Gas hydrate management is a critical part in the flow
assurance
of oil/gas production. Completely preventing their formation can be
expensive and inefficient, while allowing them to form, ensuring transportability,
may be less costly but comes with risks of accumulation/plugging.
Gas hydrate slurry transportability is defined by the absence of agglomeration,
wall deposition, bedding, and a low pressure drop. To fully account
for each but together of these pieces, one requires robust (i) understanding
of the multiscale and multiphase flow problem, (ii) testing ability
to assess each component defining transportability, and (iii) a multidimensional
approach to map transportability for a given set of conditions. In
this paper, gas hydrate slurry transportability and stability are
investigated in gas–condensate–water systems with the
application of commercial anti-agglomerant (AA) chemicals for a range
of water cuts (up to 70%) and subcoolings (8–16 °C). Stable
gas hydrate slurries formed with AA appear as a milky solution, that
is, a homogeneous finely dispersed suspension of solids. For the conditions
identified as slurry, they are stable for: prolonged time (more than
40 h), during shut-in and restart, when changing the temperature/pressure,
and when changing shear. In the systems with high water cut (>50%),
a soft deformable suspension is seen, suggesting that enough oil is
needed to disperse the hydrates. Moreover, water conversion is shown
to be a poor metric to evaluate the risk: systems with low/slow water
conversion are shown to be riskier than systems with high/fast conversion.
Finally, a hydrate slurry phase map is presented combining the critical
measures that define transportability, allowing for a simple and clear
way to define the conditions with low and high risk.