JPS5925004A - Steam power plant - Google Patents

Steam power plant

Info

Publication number
JPS5925004A
JPS5925004A JP13547282A JP13547282A JPS5925004A JP S5925004 A JPS5925004 A JP S5925004A JP 13547282 A JP13547282 A JP 13547282A JP 13547282 A JP13547282 A JP 13547282A JP S5925004 A JPS5925004 A JP S5925004A
Authority
JP
Japan
Prior art keywords
steam
water
sea water
seawater
concentrated
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
JP13547282A
Other languages
Japanese (ja)
Inventor
Shuji Hamada
浜田 修司
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.)
Niigata Engineering Co Ltd
Original Assignee
Niigata Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Niigata Engineering Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP13547282A priority Critical patent/JPS5925004A/en
Publication of JPS5925004A publication Critical patent/JPS5925004A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00Using steam or condensate extracted or exhausted from steam engine plant
    • F01K17/04Using steam or condensate extracted or exhausted from steam engine plant for specific purposes other than heating

Landscapes

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

Abstract

PURPOSE:To secure daily-use water and power source for ships etc. and use spaces effectively in said ships etc. by providing in the steam power plant system, means of separating sea water into gaseous and liquid phases, i.e., steam and concentrated sea water by flushing said sea water which is heated as a liquid phase. CONSTITUTION:Sea water 1 is introduced through a sea-water feed pump 11 into a condenser 12 and a heat exchanger 13, and is sent under pressurization to a heater 14 to be heated up to a certain temp. as in liquid phase. The heated sea water is flushed through a reducing vlave 16 and separated into gaseous and liquid phases of steam and concentrated sea water through a vapor liquid separator 17. Operating an expander 18 for the separated steam, the discharged steam is concentrated in the condenser 12 and then used as daily-use water. The steam and concentrated sea water introduced into the vapor liquid separator 17 provide smooth recovery of energy thereafter through cushioning action of the vapor liquid separator 17.

Description

【発明の詳細な説明】 本発明は船舶などで使用される蒸気原動所に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a steam power station used in ships and the like.

従来真水を容易に得ることが出来ない船舶等のボイラー
やスチームタービン等が組込まれている蒸気原動所にお
いては、海水より真水を採取するため多重効用缶等の遣
水機が設置されている。すなわち第1図に示すように海
水lを遣水機2に導入して真水を採取し、濃縮海水3を
廃棄する。上記採取した真水は、ボイラー用水として受
液器5に導入されるとともに、相当部分は飲料等の日常
用水4として使用される・上記受液器5内の真水はボイ
ラポンプ6によりてボイラー7に圧送されて蒸気を発生
する。この蒸気は発電機等の動力となるスチームタービ
ン8を駆動した後凝縮器9において海水によって冷却凝
縮され受液器5に戻され、再びボイラポンプ6によりて
ボイラー7に送られる@上記のようにボイラー水は循環
されている◎また上記ボイラーのチューブ内は気液混相
流となり、これによってボイラーチューブ内面が腐食さ
れるがこの腐食を防止するため通常清缶剤が添加されて
いる。したがってボイラー循環水は他の目的に使用出来
ない。上記ボイラー循環水は、ボイラー7のドレイン分
離器10からの抜取り、一部ワンパスの加熱使用、等よ
って水量は減少するが、水量を一定に保持するように遣
水機2の真水が補給されるとともに清缶剤も濃度が一定
となるように補給される。
BACKGROUND ART Conventionally, in steam power stations where boilers, steam turbines, etc. of ships and the like are installed, where fresh water cannot be easily obtained, water machines such as multi-effect cans are installed to extract fresh water from seawater. That is, as shown in FIG. 1, seawater 1 is introduced into a water dispenser 2, fresh water is collected, and concentrated seawater 3 is discarded. The fresh water sampled above is introduced into the receiver 5 as water for the boiler, and a considerable portion is used as water 4 for daily use such as drinking water.The fresh water in the receiver 5 is fed to the boiler 7 by the boiler pump 6. It is pumped to generate steam. This steam drives a steam turbine 8 that powers a generator, etc., is then cooled and condensed by seawater in a condenser 9, is returned to the liquid receiver 5, and is again sent to the boiler 7 by the boiler pump 6@as described above. Boiler water is circulated ◎Also, a gas-liquid multiphase flow occurs inside the tubes of the boiler, which corrodes the inner surface of the boiler tubes, but a can cleaning agent is usually added to prevent this corrosion. Therefore, boiler circulating water cannot be used for other purposes. The amount of circulating water in the boiler decreases due to extraction from the drain separator 10 of the boiler 7, partial one-pass heating, etc., but fresh water from the water dispenser 2 is replenished to keep the water amount constant. The can cleaning agent is also replenished so that the concentration remains constant.

ところで、スペースの限られた上記船舶などにおいて、
装置の占めるスペースを小さくすることは重要であり、
機器スペースを減少させる種々なこころみかなされてい
る。
By the way, in the ships mentioned above where space is limited,
It is important to reduce the space taken up by equipment;
Various efforts have been made to reduce equipment space.

本発明は、上記の事情に鑑み、多重効用缶などの造水機
を必要としない蒸気原動所システムを提供することを目
的とするもので、海水を高圧圧送して液相を保持して加
熱し、これを減圧弁を介してフラッシュさせて蒸気およ
び濃縮海水の気相、液相に分離し、上記蒸気によって膨
張機を駆動した後排出した水蒸気を凝縮器により凝縮し
真水を回収するようにしたものである。
In view of the above circumstances, it is an object of the present invention to provide a steam power station system that does not require a water generator such as a multi-effect can. Then, this is flashed through a pressure reducing valve to separate it into steam and concentrated seawater into a gas phase and a liquid phase, and after driving an expander with the steam, the discharged steam is condensed in a condenser to recover fresh water. This is what I did.

以下本発明を図面を参照して説明する。The present invention will be explained below with reference to the drawings.

第2図は本発明に係る蒸気原動所の一実施例を示すもの
である。先ず海水lを海水供給ポンプ11によりて凝縮
器12に導入し、後述する膨張機の排出蒸気を凝縮する
とともに海水を予熱する0次いでこの調水を熱交換器1
3に導き、後述する高温高圧の濃縮海水によってさらに
高温に予熱する。
FIG. 2 shows an embodiment of a steam power station according to the present invention. First, seawater 1 is introduced into a condenser 12 by a seawater supply pump 11, and exhaust steam from an expander, which will be described later, is condensed and the seawater is preheated.Then, this water is passed through a heat exchanger 1.
3, and further preheated to a high temperature using high-temperature, high-pressure concentrated seawater, which will be described later.

この予熱した海水を加熱器14に圧送して、液相を保持
した状態で所定の温度に加熱する。加熱した海水は、逆
止弁15を通り減圧弁16によってフラッシュされ所定
圧力低下するとともに気液分離器17に導入され蒸気と
濃縮海水の気液相に分離する。この分離された蒸気の大
部分は膨張機18に導かれ、これを駆動し、排出蒸気は
上記凝縮器12iこ2いて凝縮された後、飲料等日常用
水4として使用される。なお、上記気液分離器17の蒸
気の一部は、加熱その他の用途に使用してもよい。
This preheated seawater is forced into the heater 14 and heated to a predetermined temperature while maintaining the liquid phase. The heated seawater passes through a check valve 15 and is flushed by a pressure reducing valve 16 to reduce its pressure to a predetermined value, and is then introduced into a gas-liquid separator 17 where it is separated into vapor and concentrated seawater into a gas-liquid phase. Most of this separated steam is led to and drives the expander 18, and the discharged steam is condensed in the condenser 12i and used as water 4 for daily use such as drinking. Note that a part of the steam from the gas-liquid separator 17 may be used for heating or other purposes.

一方上記気液分離した高温高圧の餞縮海水は、上記熱交
換器13(こおいて海水をさらに予熱する。
On the other hand, the gas-liquid separated high-temperature, high-pressure condensed seawater is transferred to the heat exchanger 13 (where the seawater is further preheated).

この予熱することにより温度の下った高圧濃縮海水は、
圧力エネルギーを回収する減圧機(例えば水力タービン
等)19に導かれその保有する圧力エネルギーが回収さ
れて低圧となり廃濃縮海水3としてy6mされる。
This high-pressure concentrated seawater whose temperature has been lowered by preheating is
The sea water is guided to a pressure reducing machine (for example, a water turbine) 19 that recovers pressure energy, and the pressure energy held therein is recovered and becomes low pressure, which is then disposed of as waste concentrated seawater 3.

次に以上のように構成された本発明に係る蒸気原動所の
作用を説明する。
Next, the operation of the steam power station according to the present invention configured as above will be explained.

先ず海水1は供給ポンプ11によって凝縮器12および
熱交換器13を通って送られる。この間において、蒸気
および葭縮海水の熱エネルギーは海水を予熱することに
より°C@収される。したがって蒸気および濃縮tUJ
水の保有する熱エネルギーを充分薇こ回収することが出
来る。また加熱器14内1こおいて海水は、液相となっ
ているので、気液混相流と異り加熱パイプの腐食が気′
G混相流と比べ少ない。また凝縮器12の凝縮水は、日
常用水4として1史用出来る0まだ減圧弁16によって
フラッシュされ気液分離器17に導入さr15た蒸気お
よび嫉縮海水は、気液分離器17のり・ンション作用I
こよって以後のエネルギー回収操作をスムース暑こ行う
ことが出来る。特に熱エネルギーの回収された商工濃縮
海水の保有する圧力エネルギーの回収は上記気液分離器
17のクッション作用に負うものである。
Seawater 1 is first sent through a condenser 12 and a heat exchanger 13 by a feed pump 11 . During this period, the thermal energy of steam and seawater is collected by preheating the seawater. Therefore steam and concentrated tUJ
It is possible to sufficiently recover the thermal energy held by water. In addition, since the seawater in the heater 14 is in a liquid phase, unlike a gas-liquid multiphase flow, corrosion of the heating pipe is less likely to occur.
It is less than G multiphase flow. In addition, the condensed water in the condenser 12 can be used once as daily water 4. The steam and condensed seawater are flushed by the pressure reducing valve 16 and introduced into the gas-liquid separator 17. Effect I
This allows subsequent energy recovery operations to be carried out smoothly. In particular, recovery of the pressure energy possessed by the commercially concentrated seawater from which thermal energy has been recovered is due to the cushioning effect of the gas-liquid separator 17.

なお、上記説明の蒸気原動所は、発生した熱および圧力
エネルギを蒸気原動所内において有効に回収するように
なっているが、蒸気原動所内1こは加熱器14、気液分
1’ii& Mべ17、膨張機18、および凝縮器12
をe、lit、、必要に応じてエネルギー回収Iを別途
Jνることにより、エネルギーの有効な回収を行っても
よい。
The steam power station described above is designed to effectively recover the generated heat and pressure energy within the steam power station. 17, expander 18, and condenser 12
If necessary, the energy recovery I may be separately Jν to effectively recover energy.

以上述べたように本発明に係る蒸気原動所は・造水機の
設置をすることなく日常用水、動力源の確保が可能であ
るので、船舶等スペースの制限ざn、る蒸気原動所とし
て極めて有効に使用出来るものである。
As mentioned above, the steam power station according to the present invention can secure daily water and a power source without installing a water generator, so it is extremely suitable as a steam power station where space is limited such as ships. It can be used effectively.

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

第1図は従来の蒸気原動所を示す図、第2図は本発明に
係る蒸気原動所の一実施例を示す図である。 l・・・・・・海水、2・・・・・・造水機、3・・・
・・・廃棄濃縮海水・4・・・・・・日常用水、5・・
・・・・受液器、6・・・・・・ボイラーポンプ、7・
・・・・・ボイラー、8・・・・・・スチームタービン
、9・・・・・・凝縮器、10・・・・・・ドレイン分
離器、11・・・・・・海水供給ポンプ、12・・・・
・・凝縮器、13・・・・・・熱交換器、14・・・・
・・加熱器、15・・・・・・逆止弁、16′・・・・
・・減圧弁、17・・・・・・気液分離器、18・・・
・・・膨張機、19・・・・・・減圧機。
FIG. 1 is a diagram showing a conventional steam power station, and FIG. 2 is a diagram showing an embodiment of the steam power station according to the present invention. l...Seawater, 2...Water generator, 3...
...Waste concentrated seawater, 4...Water for daily use, 5...
...Liquid receiver, 6...Boiler pump, 7.
...boiler, 8 ... steam turbine, 9 ... condenser, 10 ... drain separator, 11 ... seawater supply pump, 12・・・・・・
... Condenser, 13 ... Heat exchanger, 14 ...
...Heater, 15...Check valve, 16'...
...Pressure reducing valve, 17... Gas-liquid separator, 18...
...expander, 19...pressure reducer.

Claims (1)

【特許請求の範囲】[Claims] 圧送した海水を所定の温度に加熱する加熱器と、加熱し
た昼圧海水をフラッシュする減圧弁と、フラッシュした
海水を水蒸気と濃縮海水に分ける気液分離器と、気液分
離した水蒸気によって駆動される膨張機と、膨張機より
排出した水蒸気を凝縮する凝縮器とを具備してなる蒸気
原動所。
It is driven by a heater that heats the pumped seawater to a predetermined temperature, a pressure reducing valve that flashes the heated day-pressure seawater, a gas-liquid separator that separates the flashed seawater into steam and concentrated seawater, and the steam that has been separated into gas and liquid. A steam power station equipped with an expander and a condenser that condenses water vapor discharged from the expander.
JP13547282A 1982-08-03 1982-08-03 Steam power plant Pending JPS5925004A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13547282A JPS5925004A (en) 1982-08-03 1982-08-03 Steam power plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13547282A JPS5925004A (en) 1982-08-03 1982-08-03 Steam power plant

Publications (1)

Publication Number Publication Date
JPS5925004A true JPS5925004A (en) 1984-02-08

Family

ID=15152509

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13547282A Pending JPS5925004A (en) 1982-08-03 1982-08-03 Steam power plant

Country Status (1)

Country Link
JP (1) JPS5925004A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01224405A (en) * 1988-03-01 1989-09-07 Hisaka Works Ltd Binary electricity generator using bottom sea water
JPH1162513A (en) * 1997-08-13 1999-03-05 Ryukyu Univ Sea water boiling method and stratified temperature boiler for concentrating sea water

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58195002A (en) * 1982-05-08 1983-11-14 Mitsui Eng & Shipbuild Co Ltd Water conveyance and power generation compound device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58195002A (en) * 1982-05-08 1983-11-14 Mitsui Eng & Shipbuild Co Ltd Water conveyance and power generation compound device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01224405A (en) * 1988-03-01 1989-09-07 Hisaka Works Ltd Binary electricity generator using bottom sea water
JPH1162513A (en) * 1997-08-13 1999-03-05 Ryukyu Univ Sea water boiling method and stratified temperature boiler for concentrating sea water

Similar Documents

Publication Publication Date Title
US5816048A (en) Method for utilizing acidic geothermal fluid for generating power in a rankine cycle power plant
EP0933331B1 (en) Evaporative concentration apparatus for waste water
US9453432B2 (en) Power generation system
CN107935287A (en) A kind of supercritical water oxidation energy-recuperation system
IL58801A (en) System for producing fresh water and optionally power from brine employing waste heat
KR20130025907A (en) Energy recovery and steam supply for power augmentation in a combined cycle power generation system
Heins et al. Use of evaporation for heavy oil produced water treatment
CN110593977B (en) Dual-working-medium Rankine cycle waste heat power generation method, system and power generator
US20150251144A1 (en) Method for recovering process wastewater from a steam power plant
JPH10141606A (en) Boiler plant
JPS5925004A (en) Steam power plant
JPH0821210A (en) Power generating facility in incinerator
JP2000199408A (en) Power generation method utilizing hot discharged water and power generation facility
US2626005A (en) Method and apparatus for removal of ammonia in boiler feedwater systems
US4530211A (en) System for producing steam and mechanical energy from a hydrothermal flow
KR101825316B1 (en) Flash tank design
JPH10169907A (en) Boiler plant
JPH10132207A (en) Boiler facility
EP3129548B1 (en) System and process for pulping wood
CN215440052U (en) Waste water purification device
JPS61141985A (en) Seawater desalting system
JPS6176708A (en) Waste heat recovery equipment
JPS6274499A (en) Removal of scale in hot spring water
JPS58195002A (en) Water conveyance and power generation compound device
RU2214522C2 (en) Method of operation of thermal power station