(225o) Adsorption of NO, NO2 and CO over Agx Faujasite with Water and Oxygen Gas – DFT, Equilibrium, and Dynamic Experiment Investigations
AIChE Annual Meeting
2023
2023 AIChE Annual Meeting
Separations Division
Poster Session: Fundamentals and Applications of Adsorption and Ion Exchange
Tuesday, November 7, 2023 - 3:30pm to 5:00pm
DFT calculations are in agreement with experimental results. The adsorption energy of these three pure species at zero coverage has the same behaviour. Different operating conditions have significant effects on the adsorption capacity of AgX. Naturally, the adsorbed amount of all chemical species reduces when temperature increases.
Dynamic Experiments showed that AgX adsorbs NO weakly, but it can be used to trap or separate CO and NO2 (Figure 1). The adsorption capacities and the breakthrough times increased in the following order: NO<CO<NO2. Also, water vapour, which assists in the generation of the roll-up, decreases the adsorbed amount and the breakthrough time.
Comparison with literature and other dynamic experiments has been performed especially thanks to experiments carried out with NaX zeolite with the same Si/Al ratio. Considering the adsorption capacity, AgX and NaX are potential adsorbents for the trapping of CO, NO and NO2; the AgX zeolite presents better adsorption capacities than NaY for NO2 and CO. However, chemical reaction occurs between both zeolites like NO2 with water, to generate NO.
This work shows AgX offering great performances and a long-term stability. However, although AgX has proven to be a very effective trap for CO, NO, and NO2, its affinity for water remains high. The breakthrough model and experiments supported by DFT calculations indicated that this approach can be applied for improving the design, scaling up and optimising the continuous fixed-bed adsorption systems to treat exhaust gases.
Figure 1: Breakthrough curve obtained for a mixture of CO, NO, NO2, O2 and water for AgX zeolite âExplanation of chemical reaction between NO and NO2 and the observation of two roll-up- CCO,in =1 000 ppm, CNO,in= CNO2,in 350 ppm, CO2,in = 8.5%, Cwater,in =1% ,Qv=70 NL h-1, T=30°C, P=101.3 kPa, granular bed length = 50 mm, diameter=10 mm, 0.355<dp<1mm, mAgX=4.515 g. AgX had previously been calcined (1°C/min & 500°C during 4h). The outlet concentration was determined by FTIR analysis.