This paper describes the identification of nitrogen-containing compounds in a typical feed for
diesel oil hydrotreating and how their individual concentrations change upon hydrotreating over
a conventional sulfided CoMo/Al2O3 catalyst at commercial conditions. A preconcentration
procedure followed by gas chromatographic (GC) analysis utilizing a highly sensitive nitrogen-specific detector (atomic emission detector) allowed the quantitative analysis of individual
nitrogen-containing compounds (N compounds) at levels as low as 0.05 μg N/mL. The nitrogen
compounds in the feed and products were identified by comparison with reference compounds
as well as by high-resolution GC/mass spectrometric characterization. The relative reactivities
of individual compounds in the diesel fuel feed were determined and the most refractory
compounds identified. Alkyl-substituted carbazoles were found to be the major compound class
in the feed and to be among the least reactive N compounds in the feed. Just as in the case of
alkyldibenzothiophene hydrodesulfurization, carbazoles having alkyl substituents at positions
adjacent to the nitrogen atom were found to be the least reactive N compounds in the diesel
fuel feed for hydrodenitrogenation.
In this paper, we describe the investigation of chemical vapor
deposition (CVD) of carbon from benzene
and cyclohexane on a particular pitch-based active carbon fiber (ACF)
at different deposition temperatures
as a means of controlling the pore size of ACF in order to induce true
molecular sieving capability and
to discuss the mechanism of carbon deposition. This study showed
that the specific temperature range
700−800 °C was very effective. In this range, deposition of
amorphous carbon was restricted to the pore
wall and became saturated at the level of 11% weight increase, as
further deposition stopped. This treatment
greatly enhanced the molecular sieve separation of CH4 from
CO2. Reduction of pore size appeared to
be
limited by the thickness of the benzene plane, since no further carbon
deposit took place when the pore
could no longer accept benzene. Higher temperatures allowed
deposition to occur on the outer surface of
ACF, which plugged the pore completely on extended reaction time.
Cyclohexane was found to be inferior
to benzene as a carbon precursor, as it decomposed too rapidly in the
gas phase at the temperature range
used and precipitated the carbon plugging the pores. Thus, high
molecular sieving selectivity was not
obtained.
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