JPS59508A - Electric power generation and apparatus by boiler and hot-water accumulator - Google Patents
Electric power generation and apparatus by boiler and hot-water accumulatorInfo
- Publication number
- JPS59508A JPS59508A JP10975682A JP10975682A JPS59508A JP S59508 A JPS59508 A JP S59508A JP 10975682 A JP10975682 A JP 10975682A JP 10975682 A JP10975682 A JP 10975682A JP S59508 A JPS59508 A JP S59508A
- Authority
- JP
- Japan
- Prior art keywords
- water
- accumulator
- boiler
- temperature
- turbine
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K21/00—Steam engine plants not otherwise provided for
- F01K21/005—Steam engine plants not otherwise provided for using mixtures of liquid and steam or evaporation of a liquid by expansion
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
Description
【発明の詳細な説明】
この発明は、ボイラと熱水アキュムレータによる発電方
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 method and apparatus for power generation using a boiler and a hot water accumulator.
ボイラで発生しだ熱エネルギーを蒸汽アキュムレータに
蓄えながら、所要時にこれを放出して発生蒸汽をタービ
ン発電機等に供給して発電するシステムには種々の方法
がある。例えば、離島等において給電用に供されるディ
ーゼル発電機等による発電システムの場合、その尖頭負
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蒸
汽アキュムレータに蓄えておいて、尖頭負荷時にアキュ
ムレータか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 various methods for generating electricity by storing thermal energy generated in a boiler in a steam accumulator and releasing it when necessary to supply the generated steam to a turbine generator or the like. For example, in the case of a power generation system using a diesel generator, etc. used for power supply on remote islands, etc., in order to cover the electricity during peak loads, a waste heat boiler is attached to recover the waste heat of the diesel engine, and the recovered thermal energy is is stored in a steam accumulator, and at peak load, steam is released from the accumulator to drive a turbine generator.
Electric power generated by this turbine generator is supplied to a 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ム構成は第1図に示す
通りである。すなわち第1図において、従来この種の発
電システムは、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)に
汽水分離器Q)およヒ給水ホンプ(6)を接続してなる
ボイラ系ト、コノボイラ系から発生した蒸汽を温水とし
て蓄える変圧形蒸汽アキュムレータ(4)および蒸汽タ
ービン(5)を駆動し発電機(6)により発電するター
ビン系とから成り、例えば午前中の低負荷時にディーゼ
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、夕方の尖頭負荷時にアキュムレ
ータ(4)の圧力を下けつつ所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を機(
6)から電力を得て、ディーゼル発電機の出力を補ぎな
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)、補給水ポンプ(1o)および給水加
熱器(11)を経て汽水分離器(2)の給水側に戻り、
再びボイラ(1)へ循環する。A general system configuration conventionally used as a waste heat recovery turbine power generation system for this purpose is as shown in FIG. In other words, in Fig. 1, this type of power generation system conventionally includes a waste heat boiler (1) that is operated using waste heat of exhaust gas from the engine exhaust system of diesel power generation equipment, a steam separator Q) and a water supply pump ( 6), a variable pressure steam accumulator (4) that stores the steam generated from the cono boiler system as hot water, and a turbine system that drives a steam turbine (5) and generates electricity with a generator (6). For example, during low load in the morning, waste heat from diesel power generation equipment is recovered in the boiler (1) and stored in the accumulator (4), and during peak load in the evening, the pressure in the accumulator (4) is lowered and the required amount is recovered. is evaporated and turns the turbine (5), which triggers the turbine (5).
6) to supplement the output of the diesel generator. In this case, the steam used to generate power within the turbine (5) is the condenser (7), condensate pump (8), make-up water tank (9), make-up water pump (1o), and feed water heater (11). It returns to the water supply side of the brackish water separator (2) through
It circulates again to the boiler (1).
このような従来の発電システムでは、ボイラ圧カフ キ
ュムレータ(4)の最高圧に配管及びアキュムレータ(
4)内の蒸汽噴出ノズルの抵抗等を上載せした一定圧に
保た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温度以上となる。この
ため廃熱ボイラ(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積を多く要するな
どの欠点が避けられず、特にアキュムレータ(4)の変
圧レンジを大きくとって単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る。In such conventional power generation systems, the highest pressure of the boiler pressure cuff accumulator (4) is connected to piping and the accumulator (4).
4) The boiler (1) is operated so as to maintain a constant pressure including the resistance of the steam jet nozzle, etc., and therefore the temperature of the heat transfer surface of the boiler (1) becomes higher than the saturation temperature of the operating boiler pressure. For this reason, disadvantages such as narrowing the waste heat recovery limit in the waste heat boiler (1) and requiring a large heat transfer area for the same amount of heat recovery cannot be avoided. However, if an attempt is made to increase the amount of heat storage per unit volume, the tendency of the above-mentioned drawbacks will increase as the boiler pressure increases.
この発明は前述の諸欠点を除き、経済的に有利な発電シ
ステムであり、荷に離島等において給電用に供されるデ
ィーゼル発電機等による発電システムにおいて、廃熱用
温水ボイラを設け、回収熱エネルギーを高圧温水として
アキュムレータニ蓄え、尖頭負荷時に熱水を供給し、タ
ービン発電機を駆動し発電するに際し高能率なシステム
を提供することを目的としたものである。This invention is an economically advantageous power generation system that eliminates the above-mentioned drawbacks.In a power generation system using a diesel generator or the like that is used for power supply on remote islands etc., this invention is equipped with a hot water boiler for waste heat and recovers heat. The purpose of this system is to store energy in the form of high-pressure hot water in an accumulator, supply hot water at peak loads, and provide a highly efficient system for driving turbine generators and generating electricity.
すなわちこの発明においては、ボイラで高圧高温水を発
生し、これを熱水アキュムレータに蓄蔵し、所要時に高
温水を高圧の状態で取出し、動力発生設備であるタービ
ン系に供給するに際し、前記アキュムレータを立て形と
し、アキュムレータ上部に高温水、下部に動力発生設備
に使用後の戻り水を低温水とし上下二層に貯え又、高温
水の上部に空隙を設けて高温水の飽和蒸汽を蓄えること
により、アキュムレータ器内を高温水の飽和圧力で満す
ものである。That is, in this invention, high-pressure, high-temperature water is generated in a boiler, stored in a hot water accumulator, and when required, the high-temperature water is taken out in a high-pressure state and supplied to a turbine system that is power generation equipment. The accumulator is vertically shaped, with high-temperature water in the upper part of the accumulator and low-temperature water in the lower part of the accumulator that returns after being used for the power generation equipment, and is stored in upper and lower layers.Also, a gap is provided above the high-temperature water to store saturated steam of the high-temperature water. This fills the inside of the accumulator with the saturation pressure of high-temperature water.
又動力発生設備である熱水タービンで得られる低温圧力
水は温度圧力を失うことなく、又蒸汽タービンからの復
水は出来れば熱エネルギー回収後直ちにアキュムレータ
下部に戻すことにより、アキュムレータ内に常に一定量
の液を貯えることによりアキュムレータ上部の高温域部
よりの高温水の取出しに支障を与えず又アキュムレータ
下部よリボイラ給水ポンプにより常に硫酸腐蝕を生ぜし
めない適切な温度の給水をボイラに供給可能ならしめる
ものである。この場合、装置としては、前記アキュムレ
ータ内部に整流用及び自然循環促進用の筒状体を軸心に
平行に配置し、かつアキュムレータ内上部に上層の高温
水を蒸汽を捲込まずに集水供給する集水器を備え、更に
前記ボイラからの高圧高温水温度を制御する弁及び制御
機構と、アキュムレータ内部の液位を一定にするための
戻り水を制御する弁及び制御機構等からなるボイラ系と
、熱水タービンと蒸汽タービンとが連結されかつ夫々に
復水機構とを備えたことからなるタービン系とから構成
されたものである。In addition, the low-temperature pressure water obtained from the hot water turbine, which is a power generation equipment, does not lose its temperature and pressure, and the condensed water from the steam turbine is returned to the bottom of the accumulator immediately after recovering thermal energy, so that it is always kept constant in the accumulator. By storing a certain amount of liquid, it is possible to supply water to the boiler at an appropriate temperature that does not cause sulfuric acid corrosion without causing any hindrance to the removal of high-temperature water from the high-temperature area at the top of the accumulator, and from the bottom of the accumulator using the reboiler water supply pump. It is something to tighten. In this case, the device is such that a cylindrical body for rectifying flow and promoting natural circulation is placed inside the accumulator parallel to the axis, and the upper layer of high-temperature water is collected and supplied to the upper part of the accumulator without introducing steam. A boiler system comprising a water collector, a valve and a control mechanism for controlling the temperature of high-pressure, high-temperature water from the boiler, and a valve and control mechanism for controlling return water to keep the liquid level inside the accumulator constant. and a turbine system consisting of a hot water turbine and a steam turbine connected to each other, each of which is equipped with a condensing mechanism.
本発明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。第2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、第1図と同一
符号のものは同効のものを示す。(1)は廃熱ボイラ、
(6)はボイラ給水ポンプ、(5つは熱水タービン、(
5)は蒸汽タービン、(6)は発電機、(7)は蒸汽コ
ンデンサ、[F])は復水ポンプ、(9)は補給水タン
ク、(10)は復水返送ポンプ、(13)は復水加熱用
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冷却水と蒸汽コンデンサ(7
)からの復水との熱交換を行なうもの、(7′)は汽水
分離タンク、(10’)はフラッシング水返送ポンプ、
(15)は補給水流量制御弁、(15’)は戻り水制御
弁、(25)は戻り水制御器、(16)は温水の絞り制
御弁、(17)は給水制御器、(18)は熱水アキュム
レータ蒸汽部空間、(19)は熱水アキュムレータ内高
温水、(20)は同低温水、(21)は高温水と低温水
との境界面、(22)は筒状体、(20)は高温水の集
水器、(24)はアキュムレータ本体を示すものである
。Embodiments using the present invention will be described below with reference to the drawings. FIG. 2 is a system diagram showing the configuration of a waste heat recovery power generation system according to an embodiment of the present invention, and the same reference numerals as in FIG. 1 indicate the same effects. (1) is a waste heat boiler,
(6) is a boiler feed water pump, (5 is a hot water turbine, (
5) is a steam turbine, (6) is a generator, (7) is a steam condenser, [F]) is a condensate pump, (9) is a makeup water tank, (10) is a condensate return pump, (13) is A heat exchanger for condensate heating, for example, between the engine cooling water of a diesel generator that recovers waste heat in the boiler (1) and the steam condenser (7).
), (7') is a brackish water separation tank, (10') is a flushing water return pump,
(15) is a makeup water flow control valve, (15') is a return water control valve, (25) is a return water controller, (16) is a hot water throttle control valve, (17) is a water supply controller, (18) is the steam space of the hot water accumulator, (19) is the high temperature water in the hot water accumulator, (20) is the low temperature water, (21) is the interface between high temperature water and low temperature water, (22) is the cylindrical body, ( 20) is a high-temperature water collector, and (24) is an accumulator body.
この発明のシステムにおけるボイラ系では、ボイラ(1
)はその出口管に介装された絞り制御弁(16)を介し
てアキュムレータ(24)および給水ポンプ(6)とル
ープを構成し、一方、タービン系もこのアキュムレータ
(24)を介してループを閉じている。In the boiler system in the system of this invention, the boiler (1
) forms a loop with the accumulator (24) and the water supply pump (6) via the throttle control valve (16) installed in its outlet pipe, while the turbine system also forms a loop via the accumulator (24). Closed.
絞り制御弁(16)は、温水出口温度制御装置(17)
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調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(24)
の最高圧に対応する飽和温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、その出口管からの高温水は制御弁(16
)を通過したのちにアキュムレータ(24)の上部空間
(18)に送り込む。アキュムレータ(24)の上部空
間(18)はその最高圧の飽和蒸汽に満されることにな
り、その下部に蓄熱した高温水(19)とさらにその下
部にアキュムレータの最低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。The throttle control valve (16) is a hot water outlet temperature control device (17)
By monitoring the hot water temperature in the outlet pipe of the boiler (1) and controlling the outlet pipe hot water flow rate by adjusting the opening,
The hot water temperature at the outlet of the boiler (1) is measured by the accumulator (24).
The temperature is maintained at the saturation temperature corresponding to the maximum pressure of The boiler (1) is operated as a hot water boiler under the control of the throttle control valve (16), and high temperature water from the outlet pipe is passed through the control valve (16).
) and then sent into the upper space (18) of the accumulator (24). The upper space (18) of the accumulator (24) is filled with saturated steam at its highest pressure, and the lower part contains high-temperature water (19) that has stored heat, and the lower part contains low-temperature water at the saturation temperature of the lowest pressure of the accumulator. (20
) is stored as two-layer water with an interface (21) in between.
アキュムレータ(24)内にはこの二層水の貯水のため
に筒状体(22)が配設され、フラッシング等による境
界面の乱れをその整流作用によって防止するものである
。、更に前記アキュムレータ(24)向上部に上層の高
温水を集め、かつ内部で渦流の発生を防止し蒸汽を捲込
まずに取出し供給する集水器(23)を備えている。熱
水タービン(5′ンへは所要時にアキュムレータ(24
)の上部の集水器(23)により集水した高温水を取出
しタービン入口制御弁(12)を介して供給される。熱
水タービン(51で発電に利用された蒸汽は蒸水分離器
(7勺で7ラツシングされたのち減圧後の飽和蒸汽を蒸
汽タービン(5)に供給し発電機(6)により復水器(
7)の真空圧損の断熱膨張に相当する発電を行なう。蒸
汽タービン(5)内で動力に利用された蒸汽は復水器V
)で復水ポンプ(8)を介して補給水タンク(9)に送
られ、ポンプ(10) ’e介して復水加熱用熱交換器
(13)で加熱されたのちに制御弁(15)を介して、
汽水分離器(7′)によって分離されたフラッシング水
とフラッシング水返送ポンプ(10’)を介して所定温
度に混合され、アキュムレータ(24)の下部に戻され
る。これら復水の戻り水の流量はアキュムレータ内部の
液位を一定にするため、戻り水制御弁(15’)を介し
てアキュムレータ(24)内のレベルを検出しく図示せ
ず)戻り水制御器(25)によって制御し、アキュムレ
ータ(24)の下部に供給し、再びボイラ(1)へ給水
ポツプ(9を介して供給される。A cylindrical body (22) is disposed within the accumulator (24) to store this two-layer water, and its rectifying action prevents disturbances at the interface due to flushing or the like. Furthermore, the accumulator (24) is further provided with a water collector (23) which collects the high temperature water in the upper layer in the upper part thereof, prevents the generation of vortices therein, and extracts and supplies steam without drawing it in. The accumulator (24
) The high temperature water collected by the water collector (23) at the upper part of the turbine is taken out and supplied through the turbine inlet control valve (12). The steam used for power generation in the hot water turbine (51) is lashed 7 times in a steam separator (7), and then the saturated steam after depressurization is supplied to the steam turbine (5), which is then sent to the condenser (5) by the generator (6).
7) Power generation corresponding to the adiabatic expansion of vacuum pressure loss is performed. The steam used for power in the steam turbine (5) is transferred to the condenser V.
) is sent to the make-up water tank (9) via the condensate pump (8), heated by the condensate heating heat exchanger (13) via the pump (10), and then heated by the control valve (15). Via
The flushing water separated by the brackish water separator (7') is mixed to a predetermined temperature via the flushing water return pump (10') and returned to the lower part of the accumulator (24). In order to keep the liquid level inside the accumulator constant, the flow rate of the return water of these condensates is determined by detecting the level inside the accumulator (24) via the return water control valve (15'). 25) and is fed to the lower part of the accumulator (24) and again to the boiler (1) via the water supply pot (9).
本装置は前記の構成をとることにより、高圧高温水をボ
イラで製造し、得られた高圧高温水をアキュムレータに
貯え、需要時に高温水を取出しり−ビン系に供給し発電
すると共に、戻り水を再びアキュムレータに蓄えるもの
で、アキュムレータ・・内部は常に一定容量即ち同一水
準に温水を蓄え、上部は高温水、下部に低温水父上部空
間には高温水の飽和蒸気を充満せしめ、アキュムレータ
内全体は高温水の飽和圧力となっていることを特徴とし
ている。With the above configuration, this device produces high-pressure, high-temperature water in a boiler, stores the obtained high-pressure, high-temperature water in an accumulator, and takes out the high-temperature water when needed and supplies it to the bottle system to generate electricity. The inside of the accumulator always stores hot water at a constant volume, that is, at the same level.The upper space is filled with high-temperature water, the lower part is with low-temperature water, and the upper space is filled with saturated steam of high-temperature water, and the entire inside of the accumulator is filled with saturated steam of high-temperature water. is characterized by the saturation pressure of high temperature water.
この発明のひとつの実施例において、ディーゼル機関の
廃ガスボイラ(1)によって2 Q ataの飽和温度
211℃の飽和水がアキュムレータ(24)上部より供
給される。アキュムレータ(24)下部には熱水タービ
ン(5勺にて4 ata迄膨張したのち汽水分離器(7
勺にて4 ata飽和飽和蒸発離した後の4ata14
3Cの飽和水と、汽水分離器(7′)にて分離後の飽和
蒸気が蒸気タービン(5)にて0.1ata迄膨張仕事
即ち発電した後蒸汽コンデンサ(7)→復水ポンプ(8
)→補給水タンク<9)→復水返送ポンプ(10)を経
て、ディーゼル機関冷却清水85Cにて75C迄復水加
熱々交換器(16)にて加熱された復水と混合し約16
4Cの戻り水となり、戻り水制御弁(15’)を介して
低温水として蓄えられる。蓄熱は通常終日行々われ、ア
キュムレータ(24)下部の低温水(20)がボイラ給
水ポンプ(6)を介して給水され、ボイラ出口の温度調
節絞9弁(16)によって計画の高温水温度に調節され
てアキュムレータ(24)の上部より供給する。この際
のボイラは蒸発することなく温水ボイラとして廃ガスと
完全対向流となるため充分な温度差が得られるため少い
伝熱面積が良い。又本発明は熱水タービンと蒸気タービ
ンを連結配置し、アキュムレータ(24)の表層高温水
を効率良く集めかつ取出し、高温水のみを熱水タービン
に先ず供給することにより、高圧高温水の熱エネルギー
を熱水タービンで回収することにより機械的出力が増大
する。In one embodiment of the invention, 2 Q ata of saturated water with a saturation temperature of 211° C. is supplied from the upper part of the accumulator (24) by the waste gas boiler (1) of the diesel engine. At the bottom of the accumulator (24), there is a hot water turbine (expanded to 4 ata at 5 increments, and then a brackish water separator (7 ata).
4ata14 after evaporation to saturation of 4ata in a vacuum cleaner
The 3C saturated water and the saturated steam separated in the steam water separator (7') are expanded to 0.1 ata in the steam turbine (5), that is, generate electricity, and then transferred to the steam condenser (7) → condensate pump (8).
) → Make-up water tank <9) → Via the condensate return pump (10), it is mixed with condensate heated in the condensate heating exchanger (16) until it reaches 75C with diesel engine cooling fresh water of 85C, and is mixed with condensate heated in the condensate heating exchanger (16).
The return water becomes 4C and is stored as low temperature water via the return water control valve (15'). Heat storage is normally carried out throughout the day, and the low temperature water (20) at the bottom of the accumulator (24) is supplied via the boiler feed pump (6), and the planned high temperature water temperature is maintained by the nine temperature control throttle valves (16) at the boiler outlet. It is regulated and supplied from the top of the accumulator (24). In this case, the boiler is a hot water boiler without evaporation, and the flow is completely opposite to the waste gas, so a sufficient temperature difference can be obtained, so a small heat transfer area is good. In addition, the present invention connects and arranges a hot water turbine and a steam turbine, efficiently collects and takes out the surface high temperature water of the accumulator (24), and supplies only the high temperature water to the hot water turbine first, thereby converting the thermal energy of the high pressure and high temperature water. Mechanical output is increased by recovering the water using a hydrothermal turbine.
即ちタービン系において、20ataの高圧飽和水を蒸
気タービンにて熱エネルギーを回収する場合一端A a
ta迄スロスロットリングた後減圧後の飽和蒸気により
復水器真空正文断熱膨張仕事をするのに対し、本発明法
では高圧温水がそのままd ata迄断熱膨張仕事をし
だ後4 ataの飽和蒸気により再び復水器真空正文仕
事をするので、同一回収熱量に拘らず数10チの機械的
出力(電力)増が得られる。尚熱水タービン出口の圧力
温水を減圧することなく、熱水アキュムレータに戻すこ
とにより、再びボイラに給水するための加圧エネルギー
の節減が出来ると共にボイラ入口給水温度をボイラ管の
酸腐蝕を生ぜめ温度例えば163.5Cの保持が容易で
ある等積々の利点をもつものである。That is, in a turbine system, when recovering thermal energy from 20 ata of high-pressure saturated water using a steam turbine, at one end A a
In contrast, in the method of the present invention, high-pressure hot water performs adiabatic expansion work until d ata and then saturated steam at 4 ata after being throttled up to ta and then performing adiabatic expansion work on the condenser vacuum with saturated steam after depressurization. Since the condenser vacuum works again, an increase in mechanical output (power) of several tens of inches can be obtained despite the same amount of recovered heat. By returning the pressure hot water at the outlet of the hot water turbine to the hot water accumulator without reducing the pressure, it is possible to save the pressurizing energy required to supply water to the boiler again, and to reduce the temperature of the water supply at the boiler inlet, which may cause acid corrosion of the boiler tubes. It has many advantages, such as the fact that it is easy to maintain a temperature of, for example, 163.5C.
以上に述べ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のでボイラ伝熱管内での温水の
蒸発はなく、ボイラへの給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に利用で
き、又タービン系の復水を減圧することなくアキュムレ
ータ下部に戻しアキュムレータ内の液量を一定に保持し
うるので燃焼ガスの熱エネルギー又は廃熱を高能率に回
収でき、回収熱エネルギーを前述の如きタービン系に構
成することにより発電効率の増加が期待できる。更にア
キュムレータは従来のように多数の蒸気噴出ノズル等を
設ける複雑な機構を設けずに済み、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等のだめに好適な発
電方法および発電装置である。As described 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 supplied to the boiler is constant, and the outlet temperature is also controlled to be constant. The heat transfer area of the boiler can be used effectively, and the condensate in the turbine system can be returned to the bottom of the accumulator without being decompressed, keeping the liquid level in the accumulator constant, making the thermal energy or waste heat of combustion gas highly efficient. By configuring the recovered thermal energy in the turbine system as described above, an increase in power generation efficiency can be expected. Furthermore, the accumulator does not require a complicated mechanism such as a large number of steam jetting nozzles as in the past, and is a suitable power generation method and power generation device for supplying power during peak load times of diesel power generation equipment.
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:廃熱ボイラ、5:蒸気タービン、5′:熱水タービ
ン、6:発電機、7′:汽水分離器、15′:戻り水制
御弁、16:絞り制御弁、22:筒状体、23 :集水
器、24:アキュムレータ、25:戻り水制御器。
代理人弁理士 木 村 三 朗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: Waste heat boiler, 5: Steam turbine, 5': Hot water turbine, 6: Generator, 7': Brackish water separator, 15': Return water control valve, 16: Throttle control valve, 22: Cylindrical body, 23: Water collector, 24: Accumulator, 25: Return water controller. Representative Patent Attorney Sanro Kimura
Claims (1)
ータに蓄熱し、該アキュムレータの放出エネルギーで発
電する方法において、前記ボイラを温水ボイラとして制
御運転し、前記アキュムレータは上部空間域、高温水域
、低温水域とを有し、前記アキュムレータから高温水を
取出し熱水タービンに供給し熱エネル、ギーを回収し、
次いで汽水分離器にてi−和蒸汽を分離し、該7ラツシ
ング蒸汽を蒸汽タービンに供給し発電することを特徴と
するボイラと熱水アキュムレータによる発電方法。 (2)前記汽水分離器にて得られた7ラツシング水と前
記蒸気タービンで得られ喪復水とを混合し、前記アキュ
ムレータの低温水域に補給し、ついで前記ボイラの給水
として循環供給することを特徴とする特許請求の範囲第
1項の方法。 (6)前記気水分離器よりのフラッシング水と前記蒸汽
タービンより得られた復水とを混合し、アキュムレータ
の低温域に補給するに際し、前記復水を熱交換器にて熱
交換し、前記アキュムレータの補給水温度を復水の温度
および量にて、制御することを特徴とする特許請求の範
囲第1項の方法。 (4)ボイラで発生した熱エネルギーを熱水アキュムレ
ータに蓄熱し、該アキュムレータの放出エネルギーで発
電する装置において、前記ボイラからの高温水を制御す
る弁および制御機器を、ボイラ出口とアキュムレータ上
部入口との1間に接続し、前記アキュムレータ上部高温
域の熱水を取出し、該熱水を熱水タービンと蒸汽タービ
ンとを一結してなる発電装置に供給し熱エネにギーを回
収発電し、前記熱水タービンおよび蒸気タービンからの
復水を前記アキュムレータへの戻り水として制御使用す
るための弁および制御機器を、前記アキュムレータ下部
に導通する戻シ水導管間に備え、前記アキュムレータ低
温水を前記ボイラの給水として使用するための導管とを
備えたことを特徴とするボイラと熱水アキュムレータと
による発電装置。 (5)熱水アキュムレータが立て形であって、該゛アキ
ュムレータ内部の低温域部に同心円筒状の筒状体を備え
、高温域部に集水器とを備えたことを特徴とする特許請
求の範囲第4項の装置。[Scope of Claims] (1) In a method for storing thermal energy generated in a boiler in a hot water accumulator and generating electricity using the energy released from the accumulator, the boiler is operated in a controlled manner as a hot water boiler, and the accumulator is operated in an upper space area. , has a high-temperature water area and a low-temperature water area, and extracts high-temperature water from the accumulator and supplies it to a hydrothermal turbine to recover thermal energy.
A power generation method using a boiler and a hot water accumulator, characterized in that the i-wa steam is then separated in a steam separator, and the 7 lashing steam is supplied to a steam turbine to generate power. (2) The 7 lashing water obtained from the brackish water separator and the molten condensate water obtained from the steam turbine are mixed, supplied to the low-temperature water area of the accumulator, and then circulated and supplied as feed water to the boiler. The method of claim 1, characterized in: (6) When mixing the flushing water from the steam water separator and the condensate obtained from the steam turbine and replenishing the low temperature region of the accumulator, heat exchange the condensate with a heat exchanger, 2. The method according to claim 1, wherein the temperature of make-up water in the accumulator is controlled by the temperature and amount of condensate. (4) In a device that stores thermal energy generated in a boiler in a hot water accumulator and uses the energy released from the accumulator to generate electricity, a valve and control equipment for controlling high-temperature water from the boiler are connected to the outlet of the boiler and the upper inlet of the accumulator. The hot water in the upper high temperature area of the accumulator is taken out, and the hot water is supplied to a power generation device consisting of a hot water turbine and a steam turbine, which recovers the heat energy and generates electricity. A valve and a control device for controlling and using condensate from a hot water turbine and a steam turbine as return water to the accumulator are provided between a return water conduit leading to a lower part of the accumulator, and a valve and a control device are provided between the return water conduits leading to the lower part of the accumulator, and the low-temperature water from the accumulator is connected to the boiler. A power generation device comprising a boiler and a hot water accumulator, characterized in that it is equipped with a conduit for use as a water supply. (5) A patent claim characterized in that the hot water accumulator is vertical, and includes a concentric cylindrical body in the low temperature region inside the accumulator, and a water collector in the high temperature region. Devices within the scope of item 4.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10975682A JPS59508A (en) | 1982-06-28 | 1982-06-28 | Electric power generation and apparatus by boiler and hot-water accumulator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10975682A JPS59508A (en) | 1982-06-28 | 1982-06-28 | Electric power generation and apparatus by boiler and hot-water accumulator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59508A true JPS59508A (en) | 1984-01-05 |
Family
ID=14518441
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10975682A Pending JPS59508A (en) | 1982-06-28 | 1982-06-28 | Electric power generation and apparatus by boiler and hot-water accumulator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59508A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01193007A (en) * | 1988-01-29 | 1989-08-03 | Mitsubishi Heavy Ind Ltd | Heat accumulating power generating device |
GB2480713A (en) * | 2009-10-30 | 2011-11-30 | Peter John Bayram | Closed loop cycle using saturated vapour to drive an electrical generator |
-
1982
- 1982-06-28 JP JP10975682A patent/JPS59508A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01193007A (en) * | 1988-01-29 | 1989-08-03 | Mitsubishi Heavy Ind Ltd | Heat accumulating power generating device |
GB2480713A (en) * | 2009-10-30 | 2011-11-30 | Peter John Bayram | Closed loop cycle using saturated vapour to drive an electrical generator |
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