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VERFAHREN UND ANLAGE ZUR ENTSTICKUNG VON BYPASSGASEN IN EINEM MEHRSTUFIGEN SYSTEM VON MISCHKAMMERN BEI EINER ANLAGE ZUR HERSTELLUNG VON ZEMENTKLINKER
A method and a corresponding plant for denitrifying bypass exhaust gases in a cement clinker production plant. Raw meal is sintered in a rotary kiln and deacidified in a calciner. A rotary kiln inlet chamber is connected to the calciner directly or by a riser duct. Bypass exhaust gas is drawn off near the inlet chamber. This exhaust gas is guided into a first mixing chamber, in which the exhaust gas is cooled to between 800 and 950° C., then the exhaust gas is guided through a reaction pipeline segment, wherein the dwell time is between 0.5 and 3 seconds and ammonia, aqueous ammonia solution, or ammonia-releasing substances are injected for denitrification. Then the exhaust gas is guided into a second mixing chamber, in which the exhaust gas is cooled to between 150 to 250° C. Then the exhaust gas is guided to a filter for dust removal.
VERFAHREN UND ANLAGE ZUR ENTSTICKUNG VON BYPASSGASEN IN EINEM MEHRSTUFIGEN SYSTEM VON MISCHKAMMERN BEI EINER ANLAGE ZUR HERSTELLUNG VON ZEMENTKLINKER
A method and a corresponding plant for denitrifying bypass exhaust gases in a cement clinker production plant. Raw meal is sintered in a rotary kiln and deacidified in a calciner. A rotary kiln inlet chamber is connected to the calciner directly or by a riser duct. Bypass exhaust gas is drawn off near the inlet chamber. This exhaust gas is guided into a first mixing chamber, in which the exhaust gas is cooled to between 800 and 950° C., then the exhaust gas is guided through a reaction pipeline segment, wherein the dwell time is between 0.5 and 3 seconds and ammonia, aqueous ammonia solution, or ammonia-releasing substances are injected for denitrification. Then the exhaust gas is guided into a second mixing chamber, in which the exhaust gas is cooled to between 150 to 250° C. Then the exhaust gas is guided to a filter for dust removal.
VERFAHREN UND ANLAGE ZUR ENTSTICKUNG VON BYPASSGASEN IN EINEM MEHRSTUFIGEN SYSTEM VON MISCHKAMMERN BEI EINER ANLAGE ZUR HERSTELLUNG VON ZEMENTKLINKER
METHOD AND PLANT FOR DENITRIFYING BYPASS GASES IN A MULTI-STAGE SYSTEM OF MIXING CHAMBERS IN A PLANT FOR PRODUCING CEMENT CLINKER
PROCÉDÉ ET INSTALLATION DE DÉNITRIFICATION DU GAZ PERDU DE DÉRIVATION DANS UN SYSTÈME À MULTIPLES ÉTAGES DE CHAMBRES DE MÉLANGE DANS UNE INSTALLATION DE FABRICATION DE CLINKER
SCHÜRMANN HEIKO (Autor:in) / NASSENSTEIN FLORIAN (Autor:in) / HAND ANDREAS (Autor:in) / GUSSMANN ROLF (Autor:in)
08.05.2019
Patent
Elektronische Ressource
Deutsch
IPC:
B01D
SEPARATION
,
Trennen
/
C04B
Kalk
,
LIME
/
F27B
Industrieöfen, Schachtöfen, Brennöfen, Retorten allgemein
,
FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL
/
F27D
Einzelheiten oder Zubehör für Industrieöfen, Schachtöfen, Brennöfen oder Retorten, soweit sie nicht auf eine Ofenart eingeschränkt sind
,
DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
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