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In situ FT-IR spectroscopy investigations of carbon nanotubes supported Co-Mo catalysts for selective hydrodesulfurization of FCC gasoline 被引量:3

In situ FT-IR spectroscopy investigations of carbon nanotubes supported Co-Mo catalysts for selective hydrodesulfurization of FCC gasoline
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摘要 To better understand the nature of carbon nanotubes supported Co-Mo catalysts (Co-Mo/CNTs) for selective hydrodesulfurization (HDS) of fluid catalytic cracking (FCC) gasoline, studies are carried out using in situ Fourier transform infrared spectroscopy (FT-IR). The catalytic performances of Co-Mo/CNTs catalysts were evaluated with a mixture of cyclohexane, diisobutylene, cyclohexene, 1-octene (60 : 30 : 5 : 5, volume ratio) and thiophene (0.5%, ratio of total weight) as model compounds to simulate FCC gasoline. The HDS experimental results suggested that the HDS activity and selectivity of Co-Mo/CNTs catalysts were affected by Co/Mo ratio; the optimal Co/Mo atomic ratio is about 0.4, and the optimum reaction temperature is 260 ℃. The in situ FT-IR studies revealed that 1-octene can be completely saturated at 200 ℃. In the FT-IR spectra of diisobutylene, the characteristic absorption peak around 3081 cm^-1 for the stretching vibration peak of =C-H bond was still clear at 320 ℃ indicating that diisobutylene is difficult to be hydrogenated. As for the thiophene, no characteristic absorption peak could be found around 3092 cm^-1 and 835 cm^-1 when the reaction temperature was raised to 280 ℃, indicating that thiophene had been completely hydrodesulfurized. On the basis of FT-IR results, it can be deduced that thiophene HDS reaction occurred mainly through direct hydrogenolysis route, whereas thiophene HDS and diisobutylene hydrogenation reaction over Co-Mo/CNTs catalysts might occur on two different kinds of active sites. 为了更好理解碳 nanotubes 的性质,为液体的选择 hydrodesulfurization (HDS ) 支持了合作瞬间催化剂(Co-Mo/CNTs ) 催化裂开(FCC ) 汽油,研究被执行在 situ Fourier 使用转变红外线的光谱学(英尺红外) 。Co-Mo/CNTs 催化剂的催化表演与环己烷的混合物被评估, diisobutylene, cyclohexene, 1-octene (60:30:5:5,体积比率) 并且 thiophene (0.5% ,全部的重量的比率) 当模型加重模仿 FCC 汽油。HDS 试验性的结果建议 Co-Mo/CNTs 催化剂的 HDS 活动和选择被公司 / 瞬间比率影响;最佳的公司 / 瞬间原子比率是大约 0.4,并且最佳反应温度是在揭示的 situ 英尺红外研究的 260 ° C 那 1-octene 能完全在 200 ° C 被浸透。在 diisobutylene 的英尺红外系列,在为 =C-H 债券的拉长的颤动山峰的 3081 厘米 <sup>&#8722;1</sup> 附近的典型吸收山峰在 320 ° C 仍然是清楚的,显示 diisobutylene 是困难的是 hydrogenated。至于 thiophene,当反应温度被提起到 280 ° C 时,没有典型吸收山峰能在 3092 厘米 <sup>&#8722;1</sup> 和 835 厘米 <sup>&#8722;1</sup> 附近被发现,显示有的那 thiophene 完全水疗院 desulfurized。根据英尺红外结果, thiophene HDS 反应主要通过直接 hydrogenolysis 线路发生了,这能被推出,而在 Co-Mo/CNTs 催化剂上的 thiophene HDS 和 diisobutylene 加氢反应可能发生在活跃地点的二种不同类型上。
出处 《Journal of Natural Gas Chemistry》 EI CAS CSCD 2008年第2期165-170,共6页 天然气化学杂志(英文版)
基金 National Basic Research Program of China ("973"Program,No.2004CB217807)
关键词 in situ FT-IR HYDRODESULFURIZATION carbon nanotubes HYDROGENOLYSIS THIOPHENE FCC gasoline 流化床催化裂化汽油 加氢脱硫作用 碳纳米管 氢解作用 噻吩 钴-锰催化剂
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参考文献11

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