494343 Static and Dynamic Catalytic Adsorptive Desulfurization (CADS) of Real Diesel Using Low-Cost TiO2/Fumed Silica

Xiaoling Ren, Zewei Liu, Lei Dong and Jing Xiao, School of Chemistry and Chemical Engineering, South China University of Technology, Guangzhou, China

The catalytic adsorptive desulfurization (CADS) has been developed as a promising approach for ultra-deep desulfurization of diesel with low energy comsumption (Ren, X.; Miao, G.; Xiao, Z.; Ye, F.; Li, Z.; Wang, H.H.; Xiao, J. Catalytic Adsorptive Desulfurization Using TiO2/SBA-15 under Mild Conditions. Fuel, 2016, 174, 118-125.). In this work, low-cost fumed silica were screened as the supporting substrate for TiO2 for effective CADS of real diesel (~35 ppm-S). Effect of TiO2 loading and CADS temperature were optimized in batch reactor. The dynamic breakthrough performance was evaluated in fixed-bed reactor. The sorbent was regenerated by solvent wash followed by air oxidative treatment, and its regenerability was assessed in multiple adsorption-regeneration cycles. Results suggested that TiO2/fumed silica (300-400 mesh) with higher surface area and larger amount of Si-OH groups showed higher desulfurization capacity. The TiO2 loading was optimized to 13% with the maximized utilization of Ti catalytic sites and Si-OH adsorption sites on TiO2/fumed silica for CADS. While the CADS temperature was optimized to 35°C with the balanced catalytic activity for the oxidation of dibenzothiophenes (and their derivatives, 4,6-DMDBT mainly) and minimized desorption of yielded dibenzothiophene sulfones. With a suitable O/S ratio of 5, and overall aspect ratio of 10, the TiO2/fumed silica showed the maximal desulfurization capacity of 1.44 mg-S/g-A of real diesel at the breakthrough concentration of 5 ppm-S. Considering the effect of the dimension of fixed bed, the dynamic desulfurization performance with varied aspect ratio followed the order of H/R=10 > H/R=22 ~ H/R=5. The S-breakthrough concentration decreased with increased O/S ratio. The superior regenerability of TiO2/fumed silica was suggested by no loss on desulfurization capacity was observed after six adsorption-regeneration recycles. The CADS using the low-cost TiO2/fumed silica adsorbent with superior desulfurization capacity and remarkable stability provide an effective and economic approach for ultra-deep desulfurization of real diesel with low energy consumption.

Keyword: catalytic adsorptive desulfurization, TiO2/fumed silica, diesel, dynamic adsorption.


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