in the evaporation container 1 is transferred to the vacuum vapor outlet 4.
The steam reaches the steam using device 2 and heats the object to be heated. The condensate that has been condensed again by heating is sucked into the ejector 8 through the condensate discharge pipe 7. Therefore, the vacuum steam generated from heated wastewater, which was conventionally often discarded, is forcibly circulated, and even a device using steam with a large load 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 condensate is circulated through the water supply tank 9 and the circulation pump 10, and excess water is removed from 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と真空ポンプ2
6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 Figure 2) This embodiment has a pressure regulating valve 25 and a vacuum pump 2 in addition to the first embodiment.
6 has been added, and the same members are given the same reference numerals, and a detailed explanation of the vacuum steam generator 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
の加熱温度をざら(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の運転能力は小ざなもの
ですみランニングコストの低減を計ることかできる。
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 maintains the supply pressure to the vacuum steam using device 2 at a predetermined value to keep the heating temperature of the object to be heated constant (with high precision). By providing a vacuum pump 26 separate from the vacuum pump 30 in order to maintain the desired degree of vacuum, the operating capacity of the vacuum pump 30 is small, and running costs 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 Figure 3) This embodiment is the same as the second embodiment by adding an auxiliary steam supply pipe 27 and a steam ejector 28, and the same members as in the above embodiment are given the same reference numerals. , detailed explanation 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
力を高めることかできる。
The vacuum steam generated within the evaporation container 1 is sucked into the steam ejector 28 and mixed with the auxiliary steam supplied from the auxiliary steam supply pipe 27. The mixed steam passes through the pressure regulating valve 25
The vapor is then supplied to the vacuum steam using device 2, where the object to be heated is heat-treated. The heating capacity can be further increased by supplying auxiliary steam.

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3
4を設けると共に、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を設は圧力コントローラ3
5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mすることにより、ざ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, the pressure control valve 3 is connected to the auxiliary steam supply pipe 27.
4, and a pressure sensor 29 is installed between the steam ejector 28 and the vacuum steam usage device 2.
By operating the pressure control valve 34 via the pressure control valve 5 to control the supply steam pressure, the heating temperature of the object to be heated can be controlled with rough precision.

【図面の簡単な説明】[Brief explanation of the drawing]

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 3:温水導入管    4 8:エゼクタ    12 14:冷却水供給管  23 25:圧力調整弁   27 28:蒸気エゼクタ  29 26.30:真空ポンプ31 34:圧力コントロール弁 真空蒸気使用装置 真空蒸気取出口 ノズル 連通管 補助蒸気供給管 圧力センサー コントロール部 端)田 男21図 第3図
FIG. 1 is a system diagram showing an embodiment of the vacuum steam generator of the present invention, and FIGS. 2, 3, and 4 are system diagrams showing other embodiments. 1: Evaporation container 2 3: Hot water introduction pipe 4 8: Ejector 12 14: Cooling water supply pipe 23 25: Pressure adjustment valve 27 28: Steam ejector 29 26.30: Vacuum pump 31 34: Pressure control valve Vacuum steam usage device Vacuum Steam outlet nozzle communication pipe Auxiliary steam supply pipe Pressure sensor Control section end) Tao 21 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 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と接続し、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した真空蒸気発生装置。
1. An evaporation container into which heated waste water flows is connected to a decompression means for maintaining the evaporation container at a desired degree of vacuum, and the vacuum steam generated by re-evaporation of the heated waste water is utilized in the evaporation container. A vacuum steam generation device in which a vacuum steam outlet and pressure reduction means are arranged via a vacuum steam usage device.
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 true JPH0448102A (en) 1992-02-18
JP2916699B2 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)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010065985A (en) * 2008-09-12 2010-03-25 Tlv Co Ltd Vapor compression type refrigerating machine
JP2012508862A (en) * 2008-11-13 2012-04-12 ヨンイル パムプテク カンパニー, リミテッド Re-evaporated steam and condensed water recovery equipment

Citations (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

Family Cites Families (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

Patent Citations (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

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010065985A (en) * 2008-09-12 2010-03-25 Tlv Co Ltd Vapor compression type refrigerating machine
JP2012508862A (en) * 2008-11-13 2012-04-12 ヨンイル パムプテク カンパニー, リミテッド Re-evaporated steam and condensed water recovery equipment

Also Published As

Publication number Publication date
JP2916699B2 (en) 1999-07-05

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