13
Annual Report 2015
Controlled separation of gas, oil and water, efficient treatment and handling of the
produced water and reliable transport of the hydrocarbons are central areas in sub-
sea processing. In order to optimise these processes, proper fluid characterization
and fundamental understanding of the underlying phenomena, like flocculation,
coalescence, precipitation, sedimentation and creaming, is required. The overall
goal is to develop new methods for advanced fluid characterization at conditions
relevant for subsea processing. During the first three years of SUBPRO, the focus
is on developing:
• methods for studying oil drop and gas bubble coalescence at elevated
temperature and pressure in order to facilitate design of subsea water treatment systems
• experimental and simulation methods for predicting build-up and ageing of wax deposits
• sequential separation as an approach for investigating the quality of the oil and water phases at different separation stages
• a new coalescence model
SEPARATION – FLUID CHARACTERIZATION
Research area manager,
Prof. Johan Sjöblom
Research area co-manager, Prof. Gisle Øye
Produced water quality and injectivity
Project manager and PhD
supervisor Prof. Gisle Øye
A major challenge during subsea processing
is treatment of produced water. Dispersed oil
and solids must be separated from the water so
that it reaches sufficient quality to be reinjected
into reservoirs or eventually discharged to sea.
Merging (coalescence) between oil drops or
between oil drops and gas bubbles is a central
phenomenon that will promote the separation.
In this project, the objective is to study how the
chemical composition of crude oil and water influ-
ence the route to drop-drop and drop-bubble coa-
lescence (see Figure 11) at elevated pressure and
temperature. A new microfluidic setup is built for
this purpose. The fundamental knowledge of the
produced water fluids gained in the project can be
applied in design of subsea water treatment sys-
tems for reliable water management. The project
will be carried out in close collaboration with Aker
Solutions, ENGIE, Lundin Norway and Statoil.
PhD student,
Marcin Dudek
Figure 11. The route to coalescence between two oil
drops (determined by a drop-bubble micropipette
setup)
A) Drops approaching
B) Thinning of the aqueous film between the drops
C) Breakage of the thin film
D) Merging of drops
E) Completely merged drops