| Technical Presentations at the
April 2008 Meeting
1.1
‘Computer
modelling of cathodic protection, applications on a harbour integrity
design’, Ernesto Manuel Santana-Diaz, DNV and John Baynham, CM BEASY
This presentation
demonstrated with some 3D mathematical modelling how the cathodic
protection systems installed on a dock and on a ship can interfere in
several conditions. The base case was instigated by some Aberdeen Harbour
engineers, who considered that the installation of some anodes in sheet
pile surface of the harbour and leaving the nearby surface without anodes
could affect the integrity of the harbour and the anodes installed. This was confirmed with the use of computer modelling.
Several cases were studied:
- A
bare steel pile sheet with cathodic protection, nearby pile sheet
perfectly coated
- A
bare steel pile sheet with cathodic protection, nearby pile sheet
bare steel no protection
- A
ship berthed to the dock, hence interference effects when high, low
tide and completed and uncompleted installation of anodes on the
dock.
It
was concluded that a ship berthed to the dock could have a detrimental,
prejudicial effect on the hull and dock anodes and the dock
structure near the propeller together with a beneficial effect in areas
away from it amongst other effects. These effects should be considered in
the initial installation of the anodes as they could affect the integrity
of the hull and the dock in the long term.
3.1
Keynote 1: ‘Stress
Corrosion Behaviour of Nickel Aluminium Bronzes in Sea Water’, Jean-Loup
Heuzé, DGA-DET-CEP/MC/PMA
7-9 rue des Mathurins 92 220 BAGNEUX, jean-loup.heuze@dga.defense.gouv.fr
Since
about 1960, French Navy use Nickel Aluminium Bronzes (NAB) for numerous
marine applications: cast propellers, wrought high pressure piping
systems, flanges and valves, heat exchangers,.. . . . . ...
. .
NAB
(Cu Al9 Ni3 Fe2) is used in high pressure piping systems due to their high
mechanical characteristics associated to a good corrosion resistance in
sea water. Until then,
susceptibility of NAB to stress corrosion cracking in sea water was not
reported. However, over the
last 12 years, CuAl9Ni3Fe2 has exhibited some cases where cracks were
found on piping systems located in sea water.
First, a preliminary failure analysis was carried out by "DCNS/CETEC
- Cherbourg" on cracked samples taken from a pipe after more than 20
years of exposure in seawater. In
order to gain insight to the mechanisms by which service damage develops,
we investigated the environmental and metallurgical conditions under which
stress corrosion cracking of CuAl9Ni3Fe2 occurs.
Second,
numerous tests using U-bend and C-ring specimens were conducted by DCNS/CETEC,
in various environments and conditions.
Typical cracking obtain with these tests was compared to these
detected on pipes. The
influence of possible pollution such as ammonia has been found
predominant. These test parameters have been determined to simulate SCC on
Nickel Aluminium Bronzes. The
cracks obtained in these tests are similar to those observed on actual
pipes.
Third,
a specific study to understand the mechanisms of SCC on NAB was conduct by
"ENS Mines de Saint-Etienne Materials Science and Structures
Laboratory" for a PhD thesis. Slow
Strain Rate Tensile tests (SSRT) were conducted in synthetic sea water
with different pH (acid and alkaline solutions) at free potential and at
-1050 m V/SCE. Influence of
microstructure, strengthening, pH, cathodic protection were investigated.
At
free potential, with acid pH < 4, we don't observe a SCC mechanism but
a general intergranular corrosion occurs.
With alkaline pH, intergranular cracking always occurs but
transgranular cracking increases. Cracking
proceeds by dissolution of the more anodic phase and fracture mode depends
on phases nature and repartition. When
the second phase is martensitic, back-scattered SEM observations show that
dealloying of the martensite is associated to the crack growth. At pH 10 or in synthetic sea water, we also observe local
transgranular cracking of the phase.
The
SCC phenomenon probably initiates during the dry-docking period in the
presence of stagnant sea water and in the absence of cathodic protection.
Propagation occurs during operation under cathodic protection (-1050
mV/SCE) and stresses of in services conditions.
Influence of hydrogen is excluded.
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3.2 ‘Factors Informing the Hydrogen Induced Damage to Steels in
Upstream Service', Frank Dean, Ion Science, Frank.Dean@ionscience.com
This
paper looked at hydrogen chemistry, examples of hydrogen damage, linking
hydrogen sources and susceptibility, steel qualities causing hydrogen
susceptibility, and hydrogen charging.
Conclusions
were:
- Hydrogen damage requires the activity
of hydrogen in steel to exceed the susceptibility of hydrogen in a
particular steel.
- Susceptibility of steel is
considerably enhanced by sources of tensile stress.
Environmental sources of stress, such as in deep sea service
equipment, need careful consideration.
- Hydrogen promoters, such as H2S,
need be present at very low concentrations to enhance hydrogen
activity.
- The time scale for hydrogen
equilibration in steel in seawater is up to a week for mild steel, but
centuries otherwise, except for SCC.
3.3
Keynote 2: ‘Design
and Fabrication Experiences with Titanium in Offshore Platforms’,
Torfinn Havn, Ztrong AS, Norway
This
presentation looked at experiences with Titanium installed offshore
Norway. The motivation for
use of Ti was that considerable corrosion problems are experienced in sea
water systems with carbon steel, copper alloys and stainless steels.
Services where Ti is used:
– Fire water
systems (piping, valves, deluge, sprinkler)
– Fire water
ring main
– Sea water
systems
– Heat
exchangers
– Hypochlorite
systems
– Ballast
water systems
– Sea water
pumps
– Desalination
packages
– Drilling
risers
Aspects
discussed covered problems, fabrication (welding, forming), cost and
availability.
Conclusions:
1
By experience it is found that Ti gives the best material
solution in fire water and sea water systems above 20°C
2 Ti
need special focus on design and welding
3 The
availability of the material is limited and engineering has to be aware of
the situation
4 Care
is to be taken when Ti is to be coupled to other materials.
3.4
‘Oil & Gas Related Corrosion’, Chris Fowler,
Bodycote Testing
This
presentation looked at the reasons for undertaking Sour Service Testing,
which could be: to qualify a new material; qualify a new process e.g. weld
procedure; quality assure the manufacturing route or to avoid failures.
It then considered how to test: looking to
- Understand
the material properties before embarking on a test programme
- Understand
the test methodology
- Select
the test method and conditions carefully
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