The reversible adsorption of SO 2 on 1,3-phenylenediamine was investigated using the step transient response technique coupled with operando infrared spectroscopy, mass spectrometry, UV−vis spectrometry, and density functional theory (DFT). At 50°C, the reaction of SO 2 at the amine site resulted in fixation of sulfur as hydrogen-bonded SO 3 2− (sulfite) and SO 4 2− (sulfate) species. Simulated infrared and UV−vis spectra at the DFT B3LYP/6-31G(d,p) level were compared to the experimental results to help characterize the infrared spectra, molecular interactions, and bonding of the adsorbing species. The theoretically calculated binding energies revealed the sulfite and sulfate species bind stronger at the ammonium sites as compared to the amine site, which agrees with the infrared spectroscopic observations. Temperature-programmed desorption showed a capacity of 1.39 mol SO 2 /mol sorbent for pure 1,3-phenylenediamine and 2.8 mol SO 2 /mol sorbent for the SiO 2 supported sorbent. The presence of sulfite and sulfate in the sorbent layer at 50°C resulted in the oxidative degradation of the amine site to produce −NO 2 groups and deactivation of adsorption sites in the sorbent. The infrared data indicates that the adsorbed sulfite and sulfate species remained strongly bonded at the ammonium site, whereas the SO 2 , sulfite, and sulfate species at the amine site may be thermally desorbed from the sorbent. The retained SO 3 2− and SO 4 2− species led to the rapid deactivation of the sorbent during multicycle testing.
INTRODUCTIONThe separation of sulfur dioxide (SO 2 ) from the flue gas in fossil fuel combustion processes are of particular interest for two primary reasons: (i) SO 2 is harmful to human health and the environment and (ii) SO 2 has the capability of poisoning the active site of various CO 2 capture technologies. 1,2 The mechanism of active site deactivation for amine-based sorbents is generally attributed to the irreversible adsorption of SO 2 and its competitive adsorption with CO 2 . The sorbent's capability to avoid irreversible reactions with SO 2 is an important characteristic for postcombustion applications. A solid amine sorbent for SO 2 removal having high adsorption capacity, longterm regeneration capacity, and low regeneration energy requirement may also improve plant operating costs. Our focus in investigating an amine-based sorbent for SO 2 removal is to study the amine reactive site in order to gain a greater understanding of the SO 2 −amine interactions with the purpose of creating a more effective SO 2 solid sorbent for the large-scale postcombustion scrubbing application.Recently, ionic liquids (ILs) have been proposed as adsorbents for acid gases such as SO 2 , 3−9 CO 2 , 10−14 and H 2 S, 15−17 as compared to technologies developed over the last several decades for flue gas desulfurization (FGD), such as limestone scrubbing, ammonia scrubbing, and adsorption by organic solvents. 18−20 These previous technologies have inherent disadvantages such as the production of large quantities of was...