JPH05118503A - Steam feeding equipment - Google Patents

Steam feeding equipment

Info

Publication number
JPH05118503A
JPH05118503A JP3282599A JP28259991A JPH05118503A JP H05118503 A JPH05118503 A JP H05118503A JP 3282599 A JP3282599 A JP 3282599A JP 28259991 A JP28259991 A JP 28259991A JP H05118503 A JPH05118503 A JP H05118503A
Authority
JP
Japan
Prior art keywords
steam
boiler
pipe
supply
load
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.)
Granted
Application number
JP3282599A
Other languages
Japanese (ja)
Other versions
JP2736192B2 (en
Inventor
Junro Tsunoda
淳郎 角田
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.)
Toshiba Engineering Corp
Toshiba Corp
Original Assignee
Toshiba Engineering Corp
Toshiba Corp
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 Toshiba Engineering Corp, Toshiba Corp filed Critical Toshiba Engineering Corp
Priority to JP3282599A priority Critical patent/JP2736192B2/en
Publication of JPH05118503A publication Critical patent/JPH05118503A/en
Application granted granted Critical
Publication of JP2736192B2 publication Critical patent/JP2736192B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To provide steam feeding equipment which reduces the operation cost of an in-house boiler and is rational and economical. CONSTITUTION:Steam feeding equipment has a boiler l to feed steam to a steam using load 3 is provided. Further, a steam generating device 13 to generate steam by using high enthalpy fluid serving as a heat source is further provided. The boiler 1 and the steam generating device 13 are switcheably connected to the steam using load 3.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、蒸気供給設備に係り、
特に原子力発電所に設置してある蒸気使用負荷へ蒸気を
供給する蒸気供給設備に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam supply facility,
Particularly, it relates to a steam supply facility for supplying steam to a steam use load installed in a nuclear power plant.

【0002】[0002]

【従来の技術】原子力発電所にはさまざまな蒸気使用負
荷が設置されているが、各蒸気使用負荷は、蒸気供給設
備のボイラーから蒸気を供給されるようになっている。
図3は、原子力発電所の所内蒸気使用負荷へ蒸気を供給
する従来の蒸気供給設備を示した系統図である。
2. Description of the Related Art A variety of steam use loads are installed in a nuclear power plant, and each steam use load is supplied with steam from a boiler of a steam supply facility.
FIG. 3 is a system diagram showing a conventional steam supply facility that supplies steam to the in-house steam use load of a nuclear power plant.

【0003】図3の蒸気供給設備を用いて所内蒸気使用
負荷へ蒸気を供給するには、まず、所内ボイラー1で蒸
気を発生させ、この蒸気を蒸気供給配管2を介して各蒸
気使用負荷3へ供給する。次に、蒸気使用負荷3から出
た戻り蒸気を、復水回収配管4を介し復水回収装置5へ
導く。次に、復水回収装置5で回収した復水を、復水移
送配管6を介してボイラー給水タンク7へ移送する。ボ
イラー給水タンク7の復水は、ボイラー給水ポンプ8お
よびボイラー給水配管9を介して所内ボイラー1へ送ら
れ、再びボイラー給水として再利用される。
In order to supply steam to the in-house steam use load using the steam supply equipment of FIG. 3, first, steam is generated in the in-house boiler 1, and this steam is supplied through the steam supply pipe 2 to each steam use load 3 Supply to. Next, the return steam from the steam use load 3 is guided to the condensate recovery device 5 via the condensate recovery pipe 4. Next, the condensate water recovered by the condensate water recovery device 5 is transferred to the boiler water supply tank 7 via the condensate transfer pipe 6. Condensed water in the boiler water supply tank 7 is sent to the on-site boiler 1 via the boiler water supply pump 8 and the boiler water supply pipe 9 and is reused as boiler water supply again.

【0004】[0004]

【発明が解決しようとする課題】従来の蒸気供給設備の
所内ボイラー1は、重油または電気を燃料または熱源と
して用いているが、この重油量または電気使用量は年間
を通すとかなりの量となり、エネルギーの使用量を増加
させる原因となっている。
The conventional boiler 1 of the steam supply facility uses heavy oil or electricity as a fuel or a heat source, but the amount of heavy oil or electricity used becomes a considerable amount throughout the year. This is a cause of increasing the amount of energy used.

【0005】本発明は、上述した事情を考慮してなされ
たもので、所内ボイラーのエネルギー消費量を低減し合
理的かつ効率のよい蒸気供給設備を提供することを目的
とする。
The present invention has been made in consideration of the above-mentioned circumstances, and an object of the present invention is to provide a reasonable and efficient steam supply facility by reducing the energy consumption of the in-house boiler.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するた
め、本発明の蒸気供給設備は請求項1に記載したよう
に、蒸気使用負荷に蒸気を供給するボイラーを備えた蒸
気供給設備において、高エンタルピー流体を熱源として
蒸気を発生させる蒸気発生装置をさらに備え、前記ボイ
ラーおよび前記蒸気発生装置を切替え自在に前記蒸気使
用負荷に接続したものである。
In order to achieve the above-mentioned object, the steam supply equipment of the present invention is, as described in claim 1, a steam supply equipment equipped with a boiler for supplying steam to a steam use load. A steam generator for generating steam using an enthalpy fluid as a heat source is further provided, and the boiler and the steam generator are switchably connected to the steam use load.

【0007】[0007]

【作用】ボイラーおよび蒸気発生装置を切替え自在に蒸
気使用負荷に接続したことにより、発電所が運転中のと
きは、タービン蒸気等を利用した蒸気発生装置で蒸気を
発生させてこの蒸気を使用負荷へ送ることが可能とな
り、従来のように、所内ボイラーで発生させた蒸気だけ
を各蒸気使用負荷へ供給するのに比べ、より安価に蒸気
を供給することができる。
[Function] By connecting the boiler and the steam generator to the steam load so that they can be switched, when the power plant is in operation, steam is generated by the steam generator using turbine steam, etc., and this steam is used. Therefore, it is possible to supply the steam at a lower cost as compared with the conventional case where only the steam generated in the on-site boiler is supplied to each steam use load.

【0008】[0008]

【実施例】以下、本発明の蒸気供給設備の実施例につい
て、添付図面を参照して説明する。図1は、本実施例の
蒸気供給設備の一実施例を示す系統図である。本実施例
の蒸気供給設備は、蒸気使用負荷3に蒸気を供給するボ
イラー1を備えてある。ボイラー1は、重油または電気
で蒸気を発生させるようになっている。
Embodiments of the steam supply equipment of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a system diagram showing an example of the steam supply equipment of the present embodiment. The steam supply facility of the present embodiment includes a boiler 1 that supplies steam to a steam use load 3. The boiler 1 is adapted to generate steam with heavy oil or electricity.

【0009】また、本実施例の蒸気供給設備は、高エン
タルピー流体を熱源として蒸気を発生させる蒸気発生装
置13をさらに備え、ボイラー1および蒸気発生装置1
3を切替え自在に蒸気使用負荷3に接続してある。
The steam supply equipment of this embodiment further comprises a steam generator 13 for generating steam using a high enthalpy fluid as a heat source, and the boiler 1 and the steam generator 1 are provided.
3 is switchably connected to the steam load 3.

【0010】蒸気発生装置13は、熱交換器12から送
られた高温加熱水で蒸気を発生させ、この蒸気を配管2
2および蒸気供給配管2を介して蒸気使用負荷3に送る
ように構成してある。
The steam generator 13 generates steam with the high-temperature heated water sent from the heat exchanger 12, and the steam is supplied to the pipe 2
2 and the steam supply pipe 2 to the steam use load 3.

【0011】熱交換器12は、高エンタルピー流体配管
18を流れる高エンタルピー流体との熱交換により低温
水を高温加圧水にし、この高温加圧水を蒸気発生装置1
3に送るように構成してある。
The heat exchanger 12 converts low temperature water into high temperature pressurized water by heat exchange with the high enthalpy fluid flowing through the high enthalpy fluid pipe 18, and the high temperature pressurized water is used as the steam generator 1.
It is configured to be sent to.

【0012】熱交換器12において、高エンタルピー流
体が配管10に混入するおそれがある場合には、熱交換
器12の配管10側の圧力を、高エンタルピー流体配管
18側の圧力よりも高く保つように設計するのがよい。
In the heat exchanger 12, if the high enthalpy fluid may be mixed in the pipe 10, the pressure on the pipe 10 side of the heat exchanger 12 should be kept higher than the pressure on the high enthalpy fluid pipe 18 side. It is better to design

【0013】ここで、高エンタルピー流体配管18と配
管10との間に差圧検出装置9を設けておき、高エンタ
ルピー流体配管18内の流体圧力と配管10内の流体圧
力との差が所定値以内になった場合に、高エンタルピー
流体配管18に設けた弁20を閉じることができるよう
になっているのがよい。
Here, the differential pressure detecting device 9 is provided between the high enthalpy fluid pipe 18 and the pipe 10, and the difference between the fluid pressure in the high enthalpy fluid pipe 18 and the fluid pressure in the pipe 10 is a predetermined value. It is preferable that the valve 20 provided in the high enthalpy fluid pipe 18 can be closed when the pressure falls within the range.

【0014】この構成は、熱交換器12において高エン
タルピー流体配管18から配管10に高エンタルピー流
体が流入するのを防止するのに役立ち、特に、高エンタ
ルピー流体が放射性物質である場合には上述のような構
成とするのが好ましい。これと関連して、配管10に放
射性物質が流入したのを検知する放射性物質検知装置2
8を設けるのがよい。また、蒸気発生装置13には循環
ポンプ11が接続してあり、高温加圧水から分離された
復水を再び熱交換器12に循環させるようになってい
る。
This arrangement serves to prevent the high enthalpy fluid from flowing into the pipe 10 from the high enthalpy fluid pipe 18 in the heat exchanger 12, especially when the high enthalpy fluid is a radioactive substance. It is preferable to have such a configuration. In connection with this, the radioactive substance detection device 2 for detecting the inflow of the radioactive substance into the pipe 10
8 should be provided. A circulation pump 11 is connected to the steam generator 13 so that the condensate separated from the high temperature pressurized water is circulated to the heat exchanger 12 again.

【0015】循環ポンプ11は複数設けておき、通常運
転用以外に予備機とするのがよい。また、循環ポンプ1
1の下流に圧力検出装置21を設けておき、配管10内
の圧力が熱交換器12の必要所定圧力に維持されるよう
に循環ポンプ11を作動させるのが好ましい。
It is preferable to provide a plurality of circulation pumps 11 and use them as standby machines other than those for normal operation. In addition, the circulation pump 1
It is preferable that a pressure detection device 21 is provided downstream of 1, and the circulation pump 11 is operated so that the pressure in the pipe 10 is maintained at the required predetermined pressure of the heat exchanger 12.

【0016】これらの第1の蒸気発生装置13、熱交換
器12および循環ポンプ11は配管10で相互に接続し
てあり、全体として循環ループを形成するように構成し
てある。蒸気使用負荷3は、復水回収配管4を介して復
水回収装置5に接続してあり、復水回収装置5は、配管
25を介して給水タンク15に接続してある。給水タン
ク15には給水ポンプ14が接続してあり、給水タンク
15の水を配管10の循環ポンプ11の上流側に補給水
として注入するようになっている。
The first steam generator 13, the heat exchanger 12 and the circulation pump 11 are connected to each other by a pipe 10 and are constructed so as to form a circulation loop as a whole. The steam use load 3 is connected to a condensate recovery device 5 via a condensate recovery pipe 4, and the condensate recovery device 5 is connected to a water supply tank 15 via a pipe 25. A water supply pump 14 is connected to the water supply tank 15, and water in the water supply tank 15 is injected into the upstream side of the circulation pump 11 of the pipe 10 as makeup water.

【0017】水位検出装置17が蒸気発生装置13内に
設けてあり、蒸気発生装置13内の復水の液位が所定の
レベルより下がったときに給水ポンプ14を作動させる
ように給水ポンプ14に電気的に接続してある。
A water level detection device 17 is provided in the steam generator 13, and the water supply pump 14 is operated so as to operate the water supply pump 14 when the liquid level of the condensed water in the steam generator 13 falls below a predetermined level. It is electrically connected.

【0018】一方、ボイラー1は、発生させた蒸気を、
蒸気供給配管2を介して蒸気使用負荷3に送るようにな
っているとともに、ボイラー給水タンク7からボイラー
給水ポンプ8によって給水されるようになっている。ボ
イラー給水タンク7は、復水移送配管6を介して復水回
収装置5に接続してある。
On the other hand, the boiler 1
The steam is supplied to the steam use load 3 through the steam supply pipe 2 and is supplied from the boiler water supply tank 7 by the boiler water supply pump 8. The boiler water supply tank 7 is connected to the condensate recovery device 5 via a condensate transfer pipe 6.

【0019】配管22、蒸気供給配管2には、それぞれ
弁24、23を設けてあり、これらの弁24、23の一
方を閉じ他方を開くことによって、蒸気使用負荷3に送
る蒸気の供給元を、蒸気発生装置13あるいはボイラー
1から選択できるようになっている。
The pipe 22 and the steam supply pipe 2 are provided with valves 24 and 23, respectively. By closing one of these valves 24 and 23 and opening the other, the supply source of the steam to be sent to the steam use load 3 is determined. The steam generator 13 or the boiler 1 can be selected.

【0020】同様に、配管25、復水移送配管6には、
それぞれ弁27、26が設けてあり、これらの弁27、
26の一方を閉じ他方を開くことによって、復水回収装
置5からの復水の供給先を、蒸気発生装置13に関連す
る給水タンク15あるいはボイラー1に関連するボイラ
ー給水タンク7から選択できるようになっている。
Similarly, in the pipe 25 and the condensate transfer pipe 6,
Valves 27 and 26 are provided respectively, and these valves 27 and 26 are
By closing one of 26 and opening the other, the destination of the condensate from the condensate recovery device 5 can be selected from the water supply tank 15 associated with the steam generator 13 or the boiler water supply tank 7 associated with the boiler 1. Is becoming

【0021】本実施例の蒸気供給設備が原子力発電所に
設置されている場合、発電所が通常運転状態であれば、
タービン蒸気あるいは主蒸気等の高エンタルピー流体を
用いることにより、蒸気発生装置13で蒸気を発生さ
せ、この蒸気を蒸気使用負荷3に供給することができ
る。蒸気発生装置13を用いる場合には弁24、27を
開いておき、一方、ボイラー1に関連する弁23、26
は閉じておく。次に、タービン蒸気あるいは主蒸気等の
高エンタルピー流体を高エンタルピー流体配管18を介
して熱交換器12に導く。
When the steam supply equipment of this embodiment is installed in a nuclear power plant and the power plant is in a normal operating state,
By using a high enthalpy fluid such as turbine steam or main steam, steam can be generated by the steam generator 13 and this steam can be supplied to the steam use load 3. When using the steam generator 13, the valves 24, 27 are left open, while the valves 23, 26 associated with the boiler 1 are
Keep it closed. Next, a high enthalpy fluid such as turbine steam or main steam is introduced to the heat exchanger 12 via the high enthalpy fluid pipe 18.

【0022】次に、熱交換器12は、配管10を介して
循環ポンプ11により送られた低温水を、高エンタルピ
ー流体と熱交換し、次いで、熱交換により高温に加圧さ
れた水を蒸気発生装置13の方に送りだす。高温加圧水
は、減圧弁16で減圧された後、蒸気発生装置13に送
られる。蒸気発生装置13で発生した蒸気は、配管22
および蒸気供給配管2を経て、蒸気使用負荷3に入る。
Next, the heat exchanger 12 heat-exchanges the low-temperature water sent from the circulation pump 11 through the pipe 10 with the high-enthalpy fluid, and then steams the water pressurized to a high temperature by the heat-exchange. It sends it to the generator 13. The high temperature pressurized water is decompressed by the decompression valve 16 and then sent to the steam generator 13. The steam generated by the steam generator 13 is supplied to the pipe 22.
Then, the steam use load 3 is entered through the steam supply pipe 2.

【0023】一方、蒸気使用負荷3で使用された蒸気の
復水は、復水回収配管4を介して復水回収装置5に入
り、復水回収装置5は、回収した復水を配管25を介し
て給水タンク15に送る。かくして、蒸気発生装置13
を用いて蒸気使用負荷3に蒸気を送ることができる。
On the other hand, the condensate of the steam used in the steam use load 3 enters the condensate recovery device 5 via the condensate recovery pipe 4, and the condensate recovery device 5 connects the recovered condensate to the pipe 25. To the water tank 15. Thus, the steam generator 13
Can be used to send steam to the steam usage load 3.

【0024】発電所が停止状態であれば、タービン蒸気
あるいは主蒸気等の高エンタルピー流体を用いることが
できないが、ボイラー1で蒸気を発生させ、この蒸気を
蒸気使用負荷3に蒸気を供給することができる。ボイラ
ー1を用いる場合には弁23、26を開いておき、一
方、蒸気発生装置13に関連する弁24、27は閉じて
おく。次に、ボイラー1で蒸気を発生させ、発生させた
蒸気を蒸気供給配管2を介して蒸気使用負荷3に送る。
蒸気使用負荷から出た復水は、復水回収管4を介して復
水回収装置5に入り、さらに復水移送配管6を経てボイ
ラー給水タンク7に入る。ボイラー給水タンク7の水
は、ボイラー給水ポンプ8によりボイラー給水配管9を
介してボイラー1に送られる。かくして、ボイラー1を
用いて蒸気使用負荷3に蒸気を送ることができる。
When the power plant is stopped, high enthalpy fluid such as turbine steam or main steam cannot be used, but steam is generated in the boiler 1 and this steam is supplied to the steam use load 3. You can When using the boiler 1, the valves 23, 26 are kept open, while the valves 24, 27 associated with the steam generator 13 are kept closed. Next, steam is generated in the boiler 1 and the generated steam is sent to the steam use load 3 via the steam supply pipe 2.
Condensate discharged from the steam use load enters a condensate recovery device 5 via a condensate recovery pipe 4, and further enters a boiler water supply tank 7 via a condensate transfer pipe 6. The water in the boiler water supply tank 7 is sent to the boiler 1 by the boiler water supply pump 8 through the boiler water supply pipe 9. Thus, the boiler 1 can be used to send steam to the steam usage load 3.

【0025】このように、発電所が運転中のときは、タ
ービン蒸気等を利用した蒸気発生装置13で蒸気使用負
荷3への蒸気を発生させることが可能となり、ボイラー
1の燃料費を節約できるので、従来のように、ボイラー
1で発生させた蒸気だけを各蒸気使用負荷3へ供給する
のに比べ、より安価に蒸気を供給することができる。本
実施例の蒸気供給設備の運転費を従来と比較したグラフ
を図2に示す。この図から、蒸気供給設備全体の運転費
が改善されているのがわかる。
As described above, when the power plant is in operation, it is possible to generate steam to the steam use load 3 by the steam generator 13 using turbine steam or the like, and the fuel cost of the boiler 1 can be saved. Therefore, compared to the conventional case where only the steam generated in the boiler 1 is supplied to each steam use load 3, the steam can be supplied at a lower cost. FIG. 2 shows a graph comparing the operating cost of the steam supply equipment of the present embodiment with the conventional one. From this figure, it can be seen that the operating cost of the entire steam supply facility has been improved.

【0026】また、本実施例の蒸気供給設備は、放射性
物質を含む高エンタルピー流体を熱源として使用する場
合にも、蒸気発生装置側へ混入しないような設計として
あるので、安全性、信頼性が高い蒸気供給設備を供給で
きる。本実施例の蒸気供給設備は、原子力発電所に適用
するのが最も好ましいが、これに限定されるものではな
く、他の化学プラントに適用してもよい。
Further, since the steam supply equipment of this embodiment is designed so as not to mix into the steam generator side even when a high enthalpy fluid containing a radioactive substance is used as a heat source, it is safe and reliable. Able to supply high steam supply equipment. The steam supply facility of the present embodiment is most preferably applied to a nuclear power plant, but is not limited to this and may be applied to other chemical plants.

【0027】また、本実施例の蒸気供給設備は、高エン
タルピー流体による蒸気発生装置と、ボイラーとを併用
する構成としたが、高エンタルピー流体による蒸気発生
装置だけを用いる構成としてもよい。
Further, although the steam supply equipment of this embodiment has a structure in which the steam generator using the high enthalpy fluid and the boiler are used together, it is also possible to use only the steam generator using the high enthalpy fluid.

【0028】[0028]

【発明の効果】以上述べたように、本発明の蒸気発生設
備は、蒸気使用負荷に蒸気を供給するボイラーを備えた
蒸気供給設備において、高エンタルピー流体を熱源とし
て蒸気を発生させる蒸気発生装置をさらに備え、前記ボ
イラーおよび前記蒸気発生装置を切替え自在に前記蒸気
使用負荷に接続したことにより、発電所が運転中のとき
は、タービン蒸気等を利用した蒸気発生装置で蒸気使用
負荷への蒸気を発生させることが可能となり、ボイラー
の燃料費を節約できるので、従来のように、ボイラーで
発生させた蒸気だけを各蒸気使用負荷へ供給するのに比
べ、より効果的に蒸気を供給することができる。
As described above, the steam generating equipment of the present invention is a steam supplying equipment equipped with a boiler for supplying steam to a steam use load, and a steam generating device for generating steam using a high enthalpy fluid as a heat source. Further provided, by connecting the boiler and the steam generator switchably to the steam use load, when the power plant is operating, steam to the steam use load by the steam generator using turbine steam or the like. Since it is possible to generate steam and save boiler fuel costs, it is possible to supply steam more effectively than in the conventional case where only steam generated by the boiler is supplied to each steam use load. it can.

【0029】また、蒸気発生装置およびボイラーを交替
で稼働させればよいので、原子力発電所の運転を停止す
ることなく、蒸気発生装置およびボイラーを保守点検す
ることができる。さらに、発電所が運転中に蒸気発生装
置が故障しても、ボイラーを使用することができるの
で、信頼性の高い蒸気供給設備を提供することができ
る。
Since the steam generator and the boiler may be operated alternately, the steam generator and the boiler can be maintained and inspected without stopping the operation of the nuclear power plant. Furthermore, even if the steam generator breaks down while the power plant is operating, the boiler can be used, so that a highly reliable steam supply facility can be provided.

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

【図1】本発明の蒸気供給設備の一実施例を示す系統
図。
FIG. 1 is a system diagram showing an embodiment of steam supply equipment of the present invention.

【図2】本発明の蒸気供給設備を用いたときの運転費を
従来と比較したグラフ。
FIG. 2 is a graph comparing the operating cost when using the steam supply equipment of the present invention with a conventional one.

【図3】従来の蒸気供給設備を示す系統図。FIG. 3 is a system diagram showing a conventional steam supply facility.

【符号の説明】[Explanation of symbols]

1 ボイラー 2 蒸気供給配管 3 蒸気使用負荷 4 復水回収配管 5 復水回収装置 6 復水移送配管 7 ボイラー給水タンク 8 ボイラー給水ポンプ 9 ボイラー給水配管 10 ループ配管 11 循環ポンプ 12 熱交換器 13 蒸気発生装置 14 給水ポンプ 15 給水タンク 16 減圧弁 17 液位検出装置 18 高エンタルピー流体配管 19 差圧検出装置 20 弁 21 圧力検出装置 22 配管 1 Boiler 2 Steam supply pipe 3 Steam use load 4 Condensate recovery pipe 5 Condensate recovery device 6 Condensate transfer pipe 7 Boiler water supply tank 8 Boiler water supply pump 9 Boiler water supply pipe 10 Loop pipe 11 Circulation pump 12 Heat exchanger 13 Steam generation Device 14 Water supply pump 15 Water tank 16 Pressure reducing valve 17 Liquid level detection device 18 High enthalpy fluid piping 19 Differential pressure detection device 20 Valve 21 Pressure detection device 22 Piping

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 蒸気使用負荷に蒸気を供給するボイラー
を備えた蒸気供給設備において、高エンタルピー流体を
熱源として蒸気を発生させる蒸気発生装置をさらに備
え、前記ボイラーおよび前記蒸気発生装置を切替え自在
に前記蒸気使用負荷に接続したことを特徴とする蒸気供
給設備。
1. A steam supply facility including a boiler for supplying steam to a steam load, further comprising a steam generator for generating steam using a high enthalpy fluid as a heat source, and the boiler and the steam generator can be switched freely. A steam supply facility connected to the steam load.
JP3282599A 1991-10-29 1991-10-29 Steam supply equipment Expired - Lifetime JP2736192B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3282599A JP2736192B2 (en) 1991-10-29 1991-10-29 Steam supply equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3282599A JP2736192B2 (en) 1991-10-29 1991-10-29 Steam supply equipment

Publications (2)

Publication Number Publication Date
JPH05118503A true JPH05118503A (en) 1993-05-14
JP2736192B2 JP2736192B2 (en) 1998-04-02

Family

ID=17654605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3282599A Expired - Lifetime JP2736192B2 (en) 1991-10-29 1991-10-29 Steam supply equipment

Country Status (1)

Country Link
JP (1) JP2736192B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7201954B1 (en) * 2022-08-29 2023-01-11 住友ゴム工業株式会社 Steam supply system and tire curing system

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5232401A (en) * 1975-09-08 1977-03-11 Hitachi Ltd Indoor boiler control system
JPS55123901A (en) * 1979-03-19 1980-09-24 Tokyo Shibaura Electric Co Heat exchanger
JPS582629A (en) * 1981-06-29 1983-01-08 Mitsubishi Atom Power Ind Inc Apparatus for detecting leakage from steam generator
JPS59134401A (en) * 1983-01-21 1984-08-02 富士電機株式会社 Detector for leakage of feedwater heater
JPS59217198A (en) * 1983-05-25 1984-12-07 株式会社東芝 Reactor heat transfer facility
JPH02109101U (en) * 1989-02-03 1990-08-30

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5232401A (en) * 1975-09-08 1977-03-11 Hitachi Ltd Indoor boiler control system
JPS55123901A (en) * 1979-03-19 1980-09-24 Tokyo Shibaura Electric Co Heat exchanger
JPS582629A (en) * 1981-06-29 1983-01-08 Mitsubishi Atom Power Ind Inc Apparatus for detecting leakage from steam generator
JPS59134401A (en) * 1983-01-21 1984-08-02 富士電機株式会社 Detector for leakage of feedwater heater
JPS59217198A (en) * 1983-05-25 1984-12-07 株式会社東芝 Reactor heat transfer facility
JPH02109101U (en) * 1989-02-03 1990-08-30

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7201954B1 (en) * 2022-08-29 2023-01-11 住友ゴム工業株式会社 Steam supply system and tire curing system

Also Published As

Publication number Publication date
JP2736192B2 (en) 1998-04-02

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