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Thermal regeneration and decoking optimization of chlorinated platinum/alumina catalysts for the isomerization process

机译:氯化铂/氧化铝催化剂的热再生和剥离优化异构化过程

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The samples of spent chlorinated Pt/Alsub2/subOsub3/sub catalysts that were used in the isomerization process were decoked at elevated temperatures under airflow and different oxygen concentrations. The surface of the catalyst was characterized by thermal gravimetric analysis, differential scanning calorimetry, Brunauer-Emmett-Teller analysis, attenuated total reflection fast Fourier infrared spectroscopy, scanning electron microscopy and energy-dispersive X-ray elemental mapping. The effective parameters for the catalyst decoking optimized were coke burning temperature (450-600 ), temperature ramp (5-25 /min) and oxygen content of the feed gas (0.5-2.0% vol.) in a tubular fixed-bed reactor using the response surface experimental design method. The spectroscopic tests were set based on the absorbance at 1390 cmsup-1/supsub,/sub representing the surface coverage of platinum-alumina, and the results revealed that the greatest safe regeneration of chlorinated Pt/Alsub2/subOsub3/sub catalyst is achieved under a specific concentration of oxygen, temperature domain and thermal ramp. Moreover, the mechanism and the reaction rates of the decoking step of the catalyst regeneration were examined and the kinetic parameters of chlorinated Pt/Alsub2/subOsub3/sub decoking were determined.
机译:在气流和不同氧浓度下的升高的温度下,在异构化过程中使用的废氯化Pt / al 2 o 3 / sub>催化剂的样品。通过热重分析,差示扫描量热法,Brunauer-Emmett-excuals分析,减弱全反射快速傅里叶红外光谱,扫描电子显微镜和能量 - 分散X射线元素映射的催化剂表面的表征。优化催化剂衰减的有效参数是焦炭燃烧温度(450-600),温度斜坡(5-25 / min)和进料气体(0.5-2.0%Vol.)的氧含量在管状固定床反应器中使用响应面实验设计方法。基于1390cm -1-sup> 表示铂 - 氧化铝表面覆盖的吸光度,结果表明,结果表明,氯化Pt的最大安全再生/ Al 2 O 3 催化剂在特定浓度的氧气,温度域和热斜坡下实现。此外,研究了催化剂再生的衰减步骤的机制和反应速率,并测定了氯化Pt / Al 2 o 3 脱焦的动力学参数。

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