JPH05296009A - Exhaust heat recovery system for steam turbine equipment - Google Patents
Exhaust heat recovery system for steam turbine equipmentInfo
- Publication number
- JPH05296009A JPH05296009A JP1363291A JP1363291A JPH05296009A JP H05296009 A JPH05296009 A JP H05296009A JP 1363291 A JP1363291 A JP 1363291A JP 1363291 A JP1363291 A JP 1363291A JP H05296009 A JPH05296009 A JP H05296009A
- Authority
- JP
- Japan
- Prior art keywords
- condenser
- evaporator
- refrigerator
- heat source
- water
- 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
Links
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、汽力発電のコジェネレ
ーションシステムとして適用する蒸気タービン設備の排
熱回収システムに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust heat recovery system for steam turbine equipment applied as a cogeneration system for steam power generation.
【0002】[0002]
【従来の技術】昨今では、都市のごみ焼却場などを対象
とした熱エネルギーの有効利用法として、ごみ焼却炉に
付属するボイラにて蒸気を発生させ、この蒸気を使って
汽力発電,および地域冷暖房を行うようにしたコジェネ
レーションシステムが普及化されつつあり、その一例と
して、発電機を駆動する蒸気タービンから抽出した蒸気
を熱源として吸収式冷凍機を運転し、冷房用冷水を得る
コジェネレーションシステムが知られている。2. Description of the Related Art Recently, as an effective utilization method of thermal energy for a refuse incinerator in a city, steam is generated in a boiler attached to a refuse incinerator, and steam is used for steam power generation and local use. A cogeneration system for cooling and heating is becoming widespread, and one example is a cogeneration system that obtains cold water for cooling by operating an absorption refrigerator using steam extracted from a steam turbine that drives a generator as a heat source. It has been known.
【0003】一方、冷凍機は冷凍運転の他に、蒸発器か
ら熱を取り込み、凝縮器側から暖房用温水を得るように
したヒートポンプ運転が可能であることから、特に前記
した蒸気タービン設備を対象に、蒸気タービンの復水器
から出た高温の冷却排水を熱源水として冷凍機の蒸発器
に通水し、凝縮器側から暖房用温水を得るとともに、同
時に蒸発器を通流して温度の低下した水を冷却水として
再び復水器に戻すようにしたヒートポンプによる排熱回
収システムが提唱され、その開発が進められている。On the other hand, in addition to the refrigerating operation, the refrigerator can be operated by a heat pump in which heat is taken in from the evaporator and hot water for heating is obtained from the condenser side. In addition, hot cooling wastewater from the steam turbine condenser is used as heat source water to pass through to the evaporator of the refrigerator to obtain hot water for heating from the condenser side, and at the same time, to pass through the evaporator to lower the temperature. An exhaust heat recovery system using a heat pump that returns the generated water as cooling water to the condenser again has been proposed and its development is in progress.
【0004】[0004]
【発明が解決しようとする課題】ところで、前記のよう
に蒸気タービン復水器の排熱を利用し、冷凍機をヒート
ポンプ運転して暖房用温水を得るようにした排熱回収シ
ステムでは、復水器から冷凍機の蒸発器が取り込む熱量
は復水器の負荷、つまり蒸気タービンの運転条件によっ
て決まる。このために、復水器より出た冷却排水の全量
をそのまま冷凍機の蒸発器に通流したのでは、地域暖房
のように暖房負荷の変動が大きい場合にうまく対応させ
ることができない。By the way, as described above, in the exhaust heat recovery system which utilizes the exhaust heat of the steam turbine condenser to operate the refrigerator by the heat pump to obtain the hot water for heating, The amount of heat taken from the condenser by the evaporator of the refrigerator is determined by the load of the condenser, that is, the operating conditions of the steam turbine. For this reason, if the entire amount of the cooling waste water discharged from the condenser is directly passed to the evaporator of the refrigerator, it is not possible to cope with the case where the heating load fluctuates greatly like district heating.
【0005】本発明は上記の点にかんがみなされたもの
であり、先記した蒸気タービン設備の排熱回収システム
を改良することにより、復水器の負荷,暖房負荷の変動
にも十分に対応できるようにした排熱回収システムを提
供することを目的とする。The present invention has been made in view of the above points, and by improving the exhaust heat recovery system of the steam turbine equipment described above, it is possible to sufficiently cope with fluctuations in the load of the condenser and the heating load. It is an object of the present invention to provide an exhaust heat recovery system as described above.
【0006】[0006]
【課題を解決するための手段】上記課題を解決するため
に、本発明の排熱回収システムにおいては、復水器と冷
凍機の蒸発器との間に配管した熱源水の循環ラインに対
して、熱源水の一部を循環ラインの途中から冷却塔を経
由して復水器に戻すバイパスラインを備え、暖房負荷の
変動に対応して前記蒸発器に流す熱源水の通水量とバイ
パスラインへ分流する通水量との割合を調整して運転を
行うよう構成するものとする。In order to solve the above problems, in the exhaust heat recovery system of the present invention, the heat source water circulation line connected between the condenser and the evaporator of the refrigerator is used. A bypass line that returns a part of the heat source water to the condenser from the middle of the circulation line to the condenser via the cooling tower is provided, and the heat source water flow to the evaporator and the bypass line in response to the fluctuation of the heating load. The operation shall be performed by adjusting the ratio with the flow rate of the divided water flow.
【0007】ここで、前記の構成における冷凍機として
は、蒸気タービンから抽出した蒸気を再生器に供給して
運転する吸収式冷凍機が採用できる。また、当該排気熱
回収システムを利用して夏期に冷凍機より冷房用冷水を
得るためには、冷凍機の蒸発器に対し復水器との間に配
管した熱源水循環ラインの他に冷水供給ラインを接続
し、熱源水循環ラインを蒸発器から切り離した上で冷水
供給ラインを通じて蒸発器より冷房用冷水を得ることも
できる。Here, as the refrigerator in the above-mentioned structure, an absorption refrigerator that operates by supplying steam extracted from a steam turbine to a regenerator can be adopted. In addition, in order to obtain cold water for cooling from the refrigerator in the summer using the exhaust heat recovery system, in addition to the heat source water circulation line connected between the evaporator of the refrigerator and the condenser, the cold water supply line It is also possible to obtain cold water for cooling from the evaporator through a cold water supply line after connecting the heat source water circulation line to the heat source water circulation line from the evaporator.
【0008】[0008]
【作用】上記の構成において、冷却塔は熱源水循環ライ
ンの途中からバイパスラインに分流する復水器の冷却排
水を冷却して温度を下げ、循環ポンプを経て再び復水器
に戻すように働く。そして、ヒートポンプ運転時に暖房
負荷が変動した場合には、復水器から熱源水として冷凍
機の蒸発器へ供給する冷却排水の通水量と、前記バイパ
スラインへ分流させる通水量との割合を調整することに
より、冷凍機の蒸発器に取り込む熱量を暖房負荷の変動
に対応させて適正に調整できる。In the above construction, the cooling tower works to cool the cooling waste water of the condenser diverting from the middle of the heat source water circulation line to the bypass line to lower the temperature, and to return it to the condenser again via the circulation pump. When the heating load fluctuates during the heat pump operation, the ratio between the amount of cooling waste water supplied from the condenser to the evaporator of the refrigerator as heat source water and the amount of water flow divided into the bypass line is adjusted. As a result, the amount of heat taken into the evaporator of the refrigerator can be appropriately adjusted according to the fluctuation of the heating load.
【0009】また、冷凍機として吸収式冷凍機を採用す
ることにより、圧縮機を使わずに蒸気タービンから抽出
した蒸気を利用して冷凍機を運転できる。さらに、熱源
水循環ラインを蒸発器より切り離した状態で冷凍機を冷
凍運転すれば、蒸発器に接続した冷水供給ラインを通じ
て冷房用冷水が得られる。Further, by adopting the absorption type refrigerator as the refrigerator, the refrigerator can be operated by using the steam extracted from the steam turbine without using the compressor. Further, if the refrigerator is operated in a freezing state with the heat source water circulation line separated from the evaporator, cold water for cooling can be obtained through the cold water supply line connected to the evaporator.
【0010】[0010]
【実施例】図1は本発明実施例の系統図を示すものであ
る。図において、1はごみ焼却場の焼却炉などに設置し
たボイラ、2はボイラ1の発生蒸気で運転する蒸気ター
ビン、3は蒸気タービン2に連結した発電機、4は冷却
コイル4aを内蔵した蒸気タービン2の表面式復水器、
5は吸収式冷凍機である。ここで、吸収式冷凍機5は、
再生器5a,凝縮器5b,蒸発器5c,吸収器5dを備
えており、蒸気タービン2から抽出した蒸気を熱源とし
て再生器5aに供給して運転される。なお、かかる吸収
式冷凍機の冷凍サイクルについては周知であり、ここで
はその説明を省略する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a system diagram of an embodiment of the present invention. In the figure, 1 is a boiler installed in an incinerator of a refuse incinerator, 2 is a steam turbine operated by the steam generated by the boiler 1, 3 is a generator connected to the steam turbine 2, and 4 is steam having a cooling coil 4a built therein. Turbine 2 surface condenser,
Reference numeral 5 is an absorption refrigerator. Here, the absorption refrigerator 5 is
The regenerator 5a, the condenser 5b, the evaporator 5c, and the absorber 5d are provided, and the steam extracted from the steam turbine 2 is supplied to the regenerator 5a as a heat source for operation. The refrigeration cycle of such an absorption chiller is well known, and the description thereof is omitted here.
【0011】一方、復水器4の冷却コイル4aと前記冷
凍機の蒸発器5cとの間には、冷却コイル4aより蒸発
器5c,冷却塔6,循環ポンプ7を経由して再び冷却コ
イル4aに戻る熱源水循環ライン8が配管されており、
冷凍機5をヒートポンプとして運転する場合に、復水器
4の冷却コイル4aから出た高温の冷却排水を熱源水と
して冷凍機5の蒸発器5cに通水し、吸収器5d,凝縮
器5bを通じて暖房用温水を得るようにしている。ま
た、前記の熱源水循環ライン8に対しては、ラインの途
中から分岐して冷却塔9を経由するバイパスライン10
を備えており、さらに蒸発器5cには前記した熱源水循
環ライン8の他に、冷房用冷水を得る冷水供給ライン1
1が接続配管されている。なお、12〜16は前記ライ
ンの各所に接続した開閉バルブである。On the other hand, between the cooling coil 4a of the condenser 4 and the evaporator 5c of the refrigerator, the cooling coil 4a again passes through the evaporator 5c, the cooling tower 6 and the circulation pump 7 and is again cooled. The heat source water circulation line 8 returning to
When the refrigerator 5 is operated as a heat pump, the high-temperature cooling drainage discharged from the cooling coil 4a of the condenser 4 is passed as the heat source water to the evaporator 5c of the refrigerator 5, and is passed through the absorber 5d and the condenser 5b. I try to get hot water for heating. Further, with respect to the heat source water circulation line 8, the bypass line 10 is branched from the middle of the line and passes through the cooling tower 9.
In addition to the heat source water circulation line 8 described above, the evaporator 5c further includes a cold water supply line 1 for obtaining cold water for cooling.
1 is connected and piped. In addition, 12 to 16 are open / close valves connected to various parts of the line.
【0012】かかる構成で冬期に暖房用温水を得る場合
には、基本的にはバルブ12,14を開,バルブ13,
15,16を閉とした状態で、復水器4の冷却コイル4
aより出た高温の冷却排水を熱源水として冷凍機5の蒸
発器5cに通水し、復水器4で回収した排熱を蒸発器5
cに与える。これにより冷凍機5はヒートポンプとして
作動し、凝縮器5b,吸収器5dを通じて暖房用温水が
得られる。なお、冷却排水は蒸発器5cを通流する過程
で熱が奪われるので水温が低下するが、復水器で要求さ
れる冷却水温度よりも若干高いので冷却塔6に通して冷
却し、再び循環ポンプ7を経て復水器4の冷却コイル4
aに還流する。In order to obtain hot water for heating in the winter with such a configuration, basically the valves 12 and 14 are opened and the valves 13 and 14 are opened.
Cooling coil 4 of condenser 4 with 15 and 16 closed
The high-temperature cooling waste water discharged from a is passed as the heat source water to the evaporator 5c of the refrigerator 5, and the waste heat recovered by the condenser 4 is transferred to the evaporator 5
give to c. Thereby, the refrigerator 5 operates as a heat pump, and hot water for heating is obtained through the condenser 5b and the absorber 5d. Although the cooling wastewater loses heat in the process of flowing through the evaporator 5c, the water temperature drops, but since it is slightly higher than the cooling water temperature required for the condenser, it is cooled by passing through the cooling tower 6 and then again. Cooling coil 4 of condenser 4 via circulation pump 7
reflux to a.
【0013】ここで、暖房負荷が小さい時には、バイパ
スライン10に接続したバルブ13を開き、かつその弁
開度を調節して冷却排水の一部を循環ライン8の途中か
らバイパスライン10に分流させる。これにより冷凍機
5の蒸発器5cを通流する熱源水の水量、したがって蒸
発器5cが取り込む熱量がその時点の暖房負荷に対応す
るようになる。なお、バイパスライン10に分流した冷
却排水は冷却塔9で冷却された後、蒸発器5c,冷却塔
6を経由した水と合流して再び復水器側に戻る。このよ
うに蒸発器5cに流す熱源水の通水量とバイパスライン
10に分流させる通水量との割合を調整することによ
り、暖房負荷の変動,ないし復水器の負荷変動に対応さ
せてヒートポンプの熱出力を調整することができる。Here, when the heating load is small, the valve 13 connected to the bypass line 10 is opened, and the opening degree of the valve 13 is adjusted to divert a part of the cooling drainage from the middle of the circulation line 8 to the bypass line 10. .. As a result, the amount of heat source water flowing through the evaporator 5c of the refrigerator 5, and thus the amount of heat taken in by the evaporator 5c, corresponds to the heating load at that time. The cooling wastewater that has been split into the bypass line 10 is cooled by the cooling tower 9, and then merges with the water that has passed through the evaporator 5c and the cooling tower 6 and returns to the condenser side again. By adjusting the ratio of the flow rate of the heat source water flowing to the evaporator 5c and the flow rate of the water split to the bypass line 10 in this manner, the heat of the heat pump can be adjusted in response to the fluctuation of the heating load or the fluctuation of the load of the condenser. The output can be adjusted.
【0014】一方、夏期に冷房用冷水を得る場合には、
バルブ12,14を閉じて熱源水循環ライン8を蒸発器
5cより切り離すとともに、バルブ15,16を開いて
蒸発器5cに接続した冷水供給ライン11に冷却水を流
し、この状態で冷凍機5を運転する。これにより、冷水
供給ライン11に流れる水が蒸発器5cで冷却されて冷
房用冷水が得られる。On the other hand, when obtaining cold water for cooling in the summer,
The valves 12 and 14 are closed to disconnect the heat source water circulation line 8 from the evaporator 5c, and the valves 15 and 16 are opened to flow cooling water to the cold water supply line 11 connected to the evaporator 5c, and the refrigerator 5 is operated in this state. To do. As a result, the water flowing in the cold water supply line 11 is cooled by the evaporator 5c, and cold water for cooling is obtained.
【0015】なお、図示実施例では冷凍機として吸収式
冷凍機を採用した例を述べたが、吸収式冷凍機の代わり
に圧縮式冷凍機を採用しても同様に実施できる。In the illustrated embodiment, an absorption type refrigerator is used as the refrigerator, but a compression type refrigerator may be used instead of the absorption type refrigerator.
【0016】[0016]
【発明の効果】以上述べたように、本発明による蒸気タ
ービン設備の排熱回収システムによれば、復水器と冷凍
機の蒸発器との間に配管した熱源水循環ラインに対し、
熱源水の一部を循環ラインの途中から冷却塔を経由して
復水器に戻すバイパスラインを備えたことにより、冷凍
機をヒートポンプとして運転することで、復水器から回
収した排熱を利用して地域暖房に必要な暖房用温水が得
られる。しかも、この場合に冷凍機の蒸発器に流す熱源
水の通水量とバイパスラインに分流させる通水量との割
合を調整することにより、暖房負荷の変動,復水器の負
荷変動にも容易に対応させることができる。As described above, according to the exhaust heat recovery system of the steam turbine facility according to the present invention, the heat source water circulation line connected between the condenser and the evaporator of the refrigerator is
By installing a bypass line that returns part of the heat source water from the middle of the circulation line to the condenser via the cooling tower, the exhaust heat recovered from the condenser can be used by operating the refrigerator as a heat pump. Then, the hot water for heating required for district heating is obtained. Moreover, in this case, by adjusting the ratio between the amount of heat source water flowing to the evaporator of the refrigerator and the amount of water flowing to the bypass line, it is possible to easily cope with fluctuations in heating load and fluctuations in condenser. Can be made
【0017】また、冷凍機とし吸収式冷凍機を採用する
ことで、蒸気タービンの抽気蒸気を熱源として冷凍機を
運転できる他、さらに夏期などで冷房を必要とする場合
には、前記熱源水循環ラインを蒸発器から切り離して冷
凍機を運転することにより、蒸発器に接続した冷水供給
ラインを通じて冷房用冷水が得られる。Further, by adopting an absorption type refrigerating machine as the refrigerating machine, the refrigerating machine can be operated by using the extracted steam of the steam turbine as a heat source. Further, when cooling is required in the summer, the heat source water circulation line is used. The cooling water is obtained through the cold water supply line connected to the evaporator by disconnecting from the evaporator and operating the refrigerator.
【図1】本発明の実施例による蒸気タービン設備の排熱
回収システムの系統図FIG. 1 is a system diagram of an exhaust heat recovery system for steam turbine equipment according to an embodiment of the present invention.
2 蒸気タービン 4 復水器 5 吸収式冷凍機 5a 再生器 5b 凝縮器 5c 蒸発器 5d 吸収器 8 熱源水循環ライン 9 冷却塔 10 バイパスライン 11 冷水供給ライン 2 Steam turbine 4 Condenser 5 Absorption refrigerator 5a Regenerator 5b Condenser 5c Evaporator 5d Absorber 8 Heat source water circulation line 9 Cooling tower 10 Bypass line 11 Cold water supply line
Claims (3)
用温水を得る蒸気タービン設備の排熱回収システムであ
り、表面復水器から出た冷却排水を熱源水として冷凍機
の蒸発器に通水し、該冷凍機をヒートポンプとして運転
して凝縮器より暖房用温水を得るものにおいて、復水器
と冷凍機の蒸発器との間に配管した熱源水循環ラインに
対し、熱源水の一部を循環ラインの途中から冷却塔を経
由して復水器に戻すバイパスラインを備え、暖房負荷の
変動に対応して前記蒸発器に流す熱源水の通水量とバイ
パスラインへ分流する通水量との割合を調整して運転を
行うことを特徴とする蒸気タービン設備の排熱回収シス
テム。1. An exhaust heat recovery system for steam turbine equipment, which obtains hot water for heating by utilizing exhaust heat of a steam turbine condenser, wherein the cooling waste water discharged from the surface condenser is used as heat source water to evaporate a refrigerator. In the one in which water is passed through the condenser and the refrigerator is operated as a heat pump to obtain hot water for heating from the condenser, the heat source water circulation line piped between the condenser and the evaporator of the refrigerator is used for the heat source water. A bypass line that returns a part of the circulation line to the condenser via the cooling tower is provided, and the amount of heat source water that flows to the evaporator and the amount of water that splits to the bypass line in response to changes in heating load. The exhaust heat recovery system for steam turbine equipment, which is operated by adjusting the ratio of
て、冷凍機が、蒸気タービンから抽出した蒸気を再生器
に供給して運転する吸収式冷凍機であることを特徴とす
る蒸気タービン設備の排熱回収システム。2. The exhaust heat recovery system according to claim 1, wherein the refrigerator is an absorption refrigerator that operates by supplying steam extracted from a steam turbine to a regenerator. Exhaust heat recovery system.
て、冷凍機の蒸発器に対し、復水器との間に配管した熱
源水循環ラインの他に冷水供給ラインを接続し、冷房運
転時には熱源水循環ラインを蒸発器から切り離した上
で、冷水供給ラインを通じて蒸発器より冷房用冷水を得
るようにしたことを特徴とする蒸気タービン設備の排熱
回収システム。3. The exhaust heat recovery system according to claim 1, wherein a cooling water supply line is connected to the evaporator of the refrigerator in addition to the heat source water circulation line connected between the evaporator and the condenser, and during cooling operation. An exhaust heat recovery system for steam turbine equipment, characterized in that the heat source water circulation line is separated from the evaporator, and then cold water for cooling is obtained from the evaporator through a cold water supply line.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1363291A JPH05296009A (en) | 1991-02-05 | 1991-02-05 | Exhaust heat recovery system for steam turbine equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1363291A JPH05296009A (en) | 1991-02-05 | 1991-02-05 | Exhaust heat recovery system for steam turbine equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05296009A true JPH05296009A (en) | 1993-11-09 |
Family
ID=11838614
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1363291A Pending JPH05296009A (en) | 1991-02-05 | 1991-02-05 | Exhaust heat recovery system for steam turbine equipment |
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JP (1) | JPH05296009A (en) |
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JP2006144633A (en) * | 2004-11-18 | 2006-06-08 | Tokyo Metropolitan Sewerage Service Corp | System and method for incinerating disposal objects |
JP2010038160A (en) * | 2008-07-31 | 2010-02-18 | General Electric Co <Ge> | System and method for use in combined or rankine cycle power plant |
CN101832156A (en) * | 2010-05-10 | 2010-09-15 | 江苏双良空调设备股份有限公司 | Condensation heat recovering and central heating supply system of power plant direct air cooling unit |
CN101906997A (en) * | 2010-07-05 | 2010-12-08 | 双良节能系统股份有限公司 | Condensation heat recovery central heating system of power plant indirect air cooling machine set |
CN102305424A (en) * | 2011-08-04 | 2012-01-04 | 际高建业有限公司 | Heating system with great temperature difference and low temperature radiation |
CN102705021A (en) * | 2012-05-25 | 2012-10-03 | 国电龙源电力技术工程有限责任公司 | Cold end optimizing and residual heat utilizing system for steam turbine |
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KR101603253B1 (en) * | 2014-09-15 | 2016-03-15 | 한국전력공사 | Condenser Waste-heat Recovery System |
CN106437906A (en) * | 2016-08-16 | 2017-02-22 | 华电电力科学研究院 | Circulation water waste heat recycling device and method for indirect air cooling unit |
CN106437907A (en) * | 2016-08-16 | 2017-02-22 | 华电电力科学研究院 | Direct air cooling unit exhaust steam waste heat recovery device and method |
CN106979044A (en) * | 2017-04-21 | 2017-07-25 | 重庆大学 | Pump type heat turbine condenser condensing heating system |
JP2020143880A (en) * | 2019-03-08 | 2020-09-10 | 栗田工業株式会社 | Power generation system |
CN111663971A (en) * | 2020-05-31 | 2020-09-15 | 联合瑞升(北京)科技有限公司 | Condensate system of exhaust steam recovery heat supply supercritical unit and operation method |
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1991
- 1991-02-05 JP JP1363291A patent/JPH05296009A/en active Pending
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JP2006144633A (en) * | 2004-11-18 | 2006-06-08 | Tokyo Metropolitan Sewerage Service Corp | System and method for incinerating disposal objects |
JP4707370B2 (en) * | 2004-11-18 | 2011-06-22 | 東京都下水道サービス株式会社 | Processed object incineration system and processable object incineration method |
JP2010038160A (en) * | 2008-07-31 | 2010-02-18 | General Electric Co <Ge> | System and method for use in combined or rankine cycle power plant |
CN101666249A (en) * | 2008-07-31 | 2010-03-10 | 通用电气公司 | System and method for use in a combined or rankine cycle power plant |
CN101832156A (en) * | 2010-05-10 | 2010-09-15 | 江苏双良空调设备股份有限公司 | Condensation heat recovering and central heating supply system of power plant direct air cooling unit |
CN101906997A (en) * | 2010-07-05 | 2010-12-08 | 双良节能系统股份有限公司 | Condensation heat recovery central heating system of power plant indirect air cooling machine set |
CN102305424A (en) * | 2011-08-04 | 2012-01-04 | 际高建业有限公司 | Heating system with great temperature difference and low temperature radiation |
CN102705021A (en) * | 2012-05-25 | 2012-10-03 | 国电龙源电力技术工程有限责任公司 | Cold end optimizing and residual heat utilizing system for steam turbine |
CN102777961A (en) * | 2012-08-14 | 2012-11-14 | 江西省电力设计院 | Efficient heating system of direct air cooling machine set |
KR101603253B1 (en) * | 2014-09-15 | 2016-03-15 | 한국전력공사 | Condenser Waste-heat Recovery System |
CN106437906A (en) * | 2016-08-16 | 2017-02-22 | 华电电力科学研究院 | Circulation water waste heat recycling device and method for indirect air cooling unit |
CN106437907A (en) * | 2016-08-16 | 2017-02-22 | 华电电力科学研究院 | Direct air cooling unit exhaust steam waste heat recovery device and method |
CN106437907B (en) * | 2016-08-16 | 2018-08-07 | 华电电力科学研究院 | A kind of Direct Air-cooled Unit exhausted spare heat retracting device and method |
CN106979044A (en) * | 2017-04-21 | 2017-07-25 | 重庆大学 | Pump type heat turbine condenser condensing heating system |
JP2020143880A (en) * | 2019-03-08 | 2020-09-10 | 栗田工業株式会社 | Power generation system |
CN111663971A (en) * | 2020-05-31 | 2020-09-15 | 联合瑞升(北京)科技有限公司 | Condensate system of exhaust steam recovery heat supply supercritical unit and operation method |
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