Lurgi_master_alleseiten_A4quer - Die Homepage von Dieter Ulber

Download Report

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
1
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
2
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
3
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
Metal Dusting Corrosion in SMR plants
4
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
Metal Dusting Corrosion in SMR plants
5
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
6
aC
carbon activity
Ki
equilibrium constant
Pi
partial pressure
Potential for Metal Dusting Corrosion
Metal Dusting Corrosion in SMR plants
7
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)
Metal Dusting Corrosion in SMR plants
8
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
Metal Dusting Corrosion in SMR plants
9
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
Metal Dusting Corrosion in SMR plants
10
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
11
SMR Outlet System – Reducer Sockets
Metal Dusting Corrosion in SMR plants
12
Manifold, Transfer Line
Gas Barriers
Metal Dusting Corrosion in SMR plants
13
Process Gas Boiler
„Cold“ Bypass Design
Metal Dusting Corrosion in SMR plants
14
Process Gas Boiler
Flow and temperature distribution
Metal Dusting Corrosion in SMR plants
15
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
Metal Dusting Corrosion in SMR plants
16
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)
Metal Dusting Corrosion in SMR plants
17
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
Metal Dusting Corrosion in SMR plants
18
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
Metal Dusting Corrosion in SMR plants
19
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
Metal Dusting Corrosion in SMR plants
20