When I back look my career at Fluor, my first and last projects are the
same: East Tank Farm for Suncor. What a coincidence!
The East Tank Farm Hot Bitumen Terminal was part of Voyageur upgrader
project, originally engineered by CB&I. Fluor was doing some revamp when I
joined in early 2011. In 2013, Suncor cancelled Voyager and altered this tank
farm to serve Fort Hills Oil Sands Mine. The tank farm will receive, store and
deliver diluent required for start-up and operations of Fort Hills, as well as
receive Fort Hills hot bitumen, cool and blend the bitumen with diluent and
deliver it to markets. East Tank Farm Development project was then set
up to build 8 more tanks and associated facilities.
Among CB&I’s design, I noticed Coriolis flow meters were used on hot
bitumen lines. Unlike volumetric flow meters, Coriolis flow meters directly
measure mass flow and product density, insensitive to pressure, temperature,
viscosity and density. With the ability to measure liquids, slurries and gases,
Coriolis flow meters are universal meters. They have high accuracy and wide
application. Considering total cost of ownership, Coriolis meters
increasingly replace differential-pressure (DP) devices, and their use is also
growing in the oil & gas industry.
So it is good to know things about Coriolis mass flow meters, especially
installation requirements as a piping designer.
How Coriolis Mass
Flow Meters Work
Coriolis flow meters measure flow by taking advantage of the Coriolis effect. When fluid travels through, the inertial effects are directly proportional to the mass flow of the fluid (Figure 1). The mass flow rate can be captured by measuring the time delay between the inlet and the outlet of the sensor.
Figure 1. Coriolis Meter Operational Principle
The
density measurement is derived from the natural frequency of oscillation of the
flow tube, which varies with mass. As the fluid becomes denser and heavier, the
vibrational frequency of the flow tubes decreases. If the volume of the flow
tube is constant, the oscillation frequency is a function of fluid density
There are
two basic configurations: (Dual) bent tube and (single) straight tube. The
Coriolis meter with two bent tubes has the highest flow sensitivity.
How to
install Coriolis Mass Flow Meters
· Coriolis flow meters are not affected by swirling fluid or non-uniform velocity profiles resulting from upstream or downstream piping configurations, so straight runs of pipe upstream or downstream are unnecessary. This is extremely beneficial if space is at a premium.
· Coriolis flow meters are not affected by swirling fluid or non-uniform velocity profiles resulting from upstream or downstream piping configurations, so straight runs of pipe upstream or downstream are unnecessary. This is extremely beneficial if space is at a premium.
· Keep the sensor tubes full of
process fluid. When measuring liquids, do not install the sensor at the highest
point for gas accumulation. When measuring gas, do not install the sensor at
the lowest point for condensate accumulation.
· Coriolis flow meters can be
installed both horizontally and vertically. If in vertical, liquids and
slurries should flow upward through the sensor. Gases should flow downward.
· If air entrainment exists, to avoid
the meter from malfunctioning, the Coriolis flow meter should be downwards mounted.
If solids are present in the flow, the flow meter should be upwards mounted to
ensure that solids do not accumulate in the flow tubes and cause misreading.
·
A shutoff valve downstream of the
sensor should always be installed to allow flow to be stopped to enable zeroing
of the flow meter.
· If there are control valves, they
should be installed downstream from Coriolis meters to increase backpressure on
them and to decrease the probability of cavitation or flashing.
· Coriolis flow meter designs resist
normal pipe vibration if the surrounding process piping properly supports the
meter. However, deposits and strong vibration can degrade accuracy.
· Pipe supports should not be attached
directly to the sensor and the sensor should never be used to support process
piping.