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Transcript Lurgi_master_alleseiten_A4quer - Die Homepage von Dieter Ulber
Metal Dusting Corrosion in
Steam Reforming Plants
J. Bohle, Dr. C. Beyer, U. Wolf, Dr. D Ulber
Steam Reforming Technology User Conference
Labuan, Malaysia
March 5-7, 2007
Metal Dusting Corrosion in SMR plants
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Metal Dusting Corrosion (MDC)
Disintegration of metals and alloys
into a dust of graphite and metal particles
after carbon ingress and over-saturation.
Metal Dusting Corrosion in SMR plants
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Overview
Phenomena of Metal Dusting Corrosion (MDC)
Mechanism involved / Reactions
Material considerations
Examples of MDC in Steam Reforming Plants
Prevention of MDC
Influence of MDC on process design
Literature
Metal Dusting Corrosion in SMR plants
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Steps in Metal Dusting Corrosion
Diffusion of reducing / carburizing gas through oxide
protection layers to metal surface
Formation & supersaturation of carbides
Dissociation into metal particles and graphite
Diffusion of catalytically active metal particles
Loss of carbon, metal, metal carbide, metal oxide
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Phenomena involved in MDC
Gas-phase and gas-metal reactions (T, p, composition fi)
Diffusion of reducing gas, carbon and metals (T, fi)
Flow and temperature distribution (vel, T) – equipment design
Catalytically active components in gas and metal
Thermodynamic & mechanical stability of protective layers
Stresses / fractures imposed on surfaces by gradients
Metal crystallographic structure
Sulfidic components in gas
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Reactions
Carburization reactions
CO + H2 <-> C + H2O
aC =K1*pCO*(pH2/pH2O)
2 CO <-> C + CO2
aC =K2*(p2CO/pCO2)
CH4 <-> C + 2 H2
aC =K3*(pCH4/p2H2)
Gas-phase reactions
H2O + CO <-> CO2 + H2
H2O + CH4 <-> CO + 3 H2
Metal Dusting Corrosion in SMR plants
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aC
carbon activity
Ki
equilibrium constant
Pi
partial pressure
Potential for Metal Dusting Corrosion
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Temperature range
Promoting components
450°C < MDC temp. range < 800°C / Boudouard temp.
At [Fe/Ni] > ~ 2/3 mass-frac, metal dusting is retarded at the
lower regimes of the metal dusting temp. range
MDC promoting gas components (negative impact on metal
oxide protection layer)
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Material Considerations
Surface oxide stability is enhanced by alloying elements
such as Cr, Al, Si, Ti, Mo providing a barrier to carbon
diffusion
Carbon and alloying elements diffusion is influenced by
crystallographic structure and surface condition (e.g. grain
size)
Surface coatings or surface finish (grinding) can provide
added stability by influencing the carbon diffusion and/or
physical resistance to mechanical and thermal effects
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Material Considerations
Fe-based and Ni-based metals show different behaviour
Empirical equation of alloying material resistance to MDC
(Parks & Schillmoller)
Crequiv. = Cr % + 3 x (Si % + Al %)
Inclusion of the effects of other alloying elements such as
Ti, Mo, Ni outstanding
Preferred material Nicrofer® 6025 HT – alloy 602 CA
No alloy is MDC resistant under all conditions
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Where can Metal Dusting Corrosion occur?
Reducer Sockets
Transfer Line at Reformer Outlet
Process Gas Boiler (PGB) Inlet chamber
PGB tube inlet section (ferrules) and tube sheet
PGB bypass tube, bypass flow control device
PGB outlet chamber
Heat Exchanger d/s of PGB, e.g. Feed Preheater
Metal Dusting Corrosion in SMR plants
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SMR Outlet System – Reducer Sockets
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Manifold, Transfer Line
Gas Barriers
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Process Gas Boiler
„Cold“ Bypass Design
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Process Gas Boiler
Flow and temperature distribution
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Process Gas Boiler
Flow and temperature distribution
Temperature distribution in outlet chamber mixing zone of a
process gas boiler
Gastemperatures:
below 450°C
450 – 1000°C
Bypass open
Bypass closed
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Inserts in PGB tubes for temp. control
WHB - Temperatures Cooling Fluid / Tubewall
WHB - Temperatures Cooling Fluid / Tubewall
1000
400
950
800
Wall inside
380
Temperature (°C)
850
Temperature (°C)
390
Feedgas
Wall medium
Steam Cooling
900
750
700
650
600
550
500
Wand outside
370
Steam Cooling
360
350
340
330
450
320
400
310
350
300
300
0
2000
4000
6000
8000
Distance from Inlet (mm)
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10000
0
2000
4000
6000
8000
Distance from Inlet (mm)
10000
Measures against MDC
Pro & Cons
Avoid metal wall temperatures in MDC temperature range
Use of non-metallic materials in critical areas
Change gas atmosphere
– Introduction of process gas (for purge) in critical areas
– Catalytically activated refractory (Lurgi Patent)
Material science, Protection layers
Sulfidic compounds in gas
Design for easy maintenance / replacement
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Influence of MDC on process design
Process efficiency / consumption figures
Steam to Carbon Ratio
Steam Superheater for Process Gas Cooling
Export Steam Value
Gas-heated Steam Reformer design
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Literature References
R.T. Jones, K.L. Baumert; Metal Dusting – An Overview of
Current Literature; Corrosion 2001; No. 01372
H.J. Grabke, E.M. Müller-Lorenz; Occurrence and
Prevention of Metal Dusting on Stainless Steel; Corrosion
2001; No. 01373
F. Hohmann; Improve Steam Reformer Performance;
Hydrocarbon Processing; 03/1996; p. 71-74
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