丁烷结合使用天然的葵花纳米粒子催化剂

Teguh Kurniawan, Oki Muraza
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引用次数: 1

摘要

烯烃需求的增加、热裂解能耗的高和石油消耗是寻找新工艺生产烯烃的驱动力。正丁烷催化裂化是生产烯烃的一条很有前途的途径。本文以天然沸石为原料,采用球磨重结晶法合成了纳米颗粒,并研究了纳米沸石上的酸脱铝对其催化性能的影响。使用扫描电子显微镜对颗粒尺寸进行目视评估。用X射线衍射分析方法研究了沸石相及其结晶度。用氨TPD和吡啶FTIR研究了纳米丝光沸石上酸性脱铝对酸度的影响。沸石的织构性质通过-196℃下的氮物理吸附进行表征。在正丁烷裂解制烯烃的固定床反应器中对催化剂进行了测试。在固定床反应器中,正丁烷裂化采用了350℃至650℃的各种温度条件。在350℃和650℃下,正丁烷的转化率分别为15%和90%。对烯烃的选择性从350℃时的1%提高到650℃时的47%。
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Perengkahan n-Butana Menggunakan Katalis Nanopartikel Zeolit Alam Klaten
 Increasing demand on olefins, high energy consumption of thermal cracking and oil depletion are the driving force to find new process to produce olefins. Catalytic cracking of n-butane is promising route to produce olefins. In this paper, we synthesized nanoparticle from natural zeolites by ball milling-recrystallization method and studied the effect of acid dealumination over the nanozeolites on the catalytic properties. Particle size was evaluated visually by using scanning electron microscope.  X-Ray Diffraction analysis was performed to study zeolites phase and its crystallinity. Acid dealumination effect over nanosized mordenite on the acidity were evaluated by ammonia TPD and pyridine FTIR. Textural properties of zeolites were characterized by nitrogen physisorption at -196 oC. The catalysts were tested in a fixed bed reactor for n-butane cracking to olefins product. Various temperature conditions were applied ranging from 350 oC to 650 oC for n-butane cracking in a fixed bed reactor. Conversions of n-butane were 15% and 90% at 350 oC and 650 oC, respectively. Selectivity to olefins was increase from 1% at 350 oC to 47% at 650 oC.   
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发文量
10
审稿时长
16 weeks
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