z-logo
Premium
Simultaneous catalytic reduction of N 2 O and NO x produced in a fluidized bed incineration of sewage sludge
Author(s) -
Lee SeungJae,
Ryu InSoo,
Jeon SangGoo,
Moon SeungHyun
Publication year - 2015
Publication title -
greenhouse gases: science and technology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.45
H-Index - 32
ISSN - 2152-3878
DOI - 10.1002/ghg.1504
Subject(s) - incineration , sewage sludge , fluidized bed , catalysis , sewage , chemistry , waste management , nitrogen , pulp and paper industry , environmental science , environmental engineering , organic chemistry , engineering
Fluidized bed incineration of sewage sludge could produce large amounts of N 2 O due to the relatively high nitrogen content of the sewage sludge and low incineration temperatures. In this study, N 2 O and NO x emissions released during the fluidized bed incineration of dried sewage sludge powder were investigated. Sewage sludge feeding rate was about 8∼10 kg/h, and bed aspect ratio was fixed to ca. 1.2. Superficial velocity was adjusted to ca. 1.9 m/s. The concentrations of N 2 O and NO x in the exhaust gas were greatly influenced by bed temperature in a range between 850 °C and 950 °C. In the simultaneous catalytic reduction of N 2 O and NO x on an Fe/BEA pellet catalyst with NH 3 , most of the N 2 O and NO x were removed when heated above the inlet reaction temperature 410 °C. Thus, simultaneous catalytic reduction was shown to be a promising N 2 O abatement technology for the fluidized bed incineration of sewage sludge. © 2015 Society of Chemical Industry and John Wiley & Sons, Ltd

This content is not available in your region!

Continue researching here.

Having issues? You can contact us here
Accelerating Research

Address

John Eccles House
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom