JPH0435680B2 - - Google Patents
Info
- Publication number
- JPH0435680B2 JPH0435680B2 JP60095231A JP9523185A JPH0435680B2 JP H0435680 B2 JPH0435680 B2 JP H0435680B2 JP 60095231 A JP60095231 A JP 60095231A JP 9523185 A JP9523185 A JP 9523185A JP H0435680 B2 JPH0435680 B2 JP H0435680B2
- Authority
- JP
- Japan
- Prior art keywords
- downstream
- upstream
- unit
- pressure
- water level
- 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 - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 39
- 238000011144 upstream manufacturing Methods 0.000 claims description 27
- 238000010438 heat treatment Methods 0.000 claims description 5
- 230000003247 decreasing effect Effects 0.000 claims description 2
- 230000007423 decrease Effects 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000004904 shortening Methods 0.000 description 2
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
Landscapes
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、特に器内圧が負圧になることを防
止するセパレート型ヒートパイプの制御装置に関
する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention particularly relates to a control device for a separate heat pipe that prevents the internal pressure from becoming a negative pressure.
従来の技術
セパレート型ヒートパイプは、熱交換器の一種
であり、熱交換媒体であり水の蒸発器と凝縮器が
分離して設けられていることに特徴があるが、そ
の具体例には、数セツトのクローズドサイクルの
ユニツトからなり、各ユニツトが分離された蒸発
器、凝縮器および前記両者を接続する循環水ポン
プから構成されたものがある。このようなセパレ
ート型ヒートパイプの従来の制御は、加熱側のガ
ス温度を制御し、また蒸発器内の水面レベルの制
御を行なうもので、そのために循環水の流量制御
弁を操作端にしている。しかるに、加熱側のガス
温度が低下し、あるいは熱交換量が増大すると、
器内圧が負圧になり、その結果、系外から空気の
漏れ込みが生じて熱交換効率が劣化し、また系内
酸化のために劣化が発生する欠点がある。Background Art Separate heat pipes are a type of heat exchanger, and are characterized by having separate evaporators and condensers for water, which is the heat exchange medium. Some systems consist of several sets of closed cycle units, each consisting of a separate evaporator, a condenser, and a circulating water pump that connects the two. Conventional control of such separate type heat pipes controls the gas temperature on the heating side and also controls the water level in the evaporator, and for this purpose, the circulating water flow rate control valve is used as the operating end. . However, when the gas temperature on the heating side decreases or the amount of heat exchange increases,
The internal pressure becomes negative, and as a result, air leaks in from outside the system, deteriorating heat exchange efficiency, and oxidation occurs within the system, causing deterioration.
その対策としては、真空ポンプ、あるいは負圧
ラインへの引込によつて空気を排出することが考
えられるが、漏れ込むことには変わりがなくて本
質的な解決にはならない。 As a countermeasure, it is possible to exhaust the air by using a vacuum pump or by drawing it into a negative pressure line, but this does not solve the problem since the air still leaks.
発明の解決しようとする問題点
この発明は、セパレート型ヒートパイプの器内
圧が負圧になるのを防止するように制御して熱交
換効率の劣化、および系内酸化による短命化を生
起させないようにすることにある。Problems to be Solved by the Invention This invention controls the internal pressure of a separate heat pipe to prevent it from becoming a negative pressure, thereby preventing deterioration of heat exchange efficiency and shortening of life due to oxidation within the system. The goal is to
問題点を解決するための手段
この発明は、セパレート型ヒートパイプユニツ
トを複数使用した熱交換装置の器内圧が負圧にな
り得る側のユニツトに圧力を検知する発信器を取
付け、この発信器の出力に応じて当該ユニツトよ
りも加熱側のガス流れにおいて上流側に配置され
るヒートパイプユニツトの循環水量を増減するこ
とにより前記器内圧が負圧にならないようにする
ことを特徴とする制御装置にある。Means for Solving the Problems The present invention provides a heat exchanger using a plurality of separate heat pipe units, in which a transmitter for detecting pressure is attached to the unit on the side where the internal pressure can become negative pressure. A control device that prevents the internal pressure from becoming negative pressure by increasing or decreasing the amount of circulating water in a heat pipe unit disposed upstream of the heat pipe unit in the gas flow on the heating side according to the output. be.
作 用
この発明によれば、負圧になる側のユニツトの
器内圧が負圧になつたことを検知発信すると、上
流側ユニツトの循環水が制御されてその熱交換量
が減少するので、該負圧側ユニツトのガス入口温
度が上昇して正圧に復帰する。Effects According to this invention, when it is detected and transmitted that the internal pressure of the unit on the side where the pressure becomes negative has become negative pressure, the circulating water of the upstream unit is controlled and its heat exchange amount is reduced. The gas inlet temperature of the negative pressure side unit rises and returns to positive pressure.
実施例
つぎに、この発明の実施例を図面によつて説明
する。図示の実施例では二ユニツトのクローズド
サイクルは、排ガス12の上流側において熱を吸
収する上流側蒸発器1A、Bガス13に放熱する
上流側凝縮器2Aおよび前記両者を接続する上流
側循環水制御弁4Aを備えている上流側循環水ポ
ンプ3Aからなる排ガス上流側ユニツト14A、
ならびに前記排ガスの下流側において熱を吸収す
る下流側蒸発器1B、前記Bガスに放熱する下流
側凝縮器2Bおよび前記両者を接続する下流側循
環水制御弁4Bを備えている下流側循環水ポンプ
3Bからなる排ガス下流側ユニツト14Bから構
成されている。前記上、下流側両蒸発器の1A,
1Bに上流側蒸発器水面レベル発信器5A、下流
側蒸発器水面レベル発信器5Bを夫々装着させて
ある。前記上流側水面レベル発信器には上流側蒸
発器水面レベル設定器6Aを付設している上流側
蒸発器水面レベル偏差調節計7Aを接続して該偏
差調節計を前記上流側循環水制御弁を制御するロ
ーセレクタ11に接続してある。前記下流側水面
レベル発信器には下流側蒸発器水面レベル設定器
6Bを付設している下流側蒸発器水面レベル偏差
調節計7Bを接続して該偏差調節計を前記下流側
循環水制御弁に接続してある。さらに前記下流側
凝縮器には下流側ユニツト器内圧発信器8を装置
して該器内圧発信器8を前記ローセレクタ11
に、器内圧設定器9を付設している圧力偏差調節
計10を介して接続させてある。Embodiments Next, embodiments of the present invention will be described with reference to the drawings. In the illustrated embodiment, the two-unit closed cycle includes an upstream evaporator 1A that absorbs heat on the upstream side of the exhaust gas 12, an upstream condenser 2A that radiates heat to the B gas 13, and an upstream circulating water control that connects the two. an exhaust gas upstream unit 14A comprising an upstream circulating water pump 3A equipped with a valve 4A;
and a downstream circulating water pump comprising a downstream evaporator 1B that absorbs heat on the downstream side of the exhaust gas, a downstream condenser 2B that radiates heat to the B gas, and a downstream circulating water control valve 4B that connects the two. It is composed of an exhaust gas downstream unit 14B consisting of 3B. 1A of both the upper and downstream evaporators,
1B is equipped with an upstream evaporator water level transmitter 5A and a downstream evaporator water level transmitter 5B, respectively. An upstream evaporator water level deviation controller 7A equipped with an upstream evaporator water level setting device 6A is connected to the upstream water level transmitter, and the deviation controller is connected to the upstream circulating water control valve. It is connected to the low selector 11 to be controlled. A downstream evaporator water level deviation controller 7B equipped with a downstream evaporator water level setting device 6B is connected to the downstream water level transmitter, and the deviation controller is connected to the downstream circulating water control valve. It's connected. Further, a downstream unit internal pressure transmitter 8 is installed in the downstream condenser, and the unit internal pressure transmitter 8 is connected to the low selector 11.
The internal pressure setting device 9 is connected to the pressure deviation controller 10 via a pressure deviation controller 10 attached thereto.
したがつて、通常は、前記両蒸発器水面レベル
設定器を最も効率良く熱交換が可能な値に設定し
ておけば、前記上、下流側蒸発器水面レベル偏差
調節計によつて前記両蒸発器の水面レベルが該設
定値に制御されることになる。すなわち、下流側
ユニツト器内圧発信器8の信号は、器内圧設定器
9の信号(通常は大気圧に設定)を上回つてい
て、上、下流側蒸発器水面レベル偏差調節形7
A,7Bは飽和しているので、前記ローセレクタ
は、前記上流側水面レベル偏差調節計の信号を選
択して上流側ユニツト14Aもレベル一定制御を
行なうからである。 Therefore, normally, if the water level setter for both evaporators is set to a value that allows for the most efficient heat exchange, the upper and downstream evaporator water level deviation controllers will adjust the water level for both evaporators. The water level of the vessel will be controlled to the set value. That is, the signal from the downstream unit internal pressure transmitter 8 exceeds the signal from the internal pressure setting device 9 (usually set to atmospheric pressure), and the upper and downstream evaporator water level deviation adjustment types 7
A and 7B are saturated, so the low selector selects the signal from the upstream water surface level deviation controller, and the upstream unit 14A also performs level constant control.
しかるに、前記排ガスの温度が低下すると、当
然に下流側ユニツト14Bの入口での排ガス温度
も低下してその循環水温度も低下するので、下流
側器内圧発信器8の出力が器内圧設定器9の出力
を下回ることになり、そのために圧力偏差調節計
10の出力が上流側蒸発器水面レベル偏差調節計
7Aの出力を下回るから、ローセレクタ11によ
つて圧力制御に切替えられて前記下流側ユニツト
が負圧になることが防止される。 However, when the temperature of the exhaust gas decreases, the temperature of the exhaust gas at the inlet of the downstream unit 14B naturally decreases, and the temperature of the circulating water also decreases, so that the output of the downstream chamber internal pressure transmitter 8 changes to the internal pressure setting device 9. As a result, the output of the pressure deviation controller 10 becomes lower than the output of the upstream evaporator water level deviation controller 7A, so the low selector 11 switches to pressure control and the downstream unit is prevented from becoming a negative pressure.
なお、上流側ユニツト14Aでの熱交換を零状
態にさせても、なお下流側ユニツト14Bが負圧
になる場合には、該下流側ユニツトも前記上流側
ユニツトと同様な構成にすればよい。 Note that even if the heat exchange in the upstream unit 14A is brought to zero, if the pressure in the downstream unit 14B still becomes negative, the downstream unit may be configured in the same manner as the upstream unit.
またなお、前述の説明では、排ガス12による
Bガス13の加熱としてあるが、ガスは加熱側、
被加熱側ともに気体であれば差支えなく、さらに
ユニツト数を二ユニツトとして説明したが、三ユ
ニツト以上で構成させても同様な効果があること
は詳述するまでもない。 Furthermore, in the above explanation, the B gas 13 is heated by the exhaust gas 12, but the gas is on the heating side,
There is no problem as long as both sides to be heated are gas, and although the number of units has been described as two, it is needless to say in detail that the same effect can be obtained even if the number of units is three or more.
発明の効果
上述したように、この発明は、セパレート型ヒ
ートパイプの器内圧が負圧になることがなくて運
転を行なうことができるから、負圧になるために
起こる空気漏れ込みによる熱交換効率の劣化、ま
たは系内酸化に原因する短寿命化を避けることが
でき、その産業上の利用価値は極めて大きい。Effects of the Invention As described above, the present invention allows operation of a separate heat pipe without the internal pressure becoming negative pressure, and therefore reduces heat exchange efficiency due to air leakage caused by negative pressure. It is possible to avoid deterioration or shortening of life caused by in-system oxidation, and its industrial value is extremely high.
図面は、この発明の実施例をあらわす系統図で
ある。
1A……上流側蒸発器、1B……下流側蒸発
器、2A……上流側凝縮器、2B……下流側凝縮
器、3A……上流側循環水ポンプ、3B……下流
側循環水ポンプ、4A…上流側循環水制御弁、4
B……下流側循環水制御弁、5A……上流側蒸発
器水面レベル発信器、5B……下流側蒸発器水面
レベル発信器、6A……上流側蒸発器水面レベル
設定器、6B……下流側蒸発器水面レベル設定
器、7A……上流側蒸発器水面レベル偏差調節
計、7B……下流側蒸発器水面レベル偏差調節
計、8……下流側ユニツト器内圧発信器、9……
器内圧設定器、10……圧力偏差調節計、11…
…ローセレクタ、12……排ガス、13……Bガ
ス、14A……上流側ユニツト、14B……下流
側ユニツト。
The drawing is a system diagram showing an embodiment of the present invention. 1A...Upstream evaporator, 1B...Downstream evaporator, 2A...Upstream condenser, 2B...Downstream condenser, 3A...Upstream circulating water pump, 3B...Downstream circulating water pump, 4A...Upstream circulating water control valve, 4
B...Downstream circulating water control valve, 5A...Upstream evaporator water level transmitter, 5B...Downstream evaporator water level transmitter, 6A...Upstream evaporator water level setting device, 6B...Downstream Side evaporator water level setting device, 7A... Upstream evaporator water level deviation controller, 7B... Downstream evaporator water level deviation controller, 8... Downstream unit internal pressure transmitter, 9...
Internal pressure setting device, 10...Pressure deviation controller, 11...
...Low selector, 12...Exhaust gas, 13...B gas, 14A...Upstream unit, 14B...Downstream unit.
Claims (1)
用した熱交換装置の器内圧が負圧になり得る側の
ユニツトに圧力を検知する発信器を取付け、この
発信器の出力に応じて当該ユニツトよりも加熱側
のガス流れにおいて上流側に配置されるヒートパ
イプユニツトの循環水量を増減することにより前
記器内圧が負圧にならないようにすることを特徴
とする制御装置。1 In a heat exchange device that uses multiple separate heat pipe units, a transmitter that detects pressure is attached to the unit on the side where the internal pressure can become negative pressure, and depending on the output of this transmitter, the unit on the heating side is A control device that prevents the internal pressure from becoming a negative pressure by increasing or decreasing the amount of circulating water in a heat pipe unit disposed upstream in the gas flow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60095231A JPS61252492A (en) | 1985-05-02 | 1985-05-02 | Control unit of separate type heat pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60095231A JPS61252492A (en) | 1985-05-02 | 1985-05-02 | Control unit of separate type heat pipe |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61252492A JPS61252492A (en) | 1986-11-10 |
| JPH0435680B2 true JPH0435680B2 (en) | 1992-06-11 |
Family
ID=14131985
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60095231A Granted JPS61252492A (en) | 1985-05-02 | 1985-05-02 | Control unit of separate type heat pipe |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61252492A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5607011A (en) * | 1991-01-25 | 1997-03-04 | Abdelmalek; Fawzy T. | Reverse heat exchanging system for boiler flue gas condensing and combustion air preheating |
| JP5326302B2 (en) * | 2008-03-07 | 2013-10-30 | 株式会社豊田自動織機 | Boiling cooling device and cooling method |
-
1985
- 1985-05-02 JP JP60095231A patent/JPS61252492A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61252492A (en) | 1986-11-10 |
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