Kinetic hydrate inhibitors
(KHIs) have been used for over 25 years
to prevent gas hydrate formation in oil and gas production flow lines.
The main component in KHI formulations is a water-soluble polymer
with many amphiphilic groups, usually made up of amide groups and
adjacent hydrophobic groups with 3–6 carbon atoms. KHI polymers
are one of the most expensive oilfield production chemicals. Therefore,
methods to make cheaper but effective KHIs could improve the range
of applications. Continuing earlier work from our group with maleic-based
polymers, here, we explore maleic acid/alkyl acrylate copolymers as
potential low-cost KHIs. Performance experiments were conducted under
high pressure with a structure II-forming natural gas mixture in steel
rocking cells using the slow (1 °C/h) constant cooling test method.
Under typical pipeline conditions of pH (4–6), the performance
of the maleic acid/alkyl acrylate copolymers (alkyl = iso-propyl, iso-butyl, n-butyl, tetrahydrofurfuryl,
and cyclohexyl) was poor. However, good performance was observed at
very high pH (13–14) due to the thermodynamic effect from added
salts in the aqueous phase and the removal of CO2 from
the gas phase. A methyl maleamide/n-butyl acrylate
copolymer gave very poor performance, giving evidence that direct
bonding of the hydrophilic amide and C4 hydrophobic groups is needed
for good KHI performance. Reaction of the maleic anhydride (MA) units
in MA/alkyl acrylate 1:1 copolymers with dibutylaminopropylamine or
dibutylaminoethanol gave polymers with good KHI performance, with
MA/tetrahydrofurfuryl methacrylate being the best. Oxidation of the
pendant dibutylamino groups to amine oxide groups improved the performance
further, better than poly(N-vinyl caprolactam).