JPS5942239B2 - Vacuum heat exchange equipment with temperature control device - Google Patents

Vacuum heat exchange equipment with temperature control device

Info

Publication number
JPS5942239B2
JPS5942239B2 JP11891080A JP11891080A JPS5942239B2 JP S5942239 B2 JPS5942239 B2 JP S5942239B2 JP 11891080 A JP11891080 A JP 11891080A JP 11891080 A JP11891080 A JP 11891080A JP S5942239 B2 JPS5942239 B2 JP S5942239B2
Authority
JP
Japan
Prior art keywords
temperature
heat exchanger
pressure
exhaust gas
vacuum
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
Application number
JP11891080A
Other languages
Japanese (ja)
Other versions
JPS5743199A (en
Inventor
泉 溝「淵」
義夫 林
満嗣 河合
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.)
HIRAKAWA TEKKOSHO
Original Assignee
HIRAKAWA TEKKOSHO
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 HIRAKAWA TEKKOSHO filed Critical HIRAKAWA TEKKOSHO
Priority to JP11891080A priority Critical patent/JPS5942239B2/en
Publication of JPS5743199A publication Critical patent/JPS5743199A/en
Publication of JPS5942239B2 publication Critical patent/JPS5942239B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はボイラなどから発生する熱ガス又は燃焼排ガス
により熱交換する熱交換器と減圧下に保持された真空容
器とを密閉システムで接続し、熱ガス又は燃焼排ガスの
熱量を管形熱交換器内を流動する管内作業流体にて回収
し、真空容器へ循環させて真空容器内に装荷された熱交
換器により外部へ熱を取り出すようにした真空熱交換装
置の真空容器内を常に減圧下に保持させることを目的と
する温度又は圧力制御装置を備えた真空熱交換装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention connects a heat exchanger that exchanges heat using hot gas or combustion exhaust gas generated from a boiler or the like with a vacuum container maintained under reduced pressure in a closed system. Vacuum of a vacuum heat exchange device in which the heat is recovered by the working fluid flowing inside the tube heat exchanger, circulated to the vacuum container, and the heat is taken out to the outside by the heat exchanger loaded in the vacuum container. The present invention relates to a vacuum heat exchange device equipped with a temperature or pressure control device whose purpose is to maintain the inside of a container under reduced pressure at all times.

近年世界的に石油事情は非常に緊迫し、石油エネルギー
に代る代替燃料の利用がさげばれている。
In recent years, the oil situation has become extremely tense worldwide, and the use of alternative fuels to replace petroleum energy has been discouraged.

その一方において従来ボイラーなどの様に燃焼した排ガ
スは250〜300℃の温度で大気へ放出されているも
のが多(省エネルギ一対策としての排熱回収が益々脚光
を浴びてきた。
On the other hand, in many conventional boilers, the exhaust gas that is combusted is released into the atmosphere at a temperature of 250 to 300°C (exhaust heat recovery as a measure to save energy has been increasingly attracting attention.

しかしながらボイラ排ガスのように、比較的高温度のも
のであれば大気圧以上の温度でエコノマイザ−内の流体
を作動させればよいが、さらに低温におげろ熱回収とな
るとエコノマイザ−内の流体温度も低くする必要がある
However, if the temperature is relatively high, such as boiler exhaust gas, it is sufficient to operate the fluid in the economizer at a temperature above atmospheric pressure, but if the heat is recovered by lowering it to a lower temperature, the fluid temperature in the economizer increases. also needs to be lowered.

ところが単にエコノマイザ−内の流体の温度を低くする
だけでは排ガスの露点による設備の低温腐食を惹起す欠
点がある。
However, simply lowering the temperature of the fluid in the economizer has the drawback of causing low-temperature corrosion of the equipment due to the dew point of the exhaust gas.

この欠点を除去して低温における廃熱回収の目的を達成
する方法として廃熱回収の系を密閉システムとして真空
下に保持した作業流体を使用し、沸点を下げた作業流体
の真空熱交換器を導入することが考慮されるに至った。
As a method to eliminate this drawback and achieve the purpose of waste heat recovery at low temperatures, the waste heat recovery system is made into a closed system using a working fluid kept under vacuum, and a vacuum heat exchanger for the working fluid with a lower boiling point is used. Consideration has been given to introducing it.

一般に密閉システム内において水または熱媒流体等の作
業流体はその流体の温度に応じて飽和の蒸気もしくは熱
媒蒸気圧力を有する。
Typically, within a closed system, a working fluid, such as water or a heat transfer fluid, has a saturated vapor or heat transfer vapor pressure depending on the temperature of the fluid.

一例として水の場合は100℃で1気圧の器内圧力を呈
する。
For example, water exhibits an internal pressure of 1 atm at 100°C.

上記の如く密閉したシステムにおいては熱ガス又は燃焼
排ガス等により加熱された熱交換器内部の作業流体は真
空器内ではその液温に応じた飽和蒸気となり、その飽和
蒸気圧力を示し、もとの容器内圧力が上昇することとな
るが真空容器内に熱交換器を装荷することによって加熱
された熱量に等しい熱量を外部へ取出すことが可能にな
り、真空容器内の圧力はもとの容器内圧力に等しいある
一定の圧力に保たれ、熱量バランスが保たれることにな
る。
In a sealed system as described above, the working fluid inside the heat exchanger heated by hot gas or combustion exhaust gas becomes saturated steam in the vacuum chamber according to the liquid temperature, and its saturated steam pressure is indicated. The pressure inside the vacuum container will increase, but by loading a heat exchanger inside the vacuum container, it becomes possible to take out the amount of heat equal to the amount of heat heated outside, and the pressure inside the vacuum container will be reduced to the same amount as inside the original container. The pressure is maintained at a certain level, which is equal to the pressure, and the heat balance is maintained.

ところで、もしもこの熱量バランスが崩れ、外部に取出
される熱量よりも熱ガス等により加熱される熱量の方が
多い場合には真空容器内の循環液温が上昇し、真空容器
内の圧力が上昇し、真空容器内を減圧下に保持できない
という結果を招(のである。
By the way, if this heat balance is disrupted and the amount of heat heated by hot gas etc. is greater than the amount of heat extracted to the outside, the temperature of the circulating fluid inside the vacuum container will rise, and the pressure inside the vacuum container will rise. However, this results in the inability to maintain the inside of the vacuum container under reduced pressure.

また燃焼排ガスなどにおいては、結露におげろ熱交換器
の低温腐食が問題となることより熱交換器出口の排ガス
温度を排ガスの露点温度以上とすることが必要となる。
Furthermore, in the case of combustion exhaust gas, low-temperature corrosion of the heat exchanger due to dew condensation becomes a problem, so it is necessary to make the exhaust gas temperature at the outlet of the heat exchanger higher than the dew point temperature of the exhaust gas.

これは真空容器内の器内圧力を減圧下のある一定圧力に
常に保持することによって循環する作業流体の液温が一
定となり、液温を排ガスの露点温度以上に制御すること
で達成される。
This is achieved by constantly maintaining the internal pressure in the vacuum vessel at a certain constant pressure under reduced pressure so that the temperature of the circulating working fluid remains constant, and by controlling the liquid temperature to be higher than the dew point temperature of the exhaust gas.

従来の排熱回収装置では熱交換器に流入する熱ガス、も
しくは燃焼ガスの流量を制御する場合は熱交換器の上流
もしくは下流側に流量制御用ダンパを設けているが、こ
の従来方式では熱交換器に流入する熱ガスもしくは燃焼
排ガスがダンパの影響を受けて偏流する可能性があり、
熱交換器の熱回収率が低下するばかりでな(、ダンパを
大型にする必要がある。
In conventional exhaust heat recovery equipment, when controlling the flow rate of hot gas or combustion gas flowing into the heat exchanger, a damper is provided for controlling the flow rate on the upstream or downstream side of the heat exchanger. The hot gas or combustion exhaust gas flowing into the exchanger may be influenced by the damper and become biased.
Not only will the heat recovery rate of the heat exchanger decrease (but the damper will also need to be made larger).

上記に鑑み本発明は熱ガス又は燃焼排ガスなどの流路内
に収納された作業流体を収容した管形交換器の管内作業
流体の流入、流出側のパイプを、熱交換器を装荷した真
空容器に接続し、該作業流体を管形熱交換器と該真空容
器とを循環させるようにして、該真空容器内の熱交換器
によって系外へ熱を取り出すようになし、かつ熱ガスま
たは燃焼排ガスの流路に、熱ガス又は燃焼排ガスの流量
を制御するバイパスダンパを備えたバイパス煙道を設け
、真空容器に付属して設けた真空容器内の循環流体の液
温または圧力を検出する装置(以下温度又は圧力検出器
という)と上記バイパス煙道に付属して設けたバイパス
ダンパを制御する装置(以下コントロールモータという
)とを連結して温度又は圧力検出器によって真空容器内
の液温又は圧力を検出してコントロールモーぞを作tl
lせしめることによってバイパスダンパを制御するよう
ならしめてなる温度制御装置を備えた真空熱交換装置を
提供するもので、バイパスする熱ガスもしくは燃焼排ガ
スの流量を制御することによって常に上記真空容器内を
減圧下に保持させることを可能ならしめたものである。
In view of the above, the present invention provides a method for connecting working fluid inflow and outflow side pipes of a tubular exchanger containing a working fluid such as hot gas or combustion exhaust gas in a flow path to a vacuum container loaded with a heat exchanger. The working fluid is connected to the tubular heat exchanger and the vacuum container so that heat is extracted from the system by the heat exchanger in the vacuum container, and the hot gas or combustion exhaust gas is A bypass flue equipped with a bypass damper that controls the flow rate of hot gas or combustion exhaust gas is provided in the flow path of the vacuum vessel, and a device (attached to the vacuum vessel) that detects the liquid temperature or pressure of the circulating fluid in the vacuum vessel A device (hereinafter referred to as a temperature or pressure detector) that controls a bypass damper attached to the bypass flue (hereinafter referred to as a control motor) is connected to detect the temperature or pressure of the liquid in the vacuum container by connecting the temperature or pressure detector. Detect and create control mode
The present invention provides a vacuum heat exchange device equipped with a temperature control device that controls a bypass damper by increasing the temperature of the vacuum chamber, and by controlling the flow rate of hot gas or combustion exhaust gas to be bypassed, the pressure inside the vacuum container is constantly reduced. This allows it to be held at the bottom.

本発明のバイパスする熱ガスもしくは燃焼排ガスの流量
を制御する装置は管状熱交換器に流入する熱ガスもしく
は燃焼排ガスの偏流が容易に防止されると共に制御用の
ダンパも排ガスの圧力損失を考慮して小型化できる利点
をも合せもつものであり、蒸気または熱ガスの流路に設
けた真空熱交換装置においてその機能を充分発揮させる
のに必要欠くべからざるものである。
The device for controlling the flow rate of hot gas or combustion exhaust gas to be bypassed according to the present invention can easily prevent uneven flow of hot gas or combustion exhaust gas flowing into a tubular heat exchanger, and the control damper can also be configured to take into account the pressure loss of exhaust gas. It also has the advantage of being miniaturized and is indispensable for fully demonstrating its function in a vacuum heat exchange device installed in a steam or hot gas flow path.

次に図面によって本発明を詳細説明する。Next, the present invention will be explained in detail with reference to the drawings.

第1図は本発明の実施の一例を示すもので、ボイラなど
の煙道2より排出される燃焼排ガス1と熱交換させる管
状熱交換器4と管状交換器のバイパス煙道3 、バイパ
スダンパ5とバイパスダンパ5を駆動させるコントロー
ルモータ6熱交換器と真空容器8とを接続する連絡配管
7、真空容器8内に取付けられた熱交換器9及び圧力又
は温度検出器10から成る。
FIG. 1 shows an example of the implementation of the present invention, which includes a tubular heat exchanger 4 that exchanges heat with combustion exhaust gas 1 discharged from a flue 2 of a boiler, a bypass flue 3 of the tubular exchanger, and a bypass damper 5. It consists of a control motor that drives the bypass damper 5, a connecting pipe 7 that connects the heat exchanger and the vacuum vessel 8, a heat exchanger 9 installed in the vacuum vessel 8, and a pressure or temperature detector 10.

この管状熱交換器4と連絡配管7真空容器8とが減圧下
に保持される。
This tubular heat exchanger 4 and the connecting pipe 7 vacuum vessel 8 are maintained under reduced pressure.

ボイラ及び炉などの煙道より排出される燃焼排ガスと真
空容器8及び連絡配管7、熱交換器4内に保有される水
又は熱媒流体とが熱交換され、加熱された水または熱媒
流体が真空容器内に導かれる。
Heat is exchanged between the combustion exhaust gas discharged from the flue of a boiler or furnace, etc., and the water or heat medium fluid held in the vacuum container 8, the connecting pipe 7, and the heat exchanger 4, resulting in heated water or heat medium fluid. is introduced into a vacuum vessel.

真空容器8内で加熱された水又は熱媒流体は容器内の飽
和圧力に応じた飽和蒸気となるが容器内に装備された熱
交換器9より外部へ熱が取出されることにより蒸気或は
凝縮水となって滴下し真空容器下部にたまり連絡配管を
通り、再度管状熱交換器9に戻され、循環する。
The water or heat transfer fluid heated in the vacuum container 8 becomes saturated steam according to the saturated pressure in the container, but the heat is extracted to the outside from the heat exchanger 9 installed in the container, so that it becomes steam or The condensed water drips and accumulates at the bottom of the vacuum container, passes through the connecting pipe, and is returned to the tubular heat exchanger 9 for circulation.

ところで燃焼排ガスによって水または熱媒流体の加熱さ
れる熱量が外部へ取り出される熱量より多い場合には真
空容器8の容器内循環水の液温か上昇するので、温度ま
たは圧力検出器10によってこれを検出し、該検出器1
0に連結するバイパスダンパのコントロールモータ6を
駆動シ、バイパスダンパ5を開き、燃焼排ガス1をバイ
パス煙道3より煙道11へ逃がすことによって真空容器
内の循環水の液温を一定温度になるように制御する。
By the way, if the amount of heat heated by the combustion exhaust gas in the water or heat transfer fluid is greater than the amount of heat taken out to the outside, the liquid temperature of the circulating water in the vacuum container 8 will rise, and this will be detected by the temperature or pressure detector 10. and the detector 1
By driving the control motor 6 of the bypass damper connected to 0, the bypass damper 5 is opened, and the combustion exhaust gas 1 is released from the bypass flue 3 to the flue 11, thereby keeping the liquid temperature of the circulating water in the vacuum container at a constant temperature. Control as follows.

また逆に燃焼排ガスによって加熱される熱量が外部へ取
り出される熱量よりも少ない場合は循環水の液温か低下
するので検出器10によってこれヲ検知シ、バイパスダ
ンパ5のコントロールモータ6を駆動し、バイパスダン
パ5を閉じ、燃焼排ガスを熱交換器4の方へ流すことに
よって水又は熱媒流体の加熱量を増加し、真空容器内の
循環水を一定温度となるように制御する。
Conversely, if the amount of heat heated by the combustion exhaust gas is less than the amount of heat taken out to the outside, the temperature of the circulating water will drop, so the detector 10 detects this and drives the control motor 6 of the bypass damper 5 to prevent the bypass. By closing the damper 5 and causing the combustion exhaust gas to flow toward the heat exchanger 4, the amount of heating of water or heat transfer fluid is increased, and the circulating water in the vacuum container is controlled to a constant temperature.

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

第1図は本発明の一実施例のフローシートを示す。 1・・・・・・燃焼排ガス、2,11・・・・・・煙道
、計−・・・・バイパス煙道、4・・・・・・管状熱交
換器、5・・・・・・バイパスダンパ、6・・・・・・
コントロールモータ、7°゛・・。 接続配管、8・・・・・・真空容器、9・・・・・・熱
交換器、10・・・・・・温度又は圧力検出器。
FIG. 1 shows a flow sheet of one embodiment of the present invention. 1... Combustion exhaust gas, 2, 11... Flue, Total -... Bypass flue, 4... Tubular heat exchanger, 5...・Bypass damper, 6...
Control motor, 7°... Connection piping, 8... Vacuum vessel, 9... Heat exchanger, 10... Temperature or pressure detector.

Claims (1)

【特許請求の範囲】[Claims] 1 熱ガスまたは燃焼排ガスなどの流路内に収納された
作業流体を収容した管形熱交換器の管内作業流体の流入
、流出側のパイプを、熱交換器を装荷した真空容器に接
続し、該作業流体を管形熱交換器と該真空容器とを循環
させるようにして、該真空容器内の熱交換器によって、
系外の熱を取出すようにして、かつ熱ガスまたは燃焼排
ガスの流路に熱ガス又は燃焼排ガスの流量を制御するバ
イパスダンパを備えたバイパス煙道を設け、真空容器に
付属して設けた真空容器内の循環流体の液温または圧力
を検出する装置(以下温度又は圧力検出器という)と上
記バイパス煙道に付属して設けたバイパスダンパを制御
する装置とを連結して、温度又は圧力検出器によって真
空容器内の液温又は圧力を検出して、バイパスダンパを
制御する装置を作動せしめることによってバイパスダン
パを制御するようならしめてなる温度制御装置を備えた
真空熱交換装置。
1. Connect the pipes on the inflow and outflow sides of the working fluid in the pipes of a tubular heat exchanger containing working fluid such as hot gas or combustion exhaust gas in the flow path to a vacuum container loaded with the heat exchanger, by the heat exchanger in the vacuum vessel, such that the working fluid is circulated between the tubular heat exchanger and the vacuum vessel;
A bypass flue is installed in the flow path of the hot gas or combustion exhaust gas to extract heat from the outside of the system, and is equipped with a bypass damper for controlling the flow rate of the hot gas or combustion exhaust gas. A device that detects the temperature or pressure of the circulating fluid in the container (hereinafter referred to as a temperature or pressure detector) is connected to a device that controls the bypass damper attached to the bypass flue, and the temperature or pressure is detected. A vacuum heat exchange device equipped with a temperature control device that controls a bypass damper by detecting liquid temperature or pressure in a vacuum container using a device and activating a device that controls the bypass damper.
JP11891080A 1980-08-27 1980-08-27 Vacuum heat exchange equipment with temperature control device Expired JPS5942239B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11891080A JPS5942239B2 (en) 1980-08-27 1980-08-27 Vacuum heat exchange equipment with temperature control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11891080A JPS5942239B2 (en) 1980-08-27 1980-08-27 Vacuum heat exchange equipment with temperature control device

Publications (2)

Publication Number Publication Date
JPS5743199A JPS5743199A (en) 1982-03-11
JPS5942239B2 true JPS5942239B2 (en) 1984-10-13

Family

ID=14748188

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11891080A Expired JPS5942239B2 (en) 1980-08-27 1980-08-27 Vacuum heat exchange equipment with temperature control device

Country Status (1)

Country Link
JP (1) JPS5942239B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0677643B2 (en) * 1986-03-28 1994-10-05 日本真空技術株式会社 Centrifugal evaporator
JPH04126321A (en) * 1990-09-17 1992-04-27 Hitachi Ltd Switching device for underground substation
CN104728826A (en) * 2015-03-19 2015-06-24 中国华能集团清洁能源技术研究院有限公司 Constant temperature economizer

Also Published As

Publication number Publication date
JPS5743199A (en) 1982-03-11

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