EP2307121A1 - Procédé et dispositif pour séparer le dioxyde de carbone d'un gaz d'échappement rejeté par une centrale électrique fonctionnant aux énergies fossiles - Google Patents

Procédé et dispositif pour séparer le dioxyde de carbone d'un gaz d'échappement rejeté par une centrale électrique fonctionnant aux énergies fossiles

Info

Publication number
EP2307121A1
EP2307121A1 EP09797441A EP09797441A EP2307121A1 EP 2307121 A1 EP2307121 A1 EP 2307121A1 EP 09797441 A EP09797441 A EP 09797441A EP 09797441 A EP09797441 A EP 09797441A EP 2307121 A1 EP2307121 A1 EP 2307121A1
Authority
EP
European Patent Office
Prior art keywords
steam
carbon dioxide
absorption medium
power plant
desorption
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Withdrawn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
EP09797441A
Other languages
German (de)
English (en)
Inventor
Ralph Joh
Rüdiger Schneider
Henning Schramm
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.)
Siemens AG
Original Assignee
Siemens AG
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 Siemens AG filed Critical Siemens AG
Priority to EP09797441A priority Critical patent/EP2307121A1/fr
Publication of EP2307121A1 publication Critical patent/EP2307121A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1425—Regeneration of liquid absorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456—Removing acid components
    • B01D53/1475—Removing carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00—Component parts or details of steam boilers
    • F22B37/008—Adaptations for flue gas purification in steam generators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/006—Layout of treatment plant
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/20—Sulfur; Compounds thereof
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2215/00—Preventing emissions
    • F23J2215/50—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2219/00—Treatment devices
    • F23J2219/40—Sorption with wet devices, e.g. scrubbers
    • 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
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • 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
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2
    • 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 method for operating a fossil-fired power plant and in particular a method for separating carbon dioxide from an exhaust gas of a fossil-fired power plant.
  • the invention also relates to a fossil-fired power plant with a separator for separating carbon dioxide from an exhaust gas.
  • a carbon dioxide-containing exhaust gas is produced to a great extent by the combustion of a fossil fuel.
  • the exhaust gas contains other ingredients such as e.g. the gases nitrogen, sulfur dioxide, nitrogen oxides and water vapor as well as solid particles, dusts and soot.
  • the newer or modernized power plant already uses the separation of solid components, the separation of sulfur oxides and the catalytic removal of nitrogen oxides.
  • the carbon dioxide contained in the exhaust gas is discharged so far with the exhaust gas into the atmosphere.
  • the carbon dioxide accumulating in the atmosphere impedes the heat radiation of our earth and favors by the so-called greenhouse effect an increase of the earth's surface temperature.
  • carbon dioxide can be separated from the exhaust gas.
  • the separation of carbon dioxide by the absorption-desorption process is carried out with a detergent.
  • a classical absorption-desorption process the exhaust gas in an absorption column is brought into contact with a selective solvent as a detergent.
  • the absorption of carbon dioxide takes place by a chemical or physical process.
  • the purified exhaust gas leaves the absorption column for further processing or discharge.
  • the loaded with carbon dioxide solvent is passed to separate the carbon dioxide and regeneration of the solvent in a desorption column.
  • the separation in the desorption column can be effected thermally.
  • a gas-vapor mixture of gaseous carbon dioxide and vaporized solvent is expelled from the charged solvent.
  • the evaporated solvent is then separated from the gaseous carbon dioxide.
  • the carbon dioxide can now be compressed, cooled and liquefied in several stages. In liquid or frozen state, the carbon dioxide can then be sent for storage or further use.
  • the regenerated solvent is returned to the absorber column, where it can again absorb carbon dioxide from the carbon dioxide-containing exhaust gas.
  • the main problem with the existing methods for separating carbon dioxide from a gas mixture on an industrial scale is, in particular, the very high expenditure of energy required, inter alia, in the form of heating energy for desorption.
  • a general disadvantage of known separation processes for carbon dioxide from an exhaust gas, which are connected in or after a power plant process is in particular the significant efficiency-reducing influence of the separation processes on the power plant process. The deterioration of the efficiency occurs because the energy has to be taken to carry out the carbon dioxide separation from the power plant process.
  • the economy of a fossil-fired power plant with carbon dioxide separation device is therefore significantly lower than without carbon dioxide separation device.
  • An object of the invention is to propose a method for separating carbon dioxide from an exhaust gas of a fossil-fueled power plant, which enables a high separation efficiency with at the same time favorable overall system efficiency of the power plant process.
  • a further object of the invention is to propose a fossil-fueled power plant with integrated precipitation device for carbon dioxide, which makes possible a high separation efficiency with at the same time favorable overall efficiency of the power plant.
  • the object directed to a method is achieved according to the invention with a method for separating carbon dioxide from an exhaust gas of a fossil-fired power plant, in which a fossil fuel is burned in a combustion process, whereby a hot, carbon dioxide-containing exhaust gas is generated, in which an absorption process carbon dioxide-containing exhaust gas is brought into contact with an absorption medium, wherein carbon dioxide is taken up by the absorption medium, whereby a laden absorption medium is formed, in which, in a desorption process, the carbon dioxide is thermally expelled, and a vapor is supplied, which is injected into the loaded absorption medium, wherein the heat of condensation released by the condensation of the vapor is transferred to the charged absorption medium.
  • the invention is based on the consideration that the heat of condensation introduced directly into the loaded absorption medium contributes significantly to the thermal expulsion of the carbon dioxide.
  • the steam is introduced into the desorption process.
  • the heater is relieved in the desorption process.
  • the vapor is condensed within the column, whereby the heat of condensation is transferred directly to the loaded absorption medium. Therefore, low temperature steam can be used because there are no losses due to heat transfer, e.g. in an indirect heat transfer in a heat exchanger process.
  • the desorption process by the method according to the invention is further promoted to the effect that the partial pressure of the already outgassed carbon dioxide is lowered.
  • less absorption medium has to be evaporated, as a result of which less heat has to be introduced by the heating device into the desorption process.
  • the heater is also operated with steam, thereby reducing the steam consumption. The steam saved is therefore available to the power plant process and can contribute to increasing the overall efficiency.
  • the method only a part of the heat energy required for the thermal expulsion of the carbon dioxide from the loaded absorption medium is introduced by the method. Another part of the required heat energy is introduced into the desorption process by the heating device, and primarily indirectly via a heat exchanger process.
  • the energy required to expel carbon dioxide from the laden absorption medium can be significantly reduced. The energy saved is therefore available to the power plant process, which significantly increases the efficiency of the power plant.
  • the method for separating carbon dioxide from an exhaust gas of a fossil-fired power plant thus allows a substantially more efficient operation by increasing the overall efficiency of the power plant. This is achieved by saving energy for operating the desorption process.
  • the invention also allows the subsequent installation of a carbon dioxide precipitator while meeting economic conditions.
  • the quantity of absorption medium which is removed from the absorption medium cycle by the absorption / desorption process is compensated for by the injected steam quantity. This is possible because water is introduced by the condensation of the steam in the desorption process. Since the absorption media used are generally water-soluble, and losses of absorption medium by evaporation occur in any case as a result of the process, absorbent water losses in the absorber-desorber cycle are compensated for by the introduced water. In conventional processes, makeup water flow is present to compensate for absorbent losses. By applying the method according to the invention this can be saved.
  • the supplied steam is injected into the desorption process at several points. This achieves a uniform distribution within the desorption process.
  • the steam for the injection into the loaded absorption medium is preferably taken from the steam-condensate cycle of the power plant process preceding the separation process. This is possible because a lower temperature vapor can be used for injection into the loaded absorption medium. Such a steam is about 100 and 120 0 C hot. However, heating of the heating process generally requires higher temperature steam because heat is lost through indirect heat transfer with a heat exchanger. By contrast, this higher-energy steam is generally taken, for example, from the overflow line to the low-pressure part of a steam turbine. This steam has temperatures of about 120 to 160 0 C. Depending on the operating mode of the power plant process or taking into account other parameters in the power plant process, the steam is advantageously taken from a steam generation process that is not coupled to the power generation process of the power plant.
  • This steam source can be a steam generation process, for example, which is provided specifically for the deposition process, or another steam source which is otherwise permanently provided, for example, for the provision of process steam or heating steam.
  • the supplied steam is injected into the loaded absorption medium.
  • Another part of the supplied steam is conducted with the loaded absorption medium in heat exchange.
  • the steam provided for the desorption process is divided into two parallel steam streams. The distribution of the two steam flows is regulated by a control process.
  • the supplied steam is first passed through the heat exchanger with the laden absorption medium, and then a portion of the steam is injected into the loaded absorption medium. This is advantageous if, in any case, a high-temperature steam is available for operating the separation process.
  • the steam is reduced by the heat exchange with the loaded absorption medium in the heat content and then injected, at least in part, in the desorption process.
  • the object directed to a fossil-fired power plant is achieved according to the invention by means of a separating device arranged downstream of a combustion device, for Depositing carbon dioxide from the carbon dioxide-containing waste gas, wherein the separation device comprises an absorption unit for receiving gaseous carbon dioxide and a desorption unit for the release of gaseous carbon dioxide, wherein the desorption unit has a steam injection device which is connected to a steam line, so that During operation of the separator, steam can be injected into the desorption unit.
  • the invention is based on the idea that a steam can be injected directly into the desorption unit through the injection device, wherein the vapor condenses in the desorption unit and releases heat of condensation, so that the release of carbon dioxide thermally from a carbon dioxide-laden absorption medium is brought about by the introduced condensation heat is expelled.
  • the injection device comprises a steam line which passes through the desorption unit and is preferably of annular design.
  • the arrangement of several annular lines at different heights within the desorption is possible.
  • the injection device is arranged in the lower region of the desorption unit.
  • the desorption unit comprises a column aligned along a vertical axis.
  • the column has an inlet in the upper area and an outlet in the lower area.
  • loaded absorption medium can thus be introduced in the upper region and a regenerated absorption medium can be diverted in the lower region, whereby a flow through the desorption unit with laden absorption medium is effected.
  • the expulsion of carbon dioxide from an absorption medium takes place doing primarily thermally, as this can be used on provided in the power plant heat energy.
  • the desorption unit may also have several columns. Such columns are also known in the chemical industry as columns and serve to separate mixtures by thermal processes. This is done using equilibrium states between different phases.
  • a carbon dioxide-loaded absorption medium is in the liquid phase.
  • the loaded absorption medium is heated.
  • the lower part of the desorption unit is also referred to as a sump.
  • An arrangement of the nozzle arrangement possible lest close to the sump has an advantageous effect on injection of a vapor to the partial pressure of the already dissolved carbon dioxide.
  • the achievable reduction in the partial pressure means a reduction in the concentration of carbon dioxide in the gas phase, whereby the expulsion of the bound in the loaded absorption medium carbon dioxide is favored. This requires less energy to heat the heater. If a heating device which can be heated by steam is used, the amount of steam saved in the power plant makes it possible to generate electrical energy, thereby increasing the overall efficiency of the power plant.
  • the injection device comprises a nozzle arrangement, which in turn has a number of nozzle heads.
  • a number of nozzle heads are distributed over the nozzle arrangement, so that a steam which can be introduced through the nozzles can be introduced uniformly into the desorption unit.
  • the nozzle heads are preferably in Strömungsrich- tion of the loaded absorption medium aligned. This prevents undesired flows and ensures the targeted injection of a vapor into the desorption unit, which preferably takes place uniformly.
  • the injection device is connected via the steam line to the tapping point of an overflow line or a steam condensate line of a steam turbine plant.
  • the selection of the steam extraction point to which the injector is connected via the steam line is defined as a function of the required and available steam parameters.
  • a vapor intended for injection into the desorption unit must have parameters (pressure and temperature) above the condensation point.
  • the steam is taken from the steam condensate line connecting the low pressure stage of the steam turbine to the condenser.
  • the steam conducted in the steam condensate line has temperatures of approximately 100 to 120 ° C.
  • the desorption unit comprises a heating device which can be heated by steam, which is connected to the injection device via a steam line, so that steam can be conducted from the heating device to the injection device and injected into the desorption unit.
  • This arrangement requires the use of a higher temperature steam, which is preferably removable from the overflow line between the middle and low pressure parts of a steam turbine.
  • This steam first operates the heater by the steam is conducted with the loaded absorption medium in heat exchange. This reduces the temperature of the steam. Through the steam line which connects the heating device to the injection device, this lower temperature steam is now the input nozzle device feedable, and can be injected via the injection device in the desorption.
  • FIG. 2 shows an embodiment of a fossil-fired power plant with steam turbine plant and carbon dioxide separation device
  • FIG 3 shows an embodiment of a fossil-fired power plant with gas and steam turbine plant and carbon dioxide separation device
  • FIG. 1 shows an exemplary embodiment of a carbon dioxide separation method and, in particular, the injection of steam 9 into the desorption process 7.
  • the method essentially comprises a combustion process 1, an absorption process 4 and a desorption process 7.
  • a carbon dioxide-containing exhaust gas 3 is generated, which is to be freed of carbon dioxide by the carbon dioxide separation process.
  • the carbon dioxide-containing exhaust gas 3 is supplied to the absorption process 4.
  • the absorption process moreover, an absorption medium 5 is supplied.
  • the carbon dioxide-containing exhaust gas 3 comes into contact with the absorption medium 5, whereby carbon dioxide from the absorption medium 5 is received, and a laden absorption medium 6 and a largely free of carbon dioxide exhaust gas is formed.
  • the loaded absorption medium 6 is guided into the desorption process 7, where it is regenerated.
  • a vapor 9 is now injected into the desorption process. This steam condenses to water and releases heat of condensation. This condensation heat supports the regeneration process.
  • a regenerated absorption medium 11 and a gas / vapor mixture of gaseous carbon dioxide 8 and vaporous absorption medium are formed.
  • the gas-vapor mixture is separated by a separation process into condensed absorption medium and gaseous carbon dioxide 8. Not shown is the return of the condensed absorption medium in the circulation of absorption medium 5.
  • the gaseous carbon dioxide 8 can now be fed to a compressor process, where it is liquefied for further processing or transportation.
  • FIG 2 an embodiment of a fossil-fired power plant 14, comprising a steam turbine plant 25 and separator 16 is shown for carbon dioxide.
  • the steam turbine plant 15 is preceded by a combustion device 15.
  • the combustion device 15 comprises a fired boiler 27, to which a fossil fuel can be fed via a fuel feed line 46.
  • the feedable fuel is combusted to produce a carbon dioxide-containing exhaust gas 3 and a vapor.
  • the fired boiler 27 is connected via a steam line 40 to a steam turbine 29 of the steam turbine system 25.
  • the steam turbine 29 can be driven by the supplied steam.
  • the steam turbine 29 drives again via a shaft to a generator 30 for power generation.
  • the steam leaving the steam turbine 29 is supplied to the condenser 37 via a line.
  • the condenser 37 is connected to the fired boiler 27 again via a steam condensate line 24 for the return of a condensed steam.
  • a condensate pump 28 is connected in the steam condensate line 24.
  • the carbon dioxide-containing exhaust gas 3 leaves the fired boiler and can be fed via a flue gas line 39 to the absorption unit 17 comprising the precipitator 16.
  • a flue gas cleaning system 31 a flue gas cooler 32 and a blower 33 are connected.
  • the flue gas cleaning system 31 may be e.g. a desulphurisation system or other systems for purifying the flue gas.
  • the flue gas cooler 32 Through the flue gas cooler 32, the carbon dioxide-containing exhaust gas 3 heat is removed.
  • the need for flue gas cooling is dependent on the required temperature level in the absorption unit.
  • the flue gas cleaning system 31, the flue gas cooler 32 and the blower are optional and may be arranged in a different order.
  • the separation device 16 essentially comprises an absorption unit 17 and a desorption unit 18.
  • the absorption unit 17 can consist of several columns, which in turn are provided with internals, so-called packages.
  • the packs serve to increase the surface area, which is advantageous for the absorption of the carbon dioxide from the exhaust gas into the absorption medium.
  • the absorption unit 17 can be supplied with an absorption medium via a line for regenerated absorption medium 48.
  • a purification of the exhaust gas can be achieved, so that via a flue gas line 39 a exhaust gas largely freed of carbon dioxide can be diverted.
  • a laden absorption medium 6 formed in the absorption unit 17 by the cleaning can be fed to the desorption unit via a line for laden absorption medium 47.
  • an absorbent pump 34 and a cross-flow heat exchanger 35 are connected in the line for loaded absorption medium 47.
  • the absorption medium pump 34 serves to convey the loaded absorption medium 6.
  • the cross-flow heat exchanger 35 the loaded absorption medium 6 can be conducted in the opposite direction to a hot, regenerated absorption medium 11. As a result, a preheating of the loaded absorption medium 6 can be achieved.
  • the desorption unit 18 may consist of several columns, which in turn are provided with internals, so-called packages.
  • the packages serve to enlarge the surface, which is advantageous for the desorption of the loaded absorbent 7.
  • the desorption unit further comprises a injection device 19 which is arranged in the lower region of the desorption unit 18.
  • the injection device 19 consists of a line through which a vapor can be conducted, and a nozzle arrangement 20 which has a number of nozzle heads 21 through which the steam which can be conducted through the injection device 19 can be injected into the desorption unit 17.
  • the injection is preferably carried out in the flow direction of the absorption medium, ie from top to bottom.
  • the injection device 19 is connected via a steam line 22 to a tapping point of an overflow line 23 of the steam turbine 29. Not shown here is an alternative steam line which connects the injection device 19 with the steam condensate line 24.
  • the removal of steam for the supply line in the Injection device 19 from another steam line is also possible.
  • the desorption unit 18 In the desorption unit 18, a substantial release of carbon dioxide from the loaded absorption medium 6, so that a gaseous carbon dioxide 8 and the regenerated absorption medium 11 is formed. A part of the regenerated absorption medium 11 leaving the desorption unit 18 is heated by means of a heating device 26 and fed again into the desorption unit 18. As a heater here is a reboiler used. Another part of the regenerated absorption medium 11 leaving the desorption unit 18 is fed to the absorption unit 17 via a line for regenerated absorption medium 48. Into the line for regenerated absorption medium 48 is connected an adsorbent pump 34 ', the crossflow heat exchanger 35 and an adsorbent cooler 36. Through the cross-flow heat exchanger 35 and the absorption medium cooler 36 heat can be withdrawn from the regenerated Absorptiosmedium. The use of the absorbent cooler 36 is optional.
  • the desorption unit 18 is also connected via a gas line 49 with a separator 38.
  • the so-called stripper condenser the separation of vaporous absorption medium and gaseous carbon dioxide takes place by condensation of the absorption medium.
  • the condensed absorption medium can be returned to the desorption unit 18 via a condensate line 50.
  • the gaseous carbon dioxide is now subject to further processing, e.g. a liquefaction, available.
  • the fossil-fired power plant 14 shown in FIG. 3 shows a combined-cycle power plant 51 with separator 16 for carbon dioxide.
  • the gas and steam Turbine power plant 51 is the separator 16 upstream.
  • the gas and steam turbine power plant 51 comprises a gas turbine unit and a steam turbine unit.
  • the gas turbine unit essentially consists of a gas turbine 43, which is connected via a shaft to an air compressor 41 and a generator 30.
  • the air compressor 41 is connected to the combustion chamber 42.
  • a fuel supply line 46 is likewise connected to the combustion chamber 42.
  • a carbon dioxide-containing exhaust gas produced by combustion can be supplied to the gas turbine 43 via a flue gas line.
  • a carbon dioxide-containing exhaust gas leaving the gas turbine 43 can be supplied via a flue gas line of the steam turbine unit.
  • the steam turbine unit consists of the heat recovery steam generator 45, a steam turbine 29, a generator 30 and a condenser 37.
  • the flue gas line is connected to the heat recovery steam generator 45 of the steam turbine unit.
  • the heat recovery steam generator 45 is provided for steam generation and supplies steam to the steam turbine 39 via a steam line.
  • the steam turbine 39 is connected via a shaft to a generator 30 for generating electricity.
  • the downstream separation device 16 is designed substantially analogously as in FIG 2 in the steam power plant.
  • the operation of a reduced carbon dioxide emission power plant with high efficiency is possible.
  • the bottom evaporator is relieved and higher-value steam is saved at the cost of adding lower-value steam. This saves energy for operating the desorption process.
  • the device for separating carbon dioxide from a carbon dioxide-containing exhaust gas is part of the fossil-fired power plant.
  • the improvement in terms of circuitry is a major efficiency Increase compared to a conventional gas purification device of a fossil-fired power plant achievable.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Carbon And Carbon Compounds (AREA)
  • Chimneys And Flues (AREA)

Abstract

L'invention concerne un procédé pour séparer le dioxyde de carbone d'un gaz de combustion rejeté par une centrale électrique fonctionnant aux énergies fossiles. Le procédé consiste à brûler d'abord un combustible fossile (2) au cours d'un processus de combustion à l'issue duquel on obtient un gaz d'échappement (3) chaud chargé en dioxyde de carbone. Lors d'une étape suivante de ce procédé, on met en contact le gaz d'échappement (3) chargé en dioxyde de carbone et un milieu absorbant (5) au cours d'un processus d'absorption (4), du dioxyde de carbone étant extrait du milieu absorbant (5) et un milieu absorbant (6) chargé étant ainsi obtenu. Lors d'une étape suivante de ce procédé, on chasse thermiquement le dioxyde de carbone gazeux (8) du milieu absorbant (6) chargé au cours d'un processus de désorption (7). Au cours du processus de désorption (7), on achemine de la vapeur (9) que l'on injecte dans le milieu absorbant (6) chargé. La chaleur de condensation dégagée par la condensation de la vapeur (9) est transférée sur le milieu absorbant (6) chargé et dans le même temps, la pression partielle du dioxyde de carbone baisse dans l'unité de désorption.
EP09797441A 2008-07-17 2009-05-14 Procédé et dispositif pour séparer le dioxyde de carbone d'un gaz d'échappement rejeté par une centrale électrique fonctionnant aux énergies fossiles Withdrawn EP2307121A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP09797441A EP2307121A1 (fr) 2008-07-17 2009-05-14 Procédé et dispositif pour séparer le dioxyde de carbone d'un gaz d'échappement rejeté par une centrale électrique fonctionnant aux énergies fossiles

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP08012961A EP2145667A1 (fr) 2008-07-17 2008-07-17 Procédé et dispositif de séparation de dioxyde de carbone d'un gaz d'échappement d'une centrale à combustible fossile
PCT/EP2009/055792 WO2010006825A1 (fr) 2008-07-17 2009-05-14 Procédé et dispositif pour séparer le dioxyde de carbone d’un gaz d’échappement rejeté par une centrale électrique fonctionnant aux énergies fossiles
EP09797441A EP2307121A1 (fr) 2008-07-17 2009-05-14 Procédé et dispositif pour séparer le dioxyde de carbone d'un gaz d'échappement rejeté par une centrale électrique fonctionnant aux énergies fossiles

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EP09797441A Withdrawn EP2307121A1 (fr) 2008-07-17 2009-05-14 Procédé et dispositif pour séparer le dioxyde de carbone d'un gaz d'échappement rejeté par une centrale électrique fonctionnant aux énergies fossiles

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EP (2) EP2145667A1 (fr)
JP (1) JP5465246B2 (fr)
CN (1) CN102089062A (fr)
AU (1) AU2009270451B2 (fr)
BR (1) BRPI0915754A2 (fr)
CA (1) CA2730865A1 (fr)
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WO (1) WO2010006825A1 (fr)

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DE102010003676A1 (de) * 2010-04-07 2011-10-13 Siemens Aktiengesellschaft Abscheidevorrichtung für CO2 und Kraftwerk
EP2425887A1 (fr) * 2010-09-03 2012-03-07 Siemens Aktiengesellschaft Centrale alimentée par énergie fossile dotée d'un dispositif de séparation pour dioxyde de carbone et procédé de séparation de dioxyde de carbone d'un gaz d'échappement d'une centrale alimentée par énergie fossile
JP5843464B2 (ja) 2011-04-06 2016-01-13 三菱重工業株式会社 二酸化炭素の回収システム及び方法
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US9157369B2 (en) * 2012-03-01 2015-10-13 Linde Aktiengesellschaft Waste heat utilization for energy efficient carbon capture
EP2703607A1 (fr) 2012-09-04 2014-03-05 Alstom Technology Ltd Procédé d'augmentation du rendement d'électricité pendant la demande élevée
DE102013202596B4 (de) * 2013-02-19 2014-11-06 Siemens Aktiengesellschaft Gasturbinenkraftwerk mit CO2-Abscheidung
JP6107695B2 (ja) * 2014-02-10 2017-04-05 日立化成株式会社 二酸化炭素回収装置及び二酸化炭素回収方法
JP5988285B1 (ja) * 2015-10-21 2016-09-07 株式会社島川製作所 アンモニアを含む排ガスの処理装置および処理方法
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Publication number Publication date
EP2145667A1 (fr) 2010-01-20
CA2730865A1 (fr) 2010-01-21
AU2009270451A1 (en) 2010-01-21
RU2508158C2 (ru) 2014-02-27
RU2011105825A (ru) 2012-08-27
JP5465246B2 (ja) 2014-04-09
AU2009270451B2 (en) 2014-09-04
US20110139003A1 (en) 2011-06-16
JP2011527936A (ja) 2011-11-10
CN102089062A (zh) 2011-06-08
WO2010006825A1 (fr) 2010-01-21
BRPI0915754A2 (pt) 2015-11-03
US8834609B2 (en) 2014-09-16

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