High polar asphaltenes are easy to
precipitate and deposit in transportation
pipelines and subsequent processing. Adding chemical polymer inhibitors
is an effective method to inhibit asphaltene aggregation. In this
work, ionic liquid polymers containing the imidazole cation and/or
alkyl branches were synthesized by free radical polymerization, and
anions such as the bis(trifluoromethane)sulfonimide ion (TFSI–) and [phosphoric acid bis(2-ethylhexyl)] anion (DEHP–) were introduced by substitution. The chemical structure
of asphaltenes was analyzed by Fourier transform infrared spectroscopy, 1H nuclear magnetic resonance, elemental analysis, and time-of-flight
spectroscopy. It is found the asphaltene has short side chain, a low
H/C, and a high polarity. The precipitation inhibition of asphaltenes
and the rheological behaviors of crude oil in the presence of ionic
liquid polymers were studied by measuring the initial precipitation
point (IPP), turbidity, particle size distribution, and morphology
of asphaltenes in model oil. In the presence of same anions (Br–, TFSI–, and DEHP–), with the increase of length of imidazole pendant branches, the
IPPs increase. However, when the chain length is close to the poor
solvent n-heptane, the IPP first rises, then descends.
The copolymer bearing both imidazole pendants and alkyl branches can
increase the IPPs. Alkyl branches can inhibit the aggregation of asphaltenes
by forming layers surrounding the asphaltene aggregates. With the
reduction of asphaltene agglomeration, the turbidity and particle
size decrease. For polymers bearing both the imidazole pendants and
alkyl branches, upon the increase of anionic electronegativity, the
interactions between asphaltenes are destroyed because strong hydrogen
bonding is generated between the asphaltene and the ionic liquid polymer.
DEHP– has strong electronegativity and high hydrophobicity.
The polymer with DEHP– and alkyl branches can increase
the IPP by 30%, reduce the turbidity of model oil by 50%, reduce the
size of asphaltene by 80%, and decrease the viscosity of crude oil
by 36.8% at 50 °C.