JPH0730881B2 - Extraction method and extraction device for vacuum boiler - Google Patents

Extraction method and extraction device for vacuum boiler

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Publication number
JPH0730881B2
JPH0730881B2 JP1043774A JP4377489A JPH0730881B2 JP H0730881 B2 JPH0730881 B2 JP H0730881B2 JP 1043774 A JP1043774 A JP 1043774A JP 4377489 A JP4377489 A JP 4377489A JP H0730881 B2 JPH0730881 B2 JP H0730881B2
Authority
JP
Japan
Prior art keywords
heat
extraction
heating
bleeding
set temperature
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
Application number
JP1043774A
Other languages
Japanese (ja)
Other versions
JPH02223702A (en
Inventor
聡 柴田
朝久 小川
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.)
Takuma KK
Original Assignee
Takuma KK
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Filing date
Publication date
Application filed by Takuma KK filed Critical Takuma KK
Priority to JP1043774A priority Critical patent/JPH0730881B2/en
Publication of JPH02223702A publication Critical patent/JPH02223702A/en
Publication of JPH0730881B2 publication Critical patent/JPH0730881B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、給湯や暖房用の温水等を発生するための真空
ボイラ、詳しくは、内部圧が大気圧以下の缶体と、その
缶体内に封入した熱媒液を加熱するための加熱手段と、
熱媒液が第1設定温度となるように前記加熱手段を調整
する制御器と、前記缶体内の蒸気により被加熱流体を加
熱させるための熱取出し用の熱交換器と、前記缶体内の
被凝縮性ガスを排出するための抽気手段と、前記抽気手
段の作動に連動して、前記熱交換器による熱取出しを可
逆的に抑制又は停止する熱取出制御手段とを設けてある
真空ボイラの抽気方法と抽気装置に関する。
TECHNICAL FIELD The present invention relates to a vacuum boiler for generating hot water for hot water supply or heating, and more specifically, a can body having an internal pressure of atmospheric pressure or less, and a can body thereof. Heating means for heating the heat transfer medium enclosed in
A controller for adjusting the heating means so that the heat transfer liquid reaches the first set temperature, a heat exchanger for taking out heat for heating the fluid to be heated by the vapor in the can body, and a cover for the body in the can body. Extraction of a vacuum boiler provided with extraction means for discharging a condensable gas, and heat extraction control means for reversibly suppressing or stopping heat extraction by the heat exchanger in association with the operation of the extraction means. A method and an extraction device.

〔従来の技術〕[Conventional technology]

真空ボイラにおいて、抽気ポンプを作動させることによ
り、熱交換器での熱交換を阻害する要因である水素や窒
素、酸素等の非凝縮性ガスを缶体内から外部に排出する
抽気を行うに、例えば、熱交換器による熱取出しを行い
つつその抽気を行うと、熱交換器での熱交換、つまり、
熱交換器表面での蒸気の凝縮が通常のまま活発に行なわ
れる結果、非凝縮性ガスが蒸気とともに熱交換器側に引
張られ、非凝縮性ガスが抽気手段(つまり抽気ポンプに
よる吸い込み部)側に行かずに熱交換器の表面に付着残
存し、そのため、抽気ポンプを作動させても、非凝縮性
ガスが缶体内に多く残存し易い。
In the vacuum boiler, by operating the extraction pump, to extract the non-condensable gas such as hydrogen and nitrogen, which is a factor that inhibits heat exchange in the heat exchanger, from the inside of the can to the outside, for example, , When extracting the heat while taking out the heat by the heat exchanger, the heat exchange in the heat exchanger, that is,
As a result of the steam being actively condensed on the heat exchanger surface as usual, the non-condensable gas is pulled to the heat exchanger side together with the steam, and the non-condensable gas is extracted by the extraction means (that is, the suction part by the extraction pump). Therefore, a large amount of non-condensable gas remains in the can even when the extraction pump is operated.

それに対して、熱取出制御手段を設けて、抽気時には熱
交換器による熱取出しを停止又は抑制するように構成し
てある上記の真空ボイラでは、抽気時における熱交換器
表面での蒸気の凝縮を抑制又は中止させて、非凝縮性ガ
スが抽気手段側に流動し易い条件を作り出すことによ
り、缶体内の非凝縮性ガスの排出を容易化、迅速化でき
る利点がある。
On the other hand, in the above vacuum boiler, which is provided with a heat extraction control means and is configured to stop or suppress the heat extraction by the heat exchanger at the time of bleeding, the condensation of steam on the surface of the heat exchanger at the time of bleeding is prevented. By suppressing or stopping the non-condensable gas to create a condition in which the non-condensable gas easily flows toward the extraction means, there is an advantage that the discharge of the non-condensable gas in the can can be facilitated and accelerated.

そのような利点を有する真空ボイラの抽気技術として従
来に知られている技術は、特開昭57−192705号公報に見
られるように、熱取出制御手段として、抽気時には熱交
換器への被加熱流体の供給を停止又は減少させる手段を
設け、抽気ポンプを作動させての抽気時には、熱取出制
御手段により被凝縮性ガスの排出の容易化・迅速化を図
ることのみによって抽気性能の向上を達成しようとした
技術である。
A technique conventionally known as a bleeding technique of a vacuum boiler having such an advantage is, as shown in Japanese Patent Laid-Open No. 192705/1982, as a heat extraction control means, to be heated to a heat exchanger during bleeding. A means for stopping or reducing the supply of fluid is provided, and at the time of bleeding by operating the bleeding pump, the heat extraction control means improves the bleeding performance only by facilitating and speeding the discharge of the condensable gas. This is the technology that I tried.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

しかし、前記従来技術によるときは、熱取出制御手段に
より熱交換器での熱取出しを抑制又は停止することを行
うだけで抽気していたから、缶体内が、熱交換器による
熱取出しを行っている通常時の減圧状態で抽気すること
になり、そのため、缶体内と外部(大気)との差圧が大
きい状態で抽気する結果となって、抽気ポンプに対する
負荷が大きく、熱取出制御手段を設けることによる非凝
縮性ガス排出の容易化・迅速化を活かして高性能抽気を
実現するには、抽気ポンプとして排出能力の大きいもの
が必要であった。つまり、抽気ポンプの排出能力が小さ
いと、折角、熱取出制御手段を設けることによる非凝縮
性ガス排出の容易化・迅速化を意図しながらも、抽気ポ
ンプによる排出自体に時間が掛かって、所期の抽気の高
性能化を達成することができない。
However, in the case of the above-mentioned conventional technique, since the air is extracted by simply suppressing or stopping the heat extraction in the heat exchanger by the heat extraction control means, the inside of the can is normally performing heat extraction by the heat exchanger. Therefore, air is extracted in a depressurized state at that time. Therefore, air is extracted in a state where the pressure difference between the inside of the can and the outside (atmosphere) is large, resulting in a large load on the extraction pump and providing heat extraction control means. In order to realize high-performance extraction by taking advantage of the ease and speed of non-condensable gas discharge, a large extraction capacity was required for the extraction pump. In other words, if the discharge capacity of the extraction pump is small, the discharge itself by the extraction pump takes time, although it is intended to facilitate and speed up the discharge of non-condensable gas by providing a heat extraction control means. It is not possible to achieve high performance of extraction air during the period.

本発明の目的は、排出能力の小さい抽気ポンプを用いな
がらも、熱取出手段を設けることによる非凝縮性ガス排
出の容易化及び迅速化を活かした高性能抽気を実現する
ことができるようにする点にある。
An object of the present invention is to realize a high-performance bleed air that utilizes the ease and speed of non-condensable gas discharge by providing a heat extraction means while using a bleed air pump having a small discharge capacity. In point.

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明による真空ボイラの抽気装置の特徴は、前記抽気
手段による抽気時、前記第1設定温度よりも大となる第
3設定温度になるように熱媒液を加熱させる点にある。
The feature of the vacuum boiler bleeder according to the present invention is that the heat transfer medium is heated so as to reach the third set temperature which is higher than the first set temperature during the bleeding by the bleeding means.

また、本発明による真空ボイラの抽気装置の特徴構成
は、前記抽気手段による抽気時、前記第1設定温度より
も大となる第3設定温度に熱媒液がなるように前記加熱
手段を作動させる加熱制御手段を設けてある点にある。
Further, the vacuum boiler bleeding apparatus according to the present invention is characterized in that, when bleeding by the bleeding means, the heating means is operated so that the heat transfer liquid becomes a third set temperature which is higher than the first set temperature. A heating control means is provided.

〔作用〕[Action]

上記本発明の抽気方法によれば、熱交換器による熱取出
しを抑制又は停止した状態で抽気手段を作動させての抽
気時には、熱媒液に対する加熱作用を継続させるだけで
なく、第1設定温度、つまり、熱交換器による熱取出し
を行う通常時の温度よりも高い第3設定温度に熱媒液が
なるように加熱させるから、抽気時、熱媒液加熱による
蒸気発生を通常時よりも活発に行わせ、缶体内圧力を上
昇させることができる。
According to the bleeding method of the present invention, during bleeding by operating the bleeding means in a state in which heat extraction by the heat exchanger is suppressed or stopped, not only the heating action on the heat medium liquid is continued, but also the first set temperature. That is, since the heat transfer liquid is heated to the third preset temperature higher than the normal temperature when heat is taken out by the heat exchanger, the steam generation due to the heat transfer liquid heating during the extraction is more active than the normal time. The pressure inside the can can be increased by performing the above.

その結果、抽気時には、缶体内と外部との差圧を小さく
できて抽気ポンプに対する負荷を軽減できる。
As a result, during bleeding, the pressure difference between the inside of the can and the outside can be reduced, and the load on the bleeding pump can be reduced.

また、上記本発明の抽気装置によれば、加熱制御手段に
よって、熱交換器による熱取出しを抑制又は停止した状
態で抽気手段を作動させての抽気時には、熱媒液に対す
る加熱手段の加熱作用を継続させるだけでなく、第1設
定温度、つまり、熱交換器による熱取出しを行う通常時
の温度よりも高い第3設定温度に熱媒液がなるように加
熱手段を作動させて加熱させるように構成してあるか
ら、上記の方法と同様に、抽気時、熱媒液加熱による蒸
気発生を通常時よりも活発に行わせ、缶体内圧力を上昇
させることができる。
Further, according to the bleeding device of the present invention, the heating control means, during the bleeding by operating the bleeding means in a state in which the heat extraction by the heat exchanger is suppressed or stopped, the heating action of the heating means on the heating medium liquid. Not only is it continued, but the heating means is operated to heat so that the heat transfer liquid becomes the first set temperature, that is, the third set temperature higher than the temperature at the normal time when heat is taken out by the heat exchanger. Since it is configured, similarly to the above method, during extraction, steam generation by heating the heat medium liquid can be performed more actively than in the normal time, and the internal pressure of the can can be increased.

その結果、抽気時には、缶体内と外部との差圧を小さく
できて抽気ポンプに対する負荷を軽減できる。
As a result, during bleeding, the pressure difference between the inside of the can and the outside can be reduced, and the load on the bleeding pump can be reduced.

〔発明の効果〕〔The invention's effect〕

従って、本発明によれば、抽気ポンプとして排出能力が
小さいものを用いながらも、その抽気ポンプによる排出
性能として、抽気時には熱交換器での熱交換を抑制又は
停止させることによる非凝集性ガス排出の容易化・迅速
化に対応した高性能を発揮できて、所期の熱取出制御手
段を設けることによる排出の容易化・迅速化を活かした
高性能抽気を達成できる真空ボイラの抽気技術を提供で
きるようになった。
Therefore, according to the present invention, even though a bleed pump having a small discharge capacity is used, as the discharge performance of the bleed pump, non-cohesive gas discharge by suppressing or stopping heat exchange in the heat exchanger during bleed We provide the extraction technology of the vacuum boiler that can achieve high performance corresponding to the simplification and speedup of heat generation, and can achieve high-performance extraction by making use of the ease and speed of discharge by providing the desired heat extraction control means. I can do it now.

〔実施例〕〔Example〕

次に本発明の実施例を第1図に基づいて説明する。 Next, an embodiment of the present invention will be described with reference to FIG.

真空ボイラは、内部圧が大気圧以下で、かつ、熱媒液を
封入した缶体(1)と、前記熱媒液を加熱するための加
熱手段と、負荷(2)との間でポンプ(3)を介して循
環される被加熱水を缶体(1)内の熱媒蒸気により加熱
させるための熱取出し用の熱交換器(4)と、制御器
(5)と、前記缶体(1)内の非凝縮性ガスを外部に排
出するための抽気装置とを有する。
The vacuum boiler has a pump body (1) having an internal pressure equal to or lower than atmospheric pressure and containing a heat transfer medium, a heating unit for heating the heat transfer medium, and a load (2). 3), a heat exchanger (4) for taking out heat for heating the water to be heated circulated through the heating medium vapor in the can body (1), a controller (5), and the can body ( 1) An extraction device for discharging the non-condensable gas in the outside to the outside.

前記缶体(1)は、下部を液留部(1A)に、上部を減圧
蒸気室(1B)に夫々形成されている。
The lower part of the can body (1) is formed in the liquid distillation section (1A), and the upper part thereof is formed in the reduced pressure steam chamber (1B).

前記加熱手段は、前記缶体(1)の液留部(1A)内に挿
入させた熱媒液加熱用の火炉(6)と、前記熱媒液を加
熱するための燃焼を前記火炉(6)内で行なわせる送風
機(7a)付きのバーナ(7)とから構成されている。
The heating means includes a furnace (6) for heating the heat transfer medium inserted in the liquid distillation section (1A) of the can body (1), and a combustion furnace for heating the heat transfer medium (6). ) And a burner (7) with a blower (7a).

前記熱交換器(4)は前記減圧蒸気室(1B)内に配設さ
れている。
The heat exchanger (4) is arranged in the reduced pressure steam chamber (1B).

前記制御器(5)は、基本的には、運転スイッチ(8)
のONにより、前記バーナ(7)を燃焼作動させ、かつ、
ポンプ(3)を作動させたのち、熱媒液の温度を検出す
る液温センサ(S1)による検出温度に基づいて熱媒液が
設定器(9)による第1設定温度となるように前記バー
ナ(7)への燃料供給路に介装した燃料弁(10)の開度
を調整する温度制御を行なうものである。
The controller (5) is basically an operation switch (8).
Is turned on, the burner (7) is burnt, and
After the pump (3) is operated, the heat transfer liquid is brought to the first set temperature by the setter (9) based on the temperature detected by the liquid temperature sensor (S 1 ) for detecting the temperature of the heat transfer liquid. The temperature control is performed to adjust the opening of the fuel valve (10) provided in the fuel supply path to the burner (7).

前記抽気装置は、抽気手段と熱取出制御手段と加熱制御
手段とから成る。
The air extraction device includes an air extraction means, a heat extraction control means, and a heating control means.

前記抽気手段は、前記缶体(1)の減圧蒸気室(1B)に
連通して非凝縮性ガスを留めるガス留(11)を設け、そ
のガス留(11)に非凝縮性ガスを外部(大気)に排出す
るための抽気路(12)を接続し、その抽気路(12)に、
ガス留(11)から外部への一方向のガス流通のみを許容
する逆止弁(13)とガス排出用の抽気ポンプ(14)と
を、逆止弁(13)がガス留(11)側に位置する状態に介
装し、弁手段と制御手段とを設けて構成してある。
The bleeding means is provided with a gas fraction (11) communicating with the depressurized vapor chamber (1B) of the can body (1) for retaining the non-condensable gas, and the non-condensable gas is externally supplied to the gas fraction (11) ( The air extraction path (12) for discharging to the atmosphere) is connected to the extraction air path (12),
The check valve (13) for allowing only one-way gas flow from the gas distillation (11) to the outside and the extraction pump (14) for discharging gas are provided with the check valve (13) on the gas distillation (11) side. And is provided with valve means and control means.

前記抽気ポンプ(14)、ダイアフラム式の汎用小型真空
ポンプである。
The extraction pump (14) is a diaphragm type general-purpose small vacuum pump.

前記弁手段は、前記抽気路(12)のうち前記逆止弁(1
3)と抽気ポンプ(14)との間に位置する中間部分(12
a)を外部に対して連通ならびに遮断するための手段で
ある。具体的には、前記中間部分(12a)にそれを外部
に連通させる枝管(15)を接続し、その枝管(15)に電
磁弁利用の開閉弁(16)を介装して構成してある。
The valve means includes the check valve (1) in the bleed passage (12).
Intermediate part (12) located between 3) and the bleed pump (14)
It is a means for communicating and blocking a) from the outside. Specifically, a branch pipe (15) for communicating it with the outside is connected to the intermediate portion (12a), and an opening / closing valve (16) using a solenoid valve is interposed in the branch pipe (15). There is.

前記制御手段は、前記液温センサ(S1)による検出温度
が前記第1設定温度よりも低い第2設定温度以上で、か
つ、前記ガス留(11)内の温度を検出するガス温センサ
(S2)による検出温度と前記液温センサ(S1)による検
出温度との差が第1設定値以上になった運転条件のと
き、前記開閉弁(16)を開くとともに、抽気ポンプ(1
4)を作動させ、それから設定時間〔抽気ポンプ(14)
が定常作動状態に立止るまで十分な時間で、一般に5秒
等の数秒である。〕が経過した後、開閉弁(16)を閉
じ、前記液温センサ(S1)およびガス温センサ(S2)に
よる検出温度の差が前記第1設定値よりも小なる第2設
定値以下になったとき、前記抽気ポンプ(14)を停止す
るものである。つまり、基本的には、液温とガス留(1
1)内のガス温との温度差によって、非凝縮性ガスがガ
ス留(11)に留っているか否かを判断し、その判断に基
づいて抽気ポンプ(14)を発停制御することにより、自
動抽気を行なうのであるが、抽気開始後、設定時間だけ
開閉弁(16)を開いて抽気ポンプ(14)の吸込口を大気
に連通させることにより、抽気ポンプ(14)の負荷を解
消して抽気ポンプ(14)の作動を可能にさせる立上げ運
転を自動的に行なうのである。そして、この制御手段
は、前記制御器(5)に組込まれている。
The control means is a gas temperature sensor for detecting the temperature in the gas fraction (11) when the temperature detected by the liquid temperature sensor (S 1 ) is equal to or higher than a second preset temperature lower than the first preset temperature ( When the operating condition is such that the difference between the temperature detected by S 2 ) and the temperature detected by the liquid temperature sensor (S 1 ) exceeds the first set value, the open / close valve (16) is opened and the extraction pump (1
4) actuated, then set time [bleed pump (14)
Is a sufficient time until it stops in a steady operating state, which is generally several seconds such as 5 seconds. ], The on-off valve (16) is closed, and the difference between the temperatures detected by the liquid temperature sensor (S 1 ) and the gas temperature sensor (S 2 ) is less than the second set value which is smaller than the first set value. When this occurs, the extraction pump (14) is stopped. That is, basically, the liquid temperature and gas distillation (1
By determining whether or not the non-condensable gas remains in the gas fraction (11) based on the temperature difference from the gas temperature in 1), and by controlling the start / stop of the extraction pump (14) based on that determination. , Automatic bleeding is performed, but after bleeding is started, the load on the bleeding pump (14) is eliminated by opening the open / close valve (16) for a set time and communicating the suction port of the bleeding pump (14) with the atmosphere. The start-up operation that enables the operation of the extraction pump (14) is automatically performed. This control means is incorporated in the controller (5).

前記熱取出制御手段は、前述した運転条件で、かつ、前
記液温センサ(S1)による検出温度が第2設定温度以上
で第1設定温度以下のとき、前記ポンプ(3)を停止す
ることにより、前記熱交換器(4)による熱取出しを可
逆的に停止する手段であり、前記制御器(5)に組込ま
れている。
The heat extraction control means stops the pump (3) under the above-mentioned operating conditions and when the temperature detected by the liquid temperature sensor (S 1 ) is not less than the second preset temperature and not more than the first preset temperature. Is a means for reversibly stopping the heat extraction by the heat exchanger (4), and is incorporated in the controller (5).

前記加熱制御手段は、前述した運転条件となったとき、
前記燃料弁(10)を開度大側に作動させることにより、
前記第1設定温度よりも大となる第3設定温度に液温が
なるように熱媒液を加熱する手段であり、前記制御器
(5)に組込まれている。
The heating control means, when the operating conditions described above,
By operating the fuel valve (10) to the larger opening side,
The heating means is a means for heating the heat medium liquid so that the liquid temperature becomes a third set temperature which is higher than the first set temperature, and is incorporated in the controller (5).

前記第2設定温度は抽気ポンプ(14)の性能により決ま
り、第3設定温度は、加熱可能な最高温度である。
The second set temperature is determined by the performance of the extraction pump (14), and the third set temperature is the maximum temperature that can be heated.

因みに、第2設定温度、第3設定温度の実施例を挙げる
と、75℃、90℃であり、第1設定温度は、それらの中間
の温度、例えば85℃である。また、前記抽気ポンプ(1
4)を作動させる温度差の実数例を挙げると、10℃であ
り、抽気ポンプ(14)を停止させる温度差はそれよりも
小であることはもちろん、0℃であることが好ましい。
Incidentally, examples of the second set temperature and the third set temperature are 75 ° C. and 90 ° C., and the first set temperature is an intermediate temperature between them, for example, 85 ° C. In addition, the extraction pump (1
As an example of a real number of the temperature difference for operating 4), it is 10 ° C., and the temperature difference for stopping the extraction pump (14) is smaller than that, and it is preferably 0 ° C.

上記の実施例構成によれば、前述した運転条件となって
自動抽気が開始された際、それと同時に、熱交換器
(4)での熱取出しの停止が開始されて熱交換器(4)
での蒸気の凝縮中止が始まり、熱交換器(4)側への蒸
気の流動がなくなってガス留(11)へ非凝縮性ガスが流
れ易くなるとともに、熱媒液の第3設定温度への加熱上
昇が開始されて減圧蒸気室(1B)の内部圧が上昇し、抽
気ポンプ(14)に対する負荷が軽減されて抽気ポンプ
(14)の能力が高くなる。従って、抽気を効率良く行な
えるのである。
According to the configuration of the above embodiment, when the automatic extraction is started under the above-mentioned operating conditions, at the same time, the stop of the heat extraction in the heat exchanger (4) is started, and the heat exchanger (4) is started.
At this point, the condensation of steam in the heat exchanger started, the flow of steam to the heat exchanger (4) side disappeared, and the non-condensable gas easily flowed to the gas distillation (11). The heating rise is started, the internal pressure of the decompression steam chamber (1B) rises, the load on the extraction pump (14) is reduced, and the capacity of the extraction pump (14) increases. Therefore, bleeding can be performed efficiently.

〔別実施例〕[Another embodiment]

弁手段を構成するに、第2図に示すように、中間部分
(12a)を外部に挿通させる状態と連通させない状態と
に切替自在な三方弁(V)を設ける。
As shown in FIG. 2, the valve means is provided with a three-way valve (V) which can be switched between a state where the intermediate portion (12a) is inserted into the outside and a state where it is not communicated with the outside.

尚、特許請求の範囲の項に図面との対照を便利にする為
に符号を記すが、該記入により本発明は添付図面の構造
に限定されるものではない。
It should be noted that reference numerals are added to the claims for convenience of comparison with the drawings, but the present invention is not limited to the structures of the accompanying drawings by the entry.

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

第1図は本発明の実施例を示す概略構成図、第2図は本
発明の別実施例を示す要部の概略構成図である。 (1)……缶体、(4)……熱交換器。
FIG. 1 is a schematic configuration diagram showing an embodiment of the present invention, and FIG. 2 is a schematic configuration diagram of essential parts showing another embodiment of the present invention. (1) …… can body, (4) …… heat exchanger.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】内部圧が大気圧以下の缶体(1)と、その
缶体(1)内に封入した熱媒液を加熱するための加熱手
段と、熱媒液が第1設定温度となるように前記加熱手段
を調整する制御器(5)と、前記缶体(1)内の蒸気に
より被加熱流体を加熱させるための熱取出し用の熱交換
器(4)と、前記缶体(1)内の非凝縮性ガスを排出す
るための抽気手段と、前記抽気手段の作動に連動して、
前記熱交換器(4)による熱取出しを可逆的に抑制又は
停止する熱取出制御手段とを設けてある真空ボイラにお
いて、前記抽気手段による抽気時、前記第1設定温度よ
りも大となる第3設定温度になるように熱媒液を加熱さ
せる真空ボイラの抽気方法。
1. A can body (1) having an internal pressure equal to or lower than atmospheric pressure, heating means for heating a heat medium liquid enclosed in the can body (1), and the heat medium liquid having a first set temperature. A controller (5) for adjusting the heating means so that the heat exchanger (4) for taking out heat for heating the fluid to be heated by the vapor in the can body (1), and the can body ( 1) bleeding means for discharging the non-condensable gas in the inside, and in conjunction with the operation of the bleeding means,
In a vacuum boiler provided with heat extraction control means for reversibly suppressing or stopping heat extraction by the heat exchanger (4), a third boiler having a temperature higher than the first set temperature when the air is extracted by the air extracting means. A method for extracting air from a vacuum boiler that heats a heat transfer liquid to a set temperature.
【請求項2】内部圧が大気圧以下の缶体(1)と、その
缶体(1)内に封入した熱媒液を加熱するための加熱手
段と、熱媒液が第1設定温度となるように前記加熱手段
を調整する制御器(5)と、前記缶体(1)内の蒸気に
より被加熱流体を加熱させるための熱取出し用の熱交換
器(4)と、前記缶体(1)内の非凝縮性ガスを排出す
るための抽気手段と、前記抽気手段の作動に連動して、
前記熱交換器(4)による熱取出しを可逆的に抑制又は
停止する熱取出制御手段とを設けてある真空ボイラにお
いて、前記抽気手段による抽気時、前記第1設定温度よ
りも大となる第3設定温度に熱媒液がなるように前記加
熱手段を作動させる加熱制御手段を設けてある真空ボイ
ラの抽気装置。
2. A can body (1) having an internal pressure equal to or lower than atmospheric pressure, a heating means for heating the heat medium liquid enclosed in the can body (1), and the heat medium liquid having a first set temperature. A controller (5) for adjusting the heating means so that the heat exchanger (4) for taking out heat for heating the fluid to be heated by the vapor in the can body (1), and the can body ( 1) bleeding means for discharging the non-condensable gas in the inside, and in conjunction with the operation of the bleeding means,
In a vacuum boiler provided with heat extraction control means for reversibly suppressing or stopping heat extraction by the heat exchanger (4), a third boiler having a temperature higher than the first set temperature when the air is extracted by the air extracting means. A bleeder for a vacuum boiler provided with heating control means for operating the heating means so that the heat transfer liquid becomes a set temperature.
JP1043774A 1989-02-23 1989-02-23 Extraction method and extraction device for vacuum boiler Expired - Lifetime JPH0730881B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1043774A JPH0730881B2 (en) 1989-02-23 1989-02-23 Extraction method and extraction device for vacuum boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1043774A JPH0730881B2 (en) 1989-02-23 1989-02-23 Extraction method and extraction device for vacuum boiler

Publications (2)

Publication Number Publication Date
JPH02223702A JPH02223702A (en) 1990-09-06
JPH0730881B2 true JPH0730881B2 (en) 1995-04-10

Family

ID=12673102

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1043774A Expired - Lifetime JPH0730881B2 (en) 1989-02-23 1989-02-23 Extraction method and extraction device for vacuum boiler

Country Status (1)

Country Link
JP (1) JPH0730881B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105841131A (en) * 2016-05-16 2016-08-10 方快锅炉有限公司 Automatic control device and method for steam purity of vacuum boiler
JP6965106B2 (en) * 2017-11-06 2021-11-10 株式会社日本サーモエナー Vacuum type water heater and its decompression steam chamber airtightness reduction judgment method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57192705A (en) * 1981-05-21 1982-11-26 Takuma Kk Bleed method for decompression type boiler

Also Published As

Publication number Publication date
JPH02223702A (en) 1990-09-06

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