JPH0723763B2 - Steam generator - Google Patents
Steam generatorInfo
- Publication number
- JPH0723763B2 JPH0723763B2 JP22419286A JP22419286A JPH0723763B2 JP H0723763 B2 JPH0723763 B2 JP H0723763B2 JP 22419286 A JP22419286 A JP 22419286A JP 22419286 A JP22419286 A JP 22419286A JP H0723763 B2 JPH0723763 B2 JP H0723763B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- pipe
- steam
- liquid
- solenoid valve
- 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 - Fee Related
Links
Description
【発明の詳細な説明】 産業上の利用分野 この発明は、気体又は液体等に蒸気の凝縮潜熱を与えて
加熱する蒸気発生装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam generator that applies vapor latent heat of vapor to a gas or a liquid to heat it.
従来の技術 蒸気の凝縮潜熱を利用して気体又は液体等を加熱する蒸
気発生装置としては、蒸気アイロン等の加熱源に用いる
蒸気消費型のものと、暖房器、湯沸器等の加熱源に用い
る蒸気循環型のものとがあるが、いずれも給水の水垢、
給水中に含有する鉄分等のスケールが蒸気発生器の各機
器配管各部に付着、滞積して熱伝導が悪くなるばかりで
なく蒸気発生ボイラーの吸熱管又は配管等が閉塞するこ
とがあり、上記スケールは蒸気発生ボイラー等の高熱部
に多く発生し、軟水に比べ硬水に多く含まれている。2. Description of the Related Art As a steam generator for heating a gas or a liquid by utilizing latent heat of condensation of steam, a steam consuming type used for a heating source such as a steam iron and a heating source for a heater, a water heater, etc. There is a steam circulation type used, but both are scales of water supply,
The scale of iron, etc. contained in the water supply adheres to and accumulates on each part of each equipment pipe of the steam generator, which not only deteriorates heat conduction but also may block the heat absorption pipe or piping of the steam generation boiler. A large amount of scale is generated in high heat areas such as steam generating boilers, and is contained in hard water more than in soft water.
そこで、従来技術の一例として、たとえば、第4図に示
されている蒸気循環型の蒸気発生装置は、ガスバーナ等
の加熱器(110)による加熱で蒸気を発生する蒸気発生
ボイラー(103)と、該蒸気発生ボイラー(103)によつ
て発生した蒸気を蒸気管(111)を介して熱交換器(10
4)に送りその凝縮潜熱を冷水に与えて加熱し、ここで
生成する凝縮液を還流管(112)を介して還流貯溜し大
気開放口(113)により大気に開放された受液槽(105)
と、該受液槽(105)と上端の空気吸入口(114)を受液
槽(105)の上部空間(115)に臨ませた凝縮液送出管
(106)により連通した給液槽(107)と、該凝縮液送出
管(106)の給液槽(107)内に位置する下部開口部(11
6)に装備せるフロート弁(V06)と、給液槽(107)の
低液位(a)と高液位(b)を水位センサー(117),
(118)によつて検知することにより開閉し蒸気圧の
給、断を行う開閉弁(V01)を備え蒸気発生ボイラー(1
03)の管寄せ部(119)と給液槽(107)の上部空間の空
気室(120)を連通する均圧管(108)と、蒸気発生ボイ
ラー(103)からの逆流を阻止する逆止弁(V07)を備え
蒸気発生ボイラー(103)の下部溜部(121)と給液槽
(107)の下部を連通する給水導管(109)とからなつて
おり、スケールの洗浄機能は全く備えていない。Therefore, as an example of a conventional technique, for example, a steam circulation type steam generator shown in FIG. 4 includes a steam generating boiler (103) for generating steam by heating by a heater (110) such as a gas burner, Steam generated by the steam generating boiler (103) is passed through a steam pipe (111) to a heat exchanger (10
4), the latent heat of condensation is given to cold water to heat it, and the condensate produced here is reflux-stored through a reflux pipe (112) and is opened to the atmosphere by an atmosphere opening port (113). )
And a liquid supply tank (107) in which the liquid reception tank (105) and the air intake port (114) at the upper end communicate with each other through a condensate delivery pipe (106) facing the upper space (115) of the liquid reception tank (105). ) And a lower opening (11) located in the liquid supply tank (107) of the condensate delivery pipe (106).
6) equipped with a float valve (V 06 ), a liquid level sensor (117) with a low liquid level (a) and a high liquid level (b) in the liquid supply tank (107),
(118) is equipped with an on-off valve (V 01 ) that opens and closes by supplying and disconnecting steam pressure by detecting with a steam generation boiler (1
The pressure equalizing pipe (108) that connects the pipe drawing part (119) of 03) and the air chamber (120) of the upper space of the liquid supply tank (107), and the check valve that blocks the reverse flow from the steam generating boiler (103). (V 07 ), which consists of the lower reservoir (121) of the steam generating boiler (103) and the water supply conduit (109) that connects the lower part of the liquid supply tank (107), and has no scale cleaning function. Absent.
上記蒸気発生装置においては、給水に含まれるスケール
成分により熱伝導が悪くなるばかりでなく、遂には吸熱
管又は配管時を閉塞するに至るという欠点があるため、
スケール成分を取除くための浄水器を組込んでそのイオ
ン交換樹脂によつて給水中のスケール成分を分離させる
ほか、気液分離器をも組込んでその充填材にスケールを
吸収させる等の措置を採つている。In the above steam generator, not only the heat conduction is deteriorated by the scale component contained in the feed water, but there is a drawback that it eventually blocks the heat absorption tube or piping,
Measures such as incorporating a water purifier to remove the scale component and separating the scale component in the feed water by the ion exchange resin, and also incorporating a gas-liquid separator to absorb the scale into the packing material Is taking.
この発明は、かかる措置とは別に運転、停止のサイクル
毎に、すなわち、電源OFFにより運転を停止した都度全
装置内を自動洗浄してスケールによる上記弊害の解消を
目的とした蒸気発生装置を提供するにある。The present invention provides a steam generator for the purpose of eliminating the above-mentioned harmful effects due to scale by automatically cleaning the inside of all the devices every cycle of operation and stop apart from such measures, that is, every time when the operation is stopped by turning off the power supply. There is.
問題点を解決するための手段 この発明は、蒸気を発生する蒸気発生器と該蒸気発生器
へ給水する給水装置からなる蒸気発生装置において、該
給水装置から蒸気発生器(A)の各機器配管各部に洗浄
水を給水するための電磁弁(V0)を備えた給水管(1)
と該洗浄水を排出するためのブロー電磁弁(V5)を備え
たブロー管(2)を設け、上記電磁弁(V0)とブロー電
磁弁(V5)を蒸気発生器(A)の運転停止時に電磁弁
(V0)が開放して蒸気発生器(A)の各機器配管各部に
給水し、一定時間経過後ブロー電磁弁(V5)が開放して
洗浄水を排出する洗浄動作が少なくとも1回以上自動的
に行いうるよう接続関連させてなる自動洗浄機能を組込
んだ蒸気発生装置に係り、さらに、具体的には、ガスバ
ーナ等の加熱器(10)による加熱で蒸気を発生せしめる
蒸気発生ボイラー(3)と、該蒸気発生ボイラー(3)
による蒸気を熱交換器に蒸気管(11)を介して送りその
凝縮潜熱を利用して気体又は液体を加熱し、その凝縮液
を還液管(12)で還流貯溜し大気に開放した受液槽
(5)と、該受液槽(5)と凝縮液送出管(6)によつ
て連通した給液槽(7)と、凝縮液送出管(6)の開口
部に設けたフロート弁(V6)と、給液槽(7)の低液位
(a)と高液位(b)を水位センサー(17),(18)で
検知することによつて開閉する開閉弁(V1)を備え蒸気
発生ボイラー(3)の管寄せ部(19)と給液槽(7)の
上部空間(20)の空気室を連通する均圧管(8)と、蒸
気発生ボイラー(3)からの逆流を阻止する逆止弁
(V7)を備え蒸気発生ボイラー(3)の下部溜部(21)
と給液槽(7)の下部を連通する給水導管(9)とから
なる蒸気循環型の蒸気発生装置における給水装置から蒸
気発生器(A)の各機器配管各部に洗浄水を給水するた
めの電磁弁(V0)を備えた給水管(1)と該洗浄水を排
出するためブロー電磁弁(V5)を備えたブロー管(2)
を設け、上記電磁弁(V0)とブロー電磁弁(V5)を蒸気
発生器(A)の電源OFFによる運転停止時に、電磁弁(V
0)が開放して蒸気発生器(A)の各機器配管各部に給
水管(1)を介してほぼ満水の状態に至るまで給水した
後、該電磁弁(V0)を閉じ、その後、一定時間をおいて
ブロー電磁弁(V5)を開放し各機器配管各部をほぼ満水
の状態に貯溜されている洗浄水をブロー管(21)から排
出せしめるという洗浄動作を少なくとも1回以上自動的
に行いうるよう接続関連させてなる自動洗浄機能を組込
んだ技術的手段を採り、上記問題点の解決を図つたもの
である。Means for Solving the Problems The present invention relates to a steam generator including a steam generator that generates steam and a water supply device that supplies water to the steam generator, and each device pipe from the water supply device to the steam generator (A). Water supply pipe (1) equipped with a solenoid valve (V 0 ) for supplying cleaning water to each part
And a blow pipe (2) equipped with a blow solenoid valve (V 5 ) for discharging the cleaning water, and the solenoid valve (V 0 ) and the blow solenoid valve (V 5 ) are connected to the steam generator (A). When the operation is stopped, the solenoid valve (V 0 ) is opened to supply water to each part of the steam generator (A), and after a certain period of time, the blow solenoid valve (V 5 ) is opened to discharge the wash water. Relates to a steam generator incorporating an automatic cleaning function that is connected and connected so that it can be automatically performed at least once, and more specifically, it generates steam by heating with a heater (10) such as a gas burner. Steam generating boiler (3) and steam generating boiler (3)
Is sent to the heat exchanger through the steam pipe (11) to heat the gas or liquid by utilizing the latent heat of condensation, and the condensed liquid is reflux-stored in the return liquid pipe (12) and opened to the atmosphere A tank (5), a liquid supply tank (7) communicating with the liquid receiving tank (5) through a condensate delivery pipe (6), and a float valve (provided at the opening of the condensate delivery pipe (6) ( V 6 ) and an on-off valve (V 1 ) that opens and closes by detecting low level (a) and high level (b) of the liquid supply tank (7) with water level sensors (17) and (18) And a pressure equalizing pipe (8) for connecting the pipe draw part (19) of the steam generating boiler (3) and the air chamber of the upper space (20) of the liquid supply tank (7), and the reverse flow from the steam generating boiler (3). Equipped with a check valve (V 7 ) to block the lower part (21) of the steam generating boiler (3)
And a water supply conduit (9) communicating with the lower part of the liquid supply tank (7) for supplying cleaning water from the water supply device in the steam circulation type steam generator to each device piping part of the steam generator (A) Water supply pipe (1) equipped with a solenoid valve (V 0 ) and blow pipe (2) equipped with a blow solenoid valve (V 5 ) for discharging the cleaning water
The solenoid valve (V 0 ) and the blow solenoid valve (V 5 ) are installed at the solenoid valve (V
0 ) is opened and water is supplied to each part of each equipment pipe of the steam generator (A) through the water supply pipe (1) until it is almost full, and then the solenoid valve (V 0 ) is closed, and thereafter, constant After a certain period of time, the blow solenoid valve (V 5 ) is opened and each part of the equipment piping is almost filled with water. The wash water stored in the blow tube (21) is discharged at least once automatically. This is a solution to the above-mentioned problems by adopting a technical means that incorporates an automatic cleaning function which is connected and connected.
作用 上記構成において、第3図の原理説明図に例示したよう
に、蒸気発生器(A)の運転を停止すると、ブロー電磁
弁(V5)は閉じたまゝ、電磁弁(V0),(V1)を開い
て、蒸気発生器(A)、給水装置(B)、気液分離器
(23)又はこれらとの配管に給水して、満水とし、電磁
弁(V0)を閉じ暫らく放置して後、電磁弁(V5)を開放
して、全給水を排出し、このときスケール分も一緒に排
出されて洗浄される。そしてこの作業を数回繰りかえし
て後、運転停止状態に復帰する。さらに、詳しくは、蒸
気発生ボイラー(3)によつて発生した蒸気は蒸気管
(11)を介して熱交換器へ送られるとともに、均圧管
(8)を介して給液槽(7)の上部空間(20)の空気室
にも送られる。このとき、均圧管(8)に設けた開閉弁
(V1)は給液槽(7)の液位が高液位(b)又は高液位
(b)と低液位(a)の間にあるときは開の状態にあ
る。しかして、熱交換器においてはその凝縮潜熱を利用
して気体又は液体を加熱し、ここで生成する凝縮した作
動液は還液管(12)により受液槽(5)へ還流され受液
槽(5)内に貯溜する。一方、給液槽(7)の上部空間
(20)の空気室にも均圧管(8)を介して蒸気圧が作用
するため蒸気発生ボイラー(3)と給液槽(7)は均圧
に保たれ、大気に開放している受液槽(5)の圧力との
差圧によりフロート弁(V6)はその弁シート(22)に圧
接された状態のもとに蒸気発生に伴つて減少する蒸気発
生ボイラー(3)の水量を給液槽(7)から給水導管
(9)を介して自動的に順次補給する。そして、給液槽
(7)の液位が低液位(a)に達すると水位センサー
(17)がこれを検知し均圧管(8)の開閉弁(V1)を閉
じ給液槽(7)の上部空間(20)の空気室への蒸気圧の
作用を停止する。しかして、給液槽(7)内の圧力は外
部への放熱等により低下し受液槽(5)内の圧力プラス
その水頭圧と等しくなつた時点で蒸気圧によるフロート
弁(V6)の持上げ力が解除されて該フロート弁(V6)は
落下し凝縮液送出管(6)を開放するため受液槽(5)
に貯溜している凝縮液は凝縮液送出管(6)を介して給
液槽(7)へ流入する。この際受液槽(5)は大気に開
放されているので凝縮液送出管(6)の上部吸入開口
(14)から空気も一緒に流入する。給液槽(7)内の液
位が高液位(b)にまでに達するとフロート弁(V6)は
液位により浮上して弁シート(22)に接し、かつ、水位
センサー(18)がこれを検知して均圧管(8)の開閉弁
(V1)を開放し給液槽(7)の上部空間(20)の空気室
に蒸気発生ボイラー(3)からの蒸気を再び作用させて
給液槽(7)と蒸気発生ボイラー(3)を均圧に保ち、
フロート弁(V6)を蒸気圧により持上げてその弁シート
(22)に圧接し凝縮液送出管(6)を閉塞して受液槽
(7)への凝縮液の流入を停止すると同時に給液槽
(7)から蒸気発生ボイラー(3)への水の補給を行
う。かくして、蒸気の凝縮した作動液、すなわち、凝縮
液を蒸気発生ボイラー(3)へ還液しながら連続した運
転の継続が可能である。Action In the above configuration, as illustrated in the principle explanatory diagram of FIG. 3, when the operation of the steam generator (A) is stopped, the blow solenoid valve (V 5 ) is closed, and the solenoid valve (V 0 ), ( V 1 ) is opened, water is supplied to the steam generator (A), water supply device (B), gas-liquid separator (23) or pipes with these to make it full of water, and the solenoid valve (V 0 ) is closed for a while. After leaving it for a while, the solenoid valve (V 5 ) is opened to discharge all the water supply, at which time the scale is also discharged and washed. Then, after repeating this work several times, the operation is stopped. More specifically, the steam generated by the steam generating boiler (3) is sent to the heat exchanger via the steam pipe (11), and the upper part of the liquid supply tank (7) via the pressure equalizing pipe (8). It is also sent to the air chamber of the space (20). At this time, the on-off valve (V 1 ) provided in the pressure equalizing pipe (8) has a high liquid level (b) in the liquid supply tank (7) or between the high liquid level (b) and the low liquid level (a). When it is, it is in the open state. In the heat exchanger, the latent heat of condensation is used to heat the gas or liquid, and the condensed working liquid generated here is returned to the liquid receiving tank (5) by the return liquid pipe (12) and is received in the liquid receiving tank. Store in (5). On the other hand, since the steam pressure also acts on the air chamber of the upper space (20) of the liquid supply tank (7) through the pressure equalizing pipe (8), the steam generating boiler (3) and the liquid supply tank (7) are equalized in pressure. The float valve (V 6 ) is kept in pressure contact with its valve seat (22) due to the pressure difference from the pressure in the liquid receiving tank (5) that is kept open to the atmosphere, and decreases with steam generation. The amount of water in the steam generating boiler (3) is automatically and sequentially replenished from the liquid supply tank (7) through the water supply conduit (9). When the liquid level in the liquid supply tank (7) reaches the low liquid level (a), the water level sensor (17) detects this and closes the on-off valve (V 1 ) of the pressure equalizing pipe (8) to close the liquid supply tank (7). ) Stop the action of vapor pressure on the air chamber of the upper space (20). Then, the pressure in the liquid supply tank (7) decreases due to heat radiation to the outside, and when it becomes equal to the pressure in the liquid reception tank (5) plus its head pressure, the float valve (V 6 ) of the vapor pressure Since the lifting force is released, the float valve (V 6 ) falls and the condensate delivery pipe (6) is opened, so that the liquid receiving tank (5)
The condensate stored in the tank flows into the liquid supply tank (7) through the condensate delivery pipe (6). At this time, since the liquid receiving tank (5) is open to the atmosphere, air also flows in through the upper suction opening (14) of the condensate delivery pipe (6). When the liquid level in the liquid supply tank (7) reaches the high liquid level (b), the float valve (V 6 ) floats by the liquid level and contacts the valve seat (22), and the water level sensor (18) When this is detected, the on-off valve (V 1 ) of the pressure equalizing pipe (8) is opened, and the steam from the steam generating boiler (3) is made to act again on the air chamber of the upper space (20) of the liquid supply tank (7). Maintain the liquid supply tank (7) and the steam generation boiler (3) at equal pressure,
The float valve (V 6 ) is lifted by the vapor pressure and pressed against the valve seat (22) to close the condensate delivery pipe (6) to stop the condensate from flowing into the receiving tank (7) and at the same time supply the liquid. Water is supplied from the tank (7) to the steam generating boiler (3). Thus, it is possible to continue the continuous operation while returning the condensed working liquid of the steam, that is, the condensed liquid to the steam generating boiler (3).
上記蒸気循環型の蒸気発生装置において、電源をOFFし
て運転を停止した場合、給水管(1)の電磁弁(V0)が
開放して蒸気発生器(A)の各機器配管各部に給水管
(1)を介してほぼ満水の状態に至るまで給水した後該
電磁弁(V0)を閉じ、その後、各機器配管各部に満水の
まま一定時間をおいてブロー電磁弁(V5)を開放しこの
ときスケール分が各機器配管各部に満たされている洗浄
水と一緒にブロー管(2)から排出せしめるという洗浄
動作を少なくとも1回以上自動的に行うものである。In the above steam circulation type steam generator, when the power is turned off to stop the operation, the solenoid valve (V 0 ) of the water supply pipe (1) is opened to supply water to each part of each equipment pipe of the steam generator (A). The solenoid valve (V 0 ) is closed after the water is supplied through the pipe (1) until it is almost full, and then the blow solenoid valve (V 5 ) is connected to each part of the equipment piping for a certain period of time while the water is full. The cleaning operation of opening and discharging the scale from the blow pipe (2) together with the cleaning water with which each part of the equipment pipe is filled is automatically performed at least once or more.
実施例 以下この発明の一実施例を図面に基づき説明する。Embodiment An embodiment of the present invention will be described below with reference to the drawings.
第1図はこの発明は蒸気循環型の蒸気発生装置に適用し
た場合を示し、第2図はその自動洗浄フローの一例を示
したもので、図中(1)は洗浄水を給水するための給水
管で、循環水の補給管を兼備し、その途中に電磁弁
(V0)を備えている。(2)はブロー管で、蒸気発生器
(A)の各機器配管各部に満たされている洗浄水を落差
によつて完全に排出できるよう配管されており、その途
中にブロー電磁弁(V5)を備えている。上記電磁弁
(V0)とブロー電磁弁(V5)は、電源をOFFして蒸気発
生器(A)の運転を停止した時、電磁弁(V0)が開放し
て蒸気発生器(A)の各機器配管各部に洗浄用の水を給
水し各機器配管各部に予め設定された量(ほぼ満水の状
態)の水が給水された後該電磁弁(V0)を閉じ、その
後、各機器配管各部のスケールが薄められ水中に吸収さ
れるまでの一定時間をおいてブロー電磁弁(V5)を開放
し各機器配管各部に満たされている洗浄水をブロー管
(2)から排出せしめるという洗浄動作を少なくとも1
回以上自動的に行いうるようコントロールボツクス等を
介して接続関連されている。また、(3)は蒸気発生器
(A)の蒸気発生ボイラーで、上部の管寄せ部(上部ヘ
ツダ)(19)と下部の溜部(下部ヘツダ)(21)を吸熱
フイン(3a)を備えた多数の吸熱管(3b)で連通せし
め、その外面を断熱材(3c)で覆い、吸熱管(3b)をガ
スバーナ等の加熱器(10)で加熱することにより蒸気を
発生せしめる貫流ボイラーとなしている。(3d)は上記
蒸気発生ボイラー(3)の管寄せ部(19)に設けたバキ
ユームブレーカで、大気圧以下の設定圧になると大気を
吸込んで蒸気発生ボイラー(3)内が負圧になるのを防
止して過剰給水等を防ぐためのものである。(11)は蒸
気発生ボイラー(3)の管寄せ部(19)からの蒸気取出
管(19a)と気液分離器(23)を介して接続連通させた
蒸気管で、図示しない熱交換器に接続し蒸気発生ボイラ
ー(3)で発生した蒸気を熱交換器に送出し熱交換器内
を流過する気体又は液体等に蒸気の凝縮潜熱を与え、た
とえば、湯沸し等に供するものである。(5)は受液槽
で、上記熱交換器と還液管(12)を介して接続され、熱
交換器で生成する凝縮液が該還液管(12)を経て受液槽
(5)に還流貯溜するようになし、該受液槽(5)には
下端を受液槽(5)の排出管(24)に設けた排水栓
(V8)の排水開口(25)と連通させた大気開放管(13)
の上端を受液槽(5)の上水位(c)上に開口し受液槽
(5)内を大気に開放し、かつ、この大気開放管(13)
でオーバーフロー管を兼備させている。(26)は受液槽
(5)の上水位(c)を検知するための水位センサー
で、前記給水管(1)の電磁弁(V0)と電気的に接続関
連させて蒸気発生器(A)の最も高い位置にある該受液
槽(5)の水位が上水位(c)に達したとき各機器配管
各部に満水の状態に洗浄水が給水され、該上水位(c)
を水位センサー(26)が検知すると電磁弁(V0)が閉止
し給水を停止するようになしている。(27)は受液槽
(5)の下水位(d)を検知するための水位センサー
で、運転中における循環液量の減少を該水位センサー
(27)が検知することで、電磁弁(V0)が開いて不足水
を補給するものである。(6)は上記受液槽(5)の低
部に垂設した凝縮液送出管で、その上端を受液槽(5)
に開口(6a)し下端は後述の給液槽(7)に開口(6b)
して受液槽(5)と給液槽(7)を該凝縮液送出管
(6)で連通せしめている。(V6)は上記凝縮液送出管
(6)の下部開口(6b)の近くに装備したフロート弁
で、後述の給液槽(7)内の液位及び内圧により上下動
してその弁シート(22)に接離することで凝縮液送出管
(6)を開閉し受液槽(5)から給液槽(7)への凝縮
液の給、断を行うものである。(7)は給液槽で、上記
受液槽(5)の下部一側に設けられ、該給液槽(7)に
は低液位(a)を検知する水位センサー(17)と高液位
(b)を検知する水位センサー(18)を備え、その上部
空間(20)の空気室と前記蒸気発生ボイラー(3)の管
寄せ部(19)を該管寄せ部(19)からの蒸気取出管(19
a)と気液分離器(23)を介して接続連通した均圧管
(8)で接続し、該均圧管(8)には上記水位センサー
(17),(18)と電気的に接続関連させた開閉弁、たと
えば、電磁弁(V1)を設けている。また、上記給液槽
(7)の上部空間(20)の空気室と受液槽(5)の上部
空間(15)を空気吸入管(14)で接続連通させ該空気吸
入管(14)には前記水位センサー(17),(18)と電気
的に接続関連させた開閉弁、たとえば、電磁弁(V2)を
設けて、給液槽(7)の液位が予め決められた低液位
(a)に達するとこれを水位センサー(17)が検知しそ
の検知信号により均圧管(8)の電磁弁(V1)を閉じる
と同時に空気吸入管(14)の電磁弁(V2)は開放し、給
液槽(7)の液位が予め決められた高液位(b)に達す
るとこれを水位センサー(18)が検知しその検知信号に
より均圧管(8)の電磁弁(V1)を開放し空気吸入管
(14)の電磁弁(V2)は閉じるようになしている。さら
に、空気吸入管(14)と熱交換器からの還液管(12)の
上端を受液槽(5)の上部空間(15)に設けたドレン滴
下孔(28)を有する波防板(29)の上部に臨ませ、大気
開放管(13)の上端は波防板(29)の下部に臨ませて空
気吸入管(14)及び還液管(12)と大気開放管(13)と
が直接連通しないようにしている。(9)は蒸気発生ボ
イラー(3)の下部溜部(21)と給液槽(7)の下部と
を連通した給水導管で、該給水導管(9)には蒸気発生
ボイラー(3)からの逆流を防止する逆止弁(V7)と給
水電磁弁(V4)を備えて蒸気発生に伴つて減少する蒸気
発生ボイラー(3)の水量を該給水導管(9)を介して
給液槽(7)から自動的に補給するものである。FIG. 1 shows the case where the present invention is applied to a steam circulation type steam generator, and FIG. 2 shows an example of the automatic cleaning flow. In the figure, (1) is for supplying cleaning water. The water supply pipe also serves as a supply pipe for circulating water, and a solenoid valve (V 0 ) is provided on the way. (2) is a blow pipe, which is installed so that the cleaning water filled in each part of each equipment pipe of the steam generator (A) can be completely discharged by a drop, and a blow solenoid valve (V 5 ) Is provided. The solenoid valve (V 0 ) and the blow solenoid valve (V 5 ) are turned off and the operation of the steam generator (A) is stopped, so that the solenoid valve (V 0 ) is opened and the steam generator (A) is opened. ), Water for cleaning is supplied to each part of each equipment pipe, and after a preset amount of water (a substantially full state) is supplied to each part of each equipment pipe, the solenoid valve (V 0 ) is closed, and then each Allow the blow solenoid valve (V 5 ) to open after a certain period of time until the scale of each part of the equipment piping is diluted and absorbed in water, and discharge the washing water filled in each part of the equipment piping from the blow tube (2). At least 1 cleaning action
It is connected via a control box etc. so that it can be automatically performed more than once. Further, (3) is a steam generating boiler of the steam generator (A), which is provided with an end portion (upper header) (19) and a lower reservoir (lower header) (21) for absorbing heat (3a). Without a through-flow boiler that communicates with a large number of heat absorption tubes (3b), covers the outer surface with a heat insulating material (3c), and heats the heat absorption tubes (3b) with a heater (10) such as a gas burner to generate steam. ing. (3d) is a vacuum breaker provided in the pipe draw part (19) of the steam generating boiler (3), and when the set pressure is equal to or lower than the atmospheric pressure, the atmosphere is sucked and the inside of the steam generating boiler (3) becomes negative pressure. To prevent excessive water supply. (11) is a steam pipe connected to the steam extraction pipe (19a) from the pipe draw part (19) of the steam generation boiler (3) via a gas-liquid separator (23), and is connected to a heat exchanger (not shown). The steam generated in the connected steam generating boiler (3) is sent to the heat exchanger to give the latent heat of condensation of the steam to the gas or liquid flowing through the heat exchanger, for example, for boiling water. A liquid receiving tank (5) is connected to the heat exchanger through the return liquid pipe (12), and the condensate produced in the heat exchanger passes through the return liquid pipe (12) and the liquid receiving tank (5). The lower end of the liquid receiving tank (5) is communicated with the drain opening (25) of the drain plug (V 8 ) provided in the discharge pipe (24) of the liquid receiving tank (5). Atmosphere open pipe (13)
The upper end of the liquid receiving tank (5) is opened above the upper water level (c) to open the inside of the liquid receiving tank (5) to the atmosphere, and the atmosphere open pipe (13)
It also serves as an overflow pipe. (26) is a water level sensor for detecting the upper water level (c) of the liquid receiving tank (5), which is electrically connected to the solenoid valve (V 0 ) of the water supply pipe (1) and is associated with the steam generator ( When the water level of the liquid receiving tank (5) at the highest position in (A) reaches the clean water level (c), flush water is supplied to each part of each equipment pipe to fill the clean water level (c).
When the water level sensor (26) detects, the solenoid valve (V 0 ) is closed and the water supply is stopped. (27) is a water level sensor for detecting the lower water level (d) of the liquid receiving tank (5). When the water level sensor (27) detects a decrease in the circulating fluid amount during operation, the solenoid valve (V 0 ) opens to supply the insufficient water. (6) is a condensate delivery pipe vertically provided at the lower part of the liquid receiving tank (5), and the upper end thereof is the liquid receiving tank (5)
(6a) and the lower end opens (6b) to the liquid supply tank (7) described below.
The liquid receiving tank (5) and the liquid supplying tank (7) are communicated with each other through the condensate delivery pipe (6). (V 6 ) is a float valve installed near the lower opening (6b) of the condensate delivery pipe (6), which moves up and down depending on the liquid level and internal pressure in a liquid supply tank (7) to be described later, and its valve seat The condensate delivery pipe (6) is opened and closed by contacting and separating from (22) to supply and disconnect the condensate from the liquid receiving tank (5) to the liquid supplying tank (7). (7) is a liquid supply tank, which is provided at one lower side of the liquid receiving tank (5) and has a water level sensor (17) for detecting a low liquid level (a) and a high liquid level in the liquid supply tank (7). A water level sensor (18) for detecting the position (b) is provided, and the air chamber of the upper space (20) of the water level sensor (18) and the pipe pulling part (19) of the steam generating boiler (3) are steamed from the pipe pulling part (19). Extraction pipe (19
It is connected by a pressure equalizing pipe (8) which is connected and communicated with a) through a gas-liquid separator (23), and the pressure equalizing pipe (8) is electrically connected to the water level sensors (17), (18). An on-off valve, for example, a solenoid valve (V 1 ) is provided. Further, the air chamber of the upper space (20) of the liquid supply tank (7) and the upper space (15) of the liquid receiving tank (5) are connected and communicated with each other by an air suction pipe (14) to the air suction pipe (14). Is a low liquid whose liquid level in the liquid supply tank (7) is predetermined by providing an opening / closing valve electrically connected to the water level sensors (17) and (18), for example, a solenoid valve (V 2 ). When it reaches the position (a), the water level sensor (17) detects it and the detection signal closes the solenoid valve (V 1 ) of the pressure equalizing pipe (8) and at the same time the solenoid valve (V 2 ) of the air suction pipe (14). Is opened, and when the liquid level in the liquid supply tank (7) reaches a predetermined high liquid level (b), the water level sensor (18) detects this, and the detection signal detects the electromagnetic valve (8) of the pressure equalizing pipe (8). V 1 ) is opened and the solenoid valve (V 2 ) of the air suction pipe (14) is closed. Furthermore, a wave plate having a drain dropping hole (28) provided in the upper space (15) of the liquid receiving tank (5) with the upper ends of the air suction pipe (14) and the return liquid pipe (12) from the heat exchanger ( 29), and the upper end of the atmosphere open pipe (13) faces the lower part of the wave plate (29) so that the air intake pipe (14), the return liquid pipe (12) and the atmosphere open pipe (13) Does not communicate directly. (9) is a water supply conduit that connects the lower reservoir (21) of the steam generating boiler (3) and the lower part of the liquid supply tank (7) to the water supply conduit (9). A check valve (V 7 ) for preventing backflow and a water supply solenoid valve (V 4 ) are provided, and the amount of water in the steam generating boiler (3) that decreases with steam generation is supplied through the water supply conduit (9) to a liquid supply tank. It is automatically replenished from (7).
なお、前記ブロー管(2)は気液分離器(23)の底部か
ら取出し、上記給水導管(9)と交叉させて連通し、該
ブロー管(2)の途中に空焚き防止センサー(30)を設
け、受液槽(5)の底部に開口した洗浄用導管(31)を
該空焚き防止センサー(30)に接続して受液槽(5)と
ブロー管(2)を連通させ、洗浄用導管(31)には洗浄
用電磁弁(V3)を設けている。また、前記蒸気発生ボイ
ラー(3)からの排気通路(32)に排気温度検知センサ
ー(33)を設け、上記空焚き防止センサー(30)ととも
に加熱器(10)へのガス供給路(34)に備えた電磁安全
弁(V9)と電気的に接続関連させて空焚き防止センサー
(30)と該排気温度検知センサー(33)のいずれか一方
が設定限界値以上に達したとき蒸気発生ボイラー(3)
の加熱器(10)の燃焼を自動的に停止して安全を期する
ようになしている。さらに、蒸気発生ボイラー(3)の
加熱器(10)として実施例は整流板(35)を備えた強制
給気式セラミツクバーナを用い、その給気用フアン
(F)の吹出口(36)にガス供給路(34)に接続された
ガスノズル(37)を臨ませ給気用フアン(F)からの空
気と該ノズル(37)からのガスが吹出口(36)で混合さ
れてバーナへ送給されるようになつている。図中、(V
10)は蒸気管(11)に備えた主蒸気弁、(V11)は給水
管(1)に備えた水抜栓である。The blow pipe (2) is taken out from the bottom portion of the gas-liquid separator (23) and communicates with the water supply conduit (9) by crossing the blow pipe (2). An empty heating prevention sensor (30) is provided in the middle of the blow pipe (2). And a washing conduit (31) opened at the bottom of the liquid receiving tank (5) is connected to the dry heating prevention sensor (30) so that the liquid receiving tank (5) and the blow pipe (2) communicate with each other. A solenoid valve (V 3 ) for cleaning is provided in the conduit (31). Further, an exhaust temperature detection sensor (33) is provided in the exhaust passage (32) from the steam generating boiler (3), and is provided in the gas supply passage (34) to the heater (10) together with the empty heating prevention sensor (30). A steam generating boiler (3) is provided when one of the dry heating prevention sensor (30) and the exhaust gas temperature detection sensor (33) reaches or exceeds a set limit value by being electrically connected to the provided electromagnetic safety valve (V 9 ). )
Combustion of the heater (10) is automatically stopped for safety. Further, in the embodiment, as the heater (10) of the steam generating boiler (3), a forced air supply type ceramic burner equipped with a rectifying plate (35) is used, and at the air outlet (36) of the air supply fan (F). The gas nozzle (37) connected to the gas supply path (34) is faced, and the air from the air supply fan (F) and the gas from the nozzle (37) are mixed at the air outlet (36) and sent to the burner. It is getting done. In the figure, (V
10 ) is a main steam valve provided in the steam pipe (11), and (V 11 ) is a water drain plug provided in the water supply pipe (1).
上記構成における各々の電磁弁(V1)……(V11)は、
洗浄その他の目的に応じコントロールボツクスからの指
令で予め決められたプログラムに従つて自動的に開閉制
御するよう接続関連されている。Each solenoid valve (V 1 ) ... (V 11 ) in the above configuration is
It is connected so as to automatically control opening and closing according to a predetermined program in response to a command from the control box according to cleaning or other purposes.
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 described.
給液槽(7)の液位が高液位(b)又は高液位(b)と
低液位(a)の間にあるときは、均圧管(8)の電磁弁
(V1)は開の状態にあり、空気吸入管(14)の電磁弁
(V2)は閉の状態にあるため加熱器(10)による吸熱管
(3b)の加熱で蒸気発生ボイラー(3)から発生した蒸
気は蒸気取出管(19a)から気液分離器(23)を介して
蒸気管(11)から熱交換器へ圧送されるとともに、均圧
管(8)から給液槽(7)の上部空間(20)の空気室に
も同時に作用する。しかして、熱交換器においては該熱
交換器を流過する気体又は流体に蒸気の凝縮潜熱を与え
て、たとえば、湯沸し等を行い、放熱により生成した蒸
気の凝縮液は還液管(12)により受液槽(5)へ還流さ
れ受液槽(5)内に貯溜する。一方、給液槽(7)の上
部空間(20)の空気室にも蒸気圧が作用して給液槽
(7)と蒸気発生ボイラー(3)は均圧に保たれ、この
圧力により大気開放管(13)を介して大気に開放されて
いる受液槽(5)の圧力と給液槽(7)とに差圧が生じ
フロート弁(V6)はその弁シート(22)に圧接され、凝
縮液送出管(6)を閉塞した状態のもとに蒸気発生に伴
つて減少(低下)する蒸気発生ボイラー(3)の水量
(水位)を給液槽(7)から給水導管(9)を介して自
動的に順次補給し常に一定量(一定水位)に保持する。
給液槽(7)の液位は蒸気発生ボイラー(3)の継続運
転に伴い次第に低下しその液位が予め決められた低液位
(a)に達すると、該位置に備えた水位センサー(17)
がこれを検知しその検知信号で均圧管(8)の電磁弁
(V1)を閉じ空気吸入管(14)の電磁弁(V2)は開放す
る。しかして、給液槽(7)の上部空間(20)の空気室
への蒸気圧の作用は停止され、かつ、給液槽(7)の上
部空間(20)の空気室と受液槽(5)の上部空間(15)
は空気吸入管(14)で連通されるため給液槽(7)内の
圧力は外部への放熱等によつて次第に低下し受液槽
(5)内の圧力プラスその水頭圧と等しくなつた時点に
おいてフロート弁(V6)の圧力による持上げ力が解か
れ、該フロート弁(V6)は自重で落下し弁シート(22)
から離間して凝縮液送出管(6)を開放連通し受液槽
(5)に貯溜している凝縮液を凝縮液送出管(6)の上
部開口(6a)→弁シート(22)→下部開口(6b)を経て
給液槽(7)内に流入せしめる。この際受液槽(5)は
大気開放管(13)により大気に開放されているから空気
も一緒に流入する。このようにして受液槽(5)内の貯
溜凝縮液が給液槽(7)内へ流入し、その液位が予め決
められた高液位(b)にまで達すると、フロート弁
(V6)は液位に従つて浮上し弁シート(22)に接し、か
つ、該位置に備えた水位センサー(18)がこれを検知し
その検知信号により均圧管(8)の電磁弁(V1)を開き
空気吸入管(14)の電磁弁(V2)を閉じ、給液槽(7)
の上部空間(20)の空気室に蒸気発生ボイラー(3)か
らの蒸気圧を再び作用させて給液槽(7)と蒸気発生ボ
イラー(3)を均圧に保ち、その圧力でフロート弁
(V6)を持上げ弁シート(22)に圧接して凝縮液送出管
(6)を閉塞し受液槽(5)からの凝縮液の流入を停止
すると同時に給液槽(7)から蒸気発生ボイラー(3)
への自動補給を開始し蒸気発生ボイラー(3)の水量を
一定水量に保つものである。When the liquid level of the liquid supply tank (7) is between the high liquid level (b) or between the high liquid level (b) and the low liquid level (a), the solenoid valve (V 1 ) of the pressure equalizing pipe (8) is Since the solenoid valve (V 2 ) of the air intake pipe (14) is in the open state, the steam generated from the steam generating boiler (3) by heating the endothermic pipe (3b) by the heater (10) Is pressure-fed from the steam extraction pipe (19a) through the vapor-liquid separator (23) to the heat exchanger from the steam pipe (11), and also from the pressure equalizing pipe (8) to the upper space (20) of the liquid supply tank (7). ) Also acts on the air chamber at the same time. Then, in the heat exchanger, the latent heat of vapor condensation is applied to the gas or fluid flowing through the heat exchanger, for example, boiling is performed, and the condensate of the vapor generated by heat dissipation is returned to the return pipe (12). It is refluxed to the liquid receiving tank (5) and stored in the liquid receiving tank (5). On the other hand, the vapor pressure also acts on the air chamber of the upper space (20) of the liquid supply tank (7) to keep the liquid supply tank (7) and the steam generating boiler (3) at a uniform pressure, and this pressure releases the atmosphere. A pressure difference occurs between the pressure of the liquid receiving tank (5) open to the atmosphere through the pipe (13) and the liquid supplying tank (7), and the float valve (V 6 ) is brought into pressure contact with its valve seat (22). , The water amount (water level) of the steam generating boiler (3) that decreases (decreases) with the steam generation under the condition that the condensate delivery pipe (6) is closed from the liquid supply tank (7) to the water supply conduit (9) It is automatically replenished in sequence through the and constantly maintained at a constant amount (constant water level).
The liquid level of the liquid supply tank (7) gradually decreases with the continuous operation of the steam generating boiler (3), and when the liquid level reaches a predetermined low liquid level (a), a water level sensor ( 17)
Detects this, and the detection signal closes the solenoid valve (V 1 ) of the pressure equalizing pipe (8) and opens the solenoid valve (V 2 ) of the air suction pipe (14). Thus, the action of vapor pressure on the air chamber of the upper space (20) of the liquid supply tank (7) is stopped, and the air chamber of the upper space (20) of the liquid supply tank (7) and the liquid receiving tank ( Upper space of 5) (15)
Is communicated with the air suction pipe (14), the pressure in the liquid supply tank (7) gradually decreases due to heat radiation to the outside and becomes equal to the pressure in the liquid reception tank (5) plus its head pressure. At this point, the lifting force due to the pressure of the float valve (V 6 ) is released, and the float valve (V 6 ) falls by its own weight and the valve seat (22)
The condensate which is stored in the liquid receiving tank (5) is communicated with the condensate delivery pipe (6) by opening the condensate delivery pipe (6) apart from the upper opening (6a) of the condensate delivery pipe (6) → valve seat (22) → lower part It is made to flow into the liquid supply tank (7) through the opening (6b). At this time, since the liquid receiving tank (5) is opened to the atmosphere by the atmosphere opening pipe (13), air also flows in together. In this way, when the stored condensate in the liquid receiving tank (5) flows into the liquid supplying tank (7) and the liquid level reaches a predetermined high liquid level (b), the float valve (V 6 ) floats according to the liquid level and is in contact with the valve seat (22), and the water level sensor (18) provided at this position detects this, and the detection signal detects the electromagnetic valve (V 1 of the pressure equalizing pipe (8). ) Is opened and the solenoid valve (V 2 ) of the air suction pipe (14) is closed, and the liquid supply tank (7)
The steam pressure from the steam generating boiler (3) is caused to act again on the air chamber of the upper space (20) of the liquid supply tank (7) and the steam generating boiler (3) to maintain a uniform pressure, and the float valve ( V 6 ) is brought into pressure contact with the valve seat (22) to close the condensate delivery pipe (6) to stop the inflow of the condensate from the receiving tank (5) and at the same time to generate steam from the liquid supply tank (7). (3)
The automatic water supply to the steam generating boiler (3) is started to keep the water amount constant.
上記一連の蒸気循環動作により蒸気の凝縮した作動液を
蒸気発生ボイラーに自力還流させ、連続した運転の継続
ができるものであるが、電源をOFFして蒸気発生装置の
運転を停止せしめると、コントロールボツクスからの指
令でその各機器配管各部をくまなく自動洗浄するもので
あるが、その自動洗浄の一例を第2図のフローに従つて
説明すると、蒸気発生装置の電源をOFFすると、コント
ロールボツクスからの指令で、電源OFF後30分間再運転
の可能性を考慮してそのまま停止状態で待機する。した
がつて、この30分間の間は電源をONすれば即座に再運転
ができるとともに、或る程度缶体温度を下げるためであ
る。そこで、電源OFF後30分を経過すると、コントロー
ルボツクスからの指令で、ブロー電磁弁(V5)を除いた
電磁弁(V0),(V1),(V2),(V3)を開いて各機器
配管各部を連通させこれらに給水管(1)から洗浄用の
水を給水し各機器配管各部がほぼ満水の状態に至ると受
液槽(5)内の水位が上水位(c)に達しこれを水位セ
ンサー(26)が検知しコントロールボツクスに知らせ、
給水管(1)の電磁弁(V0)を閉止して給水を停止す
る。その後一定時間、すなわち、5秒間そのまま放置
し、この5秒間の間に各機器配管各部に付着、滞積する
水垢等のスケールが満水状の洗浄水と一緒になり、その
後該一定時間が経過すると、コントロールボツクスから
の指令でブロー管(2)のブロー電磁弁(V5)が開放さ
れて各機器配管各部に満たされているスケール分と一緒
になつて洗浄水はブロー管(2)から器外へ排出され
る。この排出は落差で行われるため当初は勢いよく排出
するが次第にその勢いは弱まり遂にはチヨロチヨロの状
態になる。スケールは排水当初より排水後半のチヨロチ
ヨロの状態時の方が濃くなる。したがつて、300秒間の
排水動作を行つて後半のチヨロチヨロ排水を暫く続ける
ことにより濃いスケールまで完全に排出することができ
る。しかる後、コントロールボツクスからの指令で洗浄
用電磁弁(V3)及びブロー電磁弁(V5)を閉じ、1回の
洗浄動作を終るが、この洗浄動作は少なくとも1回以上
自動的に行い(第2図のフローでは2回)、設定回数の
洗浄動作が完了すると、コントロールボツクスからの指
令で電磁弁(V1),(V2)を閉じ、次の運転に入れる態
勢を整え洗浄を完了するものである。The above-mentioned series of steam circulation operation allows the working fluid in which steam is condensed to be returned to the steam generating boiler by itself, and continuous operation can be continued.However, if the power is turned off to stop the operation of the steam generator, the control is performed. It is a command from the box to automatically clean all parts of each equipment pipe, but an example of the automatic cleaning is explained according to the flow in Fig. 2. When the power of the steam generator is turned off, the control box Command, and wait for 30 minutes after turning off the power, considering the possibility of restarting. Therefore, during this 30 minutes, if the power is turned on, the operation can be restarted immediately and the can body temperature is lowered to some extent. Therefore, 30 minutes after the power is turned off, the solenoid valves (V 0 ), (V 1 ), (V 2 ), (V 3 ) excluding the blow solenoid valve (V 5 ) are commanded by the control box. When it is opened and each part of the equipment pipe is communicated with each other, water for cleaning is supplied from the water supply pipe (1) to each part of the equipment pipe until the water level in the liquid receiving tank (5) reaches the upper level (c). ) Has been reached and the water level sensor (26) detects this and informs the control box,
Stop the water supply by closing the solenoid valve (V 0 ) of the water supply pipe (1). After that, it is left for a certain period of time, that is, for 5 seconds, and during the 5 seconds, scales such as scale that adheres to and accumulates on each part of each equipment pipe become together with the full-flushed cleaning water, and after that, the certain time elapses. The blow solenoid valve (V 5 ) of the blow pipe (2) is opened according to a command from the control box, and the scale water filled in each part of each equipment pipe is filled with the cleaning water from the blow pipe (2). It is discharged to the outside. Since this discharge is carried out at the head, it is discharged vigorously at first, but the momentum gradually weakens, and finally it becomes a state of chilling. The scale becomes thicker in the state of the chilly chiller in the latter half of the drainage than the initial drainage. Therefore, by performing the drainage operation for 300 seconds and continuing the latter half of the drainage for a while, it is possible to completely drain to the dark scale. Then, the cleaning solenoid valve (V 3 ) and blow solenoid valve (V 5 ) are closed by a command from the control box, and one cleaning operation is completed, but this cleaning operation is performed automatically at least once ( 2 times in the flow of Fig. 2) When the set number of washing operations are completed, the control box closes the solenoid valves (V 1 ) and (V 2 ) to prepare for the next operation and complete the washing. To do.
発明の効果 この発明は以上説明したように、蒸気発生装置におい
て、電源OFFによる運転停止の都度、各機器配管各部の
洗浄を自動的に行いうる構造としたから給水の水垢、給
水中に含有する鉄分等のスケールの付着、滞積が原因す
る熱伝導の劣化及び蒸気発生ボイラーの吸熱管又は配管
等の閉塞はなくなり、該洗浄機能だけを蒸気発生装置に
組込むか、あるいは、浄水器又は気液分離器と組合せる
ことによりスケール除去処理が確実に行われて従来にな
いすぐれた効果を発揮するものである。EFFECTS OF THE INVENTION As described above, according to the present invention, in the steam generator, each time when the operation is stopped by turning off the power, each device piping part is automatically cleaned. The adhesion of scale such as iron, deterioration of heat conduction due to accumulation and blockage of the heat absorption pipe or piping of the steam generating boiler are eliminated, and only the cleaning function is incorporated in the steam generator, or the water purifier or gas liquid By combining with a separator, the scale removal process is surely performed, and an excellent effect that has never been obtained is exhibited.
また、洗浄動作により各機器配管各部の水を完全に排出
することができるから寒冷地における凍結防止を兼ね安
全である。In addition, since the water can be completely discharged from each part of each equipment pipe by the washing operation, it is safe as well as preventing freezing in cold regions.
第1図はこの発明による蒸気発生装置の一実施例を示す
概略構成図、第2図はその自動洗浄フローの一例を示す
フローチヤート、第3図はこの発明の原理説明図、第4
図は蒸気循環型蒸気発生装置の概略構成図である。 (A)…蒸気発生器、(1)…給水管、(V0)…電磁
弁、(2)…ブロー管、(V5)…ブロー電磁弁、(3)
…蒸気発生ボイラー、(4)…熱交換器、(5)…受液
槽、(V6)…フロート弁、(6)…凝縮液送出管、
(7)…給液槽、(V1)…開閉弁、(8)…均圧管、
(V7)…逆止弁、(9)…給水導管。FIG. 1 is a schematic configuration diagram showing an embodiment of a steam generator according to the present invention, FIG. 2 is a flow chart showing an example of an automatic cleaning flow thereof, FIG. 3 is an explanatory view of the principle of the present invention, and FIG.
FIG. 1 is a schematic configuration diagram of a steam circulation type steam generator. (A) ... Steam generator, (1) ... Water supply pipe, (V 0 ) ... Solenoid valve, (2) ... Blow pipe, (V 5 ) ... Blow solenoid valve, (3)
... steam generating boilers, (4) ... heat exchanger, (5) ... receiver tank, (V 6) ... float valve, (6) ... condensate delivery tube,
(7) ... Liquid supply tank, (V 1 ) ... Open / close valve, (8) ... Pressure equalizing pipe,
(V 7 ) ... Check valve, (9) ... Water supply conduit.
Claims (2)
へ給水する給水装置からなる蒸気発生装置において、該
給水装置から蒸気発生器(A)の各機器配管各部に洗浄
水を給水するための電磁弁(V0)を備えた給水管(1)
と該洗浄水を排出するためのブロー電磁弁(V5)を備え
たブロー管(2)を設け、上記電磁弁(V0)とブロー電
磁弁(V5)を蒸気発生器(A)の運転停止時に電磁弁
(V0)が開放して蒸気発生器(A)の各機器配管各部に
給水し、一定時間経過後ブロー電磁弁(V5)が開放して
洗浄水を排出する洗浄動作が少なくとも1回以上自動的
に行いうるよう接続関連させてなる自動洗浄機能を組込
んだ蒸気発生装置。1. A steam generator comprising a steam generator for generating steam and a water supply device for supplying water to the steam generator, wherein washing water is supplied from the water supply device to each part of each equipment pipe of the steam generator (A). Water pipe (1) with solenoid valve (V 0 ) for
And a blow pipe (2) equipped with a blow solenoid valve (V 5 ) for discharging the cleaning water, and the solenoid valve (V 0 ) and the blow solenoid valve (V 5 ) are connected to the steam generator (A). When the operation is stopped, the solenoid valve (V 0 ) is opened to supply water to each part of the steam generator (A), and after a certain period of time, the blow solenoid valve (V 5 ) is opened to discharge the wash water. A steam generator that incorporates an automatic cleaning function that is connected and linked so that it can be automatically performed at least once.
と、該蒸気を熱交換器によつて生成する凝縮液を還流貯
溜し大気に開放した受液槽(5)と、該受液槽(5)と
フロート弁(V6)を備えた凝縮液送出管(6)を介して
連通する給液槽(7)と、該給液槽(7)の水位検知に
よつて開閉する開閉弁(V1)を備え蒸気発生ボイラー
(3)の上部と給液槽(7)の上部を連通する均圧管
(8)と、蒸気発生ボイラー(3)からの逆流を阻止す
る逆止弁(V7)を備え蒸気発生ボイラー(3)の下部と
給液槽(7)の下部を連通する給水導管(9)とからな
る蒸気発生器(A)である特許請求の範囲第1項記載の
蒸気発生装置。2. A steam generating boiler for generating steam (3)
And a liquid receiving tank (5) in which the condensate that produces the vapor by a heat exchanger is stored under reflux and opened to the atmosphere, and a condensate having the liquid receiving tank (5) and a float valve (V 6 ). A liquid supply tank (7) communicating with the delivery pipe (6) and an opening / closing valve (V 1 ) that opens and closes according to the water level detection of the liquid supply tank (7) and an upper part of the steam generating boiler (3) A pressure equalizing pipe (8) communicating with the upper part of the liquid supply tank (7) and a check valve (V 7 ) for preventing backflow from the steam generating boiler (3) are provided and the lower part of the steam generating boiler (3) and the liquid supply. The steam generator according to claim 1, which is a steam generator (A) including a water supply conduit (9) communicating with a lower portion of the tank (7).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22419286A JPH0723763B2 (en) | 1986-09-22 | 1986-09-22 | Steam generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22419286A JPH0723763B2 (en) | 1986-09-22 | 1986-09-22 | Steam generator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6380107A JPS6380107A (en) | 1988-04-11 |
JPH0723763B2 true JPH0723763B2 (en) | 1995-03-15 |
Family
ID=16809961
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22419286A Expired - Fee Related JPH0723763B2 (en) | 1986-09-22 | 1986-09-22 | Steam generator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0723763B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5191909B2 (en) * | 2009-01-09 | 2013-05-08 | シャープ株式会社 | Heating cooker and steam generator cleaning method |
JP6455348B2 (en) * | 2015-07-10 | 2019-01-23 | 富士電機株式会社 | Heat pump steam generator and method of operating the heat pump steam generator |
-
1986
- 1986-09-22 JP JP22419286A patent/JPH0723763B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS6380107A (en) | 1988-04-11 |
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