JPS58138211A - Feeding of steam by boiler and steam accumulator and apparatus thereof - Google Patents

Feeding of steam by boiler and steam accumulator and apparatus thereof

Info

Publication number
JPS58138211A
JPS58138211A JP1810382A JP1810382A JPS58138211A JP S58138211 A JPS58138211 A JP S58138211A JP 1810382 A JP1810382 A JP 1810382A JP 1810382 A JP1810382 A JP 1810382A JP S58138211 A JPS58138211 A JP S58138211A
Authority
JP
Japan
Prior art keywords
water
accumulator
boiler
temperature
foam
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
JP1810382A
Other languages
Japanese (ja)
Inventor
Tei Misawa
三沢 禎
Yoshiho Nakai
中井 良穂
Teruhide Hamamatsu
浜松 照秀
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.)
Central Research Institute of Electric Power Industry
JFE Engineering Corp
Original Assignee
Central Research Institute of Electric Power Industry
NKK Corp
Nippon Kokan 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 Central Research Institute of Electric Power Industry, NKK Corp, Nippon Kokan Ltd filed Critical Central Research Institute of Electric Power Industry
Priority to JP1810382A priority Critical patent/JPS58138211A/en
Publication of JPS58138211A publication Critical patent/JPS58138211A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K3/00Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

PURPOSE:To enable the max. amount of heat to be recovered through the min. heat transmission area by control-operating a boiler as a hot-water boiler, storing the supplied water in the form of the max. pressure saturated steam, hot water, and the cold water having the min. saturation temperature, when steam is supplied from an accumulator. CONSTITUTION:A boiler 1 is operated as a hot-water boiler through the control by a throttle control valve 16, the hot water from an outlet pipe is made to pass through the valve 16 and sent into an upper space 18, which is filled with the max. pressure saturated steam, and the hot water 19 which stores heat in the lower part of the upper space and the min. pressure cold water 20 having a saturation temperature in an accumulator in the lowest part are stored in two layers, having the boundary surface 21 therebetween. A cylindrical body 22 is arranged in the accumulator 14, and thus the disturbance on the boundary surface is prevented by the rectification action. Steam is supplied into a turbine 5 from the upper space 18 in case of necessity, and the steam utilized as power is condensed in a condenser 7, and sent into a water supply tank 9, and heated in a heat exchanger 13, and is allowed to circulate into the lower part of the accumulator 14, and sent into the boiler 1 again.

Description

【発明の詳細な説明】 この発明は、ボイラと無泡アキュムレータによる無泡供
給方法および装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a foam-free supply method and apparatus using a boiler and a foam-free accumulator.

ボイラで発生した熱エネルギーを無泡アキュムレータに
蓄えながら、所要時にこれを放出して発生無泡を各種の
無代消費設備へ供給するシステムには櫨々のものがあり
、例えば、離島得において給w用に供されるディ(ル発
電機!IKよる給電システムに対し、そO尖慮負荷時の
電力をまかなうため、ディーゼルエンジンの廃熱を回収
する廃熱ボイラを付設し、回収熱エネルギーを無代了キ
ュムレータに蓄えておいて、7j2頭負荷時にアキュム
レータ必ら蒸汽を放出してタービン発電機を駆動し、こ
のタービン発電機による電力を負荷へ補給することが行
なわれている。
There are a variety of systems that store thermal energy generated in a boiler in a non-foam accumulator and release it when necessary to supply the generated non-foam to various types of non-foam consumption equipment. In order to cover the electric power supply system using diesel generators (IKs) used for diesel engines during special loads, a waste heat boiler is attached to recover the waste heat of the diesel engine, and the recovered thermal energy is The steam is stored in a non-capturing accumulator, and when the load is on two 7js, steam is released from the accumulator to drive a turbine generator, and the electric power from the turbine generator is supplied to the load.

このための廃熱回収タービン発電システムとして従来か
ら用いられている一般的なシステ^構成社彫1図に示す
通りである。すなわち第1図において、従来のとの種シ
ステムは、ディーゼル発電設備のエンジン排気系からの
排ガスのもつ廃熱で運転される廃熱ボイラ(1)k汽水
分離器ψ)および給水ポンプ(3)を接続してなるボイ
ラ系と、こOボイラ糸から発生した蒸汽を温水として蓄
える変圧形燕汽了キュムレータ(4)および無代ターヒ
ン(5) * 含trタービン系とから成り、例えば午
前中の低員循時にディーゼル発電設備の廃熱をボイラ(
1)で回収してアキュムレータ(4)に蓄蔵させ、夕方
の尖朧負荷時にアキュムレータ(4)の圧力を下げつつ
F9T要量の蒸発を行なわせてタービン(5)を回し、
これによってタービン発電機(6)から電力を得てこれ
によりディーゼル発電機出力を補ぎなうものである。こ
の場合、タービン(5)内で動力発生に利用した蒸汽は
、復水器(7)、復水ポンプ(8)、補給水タンク(9
)、補細水ポンプ(10)および給水加熱器(11)を
経て汽水分鵬器(2)の給水側に戻抄、再びボイラ(1
)へ循環する。
A typical system conventionally used as a waste heat recovery turbine power generation system for this purpose is shown in Figure 1. In other words, in Fig. 1, the conventional system includes a waste heat boiler (1), a steam water separator ψ), and a feed water pump (3), which are operated using the waste heat of exhaust gas from the engine exhaust system of a diesel power generation facility. It consists of a boiler system that connects a During low circulation, waste heat from diesel power generation equipment is transferred to the boiler (
1) and stored in the accumulator (4), and during the evening haze load, the pressure in the accumulator (4) is lowered and the required amount of F9T is evaporated to turn the turbine (5).
Thereby, electric power is obtained from the turbine generator (6), thereby supplementing the output of the diesel generator. In this case, the steam used to generate power within the turbine (5) is transferred to the condenser (7), the condensate pump (8), and the make-up water tank (9).
), returns to the water supply side of the steam water heater (2) via the supplementary water pump (10) and the feed water heater (11), and returns to the boiler (1)
).

このような従来のシステムでは、ボイラ圧がアキュムレ
ータ(4)の最高圧に配管及びアキュムレータ(4)内
O無泡噴出ノズルの抵抗等を上載せした一定圧に保友れ
るように運転され、従ってボイラ(1)の伝熱面温度は
前記運転ボイラ圧力の飽和湿度以上となる。この友め廃
熱ボイラ(1)において廃熱回収限度が狭められたり、
同一熱回収量に対しても伝熱面を多く要するなどの欠点
が避けらnず、特にアキュムレータ(蜀の変圧レンジ管
大きくとって率位体積あたりの蓄熱量を増そうとすると
ボイラ圧の上昇によって前記欠点がますますその傾向を
増大することとなった。
In such a conventional system, the boiler pressure is maintained at a constant pressure, which is the maximum pressure of the accumulator (4) plus the resistance of the piping and the O bubble-free jet nozzle in the accumulator (4), and therefore The heat transfer surface temperature of the boiler (1) is equal to or higher than the saturated humidity of the operating boiler pressure. In this friend waste heat boiler (1), the waste heat recovery limit is narrowed,
There are unavoidable drawbacks such as the need for a large number of heat transfer surfaces for the same amount of heat recovery, and in particular, if you try to increase the amount of heat storage per unit volume by increasing the size of the accumulator (variable range tube), the boiler pressure will increase. As a result, the aforementioned drawbacks have become more prevalent.

この発明は前述の諸欠点をなくすためになされたもので
、ボイラにおける伝熱面温度をその運転ボイラ圧力の飽
和温度まで上らないように保つことができ、漱小のボイ
ラ伝熱面積で高い熱回収効率を得ることのできる無代供
給方法および装置を提供することを目的としている。
This invention was made in order to eliminate the above-mentioned drawbacks, and it is possible to maintain the temperature of the heat transfer surface in the boiler so that it does not rise to the saturation temperature of the operating boiler pressure, and it is possible to maintain high heat transfer surface temperature with a small boiler heat transfer area. It is an object of the present invention to provide a cost-free supply method and device that can obtain heat recovery efficiency.

すなわちこの発明においては、ボイラで発生した熱エネ
ルギーを無代了キュームレータに蓄熱し、所要時に該ア
キュームレータで蒸汽を発生させて無泡消費設備例えば
タービン発電システ^、ビルIIINシステム、燃料油
ヒーター、無代動カシステムその他へ該蒸汽を供給する
に際し、前記ボイラを温水ボイラとして制御運転して給
水を前記アキュムレータの最高圧の飽和温度まで昇温し
、これを前記アキュムレータの上部へ送り込むことによ
りアキュムレータ内の上部空間を前記最高圧の飽和蒸汽
で満すと共和その下部に蓄熱した高温水とさらにその下
部に該アキュムレータの無代放出時のll1k低圧飽和
温度に相当する低温水との二層水を満すようにし、所要
時に前記アキュムレータから蒸発する蒸汽を無泡消費設
備へ供給して、前記アキュムレータの無代発生後の低温
水と補給水との混合水を前記メイラへ供給するものであ
り、この場合、装置としては前記無泡アキュムレータと
して立て形のものを用い、その内部に整流用および自然
循環促進用の筒状体を軸心に平行に配置し、ボイラ必ら
の前記高温水出口管に該高温水温度が前記最高圧の飽和
温度となるように開度wi泉さ′れる絞り制御弁を介装
するものである。
That is, in this invention, the thermal energy generated in the boiler is stored in the non-destructive accumulator, and steam is generated in the accumulator when required to be used in non-foam consumption equipment such as turbine power generation systems, building III systems, fuel oil heaters, etc. When supplying the steam to the powerless power system and others, the boiler is operated in a controlled manner as a hot water boiler to raise the temperature of the feed water to the maximum pressure saturation temperature of the accumulator, and the water is fed to the upper part of the accumulator. When the upper space of the accumulator is filled with the highest pressure saturated steam, two layers of water are formed: high-temperature water that has stored heat in the lower part of the tank, and low-temperature water that corresponds to the 11k low-pressure saturation temperature at the time of free discharge from the accumulator. steam evaporated from the accumulator is supplied to the bubble-free consumption equipment when required, and mixed water of low-temperature water and make-up water after bubble-free generation in the accumulator is supplied to the mailer. In this case, a vertical type device is used as the bubble-free accumulator, in which a cylindrical body for rectifying flow and promoting natural circulation is arranged parallel to the axis, and the high temperature water outlet of the boiler is A throttle control valve is installed in the pipe, and the opening degree is adjusted so that the temperature of the high-temperature water reaches the saturation temperature of the maximum pressure.

この発明においては、前記のようにボイラはアキュムレ
ータの最低圧飽和温度の低温水と補給水との混合水を最
高圧飽和温度に加熱するという運転状態を常に保ち、こ
の運転状態は、アキュムレータへの蓄熱時も、無代消費
e備への無代供縮のための放熱時に亀、変わりなく保持
し侍るものである。またこの場合に前記ボイラは温水ボ
イラとして運転されることになり、従ってその伝熱向は
全て温水と接し、好ましくはボイラ燃焼ガスと伝熱管内
温水流との向きを対向するよう配置することで温度差を
充分とり、最小の伝熱面積で最大の熱圓収効率を得るこ
とができるものである。さらに従来のシステムにおいて
用いる壷圧形無代アキュムレータは一般的なルーツ式横
形アキュムレータのように内部に多数の無代噴出ノズル
と配汽管を備えたII雑な本のであったが、この発明で
用−る変EEl魚汽アキュムレータはこのような多数の
蒸汽噴出ノズルなどを必要とせず、内部に整流用(撹乱
防止用)および自然循環促進用の筒状体を平行に配設し
た単なる立て形の圧力容器のようなもので済むこともひ
とつの利点である。
In this invention, as described above, the boiler always maintains an operating state in which the mixture of low-temperature water and make-up water at the lowest pressure saturation temperature of the accumulator is heated to the highest pressure saturation temperature, and this operating state is defined by the fact that the boiler is heated to the highest pressure saturation temperature. Even during heat storage, the tortoise remains unchanged during heat dissipation for free supply and contraction to free consumption. Further, in this case, the boiler is operated as a hot water boiler, and therefore, all of its heat transfer directions are in contact with hot water, and preferably, the boiler combustion gas and the hot water flow in the heat transfer tubes are arranged so that the directions are opposite to each other. It is possible to obtain a sufficient temperature difference and obtain the maximum heat collection efficiency with the minimum heat transfer area. Furthermore, the pot pressure type accumulator used in the conventional system was a crude type with a large number of pressureless jet nozzles and distribution pipes inside, like a general Roots-type horizontal accumulator, but with this invention, The modified EEL fish steam accumulator that we use does not require such a large number of steam jetting nozzles, but is simply a vertical type with cylindrical bodies arranged in parallel for rectifying the flow (preventing disturbance) and promoting natural circulation. One advantage is that it only requires a pressure vessel similar to that of a standard pressure vessel.

この発明を廃熱ボイラおよび無代消費設備としての尖頼
負a時用タービン発電システムを用いた実施例につき図
面と共に説明すれば以下の通りである。182図はこの
発明の実施例に係る廃熱回収発電システムの構成を示す
系統図で、11N1図と同一符号のものは同効のものを
示す。(12)はタービン入口無代蓋制傭弁、(13)
は給水加熱器としての熱交換器で、例えばボイラ(1)
で廃熱回収を行なうディーゼル発電機のエンジンシリン
ダ冷却水とアはたて形O蛮圧形無代アキュムレータ、(
15)は補給水流量制御弁である。
An embodiment of the present invention using a waste heat boiler and a turbine power generation system for low-demand use as a free consumption facility will be described below with reference to the drawings. Fig. 182 is a system diagram showing the configuration of the waste heat recovery power generation system according to the embodiment of the present invention, and the same symbols as in Fig. 11N1 indicate the same effects. (12) is a turbine inlet no cover valve, (13)
is a heat exchanger as a feed water heater, for example, a boiler (1)
The engine cylinder cooling water of a diesel generator that recovers waste heat is
15) is a makeup water flow rate control valve.

この発明のシステムにおけるボイラ糸では、ボイラ(1
)はその出口管に介装された散り制御弁(16)を介し
てアキュムレータ(14)および給水ポンプ(3)とル
ープを構成し、一方、タービン糸もこのアキュムレータ
(14)を介してループを閉じている。
In the boiler yarn in the system of this invention, the boiler (1
) forms a loop with the accumulator (14) and the water supply pump (3) through the dispersion control valve (16) installed in its outlet pipe, while the turbine yarn also forms a loop through the accumulator (14). Closed.

絞り制御弁(16)社、温水出口温度制御装置I (1
7)によってボイラ(1)の出口管内の温水温度を監視
しながら出口管温水流量を開度#整で制御することによ
り、ボイラ(1)の出口温水温度をアキュムレータ(1
4)の最高圧に対応する飽和湿度に保つものである。絞
り制御弁(16)による制御でボイラ(1)を温水ボイ
ラとして運転させ、その出口tからの尚渇水は制御弁(
16)を通過したのちにアキュムレータ(14)の上部
空間(18)に送り込む。アキュムレータ(14)の上
部空間(18) Uその触高圧の飽和無代で満されるこ
とになり、その下部に蓄熱した?に温水(19)とさら
にその下部にアキュムレータのam圧の飽和温度の低温
水(20)とが境界面(21)を間にして二層水となっ
て貯えられる。アキュムレータ(14)内に社この二層
水の貯水のために篩状体(22)が配設され、7ラツシ
ング等による境界面の乱れをそのIl流作用によって防
止するものとする。タービン(5)へは所要時にアキュ
ムレータ(14)の上部空間(18)内からタービン人
口無代量制御弁を介して無代が供給され、この場合、ア
キエムレータ下部の管路は遣断弁(23)によって閉じ
られる。タービン内で動力に利用された無代は復水器(
7)で復水されたのち復水ポンプ(8)を介して補給水
タンク(9)に送られる。補給水タンク(9)からの補
給水線、ポンプ(10)を介して熱交換器(13)で加
熱されたのち制−弁(15)を介してアキュムレータ(
14) O下部に循環し、再びボイラ(1)へ送られる
ことになる。
Throttle control valve (16) company, hot water outlet temperature control device I (1
7), while monitoring the hot water temperature in the outlet pipe of the boiler (1) and controlling the flow rate of hot water in the outlet pipe by adjusting the opening degree of the accumulator (1).
This is to maintain the saturated humidity corresponding to the maximum pressure in 4). The boiler (1) is operated as a hot water boiler under the control of the throttle control valve (16), and the control valve (16) operates the boiler (1) as a hot water boiler.
16) and then fed into the upper space (18) of the accumulator (14). The upper space (18) of the accumulator (14) is filled with saturated high pressure, and heat is stored in its lower part. Hot water (19) is stored below the hot water (19), and low temperature water (20) at the saturation temperature of the am pressure of the accumulator is stored as two-layer water with an interface (21) in between. A sieve-like body (22) is disposed in the accumulator (14) to store the two-layer water, and its Il flow action prevents disturbance of the interface due to 7 lashing or the like. Hydrogen is supplied to the turbine (5) from the upper space (18) of the accumulator (14) via the turbine variable control valve when required. ) is closed by The power used for power inside the turbine is the condenser (
After the water is condensed in step 7), it is sent to the make-up water tank (9) via the condensate pump (8). The make-up water line from the make-up water tank (9) is heated by the heat exchanger (13) via the pump (10) and then transferred to the accumulator (via the control valve (15)).
14) It will be circulated to the lower part of the O and sent to the boiler (1) again.

この場合、たて形アキュムレータ内に射いて筒状体(2
2)の作用によシニ層水けその境界向を保持して混合せ
ず、蓄熱時には境界面が下降し、無代放出時には筒状体
(22)の上下をめぐる自然楯票流れが生じてその混合
作用で全体の温tが徐々に最低温度にまで低下し、逐に
は1サイクルを終了する。
In this case, the cylindrical body (2
Due to the action of 2), the boundary direction of the Shini layer water is maintained and they do not mix, the boundary surface descends during heat storage, and a natural shield flow occurs around the top and bottom of the cylindrical body (22) during free release. Due to the mixing action, the overall temperature t gradually decreases to the lowest temperature, and one cycle is eventually completed.

ボイラ(1)は、アキュムレータ(14)の蓄熱時も無
代放出時も同じ条件で稼動され、無代放出時には一時的
に絞抄制御弁(16)を出てから7ラツシングを生じる
が特に支障はない また絞り制御弁(16) (D@@社112図でL温度
狐視による方式のものを例示したが、アキュムレータ(
14)の内圧を監視する方式に代えてもよく、但しこの
場合、アキュムレータの無代放出時には弁開度をホール
ド状態にするか、又は畝り制御弁(16)の直前の温水
温度によって制御信号にリミットをかけるようにする必
要がある。
The boiler (1) is operated under the same conditions both when heat is stored in the accumulator (14) and when it is discharged without heat generation, and when heat is discharged without heat generation, 7 lashing occurs temporarily after exiting the throttling control valve (16), which is a particular problem. Also, the throttle control valve (16) (D@@ Company 112 shows an example of the L temperature control valve, but the accumulator (16)
14) may be replaced with a method of monitoring the internal pressure. However, in this case, the valve opening is held in the hold state when the accumulator discharges without charge, or the control signal is controlled by the hot water temperature immediately before the ridge control valve (16). It is necessary to put a limit on

この発明のひとつの実施例において、アキュムレータ(
14) aその最高圧20 atiが無代放出時に最低
圧4 aim迄下降し、保南高温水(19)の一部約3
31onを蒸発して残部約200 tonの保有水が4
 ataの飽和温度約143°Cの低温水となる。ター
ビン(5)の非稼動時にこの低温水は給水ポンプ(3)
によって廃熱ボイラ(1)へ送られ、ボイラ(1)で加
熱されることにより20 ataの飽和温度約211°
Cとなつて絞り制御弁(16)を介しアキュムレータ(
14)の上部に戻され、上部空間(18)は20 et
a O飽和島汽で満されることとなってアキュムレータ
内圧力は20 ataとなる。一方、所要時にアキュム
レータ(14)から無代放出されてタービン(5)で仕
事をした復水約33 tollは、補給水タンク(9)
およびポンプ(10)を介して熱交換II (13)内
にて例えばナイーゼルエンジンのシリンダ冷即清水85
°Cにより75°C迄加熱され、−昼夜にわたり、っt
bヤに変わらずに略均等に1m11111弁(15)に
よって給水ポンプ(3)の吸入管部すなわちアキュムレ
ータ(14)のFilに供給される。従って給水ポンプ
(3)の出口では約134°Cとな怜、これはボイラの
低温腐蝕対策としても安全な温度範囲内である。アキュ
ムレータ(14)内部では上方の211°Cの高温水と
下方の143°CO低温水とに前述の如く上下二層水形
式で分けられ、それらの境界面(21)は蓄熱時に下降
し、無代放出時には自然循11による混合で全体が一様
の湿度で降温する。
In one embodiment of the invention, an accumulator (
14) The maximum pressure of 20 ai drops to the lowest pressure of 4 aim during the free release, and some of the Honan high temperature water (19) is about 3
After evaporating 31 tons of water, the remaining water is approximately 200 tons.
It becomes low-temperature water with a saturation temperature of about 143°C. When the turbine (5) is not operating, this low-temperature water is supplied to the water supply pump (3).
The waste heat is sent to the boiler (1) and heated by the boiler (1) to reach a saturation temperature of 211° at 20 ata.
C and the accumulator (
14), and the upper space (18) is 20 et
The pressure inside the accumulator becomes 20 ata as the accumulator is filled with a O saturated gas. On the other hand, about 33 toll of condensate, which is discharged from the accumulator (14) without charge and worked in the turbine (5), is transferred to the make-up water tank (9).
and a pump (10) in the heat exchanger II (13) for example with cylinder cold instant fresh water 85 of a Niesel engine.
°C to 75 °C, - day and night.
The water is supplied to the suction pipe section of the water pump (3), that is, the Fil of the accumulator (14), approximately evenly in a 1 m1111 valve (15) without any change. Therefore, the temperature at the outlet of the feed water pump (3) is about 134°C, which is within a safe temperature range as a countermeasure against low-temperature corrosion of the boiler. Inside the accumulator (14), water is divided into upper and lower high-temperature water at 211°C and lower low-temperature water at 143°C, as described above, and the boundary surface (21) between them descends during heat storage and is free from water. During substitute release, the temperature is lowered throughout with uniform humidity due to mixing by natural circulation 11.

以上に述ぺたようにこの発明によればボイラが常に温水
ボイラとして運転されるからボイラ伝熱管内での温水の
蒸発はなく、ボイラへの和水温度も一定で出口温度も一
定に制御され、従ってボイラの伝熱面積を有効利用して
燃焼ガスの熱エネルギー又は廃熱を高能率で回収でき、
アキュムレータ内に多数O無代噴出ノズル等を設けずに
済み、ディーゼル発電設備のピーク負荷時に電力補給を
行なうための補助電源設備を祉じめとする各aill蒸
1  汽消費設備の無泡供給装置として好適なシステム
を構成し得るものである。
As mentioned above, according to the present invention, the boiler is always operated as a hot water boiler, so there is no evaporation of hot water in the boiler heat exchanger tubes, the temperature of the water added to the boiler is constant, and the outlet temperature is also controlled to be constant. Therefore, the thermal energy or waste heat of combustion gas can be recovered with high efficiency by effectively utilizing the heat transfer area of the boiler.
A non-foam supply system for steam consuming equipment for each aill steamer, which eliminates the need to install multiple O-free jet nozzles in the accumulator, and provides auxiliary power equipment for supplying power during peak loads of diesel power generation equipment. A suitable system can be constructed as follows.

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

第1図は従来の廃熱回収発電システムの一例を示す系統
図、第2図はこの発明の実施例を示す系統図である。 (1)工廃熱ボイラ、(5):タービン、(6)二発電
機、(14) :たて形変圧形無代アキュムレータ、(
16);絞り制御弁、−(22) :筒状体。 代理人 弁理士  佐 藤 正 年
FIG. 1 is a system diagram showing an example of a conventional waste heat recovery power generation system, and FIG. 2 is a system diagram showing an embodiment of the present invention. (1) Industrial waste heat boiler, (5): Turbine, (6) Two generators, (14): Vertical transformer typeless accumulator, (
16): Throttle control valve, -(22): Cylindrical body. Agent Patent Attorney Masatoshi Sato

Claims (1)

【特許請求の範囲】 (1)ボイラで発生し良熱エネルギーを無泡アキュムレ
ータに蓄熱し、所要時に該アキュムレータテ蒸汽を発生
させて無代消費設備へ該無代を供給するKI91シ、前
記ボイラを温水ボイラとして制御運転して給水を前記ア
キュムレータの最高圧の飽和湿度まで昇温し、これを前
記アキュムレータの上部へ送り込むことによ抄了キュム
レータ内の上部空間を前記最高圧の飽和無代で満すと共
にその下86に蓄熱した高温水とさらにその下部に該ア
キュムレータの無代放出時の最低圧飽和温度に相当する
低温水との二層水を満すようにし、所要時に前記アキュ
ムレータから自己蒸発する無代を無代消費設備に供給し
て、前記アキュムレータ内の無代放出後の低温水と補給
水との混合水を前記ボイラへ供給することを特徴とする
無泡供給方法0(2)  ボイラと、該ボイラで発生し
た熱エネルギーを蓄熱する無泡アキュムレータとを備え
、赦アキュムレータから所要時に放出される無代を無代
消費設備へ供給する無代供給装置にお−て、前記ボイラ
を温水ボイラとして運転するためにボイラからの高温水
の温度が前記アキュムレータの最高圧の飽和温度となる
ように開度調整される絞り制御弁をボイラの高温水出口
管とアキュムレータとの間Km続したことを特徴とする
無代供給装置。 (3)  無代アキ二ムレータが立て形のものであって
、その内部に、熱エネルギー貯蔵時には温水の整流用と
して1L蒸無代出時には温水の自然循環促進用として働
く筒状体を有することを特徴とする特許請求の範囲第2
項に記載の無代供給装置、
[Scope of Claims] (1) KI91 system, which stores good thermal energy generated in a boiler in a non-foam accumulator, generates steam from the accumulator when necessary, and supplies the non-foam to non-foam consuming equipment; is controlled and operated as a hot water boiler to raise the temperature of the feed water to the maximum pressure and saturated humidity of the accumulator, and sends this to the upper part of the accumulator, thereby filling the upper space in the water-extracting accumulator with the maximum pressure and saturation humidity. At the same time, the layer 86 is filled with two layers of water: high-temperature water stored in the lower part 86, and low-temperature water corresponding to the lowest pressure saturation temperature of the accumulator at the time of free discharge, and when necessary, the water is self-released from the accumulator. A bubble-free supply method 0 (2) characterized in that the evaporated water is supplied to the water-free consumption equipment, and the mixed water of low-temperature water and make-up water after the water discharge in the accumulator is supplied to the boiler. ) A non-foam supply device comprising a boiler and a non-foam accumulator for storing thermal energy generated in the boiler, and supplies non-foam gas released from the non-foam accumulator to non-foam consumption equipment when required; In order to operate the boiler as a hot water boiler, a throttle control valve whose opening is adjusted so that the temperature of the high temperature water from the boiler reaches the saturation temperature of the highest pressure of the accumulator is connected between the high temperature water outlet pipe of the boiler and the accumulator. A free supply device characterized by the following. (3) The non-volatile accumulator is of vertical shape, and has a cylindrical body inside thereof that functions to rectify hot water when storing thermal energy and to promote natural circulation of hot water when discharging 1L steam. The second claim characterized in
The free supply device described in paragraph
JP1810382A 1982-02-09 1982-02-09 Feeding of steam by boiler and steam accumulator and apparatus thereof Pending JPS58138211A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1810382A JPS58138211A (en) 1982-02-09 1982-02-09 Feeding of steam by boiler and steam accumulator and apparatus thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1810382A JPS58138211A (en) 1982-02-09 1982-02-09 Feeding of steam by boiler and steam accumulator and apparatus thereof

Publications (1)

Publication Number Publication Date
JPS58138211A true JPS58138211A (en) 1983-08-17

Family

ID=11962286

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1810382A Pending JPS58138211A (en) 1982-02-09 1982-02-09 Feeding of steam by boiler and steam accumulator and apparatus thereof

Country Status (1)

Country Link
JP (1) JPS58138211A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0255806A (en) * 1988-08-16 1990-02-26 Shinei Kk Vertical type steam accumulator
CN107013897A (en) * 2017-05-26 2017-08-04 山西臣功新能源科技有限公司 A kind of accumulation of heat steam-type boiler
CN112146104A (en) * 2020-09-29 2020-12-29 无锡华光环保能源集团股份有限公司 External reheater system of garbage furnace
WO2021076083A3 (en) * 2019-10-16 2021-05-20 Maxeff Teknoloji̇ Anoni̇m Şi̇rketi̇ A mechanical energy generation system with energy recovery and a method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0255806A (en) * 1988-08-16 1990-02-26 Shinei Kk Vertical type steam accumulator
CN107013897A (en) * 2017-05-26 2017-08-04 山西臣功新能源科技有限公司 A kind of accumulation of heat steam-type boiler
WO2021076083A3 (en) * 2019-10-16 2021-05-20 Maxeff Teknoloji̇ Anoni̇m Şi̇rketi̇ A mechanical energy generation system with energy recovery and a method thereof
CN112146104A (en) * 2020-09-29 2020-12-29 无锡华光环保能源集团股份有限公司 External reheater system of garbage furnace

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