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JPS6284230A - Single pipe steam conveying device - Google Patents

Single pipe steam conveying device

Info

Publication number
JPS6284230A
JPS6284230A JP22248485A JP22248485A JPS6284230A JP S6284230 A JPS6284230 A JP S6284230A JP 22248485 A JP22248485 A JP 22248485A JP 22248485 A JP22248485 A JP 22248485A JP S6284230 A JPS6284230 A JP S6284230A
Authority
JP
Japan
Prior art keywords
pipe
steam
heat
steam generator
condensate
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
JP22248485A
Other languages
Japanese (ja)
Inventor
Tatsuo Hattori
服部 達雄
Toshiaki Omori
敏明 大森
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 JP22248485A priority Critical patent/JPS6284230A/en
Publication of JPS6284230A publication Critical patent/JPS6284230A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 ・産業上の利用分野 本発明は、蒸気発生器内にて発生した熱媒蒸気を単一の
蒸気管を利用して放熱部内の放熱チューブまで導き、こ
の放熱チューブで周囲の流体に潜熱を与え、凝縮した凝
縮液を凝縮液溜に一旦ためておき、加熱を停止すること
により生ずる減圧作用により前記蒸気発生器に還流させ
、この繰り返しにより熱エネルギを輸送する単管式蒸気
搬送装置に関するものである。
[Detailed Description of the Invention] - Industrial Field of Application The present invention utilizes a single steam pipe to guide heat medium vapor generated in a steam generator to a heat radiation tube in a heat radiation section, and to conduct heat transfer with this heat radiation tube. A single pipe that gives latent heat to the surrounding fluid, temporarily stores the condensed liquid in a condensate reservoir, and returns it to the steam generator by the decompression effect generated by stopping heating, and transports thermal energy by repeating this process. The present invention relates to a type steam conveying device.

・従来技術とその問題点 第1図は従来の単管式蒸気搬送装置を示し、符号の1は
蒸気発生器であり、その内部には熱媒液2が封入されて
おり、6,7はそれぞれ熱媒液2の!IYを検出するた
めに蒸気発生器l内に取り付けられた高液位センサ及び
低液位センサである。3はバーナであり、4は燃料供給
管5の途中に設けた燃料弁である。20は放熱部であり
、その内部には放熱チューブ9が組み込まれている。1
2は凝縮液溜であり、その上部には大気との連通口13
がおいている。10は放熱チューブ9の出口と凝縮液溜
12の底部とを結ぶ凝縮液管である。8は蒸気発生器l
の頂部と放熱チューブ9の入口とを結ぶ蒸気管である。
・Prior art and its problems Figure 1 shows a conventional single-tube steam conveying device, where numeral 1 is a steam generator, inside of which a heat transfer liquid 2 is sealed, and 6 and 7 are steam generators. Each of heat transfer liquid 2! A high liquid level sensor and a low liquid level sensor installed within the steam generator l to detect IY. 3 is a burner, and 4 is a fuel valve provided in the middle of the fuel supply pipe 5. Reference numeral 20 denotes a heat dissipation section, in which a heat dissipation tube 9 is incorporated. 1
2 is a condensate reservoir, and the upper part thereof has a communication port 13 with the atmosphere.
is standing. 10 is a condensate pipe connecting the outlet of the heat dissipation tube 9 and the bottom of the condensate reservoir 12. 8 is the steam generator l
This is a steam pipe that connects the top of the tube and the inlet of the heat radiation tube 9.

22は蒸気発生器lの周囲に燃焼ガスが流れるように設
けた内胴、23は煙道、24は煙道に取り付けた燃焼フ
ァンでありモータ25により駆動される。21は制御装
置である。
22 is an inner shell provided so that combustion gas flows around the steam generator l; 23 is a flue; and 24 is a combustion fan attached to the flue, which is driven by a motor 25. 21 is a control device.

この従来例において運転スイッチを入れるとモータ25
に通電されて燃焼ファン24がバーナ3に空気を送り込
み、燃料弁4が開いて燃焼を開始し、蒸気発生器l内の
熱媒液2を加熱する。
In this conventional example, when the operation switch is turned on, the motor 25
is energized, the combustion fan 24 sends air into the burner 3, the fuel valve 4 opens and combustion starts, and the heat transfer liquid 2 in the steam generator 1 is heated.

蒸気発生器l内の圧力が大気圧以上となったときに熱媒
蒸気が蒸気管8を通って放熱部20内の放熱チューブ9
に送出され、熱媒蒸気は放熱チューブ9の周囲流体に潜
熱を与えて凝縮し、凝縮液は凝縮液管lOより凝縮液溜
12に吐出する。TM縮液′RB12内の凝縮液面にか
かる圧力は、大気a通口13により、常に大気圧に保た
れている。
When the pressure inside the steam generator l becomes equal to or higher than atmospheric pressure, the heat medium vapor passes through the steam pipe 8 to the heat radiation tube 9 in the heat radiation part 20.
The heat medium vapor imparts latent heat to the surrounding fluid of the heat dissipation tube 9 and is condensed, and the condensed liquid is discharged from the condensed liquid pipe IO to the condensed liquid reservoir 12. The pressure applied to the surface of the condensate in the TM condensate'RB12 is always maintained at atmospheric pressure by the atmosphere a vent 13.

蒸気発生器l内の熱媒液2の量が低液位センサ7の位置
以下になると、燃料弁4が閉止して蒸気発生器lの加熱
を停止し、燃焼ファン24により送り込まれる空気によ
って蒸気発生器lが強制冷却されて減圧状態が生ずる。
When the amount of heat transfer liquid 2 in the steam generator 1 falls below the level of the low liquid level sensor 7, the fuel valve 4 closes to stop heating the steam generator 1, and the air sent by the combustion fan 24 generates steam. The generator 1 is forced to cool down and a vacuum is created.

この減圧作用により、凝縮液溜12内にためられた凝縮
液が大気圧の作用下で凝縮液管lO1放熱チューブ9、
蒸気管8を通って蒸気発生器lに還流し、熱媒液量2が
高液位センサ6の位置以上になったときに燃料弁4を開
いて加熱を再開して、蒸気を再び送出するということの
綴り返しで、蒸気を放熱部に搬送するものであった。
Due to this pressure reduction action, the condensate accumulated in the condensate reservoir 12 is moved to the condensate pipe lO1, the heat dissipation tube 9,
The heat medium is returned to the steam generator l through the steam pipe 8, and when the heat medium liquid amount 2 reaches or exceeds the position of the high liquid level sensor 6, the fuel valve 4 is opened to resume heating and send out the steam again. In other words, the steam was conveyed to the heat dissipation section.

上記従来例では蒸気発生器l内の熱媒温度が蒸気発生器
体と平衡を保ちながら冷却するので、蒸気発生器体、蒸
気発生器内に残された熱媒液および蒸気発生器周囲をお
おう内胴が大気圧下での飽和温度以五に降下するまで蒸
気発生器内への還流が始まらず、還流を完了するのに長
時間を要するとともに、飽和温度に下げるため熱エネル
ギを放出しなければならないという問題があった。
In the above conventional example, the temperature of the heat medium inside the steam generator l is cooled while maintaining equilibrium with the steam generator body, so the steam generator body, the heat medium liquid left in the steam generator, and the surroundings of the steam generator are covered. Reflux into the steam generator does not begin until the inner shell falls below the saturation temperature at atmospheric pressure, and it takes a long time to complete the reflux, and thermal energy must be released to lower the temperature to the saturation temperature. There was a problem that it had to be done.

・本発明の目的 本発明は蒸気発生器の加熱停止時に極めて短い時間で凝
縮液を蒸気発生器内に還流させる単管式蒸気搬送装置を
提案するのが目的である。
-Object of the present invention The purpose of the present invention is to propose a single-tube steam conveying device that allows condensate to flow back into the steam generator in an extremely short period of time when heating of the steam generator is stopped.

番本発明の構成 本発明は上記目的を達成するために、単管式蒸気搬送装
置において、加熱源を有する蒸気発生器と、内部に放熱
チューブを組み込んで成る放熱部と、前記蒸気発生器内
で発生した蒸気を前記放熱部まで導く蒸気管と、前記放
熱チューブに至る蒸気管の一部から分岐された還流管と
、この蒸気管と量IR,管との分岐部において、蒸気管
内の熱媒温度が所定の温度以下のときに還流管側を開放
し、所定の温度以北のときに還流管側を閉止する熱動弁
と、前記還流管に接続され、出口が凝縮液溜内に開口し
た液管と、前記放熱チューブの出口と前記液管とを接続
している凝縮液管と、放熱チs−ブ側へ凝縮した熱媒が
逆流するのを防止するために前記凝縮液管に取り付けら
れた逆止弁と、から成る構成を採用した。
Structure of the present invention In order to achieve the above object, the present invention provides a single-tube steam conveying device, which includes a steam generator having a heating source, a heat radiating section incorporating a heat radiating tube inside the steam generator, A steam pipe that guides the steam generated in the heat radiation section to the heat radiation section, a reflux pipe branched from a part of the steam pipe leading to the heat radiation tube, and a reflux pipe that branches off from a part of the steam pipe leading to the heat radiation tube; A thermal valve that opens the reflux pipe side when the medium temperature is below a predetermined temperature and closes the reflux pipe side when the temperature is higher than the predetermined temperature; An open liquid pipe, a condensate pipe connecting the outlet of the heat radiation tube and the liquid pipe, and a condensate pipe to prevent the condensed heat medium from flowing back toward the heat radiation tube side. A configuration consisting of a check valve attached to the

上記装置は運転スイッチを入れると燃料弁が開いて蒸気
発生器内の熱媒液が加熱され、熱媒蒸気は蒸気管を介し
て放熱部内の放熱チューブに送出される。放熱チューブ
入口に取り付けられた熱動弁は設定温度以上の流体に触
れると閉屯し、設定温度以下の場合は開放するようにな
っているので、熱媒蒸気が放熱部に到達すると熱動弁は
閉止して、熱媒蒸気は放熱チューブに導かれ、周囲流体
に潜熱を与えて凝縮する。凝縮した熱媒液は放熱チュー
ブ出口に接続された凝縮液管より凝縮液溜に吐き出され
る。
When the device described above is turned on, the fuel valve opens and the heat medium liquid in the steam generator is heated, and the heat medium vapor is sent through the steam pipe to the heat radiation tube in the heat radiation section. The thermal valve installed at the inlet of the heat dissipation tube closes when it comes into contact with fluid above the set temperature, and opens when the temperature is below the set temperature, so when heat medium vapor reaches the heat dissipation section, the thermal valve closes. is closed, and the heat medium vapor is led to the heat dissipation tube, imparting latent heat to the surrounding fluid and condensing it. The condensed heat transfer liquid is discharged into a condensate reservoir from a condensate pipe connected to an outlet of the heat radiation tube.

還流管の途中に設けられた逆止弁は、熱媒流人時に熱動
弁が閉止するまでの時間、および熱動弁のリークによっ
て生ずる蒸気流が還流管を通って凝縮液溜に流出するの
を防ぐ。
A check valve installed in the middle of the reflux pipe is used to control the time until the thermal valve closes when the heat medium flows, and the steam flow generated by the leakage of the thermal valve to flow out into the condensate reservoir through the reflux pipe. prevent

蒸気発生器内の熱媒液量が所定の量にまで減少すると、
燃料弁が閉じる。このとき、放熱チューブ内の圧力は急
激に減じて、凝縮液管の途中に取り付けられた逆止弁が
閉じて大気との連通を断つ。熱動弁は通過流体温度が8
5℃程度に降下するまで閉止状態を維持するように働く
、蒸気発生器と放熱チューブとは大気との連通を断たれ
ている六めに、各々の温度に基づく飽和蒸気圧をもつこ
とになり、この飽和蒸気圧差により、蒸気発生器内の蒸
気は放熱チューブに流入し、蒸気発生器内の熱媒温度は
急降下し、従って圧力も急減するので、熱動弁を通過す
る熱媒蒸気温度が約85℃になったとき熱動弁が開き、
凝縮液溜にためられていた凝縮液は大気圧の作用下で還
流管および蒸気管を通って蒸気発生器に戻される。熱媒
液が蒸気発生器に還流後、燃料弁を開き熱媒を加熱して
、再び蒸気を放熱部に送出する。このように、本発明は
ポンプを使用しない単管の間欠蒸気搬送装置において、
還流時間ならびに還流時の熱エネルギ損失を最小にし、
運転率を向上させるという効果をもたらすものである。
When the amount of heat transfer liquid in the steam generator decreases to a predetermined amount,
Fuel valve closes. At this time, the pressure inside the heat radiation tube decreases rapidly, and the check valve installed in the middle of the condensate tube closes, cutting off communication with the atmosphere. Thermal valves have a passing fluid temperature of 8
The steam generator and heat dissipation tube, which work to maintain a closed state until the temperature drops to about 5℃, are cut off from communication with the atmosphere.Sixth, each has a saturated vapor pressure based on its temperature. Due to this saturated vapor pressure difference, the steam in the steam generator flows into the heat dissipation tube, and the temperature of the heat medium in the steam generator drops rapidly, so the pressure also drops sharply, so the temperature of the heat medium vapor passing through the thermal valve decreases. The thermal valve opens when the temperature reaches approximately 85℃.
The condensate stored in the condensate reservoir is returned to the steam generator under the influence of atmospheric pressure through the reflux pipe and the steam pipe. After the heating medium liquid returns to the steam generator, the fuel valve is opened to heat the heating medium and send the steam to the heat radiation section again. As described above, the present invention provides a single pipe intermittent steam conveying device that does not use a pump.
Minimizes reflux time and thermal energy loss during reflux,
This has the effect of improving operating efficiency.

・実施例 第2図は上記本発明の一実施例を示すものであり、符号
の1は内部を密閉した蒸気発生器であり、その内部には
熱媒液2が封入されており、6.7はそれぞれ熱媒液2
の量を検出するために蒸気発生器1に取り付けられた高
液位センサと低液位センサである。
・Embodiment FIG. 2 shows an embodiment of the present invention, in which reference numeral 1 denotes a steam generator whose interior is sealed, in which a heat transfer liquid 2 is sealed; 6. 7 are respectively heat transfer liquids 2
A high liquid level sensor and a low liquid level sensor are attached to the steam generator 1 to detect the amount of water.

3はバーナであり、4は燃料供給管5の途中に設けた燃
料弁である。
3 is a burner, and 4 is a fuel valve provided in the middle of the fuel supply pipe 5.

20は放熱部であり、その内部には放熱チューブ9が組
み込まれている。8は蒸気発生器lの頂部と放熱部とを
連結する蒸気管である。放熱チューブ9の入口には熱動
弁16が取り付けられている。15は熱動弁16より分
岐する還流管であり、還流管15の一部に逆止弁17が
取り付けられている。18’aは熱動弁の感温部であり
、その先に弁棒tabが取り付けられ、弁棒先端の弁栓
と弁座19とが密着して閉止する構造になっている。
Reference numeral 20 denotes a heat dissipation section, in which a heat dissipation tube 9 is incorporated. 8 is a steam pipe connecting the top of the steam generator 1 and the heat radiation section. A thermal valve 16 is attached to the inlet of the heat radiation tube 9. Reference numeral 15 denotes a reflux pipe branching from the thermal valve 16, and a check valve 17 is attached to a part of the reflux pipe 15. Reference numeral 18'a denotes a temperature-sensing part of the thermal valve, and a valve stem tab is attached to the tip of the temperature-sensing part, so that the valve stopper at the tip of the valve stem and the valve seat 19 are in close contact with each other to close the valve.

放熱チューブ9の出口は凝縮液管10に接続しており、
凝縮液管10の一部に逆止弁11が取り付けられている
。14は液管であり、一端が凝縮液溜12の底部に開口
し、他端は凝縮液管lOおよび還流管15の末端に連結
している。13は凝縮液溜12の上部に設けられた大気
との連通口である。22は蒸気発生器lの周囲に燃焼ガ
スが流れるように設けられた内胴、23は煙道、24は
煙道に取り付けられた燃焼ファンであり、モータ25に
より駆動される。21は制御装置である。
The outlet of the heat dissipation tube 9 is connected to the condensate pipe 10,
A check valve 11 is attached to a part of the condensate pipe 10. Reference numeral 14 denotes a liquid pipe, one end of which opens at the bottom of the condensate reservoir 12, and the other end connected to the ends of the condensate pipe IO and the reflux pipe 15. Reference numeral 13 denotes a communication port with the atmosphere provided at the upper part of the condensate reservoir 12. 22 is an inner shell provided so that combustion gas flows around the steam generator l, 23 is a flue, and 24 is a combustion fan attached to the flue, which is driven by a motor 25. 21 is a control device.

実施例は以上のような構成から成り、次にその運転例を
説明する。
The embodiment has the above configuration, and an example of its operation will be explained next.

装置を設置後、初めて運転する際には、蒸気発生器1.
蒸気管8.放熱チューブ9、凝縮液管lO1還流管15
、液管14の合計容積に、凝縮液溜12の開口13から
大気への蒸発減量を見込んだ容積を加えた量の熱媒液を
用意し、この熱媒液を蒸気発生器l内に高液位センサ6
以上の液量となるように注入し、残贋を凝縮液溜12内
に注ぎ込む、J!l!転スイッチを入れると、燃料弁4
が開いてバーナ3にて燃焼を開始し、蒸気発生器l内の
熱媒液2を加熱する。熱媒液2が大気圧における飽和温
度に達すると、蒸気が発生し、蒸気発生器1内の上部空
間、蒸気管8.放熱チューブ9、凝縮液管10、液管1
4内の空気は蒸気により開口13から大気中に排出され
る。
When operating the device for the first time after installation, the steam generator 1.
Steam pipe8. Heat dissipation tube 9, condensate pipe 1O1 reflux pipe 15
, prepare a heat medium liquid in an amount equal to the total volume of the liquid pipes 14 plus the volume that takes into account the evaporation loss from the opening 13 of the condensate reservoir 12 to the atmosphere, and add this heat medium liquid to the steam generator l. Liquid level sensor 6
Pour the remaining liquid into the condensate reservoir 12, J! l! When the switch is turned on, the fuel valve 4
opens, the burner 3 starts combustion, and heats the heat transfer liquid 2 in the steam generator 1. When the heat transfer liquid 2 reaches the saturation temperature at atmospheric pressure, steam is generated and flows through the upper space in the steam generator 1 and the steam pipe 8. Heat dissipation tube 9, condensate pipe 10, liquid pipe 1
The air in the chamber 4 is discharged into the atmosphere through the opening 13 as steam.

蒸気発生器1内の熱媒液2の級が低液位センナ7以下に
減少すると、燃料弁4が閉じ蒸気発生器l内が減圧して
、凝縮液溜12内にためられた熱媒液2は蒸気発生器l
に流入し、蒸気管8、放熱チューブ9.凝縮液管101
M流管15、液管14は熱媒液2で満たされ、凝縮液溜
12内には、液管14の末端開口が凝縮液2a(熱媒液
2)の中に挿入された状態で少量残される0通常の運転
時において、運転スイッチを入れると燃焼ファン24が
回転して空気をバーナ3に送り込み、次いで燃料弁4が
開いて、蒸気発生器1内の熱媒液2を加熱する。熱媒液
2の温度が大気圧下の飽和温度に達すると蒸気が発生し
始め、蒸気管8、放熱チューブ9内の熱媒液2を凝縮液
溜12に排除し、蒸気が放熱チューブ9に到達する。蒸
気は放熱チューブ9内を通過しながら潜熱を周囲流体に
与えて凝縮する。放熱チューブ9の後段では、凝縮液2
aの顕然の一部を周囲流体に伝熱して、温度降下する。
When the level of the heat medium liquid 2 in the steam generator 1 decreases to below the low liquid level sensor 7, the fuel valve 4 closes and the pressure inside the steam generator 1 is reduced, and the heat medium liquid accumulated in the condensed liquid reservoir 12 is removed. 2 is the steam generator l
, steam pipe 8, heat dissipation tube 9. Condensate pipe 101
The M flow pipe 15 and the liquid pipe 14 are filled with the heat transfer liquid 2, and the condensate reservoir 12 contains a small amount of liquid with the end opening of the liquid pipe 14 inserted into the condensate liquid 2a (heat transfer liquid 2). During normal operation, when the operation switch is turned on, the combustion fan 24 rotates to feed air into the burner 3, and then the fuel valve 4 opens to heat the heat transfer liquid 2 in the steam generator 1. When the temperature of the heat transfer liquid 2 reaches the saturation temperature under atmospheric pressure, steam starts to be generated, and the heat transfer liquid 2 in the steam pipe 8 and the heat radiation tube 9 is expelled to the condensed liquid reservoir 12, and the steam flows into the heat radiation tube 9. reach. While passing through the heat dissipation tube 9, the steam imparts latent heat to the surrounding fluid and condenses. At the latter stage of the heat dissipation tube 9, the condensate 2
A significant portion of the heat is transferred to the surrounding fluid, resulting in a temperature drop.

放熱チューブ9の出口は、途中に逆止弁11を介装した
凝縮液管lOに接続しており、凝縮液2at−凝縮液溜
12内に吐き出す、還流管15には、熱動弁16および
逆止弁17のため蒸気は流れない、凝縮液溜12内の凝
縮液2aの表面にかかる圧力は、開口13により常に大
気圧に保たれている。
The outlet of the heat dissipation tube 9 is connected to a condensate pipe 10 with a check valve 11 interposed in the middle, and the reflux pipe 15, which discharges the condensate 2at into the condensate reservoir 12, has a thermal valve 16 The check valve 17 prevents steam from flowing, and the pressure applied to the surface of the condensate 2a in the condensate reservoir 12 is always maintained at atmospheric pressure by the opening 13.

蒸気発生器l内の熱媒液2が低液位センサ7の位置にま
で減量すると、燃料弁4が閉じて熱媒液2の加熱を中断
する。この時、放熱部20に組み込まれた放熱チューブ
9内の圧力は急減し、逆止弁11が閉じて大気との連通
状態を断つ、放熱チューブ9の入口に取り付けられた熱
動弁16は通過流体温度がたとえば85℃以下になった
とき、還流管15を経由して凝縮液溜12から蒸気管8
方向への流路を開くように設定されている。
When the heat medium liquid 2 in the steam generator 1 decreases to the position of the low liquid level sensor 7, the fuel valve 4 closes and the heating of the heat medium liquid 2 is interrupted. At this time, the pressure inside the heat dissipation tube 9 built into the heat dissipation section 20 decreases rapidly, and the check valve 11 closes to cut off communication with the atmosphere.The thermal valve 16 attached to the inlet of the heat dissipation tube 9 passes through. When the fluid temperature drops to, for example, 85°C or lower, the steam pipe 8 is routed from the condensate reservoir 12 via the reflux pipe 15.
It is set to open a flow path in the direction.

蒸気発生器lと放熱チューブ9は大気との連通を完全に
断たれているので、各々の温度における飽和蒸気圧をも
つことになり、温度の高い蒸気発生器lから、温度の低
い放熱チューブ9に向かって蒸気が流出して蒸気発生器
l内の熱媒が急冷し、従って急速に減圧する。熱媒蒸気
温度が85℃にまで降下したとき感温部18aが収縮し
て弁を開き、凝縮液2aは大気圧の作用下で凝縮液溜1
2から還流管15、蒸気管8を通って蒸気発生器lに還
流し、蒸気発生器1内の熱媒液2の量が高液位センサ位
置6にまで戻ったときに燃料弁4を開けて、熱媒液2の
加熱を再開する。蒸気発生器l内への還流量が1/3か
ら172の時点で加熱を再開しても、還流する熱媒液2
の温度が低いために、蒸気発生器lの減圧状態は保たれ
、送出熱媒体の全量が還流するのに何の妨げにもならな
い。
Since the steam generator l and the heat radiation tube 9 are completely cut off from communication with the atmosphere, they have saturated vapor pressures at each temperature. The steam flows out towards the steam generator 1, and the heating medium in the steam generator 1 is rapidly cooled, and therefore the pressure is rapidly reduced. When the heat medium vapor temperature drops to 85°C, the temperature sensing part 18a contracts and opens the valve, and the condensate 2a flows into the condensate reservoir 1 under the action of atmospheric pressure.
2 through the reflux pipe 15 and the steam pipe 8 to the steam generator 1, and when the amount of the heat transfer liquid 2 in the steam generator 1 returns to the high level sensor position 6, the fuel valve 4 is opened. Then, heating of the heat transfer liquid 2 is restarted. Even if heating is restarted when the amount of reflux into the steam generator 1 is between 1/3 and 172, the refluxing heat medium liquid 2
Due to the low temperature of the steam generator 1, the vacuum state of the steam generator 1 is maintained, and there is no obstacle to the reflux of the entire amount of the delivered heat transfer medium.

第3図は実施例の運転時に得られたデータであり、横軸
に運転スイッチ投入後の時間経過をとり、排ガス温度、
蒸気発生器内温度、蒸気発生器内圧力、累積熱媒送出量
の変化を示している。熱媒としては水を用い、出力25
00kcalハの蒸気発生器と、放熱窓とを内径7m膳
、長さlOmの単管で結んだ暖房機の例である。運転ス
イッチを入れてから2分45秒後に蒸気発生器l内の熱
媒温度が100℃に達し、蒸気管8、放熱チューブ9内
の熱媒液2を排出後10分間安定的に蒸気を送出する。
Figure 3 shows the data obtained during operation of the example, and the horizontal axis shows the elapsed time after turning on the operation switch, and the exhaust gas temperature,
It shows changes in the temperature inside the steam generator, the pressure inside the steam generator, and the cumulative amount of heat medium delivered. Water is used as the heat medium, output 25
This is an example of a heating machine in which a 00 kcal steam generator and a heat dissipation window are connected by a single pipe with an inner diameter of 7 m and a length of 10 m. Two minutes and 45 seconds after turning on the operation switch, the heat medium temperature in the steam generator l reaches 100°C, and after discharging the heat medium liquid 2 in the steam pipe 8 and heat radiation tube 9, steam is stably sent out for 10 minutes. do.

蒸気発生初期に蒸気発生器1内の温度、圧力がやや高い
のは、熱媒液2の排出のためであり、累積熱媒送出量の
傾きが急なのは、熱媒液2が蒸気に変わるとき急膨張し
て、まわりの熱媒液2を蒸気発生器lから排除するため
である。蒸気送出開始後10分経つと、燃料弁4が閉じ
、その直後逆止弁11が閉じる。蒸気発生器lと放熱チ
ューブ9内の熱媒温度の差違により、蒸気はなおも蒸気
発生器lから放熱チューブ9に送出されるため蒸気発生
器l内の圧力、温度ともに急減し、熱動弁16を通過す
る熱媒蒸気温度が85℃程度にまで下がったところで熱
動弁16が開く。
The reason why the temperature and pressure inside the steam generator 1 are slightly high at the beginning of steam generation is due to the discharge of the heat medium liquid 2, and the reason why the slope of the cumulative heat medium delivery amount is steep is when the heat medium liquid 2 changes to steam. This is because it rapidly expands and expels the surrounding heat transfer liquid 2 from the steam generator 1. Ten minutes after the start of steam delivery, the fuel valve 4 closes, and immediately after that, the check valve 11 closes. Due to the difference in heat medium temperature between the steam generator 1 and the heat radiation tube 9, steam is still sent from the steam generator 1 to the heat radiation tube 9, so the pressure and temperature inside the steam generator 1 rapidly decrease, causing the thermal valve to Thermal valve 16 opens when the temperature of the heat medium vapor passing through 16 drops to about 85°C.

蒸気発生器内の熱媒は飽和状態とみなせるので、このと
き約0.6kg/cm(ab)に減圧している。大気圧
を液面に受けている凝縮液溜12内にためられたa線源
2aは液管14、還流管15、蒸気管8を通っ□て、3
0秒間で送出された熱媒の全量が蒸気発生器lに還流し
終わる。この間排ガス温度は下がり続けているもののt
to’c程度にしかならず、内胴22など蒸気発生器l
の周囲温度は100°Cよりもかなり高い温度になって
いることを示している。
Since the heat medium in the steam generator can be considered to be in a saturated state, the pressure is reduced to approximately 0.6 kg/cm (ab) at this time. The a-ray source 2a stored in the condensate reservoir 12, whose liquid surface is exposed to atmospheric pressure, passes through the liquid pipe 14, the reflux pipe 15, and the steam pipe 8 to the 3
The entire amount of the heat medium sent out in 0 seconds finishes returning to the steam generator 1. Although the exhaust gas temperature continues to fall during this period,
The steam generator such as the inner shell 22
This indicates that the ambient temperature is considerably higher than 100°C.

蒸気発生器l内の熱媒液2の量が高液位センサ6の位置
にまで回復したとき、燃料弁4が開き加熱を再開する。
When the amount of heat transfer liquid 2 in the steam generator 1 has recovered to the position of the high liquid level sensor 6, the fuel valve 4 opens and heating resumes.

燃焼停止時間は30秒程度である。還流した熱媒液温は
60℃程度であり、蒸気の再送出にまで要する加熱時間
は1分30秒であり、従って蒸気送出の中断時間は約2
分である。
The combustion stop time is about 30 seconds. The temperature of the refluxed heat medium liquid is approximately 60°C, and the heating time required to send out the steam again is 1 minute and 30 seconds. Therefore, the interruption time for steam delivery is approximately 2 minutes.
It's a minute.

第4図は従来例の運転時のデータである。FIG. 4 shows data during operation of the conventional example.

燃焼停止後、蒸気発生器l内の熱媒液2は放熱チューブ
9の末端が凝縮液管lOを通じて大気に開放されている
ので、100℃にまでは急速に低下するものの、内胴2
2など蒸気発生器lの周囲の温度と平衡しながら冷却さ
れるため、排ガス温度が100℃以下に下がるまでの約
1分30秒間は100℃に保たれ排ガス温度が100℃
以下になって、ようやく飽和状態にある蒸気発生器1内
が減圧して還流が始まる。
After the combustion is stopped, the heat transfer liquid 2 in the steam generator 1 is exposed to the atmosphere through the condensate pipe 10 at the end of the heat dissipation tube 9, so although the temperature rapidly drops to 100°C, the inner shell 2
2 etc. Since the steam generator is cooled in equilibrium with the surrounding temperature, the exhaust gas temperature is maintained at 100°C for about 1 minute and 30 seconds until it drops below 100°C.
At this point, the pressure inside the steam generator 1, which is in a saturated state, is finally reduced and reflux begins.

′i;1流を終了するまでに2分30秒かかっており、
蒸気送出中断時間は4分である。
'i; It took 2 minutes and 30 seconds to finish the first class,
The steam delivery interruption time is 4 minutes.

第2図に示す本発明の第2の実施例の運転データと比較
すると1本発明による単管式蒸気搬送装置をmmいると
、従来例に比べて、還流時間が150秒から50秒へと
173に、蒸気送出中断時間は4分から2分へと172
に、また燃焼中断時間は130秒から30秒へとl/4
に大幅に短縮されていることがわかる。
Comparing with the operational data of the second embodiment of the present invention shown in Fig. 2, when the single-tube steam conveying device according to the present invention is 1 mm, the reflux time is reduced from 150 seconds to 50 seconds compared to the conventional example. 173, the steam delivery interruption time was increased from 4 minutes to 2 minutes 172
In addition, the combustion interruption time was increased from 130 seconds to 30 seconds by l/4.
It can be seen that it has been significantly shortened.

なお、本発明によれば蒸気発生器1内の減圧は内胴22
など蒸気発生器lの周囲と温度的な平衡を保ちながら生
ずるものではなく、放熱チューブ9内への蒸気の流出に
より生ずるものであるから、還流時に燃焼ファン24を
停止しても、還流時間にはほとんど影響が現れないので
、燃焼ファン24の運転を燃料弁4の開閉と連動させる
ようにしてもよい。
According to the present invention, the pressure inside the steam generator 1 is reduced by the inner shell 22.
This is not generated while maintaining temperature equilibrium with the surroundings of the steam generator l, but is generated due to the outflow of steam into the heat radiation tube 9. Therefore, even if the combustion fan 24 is stopped during the reflux time, the reflux time Since this has almost no effect, the operation of the combustion fan 24 may be linked to the opening and closing of the fuel valve 4.

熱動弁16としては、ベローズ弁、ワックス弁、バイメ
タル弁等が利用できる。
As the thermal valve 16, a bellows valve, a wax valve, a bimetallic valve, etc. can be used.

・本発明の効果 本発明の構成と作用は以上のごときものであり、次のよ
うな効果が得られる。
- Effects of the present invention The structure and operation of the present invention are as described above, and the following effects can be obtained.

a、燃焼停止時、蒸気発生器および放熱チューブと大気
との連通状態を一定時間遮断する間に、蒸気発生器から
放熱チューブに向って蒸気が流出することにより生ずる
急速な減圧作用を凝縮液の還流に利用しているため、還
流時間の大幅な短縮化が実現できる。
a. When combustion is stopped, the communication between the steam generator and the heat dissipation tube is cut off for a certain period of time, and the rapid decompression effect caused by the steam flowing out from the steam generator toward the heat dissipation tube is applied to the condensate. Since it is used for reflux, the reflux time can be significantly shortened.

b、燃焼停止時間が短縮化されたので、還流時のエネル
ギ損失が極めて小さくなり、運転率の向上も図れる。
b. Since the combustion stop time is shortened, the energy loss during reflux becomes extremely small, and the operating rate can also be improved.

C6ポンプを使用せずに弁の開閉のみによる蒸気搬送装
置なので、低廉なる蒸気媒体熱利用システムを構成する
ことができる。
Since the steam transfer device does not use a C6 pump and only operates by opening and closing valves, an inexpensive steam medium heat utilization system can be constructed.

d、蒸気発生器と放熱部は一本の蒸気管で熱媒を搬送す
るので施工性が非常によくなる。
d. Since the steam generator and the heat radiating section convey the heat medium through a single steam pipe, workability is greatly improved.

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

第1図は本発明に係る単管式蒸気搬送装置の説明図、第
2図は従来の単管式蒸気搬送装置の説明図、第3図は本
発明の実施例に係る装置の運転データ図、第4図は従来
例の運転データ図である。 ■・・・・・・蒸気発生器、  3・・・・・・バーナ
、8・・・・・・蒸気管、   、9・・・・・・放熱
チューブ、lO・・・・・・凝縮液管、  11・・・
逆止弁。 12・・・・・・凝縮液溜、  13・・・・・・連通
口、14・・・・・・液管、    15・・・・・・
量流管、16・・・・・・熱動弁、   21・・・・
・・制御装置、22・・・・・・内胴、    23・
・・・・・煙道、24・・・・・・燃焼ファン、25・
・・・・・モータ。 i 7’ [kg76rrI2febll逼L[0C1 累翻IL!tht [kgl
FIG. 1 is an explanatory diagram of a single-pipe steam conveying device according to the present invention, FIG. 2 is an explanatory diagram of a conventional single-pipe steam conveying device, and FIG. 3 is an operational data diagram of the device according to an embodiment of the present invention. , FIG. 4 is an operational data diagram of a conventional example. ■...Steam generator, 3...Burner, 8...Steam pipe, 9...Radiation tube, lO...Condensate Tube, 11...
non-return valve. 12... Condensate reservoir, 13... Communication port, 14... Liquid pipe, 15...
Volume flow pipe, 16... thermal valve, 21...
...Control device, 22...Inner shell, 23.
... Flue, 24 ... Combustion fan, 25.
·····motor. i 7' [kg76rrI2febll〼L[0C1 repeated translation IL! tht [kgl

Claims (1)

【特許請求の範囲】 1、加熱源を有する蒸気発生器と、 内部に放熱チューブを組み込んで成る放熱部と、前記蒸
気発生器内で発生した蒸気を前記放熱部まで導く蒸気管
と、 前記放熱チューブに至る蒸気管の一部から分岐された還
流管と、 この蒸気管と還流管との分岐部において、蒸気管内の熱
媒温度が所定の温度以下に降下したときに還流管側を開
放し、所定の温度以上のときに還流管側を閉止する熱動
弁と、 前記還流管に接続され、出口が前記蒸気液溜内に開口し
た液管と、 前記放熱チューブの出口と前記液管とを接続している凝
縮液管と、 前記凝縮液管内に放熱チューブ側へ凝縮した熱媒が逆流
するのを防止するために取り付けられた逆止弁と、 から成る単管式蒸気搬送装置。 2、還流管の一部に蒸気の流れを止め、凝縮した熱媒の
流れを開放する逆止弁を取り付けて成る特許請求の範囲
第1項記載の単管式蒸気搬送装置。
[Scope of Claims] 1. A steam generator having a heating source; a heat radiating section incorporating a heat radiating tube therein; a steam pipe guiding steam generated in the steam generator to the heat radiating section; and the heat radiating section. A reflux pipe branches off from a part of the steam pipe leading to the tube, and at the branch point between this steam pipe and the reflux pipe, the reflux pipe side is opened when the temperature of the heat medium in the steam pipe falls below a predetermined temperature. , a thermal valve that closes the reflux pipe side when the temperature is higher than a predetermined temperature; a liquid pipe connected to the reflux pipe and having an outlet opening into the vapor reservoir; and an outlet of the heat radiation tube and the liquid pipe. A single-pipe steam transfer device comprising: a condensate pipe that connects the condensate pipe; and a check valve installed in the condensate pipe to prevent the condensed heat medium from flowing back toward the heat radiation tube side. 2. The single-pipe steam transfer device according to claim 1, wherein a check valve is attached to a part of the reflux pipe to stop the flow of steam and release the flow of the condensed heating medium.
JP22248485A 1985-10-04 1985-10-04 Single pipe steam conveying device Pending JPS6284230A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22248485A JPS6284230A (en) 1985-10-04 1985-10-04 Single pipe steam conveying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22248485A JPS6284230A (en) 1985-10-04 1985-10-04 Single pipe steam conveying device

Publications (1)

Publication Number Publication Date
JPS6284230A true JPS6284230A (en) 1987-04-17

Family

ID=16783151

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22248485A Pending JPS6284230A (en) 1985-10-04 1985-10-04 Single pipe steam conveying device

Country Status (1)

Country Link
JP (1) JPS6284230A (en)

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