To alleviate the hydrate blockage risk in oil and gas
pipelines/production
facilities, thermodynamic hydrate inhibitors (THIs) and kinetic hydrate
inhibitors (KHIs) are the frequently used additives/chemicals. While
these additives are highly effective, the impact of low dosage of
THIs (under inhibited systems) and performance of KHIs at high water
cut and/or high subcooling is not well understood. In this work, a
high-pressure visual stirred tank reactor was employed to investigate
the impact of THIs and KHIs on the kinetics of the complex hydrates
of natural gas mixtures (CH4/C2H6/C3H8) and cyclopentane at high water-cut and
high subcooling (∼21 °C). Various concentrations of a
THI, mono-ethylene glycol (MEG) with a dosage ranging from 0.1 to
25 wt %, and multiple KHIs (polyvinylpyrrolidone (PVP k-30, PVP k-90),
caprolactam, butyl glycol ether (BGE), and polyglycerin with 0.1 wt
% dosage) were evaluated for hydrate formation kinetics, onset hydrate
formation/nucleation temperature, and morphological changes. Gas uptake
results reveal that hydrate blockage risk is higher at low MEG content
(0.1 to 10 wt %) compared to the baseline, while a significant reduction
in gas uptake was observed for the high MEG content trials (20–25
wt %). With 20 and 25 wt % MEG, the hydrate nucleation temperature
was reduced by 10–12 °C compared to the baseline. In context
to KHIs impact, 0.1 wt % BGE and caprolactam promoted the nucleation
temperature and the rate of hydrate formation/gas uptake. However,
PVPs not only reduced the gas uptake kinetics but also lessened the
hydrate nucleation temperature by 6–8 °C compared to the
baseline data. Our results may offer new insights into optimizing
hydrate inhibitors dosage to diminish the risk of hydrate blockage
in subsea pipelines.