JPH02272202A - Vacuum evaporator - Google Patents

Vacuum evaporator

Info

Publication number
JPH02272202A
JPH02272202A JP9385489A JP9385489A JPH02272202A JP H02272202 A JPH02272202 A JP H02272202A JP 9385489 A JP9385489 A JP 9385489A JP 9385489 A JP9385489 A JP 9385489A JP H02272202 A JPH02272202 A JP H02272202A
Authority
JP
Japan
Prior art keywords
temperature
regulating valve
steam
fluid
temperature regulating
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.)
Pending
Application number
JP9385489A
Other languages
Japanese (ja)
Inventor
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 JP9385489A priority Critical patent/JPH02272202A/en
Publication of JPH02272202A publication Critical patent/JPH02272202A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To perform a vacuum evaporation in a simple construction without requiring a complex control in such a constitution where the heating medium in the temperature regulating valve expands and contracts to open and close the main valve opening of said temperature regulating valve to regulate the flow of the heating fluid so as to adjust the secondary side temperature of the temperature regulating valve or the temperature of the heated fluid in the heat exchanger to a desired level. CONSTITUTION:The temperature regulating valve 4 detects by its sensing part 16 the temperature of the heated fluid which is to be controlled, and regulates the flow rate of steam from the primary side line 28 to the secondary side by causing its bellows to be actuated by the pressure change on account of the expansion of the thermally expandable fluid sealed therein. The secondary side of the temperature regulating valve 4 is always maintained in the negative pressure by the operation of a vacuum pump 12, and its steam temperature is also maintained below 100 deg.C. When the temperature of the heated fluid is below the set temperature, the temperature regulating valve 4 opens to supply the steam from the primary side to the heat exchanger. When the temperature of the heated fluid which exchanged heat becomes higher than the set temperature, the temperature regulating valve 4 closes to control the supply of the steam. By repeating such process, the temperature of the heated fluid is maintained at the set level.

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ioo’c以下の温度で安全且つ効
率的に加熱処理する為に、常時安定した真空蒸気を発生
供給する真空蒸気発生装置に関する。
[Detailed Description of the Invention] <Industrial Application Field> The present invention provides a vacuum steam system that constantly generates and supplies stable vacuum steam in order to safely and efficiently heat-treat objects to be heated at temperatures below IOO'C. Regarding the generator.

各種製造工場に於ては加熱処理が広く一般に行なわれて
いるが、かかる加熱処理は被加熱物を100℃以上の高
温で加熱することが多く、ボイラーからの蒸気をそのま
ま利用した、つまり正圧系の加熱装置を用いて行なわれ
ている。
Heat treatment is widely performed in various manufacturing factories, but such heat treatment often involves heating the object to a high temperature of 100°C or higher, and steam from the boiler is directly used, that is, positive pressure is used. This is done using a system heating device.

しかし、一部の化学工場や食品工場に於ては、作業の安
全や製品の品質の関係で被加熱物を100°C以下の比
較的低温で、つまり負圧系の加熱装置を用いて行なう場
合がある。
However, in some chemical and food factories, for reasons of work safety and product quality, the heating process is carried out at a relatively low temperature of 100°C or less, that is, using negative pressure heating equipment. There are cases.

〈従来の技術〉 そこで従来は特開昭64−19202号公報に記載され
る真空蒸気発生装置がおる。これは熱交換器の一次側に
自動調節弁を、そして二次側に真空ポンプを配置した装
置に於て、被加熱物の温度を温度検出器で検出し、その
信号をPtD調節計に入力し、PID調節計に予め設定
されている被加熱物の設定温度と上記検出温度との偏差
がOとなるように上記自動調節弁をPID制御せしめる
ようにしたものである。
<Prior Art> Conventionally, there is a vacuum steam generator described in Japanese Unexamined Patent Publication No. 19202/1983. This is a device that has an automatic control valve on the primary side of the heat exchanger and a vacuum pump on the secondary side.The temperature of the heated object is detected by a temperature detector, and the signal is input to the PtD controller. However, the automatic control valve is controlled by PID so that the deviation between the detected temperature and the set temperature of the object to be heated, which is preset in the PID controller, is O.

〈発明が解決しようとする課題〉 しかし、上記のような装置に於て熱交換器出口側での被
加熱物の温度変化が発生する。この原因は加熱流体の圧
力変化に伴う温度変化、被加熱物の流量の変化、または
被加熱物の温度変化が挙げられる。このような原因の発
生状況としては、加熱流体の圧力変化に伴う温度変化の
みが生じる場合と、被加熱物の流量変化または被加熱物
の温度変化のみが生じる場合と、加熱流体の圧力変化に
伴う温度変化と被加熱物の流量変化または温度変化とが
同時に生じる場合とがある。
<Problems to be Solved by the Invention> However, in the above-described apparatus, a temperature change of the object to be heated occurs on the exit side of the heat exchanger. This may be caused by a change in temperature due to a change in the pressure of the heating fluid, a change in the flow rate of the object to be heated, or a change in the temperature of the object to be heated. These causes can occur when only a temperature change occurs due to a change in the pressure of the heated fluid, when only a change in the flow rate of the heated object or a change in the temperature of the heated object occurs, and when a change in the pressure of the heated fluid occurs. There are cases where the accompanying temperature change and the flow rate change or temperature change of the heated object occur simultaneously.

これらの変動はPID調節計によって補正するが、加熱
流体の圧力変化に伴う温度変化を補正するのに最適なP
ID定数と、被加熱物の流量変化または温度変化を補正
する為に最適なPID定数と、加熱流体の圧力変化に伴
う温度変化と被加熱物の流量または温度変化の双方を補
正する為の最適なPID定数とはそれぞれ異なっており
、これら全ての場合についてPID調節計によって対応
しようとすると制御が複雑になるという問題があった。
These fluctuations are corrected by a PID controller, but the PID controller is optimal for correcting temperature changes due to pressure changes in the heating fluid.
The ID constant, the optimum PID constant for correcting the flow rate change or temperature change of the heated object, and the optimum PID constant for correcting both the temperature change due to the pressure change of the heating fluid and the flow rate or temperature change of the heated object. However, if a PID controller were used to handle all of these cases, the control would become complicated.

また、上記制御@置は非常に高価である。Furthermore, the above control system is very expensive.

従って本発明の技術的課題は、PIDli1節計のよう
な複雑な制御を必要とぜず、簡単な構造で真空蒸気を発
生させる装置を提供することである。
Therefore, the technical problem of the present invention is to provide a device that generates vacuum steam with a simple structure without requiring complicated control such as PIDli1 control.

く課題を解決する為の手段〉 上記問題点を解決する為に講じた本発明の技術的手段は
、熱交換器の一次側に、制御対象物の温度を検出する機
構によって熱媒を調整することにより弁口を開閉して制
御対象物の温度を一定に保持する温度調整弁を配置し、
その温度の検出を温度調整弁の二次側の温度、または熱
交換器に於ける被加熱流体の温度を検出し、熱交換器の
二次側に真空ポンプを接続したものである。
Means for Solving the Problems> The technical means of the present invention taken to solve the above problems is to adjust the heat medium on the primary side of the heat exchanger by a mechanism that detects the temperature of the object to be controlled. A temperature regulating valve is installed to maintain a constant temperature of the controlled object by opening and closing the valve port.
The temperature is detected by detecting the temperature on the secondary side of the temperature regulating valve or the temperature of the heated fluid in the heat exchanger, and a vacuum pump is connected to the secondary side of the heat exchanger.

く作 用〉 真空ポンプで吸引することにより温度調整弁の二次側の
圧力は負圧状態になり、−次側から蒸気が供給される。
Effect> By suctioning with a vacuum pump, the pressure on the secondary side of the temperature control valve becomes a negative pressure state, and steam is supplied from the negative side.

温度調整弁の温度検出部は温度調整弁の二次側の温度、
または熱交換器に於ける被110熱流体の温度を検出す
るように取付けられているので、温度調整弁の中の熱媒
が膨脹収縮して温度調整弁の主弁口を開閉して加熱流体
の流量を加減し、温度調整弁の二次側の温度、または熱
交換器に於ける被加熱流体の温度が所望の設定温度にな
るように調整する。
The temperature detection part of the temperature adjustment valve detects the temperature on the secondary side of the temperature adjustment valve,
Alternatively, since the heat exchanger is installed to detect the temperature of the heated fluid, the heating medium in the temperature regulating valve expands and contracts, opening and closing the main valve port of the temperature regulating valve, thereby increasing the temperature of the heated fluid. The flow rate is adjusted so that the temperature on the secondary side of the temperature regulating valve or the temperature of the heated fluid in the heat exchanger reaches the desired set temperature.

〈実施例〉 上記技術的手段の具体例を示す実施例を説明する。(第
1図及び第2図参照) ヘッダー2の一次側に温度調整弁4を配置し、そしてヘ
ッダー2の上部から配管14を取り出して止め弁8を介
して熱交換器10と接続する。熱交換器10の二次側に
は配管18を介して真空ポンプ12の吸引部20と接続
する。熱交換器10には被加熱流体の入口配管30と出
口配管32を設け、被加熱流体の温度を検出するように
温度調整弁4の感温部16を取付ける。本実施例では被
加熱流体の温度を制御すべく感温部16を取付けている
が、温度調整弁4の二次側である加熱流体の温度を制御
する為に配管14内に直接感温部16を挿入してもよい
。ヘッダー2の下端から配管22を取り出してスチーム
トラップ24を配置し、その二次側は配管26を介して
真空ポンプ12の吸引部20と接続する。温度調整弁4
の一次側配管28は正圧蒸気系でおり、その二次側以降
はすべて負圧蒸気系となる。
<Example> An example showing a specific example of the above technical means will be described. (See FIGS. 1 and 2) A temperature control valve 4 is disposed on the primary side of the header 2, and a pipe 14 is taken out from the top of the header 2 and connected to a heat exchanger 10 via a stop valve 8. The secondary side of the heat exchanger 10 is connected to a suction section 20 of a vacuum pump 12 via a pipe 18. The heat exchanger 10 is provided with an inlet pipe 30 and an outlet pipe 32 for the fluid to be heated, and a temperature sensing portion 16 of the temperature regulating valve 4 is attached to detect the temperature of the fluid to be heated. In this embodiment, a temperature sensing section 16 is installed to control the temperature of the fluid to be heated. 16 may be inserted. A piping 22 is taken out from the lower end of the header 2 and a steam trap 24 is placed therein, and its secondary side is connected to the suction part 20 of the vacuum pump 12 via a piping 26. Temperature adjustment valve 4
The primary side piping 28 is a positive pressure steam system, and everything after the secondary side is a negative pressure steam system.

温度調整弁4の構造は弁本体部6aとアクチュエータ部
6bからなる。弁本体部6a内には図示していないが流
体が通過する弁口と、その弁口を開閉する弁体を有して
おり、アクチュエータ部6b内には前記弁本体6a内の
弁体を弁棒を介して操作するベローズが内蔵されている
。ベローズは一方向にばねで付勢されており、その付勢
力を調節することにより任意の設定温度を選択すること
ができる。そして感温部16と前記アクチュエータ部6
b内のベローズ(図示せず)を可撓管17で接続し、そ
の内部にはエーテル等の熱膨脹流体を封入する。被加熱
物の制御すべき対象の温度を感温部16で検出し、封入
された熱膨脹流体の膨脹による圧力変化でベローズを駆
動せしめ、弁棒を介して弁体が弁口を開閉し、−次側配
管28から二次側へ向かう蒸気の通過量を調整する。
The structure of the temperature regulating valve 4 consists of a valve body part 6a and an actuator part 6b. Although not shown, the valve body portion 6a has a valve port through which fluid passes, and a valve body that opens and closes the valve port. It has a built-in bellows that is operated via a rod. The bellows is biased in one direction by a spring, and an arbitrary set temperature can be selected by adjusting the biasing force. The temperature sensing section 16 and the actuator section 6
A bellows (not shown) in b is connected with a flexible tube 17, and a thermal expansion fluid such as ether is sealed inside the flexible tube 17. The temperature of the object to be heated is detected by the temperature sensing part 16, and the bellows is driven by the pressure change due to the expansion of the enclosed thermal expansion fluid, and the valve body opens and closes the valve port via the valve stem, - The amount of steam passing from the next side piping 28 toward the secondary side is adjusted.

次に上記真空ポンプ12を第2図に従って説明する。Next, the vacuum pump 12 will be explained according to FIG.

タンク40とポンプ42を温度センサー44を取り付け
た吸込み管46を接続し、そしてポンプの42の二次側
に吐出管48を設ける。このポンプ42は通常の渦巻き
ポンプである。吐出管48にはエゼクタ一部50@設け
、吸引部20を形成し、更にエゼクタ−50から再び配
管にてタンク40へ戻る。タンク40には冷却水配管5
2が接続され、電動弁54を設けて温度センサー44と
連動させる。また吐出管48には圧送用電動弁56が設
けられ、タンク40に内蔵した電極棒58と連動させる
A suction pipe 46 with a temperature sensor 44 is connected to the tank 40 and the pump 42, and a discharge pipe 48 is provided on the secondary side of the pump 42. This pump 42 is a conventional centrifugal pump. A part of the ejector 50 is provided in the discharge pipe 48 to form the suction part 20, and the ejector 50 returns to the tank 40 via piping again. Cooling water piping 5 is installed in the tank 40.
2 is connected, and an electric valve 54 is provided to interlock with the temperature sensor 44. Further, the discharge pipe 48 is provided with an electric valve 56 for pressure feeding, which is linked with an electrode rod 58 built in the tank 40 .

タンク40内の流体は吸込み管46からポンプ42に吸
引され吐出管48及びエゼクタ一部50へ圧送され、再
びタンク内へ戻り循環する。この時エゼクタ一部ではそ
の中を流れる流体の温度に対する飽和圧力が発生する。
The fluid in the tank 40 is sucked into the pump 42 from the suction pipe 46, pumped to the discharge pipe 48 and the ejector part 50, and returned to the tank for circulation. At this time, a portion of the ejector generates a saturation pressure relative to the temperature of the fluid flowing therein.

従って吸込み管46に設けられた温度センサー44を任
意の温度に設定することにより、電動弁54が開閉して
冷却水がタンク内に入りタンク内を所望の流体温度に保
ち、結果設定温度に対する飽和圧力がエセクター部で発
生させることができる。つまり、タンク内の流体の温度
を100℃以下にすることによりエゼクタ一部に大気圧
以下の圧力を発生させることができる。
Therefore, by setting the temperature sensor 44 provided in the suction pipe 46 to an arbitrary temperature, the electric valve 54 opens and closes, allowing cooling water to enter the tank and maintain the tank at the desired fluid temperature, resulting in saturation at the set temperature. Pressure can be generated in the esector. That is, by lowering the temperature of the fluid in the tank to 100° C. or lower, a pressure lower than atmospheric pressure can be generated in a portion of the ejector.

エゼクタ一部50で発生した真空域により、吸引部20
から復水や蒸気等の流体を吸引しタンク40へ圧送する
。タンク40内の液位が高水位になれば、電極58が検
出し圧送用電動弁56が開弁して流体を遠方へ圧送する
。そしてタンク内が所定の低水位になれば電動弁56は
閉弁する。
Due to the vacuum area generated in the ejector part 50, the suction part 20
Fluids such as condensate and steam are suctioned from the tank 40 and sent under pressure to the tank 40. When the liquid level in the tank 40 reaches a high level, the electrode 58 detects this, and the pressure-feeding electric valve 56 opens to force-feed the fluid to a distant location. When the water level in the tank reaches a predetermined low level, the electric valve 56 closes.

次に全体の装置の作用を説明する。温度調整弁4の二次
側は真空ポンプ12の運転により常に負圧に保持されて
おり、その蒸気の温度も100℃以下に保持されている
。そして温度調整弁4は所望の設定温度に設定されてい
るので、被加熱物の温度が設定温度より低い場合には温
度調整弁4は開弁じて一次側の蒸気を熱交換器へ供給す
る。そして熱交換され被加熱物が設定温度よりも高くな
れば、温度調整弁4は閉弁方向に働き蒸気の供給を抑え
る。これを連続的に行なうことにより、被加熱物の温度
を設定値に保持する。
Next, the operation of the entire device will be explained. The secondary side of the temperature control valve 4 is always maintained at a negative pressure by the operation of the vacuum pump 12, and the temperature of the steam is also maintained at 100° C. or lower. Since the temperature regulating valve 4 is set at a desired set temperature, when the temperature of the object to be heated is lower than the set temperature, the temperature regulating valve 4 is opened to supply steam on the primary side to the heat exchanger. When the temperature of the heated object becomes higher than the set temperature after heat exchange, the temperature regulating valve 4 operates in the closing direction to suppress the supply of steam. By doing this continuously, the temperature of the object to be heated is maintained at the set value.

前述したように真空ポンプ12は任意の真空圧力を発生
させることができるので、その設定圧力即ち発生する蒸
気温度を被加熱物の目標温度よりも少し低く設定するこ
とにより、温度調整弁4の弁口は過剰に開閉することな
く安定した最も効率のよいバランス点で作動することが
できる。
As mentioned above, the vacuum pump 12 can generate any vacuum pressure, so by setting its set pressure, that is, the temperature of the generated steam, a little lower than the target temperature of the object to be heated, the temperature adjustment valve 4 can be adjusted. The mouth can operate at a stable, most efficient balance point without excessive opening and closing.

スチームトラップ24はヘッダー2内で発生した復水を
速やかに排除することにより、蒸気の乾き度を向上させ
て熱交換器の熱伝導度をよくすることができる。
The steam trap 24 quickly removes condensate generated within the header 2, thereby improving the dryness of the steam and improving the thermal conductivity of the heat exchanger.

〈発明の効果〉 本発明によれば複雑で、且つ高価な制御機器を用いるこ
となく非常に安価な装置で安定した真空蒸気を発生供給
することができる。
<Effects of the Invention> According to the present invention, stable vacuum steam can be generated and supplied using a very inexpensive device without using complicated and expensive control equipment.

また、高度な制御技術の知識を必要とせず誰にでも扱え
ることができる。
Furthermore, anyone can use it without requiring knowledge of advanced control technology.

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

第1図は本発明の具体的実施例を示す真空蒸気発生装置
の系統図、第2図は本発明の装置に用いたエゼクタ−式
真空ポンプの概略図である。 :ヘツダー :真空ポンプ :感温部 :タンク :エゼクタ一部 4:温度調整弁 10:熱交換器 24ニスチームトラツプ 42:ポンプ 44:温度センサー
FIG. 1 is a system diagram of a vacuum steam generating apparatus showing a specific embodiment of the present invention, and FIG. 2 is a schematic diagram of an ejector-type vacuum pump used in the apparatus of the present invention. : Header: Vacuum pump: Temperature sensing part: Tank: Ejector part 4: Temperature adjustment valve 10: Heat exchanger 24 Ni steam trap 42: Pump 44: Temperature sensor

Claims (1)

【特許請求の範囲】[Claims] 1、熱交換器の一次側に、制御対象物の温度を検出する
機構によつて熱媒を調整することにより弁口を開閉して
制御対象物の温度を一定に保持する温度調整弁を配置し
、その温度の検出を温度調整弁の二次側の温度、または
熱交換器に於ける被加熱流体の温度を検出し、熱交換器
の二次側に真空ポンプを接続した真空蒸気発生装置。
1. A temperature adjustment valve is placed on the primary side of the heat exchanger to maintain the temperature of the controlled object at a constant level by opening and closing the valve opening by adjusting the heat medium using a mechanism that detects the temperature of the controlled object. A vacuum steam generator that detects the temperature on the secondary side of a temperature regulating valve or the temperature of the heated fluid in a heat exchanger and connects a vacuum pump to the secondary side of the heat exchanger. .
JP9385489A 1989-04-12 1989-04-12 Vacuum evaporator Pending JPH02272202A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9385489A JPH02272202A (en) 1989-04-12 1989-04-12 Vacuum evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9385489A JPH02272202A (en) 1989-04-12 1989-04-12 Vacuum evaporator

Publications (1)

Publication Number Publication Date
JPH02272202A true JPH02272202A (en) 1990-11-07

Family

ID=14094005

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9385489A Pending JPH02272202A (en) 1989-04-12 1989-04-12 Vacuum evaporator

Country Status (1)

Country Link
JP (1) JPH02272202A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6419202A (en) * 1987-07-14 1989-01-23 Tlv Co Ltd Vacuum steam generator

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6419202A (en) * 1987-07-14 1989-01-23 Tlv Co Ltd Vacuum steam generator

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