The following focuses on the quality
of coke produced from delayed
coking blends of decant oil, coal, and resid, and it also examines
the effect of adding a cracking catalyst to each blend. We also examine
the role of coal, resid, and catalyst addition on the formation of
green coke, calcined coke, and graphitized cokes. The overall goal
was to see if use of lower quality feedstocks could produce marketable
coke. The coal sample was cleaned using the best available technology
to as low a level of ash yield (as determined by proximate analysis)
as possible. Conversion and yield results from the delayed coking
of DO, DO/coal, and DO/resid/coal as well as each reaction using catalyst
are discussed. Gas products obtained from the delayed coking experiments
were characterized, and results are discussed. Green cokes obtained
from different delayed coking processes were evaluated using optical
microscopy; the cokes were calcined and graphitized. X-ray diffraction,
temperature-programmed oxidation, and proximate/ultimate analyses
were used to characterize green coke, calcined coke, and graphitized
coke. In general, the green coke generated from the various reaction
conditions (DO and DO plus coal) produced a coke that is adequate
as an anode grade coke and is suitable as a graphite filler, but because
of either the sulfur and/or ash content is not suitable for nuclear
graphite production or metallurgical coke. In general, adding catalyst
increased the liquid yields, while decreasing the coke/gas yield,
and improved the carbon quality, but added to the ash composition.
For reactions of DO/coal/resid, the carbon is not suitable for anode
grade coke, graphite, nuclear graphite, or metallurgical coke, and
addition of catalyst actually decreased the quality of the coke.