Thermal cracking
(TC) of the Athabasca vacuum residue (ATVR) and
its deasphalted product [deasphalted oil (DAO)] was studied. A comparison
of conversion and product properties between TC and ultradispersed
catalytic steam cracking (CSC) upgrading of both feedstocks is also
reported, using K–Ni catalysts. Thermal conversions with stable
products for the deasphalted fraction (DAO), reached 20% (w/w) higher
values than the ATVR. DAOCSC provided 8% (w/w) increased conversion
compared to DAOTC, with stable products. Higher thermal conversions
for the DAO compared to the vacuum residue were explained in term
of the better properties determined for the asphaltenes produced in
DAO upgrading, i.e., higher hydrogen content and better solubilization
properties due to lower molecular sizes, solubility parameters, and
aromaticities. A definitive link between the nature of produced asphaltenes
and products stabilities, as measured via P-value,
was found. Higher DAO-steam catalytic conversions with stable products
were also obtained and rationalized based on the occurrence of water
splitting into *H and *OH radicals and hydrogen production from steam
reforming/steam cracking reactions occurring during CSC processing.
The inhibition of hydrocarbon free radical recombination (coking)
by *H capping and hydrogenation facilitated by Ni catalysts are believed
key reactions occurring, leading to better DAO product properties.
Exploratory evidence gathered with the NiCeMo CSC-catalyst for whole
bitumen processing added support to the later findings, i.e, olefin
production inhibition was evidenced, indirect evidence of hydrogenation
occurrence. A convenient field upgrading process that avoids distillation
or separation (deasphalting) carried out at low T, P is, thus, envisaged.