EP1027407A1 - Verfahren und vorrichtung zur erzeugung von brenn-, synthese- und reduktionsgas aus festen brennstoffen - Google Patents
Verfahren und vorrichtung zur erzeugung von brenn-, synthese- und reduktionsgas aus festen brennstoffenInfo
- Publication number
- EP1027407A1 EP1027407A1 EP98949009A EP98949009A EP1027407A1 EP 1027407 A1 EP1027407 A1 EP 1027407A1 EP 98949009 A EP98949009 A EP 98949009A EP 98949009 A EP98949009 A EP 98949009A EP 1027407 A1 EP1027407 A1 EP 1027407A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- gas
- combustion chamber
- gasification
- slag
- reactor
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 24
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 11
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 10
- 239000004449 solid propellant Substances 0.000 title claims description 3
- 238000002309 gasification Methods 0.000 claims abstract description 48
- 238000002485 combustion reaction Methods 0.000 claims abstract description 42
- 239000002893 slag Substances 0.000 claims abstract description 36
- 239000000446 fuel Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000000047 product Substances 0.000 claims abstract description 12
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 238000002844 melting Methods 0.000 claims abstract description 8
- 230000008018 melting Effects 0.000 claims abstract description 8
- 239000000470 constituent Substances 0.000 claims abstract description 5
- 238000003763 carbonization Methods 0.000 claims abstract description 4
- 239000002028 Biomass Substances 0.000 claims abstract description 3
- 239000003610 charcoal Substances 0.000 claims abstract description 3
- 239000002803 fossil fuel Substances 0.000 claims abstract description 3
- 239000010802 sludge Substances 0.000 claims abstract description 3
- 239000002699 waste material Substances 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 60
- 239000003795 chemical substances by application Substances 0.000 claims description 17
- 239000000428 dust Substances 0.000 claims description 15
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 8
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 8
- 239000011707 mineral Substances 0.000 claims description 8
- 238000010791 quenching Methods 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 238000007654 immersion Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 230000000171 quenching effect Effects 0.000 claims description 4
- 238000010304 firing Methods 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 239000001569 carbon dioxide Substances 0.000 claims 1
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 1
- 229910002091 carbon monoxide Inorganic materials 0.000 claims 1
- 230000015556 catabolic process Effects 0.000 claims 1
- 238000004140 cleaning Methods 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000011241 protective layer Substances 0.000 abstract description 3
- 238000010521 absorption reaction Methods 0.000 abstract 1
- 230000001850 reproductive effect Effects 0.000 abstract 1
- 239000012265 solid product Substances 0.000 abstract 1
- 238000009987 spinning Methods 0.000 abstract 1
- 239000002023 wood Substances 0.000 abstract 1
- 239000002956 ash Substances 0.000 description 6
- 239000000571 coke Substances 0.000 description 5
- 238000000197 pyrolysis Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009422 external insulation Methods 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 150000002240 furans Chemical class 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/50—Fuel charging devices
- C10J3/506—Fuel charging devices for entrained flow gasifiers
-
- 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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/485—Entrained flow gasifiers
- C10J3/487—Swirling or cyclonic gasifiers
-
- 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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/52—Ash-removing devices
- C10J3/526—Ash-removing devices for entrained flow gasifiers
-
- 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
- C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
- C10J3/60—Processes
- C10J3/64—Processes with decomposition of the distillation products
- C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
-
- 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
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/101—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
-
- 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
- C10J2300/12—Heating the gasifier
- C10J2300/1223—Heating the gasifier by burners
Definitions
- the invention relates to a method and a device for generating fuel, synthesis and reduction gas from renewable and fossil fuels, other biomass, waste or sludge, preferably for pyrolysis products made therefrom according to patent DE 44 04 673, these being used when pyrolysis products are used their supply to the reactor largely in solid and gaseous products, eg. B. carbonization gas and charcoal, separately and separately to the reactor.
- the device according to the invention can be used in the energy industry, chemical industry and metallurgy for the highly efficient generation of fuel, synthesis and reduction gas for engines, synthesis processes, ore reduction and pig iron production.
- the reactants have very short residence times.
- a very large measurement and monitoring effort is necessary.
- Entrained-flow reactors which are fed with fuel by a separate pyrolysis have the disadvantage that the pyrolysis products are cooled before being fed into the reactor and, in addition to the heat losses, also require a high outlay for gas processing and handling of the liquid products.
- the object to be achieved by the invention is to propose a process and a reactor which, compared with the prior art, operate at an average lower temperature level with higher exergetic efficiency and generate a gasification gas which is free from hydrocarbons and chlorinated hydrocarbons (dioxins, furans), which can be used as a fuel gas for electricity generation, as a synthesis gas or as a reducing gas in a heat with ore reduction.
- a gasification gas which is free from hydrocarbons and chlorinated hydrocarbons (dioxins, furans), which can be used as a fuel gas for electricity generation, as a synthesis gas or as a reducing gas in a heat with ore reduction.
- the object is achieved with the features of claim 1.
- the further claims represent embodiments of the invention.
- the solution is such that the reactor is constructed in such a way that, in principle, the physical heat is retained at a high temperature level with only minimal losses and is used to increase the chemically bound heat.
- fuel and / or gas is initially at the outlet at the firing temperature the burner or at the entrance to the combustion chamber is rotated, which leads to the fact that hot droplets of slag are thrown against the wall and flow off to a slag pan at the bottom of the combustion chamber.
- the combustion chamber wall is kept at such a temperature level that a layer of solidified slag melt forms on it, on which the further slag runs, for which purpose the (reflected) gasification gas flows around it on the outside.
- the combustion chamber floor has a central opening from which the gas freed of the slag droplets emerges as a submerged jet and reaches the entrained-flow gasifier.
- the slag running off the wall is collected in the trough surrounding the opening, which is preferably equipped with radial drainage channels, and flows parallel to the gas into the entrained-flow gasifier.
- the gas outlet is designed as a channel, whereby the gasification gas is laminarized. This accomplishes two things.
- the slag flowing off is accelerated towards the water bath at the foot of the carburettor
- the gas exiting downwards into the carburetor remains in the form of a jet for a relatively long time, whereby it is braked above the water bath by compression effects and deflected upwards (reflected) is then to rise parallel to the immersion jet on the carburetor wall.
- the carbon-containing fuel dust is blown into the descending gas jet, first taken with it in descending order and then reaches the gas section in the form of a jacket, the dimensions of the device and the flow rate being designed for extensive gasification of the fuel dust.
- a jacket made of temperature-resistant steel or ceramic can be arranged around the gas outlet, through which the fuel dust can be fed through lances.
- the rising gas arrives, for example, via a guide device in an intermediate space between an outer shell of the device and the jacket of the combustion chamber, causes a heat balance on this and leaves the device via the gasification gas outlet.
- the device is provided with a heat protection lining and is preferably cooled.
- the resulting gas is of high quality and can be used directly.
- a combination burner 1 which receives hot, gaseous products of the smoldering, including the vaporous constituents such as tar, oil, water and dust at the inlet connection of the smoldering product channel 4 and guides them into the combustion chamber 9 via the swirl device 33.
- Pipes for the supply of residual coke, ash and additives 8 are arranged in the reactor in the smoldering product channel of the combination burner, so that the mineral components to be melted in the combustion chamber 1 are also twisted, heated and flung in the combustion chamber 1 in liquid form to the wall.
- the combination burner 1 has further supply channels for oxygen 7 or air 3, which, in the same way as the smoldering products via swirl devices 33, for rapid reaction with the smoldering products into a lubricant and for melting the mineral components of the residual coke, the ash and where appropriate, the supplements are introduced into the combustion chamber 1.
- the pilot fuel supply 2, pilot air supply 5 and ignition device and ignition monitoring 6 necessary for starting and heating are installed in the combination burner, where these elements elements are protected from the other flowing media during stationary gasification operations.
- the combustion chamber 9 is operated above the melting temperature of the mineral components of the residual coke, the ashes and the additives.
- the wall of the combustion chamber 9 is thermally conductive, so that its slag solidifies to form a protective layer due to heat dissipation to the outside and liquid slag runs off due to the temperature in the combustion chamber 9.
- the bottom of the reaction chamber 10 is designed as a Schiackeaufangwanne with incorporated drainage channels 12 so that a slag bath 13 can form, the slag flow through the gas outlet 34 through the direct contact of the slag with the gasifying agent 11 and through the direct current with the gasifying agent 11 always guaranteed.
- the sensible heat introduced with the gasification agent 11 is used to cover the gas flow endothermic gasification reaction between fuel dust and gasification agent. Lances 15, 17 are therefore provided for the fuel dust in the reactor.
- the gasification agent 11 enters the endothermic entrained-flow gasifier 14 as an immersion jet 16 and accelerates the entrained slag droplets 18 so that they are introduced into the water bath 19 and solidify there to form granules which are resistant to elution.
- the slag discharge 22, the water inlet 21 and overflow 20 were provided for media removal and to supplement evaporated water. Together with the water bath 19, they form the lower end of the endothermic entrained flow reactor 14.
- the immersion jet can also be stabilized and backmixing with the reflected gas rising in the shape of a jacket parallel to the wall can be prevented if a jacket 35 made of heat-resistant steel or ceramic is arranged beneath the gas outlet 34, through which the combustion dust lances 15 are passed. Additional lances 17 can be located below.
- the construction carried out ensures by the supply of oxygen-free gasification agent 11 and fuel dust to be gasified in the endothermic entrained flow reactor 14 and by the high gasification temperature above 500 ° C. that no oxygen breakthrough can occur in cold reactor areas.
- the heat equalization channel 26, in which guide devices 24 are located if necessary, serves to heat the gasification gas 23 cooled in the endothermic gasification. They impart a swirl swirl to the gasification gas stream 23, which increases the removal of convective heat from the wall of the combustion chamber 9 in such a way that the inner wall of the combustion chamber is cooled below the melting temperature of the slag, thereby forming a protective layer of solidified slag.
- the cooling of the combustion chamber wall is intensified by the cooling device 27, which is supplied via coolant inlets and outlets 28, 29.
- the device 30 for quenching the gasification gas is provided, to which quench nozzles 31 are mounted. The gasification gas leaves the reactor via the refractory-lined gasification gas outlet 25.
- the reactor is provided with a fire-resistant delivery 32 for chemical and thermal protection. It is also designed with heat-resistant, corrosion-resistant material and thermal external insulation for pressures up to 10 MPa.
- the lower part of the heat compensation channel 26 is designed conically.
- CARL / FRITZ "NOELL CONVERSION PROCESS” EF publishing house for energy and environmental technology GmbH 1994
- Combustion chamber 27 cooling device
- Reaction space 28 coolant inlet
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Industrial Gases (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Gasification And Melting Of Waste (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
Claims
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19747324A DE19747324C2 (de) | 1997-10-28 | 1997-10-28 | Vorrichtung zur Erzeugung von Brenn-, Synthese- und Reduktionsgas aus nachwachsenden und fossilen Brennstoffen, Biomassen, Müll oder Schlämmen |
DE19747324 | 1997-10-28 | ||
PCT/EP1998/006342 WO1999021940A1 (de) | 1997-10-28 | 1998-10-06 | Verfahren und vorrichtung zur erzeugung von brenn-, synthese- und reduktionsgas aus festen brennstoffen |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1027407A1 true EP1027407A1 (de) | 2000-08-16 |
EP1027407B1 EP1027407B1 (de) | 2001-04-25 |
Family
ID=7846707
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP98949009A Expired - Lifetime EP1027407B1 (de) | 1997-10-28 | 1998-10-06 | Verfahren und vorrichtung zur erzeugung von brenn-, synthese- und reduktionsgas aus festen brennstoffen |
Country Status (20)
Country | Link |
---|---|
EP (1) | EP1027407B1 (de) |
JP (1) | JP4112173B2 (de) |
CN (1) | CN1136299C (de) |
AR (1) | AR010952A1 (de) |
AT (1) | ATE200791T1 (de) |
AU (1) | AU754147B2 (de) |
BR (1) | BR9813292B1 (de) |
CA (1) | CA2306889C (de) |
DE (2) | DE19747324C2 (de) |
DK (1) | DK1027407T3 (de) |
ES (1) | ES2157673T3 (de) |
GR (1) | GR3036233T3 (de) |
ID (1) | ID21135A (de) |
MY (1) | MY127842A (de) |
NO (1) | NO328487B1 (de) |
PL (1) | PL190794B1 (de) |
PT (1) | PT1027407E (de) |
TW (1) | TW518363B (de) |
WO (1) | WO1999021940A1 (de) |
ZA (1) | ZA989759B (de) |
Families Citing this family (38)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19906891C2 (de) * | 1999-02-19 | 2002-07-18 | Schwarze Pumpe Energiewerke Ag | Verfahren zur Verwertung von staubförmigen und schlammartigen kohlenstoffhaltigen Stoffen in der Festbettvergasung |
DE102005006305B4 (de) * | 2005-02-11 | 2015-11-26 | Consulting & Management Friess Gbr (Vertretungsberechtigte Gesellschafter: Dietmar J. Friess 14532 Kleinmachnow, Jessica Friess 14532 Kleinmachnow) | Verfahren zur Erzeugung von Brenn- und Synthesegasen mit Hochdruckdampferzeugung |
US7819070B2 (en) | 2005-07-15 | 2010-10-26 | Jc Enviro Enterprises Corp. | Method and apparatus for generating combustible synthesis gas |
DE102005035988B4 (de) * | 2005-07-28 | 2009-01-02 | Wolf, Bodo Max, Dr.-Ing. | Verfahren zur Erzeugung von flüssigen Kohlenwasserstoffen aus Gas |
DE102005035921B4 (de) * | 2005-07-28 | 2008-07-10 | Choren Industries Gmbh | Verfahren zur endothermen Vergasung von Kohlenstoff |
US20070225382A1 (en) * | 2005-10-14 | 2007-09-27 | Van Den Berg Robert E | Method for producing synthesis gas or a hydrocarbon product |
CN104194836A (zh) * | 2005-12-14 | 2014-12-10 | 国际壳牌研究有限公司 | 制备合成气的方法 |
CN1935951B (zh) * | 2006-09-21 | 2010-12-08 | 武汉凯迪工程技术研究总院有限公司 | 一种固体含碳原料的高温气化装置 |
DE102007012452B4 (de) | 2007-03-15 | 2014-01-16 | SynCraft Enegineering GmbH | Vergaser |
FI122860B (fi) | 2007-05-25 | 2012-08-15 | Gasek Oy | Menetelmä kiinteän polttoaineen kaasuttamiseksi ja myötävirtakaasutin |
CN101679885B (zh) | 2008-01-28 | 2013-03-27 | 国际壳牌研究有限公司 | 启动煤气化反应器的方法 |
DE102008027336B4 (de) * | 2008-06-07 | 2010-07-08 | Karlsruher Institut für Technologie | Vorrichtung und Verfahren zur Bestimmung einer Partikelumwandlungsintensität |
DE102008033096A1 (de) * | 2008-07-15 | 2010-02-11 | Uhde Gmbh | Verfahren und Vorrichtung zum Zünden und zum Betrieb von Brennern bei der Vergasung kohlenstoffhaltiger Brennstoffe |
DE102008035295B4 (de) * | 2008-07-29 | 2013-10-17 | Siemens Aktiengesellschaft | Kohlenmonoxid-Konvertierung mittels gestufter Quenchung |
DE102008049716A1 (de) * | 2008-09-30 | 2010-04-08 | Siemens Aktiengesellschaft | Nutzung der fühlbaren Wärme des Rohgases bei der Flugstromvergasung |
EP2403928B1 (de) | 2009-03-04 | 2017-03-29 | ThyssenKrupp Industrial Solutions AG | Verfahren und vorrichtung zur nutzung der enthalpie eines synthesegases durch zusatz- und nachvergasung von nachwachsenden brennstoffen |
US8357215B2 (en) | 2009-03-04 | 2013-01-22 | General Electric Company | Method and apparatus of particulate removal from gasifier components |
DE102010008384A1 (de) | 2010-02-17 | 2011-08-18 | Uhde GmbH, 44141 | Verfahren und Vorrichtung zur Nutzung der Enthalpie eines Synthesegases durch Zugabe von nachwachsenden Brennstoffen in den Abkühlraum einer Flugstromvergasung |
DE102009011174A1 (de) | 2009-03-04 | 2010-09-09 | Uhde Gmbh | Verfahren und Vorrichtung zur Nutzung der Enthalpie eines Synthesegases zur Zusatzvergasung von nachwachsenden Brennstoffen |
JP4486699B1 (ja) * | 2009-11-06 | 2010-06-23 | 株式会社リ・サイエンスシステム研究所 | 水素ガスの発生を伴う有機性廃棄物の改質方法および有機性廃棄物改質用装置 |
KR101096632B1 (ko) * | 2009-12-10 | 2011-12-21 | 에스케이이노베이션 주식회사 | 상부 공급 이중선회형 가스화기 |
DE102010033646B4 (de) * | 2010-02-05 | 2012-05-24 | Pyrox Gmbh | Verfahren und Schachtvergaser zur Erzeugung von Brenngas aus einem festen Brennstoff |
US8480769B2 (en) * | 2010-07-29 | 2013-07-09 | Air Products And Chemicals, Inc. | Method for gasification and a gasifier |
DE102011008187B4 (de) * | 2011-01-10 | 2015-08-27 | Suncoal Industries Gmbh | Verfahren zur Erzeugung von Brenn- und Syntheserohgas |
DE102011107726B4 (de) | 2011-07-14 | 2016-06-30 | Thyssenkrupp Industrial Solutions Ag | Vorrichtung und Verfahren zum Einleiten von nachwachsenden Brennstoffen in den Bereich der Strahlungskesselwand von Vergasungsreaktoren |
CN102399590B (zh) * | 2011-10-08 | 2014-02-19 | 湖北双环科技股份有限公司 | 一种富氧气化的生产方法 |
US20130330236A1 (en) * | 2012-06-12 | 2013-12-12 | General Electric Company | System for initiating a gasification reaction in a gasifier |
CN103589460A (zh) * | 2012-08-16 | 2014-02-19 | 王庆 | 设置点火炉头的废锅流程水冷壁水煤浆气化炉 |
DE102014219455B4 (de) | 2013-09-25 | 2019-08-14 | Technische Universität Bergakademie Freiberg | Verfahren und Vorrichtung zur Teilkonvertierung von Rohgasen der Flugstromvergasung |
CN104019460B (zh) * | 2014-06-20 | 2016-08-24 | 航天长征化学工程股份有限公司 | 一种水冷壁气化炉挂渣方法及设备 |
CN104403694B (zh) * | 2014-10-16 | 2017-02-15 | 煤炭科学技术研究院有限公司 | 一种固定床气化炉的液态连续排渣器及排渣方法 |
CN105482852B (zh) * | 2015-11-20 | 2018-03-30 | 新奥科技发展有限公司 | 一种气化炉及煤加氢气化方法 |
EP3390586B1 (de) * | 2015-12-16 | 2019-09-18 | Air Products and Chemicals, Inc. | Vergasungssystem |
DE102017005627A1 (de) | 2016-10-07 | 2018-04-12 | Lennart Feldmann | Verfahren und System zur Verbesserung der Treibhausgas-Emissionsminderungsleistung biogener Kraft-, Heiz- und Brennstoffe und/oder zur Anreicherung landwirtschaftlich genutzter Flächen mit Humus-C |
CN107129833B (zh) * | 2017-06-23 | 2024-03-29 | 航天长征化学工程股份有限公司 | 一种环形粉煤腔 |
CN107892952B (zh) * | 2017-11-13 | 2019-09-06 | 煤炭科学技术研究院有限公司 | 一种两段式熔渣气化炉 |
CN107674712B (zh) * | 2017-11-13 | 2019-09-06 | 煤炭科学技术研究院有限公司 | 一种固定床熔渣气化炉 |
RO134445B1 (ro) * | 2020-05-18 | 2021-06-30 | Bogdan-Sabin Frâncu | Procedeu şi instalaţie de gazeificare a amestecurilor eterogene de substanţe şi compuşi organici |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3840354A (en) * | 1972-03-23 | 1974-10-08 | Us Interior | Three-stage gasification of coal |
US4272255A (en) * | 1979-07-19 | 1981-06-09 | Mountain Fuel Resources, Inc. | Apparatus for gasification of carbonaceous solids |
FR2530796A1 (fr) * | 1982-07-21 | 1984-01-27 | Creusot Loire | Dispositif de conversion et de recuperation thermique |
JPS59176391A (ja) * | 1983-03-28 | 1984-10-05 | Hitachi Ltd | 石炭ガス化炉 |
US4647294A (en) * | 1984-03-30 | 1987-03-03 | Texaco Development Corp. | Partial oxidation apparatus |
JPS62236891A (ja) * | 1986-04-09 | 1987-10-16 | Hitachi Ltd | 石炭ガス化炉の石炭ガス化方法 |
EP0545241B1 (de) * | 1991-11-29 | 1996-02-28 | Noell Energie- und Entsorgungstechnik GmbH | Verfahren zur thermischen Verwertung von Abfallstoffen |
DE4404673C2 (de) * | 1994-02-15 | 1995-11-23 | Entec Recycling Und Industriea | Verfahren zur Erzeugung von Brenngas |
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GR3036233T3 (en) | 2001-10-31 |
MY127842A (en) | 2006-12-29 |
CA2306889C (en) | 2008-12-16 |
ZA989759B (en) | 1999-05-03 |
ATE200791T1 (de) | 2001-05-15 |
DE19747324C2 (de) | 1999-11-04 |
AU754147B2 (en) | 2002-11-07 |
BR9813292A (pt) | 2000-08-22 |
JP2001521056A (ja) | 2001-11-06 |
TW518363B (en) | 2003-01-21 |
NO328487B1 (no) | 2010-03-01 |
AR010952A1 (es) | 2000-07-12 |
EP1027407B1 (de) | 2001-04-25 |
JP4112173B2 (ja) | 2008-07-02 |
ID21135A (id) | 1999-04-29 |
WO1999021940A1 (de) | 1999-05-06 |
CN1278292A (zh) | 2000-12-27 |
ES2157673T3 (es) | 2001-08-16 |
AU9542798A (en) | 1999-05-17 |
PL340217A1 (en) | 2001-01-15 |
CN1136299C (zh) | 2004-01-28 |
DK1027407T3 (da) | 2001-08-13 |
NO20001993L (no) | 2000-06-15 |
DE19747324A1 (de) | 1999-04-29 |
PT1027407E (pt) | 2001-10-30 |
BR9813292B1 (pt) | 2009-12-01 |
CA2306889A1 (en) | 1999-05-06 |
DE59800654D1 (de) | 2001-05-31 |
NO20001993D0 (no) | 2000-04-17 |
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