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JP3584477B2 - Boiler power generation equipment - Google Patents

Boiler power generation equipment Download PDF

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Publication number
JP3584477B2
JP3584477B2 JP11988193A JP11988193A JP3584477B2 JP 3584477 B2 JP3584477 B2 JP 3584477B2 JP 11988193 A JP11988193 A JP 11988193A JP 11988193 A JP11988193 A JP 11988193A JP 3584477 B2 JP3584477 B2 JP 3584477B2
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JP
Japan
Prior art keywords
water
boiler
steam
power generation
steam 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.)
Expired - Fee Related
Application number
JP11988193A
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Japanese (ja)
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JPH06330708A (en
Inventor
榮勝 池野
文彦 山口
Original Assignee
石川島播磨重工業株式会社
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
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Application filed by 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP11988193A priority Critical patent/JP3584477B2/en
Publication of JPH06330708A publication Critical patent/JPH06330708A/en
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Description

【0001】
【産業上の利用分野】
本発明は、ボイラ発電設備に関するものである。
【0002】
【従来の技術】
従来、ボイラで発生した高圧蒸気により発電を行う発電設備としては、例えば、図2に示されるようなものがあり、これは、燃料と空気が供給されるボイラ1で発生した蒸気を蒸気タービン2へ導入し、該蒸気により蒸気タービン2を駆動し発電機3を回して発電を行い、前記蒸気タービン2を駆動した蒸気を復水器4で水に戻し、該水を復水ポンプ5により復水脱塩装置6へ圧送して脱塩並びに不純物除去を行い、該復水脱塩装置6で処理された水を復水昇圧ポンプ7で昇圧して低圧給水加熱器8で加熱し、脱気器9で脱気した後、ボイラ給水昇圧ポンプ10で昇圧して高圧給水加熱器11へ圧送し、該高圧給水加熱器11で加熱された水を前記ボイラ1へ送給するようにしている。
【0003】
一方、前記ボイラ1から排出される排ガスは、炭酸カルシウム等の吸収剤と補給水が供給される脱硫装置12において硫黄酸化物が除去されて清浄なガスとされた後、煙突13から大気へ放出され、又、前記脱硫装置12からは石膏等の副成品が回収されると共に、脱硫に使用された一部の水が排水として処理される。
【0004】
又、前記復水器4には、冷水塔14で冷却されポンプ15で昇圧された冷却水が、前記蒸気タービン2を駆動した蒸気の冷却用として供給され循環される。尚、前記冷却水を単に循環させていると、該冷却水に含まれるカルシウム等の不純物が析出して復水器4の伝熱管内に付着し、熱効率の低下を招いたり、伝熱管に悪影響を及ぼしたりするため、前記冷却水の一部は放流水として排出され、前記冷水塔14には補給水が供給される。
【0005】
【発明が解決しようとする課題】
しかしながら、海外等に建設されるボイラ発電設備では、河川のない内陸部の地域に設置されるケースも多く、このような場合には脱硫装置12への補給水の確保が非常に困難となっていた。
【0006】
本発明は、斯かる実情に鑑み、水の少ない地域においても脱硫装置への補給水を確保し得るボイラ発電設備を提供しようとするものである。
【0007】
【課題を解決するための手段】
本発明は、発電機を駆動する蒸気タービンと、該蒸気タービンに蒸気を供給するボイラと、前記蒸気タービンを駆動した蒸気を冷却し復水する復水器と、前記ボイラから排出される排ガスより硫黄酸化物を除去するために吸収剤と補給水が供給される脱硫装置と、前記復水器で蒸気を冷却した後外部へ排出される放流水の一部を前記脱硫装置に補給水として供給する配管系統とを備えたことを特徴とするものである。
【0008】
【作用】
従って、ボイラで加熱された蒸気は蒸気タービンへ導入され、該蒸気により蒸気タービンが駆動されて発電機で発電が行われ、前記蒸気タービンを駆動した蒸気は復水器で水に戻されて前記ボイラへ送給され、一方、脱硫装置には、復水器で蒸気を冷却した後、外部へ排出される放流水の一部が配管系統より補給水として供給されると共に、吸収剤が供給されており、ボイラから排出され前記脱硫装置へ導入された排ガスは、該脱硫装置において硫黄酸化物が除去されて清浄なガスとされた後、大気へ放出される。
【0009】
【実施例】
以下、本発明の実施例を図面を参照しつつ説明する。
【0010】
図1は本発明の一実施例であって、図中、図2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2に示す従来のものと同様であるが、本実施例の特徴とするところは、図1に示す如く、復水器4で蒸気を冷却した後、外部へ排出される放流水の一部を補給水として脱硫装置12へ供給する配管系統16を設けた点にある。
【0011】
前述の如く構成したので、ボイラ1で加熱された蒸気は蒸気タービン2へ導入され、該蒸気により蒸気タービン2が駆動されて発電機3で発電が行われ、前記蒸気タービン2を駆動した蒸気は復水器4で水に戻され、該水が復水ポンプ5により復水脱塩装置6へ圧送されて脱塩並びに不純物除去が行われ、該復水脱塩装置6で処理された水が復水昇圧ポンプ7で昇圧されて低圧給水加熱器8で加熱され、脱気器9で脱気された後、ボイラ給水昇圧ポンプ10で昇圧されて高圧給水加熱器11へ圧送され、該高圧給水加熱器11で加熱された水が前記ボイラ1へ送給され、一方、脱硫装置12には、復水器4で蒸気を冷却した後、外部へ排出される放流水の一部が配管系統16により補給水として供給されると共に、炭酸カルシウム等の吸収剤が供給されており、ボイラ1から排出され前記脱硫装置12へ導入された排ガスは、該脱硫装置12において硫黄酸化物が除去されて清浄なガスとされた後、煙突13から大気へ放出され、又、前記脱硫装置12からは石膏等の副成品が回収されると共に、脱硫に使用された一部の水が排水として処理される。
【0012】
こうして、海外等に建設されるボイラ発電設備であって、河川のない内陸部の地域に設置されるケースにおいても、脱硫装置12への補給水を確保することが可能となる。
【0013】
尚、本発明のボイラ発電設備は、上述の実施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。
【0014】
【発明の効果】
以上、説明したように本発明のボイラ発電設備によれば、水の少ない地域においても脱硫装置への補給水を確保し得るという優れた効果を奏し得る。
【図面の簡単な説明】
【図1】本発明の一実施例の全体概要図である。
【図2】従来のボイラ発電設備の一例を表わす全体概要図である。
【符号の説明】
1 ボイラ
2 蒸気タービン
3 発電機
4 復水器
12 脱硫装置
16 配管系統
[0001]
[Industrial applications]
The present invention relates to a boiler power generation facility.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, as a power generation facility for generating electric power by using high-pressure steam generated in a boiler, for example, there is one as shown in FIG. 2, which generates steam generated in a boiler 1 to which fuel and air are supplied by a steam turbine 2. The steam drives the steam turbine 2 and turns the generator 3 to generate electric power. The steam that drives the steam turbine 2 is returned to water by the condenser 4, and the water is returned by the condensate pump 5. The water treated by the condensate desalination unit 6 is pressurized by a condensate booster pump 7 and heated by a low-pressure water heater 8 to degas. After degassing in the boiler 9, the pressure is raised by the boiler feed water pressure pump 10 and sent to the high pressure feed water heater 11, and the water heated by the high pressure feed water heater 11 is sent to the boiler 1.
[0003]
On the other hand, the exhaust gas discharged from the boiler 1 is purified by removing sulfur oxides in a desulfurizer 12 to which an absorbent such as calcium carbonate and make-up water are supplied, and then discharged to the atmosphere from a chimney 13. In addition, by-products such as gypsum are collected from the desulfurization device 12, and a part of water used for desulfurization is treated as wastewater.
[0004]
Cooling water cooled by the cooling water tower 14 and pressurized by the pump 15 is supplied to the condenser 4 and circulated for cooling the steam that drives the steam turbine 2. If the cooling water is simply circulated, impurities such as calcium contained in the cooling water precipitate and adhere to the heat transfer tubes of the condenser 4, causing a decrease in heat efficiency or adversely affecting the heat transfer tubes. For example, part of the cooling water is discharged as effluent water, and makeup water is supplied to the cooling water tower 14.
[0005]
[Problems to be solved by the invention]
However, boiler power generation facilities constructed overseas are often installed in an inland area without a river, and in such a case, it is extremely difficult to secure make-up water to the desulfurization unit 12. Was.
[0006]
The present invention has been made in view of the above circumstances, and has as its object to provide a boiler power generation facility capable of securing supply water to a desulfurization device even in an area with little water.
[0007]
[Means for Solving the Problems]
The present invention provides a steam turbine that drives a generator, a boiler that supplies steam to the steam turbine, a condenser that cools and condenses steam that drives the steam turbine, and exhaust gas discharged from the boiler. A desulfurization device to which an absorbent and make-up water are supplied to remove sulfur oxides; and a part of discharge water discharged to the outside after cooling the steam by the condenser as supply water to the desulfurization device. And a piping system that performs the operation.
[0008]
[Action]
Accordingly, the steam heated by the boiler is introduced into a steam turbine, and the steam turbine is driven by the steam to generate power by a generator.The steam that has driven the steam turbine is returned to water by a condenser and is returned to the water. After being sent to the boiler, the desulfurizer cools the steam in the condenser, then discharges part of the effluent discharged to the outside as supply water from the piping system, and also supplies the absorbent. The exhaust gas discharged from the boiler and introduced into the desulfurization device is discharged into the atmosphere after the sulfur oxides are removed in the desulfurization device to form a clean gas.
[0009]
【Example】
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0010]
FIG. 1 shows an embodiment of the present invention. In the drawing, portions denoted by the same reference numerals as those in FIG. 2 represent the same components, and the basic configuration is the same as the conventional one shown in FIG. However, the feature of the present embodiment is that, as shown in FIG. 1, after the steam is cooled by the condenser 4, a part of the effluent discharged to the outside is supplied to the desulfurizer 12 as makeup water. The point is that the system 16 is provided.
[0011]
With the configuration as described above, the steam heated by the boiler 1 is introduced into the steam turbine 2, and the steam turbine 2 is driven by the steam to generate power by the generator 3. The steam that drives the steam turbine 2 is The water is returned to the water by the condenser 4, and the water is pumped to the condensate and desalination device 6 by the condensate pump 5 to perform desalination and impurity removal. After being pressurized by the condensate booster pump 7 and heated by the low-pressure feedwater heater 8 and deaerated by the deaerator 9, the pressure is increased by the boiler feedwater booster pump 10 and fed to the high-pressure feedwater heater 11. The water heated by the heater 11 is supplied to the boiler 1, while the desulfurizer 12 cools the steam by the condenser 4, and then discharges part of the discharged water discharged outside to the piping system 16. Supplied as make-up water, and an absorbent such as calcium carbonate The exhaust gas that has been supplied and discharged from the boiler 1 and introduced into the desulfurization device 12 is subjected to removal of sulfur oxides in the desulfurization device 12 to become a clean gas, and then discharged from the chimney 13 to the atmosphere. By-products such as gypsum are collected from the desulfurization unit 12, and a part of water used for desulfurization is treated as wastewater.
[0012]
In this way, even in the case of a boiler power generation facility constructed overseas or the like, which is installed in an inland area without a river, it is possible to secure supply water to the desulfurization device 12.
[0013]
Note that the boiler power generation equipment of the present invention is not limited to the above-described embodiment, and it is needless to say that various changes can be made without departing from the gist of the present invention.
[0014]
【The invention's effect】
As described above, according to the boiler power generation equipment of the present invention, it is possible to obtain an excellent effect that it is possible to secure replenishment water for the desulfurization device even in an area with little water.
[Brief description of the drawings]
FIG. 1 is an overall schematic diagram of an embodiment of the present invention.
FIG. 2 is an overall schematic diagram illustrating an example of a conventional boiler power generation facility.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Boiler 2 Steam turbine 3 Generator 4 Condenser 12 Desulfurization device 16 Piping system

Claims (1)

発電機を駆動する蒸気タービンと、該蒸気タービンに蒸気を供給するボイラと、前記蒸気タービンを駆動した蒸気を冷却し復水する復水器と、前記ボイラから排出される排ガスより硫黄酸化物を除去するために吸収剤と補給水が供給される脱硫装置と、前記復水器で蒸気を冷却した後外部へ排出される放流水の一部を前記脱硫装置に補給水として供給する配管系統とを備えたことを特徴とするボイラ発電設備。A steam turbine for driving the generator, a boiler for supplying steam to the steam turbine, a condenser for cooling and condensing the steam for driving the steam turbine, and sulfur oxides from exhaust gas discharged from the boiler. A desulfurization device to which an absorbent and makeup water are supplied for removal , and a piping system for supplying a part of the discharge water discharged to the outside after cooling the steam with the condenser as makeup water to the desulfurization device. A boiler power generation facility comprising:
JP11988193A 1993-05-21 1993-05-21 Boiler power generation equipment Expired - Fee Related JP3584477B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11988193A JP3584477B2 (en) 1993-05-21 1993-05-21 Boiler power generation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11988193A JP3584477B2 (en) 1993-05-21 1993-05-21 Boiler power generation equipment

Publications (2)

Publication Number Publication Date
JPH06330708A JPH06330708A (en) 1994-11-29
JP3584477B2 true JP3584477B2 (en) 2004-11-04

Family

ID=14772554

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11988193A Expired - Fee Related JP3584477B2 (en) 1993-05-21 1993-05-21 Boiler power generation equipment

Country Status (1)

Country Link
JP (1) JP3584477B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108087902A (en) * 2017-12-13 2018-05-29 华北电力大学(保定) Steam latent heat and water reclamation system and its recovery method and control method in power-plant flue gas

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7856829B2 (en) * 2006-12-15 2010-12-28 Praxair Technology, Inc. Electrical power generation method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108087902A (en) * 2017-12-13 2018-05-29 华北电力大学(保定) Steam latent heat and water reclamation system and its recovery method and control method in power-plant flue gas

Also Published As

Publication number Publication date
JPH06330708A (en) 1994-11-29

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