US3596888A - Arrangement of mixing condensers for steam turbine powerplants - Google Patents

Arrangement of mixing condensers for steam turbine powerplants Download PDF

Info

Publication number
US3596888A
US3596888A US750157A US3596888DA US3596888A US 3596888 A US3596888 A US 3596888A US 750157 A US750157 A US 750157A US 3596888D A US3596888D A US 3596888DA US 3596888 A US3596888 A US 3596888A
Authority
US
United States
Prior art keywords
water
condenser
mixing
level
higher level
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
US750157A
Other languages
English (en)
Inventor
Laszlo Heller
Laszlo Forgo
Janos Bodas
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.)
Transelektro Magyar Villamossagi Kulkereskedelmi
Original Assignee
Transelektro Magyar Villamossagi Kulkereskedelmi
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 Transelektro Magyar Villamossagi Kulkereskedelmi filed Critical Transelektro Magyar Villamossagi Kulkereskedelmi
Application granted granted Critical
Publication of US3596888A publication Critical patent/US3596888A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

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
    • F01K9/00Plants characterised by condensers arranged or modified to co-operate with the engines
    • F01K9/003Plants characterised by condensers arranged or modified to co-operate with the engines condenser cooling circuits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B3/00Condensers in which the steam or vapour comes into direct contact with the cooling medium
    • F28B3/04Condensers in which the steam or vapour comes into direct contact with the cooling medium by injecting cooling liquid into the steam or vapour
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/90Cooling towers
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00Gas and liquid contact apparatus
    • Y10S261/11Cooling towers

Definitions

  • a system of mixing condensers is provided in which the water levels are maintained at various levels within portions of such mixing condensers connected in series in respect of cooling waters, there being provided at least one pair of mixing condensers, the cooling water sides of which are connected in series and one of which is arranged at a higher level than the other, the cooling water introduced into the mixing condenser of higher level flowing into the mixing condenser of lower level under the action of a hydrostatic pressure difference, the water chamber of the mixing condenser of the higher level forming a vertical downflow conduit having a cross-sectional area which is a fraction of that of the mixing condenser of lower level.
  • This invention relates to an arrangement of mixing condensers for steam turbine powerplants.
  • up-to-date thermal powerplants are equipped with turbogenerators of possibly high unit power the steam turbines of which are provided with a plurality of outlet stubs for the withdrawing of dead steam.
  • Such steam flows from each outlet stub into individual condensers or into a common condenser where it becomes precipitated.
  • the arrangement is such that condenser portions connected each to an outlet stub of the steam turbine are traversed by cooling water required for precipitating the dead steam in parallel connection so that the same vacuum is generated in all outlet stubs.
  • an arrangement is known as well with which the individual condenser portions are traversed by the cooling water in series connection.
  • the greatest vacuum is generated in the outlet stub at which the cold cooling water enters the system.
  • the vacuum decreases in correspondence with the warming up of the cooling water. It can be shown that by maintaining a mean value of vacuum obtainable by such series or parallel connection of the various condenser portions traversed by the cooling water of multiflow steam turbines, the heat transmission surface of the condenser may be decreased or, the condenser surface being the same and a higher mean value of vacuum being obtainable, the efficiency of the steam turbine may be increased.
  • a series connection of the cooling water of surface condensers requires, as a rule, only that the construction of the condenser be correspondingly changed.
  • a single cooling water pump is sufficient even if the cooling water flows in seriesly connected condenser portions.
  • the cooling water traverses the steam chamber of the condenser in the form of a free jet and, therefore, two or more pumps are needed for making the cooling water flow through two or more condenser portions in series connection.
  • a single pump may be employed if the mixing condenser units disposed each downstream an individual outlet stub are arranged at various levels in such a manner that the cooling water traversing the first mixing condenser arranged at a highest level flows under the action of gravity by free drop into a subsequent condenser arranged at a lower level, etc.
  • the feasibility of such system depends on the level difference required between subsequent condenser portions. This level difference depends, in turn, considerably on the water column height between individual condenser portions or units caused by the vacuum which corresponds to the warming up of the cooling water, and on the flow resistance of the nozzles which serve to form the jets of cooling water.
  • the main object of the present invention is to provide a system of mixing condensers in which the water levels are maintained at various levels within portions of mixing condensers connected in series as regards the cooling water, and controlled in correspondence with various operational conditions of a powerplant.
  • a system of seriesly connected mixing condensers is obtained which, due to the aforesaid control of the water levels may be operated by a single circulating pump.
  • the invention provides at least one pair of mixing condensers the cooling water sides of which are connected in series and one of which is arranged at a higher level than the other, the cooling water introduced into the mixing condenser of higher level flowing from it into the mixing condenser of lower level under the action of a hydrostatic pressure difference, and the water chamber of the mixing condenser of higher level forming a vertical downflow conduit having a cross-sectional area which is a fraction of the crosssectional area of the mixing condenser of lower level.
  • FIGS. 1 and 2 are connection diagrams of known and new plants, respectively.
  • FIG. ll shows the connection diagram of a known dry cooling tower powerplant where a double-flow turbine l is employed and the mixing condenser of the plant is composed of two parts or consists of two units 2 and 3 disposed at different levels and connected in series on their cooling water sides.
  • the dead steam of the steam turbine ll becomes condensed by the mixing condenser 2 of higher level and by the mixing condenser 3 of lower level.
  • the cooling water flows through a pipe conduit 19 into the mixing condenser 2 of higher level which is provided at its top with a series of nozzles. The cooling water is discharged through these nozzles and traverses the steam chamber of the condenser 2 in the form of free jets.
  • the water level in condenser 2 of higher level exceeds the level of the nozzles of condenser 3 of lower level by a suitable amount in order to ensure that the pressure difference and the water column height in condenser 2 of higher level be enough for overwhelming the flow resistance within a pipe conduit 4 which connects the water chamber of condenser 2 of higher level with the steam chamber of condenser 3 of lower level, and of nozzles in the latter.
  • the water level appearing in the mixing condenser 3 of lower level is so much higher than the level of circulating pumps 5 that a quiet and bump-free operation of the latter is reliably ensured.
  • the cooling water is delivered by the pumps 5 through heat transmission elements 6, 7, 8 and 9 in which it is cooled down by atmospheric air flowing in the direction of arrows 18.
  • the cooled down cooling water flows in the direction of arrows illustrated in the drawing and arrives in a recuperation water turbine 10 and from here through the pipe conduit W again in the condenser 2 of higher level.
  • Feed water originating from steam which has been precipitated in the condensers 2 and 3 is fed back into not represented boilers through a pipe conduit 16, passing in its way feed water amount regulators not shown.
  • a pair of circulating water pumps 5 are shown which, in case of larger plants, are actually arranged in the illustrated manner. It is, however obvious that, from the point of view of connection diagram, the pair of smaller pumps 5 might be replaced by a single pump of higher performance so that the embodiment shown in FIG. 1 complies with the requirement that series connection of the condensers or condenser portions does not require more than one pump.
  • the pressures prefailing in the steam chambers of seriesly connected mixing condensers or condenser portions are influenced by the load of the steam turbine and the temperature of the cooling' water which depends, in turn, on whether conditions. Furthermore, the amount of water filling present in the system and the number of heat transmission surfaces disconnected due to mending or to other reasons may cause changes as well. In very huge plants, for reasons of security of operation, more than one circulating pumps will be employed in parallel connection as was the case with the plant shown in FIG. 1. Thus, it may occur that one of both pumps has to be mended and, therewhile, operation has to be kept going by means of a single pump though at circulating a decreased amount of water.
  • Reliable operation of the system according to the invention requires that the water levels in the mixing condensers 2 and 3 should stay within prescribed limits even under operational conditions changing in the above-described manner. Furthermore, it is required, that the amount of feed water necessary for operating the boilers be supplied without interruption. Another requirement is that upon connecting or disconnecting individual heat transmission surfaces changes of the water filling may be compensated. Finally, it is a requirement that the plant operate in the desired manner whether both circulating pumps 5 are working or only one of them is operated.
  • the basic idea of controlling the water levels in the seriesly connected condensers of the system is that the water level of the condenser 3 of lower level is kept constant whereas the water level in the condenser 2 of higher level is permitted to change. At the same time, the water receiving capacity of the condenser 3 of lower level is selected much greater than the water receiving capacity of the condenser 2 of higher level.
  • a control means 17 is provided for operating a pair of valves 12 and 13. Upon rising of the water level in mixing condenser 3 of lower level the valve 13 is opened whereas a sinking of the water level entails an opening of valve 12. Through valve 13 water may be discharged from the system into a receptacle 14 under atmospheric pressure.
  • Valve 12 permits to introduce water from the receptacle 14 into the vacuum space of the cooling system. Feed water the amount of which corresponds to the amount of dead steam is abducted through the pipe conduit 16 already mentioned. Control of the amount of the abducted feed water in dependence on the water level within the boilers is carried out by a regulator again not shown.
  • the water level in mixing condenser 2 of higher level is dependent on the flow resistance of the atomizing nozzles of mixing condenser 3 of lower level, on the pressure difference between the steam chambers and on the amount of water circulated through condensers 2 and 3.
  • a higher water level will be installed in mixing condenser 2 of higher level whereas, in the reversed case, the water level decreases therein.
  • mixing condenser 2 of higher level has a bot tom portion 2a of substantially reduced cross-sectional area. Fluctuations of the water level will take place within this bottom portion of reduced cross-sectional area.
  • the water chamber of mixing condenser 3 of lower level is suitable for receiving and storing a great amount of water so that surplus amounts of water introduced thereinto entail but small risings of water level.
  • control system responds as follows:
  • the amount of water circulated in the cooling system increases by 30 to 50 percent during a relatively short period of time of l to 2 sec. This surplus amount of water is sucked in by the pump 5 from the water chamber of condenser 3 of lower level.
  • the water level in the condenser 3 of lower level must not substantially decrease. It would be constant if, through the valve 12, a suitable amount of water could abruptly be introduced into the condenser 3 of lower level, or if simultaneously with starting of the second circulating pump 5, more water could flow thereinto through the water chamber 2a of the condenser 2 of higher level and the pipe conduit 4.
  • the first alternative is practically unfeasible because it would require very large valves and quick response.
  • the second alternative takes place only if the water level in the condenser 2 of higher level suddenly rises to a value which is necessary for having the surplus amount of water pressed through the atomizing nozzles of condenser 3 of lower level.
  • such quick rise of water level in condenser 2 of higher level may be obtained without permitting a substantial decrease of water level in condenser 3 of lower level. This is due to the volume of the water chamber 2a of condenser 2 of higher level being selected but to a fraction of the water chamber of condenser 3 of lower level.
  • a sudden and substantial water level rise in the water chamber 2a of condenser 2 of higher level may, according to the ratio of cross-sectional areas of the water chambers, be associated with water level decreases in condenser 3 of lower level which may be smaller even by orders of magnitude than the water level rise in the condenser 2 of higher level.
  • control system according to the invention is suitable to ensure a reliable operation even if the amount of water circulating in the water circuit of the system becomes suddenly changed.
  • the water chamber of condenser 3 of lower level has to be sized so as to deliver the maximum amount of water filling which may be required in operation of the plant without, however, undergoing a water level decrease greater than permitted.
  • the amount of water used for filling can then be made up for through the valve 12 at a speed which permits to select dimensions of the valve and the water conduits within reasonable and economical limits.
  • the valve 12 of relatively small dimensions will be opened by a feeler of the water level in condenser 3 of lower level whereupon an amount of water required for restoring the original water level therein will flow thereinto.
  • Control system for steam turbine powerplants having a cooling system consisting of a series connection of more than one mixing condenser wherein one of the mixing condensers is arranged at a higher level than the other, the cooling water introduced into the mixing condenser of higher level flowing from it into the mixing condenser of lower level under the acarranged at a higher level than the other, the cooling water introduced into the mixing condenser of higher level flowing from it into the mixing condenser of lower level under the action of hydrostatic pressure difference, and the mixing condenser of higher level having unitary water chamber located at the bottom thereof and forming a vertical downflow conduit having a cross-sectional area which is a fraction of the cross sectional area of the mixing condenser of lower level, and a water level control operated by a water level in the water chamber of the condenser of lower level, and arranged for introducing water from an exterior receptacle into the system upon decreasing of the water level in the condenser of lower level, and discharging water there

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
US750157A 1967-10-24 1968-08-05 Arrangement of mixing condensers for steam turbine powerplants Expired - Lifetime US3596888A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
HUHE000507 1967-10-24

Publications (1)

Publication Number Publication Date
US3596888A true US3596888A (en) 1971-08-03

Family

ID=10997020

Family Applications (1)

Application Number Title Priority Date Filing Date
US750157A Expired - Lifetime US3596888A (en) 1967-10-24 1968-08-05 Arrangement of mixing condensers for steam turbine powerplants

Country Status (7)

Country Link
US (1) US3596888A (de)
AT (1) AT284873B (de)
CH (1) CH475536A (de)
DE (1) DE1751724C3 (de)
FR (1) FR1589868A (de)
GB (1) GB1182900A (de)
SE (1) SE336586B (de)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4098854A (en) * 1976-01-23 1978-07-04 Gea Luftkuhlergesellschaft Happel Gmbh & Co. Kg Combined wet and dry liquid cooling system and method
US4353217A (en) * 1979-02-23 1982-10-12 Fuji Electric Co., Ltd. Direct contact type multi-stage steam condenser system
US6105368A (en) * 1999-01-13 2000-08-22 Abb Alstom Power Inc. Blowdown recovery system in a Kalina cycle power generation system
US20080006395A1 (en) * 2006-06-27 2008-01-10 Sanderlin Frank D Series-parallel condensing system
NL1036751C2 (nl) * 2009-03-23 2010-09-27 Kiremko Bv Inrichting en werkwijze voor het condenseren van periodiek vrijkomende hoeveelheden damp.
EP2610444A3 (de) * 2011-10-04 2014-07-16 Kabushiki Kaisha Toshiba Kondensator für Axialflussablassdampfturbine und geothermisches Kraftwerk damit
EP3473821A1 (de) * 2017-10-04 2019-04-24 Peter Thiessen Kraft-wärme-kopplungsanlage und verfahren zur regelung einer kraft-wärme-kopplungsanlage
WO2021092528A1 (en) * 2019-11-08 2021-05-14 University Of Pittsburgh - Of The Commonwealth System Of Higher Education Sensors with dehumidifiers

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5334242B2 (de) * 1971-08-06 1978-09-19
HU182479B (en) * 1978-10-31 1984-01-30 Energiagazdalkodasi Intezet Method and apparatus for increasing the capacity and/or energetics efficiency of pressure-intensifying stations of hydrocarbon pipelines
CN102538500B (zh) * 2012-03-09 2013-10-23 保定市伊莱克科技有限公司 降低发电厂空冷机组排汽压力的节能冷却方法及系统

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1542545A (en) * 1920-11-26 1925-06-16 William S Elliott Separation of air and dissolved gases from liquids
DE728512C (de) * 1939-04-30 1942-11-27 Caliqua Waermegesellschaft M B Verfahren und Vorrichtung zum Aufrechterhalten eines UEberschusses von Salzloesungen in den Heizungsnetz von Heisswasserheizungen
US3158666A (en) * 1961-09-11 1964-11-24 Licencia Talalmanyokat Heavy-duty mixing condenser
US3391911A (en) * 1963-05-04 1968-07-09 Komplex Nagyberendezesek Expor Mixing condensers
US3511481A (en) * 1966-08-24 1970-05-12 English Electric Co Ltd Turbine plant

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE165981C (de) *

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1542545A (en) * 1920-11-26 1925-06-16 William S Elliott Separation of air and dissolved gases from liquids
DE728512C (de) * 1939-04-30 1942-11-27 Caliqua Waermegesellschaft M B Verfahren und Vorrichtung zum Aufrechterhalten eines UEberschusses von Salzloesungen in den Heizungsnetz von Heisswasserheizungen
US3158666A (en) * 1961-09-11 1964-11-24 Licencia Talalmanyokat Heavy-duty mixing condenser
US3391911A (en) * 1963-05-04 1968-07-09 Komplex Nagyberendezesek Expor Mixing condensers
US3511481A (en) * 1966-08-24 1970-05-12 English Electric Co Ltd Turbine plant

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4098854A (en) * 1976-01-23 1978-07-04 Gea Luftkuhlergesellschaft Happel Gmbh & Co. Kg Combined wet and dry liquid cooling system and method
US4353217A (en) * 1979-02-23 1982-10-12 Fuji Electric Co., Ltd. Direct contact type multi-stage steam condenser system
US6105368A (en) * 1999-01-13 2000-08-22 Abb Alstom Power Inc. Blowdown recovery system in a Kalina cycle power generation system
US20080006395A1 (en) * 2006-06-27 2008-01-10 Sanderlin Frank D Series-parallel condensing system
US7926555B2 (en) 2006-06-27 2011-04-19 Gea Power Cooling, Inc. Series-parallel condensing system
NL1036751C2 (nl) * 2009-03-23 2010-09-27 Kiremko Bv Inrichting en werkwijze voor het condenseren van periodiek vrijkomende hoeveelheden damp.
EP2610444A3 (de) * 2011-10-04 2014-07-16 Kabushiki Kaisha Toshiba Kondensator für Axialflussablassdampfturbine und geothermisches Kraftwerk damit
EP3473821A1 (de) * 2017-10-04 2019-04-24 Peter Thiessen Kraft-wärme-kopplungsanlage und verfahren zur regelung einer kraft-wärme-kopplungsanlage
WO2021092528A1 (en) * 2019-11-08 2021-05-14 University Of Pittsburgh - Of The Commonwealth System Of Higher Education Sensors with dehumidifiers
US12203830B2 (en) 2019-11-08 2025-01-21 University Of Pittsburgh Of The Commonwealth System Of Higher Education Sensors with dehumidifiers

Also Published As

Publication number Publication date
DE1751724B2 (de) 1972-07-13
GB1182900A (en) 1970-03-04
AT284873B (de) 1970-10-12
DE1751724A1 (de) 1970-12-03
SE336586B (de) 1971-07-12
DE1751724C3 (de) 1973-02-08
FR1589868A (de) 1970-04-06
CH475536A (de) 1969-07-15

Similar Documents

Publication Publication Date Title
US2172910A (en) Power plant
US4361009A (en) Moving bed heat storage and recovery system
US3908381A (en) Geothermal energy conversion system for maximum energy extraction
EP0241049B1 (de) Zweidruckturbine
US4041710A (en) Hydraulic prime mover device
US4479353A (en) Moving bed heat storage and recovery system
US4353217A (en) Direct contact type multi-stage steam condenser system
US4979374A (en) Geothermal heat- and water supply plant
US3413805A (en) Method of and apparatus for controlling plural fluid medium thermal power plants
US3726101A (en) Method of continuously vaporizing and superheating liquefied cryogenic fluid
US3259177A (en) Liquid cooler and control therefor
US3304712A (en) Steam and gas turbine power plant
US3292372A (en) Steam power generating plant
US4608945A (en) Apparatus for recirculating boiler fluid
US4325328A (en) Vapor generator having a pair of combustion chambers
US3061276A (en) River water temperature control system
US2823650A (en) Method and means for heat exchange between flowing media, preferably for remote heating systems
US3237413A (en) Steam power plants
US5045272A (en) Fluid temperature balancing system
US3205869A (en) Cooling parts of a steam generator by feedwater
US2239886A (en) Power plant refrigerating system
US2887308A (en) Self-regulating circulating and cooling system
US3314237A (en) Startup system for a once-through steam generator
CN211273584U (zh) 一种用于硫酸生产的低温回收蒸发器系统
US4279126A (en) Method of utilizing residual heat in the production of cellulose and an installation for carrying out the method