An Experimental Investigation of the Conversion of NO to NO2 at High Pressure

Author(s):  
James W. Hunderup ◽  
Richard J. Roby

Unexpectedly high concentrations of NO2 have been noted in stack emissions from industrial combustors. NO2 formation has been reported to occur through the so called “HO2 mechanism” in which NO combines with HO2 to produce NO2 and OH. In this study, the formation of NO2 was investigated at super-atmospheric pressures through experiments and computer modeling. Computer modeling utilized the CHEMKIN chemical kinetics program and a subset of a previously published C-H-O-N system mechanism. Experimental work was conducted using a high pressure flow reactor designed and built in the course of the study. The effects of pressure, temperature, and the presence of a NO2 promoting hydrocarbon, methane, were investigated. It was discovered that as pressure increased from 1 atm. to 8.5 atm., the rate and amount of NO converted to NO2 also increased. The results also show a temperature “window” between approximately 800 K and 1000 K in which NO to NO2 conversion readily occurred. The presence of methane was seen to enhance NO conversion to NO2, and a ratio of [CH4]/[NO] was found to be a useful parameter in predicting NO2 formation. Significant NO conversion to NO2 was noted for [CH4]/[NO]>1 at the hydrocarbon injection point. Experimental results validated those trends obtained from modeling with a modified C-H-O-N mechanism.

1996 ◽  
Vol 118 (4) ◽  
pp. 756-764 ◽  
Author(s):  
J. W. Hunderup ◽  
R. J. Roby

Unexpectedly high concentrations of NO2 formation have been noted in stack emissions from industrial combustors. NO2 formation has been reported to occur through the so-called “HO2 mechanism” in which NO combines with HO2 to produce NO2 and OH In this study, the formation of NO2 was investigated at superatmospheric pressures through experiments and computer modeling. Computer modeling utilized the CHEMKIN chemical kinetics program and a subset of a previously published C–H–O–N system mechanism. Experimental work was conducted using a high-pressure flow reactor designed and built in the course of the study. The effects of pressure, temperature, and the presence of a NO2-promoting hydrocarbon, methane, were investigated. It was discovered that as pressure increased from 1 atm to 8.5 atm, the rate and amount of NO converted to NO2 also increased. The results also show a temperature “window” between approximately 800 K and 1000 K in which NO to NO2 conversion readily occurred. The presence of methane was seen to enhance NO conversion to NO2, and a ratio of [CH4]/[NO] was found to be a useful parameter in predicting NO2 formation. Significant NO conversion to NO2 was noted for [CH4]/[NO] > 1 at the hydrocarbon injection point. Experimental results validated those trends obtained from modeling with a modified C–H–O–N mechanism.


2003 ◽  
Vol 48 (8) ◽  
pp. 9-18 ◽  
Author(s):  
C. Fux ◽  
K. Lange ◽  
A. Faessler ◽  
P. Huber ◽  
B. Grueniger ◽  
...  

Separate biological elimination of nitrogen from the digester supernatant of a municipal wastewater treatment plant (WWTP) was investigated in pilot and full-scale plants. Denitrification mainly via nitrite was achieved in a sequencing batch reactor (SBR) and a continuous flow reactor (CSTR or SHARON). Suppression of nitrite oxidation in the SBR was feasible at short aerobic/anaerobic intervals allowing for immediate denitrification of the produced nitrite. Nitrate production could also be stopped by exposing the biomass to anaerobic conditions for 11 days. Temporarily high concentrations (up to 80 gNH3-Nm-3) of free ammonia could not be considered as the major reason for inhibiting nitrite oxidation. In a full-scale SBR plant 90% of the nitrogen load was denitrified in a total hydraulic retention time (HRT) of 1.6 days and with a sludge age between 15 and 20 days. Ethanol and methanol were used for denitrification. The specific average substrate consumption was 2.2 gCODdosedg-1Nremoved with an effective biomass yield of 0.2 gCODbiomassg-1CODdosed. No dosing with base was required. In the SHARON process full nitrogen elimination was achieved only with a total HRT greater than 4 days at 29°C. The overall costs were estimated at €1.4 kg-1Nremoved for the SBR and €1.63 kg-1Nremoved in SHARON mode, respectively. The SHARON process is simple in operation (CSTR) but the tank volume has to be significantly greater than in SBR.


2017 ◽  
Vol 82 (2) ◽  
pp. 1073-1084 ◽  
Author(s):  
Jennifer Tsoung ◽  
Andrew R. Bogdan ◽  
Stanislaw Kantor ◽  
Ying Wang ◽  
Manwika Charaschanya ◽  
...  

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