Hydrate
agglomeration and blockage have emerged as significant
challenges in deep-water oil and gas exploitation. Currently, there
are limited studies on the velocity and distribution of hydrate particles
inside the pipe as they move during the flow process. This study utilizes
computational fluid dynamics (CFD)–discrete element method
(DEM) methods to simulate the flow process of hydrate slurry in a
horizontal pipe. The results indicate that at low flow rates, the
pressure drop is predominantly influenced by the agglomeration of
hydrate particles and the formation of sedimentary moving beds. On
the other hand, at high flow rates, the augmentation of flow pressure
drop predominantly arises from the dissipation of energy caused by
frictional losses occurring between the fluid and the inner surface
of the pipeline. A detailed analysis is presented on the velocity
fluctuations affecting the motion of hydrate particles. The analysis
illustrates that particle velocity is lower in the region near the
wall enriched with hydrate particles, while the velocity of particles
in the uniformly distributed area at the center is higher. The results
obtained from this study provide a comprehensive theoretical framework
for further exploration into the evolutionary patterns of hydrate
plugging.