DK2847516T3 - Forbedringer inden for affaldsforarbejdning - Google Patents
Forbedringer inden for affaldsforarbejdning Download PDFInfo
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- DK2847516T3 DK2847516T3 DK13720503.5T DK13720503T DK2847516T3 DK 2847516 T3 DK2847516 T3 DK 2847516T3 DK 13720503 T DK13720503 T DK 13720503T DK 2847516 T3 DK2847516 T3 DK 2847516T3
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- DK
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- Prior art keywords
- synthesis gas
- calorific value
- gas
- syngas
- boiler
- Prior art date
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- 238000012545 processing Methods 0.000 title claims description 51
- 239000002699 waste material Substances 0.000 title claims description 43
- 239000007789 gas Substances 0.000 claims description 175
- 230000015572 biosynthetic process Effects 0.000 claims description 57
- 238000003786 synthesis reaction Methods 0.000 claims description 57
- 238000000034 method Methods 0.000 claims description 41
- 239000000463 material Substances 0.000 claims description 20
- 239000007800 oxidant agent Substances 0.000 claims description 19
- 238000007669 thermal treatment Methods 0.000 claims description 19
- 238000003860 storage Methods 0.000 claims description 18
- 230000005611 electricity Effects 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 14
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 13
- 239000001301 oxygen Substances 0.000 claims description 13
- 229910052760 oxygen Inorganic materials 0.000 claims description 13
- 238000012544 monitoring process Methods 0.000 claims description 11
- 229930195733 hydrocarbon Natural products 0.000 claims description 9
- 150000002430 hydrocarbons Chemical class 0.000 claims description 9
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 238000011144 upstream manufacturing Methods 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- 239000012855 volatile organic compound Substances 0.000 claims description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 5
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 5
- 239000001257 hydrogen Substances 0.000 claims description 5
- 229910052739 hydrogen Inorganic materials 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 230000003134 recirculating effect Effects 0.000 claims description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims description 3
- 239000005416 organic matter Substances 0.000 claims 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 11
- 239000000446 fuel Substances 0.000 description 9
- 238000002309 gasification Methods 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 9
- 238000004140 cleaning Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000001965 increasing effect Effects 0.000 description 6
- 238000004227 thermal cracking Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000003345 natural gas Substances 0.000 description 3
- -1 CH4) Chemical class 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000012805 post-processing Methods 0.000 description 2
- 238000007781 pre-processing Methods 0.000 description 2
- 239000003473 refuse derived fuel Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 239000002154 agricultural waste Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 244000309466 calf Species 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants 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
- F01K23/06—Plants 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
- F01K23/067—Plants 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C3/00—Gas-turbine plants characterised by the use of combustion products as the working fluid
- F02C3/20—Gas-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
- F02C3/26—Gas-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
- F02C3/28—Gas-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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/10—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of field or garden waste or biomasses
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/02—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/10—Drying by heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/40—Gasification
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
- F23G2206/202—Waste heat recuperation using the heat in association with another installation with an internal combustion engine
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
- F23G2206/203—Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/10—Arrangement of sensing devices
- F23G2207/104—Arrangement of sensing devices for CO or CO2
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/10—Arrangement of sensing devices
- F23G2207/108—Arrangement of sensing devices for hydrocarbon concentration
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/26—Biowaste
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2900/00—Special features of, or arrangements for incinerators
- F23G2900/50204—Waste pre-treatment by pyrolysis, gasification or cracking
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Combustion & Propulsion (AREA)
- Chemical & Material Sciences (AREA)
- Sustainable Energy (AREA)
- Sustainable Development (AREA)
- Life Sciences & Earth Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Incineration Of Waste (AREA)
Claims (16)
1. Fremgangsmåde til forarbejdning af materiale (E), der har et organisk indhold, hvilken fremgangsmåde omfatter: opvarmning af en batch af materialet i en batchforarbejdningsanordning (16) med en reduceret oxygenatmosfære for at omdanne mindst noget af det organiske indhold til gas for at producere syntesegas; hævning af temperaturen på syntesegassen og opretholdelse af syntesegassen på den forhøjede temperatur i en opholdstid, der er tilstrækkelig til at nedbryde ethvert langkædet carbonhydrid eller flygtige organiske forbindelser deri; overvågning af kalorieværdi for den producerede syntesegas, når syntesegassens kalorieværdi er under en forhåndsbestemt tærskel, omdirigeres syntesegassen, med en lav kalorieværdi, til en brænder i en kedel (22) for at producere damp; og når syntesegassens kalorieværdi overstiger den forhåndsbestemte tærskel, omdirigeres syntesegassen, med en høj kalorieværdi, til en gasmotor (40) for at producere elektricitet.
2. Fremgangsmåde ifølge krav 1, hvilken fremgangsmåde endvidere omfatter en første forhåndsbestemt tærskel og en anden forhåndsbestemt tærskel, og hvor: når syntesegassens kalorieværdi er under den første forhåndsdefinerede tærskel, omdirigeres af syntesegassen, med en lav kalorieværdi, til en brænder i en kedel (22) for at producere damp i en første driftsmodus; når syntesegassens kalorieværdi overstiger den første forhåndsdefinerede tærskel, omdirigeres syntesegassen, med en høj kalorieværdi, til en gasmotor (40) for at producere elektricitet i en anden driftsmodus; og når syntesegassens kalorieværdi falder under en anden tærskel, omdirigeres syntesegassen, med en lav kalorieværdi, til en brænder i en kedel (22) for at producere damp i en tredje driftsfase og eventuelt, hvor den første og anden tærskel har den samme værdi.
3. Fremgangsmåde ifølge krav 2, hvilken fremgangsmåde endvidere omfatter: når syntesegassens kalorieværdi overstiger en tredje tærskel, der er højere end første og anden forhåndsbestemte tærskler, omdirigeres syntesegassen, med en meget høj kalorieværdi, to en opbevaringsbeholder (44).
4. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, hvilken fremgangsmåde endvidere omfatter midlertidig oplagring af syntesegassen med en høj kalorieværdi i en opbevaringsbeholder (38) og/eller midlertidig oplagring af syntesegassen med en lav kalorieværdi i en opbevaringsbeholder (34).
5. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, hvor overvågning af kalorieværdien af den producerede syntesegas omfatter overvågning af syntesegassens gassammensætning, eventuelt hvor overvågning af syntesegassens gassammensætning omfatter overvågning af ét eller flere af syntesegassens hydrogenindhold, syntesegassens carbonmonoxidindhold og syntesegassens methanindhold.
6. Fremgangsmåde ifølge krav 3, hvor syntesegassens kalorieværdi ved den forhåndsbestemte tærskel ligger inden for intervallet fra 0,0117-0,0239 KW/0,028 m3 (40 til 100 BTU pr. kubikfod) og/eller, hvor syntesegassens kalorieværdi ved den tredje tærskel ligger inden for intervallet fra 0,0586-0,0644 KW/0,028 m3 (200 til 220 BTU pr. kubikfod).
7. Fremgangsmåde ifølge et hvilket som helst af kravene 1 til 4, hvor: omdirigering af syntesegassen, med en lav kalorieværdi, til en brænder i en kedel (22) for at producere damp omfatter omdirigering af syntesegassen gennem en første strømningsbane, der fører til en termisk oxidator (18A), på opstrømssiden af en kedelvarmeveksler (52), hvor syntesegassen forbrændes, hvorved der frembringes en varm gasstrøm over varmeveksleren (52), og opretholdelse af syntesegassen ved den forhøjede temperatur i opholdstiden; og hvor omdirigering af syntesegassen, med en højere kalorieværdi, til en gasmotor (40) omfatter omdirigering af syntesegassen gennem en anden strømningsbane til en gasmotor, via en termisk behandlingsanordning (18B), hvor temperaturen på syntesegassen er forhøjet og opretholdes ved den forhøjede temperatur i opholdstiden.
8. Fremgangsmåde ifølge et hvilket som helst af de foregående krav, hvilken fremgangsmåde endvidere omfatter tilvejebringelse af en recirkulationssløjfe (46) med en brænder (48) deri og recirkulation af varme gasser gennem batchforarbejdningsovnen (16) og recirkulationssløjfen (46) for at opvarme batchforarbejdningsovnen (16).
9. Anordning til forarbejdning af materiale (E), der har et organisk indhold, hvilken anordning omfatter: mindst én batchforarbejdningsovn (16), der er konfigureret til at opvarme en batch af materialet i en reduceret oxygenatmosfære for at omdanne mindst noget af materialets organiske indhold til gas for at producere syntesegas; mindst én termisk behandlingsanordning (18), der er konfigureret til at modtage syntesegas fra batchforarbejdningsovnen (16) og har et opvarmningsmiddel, der er forbundet dermed, hvilken termisk behandlingsanordning (18) er konfigureret til at hæve temperaturen på syntesegassen deri i en opholdstid, der er tilstrækkelig til termisk at nedbryde ethvert langkædet carbonhydrid eller flygtige organiske forbindelser, der er til stede i syntesegassen; mindst ét detekteringsmiddel (26) til at detektere sammensætning af den producerede syntesegas og konfigureret til at afgive et signal, der indikerer dens kalorieværdi, mindst én gasmotor (40); en kedel (22); et ventilmiddel (30, 32) til at dirigere syntesegas til gasmotoren eller kedlen; og en styreenhed (28), der er konfigureret til at: detektere, når syntesegassens kalorieværdi er under en forhåndsbestemt tærskel og styre ventilmidlet (30, 32) til at dirigere syntesegassen, med en lav kalorieværdi, til en brænder i kedlen (22) for at producere damp; og detektere, når syntesegassens kalorieværdi overstiger den forhåndsbestemte tærskel og styre ventilmidlet (30, 32) til at dirigere syntesegassen, med en høj kalorieværdi, til gasmotoren (40) for at producere elektricitet.
10. Anordning ifølge krav 9, hvor den forhåndsbestemte tærskel omfatter en første forhåndsbestemt tærskel og en anden forhåndsbestemt tærskel, og hvor styreenheden (28) er konfigureret til at detektere, når syntesegassens kalorieværdi er under den første forhåndsbestemte tærskel og styre ventilmidlet (30, 32) til at dirigere syntesegassen, med en lav kalorieværdi, til brænderen i kedlen (22) for at producere damp i en første driftsmodus; detektere, når syntesegassens kalorieværdi overstiger den første forhåndsbestemte tærskel og styre ventilmidlet (30, 32) til at dirigere syntesegassen, med en høj kalorieværdi, til gasmotoren (40) for at producere elektricitet i en anden driftsmodus; og detektere, når syntesegassens kalorieværdi falder under den anden tærskel, og styre ventilmidlet (30, 32) til at dirigere syntesegassen, med en lav kalorieværdi, til brænderen i kedlen (22) for at producere damp i en tredje driftsfase.
11. Anordning ifølge krav 10, hvor styreenheden (28) endvidere er konfigureret til at detektere, når syntesegassens kalorieværdi overstiger en tredje tærskel, der er højere end de første og anden forhåndsbestemte tærskler, og styre ventilmidlet (30, 32) til at dirigere syntesegassen, med en meget høj kalorieværdi, til en opbevaringsbeholder (44).
12. Anordning ifølge et hvilket som helst af kravene 9 til 11, hvilken anordning endvidere omfatter en opbevaringsbeholder (38) for midlertidig oplagring af syntesegassen med en høj kalorieværdi og/eller en opbevaringsbeholder (34) for midlertidig oplagring af syntesegassen med en lav kalorieværdi.
13. Anordning ifølge et hvilket som helst af kravene 9 til 12, hvilken anordning endvidere omfatter en gasanalysator (26) til at overvåge syntesegassens gassammensætning for at opnå et signal, der indikerer dens kalorieværdi.
14. Anordning ifølge et hvilket som helst af kravene 9 til 13, hvor den termiske behandlingsanordning (18) indbefatter et ventilmiddel (62) på nedstrømssiden af batchbehandlingsovnen (16) for omdirigering af syntesegassen ind i én eller flere af en første strømningsbane, der fører til gasmotoren (40), og en anden strømningsbane, der fører til kedlen (22), og, hvor den termiske behandlingsanordning (18) omfatter et termisk reaktor (18B), der er placeret i den første strømningsbane på opstrømssiden af gasmotoren, og en termisk oxidator (18A), der er placeret i den anden strømningsbane på opstrømssiden af kedlen (22), og eventuelt hvor den termiske reaktor (18B) er konfigureret til at opvarme syntesegassen uden at forbrænde den, og hvor den termiske oxidator (18 A) er konfigureret til at opvarme syntesegassen for at forbrænde den.
15.
Anordning ifølge krav 14, hvilken anordning endvidere omfatter en recirkulationssløjfe (46) for recirkulation af varme gasser gennem batch forarbejdningsovnen (16), uden at den passerer gennem den termiske behandlingsanordning (18), hvilken anordning endvidere omfatter en brænder (48), der er tilvejebragt i recirkulationssløjfen (46) for at tilvejebringe en strøm af varm gas gennem batchforarbejdningsovnen (16).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB1208165.9A GB2488923B (en) | 2012-05-08 | 2012-05-08 | Improvements in waste processing |
| PCT/GB2013/051101 WO2013167870A1 (en) | 2012-05-08 | 2013-04-30 | Improvements in waste processing |
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| DK2847516T3 true DK2847516T3 (da) | 2016-07-04 |
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| EP (1) | EP2847516B1 (da) |
| KR (1) | KR20150014485A (da) |
| CN (1) | CN104520645B (da) |
| AU (1) | AU2013257835B2 (da) |
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| PL (1) | PL2847516T3 (da) |
| PT (1) | PT2847516E (da) |
| WO (1) | WO2013167870A1 (da) |
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| GB2488923B (en) | 2012-05-08 | 2013-02-20 | Chinook Sciences Ltd | Improvements in waste processing |
| GB2513143B (en) * | 2013-04-17 | 2015-11-11 | Chinook End Stage Recycling Ltd | Improvements in waste processing |
| GB2526819B (en) * | 2014-06-03 | 2018-07-04 | Chinook End Stage Recycling Ltd | Waste management |
| KR102034774B1 (ko) * | 2019-05-28 | 2019-11-08 | (주)평화엔지니어링 | 미세먼지 대응 휘발성 유기화합물의 에너지 전환시스템 및 동 시스템을 이용한 에너지 전환방법 |
| CN112107970B (zh) * | 2019-06-19 | 2022-12-20 | 中国石油化工股份有限公司 | 一种储罐内VOCs处理装置和方法 |
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| US5922090A (en) | 1994-03-10 | 1999-07-13 | Ebara Corporation | Method and apparatus for treating wastes by gasification |
| US5553554A (en) * | 1994-10-04 | 1996-09-10 | Urich, Jr.; Albert E. | Waste disposal and energy recovery system and method |
| JPH10238727A (ja) | 1997-02-28 | 1998-09-08 | Hitachi Ltd | 廃棄物熱分解処理装置 |
| DE10021448A1 (de) | 2000-05-03 | 2001-11-08 | Messer Griesheim Gmbh | Verfahren und Vorrichtung für die Verbrennung von organischem Reststoff |
| KR100482187B1 (ko) | 2001-09-20 | 2005-04-13 | 니폰 조키 세야쿠 가부시키가이샤 | 유기폐기물의 탄화처리방법 및 장치 |
| JP2006218383A (ja) * | 2005-02-09 | 2006-08-24 | Kobe Steel Ltd | 高含水有機廃棄物の処理システム |
| JP4196215B2 (ja) | 2005-09-20 | 2008-12-17 | 小林製薬株式会社 | 包装用ケース |
| ITPI20070039A1 (it) * | 2007-04-10 | 2008-10-11 | Delca S P A | Impianto e metodo per la produzione di energia elettrica |
| EP2282017A1 (de) * | 2009-01-26 | 2011-02-09 | Siemens Aktiengesellschaft | Synthesegasbrennstoffsystem mit Zweitbrennstoffbeimischung sowie Verfahren zum Betrieb eines Synthesegasbrennstoffsystems |
| WO2011128918A1 (en) * | 2010-04-13 | 2011-10-20 | In Ser S.P.A | System and process for treating solid urban wastes |
| GB2470127B (en) * | 2010-05-20 | 2011-03-23 | Rifat A Chalabi | Improvements in waste recycling |
| GB2488923B (en) | 2012-05-08 | 2013-02-20 | Chinook Sciences Ltd | Improvements in waste processing |
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- 2013-04-30 IN IN10393DEN2014 patent/IN2014DN10393A/en unknown
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- 2013-04-30 BR BR112014027964A patent/BR112014027964A2/pt not_active IP Right Cessation
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Also Published As
| Publication number | Publication date |
|---|---|
| EA201401227A1 (ru) | 2015-05-29 |
| GB2488923B (en) | 2013-02-20 |
| GB201208165D0 (en) | 2012-06-20 |
| US20150089947A1 (en) | 2015-04-02 |
| EP2847516A1 (en) | 2015-03-18 |
| EP2847516B1 (en) | 2016-03-23 |
| AU2013257835A1 (en) | 2015-01-15 |
| BR112014027964A2 (pt) | 2017-06-27 |
| KR20150014485A (ko) | 2015-02-06 |
| IN2014DN10393A (da) | 2015-08-14 |
| US9447703B2 (en) | 2016-09-20 |
| ES2576494T3 (es) | 2016-07-07 |
| GB2488923A (en) | 2012-09-12 |
| AU2013257835B2 (en) | 2017-05-18 |
| WO2013167870A1 (en) | 2013-11-14 |
| PT2847516E (pt) | 2016-06-23 |
| CN104520645B (zh) | 2017-05-24 |
| MX2014013567A (es) | 2014-12-08 |
| CA2872960A1 (en) | 2013-11-14 |
| PL2847516T3 (pl) | 2016-09-30 |
| EA027222B1 (ru) | 2017-07-31 |
| MX348694B (es) | 2017-06-26 |
| CN104520645A (zh) | 2015-04-15 |
| HUE029578T2 (en) | 2017-03-28 |
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