EP2467588A1 - Method and device for utilizing biomass - Google Patents

Method and device for utilizing biomass

Info

Publication number
EP2467588A1
EP2467588A1 EP10745200A EP10745200A EP2467588A1 EP 2467588 A1 EP2467588 A1 EP 2467588A1 EP 10745200 A EP10745200 A EP 10745200A EP 10745200 A EP10745200 A EP 10745200A EP 2467588 A1 EP2467588 A1 EP 2467588A1
Authority
EP
European Patent Office
Prior art keywords
gas
thermal energy
turbine
gas turbine
downstream
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Withdrawn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
EP10745200A
Other languages
German (de)
French (fr)
Inventor
Dragan Stevanovic
Sven Johannssen
Reinhard Pritscher
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.)
Krones AG
Original Assignee
Krones 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 Krones AG filed Critical Krones AG
Publication of EP2467588A1 publication Critical patent/EP2467588A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C3/00Gas-turbine plants characterised by the use of combustion products as the working fluid
    • F02C3/20Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products
    • F02C3/26Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products the fuel or oxidant being solid or pulverulent, e.g. in slurry or suspension
    • F02C3/28Gas-turbine plants characterised by the use of combustion products as the working fluid using a special fuel, oxidant, or dilution fluid to generate the combustion products the fuel or oxidant being solid or pulverulent, e.g. in slurry or suspension using a separate gas producer for gasifying the fuel before combustion
    • 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
    • F01K23/00Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/067Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle the combustion heat coming from a gasification or pyrolysis process, e.g. coal gasification
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C1/00Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
    • F02C1/04Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C6/00Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas- turbine plants for special use
    • F02C6/18Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas- turbine plants for special use using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/0916Biomass
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0956Air or oxygen enriched air
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0973Water
    • C10J2300/0976Water as steam
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1603Integration of gasification processes with another plant or parts within the plant with gas treatment
    • C10J2300/1606Combustion processes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1671Integration of gasification processes with another plant or parts within the plant with the production of electricity
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/18Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1861Heat exchange between at least two process streams
    • C10J2300/1869Heat exchange between at least two process streams with one stream being air, oxygen or ozone
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/18Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1861Heat exchange between at least two process streams
    • C10J2300/1892Heat exchange between at least two process streams with one stream being water/steam
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Definitions

  • the invention relates to a method for converting thermal energy from carbonaceous raw materials into mechanical work, according to the preamble of claim 1, and to a device for converting thermal energy into mechanical work, according to the preamble of claim 9.
  • the invention will be described with reference to biomass However, it should be noted that the inventive method and the device according to the invention can also be used for other carbonaceous products.
  • DE 100 39 246 C2 relates to a method for converting thermal energy into mechanical work, wherein a first and a second means for storing thermal energy are switched on alternately in a turbine branch.
  • the disadvantage here is the formation of dust in the flue gases, which must be removed for example by means of a cyclone.
  • DE 102 27 074 A1 describes a method for the gasification of biomass and a system for this purpose.
  • the substances are burned in a gas-tightly separated from a gasification reactor combustion chamber and introduced the heat energy from the combustion chamber in the gasification reactor.
  • DE 198 36 428 C2 discloses methods and apparatus for gasification of biomass, in particular of wood pulp.
  • a fixed bed Degassing at temperatures up to 600 0 C and in a downstream second gasification stage, a fluidized bed gasification at temperatures between 800 0 C and 100O 0 C.
  • the present invention is therefore an object of the invention to provide a method and apparatus for converting thermal energy from combustion or gasification of carbonaceous raw materials into mechanical work available, which has a high efficiency and high efficiency while avoiding dust in the Allow flue gases. Furthermore, a method is to be created, which feeds the resulting energies, in particular waste heat, in turn to the process.
  • An essential point of the invention is that a method for converting thermal energy from carbonaceous raw materials into mechanical work with at least a first and a second means for storing thermal energy, which are switched at least temporarily alternately in a turbine branch with a downstream gas turbine following Steps:
  • a gasification of the carbonaceous raw materials takes place in a gasifier and the product gas is supplied to the gasifier downstream gas burner.
  • the use of a carburettor before the step of combustion in the gas burner enables in particular a significant reduction of dust, in particular fine dust in the flue gases.
  • a reduced dust content allows the use of higher temperatures during gas combustion.
  • a higher efficiency in power generation can be achieved.
  • the reduction of fine dust also has a positive effect on the service life of the gas turbine.
  • downstream is understood in particular to be a downstream in relation to the respective gases to be processed.
  • the gas burner is connected directly downstream of the gasifier.
  • the device for storing thermal energy is preferably also suitable for emitting the stored thermal energy, for example in the form of hot air.
  • the invention proposes to obtain the product gas for the gas burner from an additional gasification process, so that in this respect no additional dust particles, as in the prior art arise.
  • the recovered in the means for storing thermal energy hot air is preferably delivered to the gas turbine.
  • heated water vapor or air or a mixture of water vapor and air is introduced into the gasifier as gasification agent and used for gasification.
  • the gasifier is advantageously fed to a further gaseous medium as combustion gas.
  • combustion gas comes z.
  • hot air oxygen, oxygen-enriched air and the like into consideration.
  • a fixed-bed countercurrent carburetor is used as the carburetor.
  • different types of carburetors according to the prior art can be used.
  • the particular advantage of a countercurrent fixed bed gasifier is that within this reactor individual zones are formed in which different temperatures and thus different processes occur. The different temperatures are based on the fact that the respective processes are strongly endothermic and the heat only comes from below.
  • At least one further heat exchanger arranged downstream of a compressor of the gas turbine is advantageously provided, which at least partially cools supplied hot air and supplies it as cold air to the first and / or second device for storing thermal energy.
  • this is intended to ensure an increase in efficiency of the stored energy.
  • by cooling the air the temperature of the flue gas - A - ses be reduced.
  • the valve-like means is used for emergency shutdown and is preferably arranged in a bypass between a feed to the expander and a discharge line from the compressor of the gas turbine.
  • the waste heat from at least one gasification-following process is used for saturated steam production.
  • This relates in particular to the supply of waste heat to at least one of the gas turbine downstream heat exchanger, is heated with the water.
  • a heat exchanger for heating air is provided.
  • the waste heat donating gas is that gas which exits the gas turbine and still has a very high temperature.
  • the saturated steam is generated by means of a gas turbine downstream heat exchanger before it is fed to the carburetor.
  • Cooling is preferably effected by means of at least one heat exchanger and the thermal energy obtained by the cooling is decoupled as usable heat. This further contributes to environmental compatibility and to increasing the efficiency of the process.
  • relaxed hot air from the turbine is re-supplied to the gas burner to further increase the efficiency of the process.
  • combustion air leaving the gas turbine can in turn be supplied to the gas burner via a corresponding supply line.
  • relaxed hot air from the gas turbine is used to generate energy by means of another steam turbine.
  • this additional steam turbine could be integrated into a separate water circuit and the water in this circuit can be vaporized and overheated by a heat exchanger. After exiting the steam turbine, the steam is condensed and compressed in the liquid state by a pump before it passes over the heat exchanger again.
  • a gas burner for burning a fuel at least a first and a second means for storing thermal energy, which at least temporarily alternately in a turbine branch with a downstream gas turbine or its expander are switched on and at least one connecting line, which supplies flue gases formed in the gas burner to the devices for storing thermal energy, wherein the gas burner is preceded by a carburetor for generating the fuel.
  • the apparatus comprises a compressor for compressing the air supplied to the devices for storing thermal energy, wherein this compressor is particularly preferably part of the gas turbine.
  • the flue gases arise during the combustion of a product gas, which in turn is produced in a gasifier.
  • a temporary alternately switching on of the devices for storing thermal energy is understood to mean that at least partially in selected periods of time one of the two devices is supplied with flue gas, while the other device delivers hot air to the gas turbine.
  • a plurality of devices for storing thermal energy may be provided, which operate at least partially with a time delay.
  • one of these means for storing thermal energy may be supplied with flue gas while one or more of the other devices is releasing the hot air.
  • the devices for storing thermal energy work at least partially delayed.
  • the turbine branch downstream means are provided for cooling a gas.
  • These means for cooling the gas are preferably heat exchangers, which, as mentioned above, can simultaneously heat air, so as to produce hot air, which can be supplied to the gasifier.
  • these means saturated steam can be generated, which can also be supplied to the gasifier.
  • a means for alternately switching at least one first device and at least one second device into the turbine branch is preferably provided.
  • These alternately switching-on means may, for example, be a multiplicity of controllable valves, which in each case permit the flue gas to be fed alternately into the means for storing thermal energy or allow alternate discharge of heated air to the gas turbine.
  • temperature sensors can be provided, which respectively measure the temperatures at corresponding points of the devices for storing thermal energy and switch the corresponding valves in response to these measurements, so that optimal supply of the gas turbines with hot air is made possible at all times and furthermore an efficient one Recharging the means for storing thermal energy is enabled.
  • the gas turbine or a part thereof preferably also acts as a compressor to compress supplied air and to supply cold air to be heated in turn to the devices for storing thermal energy.
  • the gas turbine is connected downstream of at least one heat exchanger.
  • At least one and preferably a plurality of heat exchangers for decoupling thermal energy is switched on between the gas turbine and the gasifier.
  • the gas turbine downstream of another steam turbine.
  • the hot air from the first gas turbine can be used again to generate electricity.
  • the current efficiency can be further improved.
  • Fig. 1 is a first flowchart
  • Fig. 2 is a second flowchart
  • Fig. 3 is a third flowchart.
  • Fig. 1 shows a schematic flow diagram of the use of a device according to the invention for the conversion of thermal energy from carbonaceous raw materials into mechanical work.
  • the reference numeral 1 refers to a fixed bed countercurrent reactor.
  • the raw material 14 is introduced from above into the reactor 1 and the gasification agent (e.g., air) is fed along a supply line 16 from below. In this way it is achieved that the gasification agent and the product gas flow through the reaction space in the opposite direction to the fuel flow.
  • the resulting ash in the carburetor 1 is discharged downwards, that is, along the arrow P1.
  • the product gas enters the gas burner 2 and is burned. Subsequently, the resulting in the gas burner 2 flue gases are passed through a connecting line 3 in a first 4 or second 6 Schüttgutregenerator and supplied by the bulk regenerators 4,6 hot air 7 via a line 21 to a gas turbine 8.
  • a generator G is arranged on the gas turbine 8.
  • the reference numeral 23 denotes a discharge pipe for discharging the flue gas generated in the means 4, 6 for storing thermal energy.
  • the first regenerator 4 From the first regenerator 4 leads a line 22 to the gas turbine 8.
  • the from the gas turbine. 8 Exiting exhaust air is supplied via a further line 26 to the gas burner 2 as preheated combustion air.
  • the first 4 and the second regenerator 6 can be operated alternately in the turbine branch T or in a so-called preheating branch.
  • the reference numeral 60 refers to a generator coupled to the turbine 8.
  • the reference numerals 32, 34, 36, 38, 40, 42, 44, 46 each refer to controllable valves, the supply of the flue gas to the bulk regenerators 4.6 (valves 44 and 46) and the discharge of the hot air of bulk regenerators 4, 6 to the gas turbine 8 (valves 36 and 42), the delivery of flue gas (valves 32 and 38) as well as vice versa the supply of cold air (valves 34 and 40) to the bulk regenerators 4.6 control.
  • the respectively black drawn valves are in an open state and the only rimmed valves in a closed state.
  • Reference numerals 52, 54, 56 respectively refer to compressors for compressing air (reference numeral 56), flue gas (reference numeral 52) and exhaust air (reference numeral 54).
  • air is supplied via the line 25 of the gas turbine 8 and passed through a further heat exchanger 15 to be supplied as cold air in bulk regenerators 4 and 6.
  • the reference numeral 61 designates a valve-like means between the compressor and a gas turbine engine expander for turning off the turbine branch. Between the turbine and the heat exchanger 15, a water supply is possible. In this branch, another valve 63 is provided.
  • heat exchangers 1 1, 12 and 13 are turned on to supply heated both air and water as a gasification agent to the fixed bed countercurrent reactor 1.
  • a cooling is effected by means of at least one heat exchanger 13 and the thermal energy obtained by the cooling is decoupled as usable heat.
  • the heat exchanger 13 is directly downstream of the turbine branch T. By means of this device, it is possible to use the decoupled heat (for hot water production) at a higher temperature level.
  • the heat exchanger 1 1, 12 for heating air and water as a gasification agent are connected downstream.
  • the order of the heat exchangers is changed in the two embodiments shown. While in the embodiment shown in Figure 1, the first heat exchanger 12, which receives the combustion air with the highest temperature, for generating hot air, the next heat exchanger 1 1 for generating saturated steam and the last heat exchanger 13 for generating heat, is in the shown in Figure 2 with the hottest air generates heat and then hot air or saturated steam. Furthermore, it would also be possible to exchange the two heat exchangers 12 and 1 1 with respect to their order.
  • the reference numeral 58 in the two figures refers to a pump for conveying water.
  • the reference numeral 10 in the figures refers to the combustion gas and the reference numeral 9 designates the saturated steam.
  • Fig. 3 shows another embodiment of the present invention.
  • a further circuit 70 is provided, which is connected downstream of the gas turbine 8. More specifically, the hot air from the gas turbine 8 is passed through a heat exchanger 71, which is integrated in this circuit 70. Through the heat exchanger, water of the circuit 70 is heated and fed to a steam turbine 72, which in turn drives a generator 74.
  • the reference numeral 78 refers to a pump and the reference numeral 76 to a capacitor.

Abstract

The invention relates in particular to a method for converting thermal energy from carbonaceous raw materials into mechanical work, having at least one first (4) and one second (6) device for storing and releasing thermal energy connected at least intermittently alternatingly in a turbine branch (T) having a gas turbine (8) connected downstream thereof, comprising the following steps: a) combusting a gas in a gas burner (2); b) passing the smoke gases (3) arising in the gas burner (2) through a device (4, 6) for storing thermal energy; and c) feeding the hot air (7) released by at least one device (4, 6) into the gas turbine (8), wherein the gasification of the carbonaceous raw materials takes place in a gasifier (1) in a first step and the product gas is fed into the gas burner (2) connected downstream of the gasifier (1).

Description

Verfahren und Vorrichtung zur Verwertung von Biomasse Beschreibung  Method and device for utilization of biomass Description
Die Erfindung betrifft ein Verfahren zur Umwandlung von thermischer Energie aus kohlenstoffhaltigen Rohstoffen in mechanische Arbeit, gemäß dem Oberbegriff des Patentanspruches 1 sowie eine Vorrichtung zur Umwandlung von thermischer Energie in mechanische Arbeit, gemäß dem Oberbegriff des Patentanspruches 9. Die Erfindung wird unter Bezugnahme auf Biomasse beschrieben, es wird jedoch darauf hingewiesen, dass das erfindungsgemäße Verfahren und die erfindungsgemäße Vorrichtung auch für andere kohlenstoffhaltige Produkte verwendet werden kann. The invention relates to a method for converting thermal energy from carbonaceous raw materials into mechanical work, according to the preamble of claim 1, and to a device for converting thermal energy into mechanical work, according to the preamble of claim 9. The invention will be described with reference to biomass However, it should be noted that the inventive method and the device according to the invention can also be used for other carbonaceous products.
Die DE 100 39 246 C2 betrifft ein Verfahren zur Umwandlung thermischer Energie in mechanische Arbeit, wobei ein erstes und ein zweites Mittel zum Speichern thermischer Energie wechselweise in einen Turbinenzweig eingeschaltet werden. Als nachteilig erweist sich dabei die Bildung von Staub in den Rauchgasen, welcher beispielsweise mittels eines Zyklons entfernt werden muss. DE 100 39 246 C2 relates to a method for converting thermal energy into mechanical work, wherein a first and a second means for storing thermal energy are switched on alternately in a turbine branch. The disadvantage here is the formation of dust in the flue gases, which must be removed for example by means of a cyclone.
Die DE 102 27 074 A1 beschreibt ein Verfahren zur Vergasung von Biomasse und eine Anlage hierzu. Dabei werden die Substanzen in einer von einem Vergasungsreaktor gasdicht getrennten Verbrennungskammer verbrannt und die Wärmeenergie aus der Verbrennungskammer in den Vergasungsreaktor eingeführt. DE 102 27 074 A1 describes a method for the gasification of biomass and a system for this purpose. In this case, the substances are burned in a gas-tightly separated from a gasification reactor combustion chamber and introduced the heat energy from the combustion chamber in the gasification reactor.
Die DE 198 36 428 C2 offenbart Verfahren und Vorrichtungen zum Vergasen von Biomasse, insbesondere von Holzstoffen. Dabei erfolgt in einer ersten Vergasungsstufe eine Festbett- entgasung bei Temperaturen bis zu 6000C und in einer nachgeschalteten zweiten Vergasungsstufe eine Wirbelschichtvergasung bei Temperaturen zwischen 8000C und 100O0C. DE 198 36 428 C2 discloses methods and apparatus for gasification of biomass, in particular of wood pulp. In this case, in a first gasification stage, a fixed bed Degassing at temperatures up to 600 0 C and in a downstream second gasification stage, a fluidized bed gasification at temperatures between 800 0 C and 100O 0 C.
Der vorliegenden Erfindung liegt daher die Aufgabe zugrunde, ein Verfahren und eine Vorrichtung zur Umsetzung von thermischer Energie aus Verbrennung bzw. Vergasung kohle- stoffhaltiger Rohstoffe in mechanische Arbeit zur Verfügung zu stellen, welche eine hohe Effizienz und einen hohen Wirkungsgrad unter Vermeidung von Staub in den Rauchgasen ermöglichen. Weiterhin soll ein Verfahren geschaffen werden, welches entstehende Energien, insbesondere Abwärme, wiederum dem Prozess zuführt. The present invention is therefore an object of the invention to provide a method and apparatus for converting thermal energy from combustion or gasification of carbonaceous raw materials into mechanical work available, which has a high efficiency and high efficiency while avoiding dust in the Allow flue gases. Furthermore, a method is to be created, which feeds the resulting energies, in particular waste heat, in turn to the process.
Dies wird durch ein Verfahren nach Anspruch 1 und durch eine Vorrichtung nach Anspruch 9 erreicht. Vorteilhafte Ausführungsformen und Weiterbildungen sind Gegenstand der Unteransprüche. This is achieved by a method according to claim 1 and by a device according to claim 9. Advantageous embodiments and further developments are the subject of the dependent claims.
Ein wesentlicher Punkt der Erfindung liegt darin, dass ein Verfahren zur Umwandlung von thermischer Energie aus kohlenstoffhaltigen Rohstoffen in mechanische Arbeit mit wenigstens einer ersten und einer zweiten Einrichtung zum Speichern thermischer Energie, welche wenigstens zeitweise wechselweise in einen Turbinenzweig mit einer nachgeschalteten Gasturbine eingeschaltet werden, folgende Schritte aufweist: An essential point of the invention is that a method for converting thermal energy from carbonaceous raw materials into mechanical work with at least a first and a second means for storing thermal energy, which are switched at least temporarily alternately in a turbine branch with a downstream gas turbine following Steps:
a) Verbrennen eines Gases in einem Gasbrenner, a) burning a gas in a gas burner,
b) Durchleiten der in dem Gasbrenner entstandenen Rauchgase durch eine Einrichtung zum Speichern thermischer Energie, und b) passing the resulting in the gas burner flue gases by a device for storing thermal energy, and
c) Einleiten der von einer Einrichtung zum Speichern von thermischer Energie abgegebenen Heißluft in die Gasturbine bzw. deren Expander, c) introducing the hot air discharged by a device for storing thermal energy into the gas turbine or its expander,
wobei in einem ersten Schritt eine Vergasung der kohlenstoffhaltigen Rohstoffe in einem Vergaser erfolgt und das Produktgas dem Vergaser nachgeschalteten Gasbrenner zugeführt wird. Die Verwendung eines Vergasers vor dem Schritt der Verbrennung in dem Gasbrenner ermöglicht insbesondere eine deutliche Verminderung von Staub, insbesondere Feinstaub in den Rauchgasen. Zudem gestattet ein verminderter Staubanteil die Anwendung höherer Temperaturen bei der Gasverbrennung. Daneben kann ein höherer Wirkungsgrad bei der Stromerzeugung erzielt werden. Die Verminderung des Feinstaubs wirkt sich zudem positiv auf die Lebensdauer der Gasturbine aus. Unter dem Begriff Nachschalten wird insbesondere ein Nachschalten in Bezug auf die jeweils zu verarbeitenden Gase verstanden. Vorzugsweise ist der Gasbrenner dem Vergaser unmittelbar nachgeschaltet. Bevorzugt ist die Einrichtung zum Speichern thermischer Energie auch zur Abgabe der gespeicherten thermischen Energie, beispielsweise in Form von Heißluft, geeignet. Damit wird erfindungsgemäß vorgeschlagen, das Produktgas für den Gasbrenner aus einem zusätzlichen Vergasungsprozess zu gewinnen, so dass insoweit keine zusätzlichen Staubpartikel, wie im Stand der Technik, entstehen. Unter dem Einschalten in den Turbinenzweig wird damit insbesondere verstanden, dass die in den Mitteln zum Speichern thermischer Energie gewonnene Heißluft bevorzugt an die Gasturbine abgegeben wird. wherein in a first step, a gasification of the carbonaceous raw materials takes place in a gasifier and the product gas is supplied to the gasifier downstream gas burner. The use of a carburettor before the step of combustion in the gas burner enables in particular a significant reduction of dust, in particular fine dust in the flue gases. In addition, a reduced dust content allows the use of higher temperatures during gas combustion. In addition, a higher efficiency in power generation can be achieved. The reduction of fine dust also has a positive effect on the service life of the gas turbine. The term downstream is understood in particular to be a downstream in relation to the respective gases to be processed. Preferably, the gas burner is connected directly downstream of the gasifier. The device for storing thermal energy is preferably also suitable for emitting the stored thermal energy, for example in the form of hot air. Thus, the invention proposes to obtain the product gas for the gas burner from an additional gasification process, so that in this respect no additional dust particles, as in the prior art arise. By switching into the turbine branch is thus understood in particular that the recovered in the means for storing thermal energy hot air is preferably delivered to the gas turbine.
Als Einrichtungen zum Speichern thermischer Energie können insbesondere Schüttgutgeneratoren eingesetzt werden, wie sie beispielsweise in der EP 0 620 909 B1 oder der As devices for storing thermal energy in particular bulk generators can be used, as described for example in EP 0 620 909 B1 or the
DE 42 36 619 C2 beschrieben wurden. DE 42 36 619 C2 have been described.
Bevorzugt wird als Vergasungsmittel erhitzter Wasserdampf oder Luft oder eine Mischung aus Wasserdampf und Luft in den Vergaser eingeführt und zur Vergasung verwendet. Gemeinsam mit dem Wasserdampf wird dem Vergaser vorteilhaft ein weiteres gasförmiges Medium als Verbrennungsgas zugeführt. Als Verbrennungsgas kommt z. B. Heißluft, Sauerstoff, mit Sauerstoff angereicherte Luft und dergleichen in Betracht. Preferably, heated water vapor or air or a mixture of water vapor and air is introduced into the gasifier as gasification agent and used for gasification. Together with the steam, the gasifier is advantageously fed to a further gaseous medium as combustion gas. As combustion gas comes z. As hot air, oxygen, oxygen-enriched air and the like into consideration.
Vorzugsweise wird als Vergaser ein Festbett - Gegenstrom - Vergaser verwendet. Grundsätzlich können verschiedene Vergasertypen nach dem Stand der Technik eingesetzt werden. Der besondere Vorteil eines Gegenstromfestbettvergasers besteht jedoch darin, dass sich innerhalb dieses Reaktors einzelne Zonen herausbilden, in denen unterschiedliche Temperaturen und somit unterschiedliche Prozesse auftreten. Die unterschiedlichen Temperaturen beruhen darauf, dass die jeweiligen Prozesse stark endotherm sind und die Wärme nur von unten kommt. Preferably, a fixed-bed countercurrent carburetor is used as the carburetor. In principle, different types of carburetors according to the prior art can be used. However, the particular advantage of a countercurrent fixed bed gasifier is that within this reactor individual zones are formed in which different temperatures and thus different processes occur. The different temperatures are based on the fact that the respective processes are strongly endothermic and the heat only comes from below.
Vorteilhaft ist mindestens ein weiterer einem Verdichter der Gasturbine nachgeschalteter Wärmetauscher vorgesehen, welcher zugeführte Heißluft zumindest teilweise abkühlt und als Kaltluft der ersten und/oder zweiten Einrichtung zum Speichern thermischer Energie zuführt. Zum eine soll dadurch eine Effizienzerhöhung der gespeicherten Energie gewährleistet werden. Andererseits kann durch das Abkühlen der Luft auch die Temperatur des Rauchga- - A - ses reduziert werden. At least one further heat exchanger arranged downstream of a compressor of the gas turbine is advantageously provided, which at least partially cools supplied hot air and supplies it as cold air to the first and / or second device for storing thermal energy. On the one hand, this is intended to ensure an increase in efficiency of the stored energy. On the other hand, by cooling the air, the temperature of the flue gas - A - ses be reduced.
Des Weiteren bevorzugt ist dem Verdichter der Gasturbine nachgeschaltet eine Further preferably, the compressor of the gas turbine downstream of a
Wassereindüsung vorgesehen ist. Water injection is provided.
Bevorzugt ist wenigstens ein ventilartiges Mittel zwischen dem Verdichter und einem Preferably, at least one valve-like means between the compressor and a
Entspanner der Gasturbine zum Ausschalten des Turbinenzweigs vorgesehen. Das ventilartige Mittel dient der Notabschaltung und ist vorzugsweise in einem Bypass zwischen einer zuführenden zum Entspanner und einer abführenden Leitung vom Verdichter der Gasturbine angeordnet. Relaxer of the gas turbine provided to turn off the turbine branch. The valve-like means is used for emergency shutdown and is preferably arranged in a bypass between a feed to the expander and a discharge line from the compressor of the gas turbine.
In einer bevorzugten Ausführungsform wird die Abwärme aus wenigstens einem der Vergasung folgenden Prozesse für eine Sattdampferzeugung verwendet. Dies betrifft insbesondere das Zuleiten der Abwärme zu mindestens einem der Gasturbine nachgeschalteten Wärmetauscher, mit dem Wasser erhitzt wird. Ebenso ist ein Wärmetauscher zur Erwärmung von Luft vorgesehen. In a preferred embodiment, the waste heat from at least one gasification-following process is used for saturated steam production. This relates in particular to the supply of waste heat to at least one of the gas turbine downstream heat exchanger, is heated with the water. Likewise, a heat exchanger for heating air is provided.
Vorzugsweise handelt es sich bei dem Abwärme spendenden Gas um jenes Gas, welches aus der Gasturbine austritt und noch eine sehr hohe Temperatur aufweist. Preferably, the waste heat donating gas is that gas which exits the gas turbine and still has a very high temperature.
Dabei wird der Sattdampf mittels eines der Gasturbine nachgeschalteten Wärmetauschers erzeugt, bevor er dem Vergaser zugeführt wird. In this case, the saturated steam is generated by means of a gas turbine downstream heat exchanger before it is fed to the carburetor.
Bevorzugt wird mittels mindestens eines Wärmetauschers eine Abkühlung bewirkt und die durch die Abkühlung gewonnene thermische Energie als nutzbare Wärme ausgekoppelt. Dies trägt weiter zur Umweltverträglichkeit sowie zur Steigerung der Effizienz des Verfahrens bei. Cooling is preferably effected by means of at least one heat exchanger and the thermal energy obtained by the cooling is decoupled as usable heat. This further contributes to environmental compatibility and to increasing the efficiency of the process.
Vorzugsweise wird entspannte Heißluft aus der Turbine dem Gasbrenner erneut zugeführt, um die Effizienz des Verfahrens weiter zu erhöhen. So kann beispielsweise Verbrennungsluft, welche die Gasturbine verlässt, wiederum über eine entsprechende Zuführleitung dem Gasbrenner zugeführt werden. Bei einem weiteren bevorzugten Verfahren wird mittels einer weiteren Dampfturbine entspannte Heißluft aus der Gasturbine zur Energieerzeugung verwendet. Dabei könnte diese zusätzliche Dampfturbine in einen separaten Wasserkreislauf eingebunden werden und das Wasser in diesem Kreislauf durch einen Wärmetauscher verdampft und überhitzt werden. Nach dem Austritt aus der Dampfturbine, wird der Dampf kondensiert und in flüssigem Zustand von einer Pumpe komprimiert, bevor er wieder über den Wärmetauscher läuft. Preferably, relaxed hot air from the turbine is re-supplied to the gas burner to further increase the efficiency of the process. For example, combustion air leaving the gas turbine can in turn be supplied to the gas burner via a corresponding supply line. In a further preferred method, relaxed hot air from the gas turbine is used to generate energy by means of another steam turbine. In this case, this additional steam turbine could be integrated into a separate water circuit and the water in this circuit can be vaporized and overheated by a heat exchanger. After exiting the steam turbine, the steam is condensed and compressed in the liquid state by a pump before it passes over the heat exchanger again.
Erfindungsgemäß sind für die Vorrichtung zur Umwandlung von thermischer Energie in mechanische Arbeit ein Gasbrenner zum Verbrennen eines Brennstoffes, wenigstens eine erste und eine zweite Einrichtung zum Speichern thermischer Energie, welche wenigstens zeitweise wechselweise in einen Turbinenzweig mit einer nachgeschalteten Gasturbine bzw. deren Expander einschaltbar sind und wenigstens eine Verbindungsleitung, welche in dem Gasbrenner entstehende Rauchgase den Einrichtungen zum Speichern thermischer Energie zuführt, vorgesehen, wobei dem Gasbrenner ein Vergaser zum Erzeugen des Brennstoffes vorgeschaltet ist. According to the invention for the apparatus for converting thermal energy into mechanical work, a gas burner for burning a fuel, at least a first and a second means for storing thermal energy, which at least temporarily alternately in a turbine branch with a downstream gas turbine or its expander are switched on and at least one connecting line, which supplies flue gases formed in the gas burner to the devices for storing thermal energy, wherein the gas burner is preceded by a carburetor for generating the fuel.
Vorteilhaft weist die Vorrichtung einen Verdichter zum Verdichten der den Einrichtungen zum Speichern thermischer Energie zugeführten Luft auf, wobei dieser Verdichter besonders bevorzugt Bestandteil der Gasturbine ist. Advantageously, the apparatus comprises a compressor for compressing the air supplied to the devices for storing thermal energy, wherein this compressor is particularly preferably part of the gas turbine.
Damit wird auch vorrichtungsseitig vorgeschlagen, dass die Rauchgase bei der Verbrennung eines Produktgases entstehen, welches wiederum in einem Vergaser erzeugt wird. Unter einem zeitweise wechselweisen Einschalten der Einrichtungen zum Speichern thermischer Energie wird verstanden, dass zumindest teilweise in ausgewählten Zeiträumen eine der beiden Einrichtungen mit Rauchgas versorgt wird, während die andere Einrichtung Heißluft an die Gasturbine abgibt. Weiterhin wäre es auch möglich, dass eine Vielzahl von Einrichtungen zum Speichern von thermischer Energie vorgesehen ist, welche zumindest teilweise zeitversetzt arbeiten. So kann beispielsweise eine dieser Einrichtungen zum Speichern thermischer Energie mit Rauchgas versorgt werden, während eine oder mehrere der anderen Einrichtungen die Heißluft abgeben. Auch hinsichtlich der Abgabe von Heißluft arbeiten die Einrichtungen zum Speichern thermischer Energie zumindest teilweise zeitversetzt. Thus, it is also proposed on the device side that the flue gases arise during the combustion of a product gas, which in turn is produced in a gasifier. A temporary alternately switching on of the devices for storing thermal energy is understood to mean that at least partially in selected periods of time one of the two devices is supplied with flue gas, while the other device delivers hot air to the gas turbine. Furthermore, it would also be possible for a plurality of devices for storing thermal energy to be provided, which operate at least partially with a time delay. For example, one of these means for storing thermal energy may be supplied with flue gas while one or more of the other devices is releasing the hot air. Also with regard to the delivery of hot air, the devices for storing thermal energy work at least partially delayed.
Bevorzugt sind dem Turbinenzweig nachgeschaltete Mittel zum Abkühlen eines Gases vorgesehen. Diese Mittel zum Abkühlen des Gases sind dabei vorzugsweise Wärmetauscher, welche, wie oben erwähnt, gleichzeitig Luft erwärmen können, um so Heißluft zu erzeugen, welche dem Vergaser zugeführt werden kann. Weiterhin kann mit diesen Mitteln Sattdampf erzeugt werden, der ebenfalls dem Vergaser zugeführt werden kann. Preferably, the turbine branch downstream means are provided for cooling a gas. These means for cooling the gas are preferably heat exchangers, which, as mentioned above, can simultaneously heat air, so as to produce hot air, which can be supplied to the gasifier. Furthermore, these means saturated steam can be generated, which can also be supplied to the gasifier.
Weiterhin ist vorzugsweise ein Mittel zum wechselweisen Einschalten wenigstens einer ersten Einrichtung und wenigstens einer zweiten Einrichtung in den Turbinenzweig vorgesehen. Furthermore, a means for alternately switching at least one first device and at least one second device into the turbine branch is preferably provided.
Bei diesen Mitteln zum wechselweisen Einschalten kann es sich beispielsweise um eine Vielzahl von steuerbaren Ventilen handeln, die jeweils ein wechselweises Zuführen von Rauchgas in die Mittel zum Speichern thermischer Energie ermöglichen beziehungsweise ein wechselweises Abgeben von erhitzter Luft an die Gasturbine erlauben. Weiterhin können Temperatursensoren vorgesehen sein, die jeweils an entsprechenden Stellen der Vorrichtungen zum Speichern thermischer Energie die Temperaturen messen und in Reaktion auf diese Messungen die entsprechenden Ventile schalten, so dass zu jedem Zeitpunkt eine optimale Versorgung der Gasturbinen mit Heißluft ermöglicht wird und weiterhin auch ein effizientes Wiederaufladen der Mittel zum Speichern von thermischer Energie ermöglicht wird. These alternately switching-on means may, for example, be a multiplicity of controllable valves, which in each case permit the flue gas to be fed alternately into the means for storing thermal energy or allow alternate discharge of heated air to the gas turbine. Furthermore, temperature sensors can be provided, which respectively measure the temperatures at corresponding points of the devices for storing thermal energy and switch the corresponding valves in response to these measurements, so that optimal supply of the gas turbines with hot air is made possible at all times and furthermore an efficient one Recharging the means for storing thermal energy is enabled.
Weiterhin wirkt die Gasturbine bzw. ein Teil derselben bevorzugt auch als Kompressor, um zugeführte Luft zu komprimieren und um den Einrichtungen zum Speichern thermischer Energie wiederum zu erwärmende Kaltluft zuzuführen. Besonders bevorzugt ist der Gasturbine mindestens ein Wärmetauscher nachgeschaltet. Furthermore, the gas turbine or a part thereof preferably also acts as a compressor to compress supplied air and to supply cold air to be heated in turn to the devices for storing thermal energy. Particularly preferably, the gas turbine is connected downstream of at least one heat exchanger.
Dabei ist vorzugsweise zwischen die Gasturbine und dem Vergaser mindestens ein und bevorzugt mehrere Wärmetauscher zur Auskopplung thermischer Energie eingeschaltet. In this case, preferably at least one and preferably a plurality of heat exchangers for decoupling thermal energy is switched on between the gas turbine and the gasifier.
Bevorzugt besteht zwar keine unmittelbare Gasverbindung zwischen der Gasturbine und dem Vergaser. Mittels des Wärmetauschers wird jedoch thermische Energie der von der Gasturbine abgegebenen Gase auf andere Mittel wie den Sattdampf und die Heißluft übertragen und diese Medien werden wie oben erwähnt wiederum dem Vergaser zugeführt. Weiterhin ist vorzugsweise eine Verbindungsleitung zwischen der Gasturbine und dem Gasbrenner vorgesehen, so dass aus der Gasturbine austretende Verbrennungsluft wiederum dem Gasbrenner zugeführt werden kann, um den Verbrennungsvorgang in dem Gasbrenner noch effizienter zu gestalten. Although there is preferably no direct gas connection between the gas turbine and the gasifier. By means of the heat exchanger, however, thermal energy of the gases emitted by the gas turbine is transferred to other means such as the saturated steam and the hot air and these media are again supplied to the gasifier as mentioned above. Furthermore, a connecting line between the gas turbine and the gas burner is preferably provided, so that in turn exiting the gas turbine combustion air the gas burner can be supplied to make the combustion process in the gas burner even more efficient.
Bei einer weiteren vorteilhaften Ausführungsform ist der Gasturbine eine weitere Dampfturbine nachgeschaltet. Durch diese nachgeschaltete Turbine kann die Heißluft aus der ersten Gasturbine noch einmal zur Stromerzeugung verwendet werden. So kann die Stromausbeute weiter verbessert werden. In a further advantageous embodiment of the gas turbine downstream of another steam turbine. Through this downstream turbine, the hot air from the first gas turbine can be used again to generate electricity. Thus, the current efficiency can be further improved.
Vorteile und Zweckmäßigkeiten sind der nachfolgenden Beschreibung in Verbindung mit der Zeichnung zu entnehmen. Hierbei zeigen: Advantages and expediencies can be found in the following description in conjunction with the drawing. Hereby show:
Fig. 1 ein erstes Flussdiagramm; und Fig. 1 is a first flowchart; and
Fig. 2 ein zweites Flussdiagramm; und  Fig. 2 is a second flowchart; and
Fig. 3 ein drittes Flussdiagramm.  Fig. 3 is a third flowchart.
Fig. 1 zeigt ein schematisches Flussdiagramm der Verwendung einer erfindungsgemäßen Vorrichtung zur Umwandlung von thermischer Energie aus kohlenstoffhaltigen Rohstoffen in mechanische Arbeit. Dabei bezieht sich das Bezugszeichen 1 auf einen Festbettgegenstrom- reaktor. Der Rohstoff 14 wird von oben in den Reaktor 1 eingegeben und das Vergasungsmittel (z.B. Luft) entlang einer Zuleitung 16 von unten. Auf diese Weise wird erreicht, dass das Vergasungsmittel und das Produktgas den Reaktionsraum in entgegengesetzter Richtung zu dem Brennstoffstrom durchströmen. Die in dem Vergaser 1 entstehende Asche wird nach unten, das heißt entlang des Pfeils P1 , abgeführt. Fig. 1 shows a schematic flow diagram of the use of a device according to the invention for the conversion of thermal energy from carbonaceous raw materials into mechanical work. The reference numeral 1 refers to a fixed bed countercurrent reactor. The raw material 14 is introduced from above into the reactor 1 and the gasification agent (e.g., air) is fed along a supply line 16 from below. In this way it is achieved that the gasification agent and the product gas flow through the reaction space in the opposite direction to the fuel flow. The resulting ash in the carburetor 1 is discharged downwards, that is, along the arrow P1.
Das Produktgas gelangt in den Gasbrenner 2 und wird verbrannt. Anschließend werden die in den Gasbrenner 2 entstandenen Rauchgase durch eine Verbindungsleitung 3 in einen ersten 4 oder zweiten 6 Schüttgutregenerator geleitet und die von den Schüttgutregeneratoren 4,6 abgegebene Heißluft 7 über eine Leitung 21 einer Gasturbine 8 zugeführt. Im Turbinenzweig T ist ein Generator G auf der Gasturbine 8 angeordnet. Das Bezugszeichen 23 kennzeichnet eine Abführleitung zum Abführen des in den Mitteln 4, 6 zum Speichern thermischer Energie entstehenden Rauchgases. The product gas enters the gas burner 2 and is burned. Subsequently, the resulting in the gas burner 2 flue gases are passed through a connecting line 3 in a first 4 or second 6 Schüttgutregenerator and supplied by the bulk regenerators 4,6 hot air 7 via a line 21 to a gas turbine 8. In the turbine branch T, a generator G is arranged on the gas turbine 8. The reference numeral 23 denotes a discharge pipe for discharging the flue gas generated in the means 4, 6 for storing thermal energy.
Vom ersten Regenerator 4 führt eine Leitung 22 zur Gasturbine 8. Die aus der Gasturbine 8 austretende Abluft wird über eine weitere Leitung 26 dem Gasbrenner 2 als vorgewärmte Verbrennungsluft zugeführt. Mittels einer hier nicht gezeigten Vorrichtung können der erste 4 und der zweite Regenerator 6 wechselweise im Turbinenzweig T bzw. in einem sogenannten Vorwärmzweig betrieben werden. Das Bezugszeichen 60 bezieht sich auf einen Generator, der mit der Turbine 8 gekoppelt ist. From the first regenerator 4 leads a line 22 to the gas turbine 8. The from the gas turbine. 8 Exiting exhaust air is supplied via a further line 26 to the gas burner 2 as preheated combustion air. By means of a device not shown here, the first 4 and the second regenerator 6 can be operated alternately in the turbine branch T or in a so-called preheating branch. The reference numeral 60 refers to a generator coupled to the turbine 8.
Die Bezugszeichen 32, 34, 36, 38, 40, 42, 44, 46 beziehen sich jeweils auf steuerbare Ventile, die die Zuführung des Rauchgases an die Schüttgutregeneratoren 4,6 (Ventile 44 und 46) sowie die Abgabe der Heißluft von Schüttgutregeneratoren 4,6 an die Gasturbine 8 (Ventile 36 und 42), die Abgabe von Rauchgas (Ventile 32 und 38) sowie auch umgekehrt die Zuführung von Kaltluft (Ventile 34 und 40) an die Schüttgutregeneratoren 4,6 steuern. Die jeweils schwarz eingezeichneten Ventile sind dabei in einem geöffneten Zustand und die lediglich umrandeten Ventile in einem geschlossenen Zustand. Die Bezugszeichen 52, 54, 56 beziehen sich jeweils auf Kompressoren bzw. Gebläse, um Luft (Bezugszeichen 56), Rauchgas (Bezugszeichen 52) und Abluft (Bezugszeichen 54) zu komprimieren beziehungsweise zu fördern. The reference numerals 32, 34, 36, 38, 40, 42, 44, 46 each refer to controllable valves, the supply of the flue gas to the bulk regenerators 4.6 (valves 44 and 46) and the discharge of the hot air of bulk regenerators 4, 6 to the gas turbine 8 (valves 36 and 42), the delivery of flue gas (valves 32 and 38) as well as vice versa the supply of cold air (valves 34 and 40) to the bulk regenerators 4.6 control. The respectively black drawn valves are in an open state and the only rimmed valves in a closed state. Reference numerals 52, 54, 56 respectively refer to compressors for compressing air (reference numeral 56), flue gas (reference numeral 52) and exhaust air (reference numeral 54).
Weiterhin wird Luft über die Leitung 25 der Gasturbine 8 zugeführt und über einen weiteren Wärmetauscher 15 geführt, um als Kaltluft in Schüttgutregeneratoren 4 und 6 zugeführt zu werden. Furthermore, air is supplied via the line 25 of the gas turbine 8 and passed through a further heat exchanger 15 to be supplied as cold air in bulk regenerators 4 and 6.
Durch Verwendung des Vergasers 1 kann auf eine aufwändige Entstaubung der Rauchgase 3 verzichtet werden. By using the carburetor 1 can be dispensed with an elaborate dedusting of the flue gases 3.
Das Bezugszeichen 61 kennzeichnet ein ventilartiges Mittel zwischen dem Verdichter und einem Entspanner der Gasturbine zum Ausschalten des Turbinenzweigs. Zwischen der Turbine und dem Wärmetauscher 15 ist eine Wassereinspeisung möglich. In diesem Zweig ist ein weiteres Ventil 63 vorgesehen. The reference numeral 61 designates a valve-like means between the compressor and a gas turbine engine expander for turning off the turbine branch. Between the turbine and the heat exchanger 15, a water supply is possible. In this branch, another valve 63 is provided.
In eine von der Gasturbine 8 führenden Leitung 26 sind Wärmetauscher 1 1 , 12 und 13 eingeschaltet, um sowohl Luft als auch Wasser als Vergasungsmittel dem Festbett- Gegenstrom-Reaktor 1 erhitzt zuzuführen. Zudem wird mittels mindestens eines Wärmetauschers 13 eine Abkühlung bewirkt und die durch die Abkühlung gewonnene thermische Energie als nutzbare Wärme ausgekoppelt. Bei der in Fig. 2 gezeigten Ausführungsform ist der Wärmetauscher 13 unmittelbar dem Turbinenzweig T nachgeschaltet. Mittels dieser Vorrichtung ist es möglich, die ausgekoppelte Wärme (zur Warmwassererzeugung) auf einem höheren Temperaturniveau zu nutzen. Die Wärmetauscher 1 1 , 12 zur Erhitzung von Luft und Wasser als Vergasungsmittel sind dabei nachgeschaltet. In one of the gas turbine 8 leading line 26 heat exchangers 1 1, 12 and 13 are turned on to supply heated both air and water as a gasification agent to the fixed bed countercurrent reactor 1. In addition, a cooling is effected by means of at least one heat exchanger 13 and the thermal energy obtained by the cooling is decoupled as usable heat. In the embodiment shown in FIG. 2, the heat exchanger 13 is directly downstream of the turbine branch T. By means of this device, it is possible to use the decoupled heat (for hot water production) at a higher temperature level. The heat exchanger 1 1, 12 for heating air and water as a gasification agent are connected downstream.
Damit ist in den beiden gezeigten Ausgestaltungen die Reihenfolge der Wärmetauscher geändert. Während bei der in Figur 1 gezeigten Ausführungsform der erste Wärmetauscher 12, welcher die Verbrennungsluft mit der höchsten Temperatur aufnimmt, zur Erzeugung von Heißluft dient, der nächste Wärmetauscher 1 1 zur Erzeugung von Sattdampf und der letzte Wärmetauscher 13 zur Erzeugung von Wärme, wird bei der in Figur 2 gezeigten Ausführungsform mit der heißesten Luft Wärme erzeugt und anschließend Heißluft beziehungsweise Sattdampf. Weiterhin wäre es auch möglich, die beiden Wärmetauscher 12 und 1 1 hinsichtlich ihrer Reihenfolge zu vertauschen. Das Bezugszeichen 58 in den beiden Figuren bezieht sich auf eine Pumpe zum Fördern von Wasser. Das Bezugszeichen 10 in den Figuren bezieht sich auf das Verbrennungsgas und das Bezugszeichen 9 bezeichnet den Sattdampf. Thus, the order of the heat exchangers is changed in the two embodiments shown. While in the embodiment shown in Figure 1, the first heat exchanger 12, which receives the combustion air with the highest temperature, for generating hot air, the next heat exchanger 1 1 for generating saturated steam and the last heat exchanger 13 for generating heat, is in the shown in Figure 2 with the hottest air generates heat and then hot air or saturated steam. Furthermore, it would also be possible to exchange the two heat exchangers 12 and 1 1 with respect to their order. The reference numeral 58 in the two figures refers to a pump for conveying water. The reference numeral 10 in the figures refers to the combustion gas and the reference numeral 9 designates the saturated steam.
Fig. 3 zeigt eine weitere Ausführungsform der vorliegenden Erfindung. Bei dieser Ausführungsform ist ein weiterer Kreislauf 70 vorgesehen, der der Gasturbine 8 nachgeschaltet ist. Genauer wird die Heißluft aus der Gasturbine 8 durch einen Wärmetauscher 71 geführt, der in diesen Kreislauf 70 integriert ist. Durch den Wärmetauscher wird Wasser des Kreislaufs 70 erhitzt und einer Dampfturbine 72 zugeführt, welche wiederum einen Generator 74 antreibt. Das Bezugszeichen 78 bezieht sich auf eine Pumpe und das Bezugszeichen 76 auf einen Kondensator. Durch diese Vorgehensweise kann die Stromausbeute der Anlage weiter erhöht werden. Fig. 3 shows another embodiment of the present invention. In this embodiment, a further circuit 70 is provided, which is connected downstream of the gas turbine 8. More specifically, the hot air from the gas turbine 8 is passed through a heat exchanger 71, which is integrated in this circuit 70. Through the heat exchanger, water of the circuit 70 is heated and fed to a steam turbine 72, which in turn drives a generator 74. The reference numeral 78 refers to a pump and the reference numeral 76 to a capacitor. By this procedure, the current efficiency of the system can be further increased.
Sämtliche in den Anmeldungsunterlagen offenbarten Merkmale werden als erfindungswesentlich beansprucht, sofern sie einzeln oder in Kombination gegenüber dem Stand der Technik neu sind. Bezugszeichenliste All disclosed in the application documents features are claimed as essential to the invention, provided they are new individually or in combination over the prior art. LIST OF REFERENCE NUMBERS
1 Vergaser 1 carburetor
2 Gasbrenner  2 gas burners
3 Rauchgase, Verbindungsleitung  3 flue gases, connecting line
4 Erste Einrichtung zum Speichern und zur Abgabe thermischer Energie 4 First device for storing and dispensing thermal energy
6 Zweite Einrichtung zum Speichern und zur Abgabe thermischer EnergieSecond means for storing and dispensing thermal energy
7 Heißluft, Verbindungsleitung 7 hot air, connecting line
8 Gasturbine  8 gas turbine
9 Sattdampf  9 saturated steam
10 Heißluft  10 hot air
1 1 , 12,  1 1, 12,
13, 15 Wärmetauscher  13, 15 heat exchangers
14 kohlenstoffhaltiger Rohstoff  14 carbonaceous raw material
16 Zuleitung für Vergasungsmittel  16 Supply line for gasification agent
21 , 22 Zuleitung zur Gasturbine  21, 22 Supply line to the gas turbine
25 Leitung  25 line
26 Zuleitung zu Wärmetauschern  26 Supply line to heat exchangers
32, 34, 36,  32, 34, 36,
38, 40, 42,  38, 40, 42,
44, 46 steuerbare Ventile  44, 46 controllable valves
52, 54, 56 Gebläse  52, 54, 56 blower
58, 78 Pumpe  58, 78 pump
60 Generator  60 generator
61 Ventil  61 valve
63 Ventil  63 valve
70 Kreislauf  70 cycle
71 Wärmetauscher  71 heat exchangers
72 Dampfturbine  72 steam turbine
74 Generator  74 generator
76 Kondensator  76 capacitor
P1 Richtungspfeil  P1 directional arrow
T Turbinenzweig  T turbine branch

Claims

Patentansprüche claims
1. Verfahren zur Umwandlung von thermischer Energie aus kohlenstoffhaltigen Rohstoffen in mechanische Arbeit mit wenigstens einer ersten (4) und einer zweiten (6) Einrichtung zum Speichern und zur Abgabe thermischer Energie, welche wenigstens zeitweise wechselweise in einen Turbinenzweig (T) mit einer nachgeschalteten Gasturbine (8) eingeschaltet werden, A method of converting thermal energy from carbonaceous raw materials into mechanical work having at least first (4) and second (6) means for storing and dispensing thermal energy alternating at least temporarily into a turbine branch (T) with a downstream gas turbine (8) are switched on,
mit folgenden Schritten:  with the following steps:
a) Verbrennen eines Gases in einem Gasbrenner (2),  a) burning a gas in a gas burner (2),
b) Durchleiten der in dem Gasbrenner (2) entstandenen Rauchgase (3) durch eine Einrichtung (4,6) zum Speichern thermischer Energie, und  b) passing the flue gases (3) produced in the gas burner (2) through a device (4, 6) for storing thermal energy, and
c) Einleiten der von wenigstens einer Einrichtung (4,6) abgegebenen Heißluft (7) in die Gasturbine (8),  c) introducing the hot air (7) emitted by at least one device (4, 6) into the gas turbine (8),
dadurch gekennzeichnet, dass  characterized in that
- in einem ersten Schritt eine Vergasung der kohlenstoffhaltigen Rohstoffe in einem Vergaser (1 ) erfolgt und  - In a first step, a gasification of the carbonaceous raw materials in a gasifier (1) takes place and
- das Produktgas dem Vergaser (1 ) nachgeschalteten Gasbrenner (2) zugeführt wird.  - The product gas to the gasifier (1) downstream gas burner (2) is supplied.
2. Verfahren nach Anspruch 1 , 2. The method according to claim 1,
dadurch gekennzeichnet, dass  characterized in that
erhitzter Wasserdampf (9) und/oder Luft in den Vergaser (1 ) eingeführt und zur Vergasung verwendet wird.  heated water vapor (9) and / or air is introduced into the gasifier (1) and used for gasification.
3. Verfahren nach Anspruch 2, 3. The method according to claim 2,
dadurch gekennzeichnet, dass  characterized in that
dem Vergaser (1 ) gemeinsam mit dem Wasserdampf (9) ein weiteres gasförmiges Medium als Verbrennungsgas (10) zugeführt wird.  the carburetor (1) together with the water vapor (9) a further gaseous medium as combustion gas (10) is supplied.
4. Verfahren nach wenigstens einem der vorangegangenen Ansprüche, 4. The method according to at least one of the preceding claims,
dadurch gekennzeichnet, dass als Vergaser (1) ein Festbett - Gegenstrom - Vergaser (1) verwendet wird. characterized in that as carburetor (1) a fixed bed countercurrent carburettor (1) is used.
5. Verfahren nach wenigstens einem der vorangegangenen Ansprüche, 5. The method according to at least one of the preceding claims,
dadurch gekennzeichnet, dass  characterized in that
die Abwärme aus wenigstens einem der Vergasung folgenden Prozesse für eine Sattdampferzeugung verwendet wird.  the waste heat from at least one of the gasification processes is used for saturated steam production.
6. Verfahren nach wenigstens einem der vorangegangenen Ansprüche, 6. The method according to at least one of the preceding claims,
dadurch gekennzeichnet, dass  characterized in that
Sattdampf (9) mittels eines der Gasturbine (8) nachgeschalteten Wärmetauschers (11) erzeugt wird, bevor er dem Vergaser (1) zugeführt wird.  Saturated steam (9) by means of a gas turbine (8) downstream heat exchanger (11) is generated before it is supplied to the gasifier (1).
7. Verfahren nach wenigstens einem der vorangegangenen Ansprüche, 7. The method according to at least one of the preceding claims,
dadurch gekennzeichnet, dass  characterized in that
mittels mindestens eines Wärmetauschers (13) eine Abkühlung bewirkt und die durch die Abkühlung gewonnene thermische Energie als nutzbare Wärme ausgekoppelt wird.  By means of at least one heat exchanger (13) causes a cooling and the thermal energy obtained by the cooling is decoupled as usable heat.
8. Verfahren nach wenigstens einem der vorangegangenen Ansprüche, 8. The method according to at least one of the preceding claims,
dadurch gekennzeichnet, dass  characterized in that
entspannte Heißluft aus der Gasturbine (8) dem Gasbrenner (2) erneut zugeführt wird.  relaxed hot air from the gas turbine (8) the gas burner (2) is supplied again.
9. Verfahren nach wenigstens einem der vorangegangenen Ansprüche, 9. The method according to at least one of the preceding claims,
dadurch gekennzeichnet, dass  characterized in that
mittels einer weiteren Dampfturbine (72) entspannte Heißluft aus der Gasturbine (8) zur Energieerzeugung verwendet wird.  by means of another steam turbine (72) relaxed hot air from the gas turbine (8) is used to generate energy.
10. Vorrichtung zur Umwandlung von thermischer Energie in mechanische Arbeit, wobei vorgesehen sind: 10. Device for converting thermal energy into mechanical work, wherein it is provided:
ein Gasbrenner (2) zum Verbrennen eines Brennstoffes; wenigstens eine erste (4) und eine zweite (6) Einrichtung zum Speichern thermischer Energie, welche wenigstens zeitweise wechselweise in einen Turbinenzweig (T) mit einer nachgeschalteten Gasturbine (8) einschaltbar sind und wenigstens eine Verbindungsleitung (3), welche in dem Gasbrenner (2) entstehende Rauchgase den Einrichtungen (4,6) zum Spei- ehern thermischer Energie zuführt; a gas burner (2) for burning a fuel; at least one first (4) and one second (6) device for storing thermal energy, which at least temporarily alternately in a turbine branch (T) with a downstream gas turbine (8) are switched on and at least one connecting line (3) which in the gas burner ( 2) resulting flue gases to the facilities (4,6) for storage to supply thermal energy;
dadurch gekennzeichnet, dass  characterized in that
dem Gasbrenner (2) ein Vergaser (1 ) zum Umwandeln des Brenngases vorgeschaltet ist.  the gas burner (2) is preceded by a carburetor (1) for converting the fuel gas.
1 1 . Vorrichtung nach Anspruch 9, 1 1. Device according to claim 9,
dadurch gekennzeichnet, dass  characterized in that
dem Turbinenzweig (T) nachgeschaltete Mittel (1 1 ,12,13) zum Abkühlen eines Gases vorgesehen sind,  the turbine branch (T) downstream means (1 1, 12, 13) are provided for cooling a gas,
12. Vorrichtung nach wenigstens einem der Ansprüche 9 oder 10, 12. Device according to at least one of claims 9 or 10,
dadurch gekennzeichnet, dass  characterized in that
ein Mittel zum wechselweisen Einschalten wenigstens einer ersten Einrichtung (4) zum Speichern thermischer Energie und wenigstens einer zweiten Einrichtung (6) zum Speichern thermischer Energie in den Turbinenzweig (T) vorgesehen ist.  a means for alternately switching on at least one first means (4) for storing thermal energy and at least one second means (6) for storing thermal energy in the turbine branch (T) is provided.
13. Vorrichtung nach Anspruch 9, 13. Device according to claim 9,
dadurch gekennzeichnet, dass  characterized in that
der Gasturbine (8) mindestens ein Wärmetauscher (1 1 ,12,13) nachgeschaltet ist.  the gas turbine (8) at least one heat exchanger (1 1, 12,13) is connected downstream.
14. Vorrichtung nach Anspruch 9, 14. Device according to claim 9,
dadurch gekennzeichnet, dass  characterized in that
zwischen die Gasturbine (8) und den Vergaser (1 ) mindestens ein Wärmetauscher (13) zur Auskopplung thermischer Energie eingeschaltet ist.  between the gas turbine (8) and the carburetor (1) at least one heat exchanger (13) for decoupling thermal energy is switched on.
15. Vorrichtung nach wenigstens einem der vorangegangenen Ansprüche 9 - 14, 15. Device according to at least one of the preceding claims 9 - 14,
dadurch gekennzeichnet, dass  characterized in that
der Gasturbine (8) ein Dampfturbinenprozess nachgeschaltet ist.  the gas turbine (8) is followed by a steam turbine process.
EP10745200A 2009-08-21 2010-08-12 Method and device for utilizing biomass Withdrawn EP2467588A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102009038323A DE102009038323A1 (en) 2009-08-21 2009-08-21 Process and device for the utilization of biomass
PCT/EP2010/061753 WO2011020767A1 (en) 2009-08-21 2010-08-12 Method and device for utilizing biomass

Publications (1)

Publication Number Publication Date
EP2467588A1 true EP2467588A1 (en) 2012-06-27

Family

ID=43038095

Family Applications (1)

Application Number Title Priority Date Filing Date
EP10745200A Withdrawn EP2467588A1 (en) 2009-08-21 2010-08-12 Method and device for utilizing biomass

Country Status (12)

Country Link
US (1) US8621872B2 (en)
EP (1) EP2467588A1 (en)
JP (1) JP5580897B2 (en)
CN (1) CN102482996B (en)
AU (1) AU2010285055B2 (en)
BR (1) BR112012003584A2 (en)
CA (1) CA2771145A1 (en)
DE (1) DE102009038323A1 (en)
EA (1) EA201290057A1 (en)
NZ (1) NZ598329A (en)
UA (1) UA107196C2 (en)
WO (1) WO2011020767A1 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6057775B2 (en) * 2013-02-26 2017-01-11 三菱日立パワーシステムズ株式会社 Gas turbine plant and control method thereof
DE102013017010A1 (en) * 2013-10-14 2015-04-16 Karl Brotzmann Consulting Gmbh Power storage via thermal storage and air turbine
WO2015071697A1 (en) * 2013-11-15 2015-05-21 Apeiron Technology Incorporation Gasifier for the production of synthesis gas
DE102014103952A1 (en) * 2014-03-21 2015-09-24 Krones Ag Apparatus and method for operating a gas turbine with direct feed of this gas turbine
DE102014017346A1 (en) * 2014-10-17 2016-04-21 Carbon-Clean Technologies Gmbh Method and storage power plant to compensate for load peaks in energy production and / or for the generation of electrical energy
JP2021088977A (en) * 2019-12-05 2021-06-10 株式会社Ihi Waste heat storage system
DE102021108719A1 (en) 2021-04-08 2022-10-13 HiTES Holding GmbH Process and device for converting the chemical energy of a fuel into heat and electrical energy

Family Cites Families (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2443362B2 (en) 1974-09-11 1978-11-30 Motoren- Und Turbinen-Union Muenchen Gmbh, 8000 Muenchen Gas turbine engine with a heat exchanger system
CH601651A5 (en) 1975-05-14 1978-07-14 Bbc Brown Boveri & Cie
EP0132452A1 (en) 1983-07-28 1985-02-13 Harald F. Dr. Funk Method and device for a hot gas process, especially for a gas turbine
US4667467A (en) * 1985-06-04 1987-05-26 Westinghouse Electric Corp. Method for energy conversion
DE3931582A1 (en) * 1989-09-22 1991-04-04 Krantz Gmbh Energieplanung H Gas-turbine waste-heat utilisation - involves feeding turbine outlet air and cooled exhaust to waste-heat boiler
US5069685A (en) * 1990-08-03 1991-12-03 The United States Of America As Represented By The United States Department Of Energy Two-stage coal gasification and desulfurization apparatus
JPH08501605A (en) * 1992-05-29 1996-02-20 クワエネル パルピング テクノロイース アーベー Energy recovery method from combustible gas
AU2321092A (en) * 1992-05-29 1993-12-30 Chemrec Aktiebolag A process for recovering energy from a combustible gas
DE4236619C2 (en) 1992-10-29 1996-11-28 Air Liquide Process and regenerator for heating gases
DE4238652C1 (en) 1992-11-16 1994-05-11 Air Liquide Regenerator for heating gases
AT409405B (en) * 1993-11-12 2002-08-26 Werner Dipl Ing Schaller PLANT FOR THE PRODUCTION OF ELECTRICAL ENERGY FROM FUELS, ESPECIALLY FROM BIOGENIC FUELS
DE4342165C1 (en) * 1993-12-10 1995-05-11 Umwelt & Energietech Process for the utilisation of biomass energy
JPH07286186A (en) * 1994-04-20 1995-10-31 Hitachi Ltd Coal gasification power generation plant
US5643354A (en) 1995-04-06 1997-07-01 Air Products And Chemicals, Inc. High temperature oxygen production for ironmaking processes
US6032456A (en) 1995-04-07 2000-03-07 Lsr Technologies, Inc Power generating gasification cycle employing first and second heat exchangers
SE507116C2 (en) * 1995-12-11 1998-03-30 Abb Carbon Ab Carburetor and power plant
US5706645A (en) * 1996-04-10 1998-01-13 The United States Of America As Represented By The United States Department Of Energy Removal of oxides of nitrogen from gases in multi-stage coal combustion
AU3512399A (en) * 1998-04-28 1999-11-16 Bruno Berger Waste to energy method for producing electricity, water and/or hydrogen and/or methanol from biomass and/or organic waste
DE19836428C2 (en) 1998-08-12 2000-07-13 Siempelkamp Guss Und Anlagente Processes and devices for gasifying biomass, in particular wood materials
DE10039246C2 (en) * 2000-08-11 2002-06-13 Atz Evus Process for converting thermal energy into mechanical work
US6430915B1 (en) * 2000-08-31 2002-08-13 Siemens Westinghouse Power Corporation Flow balanced gas turbine power plant
US7189270B2 (en) 2001-12-10 2007-03-13 Gas Technology Institute Method and apparatus for gasification-based power generation
DE10227074A1 (en) 2002-06-17 2004-01-15 Clausthaler Umwelttechnikinstitut Gmbh, (Cutec-Institut) Process for gasifying biomass and plant therefor
WO2004027220A1 (en) * 2002-09-17 2004-04-01 Foster Wheeler Energy Corporation Advanced hybrid coal gasification cycle utilizing a recycled working fluid
DE102004045772A1 (en) * 2004-09-15 2006-03-16 Zentrum für Sonnenenergie- und Wasserstoff-Forschung Baden-Württemberg Preparation of product gas, useful e.g. as gaseous fuel, comprises low temperature gasification of carbon containing material in presence of absorber materials to give tar poor product gas, and regeneration of absorber material
DE202004017725U1 (en) * 2004-11-15 2005-02-03 Franke, Berndt, Prof. Dr.-Ing. habil. Power and heat generation plant fueled from biomass digestion, includes gas conditioning equipment, combustor and gas-air heat exchanger with air- and steam turbine generator sets
DE202005018849U1 (en) * 2005-12-01 2006-03-09 Franke, Berndt, Prof. Dr.-Ing. habil. Plant and device for conversion of fuel energy of renewable raw materials into useful energy has solid matter combustion unit to which is connected surface heat exchanger for utilization of flue gas enthalpy
DE102006061583A1 (en) * 2006-12-27 2008-07-03 Achim Solbach Pressurized combustion chamber integrated into gas turbine plant for power generation, combines gasification, main and secondary firing, coke combustion and waste heat recovery
DE102007024312B4 (en) * 2007-05-24 2009-04-30 Lurgi Gmbh Method and apparatus for producing reducing gas and / or fuel gas for the direct reduction of iron ore
US20090025396A1 (en) * 2007-07-24 2009-01-29 General Electric Company Parallel turbine fuel control valves
DE102007050566A1 (en) * 2007-10-23 2009-05-07 Stevanović, Dragan, Dr. Carbonic raw material e.g. coal, gasifying method, involves using superheated water vapor as gasification agent and energy carrier for gasification reaction at temperature above specified degree Celsius
DE102008014297A1 (en) * 2007-11-16 2009-05-20 Krones Ag Converting carbon-containing raw materials such as biomass into liquid fuels for internal combustion engines, comprises allothermically gasifying the raw materials in a fixed bed counter-flow gasifier by introducing heated water steam
NZ587568A (en) * 2008-02-28 2012-11-30 Krones Ag Method and device for converting carbonaceous raw materials

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2011020767A1 *

Also Published As

Publication number Publication date
CN102482996B (en) 2014-10-29
AU2010285055A1 (en) 2012-03-15
CA2771145A1 (en) 2011-02-24
JP5580897B2 (en) 2014-08-27
AU2010285055B2 (en) 2016-07-14
UA107196C2 (en) 2014-12-10
US8621872B2 (en) 2014-01-07
DE102009038323A1 (en) 2011-02-24
CN102482996A (en) 2012-05-30
JP2013502526A (en) 2013-01-24
WO2011020767A1 (en) 2011-02-24
BR112012003584A2 (en) 2016-03-15
NZ598329A (en) 2014-08-29
EA201290057A1 (en) 2012-08-30
US20120137702A1 (en) 2012-06-07

Similar Documents

Publication Publication Date Title
DE69918492T2 (en) Turbine à gaz à chauffage indirect integree à une une un separation of the gaz de l'air
EP0518868B1 (en) Process and device for generating mechanical energy
EP1307641B1 (en) Method and device for converting thermal energy into mechanical work
EP2467588A1 (en) Method and device for utilizing biomass
DE2743830C2 (en) Method for operating a combined gas-steam power plant and gas-steam power plant for carrying out the method
EP2467589A1 (en) Method and device for converting thermal energy from biomass into mechanical work
EP2167794B1 (en) Device and method for the generation of power heat
DE102018201172A1 (en) Incinerator with residual heat utilization
DE102009012668A1 (en) Process and plant for the utilization of biomass
WO2016102231A1 (en) Device and method for thermal exhaust gas cleaning
EP0086261A1 (en) Combination of a gas-turbine and steam-turbine cycle
WO1992021859A1 (en) Environmentally acceptable electric energy generation process and plant
WO2004003348A1 (en) Steam power plant
EP1658418A1 (en) Steam power plant
DE202004017725U1 (en) Power and heat generation plant fueled from biomass digestion, includes gas conditioning equipment, combustor and gas-air heat exchanger with air- and steam turbine generator sets
DE19718184C2 (en) Device for the energetic use of fuels, in particular biofuels
WO2012095288A1 (en) Method for producing fuel gas and raw synthesis gas
DE102019111827B4 (en) Method for operating a pyrolysis plant and pyrolysis plant
EP0651853B1 (en) Method and device for the operation of a combined-process power station
DE102014202190A1 (en) Method and device for generating electrical energy by gasification of solids, in particular biomass
DE102004050465B3 (en) Fluid heating/vaporizing method for driving gas turbine`s power generation device, involves passing hot gas with dust via regenerators to hold dust in one regenerator, and passing cold and pure gas via other regenerator to form hot pure gas
DE2933402C2 (en) Process and plant for the production of carbonization gas, water gas and coke from solid fuels
BE1030687B1 (en) CO2-free production of artificial pozzolans, especially from clays
EP2510199A1 (en) Method and device for combusting carbonaceous materials
AT502147B1 (en) METHOD FOR THE CATALYTIC CONVERTING OF SLUDGE SLUDGE

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20120319

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

DAX Request for extension of the european patent (deleted)
17Q First examination report despatched

Effective date: 20160615

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20161026