JP2006002729A - Steam turbine plant and moisture separation heater - Google Patents

Steam turbine plant and moisture separation heater Download PDF

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JP2006002729A
JP2006002729A JP2004182578A JP2004182578A JP2006002729A JP 2006002729 A JP2006002729 A JP 2006002729A JP 2004182578 A JP2004182578 A JP 2004182578A JP 2004182578 A JP2004182578 A JP 2004182578A JP 2006002729 A JP2006002729 A JP 2006002729A
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steam turbine
pressure steam
heater
steam
moisture
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Masayuki Nagasawa
正幸 長澤
Kiichi Hamaura
紀一 浜浦
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Hitachi Ltd
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Hitachi Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a steam turbine plant provided with a means increasing energy efficiency of the plant by efficiently collecting energy which moisture separation heater vent steam has and a moisture separation heater for that. <P>SOLUTION: This steam turbine plant includes a steam generating source 1, a high pressure steam turbine 3, and a low pressure steam turbine 7 driven by exhaust steam from the high pressure steam turbine 3. The plant is provided with the moisture separation heater 4 installed between the high pressure steam turbine 3 and the low pressure steam turbine 7, separating and removing moisture of exhaust steam from the high pressure steam turbine 3, and having heaters 5, 6 heating high pressure steam turbine exhaust steam from which moisture is separated and removed by part of main steam and high pressure turbine bleed steam built therein. Each heater vent pipe 19, 20 of the moisture separation heater 4 is connected to the high pressure steam turbine 3 respectively to increase efficiency of the high pressure turbine 3. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、蒸気タービンプラントに係り、特に、高圧蒸気タービンと低圧蒸気タービンとの間に湿分分離加熱器を備えている蒸気タービンプラントの熱効率の改善に関する。   The present invention relates to a steam turbine plant, and more particularly, to improvement of thermal efficiency of a steam turbine plant including a moisture separator heater between a high-pressure steam turbine and a low-pressure steam turbine.

原子力発電プラントなどに採用されている蒸気タービンプラントでは、高圧蒸気タービンと、この高圧蒸気タービンからの排気蒸気により駆動される低圧蒸気タービンとを備えていることが多い。高圧蒸気タービンと低圧蒸気タービンとの間には、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器が設置されており、近年では、高効率化のために湿分を分離除去した排気蒸気を加熱する湿分分離加熱器を設置してある。   A steam turbine plant employed in a nuclear power plant or the like often includes a high-pressure steam turbine and a low-pressure steam turbine driven by exhaust steam from the high-pressure steam turbine. A moisture separator is installed between the high-pressure steam turbine and the low-pressure steam turbine to separate and remove moisture from the exhaust steam of the high-pressure steam turbine. In recent years, moisture is separated and removed for higher efficiency. A moisture separator heater for heating the exhaust gas is installed.

また、従来の湿分分離器が設置されている蒸気タービンプラントでも、出力を増加させるためには、湿分分離器を湿分分離器加熱器に置き換えることが有効な手段とされている。   Further, even in a steam turbine plant in which a conventional moisture separator is installed, replacing the moisture separator with a moisture separator heater is an effective means for increasing the output.

湿分分離加熱器の加熱蒸気としては、高温の主蒸気または高圧蒸気タービン抽気蒸気の一部を使用し、加熱蒸気の凝縮により熱交換させる。   As the heating steam of the moisture separation heater, a part of high-temperature main steam or high-pressure steam turbine extraction steam is used, and heat is exchanged by condensation of the heating steam.

伝熱管内での凝縮ドレンの過冷却を防止し、また、加熱器出口水室内の非凝縮ガスを分離除去する目的で、一般的には、ベント蒸気を常時排出している(例えば特許文献1参照)。   In order to prevent overcooling of the condensed drain in the heat transfer tube and to separate and remove the non-condensable gas in the heater outlet water chamber, generally, vent steam is always discharged (for example, Patent Document 1). reference).

このベント蒸気の排出先は、加熱器圧力よりも低圧の個所にする必要がある。従来は、ベント配管を給水加熱器に接続し、ベント蒸気の熱を回収していた。   It is necessary to discharge the vent vapor at a location lower than the heater pressure. Conventionally, vent piping was connected to a feed water heater to recover the heat of vent steam.

特開平09−195713号公報 (第2頁〜第3頁、図2,図3)Japanese Patent Laid-Open No. 09-195713 (pages 2 to 3, FIGS. 2 and 3)

従来の湿分分離加熱器のベント蒸気排出/熱回収先である給水加熱器は、原子力発電プラントの場合、最も圧力が高い給水加熱器でも主蒸気圧力の1/3程度の圧力であり、ベント蒸気が持っているエネルギーを効率的には回収できていない。   In the case of a nuclear power plant, the feed water heater that is the vent steam discharge / heat recovery destination of the conventional moisture separation heater is about 1/3 of the main steam pressure even in the feed water heater with the highest pressure. The energy possessed by steam cannot be recovered efficiently.

本発明の目的は、湿分分離加熱器ベント蒸気が持つエネルギーを効率的に回収してプラントのエネルギー効率を高める手段を備えた蒸気タービンプラント,既設蒸気タービンプラントの改造方法,新設プラントおよび改造プラントのための湿分分離加熱器を提供することである。   An object of the present invention is to provide a steam turbine plant equipped with means for efficiently recovering the energy of the moisture separation heater vent steam to increase the energy efficiency of the plant, a method for remodeling an existing steam turbine plant, a new plant and a remodeled plant It is to provide a moisture separator heater for.

本発明は、上記目的を達成するために、蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、高圧蒸気タービンの排気蒸気により駆動される低圧蒸気タービンとを含む蒸気タービンプラントにおいて、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を主蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を高圧蒸気タービンと低圧蒸気タービンとの間に備え、加熱器のベント管を高圧蒸気タービンに接続した蒸気タービンプラントを提案する。   In order to achieve the above object, the present invention provides a high-pressure steam turbine including a high-pressure steam turbine driven by main steam from a steam generation source and a low-pressure steam turbine driven by exhaust steam of the high-pressure steam turbine. A moisture separation heater comprising a moisture separator for separating and removing moisture from exhaust steam of a steam turbine and a heater for heating exhaust steam of a high-pressure steam turbine from which moisture has been separated and removed by a part of main steam A steam turbine plant provided between a high-pressure steam turbine and a low-pressure steam turbine and having a heater vent pipe connected to the high-pressure steam turbine is proposed.

本発明は、また、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を高圧蒸気タービンと低圧蒸気タービンとの間に備え、加熱器のベント管を高圧蒸気タービンに接続した蒸気タービンプラントを提案する。   The present invention also heats a moisture separator that separates and removes the moisture of the exhaust steam from the high-pressure steam turbine and a high-pressure steam turbine exhaust steam from which the moisture is separated and removed by a part of the extracted steam of the high-pressure steam turbine. A steam turbine plant is proposed in which a moisture separation heater comprising a heater is provided between a high-pressure steam turbine and a low-pressure steam turbine, and a vent pipe of the heater is connected to the high-pressure steam turbine.

本発明は、さらに、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を主蒸気の一部により加熱する加熱器と湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を高圧蒸気タービンと低圧蒸気タービンとの間に備え、主蒸気の一部により加熱する加熱器のベント管を高圧蒸気タービンに接続し、高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器のベント管も高圧蒸気タービンに接続した蒸気タービンプラントを提案する。   The present invention further includes a moisture separator that separates and removes the moisture of the exhaust steam of the high-pressure steam turbine, a heater that heats the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a part of the main steam, and a humidity. A moisture separation heater comprising a heater for heating the exhaust steam of the high-pressure steam turbine from which the components have been separated and removed by a part of the extracted steam of the high-pressure steam turbine is provided between the high-pressure steam turbine and the low-pressure steam turbine. A steam turbine plant is proposed in which a vent pipe of a heater that is heated by a part of steam is connected to a high-pressure steam turbine, and a vent pipe of a heater that is heated by a part of the extracted steam of the high-pressure steam turbine is also connected to the high-pressure steam turbine. .

本発明は、上記目的を達成するために、蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と、湿分が分離除去された排気蒸気により駆動される低圧蒸気タービンとを含む既設蒸気タービンプラントの改造方法において、湿分分離器を取り外し、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を主蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を高圧蒸気タービンと低圧蒸気タービンとの間に設置し、加熱器のベント管を高圧蒸気タービンに接続する既設蒸気タービンプラントの改造方法を提案する。   In order to achieve the above object, the present invention provides a high-pressure steam turbine driven by main steam from a steam generation source, a moisture separator that separates and removes moisture from the exhaust steam of the high-pressure steam turbine, In a modification method of an existing steam turbine plant including a low-pressure steam turbine driven by exhaust gas separated and removed, a moisture separator that removes a moisture separator and separates and removes moisture of the exhaust steam of the high-pressure steam turbine; A moisture separator heater comprising a heater that heats the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a part of the main steam is installed between the high-pressure steam turbine and the low-pressure steam turbine. A retrofitting method of an existing steam turbine plant that connects a vent pipe to a high-pressure steam turbine is proposed.

本発明は、また、湿分分離器を取り外し、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を高圧蒸気タービンと低圧蒸気タービンとの間に設置し、加熱器のベント管を高圧蒸気タービンに接続する既設蒸気タービンプラントの改造方法を提案する。   The present invention also provides a moisture separator that removes the moisture from the exhaust steam of the high-pressure steam turbine and removes the moisture from the high-pressure steam turbine from which the moisture has been separated and removed. Modification of an existing steam turbine plant in which a moisture separator heater consisting of a heater that heats with a portion of steam is installed between the high-pressure steam turbine and the low-pressure steam turbine, and the vent pipe of the heater is connected to the high-pressure steam turbine Suggest a method.

本発明は、さらに、蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と、湿分が分離除去された排気蒸気により駆動される低圧蒸気タービンとを含む既設蒸気タービンプラントの改造方法において、湿分分離器を取り外し、高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器と前記加熱器により加熱された高圧蒸気タービン排気蒸気を更に主蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を高圧蒸気タービンと低圧蒸気タービンとの間に設置し、主蒸気の一部により加熱する加熱器のベント管を高圧蒸気タービンに接続し、高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器のベント管も高圧蒸気タービンに接続する既設蒸気タービンプラントの改造方法を提案する。   The present invention further includes a high-pressure steam turbine driven by main steam from a steam generation source, a moisture separator that separates and removes moisture from exhaust steam of the high-pressure steam turbine, and exhaust steam from which moisture is separated and removed. In a retrofitting method of an existing steam turbine plant including a low-pressure steam turbine driven by a moisture separator, the moisture separator is removed and the moisture is separated and removed by separating and removing the moisture of the exhaust steam from the high-pressure steam turbine. A heater that heats the exhaust steam of the high-pressure steam turbine by a part of the extraction steam of the high-pressure steam turbine, and a heater that heats the exhaust steam of the high-pressure steam turbine heated by the heater by a part of the main steam. A moisture separator heater is installed between the high-pressure steam turbine and the low-pressure steam turbine, and the vent pipe of the heater that is heated by a part of the main steam is connected to the high-pressure steam turbine. Vent pipe heater for heating the portion of the extraction steam of a steam turbine also proposes a method for retrofitting existing steam turbine plant to be connected to the high pressure steam turbine.

本発明は、上記目的を達成するために、高圧蒸気タービンへの接続口と低圧蒸気タービンへの接続口とを有し高圧蒸気タービンの排気蒸気の湿分を分離除去し低圧蒸気タービンに供給する湿分分離器と、主蒸気管への接続口と高圧蒸気タービン入口への接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を主蒸気の一部により加熱しこの加熱器のベント蒸気を高圧蒸気タービン入口に供給する加熱器とからなる湿分分離加熱器を提案する。   In order to achieve the above object, the present invention has a connection port to a high-pressure steam turbine and a connection port to a low-pressure steam turbine, and separates and removes moisture from the exhaust steam of the high-pressure steam turbine and supplies it to the low-pressure steam turbine. The exhaust steam of the high-pressure steam turbine, which has a moisture separator, a connection port to the main steam pipe and a connection port to the high-pressure steam turbine inlet and from which moisture has been separated and removed, is heated by a part of the main steam. A moisture separator heater is proposed, which comprises a heater for supplying the vent steam of the vessel to the high-pressure steam turbine inlet.

本発明は、また、高圧蒸気タービンへの接続口と低圧蒸気タービンへの接続口とを有し高圧蒸気タービンの排気蒸気の湿分を分離除去し低圧蒸気タービンに供給する湿分分離器と、高圧蒸気タービンの中間段への接続口と当該中間段よりも後段への接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱しこの加熱器のベント蒸気を高圧蒸気タービンの後段に供給する加熱器とからなる湿分分離加熱器を提案する。   The present invention also includes a moisture separator having a connection port to a high-pressure steam turbine and a connection port to a low-pressure steam turbine, and separating and removing moisture from the exhaust steam of the high-pressure steam turbine and supplying the moisture to the low-pressure steam turbine; The exhaust steam of the high-pressure steam turbine, which has a connection port to the intermediate stage of the high-pressure steam turbine and a connection port to the subsequent stage of the intermediate stage and from which moisture has been separated and removed, is heated by a part of the extracted steam of the high-pressure steam turbine A moisture separation heater is proposed which comprises a heater for supplying the vent steam of the heater to a subsequent stage of the high-pressure steam turbine.

本発明は、さらに、高圧蒸気タービンへの接続口と低圧蒸気タービンへの接続口とを有し高圧蒸気タービンの排気蒸気の湿分を分離除去し低圧蒸気タービンに供給する湿分分離器と、主蒸気管への接続口と高圧蒸気タービンへの接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を主蒸気の一部により加熱しこの加熱器のベント蒸気を高圧蒸気タービンに供給する加熱器と、高圧蒸気タービンの中間段への接続口と当該中間段よりも後段への接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱しこの加熱器のベント蒸気を高圧蒸気タービンの後段に供給する加熱器とからなる湿分分離加熱器を提案する。   The present invention further includes a moisture separator having a connection port to the high-pressure steam turbine and a connection port to the low-pressure steam turbine, and separating and removing moisture from the exhaust steam of the high-pressure steam turbine and supplying the moisture to the low-pressure steam turbine; The exhaust steam of the high-pressure steam turbine, which has a connection port to the main steam pipe and a connection port to the high-pressure steam turbine and from which moisture has been separated and removed, is heated by a part of the main steam, and the vent steam of this heater is used as the high-pressure steam. A high-pressure steam turbine is provided with a heater for supplying to the turbine, a connection port to an intermediate stage of the high-pressure steam turbine, and a connection port to a subsequent stage from the intermediate stage, and the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed A moisture separation heater is proposed which comprises a heater that is heated by a part of the extracted steam and supplies a vent steam of the heater to a subsequent stage of the high-pressure steam turbine.

本発明によれば、湿分分離加熱器のベント配管を高圧蒸気タービンに接続し、ベント蒸気を高圧蒸気タービン駆動用蒸気の一部として使用し、ベント蒸気が持つエネルギーを有効活用するので、発電出力が増加するとともに、従来回収していた給水加熱器廻りの配管を単純化し、ベント配管の物量を削減できる。   According to the present invention, the vent pipe of the moisture separation heater is connected to the high-pressure steam turbine, the vent steam is used as part of the steam for driving the high-pressure steam turbine, and the energy of the vent steam is effectively utilized. As the output increases, the piping around the feed water heater, which has been collected in the past, can be simplified and the amount of vent piping can be reduced.

また、ベント蒸気が持つエネルギーを効率的に回収するために接続先を規定した湿分分離加熱器が提供されるので、既設蒸気タービンプラントの湿分分離器に代えて、この湿分分離加熱器を設置すれば、既設の蒸気タービンプラントでも、プラントのエネルギー効率を高めることができる。   In addition, since a moisture separator / heater with a specified connection destination is provided to efficiently recover the energy of the vent steam, this moisture separator / heater can be used instead of the moisture separator of the existing steam turbine plant. If installed, even in an existing steam turbine plant, the energy efficiency of the plant can be increased.

次に、図1〜図3を参照して、本発明による蒸気タービンプラントの実施形態を説明する。   Next, with reference to FIGS. 1-3, embodiment of the steam turbine plant by this invention is described.

実施形態1〜実施形態3は、蒸気タービンプラントを新設する例であり、実施形態4〜6は、既設蒸気タービンプラントを改造する例である。   Embodiments 1 to 3 are examples of newly installing a steam turbine plant, and Embodiments 4 to 6 are examples of modifying an existing steam turbine plant.

≪実施形態1≫
図1は、本発明による蒸気タービンプラントの実施形態1の系統構成を示す図である。
Embodiment 1
FIG. 1 is a diagram showing a system configuration of Embodiment 1 of a steam turbine plant according to the present invention.

実施形態1において、原子炉(蒸気発生源)1で発生した主蒸気は、主蒸気管13および主蒸気止弁/蒸気加減弁2を介して高圧蒸気タービン3に導かれ、高圧蒸気タービン3を駆動する。   In the first embodiment, the main steam generated in the nuclear reactor (steam generation source) 1 is guided to the high-pressure steam turbine 3 through the main steam pipe 13 and the main steam stop valve / steam control valve 2, To drive.

高圧蒸気タービン3の排気蒸気は、クロスアラウンド管14により、湿分分離加熱器4に導かれ、湿分分離加熱器4で湿分を分離除去された後、加熱器5において、主蒸気管13から分岐する主蒸気側加熱蒸気管17を介して導入した主蒸気により加熱される。   The exhaust steam from the high-pressure steam turbine 3 is guided to the moisture separation heater 4 by the cross-around pipe 14, and after the moisture is separated and removed by the moisture separation heater 4, in the heater 5, the main steam pipe 13 The main steam is heated by the main steam introduced through the main steam side heating steam pipe 17 branched from the main steam side.

湿分分離加熱器4で加熱された蒸気は、クロスアラウンド管15により、低圧蒸気タービン7に導かれ、低圧蒸気タービン7を駆動する。   The steam heated by the moisture separator / heater 4 is guided to the low-pressure steam turbine 7 by the cross-around pipe 15 to drive the low-pressure steam turbine 7.

高圧蒸気タービン3および/または低圧蒸気タービン7は、例えば発電機を駆動し、熱エネルギーを電気エネルギーに変換する。   The high-pressure steam turbine 3 and / or the low-pressure steam turbine 7 drives a generator, for example, and converts heat energy into electric energy.

低圧蒸気タービン7の排気蒸気は、復水器8で凝縮される。復水器8で凝縮された復水は、復水ポンプ9により、低圧給水加熱器10に送られ、加熱される。   The exhaust steam from the low-pressure steam turbine 7 is condensed in the condenser 8. The condensate condensed in the condenser 8 is sent to the low-pressure feed water heater 10 by the condensate pump 9 and heated.

低圧給水加熱器10で加熱された復水は、給水ポンプ11により、高圧給水加熱器12に送られ、加熱される。高圧給水加熱器12で加熱された復水は、給水管16により、原子炉(蒸気発生源)1に再び給水される。   The condensed water heated by the low-pressure feed water heater 10 is sent to the high-pressure feed water heater 12 by the feed water pump 11 and heated. The condensate heated by the high-pressure feed water heater 12 is fed again to the reactor (steam generation source) 1 through the feed water pipe 16.

図1の蒸気タービンプラントは、主蒸気の一部を熱源とする加熱器5を湿分分離加熱器4に内蔵している。主蒸気管13の途中から主蒸気の一部を分岐し、加熱蒸気管17により加熱器5に供給する。熱交換により凝縮したドレンは、加熱器ドレン管21により高圧給水加熱器12に回収し、給水加熱源の一部として使用する。   The steam turbine plant of FIG. 1 includes a heater 5 using a part of main steam as a heat source in a moisture separation heater 4. A part of the main steam is branched from the middle of the main steam pipe 13 and supplied to the heater 5 through the heating steam pipe 17. The drain condensed by heat exchange is collected in the high-pressure feed water heater 12 by the heater drain pipe 21 and used as a part of the feed water heating source.

従来は、加熱器5において、伝熱管内での凝縮ドレンの過冷却を防止し、加熱器出口水室内の非凝縮ガスを分離除去するために、特許文献1に示されていたように、加熱器出口水室からのベント蒸気を常時排出するベント配管を設置し、その接続先を高圧給水加熱器12としていた。   Conventionally, in the heater 5, in order to prevent overcooling of the condensed drain in the heat transfer tube and to separate and remove the non-condensable gas in the heater outlet water chamber, A vent pipe for constantly discharging vent steam from the vessel outlet water chamber was installed, and the connection destination was the high-pressure feed water heater 12.

原子力プラントにおいて、高圧給水加熱器12の器内圧力は、通常主蒸気圧力の約1/3程度になるように設計されており、従来は、加熱器ベント蒸気を約1/3の圧力までオリフィスなどの減圧機構により減圧してから高圧給水加熱器12に回収しており、加熱器ベント蒸気の持つ圧力エネルギーを有効活用していなかった。   In a nuclear power plant, the internal pressure of the high-pressure feed water heater 12 is usually designed to be about 1/3 of the main steam pressure, and conventionally, the heater vent steam is reduced to a pressure of about 1/3. The pressure energy of the heater vent steam has not been effectively utilized since the pressure is reduced by a pressure reducing mechanism such as the above and then recovered in the high pressure feed water heater 12.

これに対して、図1の実施形態1においては、加熱器ベント管19を高圧蒸気タービン3の入口に接続し、ベント蒸気を高圧蒸気タービン3に接続してある。すなわち、加熱器5からのベント蒸気を高圧蒸気タービン駆動用蒸気として使用し、加熱器ベント蒸気が持つエネルギーを有効活用するので、高圧蒸気タービン3の出力を増加させることができる。   In contrast, in the first embodiment of FIG. 1, the heater vent pipe 19 is connected to the inlet of the high-pressure steam turbine 3, and the vent steam is connected to the high-pressure steam turbine 3. That is, since the vent steam from the heater 5 is used as the steam for driving the high-pressure steam turbine and the energy of the heater vent steam is effectively used, the output of the high-pressure steam turbine 3 can be increased.

また、高圧給水加熱器12に接続していた配管が削減され、高圧給水加熱器12周りの配管を簡素化し、ベント配管物量を削減できる。   Moreover, the piping connected to the high-pressure feed water heater 12 is reduced, the piping around the high-pressure feed water heater 12 is simplified, and the amount of vent piping can be reduced.

なお、図1の実施形態1では、主蒸気側加熱蒸気管17,加熱器5,ベント管19の合計圧力損失が、主蒸気止弁/蒸気加減弁2の圧力損失より小さく、加熱器ベント蒸気圧力が、高圧蒸気タービン3の入口圧力より大きい場合を想定した。   1, the total pressure loss of the main steam side heating steam pipe 17, the heater 5, and the vent pipe 19 is smaller than the pressure loss of the main steam stop valve / steam control valve 2, and the heater vent steam The case where the pressure was larger than the inlet pressure of the high-pressure steam turbine 3 was assumed.

逆に、加熱器ベント蒸気圧力が、高圧蒸気タービン3の入口圧力より低くなる場合には、主蒸気ベント管19を高圧蒸気タービン3の初段後など高圧蒸気タービン中間段に接続することになる。   Conversely, when the heater vent steam pressure becomes lower than the inlet pressure of the high-pressure steam turbine 3, the main steam vent pipe 19 is connected to a high-pressure steam turbine intermediate stage such as after the first stage of the high-pressure steam turbine 3.

≪実施形態2≫
図2は、本発明による蒸気タービンプラントの実施形態2の系統構成を示す図である。
<< Embodiment 2 >>
FIG. 2 is a diagram showing a system configuration of Embodiment 2 of the steam turbine plant according to the present invention.

実施形態2は、実施形態1に示した主蒸気の一部を熱源とする加熱器5に代えて、高圧蒸気タービン3の抽気蒸気の一部を熱源とする加熱器6を湿分分離加熱器4に内蔵している。高圧蒸気タービン3の途中段から蒸気の一部を抽気し、加熱蒸気管18により加熱器6に供給する。熱交換により凝縮したドレンは、ドレン管22により高圧給水加熱器12に回収し、給水加熱源の一部として使用する。   In the second embodiment, instead of the heater 5 using a part of the main steam shown in the first embodiment as a heat source, a heater 6 using a part of the extracted steam of the high-pressure steam turbine 3 as a heat source is used as a moisture separation heater. 4 is built in. A part of the steam is extracted from the middle stage of the high-pressure steam turbine 3 and supplied to the heater 6 through the heating steam pipe 18. The drain condensed by heat exchange is collected in the high-pressure feed water heater 12 by the drain pipe 22 and used as a part of the feed water heating source.

図2の実施形態2においては、加熱器ベント管20を高圧蒸気タービン3からの加熱蒸気取り出し段の後続段に接続してある。すなわち、加熱器6からのベント蒸気を高圧蒸気タービン駆動用蒸気として使用し、加熱器ベント蒸気が持つエネルギーを有効活用するので、高圧蒸気タービン3の出力を増加させることができる。   In the second embodiment of FIG. 2, the heater vent pipe 20 is connected to the subsequent stage of the heated steam take-out stage from the high-pressure steam turbine 3. That is, since the vent steam from the heater 6 is used as the steam for driving the high-pressure steam turbine and the energy of the heater vent steam is effectively used, the output of the high-pressure steam turbine 3 can be increased.

また、高圧給水加熱器12に接続していた配管が削減され、高圧給水加熱器12周りの配管を簡素化し、ベント配管物量を削減できる。   Moreover, the piping connected to the high-pressure feed water heater 12 is reduced, the piping around the high-pressure feed water heater 12 is simplified, and the amount of vent piping can be reduced.

≪実施形態3≫
図3は、本発明による蒸気タービンプラントの実施形態3の系統構成を示す図である。
<< Embodiment 3 >>
FIG. 3 is a diagram showing a system configuration of Embodiment 3 of the steam turbine plant according to the present invention.

実施形態3は、実施形態1と実施形態2とを組み合わせたものであり、主蒸気の一部を熱源とする加熱器5と、高圧蒸気タービンの抽気蒸気の一部を熱源とする加熱器6との2段の加熱器を湿分分離加熱器4に内蔵している。   The third embodiment is a combination of the first and second embodiments. The heater 5 uses a part of main steam as a heat source, and the heater 6 uses a part of extracted steam of a high-pressure steam turbine as a heat source. The moisture separation heater 4 is built in the two-stage heater.

加熱器5のベント管19は、高圧蒸気タービン3の入口に接続され、加熱器6のベント管20は、高圧蒸気タービン3からの加熱蒸気取り出し段の後続段に接続され、高圧蒸気タービン3の出力を増加させることができる。   The vent pipe 19 of the heater 5 is connected to the inlet of the high-pressure steam turbine 3, and the vent pipe 20 of the heater 6 is connected to the subsequent stage of the heating steam extraction stage from the high-pressure steam turbine 3, The output can be increased.

主蒸気側加熱蒸気管17,加熱器5,主蒸気側ベント管19の合計圧力損失が、主蒸気止弁/蒸気加減弁2の圧力損失より小さく、加熱器ベント蒸気圧力が、高圧蒸気タービン3の入口圧力より大きい場合を想定した。   The total pressure loss of the main steam side heating steam pipe 17, the heater 5, and the main steam side vent pipe 19 is smaller than the pressure loss of the main steam stop valve / steam control valve 2, and the heater vent steam pressure is higher than that of the high pressure steam turbine 3. It was assumed that the pressure was greater than the inlet pressure.

逆に、加熱器ベント蒸気圧力が、高圧蒸気タービン3の入口圧力より低くなる場合には、主蒸気ベント管19を高圧蒸気タービン3の初段後など高圧蒸気タービン中間段に接続することになる。   Conversely, when the heater vent steam pressure becomes lower than the inlet pressure of the high-pressure steam turbine 3, the main steam vent pipe 19 is connected to a high-pressure steam turbine intermediate stage such as after the first stage of the high-pressure steam turbine 3.

ベント管19を高圧蒸気タービン入口に接続するとともに、高圧蒸気タービン抽気側ベント管20を高圧蒸気タービン3からの加熱蒸気取り出し段の後続段に接続すると、出力をより一層増加させることができる。   When the vent pipe 19 is connected to the high-pressure steam turbine inlet and the high-pressure steam turbine bleed-side vent pipe 20 is connected to the subsequent stage of the heated steam take-out stage from the high-pressure steam turbine 3, the output can be further increased.

なお、実施形態1〜実施形態3においては、熱交換により凝縮したドレンを、ドレン管21および/またはドレン管22により、高圧給水加熱器12に回収したが、熱交換により凝縮したドレンの回収先を低圧給水加熱器10としてもよいし、低圧給水加熱器10および高圧給水加熱器12の双方としてもよい。   In the first to third embodiments, the drain condensed by heat exchange is collected in the high-pressure feed water heater 12 by the drain pipe 21 and / or the drain pipe 22, but the collection destination of the drain condensed by heat exchange. May be the low-pressure feed water heater 10 or both the low-pressure feed water heater 10 and the high-pressure feed water heater 12.

≪実施形態4≫
従来の湿分分離器のみを設置し運転している既設の蒸気タービンプラントでも、出力を増加させるためには、湿分分離器を湿分分離器加熱器で置き換えることが有効な手段となっている。
<< Embodiment 4 >>
Even in an existing steam turbine plant where only a conventional moisture separator is installed and operated, replacing the moisture separator with a moisture separator heater is an effective means to increase output. Yes.

実施形態4は、ここでは図示しない従来の湿分分離器を、湿分が分離除去された高圧蒸気タービン排気蒸気を主蒸気の一部により加熱する湿分分離加熱器4に置き換える例である。   Embodiment 4 is an example in which a conventional moisture separator (not shown) is replaced with a moisture separation heater 4 that heats high-pressure steam turbine exhaust steam from which moisture has been separated and removed by a part of main steam.

従来の湿分分離器に代えて、主蒸気の一部により湿分が分離除去された高圧蒸気タービン排気蒸気を主蒸気の一部により加熱する湿分分離加熱器4を設置する場合、加熱器5を含む図1の湿分分離加熱器4で既設の湿分分離器を置き換えるとともに、加熱蒸気管17と、加熱器ベント管19と、加熱器ドレン管21とを追加する必要がある。   In place of the conventional moisture separator, when the moisture separation heater 4 for heating the high-pressure steam turbine exhaust steam from which the moisture is separated and removed by a part of the main steam is heated by a part of the main steam, 1 is replaced with the existing moisture separator 4, and a heating steam pipe 17, a heater vent pipe 19, and a heater drain pipe 21 need to be added.

従来の湿分分離器のみを設置し運転している既設蒸気タービンプラントをこのように改造すると、実施形態1と同様の効果が得られる。   When an existing steam turbine plant in which only a conventional moisture separator is installed and operated is modified in this way, the same effect as in the first embodiment can be obtained.

≪実施形態5≫
実施形態4は、ここでは図示しない従来の湿分分離器を、湿分が分離除去された高圧蒸気タービン排気蒸気を高圧蒸気タービン抽気蒸気の一部により加熱する湿分分離加熱器4で置き換える例である。
<< Embodiment 5 >>
In the fourth embodiment, a conventional moisture separator (not shown) is replaced with a moisture separation heater 4 that heats the high-pressure steam turbine exhaust steam from which moisture has been separated and removed by a part of the high-pressure steam turbine extraction steam. It is.

従来の湿分分離器に代えて、湿分が分離除去された高圧蒸気タービン排気蒸気を高圧蒸気タービン抽気蒸気の一部により加熱する湿分分離加熱器4を設置する場合、加熱器6を含む図2の湿分分離加熱器4で既設の湿分分離器を置き換えるとともに、加熱蒸気管18と、加熱器ベント管20と、加熱器ドレン管22とを追加する必要がある。   In place of the conventional moisture separator, when installing the moisture separation heater 4 for heating the high-pressure steam turbine exhaust steam from which moisture has been separated and removed by a part of the high-pressure steam turbine extraction steam, the heater 6 is included. It is necessary to replace the existing moisture separator with the moisture separation heater 4 of FIG. 2, and to add a heating steam pipe 18, a heater vent pipe 20, and a heater drain pipe 22.

従来の湿分分離器のみを設置し運転している既設蒸気タービンプラントをこのように改造すると、実施形態2と同様の効果が得られる。   When an existing steam turbine plant in which only a conventional moisture separator is installed and operated is remodeled in this way, the same effect as in the second embodiment can be obtained.

≪実施形態6≫
実施形態6は、ここでは図示しない従来の湿分分離器を、湿分が分離除去された高圧蒸気タービン排気蒸気を主蒸気の一部および高圧蒸気タービン抽気蒸気の一部により加熱する湿分分離加熱器に改造する例である。
Embodiment 6
In Embodiment 6, a conventional moisture separator (not shown) is used to heat the high-pressure steam turbine exhaust steam from which moisture has been separated and removed by using a part of main steam and a part of high-pressure steam turbine extraction steam. This is an example of modification to a heater.

従来の湿分分離器に代えて、湿分が分離除去された高圧蒸気タービン排気蒸気を主蒸気の一部および高圧蒸気タービン抽気蒸気の一部により加熱する湿分分離加熱器4を設置する場合、湿分分離器を加熱器5および加熱器6を含む図3の湿分分離加熱器4で既設の湿分分離器を置き換えるとともに、加熱器5の加熱蒸気管17と、加熱器6の加熱蒸気管18と、加熱器5のベント管19と、加熱器6のベント管20と、加熱器5のドレン管21と、加熱器6のドレン管22とを追加する必要がある。   In place of the conventional moisture separator, when the moisture separator heater 4 is installed to heat the high-pressure steam turbine exhaust steam from which moisture has been separated and removed by a part of the main steam and a part of the high-pressure steam turbine extraction steam The moisture separator is replaced with the existing moisture separator 4 in FIG. 3 including the heater 5 and the heater 6, and the heating steam pipe 17 of the heater 5 and the heating of the heater 6 are heated. It is necessary to add a steam pipe 18, a vent pipe 19 of the heater 5, a vent pipe 20 of the heater 6, a drain pipe 21 of the heater 5, and a drain pipe 22 of the heater 6.

従来の湿分分離器のみを設置し運転している既設蒸気タービンプラントをこのように改造すると、実施形態3と同様の効果が得られる。   When an existing steam turbine plant in which only a conventional moisture separator is installed and operated is remodeled in this way, the same effect as in the third embodiment can be obtained.

本発明による蒸気タービンプラントの実施形態1の系統構成および改造後の実施形態4の系統構成を示す図である。It is a figure which shows the system configuration | structure of Embodiment 1 of the steam turbine plant by this invention, and the system configuration | structure of Embodiment 4 after remodeling. 本発明による蒸気タービンプラントの実施形態2の系統構成および改造後の実施形態5の系統構成を示す図である。It is a figure which shows the system configuration | structure of Embodiment 2 of the steam turbine plant by this invention, and the system configuration | structure of Embodiment 5 after remodeling. 本発明による蒸気タービンプラントの実施形態3の系統構成および改造後の実施形態6の系統構成を示す図である。It is a figure which shows the system configuration | structure of Embodiment 3 of the steam turbine plant by this invention, and the system configuration | structure of Embodiment 6 after remodeling.

符号の説明Explanation of symbols

1 原子炉(蒸気発生源)
2 主蒸気止弁/蒸気加減弁
3 高圧蒸気タービン
4 湿分分離加熱器
5 主蒸気により加熱する加熱器
6 高圧蒸気タービン抽気蒸気により加熱する加熱器
7 低圧蒸気タービン
8 復水器
9 復水ポンプ
10 低圧給水加熱器
11 給水ポンプ
12 高圧給水加熱器
13 主蒸気管
14 高圧蒸気タービン出口クロスアラウンド管
15 湿分分離加熱器出口クロスアラウンド管
16 給水管
17 加熱器5の加熱蒸気管
18 加熱器6の加熱蒸気管
19 加熱器5のベント管
20 加熱器6のベント管
21 加熱器5のドレン管
22 加熱器6のドレン管
23 高圧給水加熱器12への高圧蒸気タービン抽気管
1 Reactor (steam generation source)
2 Main Steam Stop Valve / Steam Control Valve 3 High Pressure Steam Turbine 4 Moisture Separation Heater 5 Heater Heated by Main Steam 6 High Pressure Steam Turbine Heater Heated by Extracted Steam 7 Low Pressure Steam Turbine 8 Condenser 9 Condensate Pump DESCRIPTION OF SYMBOLS 10 Low pressure feed water heater 11 Feed water pump 12 High pressure feed water heater 13 Main steam pipe 14 High pressure steam turbine outlet crossaround pipe 15 Moisture separation heater outlet crossaround pipe 16 Feed water pipe 17 Heating steam pipe 18 of heater 5 Heater 6 Steam pipe 19 of heater 5 Vent pipe 20 of heater 5 Vent pipe 21 of heater 6 Drain pipe 22 of heater 5 Drain pipe 23 of heater 6 High-pressure steam turbine bleed pipe to high-pressure feed water heater 12

Claims (9)

蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、前記高圧蒸気タービンの排気蒸気により駆動される低圧蒸気タービンとを含む蒸気タービンプラントにおいて、
前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を前記主蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を前記高圧蒸気タービンと前記低圧蒸気タービンとの間に備え、
前記加熱器のベント管を前記高圧蒸気タービンに接続したことを特徴とする蒸気タービンプラント。
In a steam turbine plant including a high-pressure steam turbine driven by main steam from a steam generation source and a low-pressure steam turbine driven by exhaust steam of the high-pressure steam turbine,
Moisture separation comprising a moisture separator that separates and removes moisture from the exhaust steam of the high-pressure steam turbine and a heater that heats the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a part of the main steam. A heater is provided between the high pressure steam turbine and the low pressure steam turbine;
A steam turbine plant, wherein a vent pipe of the heater is connected to the high-pressure steam turbine.
蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、前記高圧蒸気タービンの排気蒸気により駆動される低圧蒸気タービンとを含む蒸気タービンプラントにおいて、
前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を前記高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を前記高圧蒸気タービンと前記低圧蒸気タービンとの間に備え、
前記加熱器のベント管を前記高圧蒸気タービンに接続したことを特徴とする蒸気タービンプラント。
In a steam turbine plant including a high-pressure steam turbine driven by main steam from a steam generation source and a low-pressure steam turbine driven by exhaust steam of the high-pressure steam turbine,
A moisture separator that separates and removes moisture from the exhaust steam of the high-pressure steam turbine; and a heater that heats the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a part of the extracted steam of the high-pressure steam turbine. A moisture separator and heater between the high pressure steam turbine and the low pressure steam turbine,
A steam turbine plant, wherein a vent pipe of the heater is connected to the high-pressure steam turbine.
蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、前記高圧蒸気タービンの排気蒸気により駆動される低圧蒸気タービンとを含む蒸気タービンプラントにおいて、
前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を前記高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器と前記加熱器により加熱された高圧蒸気タービン排気蒸気を更に前記主蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を前記高圧蒸気タービンと前記低圧蒸気タービンとの間に備え、
前記蒸気の一部により加熱する加熱器のベント管を前記高圧蒸気タービンに接続し、前記高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器のベント管も前記高圧蒸気タービンに接続したことを特徴とする蒸気タービンプラント。
In a steam turbine plant including a high-pressure steam turbine driven by main steam from a steam generation source and a low-pressure steam turbine driven by exhaust steam of the high-pressure steam turbine,
A moisture separator for separating and removing moisture from the exhaust steam of the high-pressure steam turbine; a heater for heating the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a part of the extracted steam of the high-pressure steam turbine; and A moisture separator heater comprising a heater for heating the high-pressure steam turbine exhaust steam heated by the heater with a part of the main steam is provided between the high-pressure steam turbine and the low-pressure steam turbine;
A vent pipe of a heater that is heated by a part of the steam is connected to the high-pressure steam turbine, and a vent pipe of a heater that is heated by a part of the extracted steam of the high-pressure steam turbine is also connected to the high-pressure steam turbine. A featured steam turbine plant.
蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と、湿分が分離除去された排気蒸気により駆動される低圧蒸気タービンとを含む既設蒸気タービンプラントの改造方法において、
前記湿分分離器を取り外し、
前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を前記主蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を前記高圧蒸気タービンと前記低圧蒸気タービンとの間に設置し、
前記加熱器のベント管を前記高圧蒸気タービンに接続することを特徴とする既設蒸気タービンプラントの改造方法。
A high-pressure steam turbine driven by main steam from a steam generation source, a moisture separator for separating and removing moisture from the exhaust steam of the high-pressure steam turbine, and a low-pressure driven by exhaust steam from which moisture has been separated and removed In a method for remodeling an existing steam turbine plant including a steam turbine,
Remove the moisture separator,
Moisture separation comprising a moisture separator that separates and removes moisture from the exhaust steam of the high-pressure steam turbine and a heater that heats the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a part of the main steam. A heater is installed between the high pressure steam turbine and the low pressure steam turbine;
A method for remodeling an existing steam turbine plant, wherein a vent pipe of the heater is connected to the high-pressure steam turbine.
蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と、湿分が分離除去された排気蒸気により駆動される低圧蒸気タービンとを含む既設蒸気タービンプラントの改造方法において、
前記湿分分離器を取り外し、
前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を前記高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を前記高圧蒸気タービンと前記低圧蒸気タービンとの間に設置し、
前記加熱器のベント管を前記高圧蒸気タービンに接続することを特徴とする既設蒸気タービンプラントの改造方法。
A high-pressure steam turbine driven by main steam from a steam generation source, a moisture separator for separating and removing moisture from the exhaust steam of the high-pressure steam turbine, and a low-pressure driven by exhaust steam from which moisture has been separated and removed In a method for remodeling an existing steam turbine plant including a steam turbine,
Remove the moisture separator,
A moisture separator that separates and removes moisture from the exhaust steam of the high-pressure steam turbine; and a heater that heats the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a portion of the extracted steam of the high-pressure steam turbine. A moisture separator and heater is installed between the high-pressure steam turbine and the low-pressure steam turbine,
A method for remodeling an existing steam turbine plant, wherein a vent pipe of the heater is connected to the high-pressure steam turbine.
蒸気発生源からの主蒸気により駆動される高圧蒸気タービンと、前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と、湿分が分離除去された排気蒸気により駆動される低圧蒸気タービンとを含む既設蒸気タービンプラントの改造方法において、
前記湿分分離器を取り外し、
前記高圧蒸気タービンの排気蒸気の湿分を分離除去する湿分分離器と湿分が分離除去された高圧蒸気タービンの排気蒸気を前記主蒸気の一部により加熱する加熱器と湿分が分離除去された高圧蒸気タービンの排気蒸気を前記高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器とからなる湿分分離加熱器を前記高圧蒸気タービンと前記低圧蒸気タービンとの間に設置し、
前記主蒸気の一部により加熱する加熱器のベント管を前記高圧蒸気タービンに接続し、前記高圧蒸気タービンの抽気蒸気の一部により加熱する加熱器のベント管も前記高圧蒸気タービンに接続することを特徴とする既設蒸気タービンプラントの改造方法。
A high-pressure steam turbine driven by main steam from a steam generation source, a moisture separator for separating and removing moisture from the exhaust steam of the high-pressure steam turbine, and a low-pressure driven by exhaust steam from which moisture has been separated and removed In a method for remodeling an existing steam turbine plant including a steam turbine,
Remove the moisture separator,
A moisture separator that separates and removes moisture from the exhaust steam of the high-pressure steam turbine, and a heater that heats the exhaust steam of the high-pressure steam turbine from which moisture has been separated and removed by a part of the main steam and moisture are separated and removed A moisture separation heater comprising a heater for heating the exhaust steam of the high pressure steam turbine, which is heated by a part of the extracted steam of the high pressure steam turbine, is installed between the high pressure steam turbine and the low pressure steam turbine,
A vent pipe of a heater that is heated by a part of the main steam is connected to the high-pressure steam turbine, and a vent pipe of a heater that is heated by a part of the extracted steam of the high-pressure steam turbine is also connected to the high-pressure steam turbine. A method for remodeling an existing steam turbine plant.
高圧蒸気タービンへの接続口と低圧蒸気タービンへの接続口とを有し高圧蒸気タービンの排気蒸気の湿分を分離除去し低圧蒸気タービンに供給する湿分分離器と、
主蒸気管への接続口と前記高圧蒸気タービンへの接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を主蒸気の一部により加熱しこの加熱器のベント蒸気を前記高圧蒸気タービンに供給する加熱器とからなる湿分分離加熱器。
A moisture separator having a connection port to the high-pressure steam turbine and a connection port to the low-pressure steam turbine, and separating and removing moisture from the exhaust steam of the high-pressure steam turbine and supplying the moisture to the low-pressure steam turbine;
The exhaust steam of the high-pressure steam turbine, which has a connection port to the main steam pipe and a connection port to the high-pressure steam turbine and from which moisture has been separated and removed, is heated by a part of the main steam, and the vent steam of the heater is A moisture separator heater comprising a heater for supplying to a high-pressure steam turbine.
高圧蒸気タービンへの接続口と低圧蒸気タービンへの接続口とを有し高圧蒸気タービンの排気蒸気の湿分を分離除去し低圧蒸気タービンに供給する湿分分離器と、
前記高圧蒸気タービンの中間段への接続口と当該中間段よりも後段への接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱しこの加熱器のベント蒸気を高圧蒸気タービンの前記後段に供給する加熱器とからなる湿分分離加熱器。
A moisture separator having a connection port to the high-pressure steam turbine and a connection port to the low-pressure steam turbine, and separating and removing moisture from the exhaust steam of the high-pressure steam turbine and supplying the moisture to the low-pressure steam turbine;
Exhaust steam from the high-pressure steam turbine, which has a connection port to the intermediate stage of the high-pressure steam turbine and a connection port to the subsequent stage from the intermediate stage and from which moisture has been separated and removed, is partly extracted from the extracted steam of the high-pressure steam turbine. A moisture separation heater comprising: a heater for heating and supplying the vent steam of the heater to the latter stage of the high-pressure steam turbine.
高圧蒸気タービンへの接続口と低圧蒸気タービンへの接続口とを有し高圧蒸気タービンの排気蒸気の湿分を分離除去し低圧蒸気タービンに供給する湿分分離器と、
主蒸気管への接続口と前記高圧蒸気タービンへの接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を主蒸気の一部により加熱しこの加熱器のベント蒸気を前記高圧蒸気タービンに供給する加熱器と、
前記高圧蒸気タービンの中間段への接続口と当該中間段よりも後段への接続口とを有し湿分が分離除去された高圧蒸気タービンの排気蒸気を高圧蒸気タービンの抽気蒸気の一部により加熱しこの加熱器のベント蒸気を高圧蒸気タービンの前記後段に供給する加熱器とからなる湿分分離加熱器。
A moisture separator having a connection port to the high-pressure steam turbine and a connection port to the low-pressure steam turbine, and separating and removing moisture from the exhaust steam of the high-pressure steam turbine and supplying the moisture to the low-pressure steam turbine;
The exhaust steam of the high-pressure steam turbine, which has a connection port to the main steam pipe and a connection port to the high-pressure steam turbine and from which moisture has been separated and removed, is heated by a part of the main steam, and the vent steam of the heater is A heater for supplying the high-pressure steam turbine;
Exhaust steam from the high-pressure steam turbine, which has a connection port to the intermediate stage of the high-pressure steam turbine and a connection port to the subsequent stage from the intermediate stage and from which moisture has been separated and removed, is partly extracted from the extracted steam of the high-pressure steam turbine. A moisture separation heater comprising: a heater for heating and supplying the vent steam of the heater to the latter stage of the high-pressure steam turbine.
JP2004182578A 2004-06-21 2004-06-21 Steam turbine plant and moisture separation heater Pending JP2006002729A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3324008A4 (en) * 2015-08-19 2018-08-01 Mitsubishi Hitachi Power Systems, Ltd. Steam turbine plant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3324008A4 (en) * 2015-08-19 2018-08-01 Mitsubishi Hitachi Power Systems, Ltd. Steam turbine plant

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