The critical procedure
of drying offshore pipelines to allow safe transportation of natural gas is
greatly aided by use of pigs of borate-crosslinked gel, uncrosslinked gel, and
methanol pumped through the pipelines. A pig can be a piece of hardware or a
compartment of liquid pushed through a line by pressure to clean the line,
remove obstructions, dry out the line, or other functions.
A single train of
mechanical pigs and gel, driven by gas or drying liquid, can be pumped through
the pipeline to dewater the line as part of the commissioning process.
Some operators choose to
dewater the pipelines with mechanical pigs to remove most of the water, then
complete the drying by pumping a second train of pigs including foam pigs,
nitrogen, and methanol.
Commissioning, the
process of bringing a pipeline to a state of readiness for use, can present a
challenge rivaling the challenges faced by pipeline construction teams. To
allow for safe transport of dry natural gas through the completed system,
operators must purge the line of all debris left during construction and all
water left by subsea construction, cleaning, and hydrotesting procedures. A gas
pipeline must be dried to specific levels to control:
- Hydrate formation within the
pipe
- Corrosion in lines when sulfur
is a component of the gas
- Formation of carbonic acid when
carbon dioxide is a gas component.
Dryness defined
Pipelines that will be
used to transport gas must he dry before put into service. Dryness is expressed
in several different ways:
- Dew point in degrees F at 14.7
psia
- Dew point in degrees C at 14.7
psia or 1 bar absolute
- Parts per million (ppm) by
volume
- Parts per million (ppm) by
weight
- Pounds of water per volume
(lb/MMcf) of air.
A dryness level of -35°
C dew point at 14.7 psia means the same as the following: (1) -3l° dew point at
14.7 psia, (2) 222 ppm by volume, (3) 140 ppm by weight, and (4) 11.1 lb/MMcf.
One train or two?
Operators dewater
pipelines by using the pumping methods listed as follows:
- Pumping mechanical pigs to swab
out most of the water, then pumping drying pigs (consisting of foam or
methanol),
- Pumping mechanical pigs to
remove most of the water, then vacuum-dry the line or dry it by air
convection,
- Pumping a combination pig train
to swab out water and complete drying of the line by chemical means in one
trip.
Method 3 above offers
many economic benefits, especially in drying long, low-temperature subsea
pipelines. Use of hygroscopic fluids (fluids that readily take up and retain
water) in pig trains eliminates the need for vacuum or air-convection drying to
remove the last traces of moisture from pipe-wall matrices.
In vacuum drying, pressure
in the line is reduced to atmospheric level (sometimes as low as 0.l
atmospheric) for a time, then air is sent through the line to evaporate
moisture. However, air is not effective at drying subsea lines.
Hygroscopic fluids in
the pig train absorb most of the water left behind by the dewatering pigs in
the train. Further, any fluid left behind by the pig train will be hygroscopic
and hydrate-inhibiting in nature. The first contact with the product sent
through the line will absorb the last traces of moisture remaining in the line.
The advantages of
including hygroscopic compartments in the dewatering train and drying the
pipeline in a single pass are:
- The pipeline can be used for
delivery at an earlier time, while vacuum and air-convection drying times
can require months to accomplish. Hygroscopic fluid-drying can be
accomplished concurrent with the dewatering process.
- Hygroscopic-fluid drying
eliminates the need for deck space required for vacuum/air-drying
equipment.
Not every pipeline is a
candidate for single-pass dewatering/drying. Those exceptions include:
- Multiple tie-ins with
connections that cannot be swept by the dewatering train.
- Valve stations that allow water
to drain into them.
- Manifold sections that preclude
pig access cannot be commissioned in a single pass.
It is still advantageous
to include gel compartments in any dewatering train that can be used, since the
gel helps reduce the amount of water that must be dried by vacuum or heated
air. Disposal of hygroscopic fluids may present a challenge in some areas, but
in most cases will not preclude use of such fluids.
Selection of the most
appropriate commissioning method should include the following considerations:
the level of dryness required, the product that will be delivered through the
pipeline, and conditions in the pipeline that may affect drying methods.
Parameters
The volume of water left
in the pipeline by passage of pigs is influenced by (1) coating or the lack of
coating on the internal pipe (ID), (2) pipe roughness, (3) pig bypass, and (4)
pig lubrication.
- Coating: Pipeline coatings may be added to leave an almost
nonporous ID, except for weld ends. Coated pipelines are easiest to
dewater for use, since the volume of water left by swabbing is very small.
To dry most coated pipelines, operators include compartments of methanol
in the pig train to contact water on the pipeline walls. Methanol dries
water rapidly on contact. Operators may even dry coated pipelines by
including a hydrate inhibitor in the dewatering pig train sent through the
line, and allowing the gas to dry out the last remnants of water.
- Pipe roughness: In lines already in service as liquid carriers
but being converted to gas pipelines, pipe roughness causes a high level
of moisture retention in the pipe. The volume of water requiring removal
can be twice the volume required in new pipe. The film of water left after
use of foam pigs or other dewatering methods may require drying by vacuum
or air convection to remove the water contained in the matrix of the pipe
wall.
- Pig bypass: If a pig train is moved too slowly through the
pipeline, the train will start and stop in a jerking movement. Each time a
pig train stops, it may bypass fluids and gas ahead, bypass fluids or gas
to the rear, or reverse directions. Fluid and gas bypass around static
pigs occurs commonly at weld seams. Reversal of direction can occur during
fast shutdown of train movement. When a pig reverses direction, a great
volume of water can bypass the pig.
- Pig lubrication: Proper lubrication is necessary to prolong the
life of the cups/discs that contact pipeline walls to wipe moisture and
debris from the walls. Water or methanol based gels help lubricate pigs
when small amounts of fluids bypass the pig during travel. Gels also
influence the flow regime around the pig. The viscosity of these gels aids
in prevention of forward and reverse bypass of gas and fluid.
Drying gels
Use of gels (included as
compartments in the pig train) as sealants/lubricants has proven to be critical
to the success of drying long, undersea pipelines, contributing greatly to the
longevity of the pig discs/wipers. Schreurs et al. reported the successful
commissioning of a 500-mile undersea line using gel pigs and mechanical pigs in
a single train.
Results of extensive
computer simulation and laboratory experimentation led Schreurs et al to
recommend use of uncrosslinked, methanol and/or water-based gels for pipeline
drying. In actual practice, the gelled methanol pigs performed best, showing
minimal degradation. The water-based gel pigs performed adequately. Where
environmental concerns restrict the use of methanol, or when a pipeline does
not have critical dryness requirements, water-based gels can be used with only
slight degradation in gel performance.
In laboratory testing,
it was observed that uncrosslinked water gels and methanol gels provide
significantly more friction reduction than that provided by water or methanol.
High-viscosity crosslinked gels, however, provide no lubrication to the pig
train and make the train difficult to start into motion. The viscosity decline
on uncrosslinked gels compares favorably with that of borate-crosslinked gels.
Therefore, uncrosslinked gels are the preferred choice for use in dewatering
pig trains.
Operating the train
The pig train
illustrated on page 70 includes a displacement fluid supply, a dewatering
train, and a valve for water flow rate control. Flow rate helps determine the
speed of pig train travel.
On page 72, a typical
pig train that was placed in sequence to cleanse pipe walls, push debris ahead
of the train, lubricate the pigs, dry the walls (drying by hygroscopic fluid
such as methanol), and help prevent bypass of driving gas ahead of the train.
Escape of gas ahead of the train can cause formation of hydrates, which can
completely block the pipeline. A very heavy methanol gel can be designed to
help prevent bypass of propellant gas, but leave minimal residue on the
pipeline walls.
To control pig train
operation, operators modulate the supply gas rate, hold a constant pressure,
and control the water discharge through the valve at the downstream end of the
line. A rapid valve-opening schedule results in high hydraulic transient
pressures that may cause rapid velocity changes. An opening schedule that is
too slow would cause start-stop or jerky pig movement, which would result in
forward pig bypass.
During startup, the
train must be accelerated rapidly enough to avoid start-stop pig motion. During
shutdown, the train must be decelerated to a stop as quickly as possible
without causing a pig reversal. Single-pass dewatering/drying of subsea
pipelines offers economy of time and resources when conditions allow. When
single-pass drying is precluded by conditions or pipeline arrangement,
inclusions of gel compartments in any pig train used reduces subsequent drying
time required.
References
Azevedo, L.F.A., Braga, A.M.B., Nieckele, A.O., Naccache, M. F.,
Gomes, M.G.F.M.: "Simple hydrodynamic models for the prediction of pig
motion in pipelines," Pipeline Pigging Conference, Houston, February,
1995.
Schreurs, S., Falck, C., Hamid, S., Burman, P., Maribu, J.,
Ashwell, C.: "Development of Gel Systems for Pipeline Dewatering and
Drying Applications," OTC 007577, Offshore Technology Conference, Houston,
TX, May 2-4, 1994
Hamid, S., Falck, C., Wissing, M., and Grotberg, I.: "Dynamic
Characteristics of a Pipeline Dewatering Train," OTC 007578, Offshore
Technology Conference, Houston May 2-4, 1994.
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