Stress corrosion cracking occurs due to
combined corrosion and straining of a metal as a result of residual or applied
stress. It create a remarkable loss of mechanical strength with nominal metal
loss that can cause mechanical fast fracture and catastrophic failure of
components and structures.
SCC is not a predictable process and for
many metals in diverse conditions it doesn’t occur. Therefore engineers try to use materials more
efficiently by increasing work stress and using economical materials. Commonly
used alloys for SCC systems are- Carbon steel, low alloy steel, strong steel,
austenitic stainless steel, duplex stainless steel, martensitic stainless steel
and copper alloys such as Monel 400 wire excluding Copper-Nickel alloys.
Oil refineries
Aqueous hydrogen sulfide in oil and gas development
applications can create various challenges. H2S is a harmful gas that can cause
vigorous metal loss corrosion and catastrophic brittle fractures of pressurized
equipment and pipes. These brittle cracks on metallic structures can occur fast
with nominal to no signs or may take a long time to be visible.
Sulfide stress cracking is cracking of a
metal due to combined action of tensile stress and corrosion in availability of
water and H2S.
Monoethanolamine is an absorbent used to
eradicate acid gases comprising of H2S and CO2 in oil refining units. Recent
damaged in various refineries have described that cracks can be parallel or
normal to welds based on the orientation of basic tensile stresses. Cracking
has been found to be both transgranular and intergranular.
Postweld stress relief of carbon steel
weldments in MEA units was performed only when the metal temperature of the
equipment was assumed to exceed 65oC and the acid gas comprised of above 80%
carbon dioxide or when the temperatures were assumed to exceed 95oC or 200oF in
any acid gas content.
Presently any system comprising of MEA at
any temperature and at any acid gas content is postweld stress relieved. It is
the result of studies performed on various refineries to define the level of
SCC problem in this media. These inspection programs showed that leaks were
widespread and were discovered in vessels that had been postweld stress
relieved. Additionally, it was discovered that the whole concentrations of MEA
were included and the most concentrations of MEA were often at comparatively
low temperatures. Systems found to experience cracking included tanks,
absorbers, carbon treater drums, skimming drums and pipes.
Materials used in oil refinery units have
to be competent enough to perform in the various conditions for production
environments and designs. They should be strong yet ductile enough to prevent
brittle fractures. Alloy’s composition, yield strength, hardness, heat
processing, microstructure, fluid pH, partial pressure of H2S, total applied
tensile stress, cold work, temperature and time are the main factors that have
an influence on deciding whether or not SCC will occur to a specific metallic structure.
The recommended alloys to use in oil
refineries are Hastelloy C276, Monel alloys and Inconel alloys. These alloys
offer seamless and long term performance against vigorous corrosion of SCC. So
contact us to order your alloy today.
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