EP2585685A2 - Turbine à vapeur et système générateur de vapeur, et fonctionnement associé - Google Patents

Turbine à vapeur et système générateur de vapeur, et fonctionnement associé

Info

Publication number
EP2585685A2
EP2585685A2 EP11728924.9A EP11728924A EP2585685A2 EP 2585685 A2 EP2585685 A2 EP 2585685A2 EP 11728924 A EP11728924 A EP 11728924A EP 2585685 A2 EP2585685 A2 EP 2585685A2
Authority
EP
European Patent Office
Prior art keywords
steam
pressure turbine
turbine
low pressure
accordance
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.)
Withdrawn
Application number
EP11728924.9A
Other languages
German (de)
English (en)
Inventor
Pramurtta Shourjya Majumdar
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.)
Altrad Babcock Ltd
Original Assignee
Doosan Power Systems 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 Doosan Power Systems Ltd filed Critical Doosan Power Systems Ltd
Publication of EP2585685A2 publication Critical patent/EP2585685A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
    • F01K17/02—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
    • F01K17/04—Using steam or condensate extracted or exhausted from steam engine plant for specific purposes other than heating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K19/00—Regenerating or otherwise treating steam exhausted from steam engine plant
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K21/00—Steam engine plants not otherwise provided for
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/32—Direct CO2 mitigation

Definitions

  • the invention relates to a steam turbine system and a steam generator system and to the optimum operation thereof in particular together with a post combustion carbon capture plant.
  • Post-combustion carbon capture is a means of mitigating the effects of fossil fuel combustion emissions by capturing CO2 from large sources of emission such as thermal power plants which use fossil fuel combustion as the power source.
  • the CO2 is not vented to atmosphere but is removed from flue gases by a suitable absorber and stored away from the atmosphere.
  • Other industrial processes where similar principles might be applicable to capture post-process CO2 might include removal of CO2 generated in a process cycle, for example removal of CO2 from the process flow during production of ammonia, removal of CO2 from a natural gas supply etc.
  • CO2 can be separated from a gas phase, for example being the flue gas of a thermal power plant, by means of absorption by suitable absorption medium, for example absorbent in liquid phase, typically in aqueous solution.
  • suitable absorption medium for example absorbent in liquid phase, typically in aqueous solution.
  • Gas is passed through the absorption medium under conditions of pressure and temperature optimised for removal of substantially all the carbon dioxide.
  • the purified gas is then directed for further processing as necessary.
  • the absorption medium rich in CO2 is subjected to a stripping process to remove the CO2 and regenerate the absorption medium. Typically this process involves regenerative heating of the medium.
  • the CO 2 rich medium is maintained at high temperature, which may be at or near boiling point of an absorbent liquid phase under pressure. The heat necessary is typically obtained when the system is used in association with a thermal power plant by supplying steam from the LP turbine system. At higher temperatures the medium will release the absorbed CO 2 .
  • Regenerated medium may be drawn off for reuse.
  • the released CO 2 inay then be collected for example for sequestration.
  • the condensate product of the steam used to supply regenerative heat is returned to the steam generation system.
  • Steam is diverted from upstream of the LP turbine, for example, in the case where the system comprises HP, IP and LP turbines or turbine sets with combined HP/IP modules, from the vicinity of the IP/ LP crossover.
  • the diverting of steam away from the LP turbine for carbon capture moves the regime of operation along the left of the exhaust loss curve. This can be seen with reference to the example exhaust loss curve of figure 1 . If this point of operation moves to the left of the minimum point (A) in Figure 1 , then exhaust loss increases tremendously, causing substantial loss of power generation.
  • a steam turbine system comprising fluidly in series: at least one high pressure turbine; and/ or
  • At least one low pressure turbine At least one low pressure turbine
  • At least one flow restrictor in a steam extraction conduit from the or each low pressure turbine to allow the variation of mass flows therefrom by suitable modification of pressures.
  • the invention draws process steam from a location upstream of the low pressure turbine, being a location between a low pressure turbine or turbine set and a higher pressure turbine or set upstream thereof and preferably first upstream thereof, being an intermediate pressure turbine or set where present.
  • the steam turbine system comprises fluidly in series at least one high pressure turbine, at least one intermediate pressure turbine, and at least one low pressure turbine and process steam is drawn from a location between the intermediate pressure turbine and the low pressure turbine and for example at or about the IP/LP crossover.
  • the steam outlet means in the preferred case are located to enable extraction of auxiliary process steam from a location in the vicinity of the IP/LP crossover.
  • the invention is distinctly characterised by the provision of flow restrictors in the LP Turbine Extraction which allows the variation of mass flows by suitable modification of pressures thereby moving the flow regime to the right of the exhaust loss curve, simultaneously providing the operator the means of responding to planned load changes and various unanticipated modes of power plant operation involving transients, frequency support etc. This promotes stability of operation by moving the flow regime of LP Turbine along the right of Exhaust Loss Curve.
  • Process steam is drawn off to supply additional process module(s) with a source of motive power and/ or latent heat.
  • the steam generator conveniently further comprises a fluid conduit fluidly continuous with the steam outlet means to convey auxiliary process steam to such additional process module(s).
  • the steam turbine system in particular comprises a generator for generation of steam from combustion of carbonaceous fuel, for example in a thermal power plant, and is preferably adapted for use with an associated means for post-combustion carbon capture. In this preferred case, process steam is drawn off to supply
  • the steam turbine system conveniently further comprises a fluid conduit fluidly continuous with the steam outlet means to convey auxiliary process steam to an associated post combustion carbon capture plant.
  • a steam generator system with post-combustion carbon capture capability comprises:
  • a steam generator adapted in use to produce steam in use using thermal energy from combustion of carbonaceous fuel
  • At least one high pressure turbine at least one high pressure turbine; and/or
  • At least one low pressure turbine at least one low pressure turbine; and further comprising steam outlet means to enable extraction of auxiliary process steam from a location upstream of the low pressure turbine and for example between the intermediate pressure turbine and the low pressure turbine;
  • a post-combustion carbon capture apparatus fluidly disposed to recover CO 2 from combustion gases generated by the combustion of
  • a fluid conduit fluidly continuous with the steam outlet means to convey auxiliary process steam to the post-combustion carbon capture apparatus.
  • the steam generator system with post-combustion carbon capture capability conveniently comprises a steam turbine system in accordance with the first aspect of the invention in combination with a steam generator adapted in use to produce steam in use using thermal energy from combustion of
  • Process steam is drawn off to supply the associated post combustion carbon capture plant with a source of motive power and/ or latent heat.
  • process steam is drawn off to regenerate lean absorbent in a post-combustion carbon capture apparatus using absorbent medium such as absorbent solution, for example to supply latent heat to a re-boiler for lean solvent regeneration.
  • absorbent medium such as absorbent solution
  • Other supplies of auxiliary process steam may be made available for example to the steam turbine auxiliary drive, and to the reclaimer for maintaining solver properties.
  • the post-combustion carbon capture plant may for example comprise an absorber column where CO2 is separated from the flue gas by means of absorption by passing the gas through a column where the gas flows in an opposite direction to an absorbent in liquid phase, typically in aqueous solution.
  • the post-combustion carbon capture plant may for example further comprise a regeneration column where CO2 is removed from absorbent by regenerative heating, for example to at or near boiling point of an absorbent liquid phase under pressure.
  • a suitable heating means is for example a condenser reboiler as is familiar. Again, as is familiar, this condenser reboiler may be disposed to receive solution that has passed through a process volume, for example via an outlet towards the bottom of a column, and reboil the solution to regenerate lean absorbent.
  • Any suitable flow restrictor can be incorporated into the LP steam extraction conduit provided that it can be modulated to maintain the necessary pressure control.
  • the flow restrictor is for example a valve.
  • the flow restrictor may for example be selected from: a control valve, a globe valve with a suitably shaped and actuated plug, a butterfly valve with a suitably shaped and actuated disk, a non-return valve with a suitably shaped and actuated restriction.
  • the invention may comprise a method of modification of a steam generator, in particular a generator for generation of steam from combustion of carbonaceous fuel, for example in a thermal power plant, comprising at least one high pressure turbine and/ or at least one intermediate pressure turbine, and at least one low pressure turbine; and for example adapted for use with an associated post-combustion carbon capture system.
  • the method comprises the steps of:
  • the method comprises in a first step providing steam outlet means to enable extraction of process steam from a location upstream of the at least one low pressure turbine, being a location between a low pressure turbine or turbine set and a higher pressure turbine or set.
  • the steam generator comprises at least one high pressure turbine and at least one intermediate pressure turbine and at least one low pressure turbine and the method comprises in a first step providing steam outlet means to enable extraction of process steam from a location between the at least one intermediate pressure turbine and the at least one low pressure turbine for example in the vicinity of the IP/ LP crossover.
  • This aspect of the invention may comprise the two steps performed separately, or may comprise the second step performed subsequently on a steam generator already modified by the first step.
  • the method is suitable for both green field projects and retro-fitting on a brown field project. Substantial parts of existing plants can be left untouched with no necessity for modification.
  • the second aspect of the invention comprises a method of after-market modification of existing plant in situ by performance of the second foregoing step independently or of both the foregoing steps.
  • a method of operation of a steam turbine system of a steam generator having at least one high pressure turbine and/ or at least one intermediate pressure turbine and at least one low pressure turbine; and for example adapted for use with an associated post-combustion carbon capture system; the method comprising:
  • the second step is performed dynamically and simultaneously with the first to promote stability of operation by moving the flow regime of LP Turbine right along the Exhaust Loss Curve.
  • the second step may be performed by operation of a suitable flow restrictor such as a control valve in the LP turbine steam extraction conduit.
  • the method comprises drawing off auxiliary process steam from a location upstream of the at least one low pressure turbine, being a location between a low pressure turbine or turbine set and a higher pressure turbine or set.
  • the steam generator comprises at least one high pressure turbine and at least one intermediate pressure turbine and at least one low pressure turbine
  • the method comprises drawing off auxiliary process steam from a location between the at least one intermediate pressure turbine and the at least one low pressure turbine for example in the vicinity of the IP/ LP crossover.
  • auxiliary process steam is drawn to supply a post combustion carbon capture plant with a source of motive power and/ or latent heat.
  • the method is a method of operation of a steam turbine power plant having a post-combustion carbon capture plant which uses steam from the power plant for auxiliary purposes and for example as a latent heat source for regeneration of absorbent, and the method comprises circulating the process steam for such a purpose.
  • Figure 1 a typical exhaust loss curve for a typical LP turbine
  • FIG. 2 is a general schematic of a prior art steam generator with PCC apparatus with unregulated LP steam extraction
  • Figure 3 is a schematic showing the introduction of control valves to regulate mass flow in steam extraction from the LP turbines of a typical steam generator in accordance with the principles of the invention.
  • Figure 1 is a general schematic of a thermal power plant with HP, IP and LP turbine systems, and with a PCC system for capture of CO2 from the combustion flue gases supplied by process steam from the IP/ LP crossover of the steam generation system.
  • a PCC system for capture of CO2 from the combustion flue gases supplied by process steam from the IP/ LP crossover of the steam generation system.
  • Figure 1 describes the typical family of exhaust loss curves of a family of Low Pressure Steam Turbines, involving increasing heights of Last Stage Blades (LSB's); as moving from left to right.
  • LLB's Last Stage Blades
  • the preferred regime of operation is to the right of the minimum point ("A") for any particular family of Low Pressure Turbine.
  • the diverting of steam away from the LP turbine for carbon capture moves the regime of operation along the left of the exhaust loss curve. If this point of operation moves to the left of the minimum point (A) in Figure 2, then exhaust loss increases tremendously, causing substantial loss of power generation.
  • Figure 2 is an example of a prior art system with uncontrolled extraction lines from LP turbines and with steam extraction for PCC.
  • a steam generator comprises at least one high pressure turbine and/ or at least one intermediate pressure turbine and at least one low pressure turbine. Two are shown.
  • the diagram in figure 2 shows elements downstream of the HP/ IP sets.
  • the arrangement of the HP/ IP sets and other elements of the system will be familiar to those skilled in the art and the invention is not specific to any such arrangement.
  • the arrangement includes steam extraction to supply a post combustion carbon capture plant (PCC).
  • PCC post combustion carbon capture plant
  • a similar steam generator comprises again at least one high pressure turbine and/ or at least one intermediate pressure turbine and at least one low pressure turbine. Two are shown. The figure again shows elements downstream of the HP/ IP sets but the remaining arrangement will be familiar.
  • the embodiment is modified by provision of flow restrictors (in the example the control valves 25a, 25b) incorporated into the LP turbine extraction lines.
  • the figure shows an optimum location of the control valves in the LP turbine extraction lines, which allow the control of pressures and thereby mass flows within the LP turbines thereby enabling the flow regime to move towards the right of the Exhaust Flow Curve when steam is tapped from the IP/LP Crossover for example for carbon capture such as in the example system of figure 1 .
  • This method promotes stability of operation by moving the flow regime of LP Turbine along the right of Exhaust Loss Curve.
  • This method Compensates against loss of power incurred for diverting steam to PCC. This method provides operational flexibility of determining optimum regime vis-a-vis power, heat rate and carbon capture.

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)
  • Treating Waste Gases (AREA)

Abstract

La présente invention se rapporte à un système de turbine à vapeur qui comprend, reliées en série et de manière fluide : au moins une turbine haute pression et/ou au moins une turbine de pression intermédiaire et au moins une turbine basse pression ; le système comprend en outre un moyen de sortie de vapeur pour permettre l'extraction de la vapeur auxiliaire du processus à partir d'un emplacement situé en amont de la turbine basse pression et, par exemple, entre la turbine à pression intermédiaire et la turbine basse pression ; et au moins un dispositif de limitation de débit dans une conduite d'extraction de vapeur partant de la turbine basse pression ou de chaque turbine basse pression. Le système fait partie d'un générateur de vapeur alimenté par la combustion de combustibles carbonés ayant une capacité de capture post-combustion du carbone.
EP11728924.9A 2010-06-28 2011-06-23 Turbine à vapeur et système générateur de vapeur, et fonctionnement associé Withdrawn EP2585685A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB1010760.5A GB201010760D0 (en) 2010-06-28 2010-06-28 Operation of steam turbine and steam generator apparatus with post-combustion carbon capture
PCT/GB2011/051175 WO2012001391A2 (fr) 2010-06-28 2011-06-23 Turbine à vapeur et système générateur de vapeur, et fonctionnement associé

Publications (1)

Publication Number Publication Date
EP2585685A2 true EP2585685A2 (fr) 2013-05-01

Family

ID=42583031

Family Applications (1)

Application Number Title Priority Date Filing Date
EP11728924.9A Withdrawn EP2585685A2 (fr) 2010-06-28 2011-06-23 Turbine à vapeur et système générateur de vapeur, et fonctionnement associé

Country Status (6)

Country Link
US (1) US20130205781A1 (fr)
EP (1) EP2585685A2 (fr)
KR (1) KR20130086158A (fr)
CA (1) CA2801037A1 (fr)
GB (1) GB201010760D0 (fr)
WO (1) WO2012001391A2 (fr)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB201106410D0 (en) * 2011-04-15 2011-06-01 Doosan Power Systems Ltd Turbine system
US9617874B2 (en) * 2013-06-17 2017-04-11 General Electric Technology Gmbh Steam power plant turbine and control method for operating at low load
CN105134317B (zh) * 2015-08-22 2018-05-01 广州市旺隆热电有限公司 一种环保发电系统及其电网运行方法
CN112377279A (zh) * 2020-09-30 2021-02-19 广西电网有限责任公司电力科学研究院 一种适于蝶阀控制抽汽压力的热电联产机组监控系统

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JP4875303B2 (ja) * 2005-02-07 2012-02-15 三菱重工業株式会社 二酸化炭素回収システム、これを用いた発電システムおよびこれら方法
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EP2136037A3 (fr) * 2008-06-20 2011-01-05 Siemens Aktiengesellschaft Procédé et dispositif d'exploitation d'une centrale à vapeur dotée d'une turbine à vapeur et d'un utilisateur
US20100205964A1 (en) * 2009-02-13 2010-08-19 General Electric Company Post-combustion processing in power plants
JP5317833B2 (ja) * 2009-05-28 2013-10-16 株式会社東芝 蒸気タービン発電設備
EP2290200A1 (fr) * 2009-07-15 2011-03-02 Siemens Aktiengesellschaft Installation de centrale à vapeur dotée d'une unité de turbine à vapeur et récepteur de vapeur de traitement ainsi que procédé de fonctionnement d'une installation de centrale à vapeur dotée d'une unité de turbine à vapeur et récepteur de vapeur de traitement
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EP2333256B1 (fr) * 2009-12-08 2013-10-16 Alstom Technology Ltd Centrale électrique dotée de capture de CO2 et son procédé d'opération
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JP5558310B2 (ja) * 2010-10-22 2014-07-23 株式会社東芝 二酸化炭素回収方法及び二酸化炭素回収型汽力発電システム
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Also Published As

Publication number Publication date
CA2801037A1 (fr) 2012-01-05
WO2012001391A3 (fr) 2012-10-04
WO2012001391A2 (fr) 2012-01-05
US20130205781A1 (en) 2013-08-15
GB201010760D0 (en) 2010-08-11
KR20130086158A (ko) 2013-07-31

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