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Kinetic Studies on Enhanced Mercury Adsorption in Zeolite Nay and Waste Fcc Catalyst

机译:沸石NY和废FCC催化剂增强汞吸附的动力学研究

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The mercury (II) removal was studied using two adsorbents: waste FCC Catalyst and NaY zeolite, those materials were characterized under test such as TGA, XRD, IR, immersion enthalpy and N2 adsorption isotherms. The zeolite superficial area is 773 m~2/g and that of the FCC catalyst is 135 m~2/g. The maximum mercury adsorption capacity was 1.8561mg/g for the FCC catalyst and 2.6845 mg/g for the zeolite. The equilibrium isotherms were described with the Langmuir and Freundlich linear models. Besides, the kinetics was described with the Lagergren and Pseudo-second order, the latter fit better in the experiments. After the use of the adsorbents, they were regenerated, acquiring their superficial areas as 675 and 87 m~2/g for the NaY zeolite and the FCC catalyst, respectively.
机译:使用两种吸附剂研究了汞(II)去除:废弃FCC催化剂和NAY沸石,这些材料被测测试,例如TGA,XRD,IR,浸渍焓和N2吸附等温线。沸石浅表面积为773m〜2 / g,FCC催化剂的催化剂为135m〜2 / g。 FCC催化剂的最大汞吸附能力为1.8561mg / g,沸石2.6845mg / g。用Langmuir和Freundlich线性模型描述了平衡等温线。此外,通过Laggrgren和伪二次顺序描述了动力学,后者在实验中适合。在使用吸附剂之后,再生,分别再生,得到它们的浅表区域为675和87m〜2 / g,分别用于NAY沸石和FCC催化剂。

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