澳门银河赌场注册送38-澳门银河赌场招人好招吗_百家乐德州_全讯网下载 (中国)·官方网站

Adsorbent regeneration is critical for a continuous adsorption–regeneration process and often underestimated. In this work, the regeneration of bifunctional Ag_XO@SBA-15 for [O]-induced reactive adsorptive desulfurization of liquid fuel is reported and further investigated. The spent Ag_XO@SBA-15 was regenerated in various types of solvents followed by calcination and tested in multiple desulfurization–regeneration cycles. The effects of regenerate solvents were also compared systematically. The original and regenerated Ag_XO@SBA-15 was characterized by X-ray diffraction, transmission electron microscopy, energy-dispersive X-ray spectroscopy, N₂ adsorption, X-ray photoelectron spectroscopy and atomic absorption spectrometry. The recovery of desulfurization capacity using various solvents follows the order of acetonitrile＞acetone＞ethanol＞methanol＞water. Owing to the complete reduction of silver species to Ag⁰ and severe agglomeration of Ag⁰, the bifunctional Ag_XO@SBA-15 demonstrating＞85% (2.60 mg-S/g) of sulfur removal dramatically reduced to＜46% (1.56 mg-S/g) after only 1st-cycle regeneration. It is suggested that polar organic species strongly adsorbed (or residual) on the spent Ag_XO@SBA-15, in that case, after solvent wash may contribute to the accelerated decomposition of Ag⁺ to Ag⁰ in the following calcination step. The desulfurization capacity decreased rather mildly in the later regeneration runs. Cautious choice of regeneration conditions and strategies to rational design stabilized adsorbents is required to avert the adsorbent deactivation.