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ELECTROCHEMISTRY AT YOUR SERVICETM
SPECIALTIES & NEW APPLICATIONSPOOLS & ELECTROCHLORINATIONELECTRONICS & SURFACE FINISHINGCHLORINE & CAUSTIC INDUSTRY
Cathodic prevention of steel
rebars in concrete: the
international outlook.
ELECTROCHEMISTRY AT YOUR SERVICETM
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What have great projects in common?
ELECTROCHEMISTRY AT YOUR SERVICETM
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Cathodic Prevention
Pedeferri Diagram
ELECTROCHEMISTRY AT YOUR SERVICETM
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Cathodic Prevention
Limited embodied energy; small cathodic current.
Extensive Reference in International Standard EN ISO 12696:2012 “Cathodic
Protection of Steel in concrete”
ANNEX A
Concrete protection GJ/m2
Polymer Modified Cementitious Coating 0,015
Acrylic coating 0,025
Cathodic Protection (installed) 1,7
Cathodic Protection (per year) 0,004
PrevC (installed) 0,04
PrevC (operation per year) 0,002
ELECTROCHEMISTRY AT YOUR SERVICETM
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St. Nicola I Viaduct – A24 (1989)
De-icing salts
ELECTROCHEMISTRY AT YOUR SERVICETM
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St. Nicola I Viaduct – A24 (1989)
Continuous structure: 11 spans
Total surface to be protected: 5600 m2
Prefabricated concrete segments post-tensioned with high
strength steel cables.
Hydrogen embrittlement: at pH > 12 potentials more
negative than -950 mV (SCE)
ELECTROCHEMISTRY AT YOUR SERVICETM
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St. Nicola I Viaduct – A24 (1989)
Steel protection current density to a depth of 40cm: 10mA/m2
Anode layout: Titanium MMO Net single, double, triple
Small anodic zones (100m2) with 4 current distributors
Reference electrodes: Ag/AgCl and Titanium MMO close to
post-tensioned cable and rebar
Remote monitoring control unit
ELECTROCHEMISTRY AT YOUR SERVICETM
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St. Nicola I Viaduct – A24 (1989)
CP system performances
Average current density: 6mA/m2
IR drops in the anode net each zone < 50 mV
Average polarization 200 mV
Tensioned cables potential >> -900mV
ELECTROCHEMISTRY AT YOUR SERVICETM
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Sydney Opera House (1996)
ELECTROCHEMISTRY AT YOUR SERVICETM
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Sydney Opera House (1996)
Prevent corrosion of new precast elements of the substructure of western
under broad-walk
68 Zones: geometry + environment (tidal, submerged and atmospheric)
LIDA® GRID: flexibility of current density and Titanium MMO rods
Total concrete area of CPrev application: 742 m2
Protection current density: 10 mA/m2
80 Reference electrodes: Ag/AgCl, Ti MMO, Zn
ELECTROCHEMISTRY AT YOUR SERVICETM
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Sydney Opera House (1996)
ELECTROCHEMISTRY AT YOUR SERVICETM
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Sydney Opera House (1996 e 2005)
Protection criteria: 100 mV potential decay in 24h (atmospheric and splash
zones structures)
Instant OFF potential: > -900 mV < – 1100 mV Ag/AgCl/0,5M KCl as per
AS2832.5 (concrete elements submerged in SWT)
System energized in 1996: Potential well above the limit for overprotection in
A-frames (post-tensioned steel)
After 10 years of operation: no visible deterioration, spalling or delamination
Protection current density: 2-5 mA/m2
17% faulty reference electrodes (most Ag/AgCl)
ELECTROCHEMISTRY AT YOUR SERVICETM
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Swanson Dock West (2008-2009)
1 Km
Melbourne’s
Main container
Port
3 CP systems
Construction in
stages: 1974-1988
4 berths
ELECTROCHEMISTRY AT YOUR SERVICETM
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Swanson Dock West (2008-2009)
Cathodic Prevention applied to the new ship fender (500m) of berths 1
and 2 in the splash and tidal zones.
Heavily chloride contaminated: cracking and spalling.
600 mm
ELECTROCHEMISTRY AT YOUR SERVICETM
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Swanson Dock West (2008-2009)
Fender beam sections reconstruction. CP rev applied in 30 locations: 3,5m
in length up to 0,5m from the base
Anodes: MMO titanium mesh ribbon anodes applied on insulating spacers
Protection current density (conservative): 20 mA/m2
ELECTROCHEMISTRY AT YOUR SERVICETM
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Swanson Dock West (2008-2009)
Trial system: 2 anodes on each face and 3 on the base 3,5m long
Reference electrodes: 2 embedded in concrete + external (250mm grid)
24h Depolarization 100 mV : only 40% of the grid points
72h Depolarization 100 mV: 90% of the grid but not at the extremities
0,5 m
ELECTROCHEMISTRY AT YOUR SERVICETM
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Swanson Dock West (2008-2009)
New design: additional anode on each side of the beam 500mm up from the base
+ additional transverse anode at the ends of the 3,5m beam section
30 reconstructed areas with new design: 6 zones 5 areas each
Overall capacity (sized for future expansion): 30 A
Since Jan 2009 energized and succesfully polarized achieving the 100 mV decay
criterion
Durrat Al Bahrain (2007)
18
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
13 islands
13 bridges l: 3,5 km
2000 villas
3000 apartments
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
T water: 35°C
Salinity: 37-39 g/l
Bridges height:2m
Lifetime: 50 years
Rebar corrosion
chloride
contamination
Cost CPrev:
2.130.000 USD
Cost stainless
steel (304)
22 Millions USD
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
Design Life 50 years
Anode type MMO coated titanium ribbon
mesh
Cathode current density 5 mA/m2
Max Anode current
density
110 mA/m2
Protection Criteria 100 mV decay or -720 mV vs.
Ag/AgCl
Max zone size 3A
Power/Monitoring System Fully remotely controlled and
monitored
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
Name Length Total N°
Atoll Bridges 162 m 6
Hotel Bridge 680 m 1
Ring bridges 518 m 2
Ring bridges 210 m 4
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
Max Zone Size: 3 A
4 pre-cast decks + 4/6 pile heads
Bridge end: 1 abutment, 2 pile heads + 2/4 pre-cast units
Element Protection Current
Pre-cast deck unit 662 mA
Exposed section of abutments 287 mA
Piles above casing
(Pile Head)
31 mA
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
Reference electrodes:
embeddable Ag/AgCl
Recorded native and
instantaneous Eoff
potentials after 1h up to 24h
Good potential shift in 3-4 h
Homogeneity of shifts and
even protection
ELECTROCHEMISTRY AT YOUR SERVICETM
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Durrat Al Bahrain (2007)
ELECTROCHEMISTRY AT YOUR SERVICETM
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Nakilat – Qatar (2006 -2009)
54 ships
610 Mil US$
ELECTROCHEMISTRY AT YOUR SERVICETM
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Nakilat – Qatar (2006 -2009)
2 Km quays
and piers
ELECTROCHEMISTRY AT YOUR SERVICETM
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Nakilat – Qatar (2006 -2009)
54 cellular caissons in reinforced concrete
Overall dimensions: 36 m x 36 m x 11 m; weight 4000 ton
CPrev to grant 50 years design life in the Persian Gulf
MMO mesh ribbon anodes for splash and atmospheric zone
ELECTROCHEMISTRY AT YOUR SERVICETM
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Tangiers-Med Port (2005 -2012)
ELECTROCHEMISTRY AT YOUR SERVICETM
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Tangiers-Med Port (2005 -2012)
Tangier Med: 2007 first multi-purpose wharf
2008 second terminal 3,5 Millions container py
Tangier Med II: 2012-2015 2 new terminals 2800m long
5 Milions container
Larger port in the Mediterranean Sea
ELECTROCHEMISTRY AT YOUR SERVICETM
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Tangiers-Med Port (2005 -2012)
Primary and secondary breakwaters builded by consortium
Bouygues-Bymaro-Saipem to protect the port
Water depth > 20m zone: 40 precast reinforced concrete caisson
built on land then placed in the seawater and completed with
the second phase of concreting
ELECTROCHEMISTRY AT YOUR SERVICETM
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Tangiers-Med Port (2005 -2012)
1 caisson = 4 cells 28mx28mx35m h, weight 7900 ton
550 ton of steel and 3000 m3 of concrete
CPrev in tidal and splash zone to stop corrosion induced by chlorides
Grid system with MMO Titanium mesh ribbon
ELECTROCHEMISTRY AT YOUR SERVICETM
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Hangzhou Bay Bridge (2004-2005)
36 km
Opening:
14/06/2007
Among the
ten longest
trans-oceanic
bridges
ELECTROCHEMISTRY AT YOUR SERVICETM
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Hangzhou Bay Bridge (2004-2005)
ELECTROCHEMISTRY AT YOUR SERVICETM
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Xia-Zhang Bridges (2011-2013)
Total length North
Branch: 6392 m
L cable-stayed: 1290m
720m main span
6° world-wide long
cable-stayed combined
with steel and concrete
ELECTROCHEMISTRY AT YOUR SERVICETM
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Xia-Zhang Bridge (2011-2013)
Cprev 4 main pylons and 4 piers
Tidal and splash zone: 13100m2
Anode: MMO Ti activated mesh ribbon
applied on the rebar with concrete spacer
ELECTROCHEMISTRY AT YOUR SERVICETM
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Louvre Abu Dhabi, UAE (2013-2015)
On Saadiyat Island due to open end of 2015
Cprev installed on all exposed surfaces of the reinforced concrete
sub-structure up to a height of +3.45m
ELECTROCHEMISTRY AT YOUR SERVICETM
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Louvre Abu Dhabi, UAE (2013-2015)
Cprev system for a design life of
100 years
Anode: MMO Ti activated mesh
ribbon installed in the screed
to protect rebar in the lower
reinforcement of the strip
footings, ground beams and
slabs
Fixed to the rebar cage using
plastic clips for all other
surfaces
ELECTROCHEMISTRY AT YOUR SERVICETM
40
Conclusions
Cathodic Prevention, conceived by Prof. Pietro Pedeferri, has
proven to be a viable technique to stop corrosion of steel
reinforcement in concrete.
From the first trials in the mid-’80s this idea has evolved over the
course of thirty years becoming a well established technique to
preserve structures subject to corrosion induced by chlorides
contamination.
Several aspects of cathodic prevention have been incorporated in
international standards such as ISO 12696:2012 and AS2832.5-
2008.
The diffusion of the technology from the US and Europe to
Australia, Middle East, China and North Africa is a sign of the
relevance of this idea in the corrosion prevention global
market.
ELECTROCHEMISTRY AT YOUR SERVICETM
41
Thank you for your time
Q&A

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Cathodic prevention of steel rebars in concrete the international outlook

  • 1. ELECTROCHEMISTRY AT YOUR SERVICETM SPECIALTIES & NEW APPLICATIONSPOOLS & ELECTROCHLORINATIONELECTRONICS & SURFACE FINISHINGCHLORINE & CAUSTIC INDUSTRY Cathodic prevention of steel rebars in concrete: the international outlook.
  • 2. ELECTROCHEMISTRY AT YOUR SERVICETM 2 What have great projects in common?
  • 3. ELECTROCHEMISTRY AT YOUR SERVICETM 3 Cathodic Prevention Pedeferri Diagram
  • 4. ELECTROCHEMISTRY AT YOUR SERVICETM 4 Cathodic Prevention Limited embodied energy; small cathodic current. Extensive Reference in International Standard EN ISO 12696:2012 “Cathodic Protection of Steel in concrete” ANNEX A Concrete protection GJ/m2 Polymer Modified Cementitious Coating 0,015 Acrylic coating 0,025 Cathodic Protection (installed) 1,7 Cathodic Protection (per year) 0,004 PrevC (installed) 0,04 PrevC (operation per year) 0,002
  • 5. ELECTROCHEMISTRY AT YOUR SERVICETM 5 St. Nicola I Viaduct – A24 (1989) De-icing salts
  • 6. ELECTROCHEMISTRY AT YOUR SERVICETM 6 St. Nicola I Viaduct – A24 (1989) Continuous structure: 11 spans Total surface to be protected: 5600 m2 Prefabricated concrete segments post-tensioned with high strength steel cables. Hydrogen embrittlement: at pH > 12 potentials more negative than -950 mV (SCE)
  • 7. ELECTROCHEMISTRY AT YOUR SERVICETM 7 St. Nicola I Viaduct – A24 (1989) Steel protection current density to a depth of 40cm: 10mA/m2 Anode layout: Titanium MMO Net single, double, triple Small anodic zones (100m2) with 4 current distributors Reference electrodes: Ag/AgCl and Titanium MMO close to post-tensioned cable and rebar Remote monitoring control unit
  • 8. ELECTROCHEMISTRY AT YOUR SERVICETM 8 St. Nicola I Viaduct – A24 (1989) CP system performances Average current density: 6mA/m2 IR drops in the anode net each zone < 50 mV Average polarization 200 mV Tensioned cables potential >> -900mV
  • 9. ELECTROCHEMISTRY AT YOUR SERVICETM 9 Sydney Opera House (1996)
  • 10. ELECTROCHEMISTRY AT YOUR SERVICETM 10 Sydney Opera House (1996) Prevent corrosion of new precast elements of the substructure of western under broad-walk 68 Zones: geometry + environment (tidal, submerged and atmospheric) LIDA® GRID: flexibility of current density and Titanium MMO rods Total concrete area of CPrev application: 742 m2 Protection current density: 10 mA/m2 80 Reference electrodes: Ag/AgCl, Ti MMO, Zn
  • 11. ELECTROCHEMISTRY AT YOUR SERVICETM 11 Sydney Opera House (1996)
  • 12. ELECTROCHEMISTRY AT YOUR SERVICETM 12 Sydney Opera House (1996 e 2005) Protection criteria: 100 mV potential decay in 24h (atmospheric and splash zones structures) Instant OFF potential: > -900 mV < – 1100 mV Ag/AgCl/0,5M KCl as per AS2832.5 (concrete elements submerged in SWT) System energized in 1996: Potential well above the limit for overprotection in A-frames (post-tensioned steel) After 10 years of operation: no visible deterioration, spalling or delamination Protection current density: 2-5 mA/m2 17% faulty reference electrodes (most Ag/AgCl)
  • 13. ELECTROCHEMISTRY AT YOUR SERVICETM 13 Swanson Dock West (2008-2009) 1 Km Melbourne’s Main container Port 3 CP systems Construction in stages: 1974-1988 4 berths
  • 14. ELECTROCHEMISTRY AT YOUR SERVICETM 14 Swanson Dock West (2008-2009) Cathodic Prevention applied to the new ship fender (500m) of berths 1 and 2 in the splash and tidal zones. Heavily chloride contaminated: cracking and spalling. 600 mm
  • 15. ELECTROCHEMISTRY AT YOUR SERVICETM 15 Swanson Dock West (2008-2009) Fender beam sections reconstruction. CP rev applied in 30 locations: 3,5m in length up to 0,5m from the base Anodes: MMO titanium mesh ribbon anodes applied on insulating spacers Protection current density (conservative): 20 mA/m2
  • 16. ELECTROCHEMISTRY AT YOUR SERVICETM 16 Swanson Dock West (2008-2009) Trial system: 2 anodes on each face and 3 on the base 3,5m long Reference electrodes: 2 embedded in concrete + external (250mm grid) 24h Depolarization 100 mV : only 40% of the grid points 72h Depolarization 100 mV: 90% of the grid but not at the extremities 0,5 m
  • 17. ELECTROCHEMISTRY AT YOUR SERVICETM 17 Swanson Dock West (2008-2009) New design: additional anode on each side of the beam 500mm up from the base + additional transverse anode at the ends of the 3,5m beam section 30 reconstructed areas with new design: 6 zones 5 areas each Overall capacity (sized for future expansion): 30 A Since Jan 2009 energized and succesfully polarized achieving the 100 mV decay criterion
  • 18. Durrat Al Bahrain (2007) 18
  • 19. ELECTROCHEMISTRY AT YOUR SERVICETM 19 Durrat Al Bahrain (2007) 13 islands 13 bridges l: 3,5 km 2000 villas 3000 apartments
  • 20. ELECTROCHEMISTRY AT YOUR SERVICETM 20 Durrat Al Bahrain (2007) T water: 35°C Salinity: 37-39 g/l Bridges height:2m Lifetime: 50 years Rebar corrosion chloride contamination Cost CPrev: 2.130.000 USD Cost stainless steel (304) 22 Millions USD
  • 21. ELECTROCHEMISTRY AT YOUR SERVICETM 21 Durrat Al Bahrain (2007) Design Life 50 years Anode type MMO coated titanium ribbon mesh Cathode current density 5 mA/m2 Max Anode current density 110 mA/m2 Protection Criteria 100 mV decay or -720 mV vs. Ag/AgCl Max zone size 3A Power/Monitoring System Fully remotely controlled and monitored
  • 22. ELECTROCHEMISTRY AT YOUR SERVICETM 22 Durrat Al Bahrain (2007) Name Length Total N° Atoll Bridges 162 m 6 Hotel Bridge 680 m 1 Ring bridges 518 m 2 Ring bridges 210 m 4
  • 23. ELECTROCHEMISTRY AT YOUR SERVICETM 23 Durrat Al Bahrain (2007) Max Zone Size: 3 A 4 pre-cast decks + 4/6 pile heads Bridge end: 1 abutment, 2 pile heads + 2/4 pre-cast units Element Protection Current Pre-cast deck unit 662 mA Exposed section of abutments 287 mA Piles above casing (Pile Head) 31 mA
  • 24. ELECTROCHEMISTRY AT YOUR SERVICETM 24 Durrat Al Bahrain (2007)
  • 25. ELECTROCHEMISTRY AT YOUR SERVICETM 25 Durrat Al Bahrain (2007) Reference electrodes: embeddable Ag/AgCl Recorded native and instantaneous Eoff potentials after 1h up to 24h Good potential shift in 3-4 h Homogeneity of shifts and even protection
  • 26. ELECTROCHEMISTRY AT YOUR SERVICETM 26 Durrat Al Bahrain (2007)
  • 27. ELECTROCHEMISTRY AT YOUR SERVICETM 27 Nakilat – Qatar (2006 -2009) 54 ships 610 Mil US$
  • 28. ELECTROCHEMISTRY AT YOUR SERVICETM 28 Nakilat – Qatar (2006 -2009) 2 Km quays and piers
  • 29. ELECTROCHEMISTRY AT YOUR SERVICETM 29 Nakilat – Qatar (2006 -2009) 54 cellular caissons in reinforced concrete Overall dimensions: 36 m x 36 m x 11 m; weight 4000 ton CPrev to grant 50 years design life in the Persian Gulf MMO mesh ribbon anodes for splash and atmospheric zone
  • 30. ELECTROCHEMISTRY AT YOUR SERVICETM 30 Tangiers-Med Port (2005 -2012)
  • 31. ELECTROCHEMISTRY AT YOUR SERVICETM 31 Tangiers-Med Port (2005 -2012) Tangier Med: 2007 first multi-purpose wharf 2008 second terminal 3,5 Millions container py Tangier Med II: 2012-2015 2 new terminals 2800m long 5 Milions container Larger port in the Mediterranean Sea
  • 32. ELECTROCHEMISTRY AT YOUR SERVICETM 32 Tangiers-Med Port (2005 -2012) Primary and secondary breakwaters builded by consortium Bouygues-Bymaro-Saipem to protect the port Water depth > 20m zone: 40 precast reinforced concrete caisson built on land then placed in the seawater and completed with the second phase of concreting
  • 33. ELECTROCHEMISTRY AT YOUR SERVICETM 33 Tangiers-Med Port (2005 -2012) 1 caisson = 4 cells 28mx28mx35m h, weight 7900 ton 550 ton of steel and 3000 m3 of concrete CPrev in tidal and splash zone to stop corrosion induced by chlorides Grid system with MMO Titanium mesh ribbon
  • 34. ELECTROCHEMISTRY AT YOUR SERVICETM 34 Hangzhou Bay Bridge (2004-2005) 36 km Opening: 14/06/2007 Among the ten longest trans-oceanic bridges
  • 35. ELECTROCHEMISTRY AT YOUR SERVICETM 35 Hangzhou Bay Bridge (2004-2005)
  • 36. ELECTROCHEMISTRY AT YOUR SERVICETM 36 Xia-Zhang Bridges (2011-2013) Total length North Branch: 6392 m L cable-stayed: 1290m 720m main span 6° world-wide long cable-stayed combined with steel and concrete
  • 37. ELECTROCHEMISTRY AT YOUR SERVICETM 37 Xia-Zhang Bridge (2011-2013) Cprev 4 main pylons and 4 piers Tidal and splash zone: 13100m2 Anode: MMO Ti activated mesh ribbon applied on the rebar with concrete spacer
  • 38. ELECTROCHEMISTRY AT YOUR SERVICETM 38 Louvre Abu Dhabi, UAE (2013-2015) On Saadiyat Island due to open end of 2015 Cprev installed on all exposed surfaces of the reinforced concrete sub-structure up to a height of +3.45m
  • 39. ELECTROCHEMISTRY AT YOUR SERVICETM 39 Louvre Abu Dhabi, UAE (2013-2015) Cprev system for a design life of 100 years Anode: MMO Ti activated mesh ribbon installed in the screed to protect rebar in the lower reinforcement of the strip footings, ground beams and slabs Fixed to the rebar cage using plastic clips for all other surfaces
  • 40. ELECTROCHEMISTRY AT YOUR SERVICETM 40 Conclusions Cathodic Prevention, conceived by Prof. Pietro Pedeferri, has proven to be a viable technique to stop corrosion of steel reinforcement in concrete. From the first trials in the mid-’80s this idea has evolved over the course of thirty years becoming a well established technique to preserve structures subject to corrosion induced by chlorides contamination. Several aspects of cathodic prevention have been incorporated in international standards such as ISO 12696:2012 and AS2832.5- 2008. The diffusion of the technology from the US and Europe to Australia, Middle East, China and North Africa is a sign of the relevance of this idea in the corrosion prevention global market.
  • 41. ELECTROCHEMISTRY AT YOUR SERVICETM 41 Thank you for your time Q&A