EP 1027407 A1 20000816 - METHOD AND DEVICE FOR PRODUCING COMBUSTIBLE GAS, SYNTHESIS GAS AND REDUCING GAS FROM SOLID FUELS
Title (en)
METHOD AND DEVICE FOR PRODUCING COMBUSTIBLE GAS, SYNTHESIS GAS AND REDUCING GAS FROM SOLID FUELS
Title (de)
VERFAHREN UND VORRICHTUNG ZUR ERZEUGUNG VON BRENN-, SYNTHESE- UND REDUKTIONSGAS AUS FESTEN BRENNSTOFFEN
Title (fr)
PROCEDE ET DISPOSITIF DE PRODUCTION DE GAZ DE COMBUSTION, DE GAZ DE SYNTHESE ET DE GAZ DE REDUCTION A PARTIR DE COMBUSTIBLES SOLIDES
Publication
Application
Priority
- DE 19747324 A 19971028
- EP 9806342 W 19981006
Abstract (en)
[origin: DE19747324A1] The reactor has a combined fuel burner (1), a combustion chamber (9) endothermal suspended flow gasifier (14) and thermal equalization channel (26) from the combustion chamber, with thermally protective cladding (32) of the reactor. A water bath (19) is located below the reactor. The channel includes quenching (30) for gases (23) leaving the gasifier (14). The cladding at combustion chamber level has a matching cooling unit (27). The combination burner (1) ignites and heats the reactor, with connections for ignition air (5) and fuel (2). Combustion air (3) and an igniter (6) are connected. Sub-stoichiometric combustion is maintained at up to 500 deg C. Heat is evolved, with gaseous products (4), residual coke or char and ash (with additives). The gasification media enter via swirl baffles (33) to react in the combustion chamber (9), where the ash fusion temperature is exceeded. Swirl centrifuges molten solids to the walls. The reaction chamber base is a slag interception sump with drain channels (12) for liquid slag, and a gas outlet (34). Slag droplets (18) are led off with the plunging jet (16) into the suspension flow gasifier, to fall into the water sump, where they cool as glass granules. The plunging jet carries slag droplets countercurrent to the rising gas flow (23). Fly ash is entrained by pneumatic lances for further reaction at up to 500-1500 deg C. Baffles connected to the heat exchange channel cause swirling and convective heat transfer, reducing the temperature of the combustion chamber wall. On the inner wall (9), this forms a protective layer of solidified slag, The flow leaves by the outlet (25), carrying away heat accepted. The water bath has with an outlet for the non-eluting slag granules, a weir (20) and a water supply.
IPC 1-7
IPC 8 full level
C10J 3/48 (2006.01); C10J 3/66 (2006.01); C10J 3/46 (2006.01)
CPC (source: EP)
C10J 3/487 (2013.01); C10J 3/506 (2013.01); C10J 3/526 (2013.01); C10J 3/66 (2013.01); C10J 3/84 (2013.01); C10K 1/04 (2013.01); C10K 1/101 (2013.01); C10J 2200/152 (2013.01); C10J 2300/1223 (2013.01)
Designated contracting state (EPC)
AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE
DOCDB simple family (publication)
WO 9921940 A1 19990506; AR 010952 A1 20000712; AT E200791 T1 20010515; AU 754147 B2 20021107; AU 9542798 A 19990517; BR 9813292 A 20000822; BR 9813292 B1 20091201; CA 2306889 A1 19990506; CA 2306889 C 20081216; CN 1136299 C 20040128; CN 1278292 A 20001227; DE 19747324 A1 19990429; DE 19747324 C2 19991104; DE 59800654 D1 20010531; DK 1027407 T3 20010813; EP 1027407 A1 20000816; EP 1027407 B1 20010425; ES 2157673 T3 20010816; GR 3036233 T3 20011031; ID 21135 A 19990429; JP 2001521056 A 20011106; JP 4112173 B2 20080702; MY 127842 A 20061229; NO 20001993 D0 20000417; NO 20001993 L 20000615; NO 328487 B1 20100301; PL 190794 B1 20060131; PL 340217 A1 20010115; PT 1027407 E 20011030; TW 518363 B 20030121; ZA 989759 B 19990503
DOCDB simple family (application)
EP 9806342 W 19981006; AR P980105392 A 19981028; AT 98949009 T 19981006; AU 9542798 A 19981006; BR 9813292 A 19981006; CA 2306889 A 19981006; CN 98810657 A 19981006; DE 19747324 A 19971028; DE 59800654 T 19981006; DK 98949009 T 19981006; EP 98949009 A 19981006; ES 98949009 T 19981006; GR 20010401085 T 20010718; ID 981403 A 19981023; JP 2000518034 A 19981006; MY PI9804746 A 19981016; NO 20001993 A 20000417; PL 34021798 A 19981006; PT 98949009 T 19981006; TW 87117842 A 19981028; ZA 989759 A 19981027