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Process design for gas condensate desulfurization and synthesis of nano-13X zeolite adsorbent: equilibrium and dynamic studies

机译:气体冷凝物脱硫和合成纳米13X沸石吸附剂的工艺设计:平衡和动态研究

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This paper summarizes the results of a study of adsorption of sulfur compounds from a high-sulfur feed on improved spherical-shaped nano-AgX zeolite. For this purpose, the nano-AgX zeolite was initially synthesized and improved with silver compounds such as silver nitrate, and then it was utilized in the adsorption process. In order to investigate the equilibrium and dynamics of the adsorption process, adsorptive desulfurization of real feed (i.e., sour gas condensate from the South Pars gas field) was carried out in batch and continuous processes under several operating conditions; a temperature-dependent Langmuir isotherm model was used to fit the equilibrium data. The value of monolayer adsorption capacity ( q _(m))?and adsorption enthalpy (left( {Delta H} ight)) were calculated to be 1.044?mmol/g and 16.8?kJ/mol, respectively. Furthermore, a detailed theoretical model was employed in order to model the breakthrough experiments. The results revealed that an increase in the feed flow rate and (1/T) values will cause linear and exponential increase in the total mass transfer coefficient ((k_{ext{s}})). Isotherm and dynamic breakthrough models were found to be in agreement with the experimental data.
机译:本文总结了在改进的球形纳米-AgX沸石上从高硫饲料吸附硫化合物的研究结果。为此目的,最初合成纳米-Agx沸石并用银化合物如硝酸银,然后在吸附过程中得到改善。为了探讨吸附过程的平衡和动力学,在几种操作条件下,在批量和连续的过程中进行真实饲料(即酸气体凝结物)的真实饲料(即酸气体冷凝物);使用温度依赖的Langmuir等温模型来拟合平衡数据。单层吸附容量的值(Q _(m))?和吸附焓(左({ delta h} 右))分别计算为1.044?mmol / g和16.8?kj / mol。此外,采用详细的理论模型来模拟突破性实验。结果表明,饲料流速和(1 / t )值的增加将导致总质量传递系数的线性和指数增加((k_ { text {s}})。发现等温线和动态突破模型与实验数据一致。

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