کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
231105 | 1427411 | 2012 | 9 صفحه PDF | دانلود رایگان |

A commercially produced petroleum pitch (M-50) consisting of PAH oligomers was fractionated via supercritical (SC)/dense-gas extraction, using two packed columns operating in series on a continuous basis. In the 1st column, toluene was used as the SC solvent, and a monomer- and dimer-rich cut was obtained as the top product. In the 2nd column, supercritical pentane was used to obtain 96+% pure monomer (as top product) and 96+% pure dimer (as bottom product) streams. All of the monomer and almost 90% of the dimer present in the original feed pitch were recovered in these two product streams. High (>10) solvent-to-feed ratios, positive column temperature gradients, and rectifying/stripping (vs. stripping only) operation were all found to significantly improve selectivities for a given oligomer. The above two-column setup was also used to isolate a trimer-rich cut by using SC toluene as the solvent for both columns.
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► An oligomeric petroleum pitch (M-50) was fractionated on a continuous basis via supercritical extraction, using two packed columns operating in series.
► Obtained improved selectivities at high solvent-to-pitch ratios and positive column temperature gradients while operating columns in rectifying/stripping mode.
► Isolated 96+% monomer and dimer fractions of M-50 pitch.
► Supercritical toluene used to obtain a 60% pure trimer.
► Mass balance around the two columns yields composition estimate of M-50 as 49 ± 1 wt% monomer, 26 ± 1 wt% dimer, and 25 ± 1 wt% trimer and higher oligomers.
Journal: The Journal of Supercritical Fluids - Volume 66, June 2012, Pages 120–128