HRP20171737T1 - Arrangement and method for burning fuel - Google Patents

Arrangement and method for burning fuel Download PDF

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Publication number
HRP20171737T1
HRP20171737T1 HRP20171737TT HRP20171737T HRP20171737T1 HR P20171737 T1 HRP20171737 T1 HR P20171737T1 HR P20171737T T HRP20171737T T HR P20171737TT HR P20171737 T HRP20171737 T HR P20171737T HR P20171737 T1 HRP20171737 T1 HR P20171737T1
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HR
Croatia
Prior art keywords
combustion
separator
gaseous product
gasification equipment
fuel
Prior art date
Application number
HRP20171737TT
Other languages
Croatian (hr)
Inventor
Timo Honkola
Original Assignee
Valmet Technologies Oy
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Application filed by Valmet Technologies Oy filed Critical Valmet Technologies Oy
Publication of HRP20171737T1 publication Critical patent/HRP20171737T1/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/82Gas withdrawal means
    • C10J3/84Gas withdrawal means with means for removing dust or tar from the gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C6/00Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
    • F23C6/04Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/02Dust removal
    • C10K1/026Dust removal by centrifugal forces
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00Fluidised bed combustion apparatus
    • F23C10/02Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/0916Biomass
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1603Integration of gasification processes with another plant or parts within the plant with gas treatment
    • C10J2300/1606Combustion processes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/16Integration of gasification processes with another plant or parts within the plant
    • C10J2300/164Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
    • C10J2300/1643Conversion of synthesis gas to energy
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/54Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/54Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
    • C10J3/56Apparatus; Plants

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Feeding And Controlling Fuel (AREA)

Claims (15)

1. Sustav za izgaranje goriva, gdje sustav (1) sadrži rasplinjačku opremu (3) za prevođenje goriva (F) u plinoviti proizvod (G) rasplinjačkem i postrojenje za izgaranje (5), namijenjeno izgaranju plinovitog proizvoda (G), gdje rasplinjačka oprema (3) sadrži sredstvo za rasplinjavanje goriva na niskoj temperaturi, gdje sustav (1) dodatno sadrži separator (4), koji se nalazi između rasplinjačke opreme (3) i postrojenja za izgaranje (5), tako da uglavnom sav plinoviti proizvod (G) prenesen u postrojenje za izgaranje (5) istječe iz rasplinjačke opreme (3) kroz separator u postrojenje za izgaranje (5); separator (4), koji sadrži sredstvo za pročišćavanje plinovitog proizvoda (G) od krutina, gdje se između rasplinjačke opreme (3) i separatora (4) i/ili između separatora (4) i postrojenja za izgaranje (5) nalazi izmjenjivač topline (14a, 14b), naznačen time što postrojenje za izgaranje (5), namijenjeno izgaranju plinovitog proizvoda (G) je predviđeno za prihvat plinovitog proizvoda (G), proizvedenog u rasplinjačkoj opremi (3) i ohlađenog u izmjenjivaču topline (14a, 14b).1. A fuel combustion system, where the system (1) contains a gasification equipment (3) for converting fuel (F) into a gaseous product (G) by a gasifier and a combustion plant (5), intended for the combustion of a gaseous product (G), where the gasification equipment (3) contains an agent for fuel gasification at low temperature, where system (1) additionally contains separator (4), which is located between the gasification equipment (3) and the combustion plant (5), so that basically all the gaseous product (G) transferred to the combustion plant (5) flows from the gasification equipment (3) through the separator to the plant for combustion (5); separator (4), which contains means for purifying the gaseous product (G) from solids, where a heat exchanger (14a, 14b) is located between the gasification equipment (3) and the separator (4) and/or between the separator (4) and the combustion plant (5), indicated by the fact that the combustion plant (5), intended for the combustion of the gaseous product (G), is designed to receive the gaseous product (G), produced in the gasification equipment (3) and cooled in the heat exchanger (14a, 14b). 2. Sustav u skladu s patentnim zahtjevom 1, naznačen time što je rasplinjačka oprema (3) CFB rasplinjač.2. System according to patent claim 1, characterized in that the carburetor equipment (3) is a CFB carburetor. 3. Sustav u skladu s patentnim zahtjevom 1 ili 2, naznačen time što je navedena niska temperatura niža od 800°C, po mogućnosti u rasponu temperatura od 600 do 750°C.3. System according to patent claim 1 or 2, characterized in that the specified low temperature is lower than 800°C, preferably in the temperature range of 600 to 750°C. 4. Sustav u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što donji dio rasplinjačke opreme (3) sadrži sredstvo (11) za oksidiranje troske.4. A system according to any of the previous patent claims, characterized in that the lower part of the gasification equipment (3) contains a means (11) for oxidizing the slag. 5. Sustav u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što rasplinjačka oprema (3) ima zidane zidove.5. A system according to any of the preceding patent claims, characterized in that the gasification equipment (3) has masonry walls. 6. Sustav u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što je postrojenje za izgaranje (5) parni kotao.6. A system according to any of the preceding claims, characterized in that the combustion plant (5) is a steam boiler. 7. Sustav u skladu s bilo kojim od patentnih zahtjeva 1 do 6, naznačen time što je postrojenje za izgaranje (5) peć.7. A system according to any one of claims 1 to 6, characterized in that the combustion plant (5) is a furnace. 8. Sustav u skladu s bilo kojim od prethodnih patentnih zahtjeva, naznačen time što separator (4) uključuje ciklon ili multiciklon.8. A system according to any of the preceding patent claims, characterized in that the separator (4) includes a cyclone or a multicyclone. 9. Sustav u skladu s bilo kojim od patentnih zahtjeva 1 do 7, naznačen time što separator (4) uključuje spremnik za razdvajanje.9. A system according to any one of claims 1 to 7, characterized in that the separator (4) includes a separation tank. 10. Sustav u skladu s bilo kojim od patentnih zahtjeva 1 do 7, naznačen time što separator (4) uključuje keramički filtar ili električni filtar.10. A system according to any one of claims 1 to 7, characterized in that the separator (4) includes a ceramic filter or an electric filter. 11. Postupak izgaranja goriva, gdje se u navedenom postupku gorivo (F) prevodi u plinoviti proizvod (G) rasplinjavanjem u rasplinjačkoj opremi (3), a plinoviti proizvod (G) izgara u postrojenju za izgaranje (5), podešavanjem temperature rasplinjačke opreme (3), tako da bude najviše 800 °C; prijenosa gorivog plina (P) proizvedenog u rasplinjaču iz rasplinjačke opreme (3) u separator (4); pročišćavanja gorivog plina (P) od krutina, gdje se proizvodi plinoviti proizvod (G); i prijenosa plinovitog proizvoda (G) u postrojenje za izgaranje (5) radi izgaranja, smanjivanja temperature gorivog plina (P) i/ili plinovitog proizvoda (G) izmjenjivačem topline (14a, 14b), koji se nalazi između rasplinjačke opreme (3) i separatora (4) i/ili između separatora (4) i postrojenja za izgaranje (5), naznačen time što izgaranje plinovitog proizvoda (G), proizvedenog u rasplinjačkoj opremi (3) i ohlađenog u izmjenjivaču topline (14a, 14b) u postrojenju za izgaranje (5).11. Fuel combustion process, where in the mentioned process the fuel (F) is converted into a gaseous product (G) by gasification in the gasification equipment (3), and the gaseous product (G) is burned in the combustion plant (5), by adjusting the temperature of the gasification equipment (3), so that it is at most 800 °C; transfer of fuel gas (P) produced in the gasifier from the gasifier equipment (3) to the separator (4); purification of fuel gas (P) from solids, where a gaseous product (G) is produced; and transfer of the gaseous product (G) to the combustion plant (5) for combustion, reducing the temperature of the fuel gas (P) and/or the gaseous product (G) by the heat exchanger (14a, 14b), which is located between the gasification equipment (3) and the separator (4) and/or between the separator (4) and the combustion plant ( 5), indicated by what combustion of the gaseous product (G), produced in the gasification equipment (3) and cooled in the heat exchanger (14a, 14b) in the combustion plant (5). 12. Postupak u skladu s patentnim zahtjevom 11, naznačen time što se gorivo (F), uključući agro gorivo, šalje u rasplinjačku opremu (3).12. The method according to patent claim 11, characterized in that the fuel (F), including agricultural fuel, is sent to the gasification equipment (3). 13. Postupak u skladu s patentnim zahtjevom 11 ili 12, naznačen time što se gorivo rasplinjava u CFB rasplinjaču.13. The method according to claim 11 or 12, characterized in that the fuel is gasified in a CFB gasifier. 14. Postupak u skladu s bilo kojim od patentnih zahtjeva 11 do 13 naznačen time što se temperaturu rasplinjačke opreme (3) podešava da bude u rasponu od 600 do 750°C.14. The method according to any one of patent claims 11 to 13 characterized in that the temperature of the gasification equipment (3) is adjusted to be in the range of 600 to 750°C. 15. Postupak u skladu s bilo kojim od patentnih zahtjeva 11 do 14, naznačen time što pročišćavanje gorivog plina (P) od krutina u ciklonu (6), multiciklonu, spremniku za razdvajanje, na keramičkom filtru ili električnom filtru.15. The method according to any one of patent claims 11 to 14, characterized in that the purification of the fuel gas (P) from solids in a cyclone (6), a multicyclone, a separation tank, on a ceramic filter or an electric filter.
HRP20171737TT 2013-09-03 2017-11-13 Arrangement and method for burning fuel HRP20171737T1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FI20135887A FI126917B (en) 2013-09-03 2013-09-03 Arrangement and method for burning fuel
PCT/FI2014/050673 WO2015033022A1 (en) 2013-09-03 2014-09-03 Arrangement and method for burning fuel
EP14781612.8A EP3041919B1 (en) 2013-09-03 2014-09-03 Arrangement and method for burning fuel

Publications (1)

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HRP20171737T1 true HRP20171737T1 (en) 2018-01-26

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HRP20171737TT HRP20171737T1 (en) 2013-09-03 2017-11-13 Arrangement and method for burning fuel

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EP (1) EP3041919B1 (en)
FI (1) FI126917B (en)
HR (1) HRP20171737T1 (en)
HU (1) HUE035411T2 (en)
SI (1) SI3041919T1 (en)
WO (1) WO2015033022A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105588120B (en) * 2016-03-02 2018-05-11 内蒙古金土环保科技有限公司 A kind of general oxygen combustion system of desulfurization
CN106635179B (en) * 2017-01-23 2019-03-08 江苏华威机械制造有限公司 A kind of technique and its device of recirculating fluidized bed and pyrolysis bed combined gasification

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4211669A (en) * 1978-11-09 1980-07-08 Exxon Research & Engineering Co. Process for the production of a chemical synthesis gas from coal
DE3217030A1 (en) * 1982-05-06 1983-11-10 BKMI Industrieanlagen GmbH, 8000 München Process for carbonising and gasifying carbonaceous solids
US4676177A (en) 1985-10-09 1987-06-30 A. Ahlstrom Corporation Method of generating energy from low-grade alkaline fuels
US5059404A (en) * 1989-02-14 1991-10-22 Manufacturing And Technology Conversion International, Inc. Indirectly heated thermochemical reactor apparatus and processes
US5536285A (en) 1993-07-12 1996-07-16 Foster Wheeler Energia Oy Ceramic filtering of gases
US5626088A (en) 1995-11-28 1997-05-06 Foster Wheeler Energia Oy Method and apparatus for utilizing biofuel or waste material in energy production
RU2270849C2 (en) * 1998-11-05 2006-02-27 Ибара Корпорейшн System producing electric power with the help of gasification of combustibles
FI126542B (en) 2008-06-13 2017-02-15 Valmet Technologies Oy Method and plant for handling lime slurry and bed material
JP5535732B2 (en) 2010-04-05 2014-07-02 三菱重工業株式会社 Boiler equipment

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Publication number Publication date
EP3041919B1 (en) 2017-11-08
EP3041919A1 (en) 2016-07-13
FI20135887A (en) 2015-03-04
SI3041919T1 (en) 2018-04-30
WO2015033022A1 (en) 2015-03-12
HUE035411T2 (en) 2018-05-02
FI126917B (en) 2017-08-15

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