JPH0252177B2 - - Google Patents

Info

Publication number
JPH0252177B2
JPH0252177B2 JP13163886A JP13163886A JPH0252177B2 JP H0252177 B2 JPH0252177 B2 JP H0252177B2 JP 13163886 A JP13163886 A JP 13163886A JP 13163886 A JP13163886 A JP 13163886A JP H0252177 B2 JPH0252177 B2 JP H0252177B2
Authority
JP
Japan
Prior art keywords
liquid
pressure
pipe
steam
liquid supply
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
JP13163886A
Other languages
Japanese (ja)
Other versions
JPS62288422A (en
Inventor
Masaaki Kuroki
Yoshimitsu Hashizume
Mikio Itazawa
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.)
Tokyo Gas Co Ltd
Original Assignee
Tokyo Gas 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 Tokyo Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Priority to JP13163886A priority Critical patent/JPS62288422A/en
Publication of JPS62288422A publication Critical patent/JPS62288422A/en
Publication of JPH0252177B2 publication Critical patent/JPH0252177B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、蒸気の凝縮潜熱を利用して気体又は
液体を加熱すると共に循環ポンプを使用しないで
凝縮した作動液を蒸気発生器内に環液する方式を
採用した蒸気式加熱装置における加熱用蒸気(作
動液)の循環装置に関するものである。
Detailed Description of the Invention [Industrial Application Field] The present invention heats gas or liquid using the latent heat of condensation of steam, and circulates the condensed working fluid in a steam generator without using a circulation pump. This invention relates to a heating steam (working fluid) circulation device in a steam heating device that employs a liquid heating system.

[従来例の構成とその問題点] 第2図の受液容器03と逆止弁04を介した給
液容器09とで構成される環液装置と貫流ボイラ
である蒸気発生器01とを給液管010と均圧管
011とで連結した構造の装置において、蒸気発
生器01を加熱器05で加熱した場合、給液容器
09の液温が沸点になつているか、又は均圧管0
11の径が極めて大きい場合以外には給液容器0
9から蒸気発生器01への給水は行なわれず、従
つて、蒸気も発生できないことが判つている。
[Configuration of conventional example and its problems] A circulating liquid device consisting of a liquid receiving container 03 and a liquid supply container 09 via a check valve 04 shown in FIG. 2 and a steam generator 01 which is a once-through boiler are supplied In a device having a structure in which a liquid pipe 010 and a pressure equalizing pipe 011 are connected, when the steam generator 01 is heated by the heater 05, the liquid temperature in the liquid supply container 09 is at the boiling point, or the pressure equalizing pipe 0
Unless the diameter of 11 is extremely large, the liquid supply container 0
It is known that no water is supplied from 9 to the steam generator 01 and therefore no steam can be generated.

このような環液装置を用いて蒸気発生器への自
力給水を行なわせる場合、給水を正常に維持する
ためには、給液容器09の上部空間に空気などの
不凝縮ガスの封入が有効となる。すなわち始動時
に大気圧程度の空気を給液容器09の上部空間に
封入し、蒸気発生器01を加熱器05で加熱する
と、発生蒸気の一部は均圧管011を介して給液
容器09に流入する。流入した蒸気は封入空気を
加温し、給液容器09の圧力を上昇させ、その結
果給液容器09の温度を蒸気発生器01のヘツダ
ー温度よりも低い温度で蒸気発生器01のヘツダ
ー圧力と給液容器09の圧力とを等しくすること
ができる。そのため蒸気発生器01の蒸発減量分
だけ蒸気発生器01の加熱管の水位が低下し、給
液容器09の液面と水位差が生じ、そのヘツド差
で給水を行なわせる。
When self-supplying water to the steam generator using such a reflux device, it is effective to fill the upper space of the liquid supply container 09 with non-condensable gas, such as air, in order to maintain the water supply normally. Become. In other words, when air at about atmospheric pressure is filled in the upper space of the liquid supply container 09 at startup, and the steam generator 01 is heated by the heater 05, a part of the generated steam flows into the liquid supply container 09 via the pressure equalization pipe 011. do. The inflowing steam warms the enclosed air and increases the pressure in the liquid supply container 09, so that the temperature in the liquid supply container 09 is lower than the header temperature of the steam generator 01 and the header pressure of the steam generator 01 is lowered. The pressure of the liquid supply container 09 can be made equal to the pressure of the liquid supply container 09. Therefore, the water level in the heating tube of the steam generator 01 is lowered by the evaporation loss of the steam generator 01, creating a water level difference with the liquid level in the liquid supply container 09, and water is supplied using the head difference.

このように給液容器09の上部空間に封入され
た空気の分圧効果で蒸気発生器への給水と蒸気の
発生が保証されるが、この装置では給液容器09
の水位が低下し、液位検知装置012の下限水位
に達したら加熱器05を停止し、給液容器09を
冷却、減圧させ逆止弁04を介して受液容器03
の作動液を給液容器09に落下還液させ、高水位
になつたら加熱器05を再着火し、蒸気を発生さ
せる。このようなサイクルの繰り返しで封入空気
の量が不足し、作動性能が低下するため、空気を
補給する必要がある。
In this way, water supply to the steam generator and generation of steam are guaranteed by the partial pressure effect of the air sealed in the upper space of the liquid supply container 09, but in this device, the liquid supply container 09
When the water level decreases and reaches the lower limit water level of the liquid level detection device 012, the heater 05 is stopped, the liquid supply container 09 is cooled and depressurized, and the liquid receiving container 03 is cooled through the check valve 04.
The working fluid is allowed to fall back into the liquid supply container 09, and when the water level reaches a high level, the heater 05 is re-ignited to generate steam. Repeating such a cycle causes the amount of sealed air to become insufficient and the operating performance to deteriorate, so it is necessary to replenish the air.

又、空気の補給を自動的に行なわせるために第
3図に示したような還液装置を連結した蒸気発生
器がある。
In addition, there is a steam generator connected to a liquid return device as shown in FIG. 3 in order to automatically replenish air.

この装置の還液装置は受液容器02内に小孔の
ある円筒状の空気吸入管012を給液容器01内
にフロート弁11を内蔵した還液管010の上部
に設置した構成のものである。
The liquid return device of this device has a configuration in which a cylindrical air suction pipe 012 with a small hole is placed in a liquid receiving container 02 above a liquid return pipe 010 that has a built-in float valve 11 in a liquid supply container 01. be.

この還液装置では給液容器01の液位検知装置
013の下限水位の検知で加熱器04を停止し、
給液容器01を冷却、減圧する。この結果、空気
吸入管012内の作動液を重力により、フロート
弁011を押し下げ、給液容器01に優先的に落
下させる。このとき給液容器01の上部空間は空
気吸入管012を通じて空気と連通し、給液容器
01内に空気を吸引・封入することができる。そ
して給液容器01内は上限水位になるまで受液容
器02の作動液が空気吸入管012の小孔から落
下還液しフロート弁011のフロートを押し上げ
る。上限水位に達したら、加熱器05を再着火さ
せ、蒸気発生器03を加熱して蒸気を発生し、そ
の一部が均圧管08を通して、給液容器01の上
部空間に流れ込み、封入空気を加温する。その結
果、給水が行なわれることになる。このように受
液容器02から給液容器01への作動液の落下還
液の際に空気を自動的に吸引・封入できることに
より、蒸気発生器としての貫流ボイラへ、ポンプ
を使用しないで給水することが可能になるが、こ
の方法では、還液操作を加熱器05を一時的に停
止し、給液容器01を冷却、減圧して行なつてい
るため、蒸気の発生は不連続(間欠的)となり、
実用面で不利になる。
In this liquid return device, the heater 04 is stopped when the lower limit water level is detected by the liquid level detection device 013 of the liquid supply container 01.
The liquid supply container 01 is cooled and depressurized. As a result, the hydraulic fluid in the air suction pipe 012 is caused to fall preferentially into the fluid supply container 01 by pushing down the float valve 011 due to gravity. At this time, the upper space of the liquid supply container 01 communicates with air through the air suction pipe 012, so that air can be sucked and sealed into the liquid supply container 01. Then, the working fluid in the liquid receiving container 02 falls through the small hole of the air suction pipe 012 and returns until the upper limit water level is reached in the liquid supply container 01, pushing up the float of the float valve 011. When the upper limit water level is reached, the heater 05 is re-ignited and the steam generator 03 is heated to generate steam, a part of which flows into the upper space of the liquid supply container 01 through the pressure equalization pipe 08, adding sealed air. Warm up. As a result, water will be supplied. In this way, air can be automatically sucked and sealed when the working fluid falls back from the liquid receiving container 02 to the supplying liquid container 01, allowing water to be supplied to the once-through boiler as a steam generator without using a pump. However, in this method, the liquid return operation is performed by temporarily stopping the heater 05 and cooling and depressurizing the liquid supply container 01, so the generation of steam is discontinuous (intermittent). ),
This will be disadvantageous in practical terms.

[本発明の目的] 本発明の目的は、ポンプを使用しないで、空気
を自動的に吸引・封入することのできる還液装置
で、高圧作動する貫流ボイラへ給水を可能にする
方式において、上記の蒸気の発生が不連続になる
点を排除し、還液時も蒸気を連続して発生できる
還液装置を提案することである。
[Object of the present invention] The object of the present invention is to provide a liquid return device that can automatically suck and enclose air without using a pump, and in a system that enables water supply to a once-through boiler operating at high pressure, the above-mentioned method is provided. An object of the present invention is to propose a liquid return device that can eliminate the discontinuous generation of steam and can continuously generate steam even during liquid return.

[本発明の構成とその作用] 本発明は上記目的を達成する手段として、下記
構成を採用するものである。
[Configuration of the present invention and its operation] The present invention employs the following configuration as a means for achieving the above object.

加熱源を付属した蒸気発生器と蒸気発生器で発
生した蒸気を導いて気体又は液体に凝縮潜熱を与
える熱交換器と、その熱交換器内で凝縮した凝縮
液体を熱交換器内に圧送されてくる蒸気圧により
大気開放型の受液容器内に還液する還液管と、前
記受液容器とはフロート弁付の凝縮液送出管を介
して接続しており、かつ蒸気発生器とは凝縮液供
給管及び均圧管で結ばれていると共に液位検知装
置を取り付けた給液容器とからなる加熱用蒸気の
循環装置において、受液容器の上部空間と給液容
器の上部空間とを圧抜弁付の空気吸引管にて連通
すると共に、前記均圧管に均圧弁を取り付け、給
液容器に取り付けた液位検知装置において、下位
水位を検出したときに前記圧抜弁を開放し、均圧
弁を閉じ、上位水位を検出したときに圧抜弁を閉
じ、均圧弁を開放する構成として成る蒸気式加熱
装置における加熱用蒸気の循環装置。上記装置に
おいては蒸気発生器で発生した蒸気は放熱器にお
いて凝縮潜熱を周囲に与えて凝縮し、この凝縮し
た液は受液容器にためられる。蒸気発生器での蒸
気発生が継続し、給液容器内の水位が下位水位ま
で下がるとこれを液位検出装置が検出して圧抜弁
を開放し、受液容器内と給液容器内を均圧にす
る。両容器内が均圧になると受液容器内に貯えら
れた凝縮液はその重力でフロート弁を押し開き、
給液容器内に流下する。このようにして給液容器
内に凝縮液が入り、この中の水位が上つて上位水
位になると液位検知装置がこれを検出して圧抜弁
を閉じ、均圧弁を開く。同時にフロート弁は受液
容器と給液容器との間の還液管を閉塞する。この
繰り返しにより受液容器内に貯えられた凝縮液が
給液容器内に還液される。
A steam generator with a heating source attached, a heat exchanger that guides the steam generated by the steam generator to give latent heat of condensation to the gas or liquid, and a condensed liquid condensed in the heat exchanger that is pumped into the heat exchanger. A liquid return pipe that returns liquid into a liquid receiving container open to the atmosphere due to the vapor pressure generated by the liquid is connected to the liquid receiving container via a condensate delivery pipe equipped with a float valve, and is connected to the steam generator. In a heating steam circulation system consisting of a condensate supply pipe and a supply liquid container connected by a pressure equalization pipe and equipped with a liquid level detection device, the upper space of the liquid receiving container and the upper space of the liquid supply container are kept under pressure. A pressure equalizing valve is connected to the pressure equalizing pipe, and the pressure equalizing valve is opened when a lower water level is detected in the liquid level detection device attached to the liquid supply container. A heating steam circulation device in a steam-type heating device, which closes a pressure relief valve and opens a pressure equalization valve when an upper water level is detected. In the above device, the steam generated by the steam generator is condensed by imparting latent heat of condensation to the surroundings in the radiator, and the condensed liquid is stored in the liquid receiving container. When the steam generator continues to generate steam and the water level in the liquid supply container falls to the lower water level, the liquid level detection device detects this and opens the pressure relief valve to equalize the inside of the liquid receiving container and the liquid supply container. Pressure. When the pressure in both containers becomes equal, the condensate stored in the receiving container pushes the float valve open with its gravity.
Flows down into the liquid supply container. In this way, the condensate enters the liquid supply container, and when the water level in the condensate rises to the upper water level, the liquid level detection device detects this, closes the pressure relief valve, and opens the pressure equalization valve. At the same time, the float valve closes the liquid return pipe between the liquid receiving container and the liquid supply container. By repeating this process, the condensed liquid stored in the liquid receiving container is returned to the liquid supplying container.

[実施例及びその作用] 第1図において1は給液容器、2は受液容器、
3は貫流型の蒸気発生器であり、給液容器1と蒸
気発生器3とは蒸気発生器3の方向のみに流れる
作用を持つ逆止弁11を介在した給液管5と均圧
弁12を介在した均圧管6とで接続されている。
7は蒸気管であり、加熱器4の熱エネルギーを受
けて蒸気発生器3で発生した蒸気を送出するもの
である。受液容器2の上部には凝縮管8と大気開
放管15が取り付けてある。給液容器1の上部に
は、受液容器2の底部に接続されたフロート弁1
0を内蔵した還液管9が取り付けてある。受液容
器2の上部空間部と給液容器1の上部空間部は圧
抜弁14を介在した圧抜管を兼ねる空気吸引管1
3で接続されている。又、給液容器1内には液位
検知装置16が取り付けてある。この液位検知装
置16は低水位検知部16bで均圧弁12を閉作
動させ、圧抜弁14を開動作するように働き、高
水位検知部16aで均圧弁12を開作動させ、圧
抜弁14を閉動作するように働く。
[Embodiments and their effects] In FIG. 1, 1 is a liquid supply container, 2 is a liquid receiving container,
Reference numeral 3 designates a once-through type steam generator, in which the liquid supply container 1 and the steam generator 3 are connected to a liquid supply pipe 5 and a pressure equalization valve 12 with a check valve 11 interposed therebetween, which allows flow only in the direction of the steam generator 3. It is connected with an intervening pressure equalizing pipe 6.
A steam pipe 7 receives the thermal energy of the heater 4 and sends out the steam generated by the steam generator 3. A condensing pipe 8 and an air release pipe 15 are attached to the upper part of the liquid receiving container 2. At the top of the liquid supply container 1, there is a float valve 1 connected to the bottom of the liquid receiving container 2.
A return liquid pipe 9 containing 0 is attached. The upper space of the liquid receiving container 2 and the upper space of the liquid supply container 1 are connected to an air suction pipe 1 which also serves as a pressure relief pipe with a pressure relief valve 14 interposed therebetween.
Connected by 3. Further, a liquid level detection device 16 is installed inside the liquid supply container 1. This liquid level detection device 16 operates to close the pressure equalizing valve 12 and open the pressure relief valve 14 with the low water level detection section 16b, and operates to open the pressure equalization valve 12 and open the pressure relief valve 14 with the high water level detection section 16a. Works to close.

次に上記実施例の動作について説明する。 Next, the operation of the above embodiment will be explained.

先ず給液容器1の水位が液位検知装置16の高
水位と低水位の中間にある場合、均圧弁12は開
の状態であり、圧抜弁14は閉の状態である。蒸
気発生器3は加熱器4の燃焼により熱エネルギー
を受け、発生した蒸気は蒸気管7より放熱器17
に送られる。放熱器17での放熱により生成した
凝縮液は凝縮液戻り管8を介して受液容器2に返
送される。蒸気発生器3で発生した蒸気の一部
は、この状態で均圧弁12は開であるため、均圧
管6を介して給液容器1の上部空間に流入し、前
回の落下還液の際、吸引・封入された空気を加温
する。このときの給液容器1の上部空間の圧力は
加温された空気の分圧と流入する蒸気が呈する分
圧の和となり、その圧力は蒸気発生器3の蒸気圧
と均圧となる。この圧力により大気解放されてい
る受液容器2の圧力と給液容器1との差圧が生じ
フロート弁10は閉止方向に押圧される。又、給
液容器1内の液体は沸点に達することなく、蒸気
発生器3の給水が保証され、給液管5を介して蒸
気発生器3に給水される。すなわち蒸気発生器3
で発生した蒸気の量だけ、蒸気発生器3の加熱管
の水位が減少し、給液容器1との間に水位差が生
じる。そのためヘツド差が生じ、給液容器1から
連続して蒸気発生器3に給水される。給液容器1
の水位は蒸気発生器3の継続運転に伴ない低下
し、液位検知装置16により低水位を検知され、
その信号が均圧弁12と圧抜弁14に送られ、均
圧弁12を閉にし、圧抜弁14を開にする。この
とき均圧弁12の閉により、蒸気発生器3は均圧
弁12と逆止弁11により給液容器1と切り離さ
れた状態となるが、蒸気発生器3の滞溜水を加熱
器4の燃焼により継続して蒸気を発生する。一方
均圧弁12の閉により、均圧管6を介しての給液
容器1の上部空間への蒸気の流入が止まり、同時
に圧抜弁14の開により、給液容器1の圧力は圧
抜管13を介して受液容器2に導かれ、大気に開
放される。そのため給液容器1の圧力が受液容器
2の圧力(大気圧)と等しくなつた時点で給液容
器1内のフロート弁10が受液容器2内の作動液
の重力により押し下げられ、受液容器2内の作動
液を還液管9を介して給液容器1内に落下還液す
る。又このとき、給液容器1内は冷却され負圧の
状態となり圧抜管を兼ねた空気吸引管13を介し
て空気を給液容器1の上部空間部に吸引・封入す
ることができる。給液容器1の水位が高水位に達
したら液位検知装置16により高水位が検知さ
れ、その信号が均圧弁12と圧抜弁14に送ら
れ、均圧弁12は開となり、圧抜弁14は閉とな
る。このため、蒸気発生器3で発生した蒸気の一
部は再び均圧管6を介して給液容器1の上部空間
に流入し、空気を加温して、給液容器1の圧力と
蒸気発生器3の圧力とが、給液容器1内の温度を
蒸気発生器3の蒸気温度よりも低い温度で等しい
圧力(均圧)にすることができ、フロート弁10
を押圧し、蒸気発生器3への給水を保証する。
First, when the water level of the liquid supply container 1 is between the high water level and the low water level of the liquid level detection device 16, the pressure equalization valve 12 is in an open state and the pressure relief valve 14 is in a closed state. The steam generator 3 receives thermal energy from the combustion of the heater 4, and the generated steam is passed through the steam pipe 7 to the radiator 17.
sent to. The condensate generated by heat dissipation in the radiator 17 is returned to the liquid receiving container 2 via the condensate return pipe 8 . Since the pressure equalization valve 12 is open in this state, a part of the steam generated in the steam generator 3 flows into the upper space of the liquid supply container 1 via the pressure equalization pipe 6, and during the previous falling liquid return. Heats the sucked and sealed air. At this time, the pressure in the upper space of the liquid supply container 1 is the sum of the partial pressure of the heated air and the partial pressure of the inflowing steam, and this pressure is equal to the steam pressure of the steam generator 3. This pressure creates a pressure difference between the pressure in the liquid receiving container 2, which is open to the atmosphere, and the liquid supply container 1, and the float valve 10 is pushed in the closing direction. Furthermore, the liquid in the liquid supply container 1 does not reach its boiling point, ensuring water supply to the steam generator 3, and is supplied to the steam generator 3 via the liquid supply pipe 5. That is, steam generator 3
The water level in the heating tube of the steam generator 3 decreases by the amount of steam generated, and a difference in water level with the liquid supply container 1 occurs. Therefore, a head difference occurs, and water is continuously supplied to the steam generator 3 from the liquid supply container 1. Liquid supply container 1
The water level decreases as the steam generator 3 continues to operate, and the low water level is detected by the liquid level detection device 16.
The signal is sent to the pressure equalization valve 12 and the pressure relief valve 14, causing the pressure equalization valve 12 to close and the pressure relief valve 14 to open. At this time, when the pressure equalization valve 12 is closed, the steam generator 3 is separated from the liquid supply container 1 by the pressure equalization valve 12 and the check valve 11. continuously generates steam. On the other hand, by closing the pressure equalizing valve 12, the flow of steam into the upper space of the liquid supply container 1 via the pressure equalizing pipe 6 is stopped, and at the same time, by opening the pressure relief valve 14, the pressure in the liquid supply container 1 is reduced via the pressure relief pipe 13. The liquid is introduced into the liquid receiving container 2 and exposed to the atmosphere. Therefore, when the pressure in the liquid supply container 1 becomes equal to the pressure (atmospheric pressure) in the liquid receiving container 2, the float valve 10 in the liquid supply container 1 is pushed down by the gravity of the hydraulic fluid in the liquid receiving container 2, and the receiving liquid is The working fluid in the container 2 falls into the liquid supply container 1 via the liquid return pipe 9 and is refluxed. Also, at this time, the inside of the liquid supply container 1 is cooled to a negative pressure state, and air can be sucked and sealed into the upper space of the liquid supply container 1 through the air suction pipe 13 which also serves as a pressure release pipe. When the water level in the liquid supply container 1 reaches a high water level, the high water level is detected by the liquid level detection device 16, and the signal is sent to the pressure equalization valve 12 and the pressure relief valve 14, and the pressure equalization valve 12 is opened and the pressure relief valve 14 is closed. becomes. Therefore, a part of the steam generated in the steam generator 3 flows into the upper space of the liquid supply container 1 again via the pressure equalization pipe 6, heats the air, and increases the pressure of the liquid supply container 1 and the steam generator. 3 can make the temperature inside the liquid supply container 1 equal pressure (equal pressure) at a temperature lower than the steam temperature of the steam generator 3, and the float valve 10
Press to ensure water supply to the steam generator 3.

[本発明の効果] 本発明は以上のように、給液容器に封入した空
気の分圧効果を利用しヘツド差による給液容器か
ら蒸気発生器への給水を行なう水頭還液と、給液
容器の作動液がなくなつた場合の、受液容器から
給液容器に重力により落下還液する重力還液を組
合せることにより、ポンプを使用することなく、
高圧の貫流ボイラである蒸気発生器に、給液容器
から給水することができ、又還液時には高圧の給
液容器に大気圧下の受液容器の作動液を落下還液
することができる、又、この還液時においても蒸
気を継続して発生することができる。
[Effects of the present invention] As described above, the present invention provides a water head return system that uses the partial pressure effect of the air sealed in the liquid supply container to supply water from the liquid supply container to the steam generator based on the head difference, and When the working fluid in the container runs out, by combining the gravity return liquid that falls back from the liquid receiving container to the liquid supply container by gravity, without using a pump,
Water can be supplied to the steam generator, which is a high-pressure once-through boiler, from the liquid supply container, and when liquid is returned, the working liquid in the liquid receiving container under atmospheric pressure can be dropped into the high-pressure liquid supply container and returned. Moreover, even during this liquid return, steam can be continuously generated.

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

第1図は本発明に係る循環装置の説明図、第
2,3図は従来例の循環装置の説明図である。 1……給液容器、2……受液容器、3……蒸気
発生器、4……加熱器、5……給液管、6……均
圧管、7……蒸気管、8……凝縮液戻り管、9…
…還液管、10……フロート弁、11……逆止
弁、12……均圧弁、13……圧抜管(空気吸引
管)、14……圧抜弁、15……大気開放管、1
6……液位検知装置、17……放熱器。
FIG. 1 is an explanatory diagram of a circulation device according to the present invention, and FIGS. 2 and 3 are explanatory diagrams of a conventional circulation device. 1...Liquid supply container, 2...Liquid receiving container, 3...Steam generator, 4...Heater, 5...Liquid supply pipe, 6...Pressure equalization pipe, 7...Steam pipe, 8...Condensation Liquid return pipe, 9...
...Return pipe, 10...Float valve, 11...Check valve, 12...Pressure equalization valve, 13...Pressure relief pipe (air suction pipe), 14...Pressure relief valve, 15...Atmospheric release pipe, 1
6...Liquid level detection device, 17...Radiator.

Claims (1)

【特許請求の範囲】[Claims] 1 加熱源を付属した蒸気発生器と蒸気発生器で
発生した蒸気を導いて気体又は液体に凝縮潜熱を
与える熱交換器と、その熱交換器内で凝縮した凝
縮液体を熱交換器内に圧送されてくる蒸気圧によ
り大気開放型の受液容器内に還液する還液管と、
前記受液容器とはフロート弁付の凝縮液送出管を
介して接続しており、かつ蒸気発生器とは凝縮液
供給管及び均圧管で結ばれていると共に液位検知
装置を取り付けた給液容器とからなる加熱用蒸気
の循環装置において、受液容器の上部空間と給液
容器の上部空間とを圧抜弁付の空気吸引管にて連
通すると共に、前記均圧管に均圧弁を取り付け、
給液容器に取り付けた液位検知装置において、下
位水位を検出したときに前記圧抜弁を開放し、均
圧弁を閉じ、上位水位を検出したときに圧抜弁を
閉じ、均圧弁を開放する構成として成る蒸気式加
熱装置における加熱用蒸気の循環装置。
1. A steam generator with a heating source attached, a heat exchanger that guides the steam generated by the steam generator to give latent heat of condensation to the gas or liquid, and pumps the condensed liquid condensed in the heat exchanger into the heat exchanger. a liquid return pipe that returns liquid into an atmosphere-open liquid receiving container due to the vapor pressure generated;
It is connected to the liquid receiving container through a condensate delivery pipe equipped with a float valve, and connected to the steam generator through a condensate supply pipe and a pressure equalization pipe, and is connected to a liquid supply pipe equipped with a liquid level detection device. In a heating steam circulation device consisting of a container, the upper space of the liquid receiving container and the upper space of the liquid supply container are communicated through an air suction pipe with a pressure relief valve, and a pressure equalizing valve is attached to the pressure equalizing pipe,
In the liquid level detection device attached to the liquid supply container, the pressure relief valve is opened and the pressure equalization valve is closed when a lower water level is detected, and the pressure relief valve is closed and the pressure equalization valve is opened when an upper water level is detected. A heating steam circulation device in a steam heating device consisting of:
JP13163886A 1986-06-06 1986-06-06 Circulation device for heating steam in steam heater Granted JPS62288422A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13163886A JPS62288422A (en) 1986-06-06 1986-06-06 Circulation device for heating steam in steam heater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13163886A JPS62288422A (en) 1986-06-06 1986-06-06 Circulation device for heating steam in steam heater

Publications (2)

Publication Number Publication Date
JPS62288422A JPS62288422A (en) 1987-12-15
JPH0252177B2 true JPH0252177B2 (en) 1990-11-09

Family

ID=15062735

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13163886A Granted JPS62288422A (en) 1986-06-06 1986-06-06 Circulation device for heating steam in steam heater

Country Status (1)

Country Link
JP (1) JPS62288422A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6349102U (en) * 1986-09-12 1988-04-02
KR101151771B1 (en) 2010-05-04 2012-05-31 신화에이치 주식회사 A hot water circulation device using the vapor pressure
KR101161677B1 (en) * 2010-12-28 2012-07-02 임주혁 Steam generator for automatic water supply which uses vapor pressure
KR101058430B1 (en) * 2010-12-28 2011-08-24 임주혁 Water supply pumping system for power station which uses vapor pressure
JP6063185B2 (en) * 2012-09-12 2017-01-18 関西熱化学株式会社 Coke oven combustion chamber cleaning apparatus and coke oven combustion chamber cleaning method
CN103697453B (en) * 2013-12-07 2016-04-06 唐升华 Steam generator

Also Published As

Publication number Publication date
JPS62288422A (en) 1987-12-15

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