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A new approach to deep desulfurization of gasoline by electrochemically catalytic oxidation and extraction

机译:电化学催化氧化萃取法对汽油进行深度脱硫的新方法

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In order to further reduce the sulfur content in gasoline,a new desulfurization process for gasoline was obtained by means of electrochemically catalytic oxidation and extraction with an electrochemical fluidized-bed reactor.The particle group anode was activated carbon-supported lead dioxide (beta-PbO2/C).The electrolyte was aqueous NaOH solution,and copper pillar was cathode in the electrochemical reactions.The fi-Pb02/C particle group anodes can remarkably accelerate the electrochemical reaction rate and promote the electrochemical catalysis performance for the electrochemical desulfurization reaction.Also,gasoline desulfurization rule was investigated in an alkali solution.The experimental results indicated that the optimal desulfurization conditions were as follows;the cell voltage,the pH value of the electrolyte,feed volume flow rate and the beta-PbO2 percentage by weight were 3.2 V,pH value 13.1,300 ml min~(-1) and 5.0 wt.%,respectively.Under these conditions the concentration of sulfur in gasoline was reduced from 310 to 40 mug g~(-1),and the main properties of the product were not significantly affected.Based on these experimental results,a mechanism of indirect electrochemical oxidation was proposed.
机译:为了进一步降低汽油中的硫含量,通过电化学催化氧化和电化学流化床反应器萃取,获得了一种新的汽油脱硫工艺。粒子群阳极是活性炭负载的二氧化铅(β-PbO2) / C)。在电化学反应中,电解质为NaOH水溶液,铜柱为阴极.fi-PbO2 / C粒子群阳极可显着加快电化学反应速率,并促进电化学脱硫反应的电化学催化性能。实验结果表明,最佳脱硫条件为:电池电压,电解液的pH值,进料流量,β-PbO2重量比为3.2V。 pH值分别为13.1,300 ml min〜(-1)和5.0 wt。%。将汽油中的硫从310马克降低到40马克·g(-1),并且产品的主要性能没有受到明显的影响。基于这些实验结果,提出了一种间接电化学氧化的机理。

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