Thermal catalytic cracking of naphtha over multi wall carbon nanotube catalysts

被引:10
作者
Alyani, Mina [1 ]
Mohamadalizadeh, Ali [2 ]
Towfighi, Jafar [1 ]
Hosseini, Nasibeh [1 ]
机构
[1] Tarbiat Modares Univ, Fac Chem Engn, Tehran, Iran
[2] Res Inst Petr Ind, Gas Res Div, Tehran, Iran
基金
美国国家科学基金会;
关键词
Thermal-catalytic cracking; Multi wall carbon nanotubes; Light olefins; Naphtha; SELECTIVE CRACKING; STEAM CRACKING; LIGHT OLEFINS; N-HEPTANE; OPTIMIZATION; PYROLYSIS; HYDROCARBONS; SIMULATION; ISOBUTANE; ZEOLITES;
D O I
10.1016/j.jaap.2012.03.002
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
The effects of temperature and Fe loading over multi wall carbon nano tube catalysts in thermal catalytic cracking of naphtha to produce light olefins have been studied in this paper. The CCD method was utilized and a set of experiments were designed and carried out. The temperature and loading varied from 572 to 628 degrees C and 0.34 to 11.66 wt.% Fe, respectively. In order to determine the effects of the variation of the operating conditions on the yield distributions, a set of statistical models were utilized and the maximum point of the yield of each product was determined. The maximum yield of ethylene (18.84 wt.% of product) and propylene (12.85 wt.% of product) was obtained at 628 degrees C and 10.6 wt.% loading of Fe over CNTs. Finally, thermal cracking of naphtha was carried out and was compared with thermal catalytic cracking of naphtha. As a result, at 620 degrees C, the yield of ethylene and propylene in thermal-catalytic cracking was 6.3% and 4.7%, respectively, more than those in thermal cracking of naphtha. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:7 / 14
页数:8
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