EP3067407B1 - Vorrichtung und verfahren zum vergasen von kohlenstoffhaltigem material - Google Patents
Vorrichtung und verfahren zum vergasen von kohlenstoffhaltigem material Download PDFInfo
- Publication number
- EP3067407B1 EP3067407B1 EP15158828.2A EP15158828A EP3067407B1 EP 3067407 B1 EP3067407 B1 EP 3067407B1 EP 15158828 A EP15158828 A EP 15158828A EP 3067407 B1 EP3067407 B1 EP 3067407B1
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- EP
- European Patent Office
- Prior art keywords
- filter
- gas
- hot gas
- gasification
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- 238000002309 gasification Methods 0.000 title claims description 23
- 238000000034 method Methods 0.000 title claims description 16
- 239000003575 carbonaceous material Substances 0.000 title description 2
- 239000007789 gas Substances 0.000 claims description 68
- 239000002023 wood Substances 0.000 claims description 25
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 15
- 229910052760 oxygen Inorganic materials 0.000 claims description 14
- 239000001301 oxygen Substances 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 9
- 239000007787 solid Substances 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 23
- 229910002091 carbon monoxide Inorganic materials 0.000 description 23
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Natural products C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 19
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 16
- 238000006722 reduction reaction Methods 0.000 description 13
- 238000006243 chemical reaction Methods 0.000 description 10
- 239000001257 hydrogen Substances 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 9
- 239000001569 carbon dioxide Substances 0.000 description 9
- 229910002092 carbon dioxide Inorganic materials 0.000 description 9
- 229920002678 cellulose Polymers 0.000 description 9
- 239000001913 cellulose Substances 0.000 description 9
- 239000003610 charcoal Substances 0.000 description 9
- 230000003647 oxidation Effects 0.000 description 9
- 238000007254 oxidation reaction Methods 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 229920002488 Hemicellulose Polymers 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 150000002431 hydrogen Chemical class 0.000 description 6
- 229920005610 lignin Polymers 0.000 description 6
- 238000000197 pyrolysis Methods 0.000 description 6
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 5
- 241000196324 Embryophyta Species 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000002817 coal dust Substances 0.000 description 3
- 239000012065 filter cake Substances 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000003077 lignite Substances 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000010744 Boudouard reaction Methods 0.000 description 1
- 240000000731 Fagus sylvatica Species 0.000 description 1
- 235000010099 Fagus sylvatica Nutrition 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 241000218657 Picea Species 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 239000013590 bulk material Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 125000001547 cellobiose group Chemical group 0.000 description 1
- 238000012993 chemical processing Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 235000013681 dietary sucrose Nutrition 0.000 description 1
- 150000002016 disaccharides Chemical class 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 150000002402 hexoses Chemical class 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 150000002972 pentoses Chemical class 0.000 description 1
- 230000002688 persistence Effects 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- ODLMAHJVESYWTB-UHFFFAOYSA-N propylbenzene Chemical group CCCC1=CC=CC=C1 ODLMAHJVESYWTB-UHFFFAOYSA-N 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000001648 tannin Substances 0.000 description 1
- 229920001864 tannin Polymers 0.000 description 1
- 235000018553 tannin Nutrition 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Images
Classifications
-
- 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
- C10K1/02—Dust removal
- C10K1/024—Dust removal by filtration
-
- 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
- C10J3/24—Arrangements or dispositions of valves or flues to permit flow of gases or vapours other than upwardly through the fuel bed
- C10J3/26—Arrangements or dispositions of valves or flues to permit flow of gases or vapours other than upwardly through the fuel bed downwardly
-
- 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
- C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
- C10K3/001—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by thermal treatment
- C10K3/003—Reducing the tar content
- C10K3/005—Reducing the tar content by partial oxidation
-
- 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
- C10J2300/0913—Carbonaceous raw material
- C10J2300/0916—Biomass
- C10J2300/092—Wood, cellulose
-
- 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
- C10J2300/0959—Oxygen
Definitions
- the invention relates to an apparatus and a method for the gasification of wood or other carbonaceous material according to claims 1 and 3.
- a special process and a plant for the gasification of lignite are known in which the lignite or brown coal gasified in a reactor, then roughly cleaned in a cyclone and finally finely cleaned in a hot gas filter.
- an additive for example, (lime) lime, buried, but undesirably reduces the temperature of the reaction gas.
- fine coal dust and air are added to the raw gas after the reactor, in its transport lines before and / or after the cyclone, by the reaction of which the temperature rises again.
- the main constituent of all woody plants is about 50% cellulose.
- Cellulose is a chain-shaped molecule of individual glucose units.
- the real component of cellulose is cellobiose, a disaccharide (double sugar).
- Hemicellulose is composed of polymeric carbohydrates whose constituents are pentoses and hexoses. Hemicellulose, like cellulose, is a polysaccharide (polyhydric sugar).
- the third component of wood is lignin, a polymer of phenylpropane units.
- the wood In addition to cellulose, hemicellulose and lignin, the wood also contains fats, resins, terpenes, dyes, tannins and mineral components.
- thermo-chemical processing solid bioenergy carriers are transformed primarily under the influence of heat into gaseous secondary energy sources.
- biomass is converted as completely as possible into flammable gases (ie into so-called synthesis gas) at high temperatures.
- the process is substoichiometrically an oxygen-containing gasification agent (air) supplied by the u. a. the carbon contained in the biomass can be converted into carbon monoxide.
- the partial combustion of the feed material provides the required process heat so that the gasification process can even take place (autothermal gasification).
- the resulting low calorific gas can in burners for heat supply and u. a. used in gas engines or turbines for power generation.
- the first phase is characterized by the fact that the wood is slowly heated from the outside to the inside. Unbound water is released in the form of water vapor. This process is endothermic (energy is needed).
- the temperature in the pyrolysis phase or zone ranges between 200 ° C and 400 ° C. At these temperatures, oxygen (O2) and hydrogen (H2) are degassed.
- the pyrolysis solid is charcoal.
- the reduction is dependent on the prevailing temperature.
- the conversion of hydrogen and carbon to methane between 400 ° C and 600 ° C decreases sharply. At temperatures above 1000 ° C no methane is formed.
- the Boudouard reaction achieves a good yield of carbon monoxide at high temperatures. This reaction is relatively slow.
- wood is heated by supplying heat and thereby evaporated in the Vergasergut water.
- the required amount of heat is generated by the partial combustion of the resulting carbonization and the oxidation of carbon and hydrogen.
- the resulting charcoal serves as a reaction surface for the oxidation and reduction of carbon, carbon monoxide, carbon dioxide and hydrogen. This reduces the charcoal, ie the surface of the particles is larger, thus increasing the reaction rate.
- reaction zone must be considered as a whole and the reduction or oxidation take place simultaneously.
- Typical calorific values for wood are on the order of 3.5-5.5 MJ / m3, so wood gas is a lean gas.
- the invention solves this problem with a device having the features specified in the characterizing part of claim 1 and with a method having the features specified in the characterizing part of claim 3.
- it is at least for the most part transferred to the gas stream to the subsequently arranged hot gas filter which accumulates uncharged in the bottom region of the gas generator charcoal.
- This can be done by appropriate choice of flow rate in the manner of a pneumatic Transportes, as he has been known for a long time as the bulk material promotion.
- charcoal, as well as coal dust and entrained ash, on the surface of the filter it is preferred filter cartridges, deposited.
- oxygen (usually in the form of air) is introduced as abruptly as possible, whereby the filter cake is blown off the filter cartridges and, favored by pressure surge and temperature, a second gasification step takes place through which the charcoal or charcoal brought along the coal dust is for the most part gasified.
- the still non-gasified portion is finally gasified by the oxygen supplied in the lower part of the filter - again preferably in the form of air.
- the system according to the invention is shown schematically with its elements and components necessary for the invention, albeit without the measuring devices, etc., in the single FIGURE. It essentially has: a gas generator 1 and a hot gas filter 2. wood chips, wood pellets, coal or the like are fed from a storage bin, not shown, via a feed 3 the gas generator 1 fitting at his head and go through in him from the state of Technique known and initially mentioned steps of drying, carbonization, oxidation and reduction, which is indicated in the lower part, indicated by the installation 4, via a line and a manifold system 5 air is supplied appropriately.
- filter cartridges 7 project from a filter bottom 13 directed downwards into it. Even if a filter cartridge is sufficient under certain circumstances, it is advantageous for continuous operation, if not essential, to provide at least two such filter cartridges 7. Through the filter cartridges through the product gas passes and comes, here referred to as clean gas product in the upper part of the hot gas filter 2, from where it is withdrawn via a clean gas line 8 and the further processing or use is supplied.
- the filter cartridges 7 are controllably connected to a compressed air supply 9, they can be set by means of this compressed air supply jerky on your clean gas side under pressure to blow off on the raw gas side accumulated filter cake and at least partially gas.
- a trigger 10 for the non-gasified components and a corresponding ash cone 11 is provided in the lower part of the hot gas filter 2.
- oxygen for example in the form of air, optionally heated and / or dried, fed into the region below the filter bottom 13 (approximately at the lower end of the filter cartridges), whereby it in the raw gas range of the hot gas filter 2 to another, very complete gasification of the previously not gasified wood components comes.
- the invention is not limited to the illustrated embodiment, but may be variously modified.
- several gas generators and / or several hot gas filters can be suitably combined with one another in order to achieve continuous operation even in the case of maintenance. It may be provided in the gas generator for wood components, which are too heavy for the increased train, a discharge for such parts, whether these are then returned to the gas generator or disposed of, depends on the nature of the starting material and the possibility of a return in the Product flow off.
- the invention can be combined with various other embodiments of the method or the device, as long as the only reaction in the hot gas filter is not disturbed or the other embodiments of the filtering process do not interfere.
- the height of the entry of the nozzles or other openings of the supply line 12 into the hot gas filter 2 is suitable in the presence of filter cartridges 7 at the lower end. There, when blowing off the filter cake, the entire material will pass, as well as during the undisturbed operation, the not yet gasified material passes as well. Operating parameters such as overpressure and volume flow can be easily determined by a few tests. If different materials are gasified, it may be advantageous to provide nozzles of different heights that can be supplied individually or in groups.
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)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
- Coke Industry (AREA)
- Solid-Fuel Combustion (AREA)
Priority Applications (12)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP15158828.2A EP3067407B1 (de) | 2015-03-12 | 2015-03-12 | Vorrichtung und verfahren zum vergasen von kohlenstoffhaltigem material |
PL15158828T PL3067407T3 (pl) | 2015-03-12 | 2015-03-12 | Urządzenie i sposób zgazowywania materiałów zawierających węgiel |
PT15158828T PT3067407T (pt) | 2015-03-12 | 2015-03-12 | Dispositivo e método para a gaseificação de material carbonatado |
LTEP15158828.2T LT3067407T (lt) | 2015-03-12 | 2015-03-12 | Karbonatinės medžiagos dujinimo sistema ir būdas |
HUE15158828A HUE040505T2 (hu) | 2015-03-12 | 2015-03-12 | Berendezés és eljárás széntartalmú anyag elgázosítására |
DK15158828.2T DK3067407T3 (en) | 2015-03-12 | 2015-03-12 | Apparatus and method for gasification of carbonaceous material |
SI201530467T SI3067407T1 (sl) | 2015-03-12 | 2015-03-12 | Naprava in postopek za uplinjanje materialov, ki vsebujejo ogljik |
TR2018/16526T TR201816526T4 (tr) | 2015-03-12 | 2015-03-12 | Karbon içerikli maddelerin gazlaştırılmasına yönelik cıhaz ve yöntem. |
ES15158828T ES2696674T3 (es) | 2015-03-12 | 2015-03-12 | Sistema y método para gasificación de material carbonáceo |
RS20181354A RS57998B1 (sr) | 2015-03-12 | 2015-03-12 | Uređaj i postupak za gasifikaciju ugljeničnih materijala |
HRP20181834TT HRP20181834T1 (hr) | 2015-03-12 | 2018-11-06 | Sustav za rasplinjavanje ugljičnih materijala |
CY181101186T CY1120840T1 (el) | 2015-03-12 | 2018-11-09 | Διαταξη και μεθοδος για την αεριοποιηση ανθρακουχου υλικου |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP15158828.2A EP3067407B1 (de) | 2015-03-12 | 2015-03-12 | Vorrichtung und verfahren zum vergasen von kohlenstoffhaltigem material |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3067407A1 EP3067407A1 (de) | 2016-09-14 |
EP3067407B1 true EP3067407B1 (de) | 2018-08-15 |
Family
ID=52684060
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP15158828.2A Active EP3067407B1 (de) | 2015-03-12 | 2015-03-12 | Vorrichtung und verfahren zum vergasen von kohlenstoffhaltigem material |
Country Status (12)
Country | Link |
---|---|
EP (1) | EP3067407B1 (lt) |
CY (1) | CY1120840T1 (lt) |
DK (1) | DK3067407T3 (lt) |
ES (1) | ES2696674T3 (lt) |
HR (1) | HRP20181834T1 (lt) |
HU (1) | HUE040505T2 (lt) |
LT (1) | LT3067407T (lt) |
PL (1) | PL3067407T3 (lt) |
PT (1) | PT3067407T (lt) |
RS (1) | RS57998B1 (lt) |
SI (1) | SI3067407T1 (lt) |
TR (1) | TR201816526T4 (lt) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3323495B1 (de) | 2016-11-16 | 2020-04-29 | Glock Health, Science and Research GmbH | Produktgasfilter für abgase von holz-gasreaktoren umfassend filterkerzen und eine zeolith-einspeisung |
EP3581636A1 (de) | 2018-06-11 | 2019-12-18 | Glock Technology GmbH | Vorrichtung und verfahren zum speichern von energie von blockheizkraftwerken |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995024591A1 (de) * | 1994-03-09 | 1995-09-14 | Veag Vereinigte Energiewerke Ag | Verfahren und anordnung zum betrieb einer druckaufgeladenen zirkulierenden mit braunkohle betriebenen wirbelschichtfeuerung für ein kombikraftwerk |
US6077490A (en) * | 1999-03-18 | 2000-06-20 | Mcdermott Technology, Inc. | Method and apparatus for filtering hot syngas |
US7896956B2 (en) * | 2006-11-30 | 2011-03-01 | Mitsubishi Heavy Industries, Ltd. | Method for regenerating filter and apparatus thereof |
GB2514312B (en) * | 2012-12-13 | 2016-08-31 | Future Blends Ltd | Filter and process for producing liquid products from biomass pyrolysis products |
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2015
- 2015-03-12 SI SI201530467T patent/SI3067407T1/sl unknown
- 2015-03-12 RS RS20181354A patent/RS57998B1/sr unknown
- 2015-03-12 HU HUE15158828A patent/HUE040505T2/hu unknown
- 2015-03-12 ES ES15158828T patent/ES2696674T3/es active Active
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- 2015-03-12 DK DK15158828.2T patent/DK3067407T3/en active
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- 2015-03-12 EP EP15158828.2A patent/EP3067407B1/de active Active
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Publication number | Publication date |
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DK3067407T3 (en) | 2018-12-03 |
HRP20181834T1 (hr) | 2018-12-28 |
CY1120840T1 (el) | 2019-12-11 |
EP3067407A1 (de) | 2016-09-14 |
TR201816526T4 (tr) | 2018-11-21 |
LT3067407T (lt) | 2018-11-26 |
ES2696674T3 (es) | 2019-01-17 |
RS57998B1 (sr) | 2019-01-31 |
HUE040505T2 (hu) | 2019-03-28 |
PT3067407T (pt) | 2018-11-26 |
PL3067407T3 (pl) | 2019-01-31 |
SI3067407T1 (sl) | 2018-12-31 |
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