For
the pipeline transportation of waxy crude oil, pour point depressants
(PPDs) have been developed and used to improve its flowability at
low temperature. As supercritical CO2 (scCO2) flooding becomes a common technique to improve oilfield recovery,
how the sensitivity of PPD changes due to the degassed crude oil treated
by CO2 should be studied. In this work, the effect of scCO2 extraction on the performance of EVA in improving the flowability
of Changqing degassed crude oil is investigated by means of a self-developed
scCO2 treating equipment, SARA/HTGC analysis, SEM analysis,
pour point test, rheological measurement, asphaltene precipitation
test, particle size analysis, DSC test, and microscopic observation.
The results show that without EVA addition, scCO2 extraction
aggravates the flowability of the crude oil at low temperature. The
scCO2 extraction extracts light components from asphaltene
aggregates causing asphaltenes to precipitate, which inhibits the
asphaltenes on playing a role as the natural PPD. As a result, it
leads to the formation of smaller needle-like wax crystals with large
amount, worsening the flowability of the crude oil. When the EVA is
present, however, scCO2 extraction favors the functioning
of EVA on improving the flowability of the crude oil at low temperature.
The addition of EVA can slightly enhance the solubility of wax molecules
thus decreasing the crude oil WAT to some extent, while can significantly
change the morphology of precipitated wax crystals from small needle-like
to agglomerated clusters, thus improving the flowability of the crude
oil. Because of the synergistic effect of EVA and asphaltene aggregates
after scCO2 extraction, a more compact EVA–asphaltene–wax
ternary crystal structure will form thus further decreasing the pour
point, elastic modulus, and equilibrium viscosity at low temperature.