Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP4109488B2 - Marine gas turbine system with pure water production equipment - Google Patents
[go: Go Back, main page]

JP4109488B2 - Marine gas turbine system with pure water production equipment - Google Patents

Marine gas turbine system with pure water production equipment Download PDF

Info

Publication number
JP4109488B2
JP4109488B2 JP2002126132A JP2002126132A JP4109488B2 JP 4109488 B2 JP4109488 B2 JP 4109488B2 JP 2002126132 A JP2002126132 A JP 2002126132A JP 2002126132 A JP2002126132 A JP 2002126132A JP 4109488 B2 JP4109488 B2 JP 4109488B2
Authority
JP
Japan
Prior art keywords
steam
pure water
water
gas turbine
supply means
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 - Lifetime
Application number
JP2002126132A
Other languages
Japanese (ja)
Other versions
JP2003312588A (en
JP2003312588A5 (en
Inventor
幸雄 大槻
義美 西原
隆雄 杉本
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.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
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 Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP2002126132A priority Critical patent/JP4109488B2/en
Publication of JP2003312588A publication Critical patent/JP2003312588A/en
Publication of JP2003312588A5 publication Critical patent/JP2003312588A5/ja
Application granted granted Critical
Publication of JP4109488B2 publication Critical patent/JP4109488B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T70/00Maritime or waterways transport
    • Y02T70/50Measures to reduce greenhouse gas emissions related to the propulsion system

Landscapes

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、ガスタービンの排ガスから熱回収して蒸気を生成し、燃焼器に噴射注入する蒸気噴射方式ガスタービンに純水製造装置を設けた舶用ガスタービンシステムに関する。
【0002】
【従来の技術】
熱効率に優れたガスタービンの1つとして、ガスタービンの排ガスの廃熱を利用して廃熱ボイラで生成した蒸気を、ガスタービンの燃焼器に噴射注入して燃焼ガスと蒸気の混合体でタービンを作動させるようにした蒸気噴射(チェンサイクル)方式が知られている。この蒸気噴射方式ガスタービンは、燃焼器に噴射注入した蒸気により燃焼室内の燃焼温度を下げられるが、さらに燃料を供給することによって、蒸気を噴射しない場合と同じ燃焼温度に保ち、その結果、軸出力が大幅に増加し、熱効率が向上して燃費が低減し、かつNOも低減できる利点がある。
【0003】
【発明が解決しようとする課題】
前記蒸気噴射方式ガスタービンを舶用とする場合、海水をそのまま使用するとボイラ管やタービンブレードの腐食といったような廃熱ボイラやガスタービンの損傷を招き易いので、海水の代わりに純水を使用するのが好ましい。他方、船舶では航行中の飲料水が必要である。このような純水を予め陸から積み込んで航行する場合、航行期間中に必要な純水を全て積み込まなければならないため、重量やスペースの点で不利になる。
【0004】
また、前記ガスタービンからの排ガスは大きな熱量を持っており、燃焼器に噴射注入する蒸気生成のみでは、充分な熱回収が行われないので、排ガスの温度低下が不十分であり、そのままの温度で大気中に放出するとサーマルポリューションの一因となる恐れがある。
【0005】
そこで本発明は、舶用ガスタービンシステムにおいて、ガスタービンの排ガスから熱回収して蒸気を生成し、燃焼器に供給することによりガスタービンシステムの出力および効率の向上を図り、さらに、前記排ガスから熱回収して純水を造ることにより、ガスタービンシステムおよび飲料水に供される純水を確保することを目的とする。
【0006】
【課題を解決するための手段】
前記目的を達成するために、本発明の請求項1に係る舶用ガスタービンシステムは、圧縮機、燃焼器、およびタービンを有し、舶用推進機を駆動するガスタービンと、ガスタービンの排ガスから熱回収して蒸気を生成する第1蒸気生成器と、前記排ガスから熱回収して原水を加熱する原水加熱器と、加熱された原水から純水を得る純水製造装置と、前記純水製造装置で得られた純水を貯留する貯水タンクと、前記貯水タンク内の純水の一部を飲料水として取り出す飲料水供給手段と、前記第1蒸気生成器で得られる蒸気を前記燃焼器に供給する蒸気供給手段と、蒸気をエネルギ源として冷媒を生成する吸収式冷凍機と、記排ガスから熱回収して貯水タンクの純水の他の一部から蒸気を生成して前記吸収式冷凍機に供給する第2蒸気生成器と、前記純水のさらに他の一部を貯水タンクから前記第1蒸気生成器に供給する純水供給手段と、前記吸収式冷凍機で得られた冷媒を船内の空調機に供給する冷媒供給手段とを備えている。
【0007】
前記舶用ガスタービンシステムによれば、第1蒸気生成器において排ガスから熱回収して生成された蒸気を燃焼器に供給することにより、蒸気が持つエネルギが注入されることと、定圧比熱が増大することから、タービン内で大きな膨張仕事を行うので、ガスタービンの出力が増大し、熱効率が向上して燃費が低減し、かつNOも低減できる。また、ガスタービンの排ガスから熱回収して純水製造装置を作動させるので、前記第1蒸気生成器での熱回収と合わせて、ガスタービンから出る比較的高温の排ガスの熱を有効に回収できるから、システムとしての熱効率が向上する。また、燃焼器には純水から生成された蒸気が供給されるので、ボイラ管やタービンブレードの腐食といったような廃熱ボイラやガスタービンの損傷がない。さらに、船舶の運航上で必要な乗員または船客の飲料水も確保される。
純水製造装置で得られた純水は貯水タンクに一旦貯留される。例えば、フラッシュ型純水製造装置では海水から短時間で多量の純水を得ることができないが、ガスタービンの出力を急激に上げる時などのように多量の純水を必要とする場合には、貯水タンクの純水を純水供給手段によって第1蒸気生成器に供給することにより対応できる。また、貯水タンクに飲料水供給手段を接続することにより、飲料水として使用される純水の使用量の一時的な変動が、燃焼器へ供給される蒸気となる純水の量に影響を与えない。
【0009】
また、前記ガスタービンシステムによれば、吸収式冷凍機における冷媒生成のためのエネルギ源を別に用意する必要がなくなるとともに、排ガスの熱を利用することでガスタービンシステム全体としての熱効率がさらに向上する。
【0012】
さらに、本発明の好ましい実施形態では、前記第1蒸気生成器から燃焼器に供給される蒸気が過熱蒸気である。
【0013】
前記構成により、ガスタービンの燃焼器内に高エネルギの蒸気が供給されるから、ガスタービンの出力が一層増大する。
【0014】
【発明の実施の形態】
以下、本発明の好ましい実施形態について図面を参照しながら詳述する。
図1は本発明の一実施形態に係る純水製造装置を備えたガスタービンシステムを示す概略構成図である。
本発明の舶用ガスタービンシステムは、スクリュー、ウォータージェット、ホーバークラフト用空気圧縮機などの舶用推進機2および電気推進用の発電機を負荷とするガスタービン1を備えている。ガスタービン1は、圧縮機3で空気を圧縮して燃焼器4の燃焼室に導くとともに、燃焼室内に燃料を噴射して燃焼させ、その高温高圧の燃焼ガスでタービン5を駆動させる。
【0015】
ガスタービン1の排ガスは廃熱ボイラ10に導かれる。この廃熱ボイラ10は、第1蒸気生成器11、第2蒸気生成器12、および原水加熱器13からなる。第1蒸気生成器11では、導入された排ガスから熱回収して過熱蒸気を生成し、その過熱蒸気は蒸気供給配管15を介してガスタービン1の燃焼器4の燃焼室内に噴射される。一方、第1蒸気生成器11で熱回収されたのちの排ガスは、まだ十分に熱エネルギーを有していることから、さらに、第2蒸気生成器12、および原水加熱器13を順次通過して、熱エネルギを十分に回収されたのちに廃熱ボイラ10から排出され、煙突(図示せず)を通って大気中に放出される。
【0016】
第1蒸気生成器11に供給する蒸気生成用の水としては、純水製造装置20において船舶航行中に海水を原水として得られた純水が用いられる。この海水から純水を得る純水製造装置20としては、フラッシュ型、リヒート型および蒸気圧縮型などがあるが、熱効率、その他の点でフラッシュ型を用いるのが好ましい。
【0017】
つぎに、前記純水製造装置20について説明する。この純水製造装置20は、海水を加熱してフラッシュ型蒸発法により純水を得るものであり、海から取り込んだ海水を、低圧の循環ポンプ21で循環させるとともに、その循環経路に設けた前記原水加熱器13で加熱したのちに、ノズルから純水製造装置20内の蒸発室に吹き出される。一方、第1蒸気生成器11の中途から飽和蒸気がエゼクタ25に供給されており、このエゼクタ25内で膨張する蒸気の吸引力により蒸発室内を真空引きし、蒸発室内の圧力が飽和蒸気圧以下になったときに、前記加熱されて蒸発室内に吹き出された海水が沸騰して蒸気が発生する。この蒸気は、蒸発室内を上昇していくときに純水製造装置20内を循環する冷たい海水に触れて凝縮し、液化して蒸留器に溜まる。この溜まった蒸留水、つまり塩分等が除去された純水を、低圧給水ポンプ23で汲み出して、低圧給水配管22に送水する。
【0018】
低圧給水ポンプ23の作動により低圧給水配管22に送水された純水は、水位センサ32を備えた貯水タンク30に一旦貯留される。低圧給水配管22には制御弁33が設けられており、前記水位センサ32からの水位検出信号により開閉される。前記貯水タンク30に貯留された純水の一部は、貯留タンク30に接続された飲料水用配管35aと送水ポンプ35bとを有する飲料水供給手段35により取り出され、飲料水として利用される。前記貯水タンク30に貯留された純水の他の一部は、純水供給用配管36aと高圧ポンプ36bとを有する純水供給手段36により、燃焼器4内の高い圧力に抗して噴射できる高圧力に昇圧されたのち第1蒸気生成器11に供給される。第1蒸気生成器11では、純水供給手段36により送られてくる純水をガスタービン1から供給される排ガスにより加熱して蒸気を生成し、発生した高圧の過熱蒸気を蒸気供給配管15に送出して、ガスタービン1の燃焼器4内の燃焼室に噴射する。一方、第1蒸気生成器11の中途からは、前述の通り、エゼクタ25に飽和蒸気が供給されており、エゼクタ25を出て液化した蒸気は、貯水タンク30に回収される。
【0019】
さらに、吸収式冷凍機40について説明する。吸収式冷凍機40は、蒸気をエネルギ源として、冷水を生成する周知のタイプであり、第2蒸気生成器12で生成され、蒸気供給配管を有する蒸気供給手段41を介して供給される蒸気により作動する。吸収式冷凍機40で得られた冷水は、冷媒として冷媒供給配管を有する冷媒供給手段45を介して、船内の1つまたは複数の空調機46に供給される。空調機46は、図2のラジエータ47および送風用のファン48を有し、ラジエータ47に冷媒供給手段45から冷媒が供給される。ラジエータ47で使用された冷媒は、前記冷媒供給手段45の下流側に供給され、再び吸収式冷凍機40に戻される。冷媒供給手段45から分岐し、空調機46につながる配管には、開閉弁49が設けられており、空調機46を使用する場合に開かれる。
【0020】
前記第2蒸気生成器12から吸収式冷凍機40に向かう蒸気供給手段41には、その蒸気の一部を、船内の蒸気や温水を要求する場所にプロセス蒸気として供給するプロセス蒸気供給配管50が接続されている。前記プロセス蒸気供給配管50には、蒸気の供給および停止を行うための開閉弁51が設けられている。
【0021】
つぎに、前記純水製造装置を備えた舶用ガスタービンシステムの作用について説明する。
【0022】
上記構成において、純水は、海水を汲み上げて低圧ポンプ21で原水加熱器13へ送り、加熱して純水製造装置20に供給することにより製造される。純水製造装置20で得られた純水は、低圧給水ポンプ23により、低圧給水配管22を介して貯水タンク30に貯留される。貯水タンク30への純水の供給量は、水位センサ32により低圧給水配管22に設けられた制御弁33を作動させて調節される。つまり、水位センサ32が上限レベルの水位を検出したとき検出信号を出力して、制御弁33を閉止することにより、水位を上限レベル以下に規制する。また、飲料水供給手段35により、純水の一部が船内で使用される飲料水として供給される。貯水タンク30に貯留された他の一部の純水は、純水供給手段36を通して第1蒸気生成器11に供給され、得られた過熱蒸気が、ガスタービン1の燃焼器4に噴射注入される。さらに、貯水タンク30に貯留された純水の一部を第2蒸気生成器12に供給し、得られた蒸気が蒸気供給配管41を介して吸収式冷凍機40に供給される。吸収式冷凍機40で得られた冷媒は、船内の空調機46に送られ、船内を冷房する。空調機46の温度調節は、蒸気供給手段41を通って供給される蒸気を制御することにより行われる。例えば、冷媒供給手段45に温度センサ42を設けるとともに、蒸気供給手段41に制御弁43を設け、温度センサ42からの温度検知信号に基づいて制御弁43の開度を調節することにより、供給する蒸気量を制御して冷媒供給手段45内の冷媒が予め温度センサ42に設定された温度となるように調節する。空調機46で使用された冷媒は、冷媒供給手段45の下流側に供給され、再び吸収式冷凍機40に戻される。また、吸収式冷凍機40からのドレンは、低圧給水配管22に供給され、この低圧給水配管22を通って貯水タンク30に戻される。さらに、前記プロセス蒸気供給配管50に設けられた開閉弁51を開くことにより、プロセス蒸気供給配管50を介して船内の蒸気や温水を要求する場所にプロセス蒸気を供給する。
【0023】
本実施例では、蒸発生成器として、第1蒸気生成器11および第2蒸気生成器12を別々に設けたが、第1蒸気生成器11および第2蒸気生成器12は共通としてもよい。
【0024】
【発明の効果】
以上のように本発明の舶用ガスタービンシステムによれば、第1蒸気生成器において排ガスから熱回収して生成された蒸気を燃焼器に供給することにより、蒸気が持つエネルギが注入されることと、定圧比熱が増大することから、タービン内で大きな膨張仕事を行うので、ガスタービンの出力が増大し、熱効率が向上して燃費が低減し、かつNOも低減できる。また、ガスタービンの排ガスから熱回収して純水製造装置を作動させるので、前記第1蒸気生成器での熱回収と合わせて、ガスタービンから出る比較的高温の排ガスの熱を有効に回収できるから、システムとしての熱効率が向上する。また、燃焼器には純水から生成された蒸気が供給されるので、ボイラ管やタービンブレードの腐食といったような廃熱ボイラやガスタービンの損傷がない。さらに、船舶の運航上で必要な乗員または船客の飲料水も確保される。
【図面の簡単な説明】
【図1】本発明の一実施形態である純水製造装置を備えた舶用ガスタービンシステムを示す概略構成図である。
【図2】本発明に係る舶用ガスタービンの空調機46の概略図である。
【符号の説明】
1…ガスタービン、2…舶用推進機、3…圧縮機、4…燃焼器、5…タービン、11…第1蒸気生成器、12…第2蒸気生成器、13…原水加熱器、15…蒸気供給手段、20…純水製造装置、30…貯水タンク、35…飲料水供給手段、36…純水供給手段、40…吸収式冷凍機、45…冷媒供給手段、46…空調機。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a marine gas turbine system in which a pure water production apparatus is provided in a steam injection type gas turbine that generates heat by recovering heat from exhaust gas of a gas turbine and injects and injects it into a combustor.
[0002]
[Prior art]
As one of gas turbines with excellent thermal efficiency, steam generated in a waste heat boiler using waste heat of exhaust gas from a gas turbine is injected and injected into a combustor of a gas turbine, and a mixture of combustion gas and steam is used as a turbine. There is known a steam injection (chain cycle) system in which the is operated. In this steam injection type gas turbine, the combustion temperature in the combustion chamber can be lowered by the steam injected and injected into the combustor, but by supplying further fuel, the same combustion temperature is maintained as when steam is not injected. output greatly increases, reducing fuel consumption and improving the thermal efficiency, and is advantageous in that NO x can be reduced.
[0003]
[Problems to be solved by the invention]
When the steam injection type gas turbine is used for marine use, if seawater is used as it is, it is easy to cause damage to the waste heat boiler and gas turbine, such as corrosion of boiler tubes and turbine blades. Is preferred. On the other hand, the ship needs drinking water during navigation. When navigating with such pure water loaded in advance from the land, it is disadvantageous in terms of weight and space because all of the necessary pure water must be loaded during the navigation period.
[0004]
Further, the exhaust gas from the gas turbine has a large amount of heat, and sufficient heat recovery is not performed only by the generation of steam injected and injected into the combustor. If released into the atmosphere, there is a risk of contributing to thermal pollution.
[0005]
Therefore, the present invention provides a marine gas turbine system that recovers heat from exhaust gas from a gas turbine to generate steam and supplies it to a combustor to improve the output and efficiency of the gas turbine system. It aims at securing the pure water provided to a gas turbine system and drinking water by collect | recovering and making a pure water.
[0006]
[Means for Solving the Problems]
In order to achieve the above object, a marine gas turbine system according to claim 1 of the present invention includes a compressor, a combustor, and a turbine, and drives a marine propulsion device, and heat from exhaust gas of the gas turbine. A first steam generator that recovers and generates steam, a raw water heater that recovers heat from the exhaust gas and heats raw water, a pure water manufacturing apparatus that obtains pure water from the heated raw water, and the pure water manufacturing apparatus a water storage tank for storing pure water obtained in a portion of purified water in the water storage tank and water supply means for taking as drinking water, the steam obtained in the previous SL first steam generator to the combustor a steam supply means for supplying an absorption chiller that produces a refrigerant vapor steam as an energy source, said absorption type from another part of the pure water heat recovery to the water storage tank before Symbol exhaust gas to produce steam a second steam generator for supplying to the refrigerator Further pure water supply means for supplying a part of the other from the holding tank to the first steam generator of the pure water, and coolant supply means for supplying a refrigerant obtained by the absorption chiller inboard of the air conditioner It is equipped with.
[0007]
According to the marine gas turbine system, by supplying the steam generated by recovering heat from the exhaust gas in the first steam generator to the combustor, the energy of the steam is injected and the constant pressure specific heat increases. since, since the large expansion work in the turbine, increasing the output of the gas turbine, and reduced fuel consumption and improved heat efficiency, and NO x can be reduced. Further, since the pure water production apparatus is operated by recovering heat from the exhaust gas of the gas turbine, the heat of the relatively high temperature exhaust gas coming out of the gas turbine can be effectively recovered together with the heat recovery in the first steam generator. Therefore, the thermal efficiency of the system is improved. In addition, since steam generated from pure water is supplied to the combustor, there is no damage to the waste heat boiler and gas turbine such as corrosion of the boiler pipe and turbine blade. In addition, drinking water for passengers or passengers necessary for the operation of the ship is secured.
The pure water obtained by the pure water production apparatus is temporarily stored in a water storage tank. For example, in a flash type pure water production device, a large amount of pure water cannot be obtained from seawater in a short time, but when a large amount of pure water is required such as when the output of a gas turbine is suddenly increased, This can be dealt with by supplying pure water from the water storage tank to the first steam generator by the pure water supply means. In addition, by connecting drinking water supply means to the water storage tank, temporary fluctuations in the amount of pure water used as drinking water will affect the amount of pure water that becomes steam supplied to the combustor. Absent.
[0009]
In addition, according to the gas turbine system, it is not necessary to separately prepare an energy source for generating a refrigerant in the absorption chiller , and the heat efficiency of the entire gas turbine system is further improved by using the heat of the exhaust gas. .
[0012]
Furthermore, in a preferred embodiment of the present invention, the steam supplied from the first steam generator to the combustor is superheated steam.
[0013]
With this configuration, high-energy steam is supplied into the combustor of the gas turbine, so that the output of the gas turbine is further increased.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic configuration diagram showing a gas turbine system including a pure water producing apparatus according to an embodiment of the present invention.
The marine gas turbine system of the present invention includes a gas turbine 1 having a marine propulsion device 2 such as a screw, a water jet, an air compressor for hovercraft, etc. and a generator for electric propulsion as loads. The gas turbine 1 compresses air with the compressor 3 and guides it to the combustion chamber of the combustor 4, injects fuel into the combustion chamber and burns it, and drives the turbine 5 with the high-temperature and high-pressure combustion gas.
[0015]
The exhaust gas from the gas turbine 1 is guided to the waste heat boiler 10. The waste heat boiler 10 includes a first steam generator 11, a second steam generator 12, and a raw water heater 13. The first steam generator 11 recovers heat from the introduced exhaust gas to generate superheated steam, and the superheated steam is injected into the combustion chamber of the combustor 4 of the gas turbine 1 through the steam supply pipe 15. On the other hand, since the exhaust gas after heat recovery by the first steam generator 11 still has sufficient thermal energy, it further passes through the second steam generator 12 and the raw water heater 13 in order. After sufficiently recovering the thermal energy, it is discharged from the waste heat boiler 10 and discharged into the atmosphere through a chimney (not shown).
[0016]
As water for steam generation supplied to the first steam generator 11, pure water obtained using seawater as raw water during ship navigation in the pure water production apparatus 20 is used. Examples of the pure water production apparatus 20 for obtaining pure water from seawater include a flash type, a reheat type, and a vapor compression type. It is preferable to use a flash type in terms of thermal efficiency and other points.
[0017]
Next, the pure water production apparatus 20 will be described. The pure water production apparatus 20 heats seawater to obtain pure water by flash evaporation, and circulates seawater taken from the sea with a low-pressure circulation pump 21 and is provided in the circulation path. After heating with the raw water heater 13, the water is blown out from the nozzle to the evaporation chamber in the pure water production apparatus 20. On the other hand, saturated steam is supplied from the middle of the first steam generator 11 to the ejector 25, and the evaporation chamber is evacuated by the suction force of the steam expanding in the ejector 25, so that the pressure in the evaporation chamber is equal to or lower than the saturated vapor pressure. When this happens, the seawater heated and blown into the evaporation chamber boils to generate steam. This steam condenses by touching the cold seawater circulating in the pure water production apparatus 20 as it rises in the evaporation chamber, liquefies and accumulates in the distiller. The accumulated distilled water, that is, pure water from which salt or the like has been removed, is pumped out by the low-pressure feed pump 23 and fed to the low-pressure feed pipe 22.
[0018]
The pure water sent to the low-pressure water supply pipe 22 by the operation of the low-pressure water supply pump 23 is temporarily stored in a water storage tank 30 provided with a water level sensor 32. The low pressure water supply pipe 22 is provided with a control valve 33 that is opened and closed by a water level detection signal from the water level sensor 32. A portion of the pure water stored in the water storage tank 30 is taken out by a drinking water supply means 35 having a drinking water pipe 35a and a water pump 35b connected to the storage tank 30, and used as drinking water. Another part of the pure water stored in the water storage tank 30 can be injected against the high pressure in the combustor 4 by the pure water supply means 36 having a pure water supply pipe 36a and a high pressure pump 36b. The pressure is increased to a high pressure and then supplied to the first steam generator 11. In the first steam generator 11, pure water sent from the pure water supply means 36 is heated by the exhaust gas supplied from the gas turbine 1 to generate steam, and the generated high-pressure superheated steam is supplied to the steam supply pipe 15. It is sent out and injected into the combustion chamber in the combustor 4 of the gas turbine 1. On the other hand, as described above, the saturated steam is supplied to the ejector 25 from the middle of the first steam generator 11, and the steam liquefied from the ejector 25 is collected in the water storage tank 30.
[0019]
Further, the absorption refrigerator 40 will be described. The absorption refrigerator 40 is a well-known type that generates cold water using steam as an energy source. The absorption refrigerator 40 is generated by the steam generated by the second steam generator 12 and supplied via steam supply means 41 having a steam supply pipe. Operate. The cold water obtained by the absorption chiller 40 is supplied to one or more air conditioners 46 in the ship via a refrigerant supply means 45 having a refrigerant supply pipe as a refrigerant. The air conditioner 46 includes the radiator 47 and the air blowing fan 48 shown in FIG. The refrigerant used in the radiator 47 is supplied to the downstream side of the refrigerant supply means 45 and returned to the absorption refrigeration machine 40 again. An opening / closing valve 49 is provided in a pipe branched from the refrigerant supply means 45 and connected to the air conditioner 46 and is opened when the air conditioner 46 is used.
[0020]
The steam supply means 41 from the second steam generator 12 to the absorption refrigerator 40 has a process steam supply pipe 50 for supplying a part of the steam as process steam to a place where steam or hot water is required in the ship. It is connected. The process steam supply pipe 50 is provided with an on-off valve 51 for supplying and stopping steam.
[0021]
Next, the operation of the marine gas turbine system provided with the pure water production apparatus will be described.
[0022]
In the above configuration, pure water is produced by pumping seawater, sending it to the raw water heater 13 with the low-pressure pump 21, heating it, and supplying it to the pure water production apparatus 20. The pure water obtained by the pure water production apparatus 20 is stored in the water storage tank 30 by the low pressure water supply pump 23 via the low pressure water supply pipe 22. The amount of pure water supplied to the water storage tank 30 is adjusted by operating a control valve 33 provided in the low-pressure water supply pipe 22 by a water level sensor 32. That is, when the water level sensor 32 detects the water level at the upper limit level, a detection signal is output and the control valve 33 is closed, thereby regulating the water level below the upper limit level. Moreover, a part of pure water is supplied by the drinking water supply means 35 as drinking water used in the ship. The other part of pure water stored in the water storage tank 30 is supplied to the first steam generator 11 through the pure water supply means 36, and the obtained superheated steam is injected and injected into the combustor 4 of the gas turbine 1. The Furthermore, a part of the pure water stored in the water storage tank 30 is supplied to the second steam generator 12, and the obtained steam is supplied to the absorption chiller 40 through the steam supply pipe 41. The refrigerant obtained by the absorption chiller 40 is sent to the air conditioner 46 in the ship to cool the ship. The temperature adjustment of the air conditioner 46 is performed by controlling the steam supplied through the steam supply means 41. For example, the temperature sensor 42 is provided in the refrigerant supply means 45, the control valve 43 is provided in the vapor supply means 41, and the supply is performed by adjusting the opening of the control valve 43 based on the temperature detection signal from the temperature sensor 42. The amount of vapor is controlled to adjust the refrigerant in the refrigerant supply means 45 to a temperature set in advance in the temperature sensor 42. The refrigerant used in the air conditioner 46 is supplied to the downstream side of the refrigerant supply means 45 and returned to the absorption refrigerator 40 again. Further, the drain from the absorption refrigerator 40 is supplied to the low-pressure water supply pipe 22 and returned to the water storage tank 30 through the low-pressure water supply pipe 22. Further, by opening the on-off valve 51 provided in the process steam supply pipe 50, the process steam is supplied to the place where steam or hot water is required through the process steam supply pipe 50.
[0023]
In the present embodiment, the first steam generator 11 and the second steam generator 12 are provided separately as the evaporation generator, but the first steam generator 11 and the second steam generator 12 may be common.
[0024]
【The invention's effect】
As described above, according to the marine gas turbine system of the present invention, by supplying the steam generated by recovering heat from the exhaust gas in the first steam generator to the combustor, the energy of the steam is injected. , since the specific heat at constant pressure is increased, since the large expansion work in the turbine, increasing the output of the gas turbine, and reduced fuel consumption and improved heat efficiency, and NO x can be reduced. Further, since the pure water production apparatus is operated by recovering heat from the exhaust gas of the gas turbine, the heat of the relatively high temperature exhaust gas coming out of the gas turbine can be effectively recovered together with the heat recovery in the first steam generator. Therefore, the thermal efficiency of the system is improved. In addition, since steam generated from pure water is supplied to the combustor, there is no damage to the waste heat boiler and gas turbine such as corrosion of the boiler pipe and turbine blade. In addition, drinking water for passengers or passengers necessary for the operation of the ship is secured.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram showing a marine gas turbine system including a pure water producing apparatus according to an embodiment of the present invention.
FIG. 2 is a schematic view of an air conditioner 46 for a marine gas turbine according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Gas turbine, 2 ... Marine propulsion device, 3 ... Compressor, 4 ... Combustor, 5 ... Turbine, 11 ... 1st steam generator, 12 ... 2nd steam generator, 13 ... Raw water heater, 15 ... Steam Supply means, 20 ... pure water production apparatus, 30 ... water storage tank, 35 ... drinking water supply means, 36 ... pure water supply means, 40 ... absorption refrigerator, 45 ... refrigerant supply means, 46 ... air conditioner.

Claims (2)

圧縮機、燃焼器、およびタービンを有し、舶用推進機を駆動するガスタービンと、
ガスタービンの排ガスから熱回収して蒸気を生成する第1蒸気生成器と、
前記排ガスから熱回収して原水を加熱する原水加熱器と、
加熱された原水から純水を得る純水製造装置と、
前記純水製造装置で得られた純水を貯留する貯水タンクと、
前記貯水タンク内の純水の一部を飲料水として取り出す飲料水供給手段と
記第1蒸気生成器で得られる蒸気を前記燃焼器に供給する蒸気供給手段と
気をエネルギ源として冷媒を生成する吸収式冷凍機と、
記排ガスから熱回収して貯水タンクの純水の他の一部から蒸気を生成して前記吸収式冷凍機に供給する第2蒸気生成器と、
前記純水のさらに他の一部を貯水タンクから前記第1蒸気生成器に供給する純水供給手段と、
前記吸収式冷凍機で得られた冷媒を船内の空調機に供給する冷媒供給手段と
を備えた舶用ガスタービンシステム。
A gas turbine having a compressor, a combustor, and a turbine and driving a marine propulsion device;
A first steam generator for generating steam by recovering heat from the exhaust gas of the gas turbine;
A raw water heater for recovering heat from the exhaust gas and heating the raw water;
A pure water production apparatus for obtaining pure water from heated raw water;
A water storage tank for storing pure water obtained by the pure water production apparatus;
Drinking water supply means for taking out a portion of pure water in the water storage tank as drinking water ;
A steam supply means for supplying steam obtained in the previous SL first steam generator to the combustor,
And the absorption chiller to produce a refrigerant as an energy source a gas steam,
A second steam generator supplied to the absorption chiller to generate steam from another part of the pure water heat recovery to the water storage tank before SL gas,
Pure water supply means for supplying still another part of the pure water from a water storage tank to the first steam generator;
Refrigerant supply means for supplying the refrigerant obtained by the absorption refrigeration machine to the air conditioner in the ship ,
Marine gas turbine system equipped with
請求項1において、前記第1蒸気生成器から燃焼器に供給される蒸気が過熱蒸気である舶用ガスタービンシステム。  The marine gas turbine system according to claim 1, wherein the steam supplied from the first steam generator to the combustor is superheated steam.
JP2002126132A 2002-04-26 2002-04-26 Marine gas turbine system with pure water production equipment Expired - Lifetime JP4109488B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002126132A JP4109488B2 (en) 2002-04-26 2002-04-26 Marine gas turbine system with pure water production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002126132A JP4109488B2 (en) 2002-04-26 2002-04-26 Marine gas turbine system with pure water production equipment

Publications (3)

Publication Number Publication Date
JP2003312588A JP2003312588A (en) 2003-11-06
JP2003312588A5 JP2003312588A5 (en) 2005-08-18
JP4109488B2 true JP4109488B2 (en) 2008-07-02

Family

ID=29540651

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002126132A Expired - Lifetime JP4109488B2 (en) 2002-04-26 2002-04-26 Marine gas turbine system with pure water production equipment

Country Status (1)

Country Link
JP (1) JP4109488B2 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4762555B2 (en) * 2004-08-02 2011-08-31 日揮株式会社 Power generation desalination method
CN100453403C (en) * 2006-11-30 2009-01-21 上海交通大学 Gas-steam power propulsion, power supply and steam supply combined system for giant ships
JP5492695B2 (en) * 2010-07-23 2014-05-14 本田技研工業株式会社 pump
JP2014080878A (en) * 2012-10-15 2014-05-08 Rui Qi Tong Heat recovery converter
CN104895675B (en) * 2015-06-04 2017-01-04 中国科学院工程热物理研究所 Can the solar energy that runs continuously of whole day and biomass complementation association circulating power generation system
JP6192771B2 (en) * 2016-05-30 2017-09-06 ヤンマー株式会社 Exhaust gas purification equipment for ships
JP6562105B1 (en) * 2018-03-23 2019-08-21 栗田工業株式会社 Pure water production equipment
JP6562107B1 (en) * 2018-03-23 2019-08-21 栗田工業株式会社 Pure water production equipment
JP6575626B1 (en) * 2018-03-23 2019-09-18 栗田工業株式会社 Pure water production equipment

Also Published As

Publication number Publication date
JP2003312588A (en) 2003-11-06

Similar Documents

Publication Publication Date Title
CA2230325C (en) Steam cooled gas turbine system
RU2468214C2 (en) Device including steam turbine and condenser
CA2084862C (en) Gas turbine steam addition
US11199361B2 (en) Method and apparatus for net zero-water power plant cooling and heat recovery
JP4109488B2 (en) Marine gas turbine system with pure water production equipment
CA2768347C (en) Gas turbine exhaust gas cooling system
JP2003161164A (en) Combined cycle power plant
KR20190010038A (en) Hybrid power generating system
WO2012042641A1 (en) Combined cycle plant utilizing solar heat
EP1752618A3 (en) Steam cooled system in combined cycle power plant
US6286297B1 (en) Steam cooled type combined cycle power generation plant and operation method thereof
JP2012189008A (en) Thermal power generating plant
JP2006249942A (en) Exhaust heat recovery system of reciprocation type internal combustion engine with supercharger
JPH11173109A (en) Power generation and hot water supply system
JP2680288B2 (en) Steam injection gas turbine system and operating method thereof
CN111608741A (en) An ORC system for recovery and utilization of generator waste heat
JP2002004943A (en) How to increase overall efficiency in cogeneration systems
RU2409746C2 (en) Steam-gas plant with steam turbine drive of compressor and regenerative gas turbine
JP2003312588A5 (en)
JPH0688538A (en) Gas turbine plant
CN105041394B (en) A power generation system and its operation control method
JP4555784B2 (en) Steam generating apparatus using low-temperature waste heat, thermoelectric supply apparatus using the apparatus, and steam generating method
JPH11270347A (en) Gas turbine combined power generation device using LNG
KR101215477B1 (en) Combustion air cooling systemm of engine for vessel
JP2012159238A (en) Steam system

Legal Events

Date Code Title Description
A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050204

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050204

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070607

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070619

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20070820

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20071204

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080121

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080110

A911 Transfer of reconsideration by examiner before appeal (zenchi)

Free format text: JAPANESE INTERMEDIATE CODE: A911

Effective date: 20080215

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20080401

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20080404

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110411

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120411

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120411

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130411

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130411

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140411

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150411

Year of fee payment: 7