JP2002079017A - Steam separator - Google Patents

Steam separator

Info

Publication number
JP2002079017A
JP2002079017A JP2000273460A JP2000273460A JP2002079017A JP 2002079017 A JP2002079017 A JP 2002079017A JP 2000273460 A JP2000273460 A JP 2000273460A JP 2000273460 A JP2000273460 A JP 2000273460A JP 2002079017 A JP2002079017 A JP 2002079017A
Authority
JP
Japan
Prior art keywords
separator
water
steam
nozzle
end plate
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
JP2000273460A
Other languages
Japanese (ja)
Inventor
Masue Abe
益栄 阿部
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.)
IHI Corp
Original Assignee
IHI Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by IHI Corp filed Critical IHI Corp
Priority to JP2000273460A priority Critical patent/JP2002079017A/en
Publication of JP2002079017A publication Critical patent/JP2002079017A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separating Particles In Gases By Inertia (AREA)
  • Cyclones (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a steam separator suppressing wear in the inner face of a lower end plate and the inner face of a drain pipe without deteriorating steam separation efficiency even if abrasive powders such as hard scales enter the inside of a separator. SOLUTION: A flow-in nozzle 26 for generating a swirling current and a swirling current supplying water flow-in nozzle 29 for introducing water in the reverse direction of the swirling current are installed in a side face of the lower part end plate 25.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、汽水分離器に関す
るものである。
TECHNICAL FIELD The present invention relates to a brackish water separator.

【0002】[0002]

【従来の技術】図4はボイラの一例を表わすものであっ
て、図4中、1はボイラ本体、2はボイラ本体1内へ燃
料を噴射して燃焼させるバーナ、3は一次過熱器、4は
二次過熱器、5は三次過熱器、6は最終過熱器、7は一
次再熱器、8は二次再熱器、9は節炭器であり、バーナ
2からボイラ本体1内へ燃料を噴射して燃焼させること
により、燃焼ガスを生成し、生成された燃焼ガスを流通
させ、二次過熱器4、三次過熱器5、最終過熱器6、二
次再熱器8、一次過熱器3、一次再熱器7及び節炭器9
と熱交換させ、熱交換した後の排ガスを排ガスダクト1
0へ流出させ、下流側に設けられた脱硝、脱硫等の排煙
処理装置(図示せず)で窒素酸化物や硫黄酸化物等を除
去した後、大気へ放出するようになっている。
2. Description of the Related Art FIG. 4 shows an example of a boiler. In FIG. 4, reference numeral 1 denotes a boiler main body, 2 denotes a burner for injecting fuel into a boiler main body 1 and burns, 3 denotes a primary superheater, Is a secondary superheater, 5 is a tertiary superheater, 6 is a final superheater, 7 is a primary reheater, 8 is a secondary reheater, 9 is a economizer, and fuel is supplied from the burner 2 into the boiler body 1. By injecting and burning the fuel, a combustion gas is generated, and the generated combustion gas is circulated, and the secondary superheater 4, the tertiary superheater 5, the final superheater 6, the secondary reheater 8, the primary superheater 3. Primary reheater 7 and economizer 9
Heat exchange with the exhaust gas, and the exhaust gas after the heat exchange
After removing nitrogen oxides and sulfur oxides by a flue gas treatment device (not shown) such as denitration and desulfurization provided on the downstream side, it is released to the atmosphere.

【0003】一方、図5は前述のボイラの給水・蒸気系
統を表わすものであり、ボイラ給水は、燃料が燃焼され
るボイラ本体1の火炉炉壁に形成される蒸発器11で加
熱され、ノーズ部12を経て、汽水分離器13で水と蒸
気に分離され、該汽水分離器13で水と分離された蒸気
は、ボイラ本体1の天井並びに後部伝熱部周壁14を通
過し、一次過熱器3、二次過熱器4、三次過熱器5及び
最終過熱器6で過熱され、高圧タービン15へ導かれ、
該高圧タービン15が駆動されて発電が行われると共
に、前記高圧タービン15を駆動した後の蒸気は、一次
再熱器7及び二次再熱器8へ導かれ、該一次再熱器7及
び二次再熱器8で再熱された後、中・低圧タービン16
へ導入され、該中・低圧タービン16が駆動されて発電
が行われ、前記中・低圧タービン16を駆動した後の蒸
気は、復水器17へ導かれてボイラ給水に戻され、該ボ
イラ給水は、復水脱塩装置18と低圧給水加熱器19と
脱気器20とを経由し、給水ポンプ21により高圧給水
加熱器22を介して節炭器9へ圧送され、該節炭器9で
加熱され、前記蒸発器11へ送給され、循環されるよう
になっている。
On the other hand, FIG. 5 shows a feed / steam system of the above-mentioned boiler. The feed water of the boiler is heated by an evaporator 11 formed on a furnace wall of a boiler body 1 in which fuel is burned, and a nose is formed. Through the section 12, the steam and water are separated by the steam separator 13, and the steam separated from the water by the steam separator 13 passes through the ceiling of the boiler main body 1 and the peripheral wall 14 of the rear heat transfer section, and the primary superheater 3, superheated by the secondary superheater 4, the tertiary superheater 5, and the final superheater 6, and guided to the high-pressure turbine 15,
The high-pressure turbine 15 is driven to generate electric power, and the steam after driving the high-pressure turbine 15 is guided to the primary reheater 7 and the secondary reheater 8, where the primary reheaters 7 and After being reheated by the secondary reheater 8, the medium / low pressure turbine 16
And the steam after driving the medium / low pressure turbine 16 is guided to the condenser 17 and returned to the boiler feedwater, where the steam is supplied to the boiler feedwater. Is conveyed to the economizer 9 via a condensate desalination unit 18, a low-pressure feedwater heater 19 and a deaerator 20, and a high-pressure feedwater heater 22 by a feedwater pump 21. It is heated, sent to the evaporator 11, and circulated.

【0004】ところで、前記汽水分離器13は、図6に
示される如く、鉛直方向へ配置される円筒状の分離器本
体23の上下端に、上部鏡板24と下部鏡板25を一体
に取り付け、前記分離器本体23の上部側面に、汽水混
合流体を略接線方向へ流入させる流入ノズル26を接続
し、前記上部鏡板24に蒸気出口管台27を接続すると
共に、前記下部鏡板25にドレン管台28を接続してな
る構成を有している。
As shown in FIG. 6, the steam separator 13 has an upper end plate 24 and a lower end plate 25 integrally attached to the upper and lower ends of a cylindrical separator main body 23 arranged vertically. An inflow nozzle 26 for flowing the brackish water mixed fluid in a substantially tangential direction is connected to an upper side surface of the separator body 23, a steam outlet nozzle 27 is connected to the upper head 24, and a drain nozzle 28 is connected to the lower head 25. Are connected.

【0005】前記汽水分離器13においては、汽水混合
流体が流入ノズル26から分離器本体23の略接線方向
へ流入して旋回流となり、遠心力により蒸気より比重の
大きい水が下部鏡板25の内面に沿ってドレン管台28
からドレンとして排出される一方、水と分離された蒸気
は上部鏡板24を経て蒸気出口管台27から送り出され
るようになっている。
In the brackish water separator 13, a brackish water mixed fluid flows from the inflow nozzle 26 in a substantially tangential direction of the separator body 23 to form a swirling flow, and water having a higher specific gravity than the steam is formed on the inner surface of the lower head 25 by centrifugal force. Along the drain nozzle 28
The steam separated from the water is discharged from the steam outlet nozzle 27 via the upper end plate 24 while being discharged as drain from the steam generator.

【0006】[0006]

【発明が解決しようとする課題】前述の如き汽水分離器
13の場合、分離器本体23内に硬質スケール等の摩耗
粉体が侵入すると、図7に示される如く、該摩耗粉体が
内部流体の旋回流により汽水分離器13の底部に滞留し
下部鏡板25内面及びドレン管台28内面に摩耗が発生
するという問題を有していた。尚、説明上、摩耗粉体は
実際よりかなり大径化して図示してある。
In the case of the brackish water separator 13 as described above, when wear powder such as a hard scale enters the separator main body 23, as shown in FIG. This causes a problem that the swirling flow stagnates at the bottom of the steam separator 13 to cause wear on the inner surface of the lower head plate 25 and the inner surface of the drain nozzle 28. For the sake of explanation, the diameter of the wear powder is shown to be considerably larger than the actual diameter.

【0007】このため、従来においては、分離器本体2
3内部や下部鏡板25内部等にボルテックスエリミネー
タを取り付け、下部鏡板25内面及びドレン管台28内
面における旋回流を緩和させることも行われていた。
For this reason, conventionally, the separator body 2
A vortex eliminator is mounted inside the lower end plate 3 and inside the lower end plate 25 to reduce the swirling flow on the inner surface of the lower end plate 25 and the inner surface of the drain nozzle 28.

【0008】しかしながら、分離器本体23内部や下部
鏡板25内部等にボルテックスエリミネータを取り付け
るのでは、旋回流速の低下に伴う汽水分離性能の低下や
ボルテックスエリミネータ自身の摩耗欠損が起こりやす
く、好ましくなかった。
However, mounting the vortex eliminator inside the separator main body 23 or the lower end plate 25 is not preferable because the brackish water separation performance is reduced and the vortex eliminator itself is liable to wear due to a decrease in the swirling velocity.

【0009】本発明は、斯かる実情に鑑み、分離器本体
内に硬質スケール等の摩耗粉体が侵入した場合でも、汽
水分離性能を低下させたりすることなく、下部鏡板内面
及びドレン管台内面に摩耗が発生することを防止し得る
汽水分離器を提供しようとするものである。
The present invention has been made in view of the above circumstances, and even when wear powder such as a hard scale enters the separator main body, the inner surface of the lower end plate and the inner surface of the drain nozzle are maintained without deteriorating the brackish water separation performance. It is an object of the present invention to provide a brackish water separator capable of preventing the occurrence of abrasion on the surface.

【0010】[0010]

【課題を解決するための手段】本発明は、鉛直方向へ配
置される円筒状の分離器本体の上下端に、上部鏡板と下
部鏡板を取り付け、前記分離器本体の上部側面に、蒸気
と水が混ざった汽水混合流体を略接線方向へ流入させる
流入ノズルを接続し、前記上部鏡板に蒸気出口管台を接
続すると共に、前記下部鏡板にドレン管台を接続してな
る汽水分離器において、下部鏡板の側面に、流入ノズル
による旋回流と逆方向へ水を流入させる旋回流抑制水流
入ノズルを配設したことを特徴とする汽水分離器にかか
るものである。
According to the present invention, an upper end plate and a lower end plate are attached to upper and lower ends of a cylindrical separator body arranged in a vertical direction, and steam and water are attached to upper side surfaces of the separator body. In a brackish water separator that connects an inflow nozzle that allows the brackish water mixed fluid mixed with the mixture to flow in a substantially tangential direction, connects a steam outlet nozzle to the upper head plate, and connects a drain nozzle to the lower head plate. The present invention relates to a brackish water separator, wherein a swirl flow suppressing water inflow nozzle for inflowing water in a direction opposite to the swirl flow by the inflow nozzle is provided on a side surface of the head plate.

【0011】上記手段によれば、以下のような作用が得
られる。
According to the above means, the following effects can be obtained.

【0012】分離器本体内に硬質スケール等の摩耗粉体
が侵入した場合、必要に応じて、旋回流抑制水流入ノズ
ルから流入ノズルによる旋回流と逆方向へ水を流入させ
ると、流入ノズルから分離器本体の略接線方向へ流入し
た内部流体の旋回流が弱められ、摩耗粉体は汽水分離器
の底部に滞留せず水と一緒にドレン管台から排出される
形となる。
When abrasion powders such as hard scales enter the separator main body, if necessary, water is introduced from the swirl flow suppressing water inflow nozzle in a direction opposite to the swirl flow by the inflow nozzle. The swirling flow of the internal fluid that has flowed substantially tangentially to the separator body is weakened, and the abrasion powder does not stay at the bottom of the steam separator, and is discharged from the drain nozzle together with water.

【0013】この結果、分離器本体内に硬質スケール等
の摩耗粉体が侵入しても、旋回流が弱められることによ
り、下部鏡板内面及びドレン管台内面に摩耗が発生せ
ず、しかも、従来のように、分離器本体内部や下部鏡板
内部等にボルテックスエリミネータを取り付けるのとは
異なり、旋回流速の低下に伴って汽水分離性能が低下し
たり、ボルテックスエリミネータ等の摩耗欠損が生じる
心配もない。
As a result, even if abrasion powder such as hard scale enters the separator main body, the swirling flow is weakened, so that no wear occurs on the inner surface of the lower end plate and the inner surface of the drain nozzle. Unlike the case where the vortex eliminator is attached to the inside of the separator body or the lower end plate, there is no concern that the brackish water separation performance will be reduced due to the decrease in the swirling flow rate, or the wear loss of the vortex eliminator will occur.

【0014】[0014]

【発明の実施の形態】以下、本発明の実施の形態を図示
例と共に説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0015】図1〜図3は本発明を実施する形態の一例
であって、図中、図6及び図7と同一の符号を付した部
分は同一物を表わしており、基本的な構成は図6及び図
7に示す従来のものと同様であるが、本図示例の特徴と
するところは、図1〜図3に示す如く、下部鏡板25の
側面に、流入ノズル26による旋回流と逆方向へ水を流
入させる旋回流抑制水流入ノズル29を配設した点にあ
る。
FIGS. 1 to 3 show an example of an embodiment of the present invention. In the drawings, the portions denoted by the same reference numerals as those in FIGS. 6 and 7 represent the same components. 6 and FIG. 7, the present embodiment is characterized in that, as shown in FIG. 1 to FIG. The point is that a swirl flow suppressing water inflow nozzle 29 for inflowing water in the direction is provided.

【0016】本図示例の場合、前記旋回流抑制水流入ノ
ズル29は、ボイラ本体1の火炉壁管から延びる流入配
管30が接続される流入ノズル26の分離器本体23に
対する平面配置(図2参照)を反転させるような形で、
図3に示す如く、下部鏡板25の側面に接続してあり、
該旋回流抑制水流入ノズル29に対しては、途中に逆止
弁31が設けられた水配管32を介してリング状水配管
33を接続し、該リング状水配管33には、図1に示す
如く、途中に遮断弁34が設けられた水供給配管35を
接続し、該遮断弁34を必要に応じて開くことにより、
水供給配管35からリング状水配管33と水配管32を
介して旋回流抑制水流入ノズル29へ水を供給するよう
にしてある。
In the illustrated example, the swirl flow suppressing water inflow nozzle 29 is arranged in a plane with respect to the separator body 23 of the inflow nozzle 26 to which the inflow pipe 30 extending from the furnace wall tube of the boiler body 1 is connected (see FIG. 2). )
As shown in FIG. 3, it is connected to the side surface of the lower head plate 25,
A ring-shaped water pipe 33 is connected to the swirling flow suppression water inflow nozzle 29 via a water pipe 32 provided with a check valve 31 in the middle thereof. As shown, by connecting a water supply pipe 35 provided with a shut-off valve 34 on the way, and opening the shut-off valve 34 as necessary,
Water is supplied from the water supply pipe 35 to the swirl flow suppressing water inflow nozzle 29 via the ring-shaped water pipe 33 and the water pipe 32.

【0017】次に、上記図示例の作動を説明する。Next, the operation of the above illustrated example will be described.

【0018】分離器本体23内に硬質スケール等の摩耗
粉体が侵入した場合、必要に応じて、遮断弁34を開
き、水供給配管35からリング状水配管33と水配管3
2を介して、旋回流抑制水流入ノズル29から流入ノズ
ル26による旋回流と逆方向へ水を流入させると、流入
ノズル26から分離器本体23の略接線方向へ流入した
内部流体の旋回流が弱められ、摩耗粉体は汽水分離器1
3の底部に滞留せず水と一緒にドレン管台28から排出
される形となる。
When abrasion powder such as hard scale enters the separator main body 23, the shut-off valve 34 is opened as necessary, and the ring-shaped water pipe 33 and the water pipe 3 are connected from the water supply pipe 35.
When water flows from the swirl flow suppression water inflow nozzle 29 through the nozzle 2 in a direction opposite to the swirl flow of the inflow nozzle 26, the swirl flow of the internal fluid flowing from the inflow nozzle 26 in a substantially tangential direction of the separator body 23 is generated Weakened and worn powder is brackish water separator 1
3 is discharged from the drain nozzle 28 together with water without staying at the bottom of the nozzle 3.

【0019】この結果、分離器本体23内に硬質スケー
ル等の摩耗粉体が侵入しても、旋回流が弱められること
により、下部鏡板25内面及びドレン管台28内面に摩
耗が発生せず、しかも、従来のように、分離器本体23
内部や下部鏡板25内部等にボルテックスエリミネータ
を取り付けるのとは異なり、旋回流速の低下に伴って汽
水分離性能が低下したり、ボルテックスエリミネータ等
の摩耗欠損が生じる心配もない。
As a result, even if wear powder such as a hard scale enters the separator main body 23, the swirling flow is weakened, so that no wear occurs on the inner surface of the lower end plate 25 and the inner surface of the drain nozzle 28, Moreover, as in the conventional case, the separator body 23
Unlike mounting the vortex eliminator inside the lower end plate 25 or the like, there is no fear that the brackish water separation performance is reduced due to a decrease in the swirling flow rate or wear defects such as the vortex eliminator are generated.

【0020】こうして、分離器本体23内に硬質スケー
ル等の摩耗粉体が侵入した場合でも、汽水分離性能を低
下させたりすることなく、下部鏡板25内面及びドレン
管台28内面に摩耗が発生することを防止し得る。
In this way, even when abrasion powder such as hard scale enters the separator main body 23, abrasion occurs on the inner surface of the lower head plate 25 and the inner surface of the drain nozzle 28 without deteriorating the steam separation performance. Can be prevented.

【0021】尚、本発明の汽水分離器は、上述の図示例
にのみ限定されるものではなく、本発明の要旨を逸脱し
ない範囲内において種々変更を加え得ることは勿論であ
る。
It should be noted that the steam separator of the present invention is not limited to the above-described illustrated example, and it is needless to say that various modifications can be made without departing from the gist of the present invention.

【0022】[0022]

【発明の効果】以上、説明したように本発明の汽水分離
器によれば、分離器本体内に硬質スケール等の摩耗粉体
が侵入した場合でも、汽水分離性能を低下させたりする
ことなく、下部鏡板内面及びドレン管台内面に摩耗が発
生することを防止し得るという優れた効果を奏し得る。
As described above, according to the brackish water separator of the present invention, even if abrasion powder such as a hard scale enters the separator body, the brackish water separation performance is not reduced. An excellent effect of preventing abrasion from occurring on the inner surface of the lower head plate and the inner surface of the drain nozzle can be obtained.

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

【図1】本発明を実施する形態の一例の側断面図であ
る。
FIG. 1 is a side sectional view of an example of an embodiment of the present invention.

【図2】図1のII−II断面図である。FIG. 2 is a sectional view taken along line II-II of FIG.

【図3】図1のIII−III断面図である。FIG. 3 is a sectional view taken along the line III-III of FIG. 1;

【図4】一般的なボイラの一例を表わす全体概要構成図
である。
FIG. 4 is an overall schematic configuration diagram illustrating an example of a general boiler.

【図5】図4に示されるボイラの給水・蒸気系統を表わ
す概要構成図である。
FIG. 5 is a schematic configuration diagram showing a water supply / steam system of the boiler shown in FIG.

【図6】汽水分離器の一例を表わす全体斜視断面図であ
る。
FIG. 6 is an overall perspective sectional view illustrating an example of a brackish water separator.

【図7】図6に示される汽水分離器の一例の部分的な断
面図であって、摩耗粉体が流れる様子を概念的に表わす
図である。
7 is a partial cross-sectional view of an example of the brackish water separator shown in FIG. 6, and is a view conceptually showing a state in which abrasion powder flows.

【符号の説明】[Explanation of symbols]

13 汽水分離器 23 分離器本体 24 上部鏡板 25 下部鏡板 26 流入ノズル 27 蒸気出口管台 28 ドレン管台 29 旋回流抑制水流入ノズル 13 Steam separator 23 Separator main body 24 Upper head plate 25 Lower head plate 26 Inflow nozzle 27 Steam outlet nozzle 28 Drain nozzle 29 Swirl flow suppression water inflow nozzle

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 鉛直方向へ配置される円筒状の分離器本
体の上下端に、上部鏡板と下部鏡板を取り付け、前記分
離器本体の上部側面に、蒸気と水が混ざった汽水混合流
体を略接線方向へ流入させる流入ノズルを接続し、前記
上部鏡板に蒸気出口管台を接続すると共に、前記下部鏡
板にドレン管台を接続してなる汽水分離器において、 下部鏡板の側面に、流入ノズルによる旋回流と逆方向へ
水を流入させる旋回流抑制水流入ノズルを配設したこと
を特徴とする汽水分離器。
1. An upper end plate and a lower end plate are attached to upper and lower ends of a cylindrical separator main body arranged in a vertical direction, and a brackish water mixed fluid in which steam and water are mixed is substantially applied to an upper side surface of the separator main body. In a steam separator comprising a tangential inflow nozzle connected, a steam outlet nozzle connected to the upper head plate, and a drain nozzle connected to the lower head plate, a side surface of the lower head plate is provided with an inflow nozzle. A brackish water separator having a swirl flow suppression water inflow nozzle for flowing water in a direction opposite to the swirl flow.
JP2000273460A 2000-09-08 2000-09-08 Steam separator Pending JP2002079017A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000273460A JP2002079017A (en) 2000-09-08 2000-09-08 Steam separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000273460A JP2002079017A (en) 2000-09-08 2000-09-08 Steam separator

Publications (1)

Publication Number Publication Date
JP2002079017A true JP2002079017A (en) 2002-03-19

Family

ID=18759398

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000273460A Pending JP2002079017A (en) 2000-09-08 2000-09-08 Steam separator

Country Status (1)

Country Link
JP (1) JP2002079017A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104645671A (en) * 2015-01-13 2015-05-27 杭州路弘科技有限公司 Liquid degassing device and liquid degassing method
WO2018152464A1 (en) * 2017-02-17 2018-08-23 XDI Holdings, LLC Large scale cost effective direct steam generator system, method, and apparatus
US11262022B2 (en) * 2016-08-31 2022-03-01 XDI Holdings, LLC Large scale cost effective direct steam generator system, method, and apparatus

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104645671A (en) * 2015-01-13 2015-05-27 杭州路弘科技有限公司 Liquid degassing device and liquid degassing method
CN104645671B (en) * 2015-01-13 2016-03-30 杭州路弘科技有限公司 Liquid degassing device and method
US11262022B2 (en) * 2016-08-31 2022-03-01 XDI Holdings, LLC Large scale cost effective direct steam generator system, method, and apparatus
US11802662B2 (en) 2016-08-31 2023-10-31 XDI Holdings, LLC Large scale cost effective direct steam generator system, method, and apparatus
WO2018152464A1 (en) * 2017-02-17 2018-08-23 XDI Holdings, LLC Large scale cost effective direct steam generator system, method, and apparatus
US11242772B2 (en) 2017-02-17 2022-02-08 XDI Holdings, LLC Large scale cost effective direct steam generator system, method, and apparatus
US11624299B2 (en) 2017-02-17 2023-04-11 XDI Holdings, LLC Large scale cost effective direct steam generator system, method, and apparatus

Similar Documents

Publication Publication Date Title
US6598399B2 (en) Integrated power plant and method of operating such an integrated power plant
EP0915288B1 (en) Exhaust heat recovery boiler
RU2193726C2 (en) Waste heat-powered steam generator
EP1005894A1 (en) Reheating flue gas for selective catalytic systems
TWI648506B (en) Coal-fired oxygen plant with heat integration
EP2942495B1 (en) Coal fired oxy plant with heat integration
US5474034A (en) Supercritical steam pressurized circulating fluidized bed boiler
JP2002079017A (en) Steam separator
JP3851165B2 (en) Gas turbine and its operating method
JP2002102628A (en) Gas-liquid separator
CN111495175A (en) Exhaust gas treatment device
US4151813A (en) Jet pump in natural circulation fossil fuel fired steam generator
JP2002013703A (en) Air-water separator
JP4465784B2 (en) Brackish water separator
JP3978888B2 (en) Thermal power plant and operation method thereof
CN201688715U (en) Kiln head waste heat boiler with fly ash separating chamber
JP2001232244A (en) Steam separator
JP2001232124A (en) Steam separator
JP2002106804A (en) Feedwater flow-rate controller of variable once- through boiler
JP2002115806A (en) Structure of economizer of boiler
JP2002267154A (en) Boiler device
JP2003322310A (en) BOILER NOx REDUCING DEVICE
JP3176435B2 (en) Steam generator
JPH10176821A (en) Boiler with denitrification apparatus
JPH0681610A (en) Composite electric power plant