Hydrate formation, aggregation, and deposition have become
major
hazards for the safe transportation of oil and gas pipelines. Although
there has been a great deal of research into the behavior of particles
during hydrate formation and transport, there is less research into
the multiphase generation and flow characteristics of hydrate gas
and liquids. In this paper, the flow characteristics of hydrate slurry
and the flow pattern transition in gas–liquid multiphase system
were studied, and the generations of it were compared between a gas–liquid
multiphase system and oil–water emulsion system. The results
showed that the flow parameters such as pressure, pressure drop, and
density fluctuated more drastically in the gas–liquid system
than that in the emulsion system, the higher fluctuation meant a higher
risk of pipe plugging. At the same time, the influence of pressure
and dosage on multiphase flow pattern transformation and boundary
change conditions were studied. A gas-slurry flow pattern transformation
diagram was drawn based on the defined transformation conditions between
flow patterns. The results also indicated that, with the increase
of pressure from 5 to 6 MPa, the boundary of slug flow and air mass
flow changed to the direction of higher gas and liquid flow velocity.
While the boundary of slug flow and wave flow, stratified flow and
wave flow changed to the direction of higher gas flow velocity. The
boundary of slug flow and air mass flow changed to the direction of
lower liquid flow velocity. In contrast, the boundary of slug flow
and wave flow, stratified flow and wave flow, slug flow and stratified
flow changed to the direction of higher gas flow velocity and lower
liquid flow velocity in the 1% inhibitor period compared with that
without the inhibitor. This study will provide theoretical references
and technological supports for the safety of multiphase transportation
pipelines and the safety of deep water production.