EP2589870A1 - Updraft gasifier comprising a grate - Google Patents
Updraft gasifier comprising a grate Download PDFInfo
- Publication number
- EP2589870A1 EP2589870A1 EP11187993.8A EP11187993A EP2589870A1 EP 2589870 A1 EP2589870 A1 EP 2589870A1 EP 11187993 A EP11187993 A EP 11187993A EP 2589870 A1 EP2589870 A1 EP 2589870A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- gasifier
- grate
- ash
- updraft
- air channel
- 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- Withdrawn
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/34—Grates; Mechanical ash-removing devices
- C10J3/40—Movable grates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/22—Arrangements or dispositions of valves or flues
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/32—Devices for distributing fuel evenly over the bed or for stirring up the fuel bed
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23H—GRATES; CLEANING OR RAKING GRATES
- F23H13/00—Grates not covered by any of groups F23H1/00-F23H11/00
- F23H13/08—Grates specially adapted for gas generators and also applicable to furnaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23H—GRATES; CLEANING OR RAKING GRATES
- F23H3/00—Grates with hollow bars
- F23H3/02—Grates with hollow bars internally cooled
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23H—GRATES; CLEANING OR RAKING GRATES
- F23H9/00—Revolving-grates; Rocking or shaking grates
- F23H9/04—Grates rocked as a whole
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/152—Nozzles or lances for introducing gas, liquids or suspensions
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/0916—Biomass
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0956—Air or oxygen enriched air
Definitions
- the invention relates to an updraft gasifier for a biomass gasification system to generate gasifier product gas to be burned in a combustion unit, which gasifier comprises:
- the document WO 2007/081296 A1 discloses a cross draft gasifier for biomass that uses a downdraft and an updraft mode to produce gasifier product gas, which can be burned in a combustion unit.
- the disclosed gasifier comprises a first inlet for municipal waste in the upper area of the gasifier and a first outlet of the gasifier for the ash at the bottom of the gasifier.
- the gasifier furthermore comprises a second inlet for preheated air or oxygen with nozzles in the wall of the lower area of the gasifier and a second outlet in the wall of the upper area of the gasifier for syngas as gasifier product gas generated in the gasifier.
- a fix mounted ash grate made of special material which is high temperature resistant is used to enable that the syngas in the accumulated ash content in this portion can be sucked easily in the updraft mode.
- This known gasifier processed in the downdraft mode comprises the disadvantage that the gasification agent is not well distributed into the ash and biomass by the nozzles in the wall of the gasifier. Due to the unequal distribution of the gasification agent hot zones are created that cause ash melting and ash agglomeration what finally can lead to blocking of the gasifier.
- a gasifier according to the invention is characterized in, that the grate is arranged in a cross-sectional area of the gasifier and comprises at least one air channel connected to the second inlet and at least one nozzle connected to the air channel to transport the gasification agent into the cross-sectional area of the gasifier.
- the updraft gasifier according to the invention comprises the advantage that the gasification agent is distributed by at least one, but preferable several nozzles, arranged at the grate in the cross-sectional area of the gasifier.
- the grate comprises a moving scraper with an air channel and nozzles to distribute the gasification agent. Due to the movement of the scraper, the position of the nozzles changes over time what ensures a smooth and even distribution of the gasification agent within the ash and biomass. Furthermore, the flow of the gasification agent through the air channel and nozzles of the scraper advantageously cools the temperature of the scraper.
- FIG 1 is a perspective view and Figure 2 is a side view of a Stirling plant 1 to generate heat and electricity from biomass.
- the Stirling plant 1 comprises a biomass gasification system 2 to generate heat, which heat to some extent is transformed into electricity by four Stirling engines 3.
- the biomass gasification system 2 comprises an updraft gasifier 4, from which gasifier product gas is transported through pipes 5 to four combustion units 6 where the gasifier product gas is burnt to heat up a transfer medium used to drive the Stirling engines 3.
- FIG 3 is a perspective view of the gasifier 4 of the biomass gasification system 2.
- the gasifier 4 is built as updraft gasifier.
- the updraft gasifier is a standing tubular reactor 7 which consists essentially out of cylindrical steel shell isolated and lined with bricks on the inner side. Additional the reactor 7 is isolated on the outer side as well, to avoid hot surfaces.
- the gasifier 4 comprises a wood chip conveyor 8 connected to a first inlet 9 of the gasifier 4 as fuel feed and an ash conveyer 10 connected to a first outlet 11 of the gasifier 4 as fuel discharge.
- the wood chip conveyor 8 feeds the gasifier 4 through the lateral first inlet 9 which is arranged in the upper area 12 of the gasifier 4.
- the feeding is monitored by a filling level indicator.
- the filling level indicator consists out of a rotating blade in the filling space mounted on a geared motor. The filling level is periodically checked and if necessary the fuel feed activated.
- the gasification in the updraft gasifier 4 takes place in a counterflow principle, thereby the fuel passes the gasifier 4 from its upper area 12 to its lower area 13, while the gasification agent enters the gasifier 4 at a second inlet 14 at the bottom of the gasifier 4 and leaves the gasifier 4 as gasification product gas (syngas) at a second outlet 15 in the upper area 12 of the gasifier 4.
- gasification product gas gas (syngas)
- different zones are formed in the gasifier 4. Basically four zones are formed, the drying zone, the pyrolysis zone, the reduction zone and the oxidation zone.
- a gasification agent a defined mixture of flue gas and air is used.
- the gasification agent is preheated in a gas pre-heater of the biomass gasification system 2 and afterwards fed at the second inlet 14 at the bottom of the gasifier 4.
- the updraft gasifier 4 furthermore comprises a grate 16 that is arranged in the cross-sectional area of the gasifier 4 at the bottom of the gasifier 4 just above the first outlet 11 to handle and thereby discard the ash.
- Figure 4 is a sectional view and top view of the grate 16 in the gasifier 4.
- the grate 16 comprises an air channel 17 connected to the second inlet 14 to transport the gasification agent through the grate 16.
- the grate 16 furthermore comprises a scraper 18 realized by eight hollow triangle shaped profile elements 19 fixed to the air channel 17.
- the profile elements 19 comprise openings 20 functioning as nozzles to enable a flow of the gasification agent from the second inlet 14 through the air channel 17 and the profile elements 19 into the lower area 13 of the gasifier 4.
- the gasification agent is distributed through the openings 20 more or less equally over the cross-sectional area of the gasifier 4 into the ash and biomass within the gasifier 4.
- the creation of hot zones which may cause ash melting and ash agglomeration what finally can lead to blocking of the gasifier 4 is avoided.
- the updraft gasifier 4 furthermore comprises a grate drive 21 connected to a connection element 22 of the air channel 17.
- the grate drive 21 periodically moves the air channel 17 and the scraper 18 fixed to the air channel 17. This provides the advantage that the ash is moved by the scraper 18 into the ash conveyer not shown in Figure 4 .
- this movement of the scraper 18 with the openings 20 provides the advantage that the position of the openings 20 changes over time what enables that the gasification agent gets even better distributed into the ash and biomass.
- FIG. 5 is a sectional and top view of a grate 23 in a gasifier according to a second embodiment of the invention.
- the grate 23 could be attached to the bottom of the updraft gasifier 4 and would push the ash within the gasifier 4 into a screw drive 24 connected to the first outlet 11 to discharge the ash into the ash conveyor 10.
- the grate 23 comprises an air channel with a ring channel area 25 that is connected to the second inlet 14. Eight smaller air channels 26 are connected to the ring channel area 25, which air channels 26 are spread over the cross-sectional area of the gasifier 4. Each of these air channels 26 comprises several nozzles to distribute the gasification agent.
- the nozzles are shielded by covers 27. This has the advantage that the maintenance work to keep the distribution of the gasification agent through the nozzles functional is reduced.
- the grate 23 furthermore comprises two movable scrapers 28, each connected to a scraper drive 29. With the movement of the scrapers 28, ash is moved from the bottom of the gasifier 4 into the screw drive 24 to discharge the ash.
- the scrapers 28 do not comprises air channels to discharge the gasifier agent which gets distributed through the fixed nozzles only. This provides the advantage that the scrapers 28 are robust and easy manufactured.
- the air channel 25 of the grate 23 furthermore comprises two cleanouts 30. These cleanouts 30 are closed during normal production of the gasifier product gas and may be opened by a service personal to enable cleaning of the air channels 25 and 26. These cleanouts 30 provide the advantage that the air channels of the grate 23 may be kept clean and fully functional.
- the screw drive 24 in the gasifier 4 as part of the ash conveyer comprises an air channel 31 and nozzles 32 as well.
- These nozzles 32 advantageously add to the equal distribution of the gasifier agent into the ash and biomass. But it has to be stated that in a less preferred embodiment the invention works without these elements 31 and 32 as well. Furthermore there could be other ways to connect the air channel 31 with the nozzles 32 as shown in Figure 5 .
- the grate could comprise all kind of different air channels and types of nozzles to distribute the gasifier agent.
- the scraper may be fixed, but preferable is movable to transport the ash into the ash conveyer.
- the air channel could comprise the form of a square or rectangle or any other from that might have advantages for the particular realization.
- the air channel functions as a manifold system to transport the gasification agent to the nozzles.
- the first embodiment of a grate 16 according to Figure 4 comprises only movable nozzles 20 in the profile elements 19 and the second embodiment of a grate 23 according to Figure 5 comprises only fixed nozzles in the air channels 26.
- the grate comprises fixed and movable nozzles to achieve the advantage that the gasification agent gets distributed through the fixed nozzles and the nozzles of the movable scrapers. This ensures an equal distribution of the gasification agent into the ash and biomass.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
• a first inlet (9) for biomass in the upper area (12) of the gasifier (4), and
• a first outlet (11) for ash in the lower area (13) of the gasifier (4), and
• a second inlet (14) for a gasification agent in the lower area (13) of the gasifier (4), and
• a second outlet (15) for the gasifier product gas in the upper area (12) of the gasifier (4), and
• a grate (16; 23) between the first inlet (9) and the first outlet (11) to handle the ash;
wherein the
• grate (16; 23) is arranged in a cross-sectional area of the gasifier (4) and comprises at least one air channel (17; 25, 26, 31) connected to the second inlet (14) and at least one nozzle (20; 32) connected to the air channel (17; 25, 26, 31) to transport the gasification agent into the cross-sectional area of the gasifier (4).
Description
- The invention relates to an updraft gasifier for a biomass gasification system to generate gasifier product gas to be burned in a combustion unit, which gasifier comprises:
- a first inlet for biomass in the upper area of the gasifier, and
- a first outlet for ash in the lower area of the gasifier, and
- a second inlet for a gasification agent in the lower area of the gasifier, and
- a second outlet for the gasifier product gas in the upper area of the gasifier, and
- a grate between the first inlet and the first outlet to handle the ash.
- The document
WO 2007/081296 A1 discloses a cross draft gasifier for biomass that uses a downdraft and an updraft mode to produce gasifier product gas, which can be burned in a combustion unit. The disclosed gasifier comprises a first inlet for municipal waste in the upper area of the gasifier and a first outlet of the gasifier for the ash at the bottom of the gasifier. The gasifier furthermore comprises a second inlet for preheated air or oxygen with nozzles in the wall of the lower area of the gasifier and a second outlet in the wall of the upper area of the gasifier for syngas as gasifier product gas generated in the gasifier. A fix mounted ash grate made of special material which is high temperature resistant is used to enable that the syngas in the accumulated ash content in this portion can be sucked easily in the updraft mode. - This known gasifier processed in the downdraft mode comprises the disadvantage that the gasification agent is not well distributed into the ash and biomass by the nozzles in the wall of the gasifier. Due to the unequal distribution of the gasification agent hot zones are created that cause ash melting and ash agglomeration what finally can lead to blocking of the gasifier.
- Thus in view of the foregoing it is desirable to have an improved biomass gasifier that ensures an even distribution of the gasification agent into the ash and biomass. To solve this problem a gasifier according to the invention is characterized in, that the grate is arranged in a cross-sectional area of the gasifier and comprises at least one air channel connected to the second inlet and at least one nozzle connected to the air channel to transport the gasification agent into the cross-sectional area of the gasifier.
- The updraft gasifier according to the invention comprises the advantage that the gasification agent is distributed by at least one, but preferable several nozzles, arranged at the grate in the cross-sectional area of the gasifier. In a preferred embodiment the grate comprises a moving scraper with an air channel and nozzles to distribute the gasification agent. Due to the movement of the scraper, the position of the nozzles changes over time what ensures a smooth and even distribution of the gasification agent within the ash and biomass. Furthermore, the flow of the gasification agent through the air channel and nozzles of the scraper advantageously cools the temperature of the scraper. These and other advantages of the invention will be explained based on to embodiments of the invention.
-
Figure 1 is a perspective view of a Stirling plant with the preferred biomass gasifier of this invention. -
Figure 2 is a side view of the Stirling plant ofFigure 1 . -
Figure 3 is a perspective view of the gasifier of the Stirling plant ofFigure 1 . -
Figure 4 is a sectional view and top view of a grate within a gasifier ofFigure 3 . -
Figure 5 is a sectional view and top view of a grate according to a second embodiment of the invention. -
Figure 1 is a perspective view andFigure 2 is a side view of a Stirling plant 1 to generate heat and electricity from biomass. The Stirling plant 1 comprises abiomass gasification system 2 to generate heat, which heat to some extent is transformed into electricity by four Stirlingengines 3. Thebiomass gasification system 2 comprises anupdraft gasifier 4, from which gasifier product gas is transported throughpipes 5 to fourcombustion units 6 where the gasifier product gas is burnt to heat up a transfer medium used to drive the Stirlingengines 3. -
Figure 3 is a perspective view of thegasifier 4 of thebiomass gasification system 2. Thegasifier 4 is built as updraft gasifier. In principle the updraft gasifier is a standingtubular reactor 7 which consists essentially out of cylindrical steel shell isolated and lined with bricks on the inner side. Additional thereactor 7 is isolated on the outer side as well, to avoid hot surfaces. Thegasifier 4 comprises awood chip conveyor 8 connected to afirst inlet 9 of thegasifier 4 as fuel feed and anash conveyer 10 connected to afirst outlet 11 of thegasifier 4 as fuel discharge. - The
wood chip conveyor 8 feeds thegasifier 4 through the lateralfirst inlet 9 which is arranged in theupper area 12 of thegasifier 4. The feeding is monitored by a filling level indicator. The filling level indicator consists out of a rotating blade in the filling space mounted on a geared motor. The filling level is periodically checked and if necessary the fuel feed activated. - The gasification in the
updraft gasifier 4 takes place in a counterflow principle, thereby the fuel passes thegasifier 4 from itsupper area 12 to itslower area 13, while the gasification agent enters thegasifier 4 at asecond inlet 14 at the bottom of thegasifier 4 and leaves thegasifier 4 as gasification product gas (syngas) at asecond outlet 15 in theupper area 12 of thegasifier 4. Thereby different zones are formed in thegasifier 4. Basically four zones are formed, the drying zone, the pyrolysis zone, the reduction zone and the oxidation zone. As a gasification agent, a defined mixture of flue gas and air is used. The gasification agent is preheated in a gas pre-heater of thebiomass gasification system 2 and afterwards fed at thesecond inlet 14 at the bottom of thegasifier 4. - The
updraft gasifier 4 furthermore comprises agrate 16 that is arranged in the cross-sectional area of thegasifier 4 at the bottom of thegasifier 4 just above thefirst outlet 11 to handle and thereby discard the ash.Figure 4 is a sectional view and top view of thegrate 16 in thegasifier 4. Thegrate 16 comprises anair channel 17 connected to thesecond inlet 14 to transport the gasification agent through thegrate 16. Thegrate 16 furthermore comprises ascraper 18 realized by eight hollow triangle shapedprofile elements 19 fixed to theair channel 17. Theprofile elements 19 compriseopenings 20 functioning as nozzles to enable a flow of the gasification agent from thesecond inlet 14 through theair channel 17 and theprofile elements 19 into thelower area 13 of thegasifier 4. - As a result the advantage is achieved, that the gasification agent is distributed through the
openings 20 more or less equally over the cross-sectional area of thegasifier 4 into the ash and biomass within thegasifier 4. The creation of hot zones which may cause ash melting and ash agglomeration what finally can lead to blocking of thegasifier 4 is avoided. - The
updraft gasifier 4 furthermore comprises agrate drive 21 connected to aconnection element 22 of theair channel 17. Thegrate drive 21 periodically moves theair channel 17 and thescraper 18 fixed to theair channel 17. This provides the advantage that the ash is moved by thescraper 18 into the ash conveyer not shown inFigure 4 . In addition, this movement of thescraper 18 with theopenings 20 provides the advantage that the position of theopenings 20 changes over time what enables that the gasification agent gets even better distributed into the ash and biomass. -
Figure 5 is a sectional and top view of agrate 23 in a gasifier according to a second embodiment of the invention. Thegrate 23 could be attached to the bottom of theupdraft gasifier 4 and would push the ash within thegasifier 4 into ascrew drive 24 connected to thefirst outlet 11 to discharge the ash into theash conveyor 10. Thegrate 23 comprises an air channel with aring channel area 25 that is connected to thesecond inlet 14. Eightsmaller air channels 26 are connected to thering channel area 25, whichair channels 26 are spread over the cross-sectional area of thegasifier 4. Each of theseair channels 26 comprises several nozzles to distribute the gasification agent. - To avoid plugging of these nozzles with ash, the nozzles are shielded by
covers 27. This has the advantage that the maintenance work to keep the distribution of the gasification agent through the nozzles functional is reduced. - The
grate 23 furthermore comprises twomovable scrapers 28, each connected to ascraper drive 29. With the movement of thescrapers 28, ash is moved from the bottom of thegasifier 4 into thescrew drive 24 to discharge the ash. In this embodiment thescrapers 28 do not comprises air channels to discharge the gasifier agent which gets distributed through the fixed nozzles only. This provides the advantage that thescrapers 28 are robust and easy manufactured. - The
air channel 25 of thegrate 23 furthermore comprises twocleanouts 30. Thesecleanouts 30 are closed during normal production of the gasifier product gas and may be opened by a service personal to enable cleaning of the 25 and 26. Theseair channels cleanouts 30 provide the advantage that the air channels of thegrate 23 may be kept clean and fully functional. - The
screw drive 24 in thegasifier 4 as part of the ash conveyer comprises anair channel 31 andnozzles 32 as well. Thesenozzles 32 advantageously add to the equal distribution of the gasifier agent into the ash and biomass. But it has to be stated that in a less preferred embodiment the invention works without these 31 and 32 as well. Furthermore there could be other ways to connect theelements air channel 31 with thenozzles 32 as shown inFigure 5 . - In another embodiment of the invention, the grate could comprise all kind of different air channels and types of nozzles to distribute the gasifier agent. The scraper may be fixed, but preferable is movable to transport the ash into the ash conveyer.
- In another embodiment the air channel could comprise the form of a square or rectangle or any other from that might have advantages for the particular realization. In principle the air channel functions as a manifold system to transport the gasification agent to the nozzles.
- The first embodiment of a
grate 16 according toFigure 4 comprises onlymovable nozzles 20 in theprofile elements 19 and the second embodiment of agrate 23 according toFigure 5 comprises only fixed nozzles in theair channels 26. In a preferred embodiment the grate comprises fixed and movable nozzles to achieve the advantage that the gasification agent gets distributed through the fixed nozzles and the nozzles of the movable scrapers. This ensures an equal distribution of the gasification agent into the ash and biomass.
Claims (9)
- Updraft gasifier (4) for a biomass gasification system (2) to generate gasifier product gas to be burned in a combustion unit (6), which gasifier (4) comprises:• a first inlet (9) for biomass in the upper area (12) of the gasifier (4), and• a first outlet (11) for ash in the lower area (13) of the gasifier (4), and• a second inlet (14) for a gasification agent in the lower area (13) of the gasifier (4), and• a second outlet (15) for the gasifier product gas in the upper area (12) of the gasifier (4), and• a grate (16; 23) between the first inlet (9) and the first outlet (11) to handle the ash;characterized in, that the• grate (16; 23) is arranged in a cross-sectional area of the gasifier (4) and comprises at least one air channel (17; 25, 26, 31) connected to the second inlet (14) and at least one nozzle (20; 32) connected to the air channel (17; 25, 26, 31) to transport the gasification agent into the cross-sectional area of the gasifier (4).
- Updraft gasifier (4) of claim 1 characterized in, that the air channel comprises a manifold system and in particular a ring channel area (25) to distribute the gasification agent to at least two nozzles (32) of the grate (23).
- Updraft gasifier (4) according to any of the preceding claims characterized in, that the updraft gasifier (4) comprises a grate drive (29) to periodically move a scraper (18; 28) of the grate (16; 23) to transport ash into an ash conveyer (24) connected to the first outlet (11) of the gasifier (4).
- Updraft gasifier (4) according to claim 3 characterized in, that the movable scraper (18; 28) comprises at least one nozzle (20) connected to the air channel (17; 25).
- Updraft gasifier (4) according to claim 3 characterized in, that the ash conveyer (24) within the gasifier (4) comprises at least one nozzle (32) connected to the air channel (25, 31).
- Updraft gasifier (4) according to any of the preceding claims characterized in, that the air channel (25) comprises at least one cleanout (30).
- Updraft gasifier (4) according to any of the preceding claims characterized in, that the nozzles are shielded by a cover (27) to avoid plugging with ash.
- Grate (16; 23) for an updraft gasifier (4) of a biomass gasification system (2) to generate gasifier product gas to be burned in a combustion unit (6), characterized in that the grate (16; 23) comprises the features characterized in the preceding claims.
- Stirling plant (1) to generate heat and/or electricity from biomass which plant (1) comprises at least one Stirling motor (3) to transform heat into electricity, characterized in, that the plant (1) comprises the updraft gasifier (4) according to any of the claims 1 to 7.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP11187993.8A EP2589870A1 (en) | 2011-11-07 | 2011-11-07 | Updraft gasifier comprising a grate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP11187993.8A EP2589870A1 (en) | 2011-11-07 | 2011-11-07 | Updraft gasifier comprising a grate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP2589870A1 true EP2589870A1 (en) | 2013-05-08 |
Family
ID=44925395
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP11187993.8A Withdrawn EP2589870A1 (en) | 2011-11-07 | 2011-11-07 | Updraft gasifier comprising a grate |
Country Status (1)
| Country | Link |
|---|---|
| EP (1) | EP2589870A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101721823B1 (en) | 2015-11-06 | 2017-04-10 | 정동규 | Updraft gasification reactor using combustable waste and biomass resources |
| WO2020065008A1 (en) | 2018-09-27 | 2020-04-02 | Wieslaw Wilczynski | A system for heating a head of a stirling engine |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB209211A (en) * | 1922-10-13 | 1924-01-10 | George Herbert Bentley | Improvements in gas producers and the like |
| US3841851A (en) * | 1974-02-12 | 1974-10-15 | E Kaiser | Process and apparatus for the gasification of organic matter |
| US4154582A (en) * | 1977-08-01 | 1979-05-15 | General Electric Company | Method of solids discharge from coal gasifier grate |
| US20020069798A1 (en) * | 2000-09-14 | 2002-06-13 | Aguadas Ellis Charles W. | Method and apparatus for generating and utilizing combustible gas |
| WO2007081296A1 (en) | 2006-01-16 | 2007-07-19 | Gep Yesil Enerji Uretim Teknolojileri Ltd. Sti. | Downdraft/updraft gasifier for syngas production from solid waste |
| EP2012059A1 (en) * | 2007-07-02 | 2009-01-07 | Suncue Company Ltd. | Furnace |
| WO2009149311A1 (en) * | 2008-06-05 | 2009-12-10 | Synthesis Energy Systems, Inc.Reply To # | Fluidized bed gasifier with solids discharge and classification device |
-
2011
- 2011-11-07 EP EP11187993.8A patent/EP2589870A1/en not_active Withdrawn
Patent Citations (7)
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| GB209211A (en) * | 1922-10-13 | 1924-01-10 | George Herbert Bentley | Improvements in gas producers and the like |
| US3841851A (en) * | 1974-02-12 | 1974-10-15 | E Kaiser | Process and apparatus for the gasification of organic matter |
| US4154582A (en) * | 1977-08-01 | 1979-05-15 | General Electric Company | Method of solids discharge from coal gasifier grate |
| US20020069798A1 (en) * | 2000-09-14 | 2002-06-13 | Aguadas Ellis Charles W. | Method and apparatus for generating and utilizing combustible gas |
| WO2007081296A1 (en) | 2006-01-16 | 2007-07-19 | Gep Yesil Enerji Uretim Teknolojileri Ltd. Sti. | Downdraft/updraft gasifier for syngas production from solid waste |
| EP2012059A1 (en) * | 2007-07-02 | 2009-01-07 | Suncue Company Ltd. | Furnace |
| WO2009149311A1 (en) * | 2008-06-05 | 2009-12-10 | Synthesis Energy Systems, Inc.Reply To # | Fluidized bed gasifier with solids discharge and classification device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101721823B1 (en) | 2015-11-06 | 2017-04-10 | 정동규 | Updraft gasification reactor using combustable waste and biomass resources |
| WO2020065008A1 (en) | 2018-09-27 | 2020-04-02 | Wieslaw Wilczynski | A system for heating a head of a stirling engine |
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