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CFRP Wraps for Corrosion Repair of Reinforced Concrete Columns and Corrosion Monitoring Ioulia Milman A thesis submitted in conformity with the requirements for the degree of Master of Applied Science Graduate Department of Civil Engineering University of Toronto O Copyright by Ioulia Milman (200 1)

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CFRP Wraps for Corrosion Repair of

Reinforced Concrete Columns and Corrosion Monitoring

Ioulia Milman

A thesis submitted in conformity with the requirements

for the degree of Master of Applied Science

Graduate Department of Civil Engineering

University of Toronto

O Copyright by Ioulia Milman (200 1)

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ABSTRACT

CFRP Wraps for Corrosion Repair of

Reinforced Concrete Columns and Conwsion Monitoring

loulia Milman, M.A.Sc., 21 00 1

Department of Civil Engineering, Univaers@ of Toronto

This experimentai study is a part of an oagoing research project initiated by Lee (1998) and

continued by Khajehpour (2001). This research is aimed- at evaluating repair of large-scale

reinforced concrete columns using carbon fibre reinforceai polymer (CFRP) sheets, in terms

of establishing the effect of wraps on the corrosion of steen reinforcement.

This project involves the construction and testing of six reinforced concrete columns, testing

eleven colunuis remaining from the previous study. Four specimens were repaired with

CFRP wraps. Testing included accelerated corrosion of bmth new and repaired specimens and

natural corrosion of the reinforcement in five columns (including two repaired), and one

prism specimen.

It was found that corrosion activity temporarily increases after repair. After initial increase,

the rate of corrosion becomes the same as in unwrapped columns or slightly lower. Columns

subjected to natural corrosion expand less than before rewair due to restraining effect of the

wrap. Columns subjected to accelerated corrosion do notz expand for sornetime, after which

they expand gradually.

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I would like to thank my supervisors, Dr- J.F. Bonacci and Dr. M.D.A. Thomas for providing

me with the opportunity to work on this project and for d l their invaluable support,

encouragement and patience during this work.

This research was supported by ISIS Canada and 1 would like to acknowledge their financial

suppoa of this project.

1 am very gratefd to P. Malvihill and G. Fishbein fiom Aerospace Engineering, University of

Toronto for providing help with fibre optic sensing technology.

1 am dso gratefùl to many people helping me to complete this project, especially to Nadine

Mobamed Ibrahim and Ali Debaj Ja£f?y for their invaluable help with my experirnents.

It would be impossible to complete this project without help of technical staff at the

University of Toronto. A special thanks to Joel Babbin, Giovanni Buueo, Mehmet Citak,

Peter Heliopoulos, Remo Basset, Alan McClenaghan and John MacDonald.

Findly, 1 wish to express rny gratitude to my husband and my parents for dl their love,

support, and understanding.

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TABLE OF CONTENTS

ABSTRACT

ACKNOWEDGEMENT

TABLE OF CONTENTS

LIST OF TABLES

LIST OF F I G W S

Chapter 1, INTRODUCTION

1.1 Background

1.2 Previous Research

1.3 Overview

Chapter 2, LITERATURE REVIEW

2.1 Corrosion of Steel in Concrete

2.1.1 Chloride-Induced Corrosion

2.1.2 Carbonation-Induced Corrosion

2.2 Mechanism of Concrete Confinement

2.3 RC and Steel Jacketing

2.4 Fibre Reinforced Polymers

2.4.1 Manufacture of Carbon Fibres

2.4.2 Extemally-Bonded FRP for Confinement

2.4.3 FRP for Corrosion Repair

2.5 Corrosion Inhibitors

2.5.1 Classification of Corrosion Inhibitors

2.5.2 Application of Corrosion lnhibitors

252.1 Tnhibitors in Concrete Mix

2.5.2.2 Penetrating Corrosion Inhibitors

2.6 Grout

2.7 Methods for Monitoring Corrosion

2.7.1 Non-Perturbative Methods

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2.7.1.1 Potential Mapping

2.7.1.1.1 Interpretation of Results

2.7.1.1.2 Influences on Measured Potential

2.7.1.2 Electrochernical Noise

2.7.1.3 Electrical Resistance

2.7.2 Perturbative Methods

2.7.2.1 Linear Polarization Resistance

2.7.2.1.1 Tafiel Constants

2.7.2.1 -2 Galvanostatic and Po tentiostatic Approach

2.7.2.1.3 Interpretation of Results

2.7.2.2 AC Impedance

2.7.3 Probe Applications

2.8 Fibre Optic Sensors in Structure

2.8.1 Manufacture of FOS

2.8.2 Basic Principles of Application

2.8.3 Fibre Optic Bragg Gratings Sensor

2.9 Remarks on Literature Review

Chapter 3, EXPERIMENTAL PROGRAM

3.1 Laboratory Test Plan

3.1.1 Test Regimes

3.1.2 Farnilies of Column Specimens

3.1.2.1 Pilot Series

3.1.2.2 Natural Damage Series

3.1 -2.3 Moderate Damage Series

3.1 -2.4 High Damage Series

3.1.2.5 Expansive Grout Senes

3.1.2.6 Corrosion Inhibitor Series

3.1.2.7 One Layer Repair Series

3.1.2.8 Special Cases

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3.2 Column Specîmen

3.2.1 Column Specimen Geometry

3 -2.2 Multi Elernent Probe (MEP)

3 22.1 Pnsm Specirnen

3 -2.2.2 Modified Multi-Element Probe

3 -2.3 Column Specirnen Fabrication

3.3 Matends

3 -3.1 Concrete Materials

3 -3.1.1 Mix Design

3 -3.1 -2 Mwng and Casting Procedures

3 -3-1 -3 Compressive Strength Test Results

3 -3 -2 Steel Reinforcement

3 -3 -3 Repair Materials

3 -4 Laboratory Test Procedures

3.4.1 Accelerated Corrosion Regirne

3 -4.1.1 Mechanical Expansion Collar

3.4.1.2 Fibre Optic Sensors

3 -4.2 Natural Corrosion Regime

3 -4.2.1 Linear PoIarization Resistance Technique

3 -4.2.2 Macro-Ce11 Measurements

3 -4.3 Repair Procedure

Chapter 4, DISCUSSION OF EXPERIMENTAL RESULTS

4.1 Natural Corrosion Testing

4.1.1 Linear Polarization Resistance Testing

4.1.1.1 Pilot Series (2,4)

4.1.1 -2 Linear Polarization Specimen (Prism)

4.1.1.3 Natural Darnage Series ( S 1 1, J 12)

4.1.1.3.1 Column SI1

4.1.1.3.2 Colunin .JI2

4.1.1.4 Moderate Darnage Series (S 10)

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4.1.2 Macro-Ce11 Measurements

4.1.2-1 Pilot Series (2,4)

4.1.2.2 Linear Polarization Spechen (Prism)

4.1 -2.3 Natural Damage Series (S 1 1, J 12)

4.1 -2.4 Moderate Damage Series (S 10)

4.1.3 Circumferential Expansion (S 1.0)

4.2 AcceIerated Corrosion Testing

4.2.1 Corroded-Repaired-Accelerated Test Regime (S 1 and S2)

4.2.1-1 Steel Loss Rate

4.2.1.2 Circumferential Expansion

4.2.1.2.1 Mechanical Expansion Collar

4.2-1.2.2 Fibre Optic Sensors

4.2.2 High Damage, Expansive Grout, Corrosion Inhibitor Series

4.2.2.1 Applied Potential

4.2.2.2 Wetting and Drying Cycles

4.3 Summary of Experimentd Results

4.3.1 Natural Corrosion Testing

4.3 -2 Accelerated Corrosion Testing

Chapter 5, CONCLUSIONS AND RECOMMENDATIONS

5.1 Earlier Developments

5 -2 Conciusions

5 -3 Recomrnendations

Chapter 6, REFERENCES

APPENDM A. Procedure for Taking Readings Using FOS Equipment

APPENDIX B. Procedure for Linear Polarization Tests

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LIST OF TABLES

Chapter 3

Table 3.1

Table 3.2

Table 3.3

Table 3.4

Table 3.5

Table 3 -6

Table 3 -7

Table 3.8

Table 3.9

Laboratory testing plan

History of colurnn specimens treatment

Electrode configurations used for LP tests of pnsm

Concrete mix design for pilot series

Concrete mix design for subsequent senes

Concrete properties

Mechanical properties of steel reinforcement

Mechanical properties of CFRP sheets

Electrode configurations used for LP tests of colurnns S 10 and S 1 1

Chapter 4

Table 4.1 The rate of steel loss for repaired column S 1

Table 4.2 The rate of steel loss for repaired column S3

Table 4.3 Accelerated corrosion history for S7, S8, S9

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LIST OF FIGURES

Chapter 2

Figure 2.1

Figure 2.2

Figure 2.3

Figure 2.4

Figure 2.5

Figure 2.6

Figure 2.7

Figure 2.8

Figure 2.9

Figure 2.10

Figure 2- 1 1

Fi,oure 2.12

Figure 2.13

Figure 2.14

Figure 2.15

Figure 2.16

Figure 2.17

Figure 2.18

Figure 2.19

Figure 2.20

Figure 2.21

Figure 2.22

Figure 2.23

Figure 2.24

Figure 2.25

Figure 2.26

Electrical curent loop during the corrosion process

The relative volume of iron and its corrosion reaction products

Stages of corrosion process

Chloride concentration at the steel surface in the region of crack

Schematic representation of carbonation process

Profile of pH range of carbonated and non-carbonated concrete

The degree of carbonation as a function of relative humidity

Confinement by (a) square hoops, (b) circdar spirals

Confining action of continuous sleeve

Stress-strain relationship for fibrous reinforcement and matrix

Typical behaviour for concrete confined with steel, CFRP, GFRP

Effect of adding (a) an anodic inhibitor, (b) a cathodic inhibitor,

(c) a mixed inhibitor

Effect of calcium nitrite on the corrosion of steel in rnortar

Moderating of inhibitors on corrosion process

Migration concentration curve for MCI@ 2000

Migration concentration cuve for Sika FerroGard-903

Corrosion monitoring techniques

Half-ce11 electrode measurements

Sarnple schematic of half-ce11 potential data

Linear polarization technique

Two types of polarization resistance probes

Simplified Randles' circuit for steel corrosion

Nyquist diagram

Bondable sensor

Bragg grating description

Schematic diagram of arbitrary gauge length, localized fibre optic

structural sensor based on 10 w coherence intefierometry

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Figure 2.27 Application of the localized fibre optic structural sensor to the

measurement of hoop strain in concrete columns

Chapter 3

Figure 3.1 Geometry of concrete column specimen

Figure 3 -2 Commercial multi element probe

Figure 3.3 Geometry of the prism specimen

Figure 3.4 Set up for LP tests for prism

Figure 3.5 Modified multi element probe

Figure 3 -6

Figure 3.7

Figure 3 -8

Figure 3.9

Figure 3.10

Figure 3.1 1

Figure 3-12

Figure 3.13

Figure 3.14

Figure 3.15

Figure 3.1 6

Chapter 4

Figure 4.1

Figure 4.2

Figure 4.3

Figure 4.4

Figure 4.5

Figure 4.6

Figure 4.7

Figure 4.8

Figure 4.9

Reinforcement cage in the formwork

Alignment of probe details

MEP installation

Stress-strain characteristics of reinforcing steel

Corrosion ce11

Accelerated corrosion system

Mechanical expansion collar

Expansion measurements

Fibre optic sensor equipment

Experimental set up for LP testing

Repair procedure

Corrosion potential vs. time for columns 2 and 4

Corrosion current vs. time for columns 2 and 4

Corrosion potential vs. time for prism

Corrosion current vs. time for prism using probe

Corrosion current vs. t h e for prism using 10M bar

Current density vs. time for prism

Corrosion potential vs. time for column SI1

Corrosion current vs. time for column S 11 using probe

Corrosion current vs. time for column S 1 1 using 15M bar

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Figure 4.10

Figure 4.1 1

Figure 4.12

Figure 4.13

Figure 4.14

Figure 4.1 5

Figure 4.16

Figure 4.17

Figure 4.18

Figure 4.1 9

Figure 4.20

Figure 4.2 1

Figure 4.22

Figure 4.23

Figure 4.24

Figure 4.25

Figure 4.26

Figure 4.27

Figure 4.28

Figure 4.29

Figure 4.30

Figure 4-3 1

Figure 4.32

Figure 4.33

Figure 4.34

Corrosion potential vs. time for column 512

Corrosion potential vs. time for naturall y corroding specimens

using probe

Corrosion potential vs. time for naturally corroding specimens

using rebar

Cross section of column 51 2 with modified MEP

Corrosion potential vs. tkne for column S IO

Corrosion current vs. time for column S 10 using Probe

Corrosion current vs. time for column S 10 using 15M bar

Macro-ce11 corrosion current vs. time for colurnns 2 and 4

Macro-ce11 corrosion current vs. t h e for pnsm specimen

Macro-ce11 corrosion current vs. t h e for column S 1 1 and J 12

Macro-ce11 corrosion current vs. time for column S 1 0

Expansion vs. time for column S 1 O

Current vs. time for repaired columns S 1 and S2

Steel loss vs. time for repaired columns S 1 and S2

Expansion vs. tirne for columns S 1 and S2 during

accelerated corrosion before and after repair

Expansion vs. time for repaired column S Z

Expansion vs. time for repaired column S 1

Cornparison of expansion data for column S 1

Applied potential vs. tirne for columns S7-S9

Current vs. time for columns S7-S9

Current vs. time for columns 513-17

Expansion vs. time for columns S7-S9, JI3417

Steel loss vs. time for columns S 7 4 9 and 513417

Expansion vs. steel loss for columns S7-S9,513-J17

Current vs. applied potential for S7-S9

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C W T E R 1. INTRODUCTION

1.1 Background

Reinforced concrete has been successfully used over a numrber of decades. It possesses many

desirable performance properties including high strength,. durability, availability, and low

cost. Concrete normally provides a protective environment agaïnst corrosion of the

embedded steel. The thermodynamically unstable steel is protected fiom corrosion by the

high aikalinity of an appropriately thick and dense concrete cover (Muller and Henriksen,

1995). As a result, iron passivates and the passive film protects the steel against corrosion.

Nevertheless, once the passive layer is damaged (e.g. due bo the presence of chlorides at the

steel surface), the corrosion process may take place in reidorced concrete and cause severe

damage to the structure. Evidence of degradation of a reinforced concrete member due to

corrosion was found as earIy as 1907 (Chess et al, 1998). The darnage associated with

corrosion is cracking, spalling, and delamination of concrete as well as the loss of reinforcing

steel cross section, leading to the reduction of the ultirmate load bearing capacity of the

concrete member.

Inadequacies and errors in design of

susceptible to corrosion. Freeze-thaw

and ice removal) are major causes

concrete mixes produce structures that are relatively

cycles and exposure to de-icing salts (used for snow

of the deterioration in highway structures in many

countries. Many bridge columns in cold climate regions are suffering fkom reinforcement

corrosion and failing to meet their Me-expectancy requirements. While it is impossible to

immediately replace al1 of the corrosion-damaged concrete structures, appropriate and timely

rehabilitation can add years to the remaining service life.

As an alternative to the removal and replacement o f the damaged concrete cover,

circumferential reinforced concrete or steel jackets can be irnstalled around concrete columns.

Although these methods improve significantly the compressive, f l e d and shear strength of

the columns and increase ductility, they have some drawb~acks, such as increased weight of

the structure, and difficulties associated with hancilhg and installation. Moreover, since

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repaired structures are still susceptible to corrosion, second and sometirnes third generation

repair are often necessary.

Advanced composite materials are now being used for the rehabilitation of structures around

the world. Fibre reinforced polymer composites have long been recognized for their high

strength, good fatigue life, light weight, ease of transportation and handling, low maintenance

cost and also good corrosion resistance.

The use of fibre-reinforced polymer (FRP) composites is growing significantly in

construction where durability under harsh environmental conditions is required. Although the

provision of external confinement is well established for strengthening reinforced concrete

(e-g. for seismic upgrade), the repair cornmunity does not yet generally accept the philosophy

of wrapping elements suffering f?om the corrosion of steel reinforcement. Such an approach

does not directly address the underlying cause of detenoration (Le. the presence of chlorides

in the vicinity of the steel). However, it is expected that the corrosion process may be

significantly retarded by the presence of the FRP, due to its action as an impermeable barrier

impeding the supply of oxygen and moisture required for corrosion, and perhaps also as a

result of the wrap providing physical restraint to the development of expansive corrosion

products. Furthemore, repaired columns appear to be able to tolerate continued corrosion of

the embedded steel reinforcement under concentric loading (Lee, 1998). These data are

prelirninary in nature and the need to properly monitor repairs of t h i s type in the laboratories

and in the field is emphasised.

1.2 Previous Research at University of Toronto

This study is a part of a larger project to develop a rehabilitation system for corroded

reinforced columns using carbon fibre reinforced polymer (CFRP) wraps. Lee (1998) and

Khajehpour (2001) conducted the previous studies. It is part of an ongoing research project at

the University of Toronto supported by ISIS Canada, a Canadian Network of Centres of

Excellence.

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As a result of previous research, simulation of corrosion damage was achieved using

accelerated corrosion. Adding sodium chlonde to the concrete, applying a potential to the

reinforcement cage and subjecting specimens to cyclic wetting and drying accomplished the

accelerated corrosion. Structural tests performed by Lee (1998) and Khajehpour (2001) have

Midicated loss of strength and considerable loss of ductility due to corrosion as well as

extensive pitting corrosion of the spiral reinforcement. By structural testing of repaired

colurnns it was shown that CFRP wraps can restore the coIumn strength and ductirity lost due

to corrosion. Wrapped colurnns subjected to considerable post-repair corrosion still

outperform undarnaged control specimens. The performance of corroded and repaired

specimens has shown reasonable repeatability.

1.3 Overview

The present work sumrnarises the results of previous and ongoing research involving thirty-

one large-scale reinforced concrete columns, twenty-five of which were corroded using an

accelerated corrosion regime, twelve of which were then repaired using CFRP wraps. Six

non-repaired columns, six repaired and two control column specimens were structurally

tested. The rernainder of the colurnn specimens were left for long-term monitoring. The

detailed Iaboratory test plan is presented in Chapter 3.

The main objective of the overall project is to develop a "smart" wrap system for corrosion

damaged RC columns capable of restoring structural capacity, slowing down corrosion and

providing data that can be used to determine colurnn condition and estimate remaining

service life.

The following developrnents are required in order to rneet the above objective:

Provide realistic simulation of corrosion-damaged colurnns in the laboratory

environment.

Detennine the effect of confinement by FRP wraps on the corrosion of chloride-

contaminated, steel-reinforced concrete columns.

Develop a corrosion monitoring system for use with wmpped columns in the laboratory

and field.

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Ongohg research is aimed at evaluating the repair technique using CFRP wraps, particdarly

in terms of establishing the effect of CFRP wraps on the corrosion process.

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Many existing reinforced concrete structures in North Amer-ica show a high degree of

darnage and are not able to per£orm their original fùnctions. The cracking of concrete and

the use of de-icing salts in cold-climate regions lead to rapid corrosion of the reinforcing

steel in bridge columns, Recent studies (Emmons and Vaysburd, 1997) show that billions of

dollars are spent every year to repair existing structures. Therefore, there is a growing need

for cost-effective repair solutions- Rehabilitation of reinforced concrete columns using CFRP

wraps represents an alternative solution to the traditiod method of replacing the deteriorated

concrete.

This research is devoted to development of repair and monitoring technologies for corrosion

darnaged reinforced concrete infrastructure. This overall objective touches on a wide variety

of subjects, which are to be considered in the literature review that follows. These include:

aspects of corrosion in reinforced concrete, the effects of corrosion on structural

performance; aspects of repair (including steel or concrete jacketing and FRP wrapping for

confinement, corrosion inhibiting chemical products and grouting); and monitoring issues for

both corrosion and structural peI5orrnance-

This necessarily broad literature review is organized by these main aspects of the overall

problem- Section 2.1 discusses the mechanism of corrosion including both: chloride induced

corrosion and carbonation. Section 2.2 thrOugh Section 2.4 briefly discuss the mechanism of

concrete confinement and compares steel or concrete jacketing to FRP wrapping as a repair

strategy for corrosion damaged reinforced concrete columns. FRP wrapping with application

of penetrating corrosion inhibitors or grouting are discussed in Sections 2.5 and 2.6.

Furthermore, in order to understand the corrosion process in FRP wrapped colurnns,

laboratory monitoring is necessary. Thus some methods of corrosion monitoring are bnefly

descrïbed in Section 2-7. The introduction of advanced composite matenals into

rehabilitation and strengthening of existing structures could be accelerated by the integrated

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monitoring capability provided by fibre optic structural sensing technology in the field. Fibre

optic sensing (FOS) technology is reviewed in Section 2.8.

2.1 Corrosion of Steel in Concrete

Corrosion of steel in concrete is an elec~ochernical process. It requires a cathode, an anode

and an electrolyte (solution that can conduct ions). Since concrete incorporates some water it

can act as an electrolyte. In new concrete, the pH of the pore solution is usually in excess of

13; and under such conditions steel is protected from corrosion by a passivating film of iron

oxide bonded to its surface. When steel becomes depassivated corrosion may occur. Many

factors can lead to the breakdoai of passivation of reinforcing steel in concrete. including

the ingress of aggressive chloride ions into the concrete and carbonation of concrete, which

are discussed in Sections 2.1.1 and 2-1 -2.

Corrosion can be descnbed by two electrochemical reactions:

Anodic reaction: Fe + ~ e ' - -+ 2 e -

Cathodic reaction: H 2 0 + - B 0 7 f 2 e - + 2 0 H -

where Fe - metallic iron (the main constituent of steel)

~ e ' - - dissolved iron in the electrolyte which carries positive elecû-ical

charges

Oz - oxygen dissolved in the electrolyte

O H - hydroxyl ion in the electrolyte. which carries negativs electricd charge

The anodic and cathodic reactions occur simultaneously, with the movement of the eIectric

charge in metal as electrons and through the electrolyte as ions. Electrons flow from the

anode to the cathode. Therefore, the loss of metai takes place on the anode since the product

of anodic reaction ~ e " dissolves in water around the steel. The anode and the cathode are

usually adjacent on the same bar. This cornrnon type of corrosion is called micro-ce11

corrosion.

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Figure 2.1 illustrates the current flow, in which electrons travel £iom the anode to the cathode

inside the metal. There is also a flow of ionic cment through the electrolyte (concrete pore

solution). ~ e ~ ' a n d (OH) react to form Fe (OH) 2 which will react with additional (OH) and

oxygen to form rust FeO, which may expand to occupy £kom two to seven times the volume

of the original steel, as shown on Figure 2.2. (Rosenberg et al, 1989). This imposes intemal

tension, which can Iead to cracking and spalling as well as loss of bond between steel and

concrete (Chess and Gronvold, 1996). Cracking of concrete may accelerate corrosion since

the steel is open to the environment, providing an ample supply of moisture and oxygen.

Figure 2.1. Electrical Current Loop during the Corrosion Process

(Bentur et al, 1997)

Volume -cms

Figure 2.2. The Relative Volume of Iron and its Corrosion Reaction Products

(Rosenberg et al, 1989)

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As corrosion proceeds, the reduction in the cross-section area of the reidorcement steel takes

place, reducing the strength and ductility of the RC concrete member. Fi-aure 2-3 summarizes

two major concerns associated with corrosion of reinforcement in concrete; speiling of

concrete and reduction of cross-section area of the reinforcing bar.

t Soluble uon ions

Hydraxyl

Imn hydroxide

Red . u t (haema-1

Figure 2.3. Stages of Corrosion Process (Chess and Gronvold, 1996)

2.1.1 Chloride-Induced Corrosion

As rnentioned above, one of the causes of steel depassivation is due to the presence of

aggressive chloride ions. Chlondes may be introduced to the concrete as set accelerators

(such as calcium chloride) or constituents of some aggegates or the mixing water. It is now

standard practice to limit chloride content in concrete mixes.

If a concrete structure is exposed to seawater or de-icing salts, chlorides rnay penetrate into

the concrete surface. This process rnay take some tirne depending on the amount of chlorides

coming into concrete, the arnount of moisture present, pH of the concrete, permeability of the

concrete, presence of cracks, and the depth of the concrete cover. Repeated wetting and

drying accelerate the ingress of chlorides. Drying to a greater depth aIlows subsequent

wetting to cany the chlorides well into concrete, thus speeding up the ingress of chloride ions

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(Neville, 1997). As descnbed by Rosenberg et al, (1989), chloride ions becorne uicorporated

in the passive film, replacing some of the oxygen and increasing its conductivity and

solubility causing the fiLm to lose its protective character.

Corrosion due to chloride penetration is often localized and takes the f o m of pitting. In

addition to overall chloride concentration and the availability of moisture and oxygen, other

factors such as the cathodehode area ratio and the elecûical resistivity of the concrete affect

the rate of dissolution of iron (Rosenberg et al, 1989). If a concrete structure is subjected to

alternative wening and drying in combination with chlonde salts, the critical chlonde content

at the crack tip will be reached often within years. The concentration profile dong the

reinforcement will have the form depicted in Figure 2.4. This Spe of corrosion is

charactenzed by galvanic action between relatively large areas of passive steel acting as a

cathode and small anodic pits where the local environment develops a high chlonde

concentration

CRACK

/ y / / / / / / O '

2-1.2 Carbonation Induced Corrosion

Another cause of steel passive layer breakdown is a decrease in the pH value of the aqueous

solution in the concrete pores due to reaction of the cernent paste with CO2 from the

Amounts o f 4 chloride at the steel surface - c - - - - Crifical anoun?

Figure 2.4. Chloride Concentration at the Steel Surface in the Region of Crack

(Bakker, 1988)

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atmosphere. Such a reaction is called carbonation. Schematic representation of the

carbonation process is illustrated in Figure 2-5.

MOOEL Chernial rearhn wifir free - 9 m w m : 1 Ca(0HI2 + CO2 - CaC03 + HP.

-Sm I - t

Figure 2.5. Schematic Representation of Carbonation Process

(Bakker, 1 98 8)

By difision, carbon dioxide penetrates into concrete and reacts with calcium hydroxide

dissolved in water.

As a result of this reaction, pH of the pore solution reduces. As carbonation proceeds, the pH

varies accorduigly in different regions, as shown on Figure 2.6.

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d'istance from concme surface

Figure 2.6. Pronle of pH range of Carbonated and Non-Carbonated Concrete

(Chandra and Ohama, 1 994)

The rate of carbonation highly depends on the relative humidity of the environment around

the concrete structure. If a concrete sû-ucture is exposed to air, carbonation proceeds faster

than if the concrete structure is exposed to water because the rate of gas diffusion is 4 tirnes

higher than the liquid penetration (Torok, 1995). As can be seen fiom Figure 2.7, carbonation

does not occw at relative humidity of O or 100%. In a completely dry concrete, the CO2

c a ~ o t react due to the lack of water in the pores for the dissolution. If a concrete structure is

submerged in water (Le. relative humidity is 100%) carbonation will not occur since the

pores are so full that there is no room for carbon dioxide to enter and disperse (Chandra and

Ohama, 1994). Therefore, when the pores contain some moisture but are not completely

saturated, the CO2 rapidly reaches the area of the pore walls and has enough moisture for

reaction (Rosenberg et al, 1989).

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Figure 2.7. The Degree of Carbonation as a Function of Relative Humidity

(Rosenberg et al, 1989)

Phenolphthalein indicator can be used to indicate the change in the pH value by changing

colour at pH of approximately 9.5. However, it is not the measure of carbonation depth.

When the carbonation reaction is in progress (pH between 9.5 and 12.5, as shown on Figure

2.6), i.e. beyond die boundary shown by the colour change, it cannot be detected by a

phenolphthalein indicator (Chandra and Oharna, 1994). Depth of the carbonation can also be

established by core sampling. In some cases, when the exposure conditions are steady, the

depth of carbonation (D in mm) is proportional to the square root of t h e ( r in years):

D = i2-41

where K= carbonation coefficient in ~ n m / y r ~ - ~ , which is approximately 3 or 4 mm/yr0.5 for

low-strength concrete (Neville, 1997).

2.2 Mechanism of Concrete Confinement

The pnnciple of concrete confinement consists of restraining lateral expansion that occurs

under axial compression. The compressive strength, and especially ductility of the concrete

can be increased by confinement, Circular sections are easiest to confine efficiently since

confuiing pressure puts the concrete in a compressive state of stress in al1 directions when

axial compression is applied and because the connning shell is in tension only and thus

provides a contuiuous connning pressure around the circumference. In case of square hoops,

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the confining pressure varies from a maximum at the corners to a minimum in between the

edges (Figure 2.8) thus the considerable portion of the concrete cross-section may be

unconfined (Park and Paulay, 1975)

Unwnfined

(a) (6

Figure 2.8. Confinement by (a) Square Hoops, (b) Circular Spirals (Park and Paulay, 1975)

Confinement effectiveness is defined as f / f ,,, where f, is the strength of confined

concrete, fi0 is the strength of unconfined concrete. Richart et al (1928) suggested the

following relationship between confinement effectiveness and confinement ratio Cf, /&),

where f, is confinement pressure:

f cc /fco = If k r r r / f CU)

where kl is effectiveness coefficient = 4.1, depends on lateral pressure

Since confinement is not as effective at high levels of lateral pressure, Newman suid Newman

(1 97 1) suggested the following relationship:

k, = 3.7( fI/fca) do-14 [2.6]

Saatcioglu and Rami (1992) suggested the foUowing non-linear relationship based on the test

data fiom Richart et al (1 928): -0.17 kl = 6-75 12-71

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The confinement provided by transverse reinforcement or an extenial jacket depends on two

factors: the tendency of concrete to diIate and the radial sti£fiiess of the confinhg member to

restrain the dilation. In modelling confinement effects, the following conditions are assumed

to be satisfied:

1. Strain compatibility between the core and the shell

2. Equilibriuni of forces in the free-body diagram for any sector of the confined section, as

illustrated in Figure 2-9.

Figure 2.9. Confining Action of Continuous Sleeve (Mirmiran and Shahawy, 1997)

Assuming the case of confinement providing by a cylindricd shell, the following relationship

can be drawn fiom equilibrium and geometry of Figure 2.8:

5 = 2L 5 / D

where f,- confinement pressure

A- hoop stress in the confining element

Mirmiran and Shahawy (1997) estabiished the following relationship for FRP-encased

concrete:

fcc =fco +d-2695 0.587

~2.91

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2.3 RC and Steel Jacketing

Until recently, the most common method of strengthening was to install circumferential

reinforced concrete or steel jackets around concrete column, It is an effective method of

column strengthening. However, installation of steel jacketing is a labour intensive and time-

consuming method that requires heavy equipment. Individual plates are heavy and they need

on-site welding md/or bolting to form a continuous jacket.

Steel plate jackets c m o t be constnicted to fit in direct contact with the existing concrete

shape. Therefore, in order to provide confinement, the annular space between the steeI plate

jacket and the concrete must be filled with a structural concrete or epoxy-type resin that is

capable of transferring structural loads. This process is labour intensive and it is generally

difficult to completely fiII the annular space (Ballinger et al, 1993).

Moreover, installation requirements rather than confinement requirements determine steel

jacket thickness and weight. Each jacket has to be extremely heavy and strong to prevent it

fiom buckling under its own weight during lifting, placing and grouting, which makes this

retrofit method expensive (Cercone and Korff, 1997). Increased weight and cross-sectional

area of the structure may influence seismic response and/or clearance (Bdlinger, 1997).

As an alternative to steel and RC concrete jackets, fibre reinforced polymer composites can

be used as wraps for retrofitting and rehabilitation of existing concrete columns. The use of

externally-bonded fibre reinforced polymer materials is thought to elirninate many of

problems associated with application of steel and RC concrete jackets for concrete repair.

2.4 Fibre Reinforced Polymers (FRP)

"Fibre reuiforced composite materials have long been recognized for their high strength,

good fatigue life, light weight, ease of transportation and handling, low maintenance cost and

good corrosion resistance" (Levergne and Labossiere, 1997). They have been used

extensively in the aerospace, aeronautic, automotive and other fields.

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The FRP materials are made of fibre such as glass, ararnid, or carbon embedded in a resin

rnatrix. As iilustrated in Figure 2.10, the fibres are stronger than the rnatrix. Therefore, the

fibres are the primary load-carrying part of the composite. The ma& binds fibres together,

bonds them to the structure (in case of extemally bonded FRP), and protects them fiom

environmentai attack.

Figure 2.10. Stress-S train Relations hip for Fibrous Reinforcement and Matrix

(ISIS Canada, 2000)

In this thesis, mostly extemaily-bonded carbon fibres are discussed. Although, carbon fibres

are more expensive, they have higher strength and higher elastic modulus than other fibres.

For example, the effective strength of g las fibres is less thao 2/3 that of carbon fibres and the

elastic modulus is about 1/5 of that of carbon fibres (Ballinger, 1997).

Carbon fibre reinforced polyrner (CFRP) requires little if any heavy equipment, hardens

rapidly and needs no additional treatment after hardening. Therefore, less installation time is

required than with other conventional strengthening methods. While carbon fibre reinforced

composite materials are relatively expensive, experiments have shown that the labour costs

for CFRP strengthening can be 20 to 30% less than for conventional strengthening work

(Emmons et al, 1998). The advaotages of carbon fibres also include ultraviolet resistance and

the fact that carbon fibres are not reactive with concrete, and do not corrode.

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2.4.1 Manufacture of Carbon Fibres

Carbon fibres are manufactured by extrusion of a polymer into a continuous nlament. The

filament undergoes a stabilization treatment in air at 200 to 350°C, after which it is heated-

treated (carbonized) at temperatures between 350 and 1600°C in a . inert gas atmosphere to

remove H, O, N and other contaminating elements.

The mechanical properties of the resulting fibres can be modified by a subsequent heat

treatment at temperatures between 1300 and 3000°C. Commercial carbon fibres with elastic

modulus of about 230 GPa are known as high-strength or low-modulus fibres. If the elastic

modulus is in the range of 480 to 700 GPa, this is referred to as high-modulus fibres.

Theoretically, the modulus of perfectly aligned fibres would be about 1000 GPa (Meier,

1992).

2.4.2 Externally-Bonded FRlP for Confinement

External confinement of concrete by means of high-strength fibre composites can

significantly enhance its strength and ductility as well as result in a large energy absorption

capacity (Mk-mkan et al, 1997).

An FRP jacket, as opposed to a steel one, has an elastic behaviour up to failure and therefore

exerts a continuously increasing connning action (Spoelstra and Monti, 1999). Figure 2.1 1

represents the stress-strah relation for CFRP, GFRP and steel-confined concrete. The Fm-

confined concrete shows an ever-increasing branch, as opposed to steel-confined concrete,

which after reaching the peak strength decays with a sofiening branch.

Parameters that affect ductility of FRP-confined concrete include unconfined concrete

strength, types of fibres and resin, fibre volume fraction and fibre orientation, thickness of

wrap, and interface bond between the member and FRP. Also, shape of the column as well as

column length-to-diameter ratio can a e c t the effectiveness of FRP rehabilitation methods.

The effect of some of these parameters on FRP-confhed concrete performance is discussed

below.

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CFRP

nonnalized axial strain

Figure 2.11. Typical Behaviour for Concrete Confined with Steel, CFRP, and GFRP

(Spoelstra and Monti, 1999)

Orientation of Fibres

The orientation of fibres is very important for rehabilitation of columns. Fibres can be

oriented al1 in one direction, but for the optimum structural performance they may be

oriented in different directions. The layers with fibres in the axial direction enhance the

flexural strength of a colurnn, while the layers with fibres in the circumferential direction

provide confinement. When the confinement layers cover only a lirnited region of the

column, shear resistance does not increase, but ductility under axial compression is expected

to irnprove. Experiments conducted by Levergne and Labossiere (1997) have shown that

application of one layer of carbon fibres oriented in the axial direction in the potential plastic

hinge region did not enhance signîficantly the flexural strength of a column, although, it

inhibited the development of transverse cracking in the composite straps until failure. When a

column was repaired with 6 layers of carbon fibre oriented in the circumferential direction on

top of one layer oriented in the longitudinal direction, its initial strength was exceeded.

A retrofit concept developed in Japan involves application of CFRP in the longitudinal

direction of a column and CFRP sheets or strands in the transverse direction, to provide the

necessary flexural and shear strength and ductility to meet new seisrnic design critena. This

rehabilitation technique has shown good results as far as flexural and shear strength and

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ductility is concerned. This methodoIogy was also suggested for repair of damaged colurnns

(Baiiinger, 1 997)-

Thickness of Wrap

Experiments carried out at the uni ver si^ of Toronto involved 150 x 300 mm cylinders

containing polypropylene and micro fibres. Cylinders were wrapped with zero degree angles

of orientation (i. e. perpendicular to the loading direction) CFRP sheets. The results have

indicated that the increase in the nurnber of wrapping layers increases signifïcantly the

maximum strength of concrete (Zanganeh, 1997).

Experiments carried out at the University of Sherbrooke have shown that the stren-& of 150

x 300 mm cylinders increased with the increase of number of layers of ararnid/epoxy

composite wrap (Demers et al, 1996).

Mirmiran et al. (1998) reported the results of a study to determine the effect of the thickness

of E-glas fibre on the confinement of circular and square section colurnns. The results have

indicated that while wrap thickness greatly affected the response of circular section, for

square section this effect was minimal.

Bond

Extemal FRP requires a sound bond to sound concrete substrate to remain intact throughout

its service lifte. The bond strength and integrïty depend on the physical and chernical

characteristks o f the components, which include the fibres, the concrete substrate and the

epoxy that acts as a binding agent. The interface bond affects the state of stress in the

concrete, and also affects the capacity of the member. The bond must be capable of

withstanding stresses and the processes of degradation normally irnposed on the concrete

structure. EssentiaIly, FRP provides exterior non-corroding reinforcement to the concrete.

Unfortunately, the bond surface, the skin of existing concrete, is the weakest part of the

concrete cross Section (Emmons et al, 1998). Factors detennuiing the strength and durability

of FRP bond sumniarized by Emmons et al, (1998) include:

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Tensile strength of the concrete skin

S trength of the epoxy adhesive system

Cleanliness of the concrete and FRP surface

Uniformity and thickness of the adhesive layer

Geometry of exterior strengthening

Types of loading

Environmental conditions at the time of application and curing

Workmanship and quaiity control.

Colunui Shape

Experiments performed by Mirmiran et al, (1998) have shown that confinement of square

sections using E-glas fibre jackets is less effective than their circdar counterparts. It can be

explained by the distribution of confining pressure in circular and square sections. While for

a circular section the confinhg pressure is uniform, for a square section the connnuig

pressure varies fiom a maximum at the corners tu a minimum in between the edges.

2.4.3 FRP for Corrosion Repair

FRP wraps c m also be used for repair of corroded reinforced concrete mernbers. Post-repair

corrosion c m be altered by a combination of two mechanisms. First the FRP wrap works as a

diffusion barrier that isolates the column fkom the environment and lirnits the ingress of

oxygen and moisture to the reinforcing steel. Aiso the wrap can develop conf ing pressure

to resist the expansive tendencies that are generated by corrosion products. (Sheikh et al,

1997).

CFRP, because it is composed of inert substances, is ideal as a strengthener in corrosive

environments because it does not react with the majonty of corrosive agents. Carbon

composites are unafEected by water and alkalis, and do not corrode (Cercone and KorfT:

1997).

Experiments on the tensile performance of FRP composite sheets subjected to wet/dry and

fkeezehhaw cycles performed by Toutanji and El-Korchi (1999) have shown that glass-fibre-

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wrapped specimens experienced a significant reduction in strength due to environmental

exposures, as opposed to carbon-fibre-wrapped ones. Therefore, carbon-fibre-reinforced

polymer is superior to g las when exposed to harsh environmental conditions.

Experiments conducted at the University of Toronto involved the repair of large-scale

corroded RC columns. The specimens 1524 mm long and 406 mm in diarneter were repaired

with the TYFO Fibnvrap System. The material is a woven fabric 1.7mm thick, containing

glass fibres in the primary direction and orthogonally oriented aramid fibres. A strength gain

in the range of 11 to 25% was observed when the columns were wrapped with 2 Iayers with

various expansive grouts between the wrap and the original column surface (Sheikh et al,

1997). Additionally the ductïlity of the repaired column was significantly higher than that of

the undamaged column.

Experiments carried out by Lee (1998) and Khajehpour (2001) at the University of Toronto

as a part of the overall project involved large-scale RC columns. The corroded specimens

10 16 mm high and 305 mm in diameter were repaired with 2 layers of pre-impregnated

Replark Type 30 CFRP sheets. Corrosion damage reduced the load-carrying capacity of the

specimens by 7 to 16% (dependhg on the level of damage). As a result of repair, Ioad-

carrying capacity of the corroded specimens increased by up to 32%. Moreover, repair

signifïcantly uicreased ductility of the column.

2.5 Corrosion Inhibitors

As defined by Bradford (1993), an inhibitor is a chernical substance added to the corrosive

environment to reduce the corrosion rate. In the majority of cases inhibition is achieved

through the reaction between the corrosion inhibitor and the metal surface, resdting in the

formation of an inhibitive surface film. In other cases the chemistry of the environment may

be modified to render it less corrosive, e.g. by chemically scavenging dissolved oxygen;

chemically neutralizing dissolved acidic gases; or by adjusting pH to promote stable

passivation (Harrop, 1990). Inhibitors have a critical concentration that rnust be reached or

exceeded for them to be effective, and in some cases to prevent them fiorn making corrosion

worse (Bradford, 1993).

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2.5.1 Classification of Corrosion Inhibitors

Corrosion inhibitors can either affect the anodic partial reaction, cathodic partial reaction or

both. Thus, there are two major types of inhibitors: anodic and cathodic. This classincation

depends on inhibitor's reaction at the metal surface and how the potential of the metal is

affected. in reducing the corrosion current, the corrosion potential is shifted positively for an

anodic inhibitor (Figure 2.12a) and negatively for a cathodic inhibitor (Figure 2.12b). In the

case where the inhibitor affects both partial reactions, the shift in corrosion potential will

depend on which is the more dominant effect (Figure 2.12~) (Bradford, 1993).

Figure 2.12. Effect of Adding (a) an Anodic Inhibitor, (b) a Cathodic Inhibitor, (c) a Mixed

Inhibitor. Broken lines show inhibitor addition (Bradford, 1993)

2.5.2 Application of Corrosion Inhibitors

Corrosion inhibitors have been used successfully for a number of years in order to control

corrosion of steel in aggressive environments. There are a large variety of corrosion

inhibitors available on the market that can be used for specific applications, such as water

treatment, packaging, and petroleurn refining (Montani, 1996).

The use of inhibitors for corrosion control of reinforcing steel in concrete is a relatively new

development. In 1957 Moskvin and Alexeev found that barium nitrite, sodium nitrite,

potassium chromate and potassium dichromate added to the concrete mix, in arnount varying

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fkom 0.5 to 3.0% based on the weight of cernent, improve corrosion protection, with sodium

nitrite offering the best protection fkom chloride-induced corrosion (Ehrlich and Rosenberg,

199 1). In the 1960s, calcium nitrite became available for use as a corrosion inhibitor. It was

found to be very effective as far as corrosion resistance is concerned (Figure 2.1 3), relatively

inexpensive, and it does not lower the strength of concrete. However, calcium nitrite is a set

accelerator, so care must be taken that flash setting does not occur @roomfield, 1997). In the

1980s amino-aicohol-based inhibitors were discovered and have s h o w good results

(Montani, 1996).

I I I I t *

- -

OAtA OETE RUINE0 fN THE PRESEUCE O F 013% SODIUM CHLORIDE BASE0 ON WElGt fT O F SAWO ot -400 mv 4

d

-

Figure 2.13. Effect of Calcium Nitrite on the Corrosion of Steel in Mortar

(US. Pat. No 092 109) (Ehrlich and Rosenberg, 199 1)

As illustrated in Figure 2.14, corrosion inhibitors may have two moderating effects on the

corrosion process in the reinforced concrete; increase the time for corrosion initiation and

reduce the rate of corrosion (Montani, 1996).

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Time to and rate of corrosion Limit of service life

To Tz TL! +-. f r*

-- - without inhibitor with inhibitor

Figure 2.14. Moderating Effect of InhibZtors on Corrosion Process (Montani, 1996)

The method of application varies: in new structures inhibitors are admixed in suficiently

high concentrations to the fiesh concrete; for repair work inhibitors c m be present in paints

for the reinforcement or in repair mortars; on existing structures, where the onset of corrosion

has to be prevented, inhibitors are applied at the concrete surface (Elsener et al, 1997).

2.5.2.1 Inbibitors in Concrete Mix

In order to increase the tïme for corrosion initiation in newly cast concrete, inhibitors can be

added to the concrete mix dong with such preventive measures as low permeability, concrete

cover and epoxy-coated re-bars (Montani, 1996). However, some inhibitors when added to

concrete may influence other concrete properties; e.g. lower the ultimate strength, retarded

setting time of the cernent, and the development of efflorescence. Therefore, it is very

important to test the inhibitor under the conditions intended for use to insure that it does not

impair the performance of the concrete (Ehrlich and Rosenberg, 1991).

Inhibitors also can be incorporated in large-scale concrete repairs. When the carbonated or

chloride-contaminated concrete is replaced with a new low permeability material, a liquid

inhibitor can be sprayed on the concrete prior to repair to protect the reinforcement below the

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surface andor an inhibitor can be included in the overlay material as an admixture. However,

it is very important to consider any synergistic effects of inhibitors and other admixtures on

concrete properties in order to avoid alteration of setting time, strength, slump, and air

content (Montani, 1996).

2.5.2.2 Penetrating Corrosion Inhibitors

The usual approach of locdized repairs includes the replacement of the unsound concrete

with low permeability materid. However, indications of future corrosion ofien occur shortly

d e r repair, particdarly at the interface of the replaced material; such areas are called

incipient anodes. These areas corrode at an even façter rate then the original anode areas. Ln

order to prevent corrosion on the incipient anodes, penetrating corrosion inhibitors c m be

included in the repairing material (Montani, 1996).

The future corrosion activity in larger areas surrounding repairs is cucrently addressed by

applying protective coatings to stop COa and/or chlorides fiom penetrating. However,

additional surface treatment with penetrating corrosion inhibitors prior to the application of

protective coating may reduce the effect of active corrosion present at the steel (Montani,

1996).

Penetration of corrosion inhibitor occurs via both liquid and vapour diffusion. The rate of

penetration depends on the density and permeability of the concrete and is relatively

independent of the rnoisture content The migration of the MCI@ 2000 admixture is

documented to be about 7Scm within 7 days of initial application (Figure 2.15, CORTEC

Corporation - 2, 1996). Corrosion inhibitor Sika FerroGard-903 was proven to achieve

penetration rated of 2-20mm per day, as stated in the manufacturer brochure (Figure 2.16,

SIKA Ferrogard @, 1996).

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Figure 2.15. Migration Concentration Curve for MCI@ 2000

(CORTEC Corporation - 2, 1 996)

Figure 2.16. Migration Concentration C u v e for Sika FerroGard-903

(SIKA Ferrogard @, 1996)

2.6 Grout

Grout is a mixture of cernent (or binder of cernent plus supplementary cementing materials)

with water and adrnixtures. However, it also may include inert filler (i.e. a fine aggregate).

Cementitious grouts are used for an increasing number of existing structurai purposes. Any

type of cernent may be used though care should be taken if rapid-hardening Portland cernent

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is used in large quaatities due to its uicreased heat of hydration Thus, the use of grout in

structures is generally restricted to smaü ùiickness sections. Grout needs to be sufficiently

fluid to be efficiently pumped and injected to fiIl al l the voids. (McLeish, 1994).

When considering the use of cementitious grout for structural repair purposes attention must

be paid to the inherent properties of the grout and in particuiar the problems that may be

encountered. Compared with concrete, grout typically has a nurnber of disadvantages when

used as a structural materiai (McLeish, 1994):

It is expensive when used in large quantities

It sufférs fkom a high drymg shrinkage

It has a high heat of hydration and coefficient of thermal expansion, often resulting in

temperature-induced cracking when used in thick sections.

The inclusion of small-size aggregate overcomes to a large extent many of these problems.

The mixture consisting of grout and small aggregate can be designed to have the same

properties as grout. It can be pumped to flow into position around reinforcernent without

vibration (McLeish, 1994).

Expansive Grouts

Expansive cements are inorganic hydraulic binders which, when hydrated, generate stresses

in the set matrix leading to an overail expansion of the concrete mass (Odler, 199 1). Cements

with high sulphate content exhibit their expansive properties due to formation of ettringite

(Cusick and KesIer, 1980).

It has long been recognized that there is a problern of cracking of concrete afler hardening

and that this problem is contrïbuted to by many different factors such as cooling and drying.

Cooling causes contraction; drying causes shrinkage; both contraction and shrinkage cause

tension, which if in excess of the tensile strength, causes cracking (Mather, 1980). Therefore,

the basic purpose of expansive cements is to eliminate the drying shrinkage inherent in

conventiond concrete by an initial expansion, and thus minimize cracking (Li and

Ramakrishnan, 1980). Thus, this cernent may be referred to as shrinkage compensating. The

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reduction or elimination of cracking will reduce or prevent the rapid corrosion of the

reinforcement that can occur at a crack (Cusick and KesIer, 1980).

The use of expansive grouts in conjunction with FRP wraps for repair of corroded concrete

columns with circula cross-section was investigated at University of Toronto (Sheikh et al,

1997). The specimens were 1524 mm long and 406 mm in diameter. Expansive grout was

introduced in order to establish initial prestressing forces in the wrap, and thus enhance initial

amount of confinement provided by the wrap. The Level of confinement stress applied to the

member by the connoing repair system depends on the amount of deformation induced in the

composite wrap by concrete expansion. The composition of the grout used in these

experiments was 60% (by weight) Portland cement Type 10,25% high a l d a cement, 12%

plaster of Paris, 3% hydrated lime, superplasticizer (0.3% by weight of Portland cernent), and

wlc of 0.4. This type of grout develops 2.540% unrestrained expansion, and it is known to

develop significant confining stress under restrained conditions. The use of expansive cernent

with two layers of FRP wrap resdted in excellent behaviour of the specimens (Sheikh et al,

1997).

2.7 Methods for Monitoring Corrosion

The need for early detection and diagnosis of corrosion related deterioration in reinforced

concrete structures is widely acknowledged. Many types of corrosion monitoring techniques

have been developed. McKenzie (1986) classified corrosion monitoring techniques into two

broad groups, as shown in Figure 2.17. The Grst group represents non-perturbative

monitoring methods, whic h measure the signal generated b y an electrode (reinforcement)

without the application of any extemal signals. On the contrary, the other group represents

perturbative methods, which measure the response of the reinforced concrete structure to

extemally applied stimulants (electrical signais).

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Corrosion monitoring of steel in concrete

resisrance

Potentiallcurrent W P ~ ~ Q noise

resis tance I

Figure 2.17. Corrosion Monitoring Techniques (McKenzie, 1986)

2.7.1 Non-Perturbative Methods

Non-perturbative techniques include half-ce11 potentiai (potential mapping), electrical

resistance, and potential noise measurements. These are discussed in the following sections.

2.7.1.1 Potential Mapping

The potential mapping technique is the most widely used on-site electrochemical method.

This method has the advantage of being a non-destructive and easy to perform technique for

determinhg the probability of active corrosion. Theoretically this method can be used to

cdculate the rate of corrosion, although Chess et al, (1998) noted that in practice s a c i e n t

accuracy couldn't be achieved to provide anythmg but general indication of the corrosion

rate.

Half-ce11 potential method is described in ASTM C876-91. As corrosion proceeds, some

areas depassivate and becorne anodic, while others remain passive, thus cathodic. The

objective of the half-ceil potential test is to mesure the areas of different potential on the

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surface of the concrete with respect to a stable reference cell in order to identis, and map

anodic and cathodic areas. Many types of electrodes can be used as a stable reference half-

cell:

Silver/silver chloride (AdAgCi)

Mercury/mercury chloride (Hg/HgzCl2)

Copper/copper sulphate (Cu/CuS04)

Zirdseawater (Zdseawater)

Manganese dioxide (Mi10z)

Generally, copper/copper sulphate cells are used since they are robust, relatively cheap and

easy to use, although silver/silver chloride ceils can be more stable, and have faster response

time (Baker, 1986).

The values of reinforcement potential c m be found using the following equation (Rosenberg

et al, 1989):

Eco, = Eo + (RT/F) Zn K

where Eco, - metal potential at equilibrium

Eo - standard electrode potential for the reaction

R - the gas constant

T - the absolute temperature

F - Faraday's constant

K - equilibrium constant for the ions present in the solution

Therefore, E,, c m be measured with respect to the standard reference electrode (Figure

2.18).

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l High impedance voltmeter

Reference electrode Sintered glass eg. CulCu S O ~ membrane plug

High conductivity sponge

- Reinforcing

1 Concrete

Figure 2.18. HaE-Cell Electrode Measurements (McKenzie, 1986)

2-7.1.1.1 Interpretation of Results

Van Deveer found the following relationship between the calcdated potential and the

probability of corrosion (Chess et al, 1998).

E,,,, (vs Cu/CuS04), volts

More negative than -0 -3 5

More positive than 4.20

Between -0.20 and 4.35

Probabiiity of Corrosion, %

95

5

uncertain (probably b e ~ e e n 5 and 95%)

This method was initialIy used to monitor corrosion of steel pipelines. Later, the use of the

half-ce11 potential method was developed to investigate the corrosion process in concrete

bridge decks; therefore, the results should be interpreted very carefully in structures other

than bridge decks.

Half-ce11 potential results can be presented as equipotential contour maps (Figure 2.19).

Potential mapping survey gives difference in potential, which can identiS the anodic zones

(rnacro-cells), and their paaicular location. The measurements of the potential gradients

created by the corrosion process allow areas of possible corrosion to be identified. It was

found that the pattern of these contours provides more valuable information about the status

of the corrosion in concrete structures than the precise values of the potentials (Baker, 1986).

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Figure 2.19. Sample Schematic of Half-Cet1 Potential Data

(Chess, Gronvold & Karnov, 1998)

Spacîng between plotted points on the contour maps should satisS the type of investigation.

For example, when chloride-induced pitthg corrosion is under investigation, relatively small

spacing should be used in order not to overlook localized pits (Baker, 1986).

2.7.1.1.2 Influences on Measured Potential

Potential measured on the surface of the concrete can be influenced by a wide variety of

factors. Baker (1 986) surnmarized these factors as follows:

Equi~ment and Technique

There could be up to about lOOmV difference due to voltmeter stability, electrode variability,

electrode position, and electrolyte concentration in the reference electrode.

Surface Skid Resistance Effect

Carbonation of surface, quality of surface, contact electrolyte between electrode and

concrete, could give up to approximately 500mV difference.

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Concrete Properties

Quality of concrete (Le. depth of concrete cover, moisture content of concrete, salt

concentration effects, concrete degradation due to some destructive mechanisms, electrical

potential of steel in concrete) effects electrical resistivity and could give up to 400mV effect.

It must be pointed out that greater depth of cover will result in shallower potential gradients

and corrosion in lower layers of reinforcement wilI be dBïcult to detect. In structures with

complicated reinforcement layout or with a concrete of low resistance it might be hard to

i d e n t e which layer of reinforcement is corroded (Chess and Gronvold, 1996). Also, if the

concrete structure is submerged in the water or soil, local corrosion occumbg in the

submerged parts of the structure cannot be dehed. Half-ce11 potential mapping can give

precise information about the local corrosion damage on structures that do not have several

layers of reinforcement (Chess and Gronvold, 1996). However, the analysis of the results can

be rnisleading and a qualified specialist must interpret the data in order to identie the

influence of the circurnstances, such as variations in hurnidity and other inhomogeneties,

which may lead to wrong conclusions.

2.7.1.2 EIectrochemical Noise

The technique of electrochemical potentid noise monitoring of steel in concrete measures the

noise fluctuations in the free corrosion potential of the reinforcernent (E,,,) by applying a

high input irnpedance voltmeter against a stable reference electrode, as for potential mapping.

It is believed that the noise represents the activity of the passive oxide film on the surface of

the electrode (McKenzie, 1986). When reinforcement is corroded, broken or damaged

passive oxide film generates curent.

When noise data are collected they should be conditioned in order to remove trends. The

relationship between the standard deviation of the amplitude of noise tirne record and a

corrosion rate determined by polarization resistance could be established (McKenzie, 1986).

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2.7.1.3 Electrical Resistance

The electrical resistance method for monitoring corrosion is based on the fact that when

metal corrodes, electricd resistance changes. In case of uaiform corrosion, measured

electrical resistance is proportional to the growth of corrosion; however, in case of pitting

corrosion this method rnay give misleading resdts (McKenzie, 1986).

The embedded corrosion probe adjacent to the reinforcement consists of two components of

an AC bridge. While one element is exposed, the other one is covered to compensate for

fluctuations in resistance due to temperature changes. The electrical resistance monitoring

method measures the instantaneous value of corrosion rate. Therefore, a few readings should

be taken in order to find an average value of corrosion rate (McKenzie, 1986).

2.7.2 Perturbative Methods

This group includes the linear polarization resistance technique and the AC impedance

method, which are explained in the following sections.

2.7.2.1 Linear Polarization Resistance

Linear polarization has been used extensively for corrosion rate measurements and dates

back to Tafel's original work in 1905 (Cameron and Chiu, 1986). The polarization resistance

method involves the displacement of the voltage of an electrode relative to the solution or

concrete in contact with this electrode, and consequently some modifications to the rates o f

cathodic and anodic reactions (Lawrence, 1990). The potential - current density plot is

approximately linear in the region within lOmV of the corrosion potential (Figure 2.20). The

slope of this plot in terms of potential divided by curent density has the units of resistance-

area and is often called the polarisation resistance (Dean, 1986). The polarization resistance

is related to corrosion current density by the Stem-Geary relationship (McKenzie, 1986):

r,, = (p, *pj/2.3(--+ pj *m =BIR, [2.111

where l$, = polarization resistance

B = Stem-Geary constant, dependent on contributions fiom cathodic and anodic

reactions

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Pa = anodic Tafel constant

p, = cathodic Tafel constant

AI = applied current

AV= change in potentiai

I ,, = corrosion current

Figure 2.20. Linear Polarization Technique (Ehrlich and Rosenberg, 1991)

Linear polarization method is very attractive both in the laboratory and in the field, because it

is relatively quick and easy to perform. The luiear polarization techniques determine the

"instautaneous7' value for corrosion of steel in concrete (McKeruie, 1986). Because the

extent of polarization of the specimen is small, the measurement technique does not

significantly damage the specimen, and so the measurement approach can be used for a long

penod of t h e as long as the general corrosion rate is not too high.

2.7.2.1.1 Tafel Constants

In order to use linear polarization technique it is necessary to know the Tafel constants. In

many cases reasonable estimates can be made as to what these Tafel constants should be, and

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in other cases, the method can be calibrated using mass loss data. The Stern-Geary constant

(B) is a function of the environment and alloy under study, and seldom known with accuracy.

The Stem-Geary constant can be related to TaféI constants using the relationship:

As suggested by Corrosion Senrice Co. Ltd. (1998), Stem-Geary constant in many cases can

be approxirnated with 20 rr,V for active state (corrosion current >1 to 2 jA) and 52 mV for

passive state (corrosion current 1 pA).

2.7.2.1.2 Galvanostatic and Potentiostatic Approach

Chess et al, (1998) describe two approaches for measuring corrosion rate by linear

po larization methods.

The first one is called the galvanostaric approach. Two similar electrodes are cast into

concrete at srnall spacing (Figure 2.2Ia). After measurine, the corrosion potential (Eco,), a

few fixed smdl levels of direct current (DC) are prissed fiom the auxiliary electrode to the

reinforcement. Then the corresponding change in potential is measured. in this case, it is

assurned that the potential drop divides equally between the cathode and anode.

BOTH ARE TEST

pELECTROOES * REFERENCE

AUXlLlARY ELECfRODE + ELECTFtODE - __ _1 M

TWO ELECTRODE SYSTEM THREE ELECTRODE SVSTEM

Figure 2.21. Two Types of Polarization Resistance Probes; (a) Two-Electrode System,

(b) Three-Electrode System (Dean, 1986)

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The second method is cdled the potentios~aîic qproach. The system used for this method

employs three electrodes (Figure 2.21b). One of them is the working electrode, while the

second one is the auxiliary electrode and the third one is the reference electrode. The

potential between the working and reference electrode is monitored. In order to mesure the

corrosion rate, a small voltage signal (10-20 mV) is applied both anodically and cathodically

to the test sample using a potentiostat and separate counter electrode (Ehrlich and Rosenberg,

1991). The current required for this potential perturbation is recorded and the potential is

plotted as a function of current (Figure 2.20). In conductive electrolytes, the slope of this

curve is referred to as polarization resistance (in ohms). The corrosion rate can be determined

using the Stem - Geary relationship (equation 2.1 1).

2.7.2.1.3 Interpretation of Results

The original method, proposed by Stem and Geary denves the corrosion current from

polarization resistance measurement under the assurnptions, sumrnarized by Giuliaai (1 986):

The potential at which rneasurement is taken (i.e. the corrosion potential) is sufnciently

far from equilibrium potentials that the cathodic deposition of the metal and the anodic

oxidation of the oxidant do not affèct it.

The potential shift induced during the measurement is sufficiently small to allow a series

expansion for the exponential function linking potential and partial current and to limit

such series to the second tenn.

Both anodic and cathodic reactions exhibit Tafel slopes in a voltage vs. log of current plot

at the corrosion potential or the cathodic reaction is under diffusion control and therefore

has an infinite slope.

Only the anodic reaction occurs at the corrosion potential, Le., the entire anodic current is

due to metal dissolution.

Corrosion system is in a steady state, Le., that potential variation over time is negligible,

at least during the measurement time.

Practical expenence indicates that generally reasonable agreement exists between resdts

obtained using linear polarization technique and measured weight losses for a large number

of corroding systems (Giuiiani 1986).

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There are some cases, however, for which polarization resistance technique may lead to large

errors, therefore care needs to be taken while interpreting the results. Tests performed in low-

conductivity electrolytes, Iike concrete, c m lead to an underestimation of the corrosion rate if

the electrolyte resistance is not subtracted out Çom the measured resistance. The measured

resistance (the slope of the cuve on Figure 2.20) is actuaily a sum of the electrolyte

resistance and the polarization resistance and only the polarkation resistance is inversely

proportional to the corrosion rate as can be seen fiom Stern-Geary relationship (equation

2.1 1). Since the electrolyte resistance in concrete is so hi& (1000 - 30000 ohm-cm), it

should be accounted for when using polarization resistance technique to measure corrosion

rates (Ehrlich and Rosenberg, 199 1). At high corrosion rates, readings c m be misleading in

case of localized (pitting) corrosion. Moreover, it is usually hard to accurately deterrnine the

area of polarized steel (Chess et al, 1998).

2.7.2.2 AC Impedance

Another non-destructive curent-measuring technique is AC impedance. The AC impedance

method involves application of a small amplitude (t 10 to 20 mV) AC signal to an embedded

electrode and cornparison of the initial perturbation with the response of the embedded

electrode (McKemie, 1986). In order to measure current required to cause voltage

perturbation, the srnall voltage signals should be applied over a range of fiequencies usually

O.SmHz to 100 mHz for concrete (Ehrlich and Rosenberg, 1991). The impedance method is

based on the assumption that the corroding electrode can be represented by an equivalent

electric circuit, combining resistors, capacitors, and indicators to represent the corrosion

process. Most corroding interfaces can be modeled by a simplified Randles' circuit illustrated

on Figure 2.22; where & represents the polarization resistance, Rn is the ohrnic (or

electrolyte) resistance, and C is the double-layer capacitance which exists as a result of

charge separation at the metaVelectrolyte surface (Ehrlich and Rosenberg, 1991).

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Figure 2.22. Simplified Randles' Circuit for Steel Corrosion

(Ehrlich and Rosenberg, 199 1)

At low fiequencies, the current going through the circuit can flow only through Rp and Rn.

Therefore, the measured impedance is & + Rn. While at high fiequencies current flows

through the capacitor instead of R,,, thus measured impedance is Rn. Consequently,

polarization resistance is the difference between the low fiequency and high fiequency

ùnpedances (Ehrlich and Rosenberg, 199 1).

Theoretically, the imaginary part of the measured impedance shouid descnbe a semicircle

when plotted against fiequency (Nyquist diagram, Figure 2.23). The two intercepts on the x-

axis are Rn or Rs and Rs + % values. The drawback of this sirnplified impedance method is

the difficulty in finding a second intercept at very low fiequencies (Guiliani, 1986).

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I

nrru RE8iSTAHCL ohm 1

Figure 2.23. Nyquist Diagram (Dean, 1986)

2.7.3 Probe Applications

Embedded corrosion probes adjacent to the reinforcernent are beneficial for measurements of

corrosion rate. The major advantage occurbg fiom embedding corrosion probes is that the

corrosion monitoring techniques c m be promptly applied to determine corrosion rates. Some

of the disadvantages sumrnarized by McKenzie (1986) include:

The probe only yields corrosion data confined to its Iocal environment

The probe vdl not be in the same electrochemical state as the resorcement

If embedded subsequent to construction, the probe will necessarily see a different

environment to that of the reinforcement bar

Unknown working area of the working electrode/reinforcement.

There are different types of commercial probes now available. In the case of resistance

probes, the electrical comection to the reinforcement pennits the probe to adopt a potential

and corrosion state similar to, although not exactly the same, as the reinforcement. An

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alternative to a resistance probe would be to embed a haE-ce11 reference electrode, working

electrode and cornter electrode close to the reinforcement. This three-electrode arrangement

would permit ha-cell potential, DC polarization and AC impedance measurements to be

conducted (McKenzie, 1986). There are different embeddable haif-ceil electrodes available.

Ag/AgCl cells have shown a stable performance and a very fast response tirne (Baker, 1986).

However, they give potentids that are a function of chioride concentration in them

(Broomfield, 1997). In 1986 an embeddable MnOz reference electrode was developed.

Results compare favourably with published data for other embeddable elecirodes and show

that the MnOz electrode has found wide acceptance, rnainly because of its very good long-

term stability (Amp et al, 1997).

2.8 Fibre Optic Sensors (FOS) in Structures

Until adequate repairs are made, monitoring of deterioration and progressive decay, and the

ability to wam against impending faiIure are essential for saving human life. Recent

developments in the field of fibre optic sensors offer advantages that can essentially

eliminate such deficiencies and enable the early warning of impending failure.

The introduction of advanced composite materials into rehabilitation and strengthening of

existing structures could be accelerated by the integrated monitoring capability provided by

fibre optic structural sensing technology. Installation of FRP wraps and patches provides the

opportunity to integrate fibre optic sensors with the composite materials to monitor

subsequent behaviour of the structure.

Fibre optic structural sensors are h u n e to electromagnetic interference making them more

suitable than conventional sensors for remote settings within large structures that are subject

to lightning or manmade sources of electrical interference. Due to their small size, linear

geometry and dielectric nature, optical fibres are embeddable in advanced composite

materials used for rehabilitation of concrete structures. Besides ruggedness, flexibility, and

small size, the most attractive feature of fibre optic sensors are their inherent ability to serve

as both the sensing element and the signal transmission medium, allowing the electronic

instrumentation to be remotely located fiom the measurement site (Ansari, 1 997).

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2.8.1 Manufacture of FOS

As shown in Figure 2.24, optical fibres manufactured at the University of Toronto Institute

for Aerospace Studies (1998) incorporate severai protective layers of material. A 0.007 mm-

thick optical core, at the centre of the fibre, carries the optical signai. Enclosing the core is an

amorphous solid hsed silica g las shell about 0.125 mm in thickness. The optical ciadding is

contained within a 0.75-mm thick coating of material such as acrylate or polymid buffer. The

various coatings surrounding the fibre optic core protect the g las fibre surface fiom abrasion

during handling and installation; fkom moisture, which weakens the fibre and can contribute

to the growth of micro cracks; and fiom the alkaline environment in concrete, which is

corrosive to conventional glass fibre. An outer jacket, either tightly bound to the fibre or in

the form of a loose tube, is surrounded by Kevlar-reinforcing fibres embedded in a polyrner

such as PVC plastic.

Keviar (Tight or toose) Fibre Buffer Reinforcing Fibres

Figure 2.24. Bondable Sensor (U of T, Institute for Aerospace Studies, 1998)

2.8.2 Basic Principlesof Application

Fibre optic sensing technology involves the installation of optical fibre sensors, which

measure strain and temperature, in or on concrete or steel structures and advanced composite

material patches. Basic principles described by U of T Institute of Aerospace Studies (1998)

are presented below.

Due to strain in the structure and temperature variations, fibre optic sensors expand or

contract by small amounts. A light signal is sent down the fibre to the sensor and is

moduiated according to the amount of expansion or contraction (the change in length of the

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sensor). The sensor reflects back an optical signal to an analytical device, which translates

the reflected light into numencal measurements of the change in sensor length. These

measurements indicate the precise amount of strain in the structure, and compensatory

calculations are made to eliminate the eEect of temperature change on the strain

measurements.

2.8.3 Fibre Optic Bragg Grating Sensor

A fibre Bragg grathg (FBG) is a segment in optical fibre having an axial periodic variation

in its core index of refraction, as illustrated in Figure 2.25.

Optical Fibre Grating Sensor

Figure 2.25. Bragg Grating Description (U of T, lnstitute for Aerospace Studies, 1998)

A fibre Bragg grating sensor consists of a continuous fibre core surrounded by germanium-

doped silica The grating portion consists of modulation in the index of lefiaction dong a

short length of that continuous fibre core. A change in length of the grating is due to

mechanicd strain or thermal effects in the matenal in which it is ernbedded (U of T, lnstitute

for Aerospace Studies, 1998). Fibre optic Bragg grating sensors rneasure strain through a

spectral shift of wavelength, which provides good isolation fiom noise sources such as

intensity fluctuation caused by light source or bending loss in the fibre. Typical grating

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lengths range fiom 1.5 to 15 mm, with longer gratings giving a narrower spectral bandwidth

(Nawy and Chen, 1994). The grating forms a narrow band reflechon at wa-velength, which

matches the Bragg condition:

where RB = Bragg wavelength

n = refiaction index of fibre

A = Penod of Bragg grating in the fibre

The narrowness o f this band gives good resolution and strains less then 10 miicrostrain can be

detected. A theoretical relationship has been established between fiactieonal change in

wavelength and induced strain (Nawy and Chen, 1994):

where k is a constant of strain coefficient for grating. A typical value of k is about 1.3.

For certain applications it is desirable to have a gauge length that is longer t&an practical for

a single Bragg grating. In this case it is possible to use either one short brmadband grating

and mirrored tip of the optical fibre. or two short broadband gratings. The sëeparation of the

reflection elements now defines the gauge Ien-@h of the localized sensor. The arbitrary bauge

length structural sensor is illustrated in Figure 2.26 (Measures, 1997). T h i s type of sensor

makes an ideal hoop-strain sensor for use directly ullth concrete coa1urnns or with

rehabilitation and strengthening wraps for corroded or earthquake darnaged cmncrete columns

as shown in Figure 2-37.

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Figure 2.26. Schematic Diagram of Arbitrary Gauge Length, Localized Fibre

Optic Structural Sensor Based on Low Coherence uiterferometry

(Measures, 1997)

Corrvded Cuncrete Colum

Jxketed Opticai Fi

Demodulation System

Cornpositc Material ~ehabilitation and Strenglhening Wrap

Figure 2.27. Application of the Localized Fibre Optic Structural Sensor to the

Measurement of Hoop Strain in Concrete Columns (Measures, 1997)

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The performance of these kinds of sensors has been recently tested on site: a concrete column

under Highway 401 in Toronto (Measures, 1997). It is anticipated that these sensors will be

able to monitor pressure built-up within the composite repair wraps and relate this to

continuhg corrosion of the steel within the concrete column.

2.9 Remarks on Literature Review

The outlined literature review represents the main background for the effective experimental

design. The future research will focus on the development of restorative and monitoring

techniques for corrosion damaged CO ncrete infrastnrcture repaired with FRP wrapping

material.

The deterioration of the reinforcing steel embedded into concrete due to electrochemical

process has been discussed and appreciated. While mechanism of corrosion is well

understood, several interrelated factors determine the nature and severity of the corrosion.

These factors Vary fiom case to case and will be addressed specifically in the research.

The mechanism of concrete confinement restraining the Iateral expansion has proven to be

extremely effective and will be utilised in the research. FRP wrapping rather than reinforced

concrete or steel jacketing will be chosen as a repair strategy for extemal confinement of

corrosion damaged columns. Fibre reinforced polyrnets will be chosen because of the high

strength, ease of handling, low maintenance cost, corrosion resistance and impermeability to

chlorides, moisture and oxygen. The proper orientation of fibres, thickness of wrapping

sheets, and colurnn shape will be considered to optimize the structural pedormance and to

enhance the energy absorption capacity. The restorative techniques of the steel reinforced

corrosion damaged colurnns may include the application of the expansive grouts. The usage

of appropriate corrosion inhibitors of the proper concentration will be also thoroughly

considered to facilitate the effective research.

Since the corrosion of reinforcement is one of the most important causes of the inadequate

performance of the reinforced concrete stnictures, great attention will be provided to the

effective monitoring of this process in FRP wrapped columns. Various monitoring techniques

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have been discussed and acknowledged in this literature review. These techniques are more

or less advantageous depending if used to monitor corrosion in the laboratory or in the field

environment. Half-cell potential mapping can yield good laboratory results in cases of pitting

corrosion on structures with uncomplicated reinforcement layouts. However, this technique is

mostly used to i d e n w the existence of corrosion rather than quantity. It gives little

information regarding the severity of a corrosion process. Electrical resistance as well as the

electrochemical noise method have shown satisfactory laboratory performance in the case of

unifôrm corrosion, however, in the case of pitting corrosion, results can be rnisleading.

Linear polarisation method has a good record of being used in the field. However, iinear

polarisation method detects the instantaneous corrosion rate, which can change with

temperature and relative humidity. To address the mentioned advantages and to generate

highly reliable monitoring results the half-ce11 potential mapping and the linear polarisation

rnethods will be used in the current research.

The monitoring of the lateral expansion of columns due to corrosion of reinforcing steel will

be conducted using mechanical collars in conjunction with the effective application of the

fibre optic stnictural sensing technology. The unique benefits associated with fibre optic

sensors include immunity to electromagnetic fiequency interference, small dimensions and

light weight, low disturbance to the structure, capability of intermittent readings with

reconnection between readings, long-tem stability, and corrosion resistance. Thus, the usage

of fibre optic sensors will insure the high monitoring standards in the investigation of the

FRP repaired columns.

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CHAPTER 3. EXPERIMENTAL PROGRAM

This work is part of a larger study, initiated by Lee (1998) and continued by Khajehpour

(2001), involving the development of a repair system consisting of advanced composite

materials for rehabilitation and remote monitoring of corrosion-darnaged reinforced concrete

columns. A detailed laboratory testing plan for a total of thirty-one columns in the ove rd

study is outlined in Table 3.1.

Specific objectives of this experimental work include:

1. Establishing an optirnai laboratory procedure for accelerating corrosion activity.

2. Monitoring naturai corrosion behaviour in reinforced concrete columns.

3. Long-term monitoring of the corrosion process in repaired columns.

4. Obtaining the necessary data to compare the corrosion process in repaired and non-

repaired reinforced concrete columns.

3.1 Laboratory Test Plan

The previous laboratory studies conducted by Lee (1998) and Khajehpour (2001) consisted

of casting twenty-five coluwi specimens, and conducting various experiments on them,

which are discussed in the earlier theses.

This experimental study consisted of:

casting 6 new column specimens identical in form to earlier specimens (305 mm

diameter, 10 16 mm height), as detailed in Section 3.2.1.

subjecting 10 column specimens to accelerated corrosion regime (5 newly cast columns,

3 specimens cast by Khajehpour (200 1) and 2 repaired columns)

mod-g the accelerated corrosion regirne to maintain the consistency of the degree of

damage caused by corrosion process in al1 new corroding columns

m o d e i n g the commercial multi-element probe for corrosion monitoring

monitoring corrosion in 5 column specimens and one pnsm

repairing 4 coliimns with carbon fibre reinforced polyrners

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Corroded-Tested Corroded-Repaired-Tested

Corrodcd-Rcpaired- Accelerated Corrodcd-Repaircd-Natural

P Mdti-Element Probe MP Modified Multi Element Probe li< Expansion Grout and Corrosion Inhibitor - High Darnagc ** Specimen trcatcd with corrosion inhibitor should not be subjected to accelerated corrosion after repair.

Table 3.1. Laboratory Testing Plan

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3.1.1 Test Regimes

Specimens summarized in Table 3.1, are compared by test regimes (horizontally) and by

series (vertically). There are seven different test regimes- The main purpose of the first three

regimes is to assess the structural performance of corroded specimens confined with CFRP

wraps with the performance of unconti~ned column specimens. First row (control) represents

specimens, which afier casting were tested to failure in compression in order to evaluate the

capacity, strength and ductility of non-corroded spirally reinforced RC columns. Second test

regirne, designated corroded-tested, corresponds to the column specimens that are subjected

to an accelerated corrosion, as described in Section 3.4.1. until they reach targeted Ievel of

damage (moderate or hi&). Moderate damage is consigned to 6.5% of steel loss, while hi&

damage is assigned to 13% of steel loss. Afier reaching the targeted level of damage,

specirnens are to be tested to failure in corr~pressien to compare the capacity. ductility and

strength of corroded unconfined col~mns with the performance of control specimens. The

third test regime is denoted corroded-repaired-rested. Afier being corroded to a targeted

leveI of darnage, colurnn specimens from this row are to be wrapped with CFRP sheets prior

to structural testing. The repair procedure is discussed in details in Section 3.4.3. The

structura1 performance of corroded confined columns is to be compared with the performance

of corroded unconfined and control column specimens.

TweIve specimens assigned to the above-described test regimes and shown in shaded cells of

the Table 3.1 have already been structurally tested and results are described in earlier theses

(Lee, 1998; Khajehpour, 200 1). Remaining specimens are currently subjected to accelerated

corrosion and will be repaired and tested afier they will reach targeted level of darnage, For

that reason, this thesis is concentrating only on corrosion monitoring rather then structural

performance of the columns.

The prime purpose of the next two rows of specirnens is post repair corrosion monitoring.

Specimens subjected to the test regime denoted corroded-repaired-accelerated (corrosion),

are corroded to a targeted level of damage (moderate or high), repaired with CFRP wraps and

subjected to post-repair induced corrosion in order to evaluate the amount of expansion and

the rate of steel loss under accelerated corrosion. and to compare the performance of

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specimens before and after repair. Column specimens assigned corroded-repaired-natural

(corrosion) test regime are rneant for long term monitoring to assess the performance of

CFRP wrapped column specimens subjected to "natural corrosion", as specifically deçled

for the purpose of this study. The rate of steel loss and the amount of expansion is compared

to that before repair. Natural corrosion was achieved by cyclic variation of wetting in 3%

NaCl solution and dryïng in laboratory air (1 day wetting and 2.5 days drying) without

applying an electrical potential. Natutal corrosion was monitored using multi element probe,

a commercial device for corrosion monitoring described in Section 3.2.2.

Specimens in the next row (natural corrosion) are subjected to natural corrosion regime

since the time of casting. These specimens were also cast with multi-element probe for

corrosion monitoring- The purpose of this test regime is to establish natural corrosion rate

and to evaluate the performance of multi element probe. The 1 s t row, named natural

corrosion-moisture barrier consists of one column, which was cast with modified rnulti

elernent probe discussed in detail in Section 3.2.2.2. Since the time of casting, thîs column is

subjected to naturd corrosion regime. It will be repaired with a membrane, which replicates

the moisture barrier effect of the CFRP wrap without the mechanical restraining effect.

3.1.2 Families of Column Specimens

Prirnary variables of the test plan (Table 3-1) are organized in columns for the various

families of specimens. The main purpose of the pilor series was to establish an acceptable

accelerated corrosion regime. Furthermore, the repeatabiIity of structural test results was

evaluated. The function of the nutural damage series was to establish natural corrosion rate

and to evaluate performance of the commercial and modified multi element probes described

in Section 3.2.2. Specimens assigned to the moderate damage series are to be subjected to an

accelerated corrosion as discussed in Section 3.4.1 until they reach a moderate level of

damage (estimated as 6.5% of steel loss). Consequently, specimens fkom the high damage

series are supposed to reach high level of damage (estimated as 13% of steel loss) as a result

of an accelerated corrosion.

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As opposed to the previous three families of columns, which corresponded to the level of

damage, the next three characterize different repair techniques. After being corroded,

specimens fiom the expansive grout series are to be repaired using expansive grout. This

kind of repair involves the removal of delaminated concrete. In order to make this procedure

easier, columns should be subjected to an accelerated corrosion until they reach a high level

of damage (13% steel 1oss)- Afier removal of concrete cover and application of expansive

grout, colurnn shoüld be wrapped with two layers of CFRP sheet. Accordingly, since the

repair of colurnn fiom corrosion inhibitor series involves the removd of delarninated

concrete, this coIumn should be corroded to high level of darnage (13% steel loss). M e r

removal of cover and application of penetrating corrosion inhibitor. column should be

confined with two layers of CFRP wrap. These repair techniques are then compared to the

approach of wrapping column without "fixing" it first. Colurnn specimens fiom one Zayer

repair series are corroded until they reach a high level of darnage and repaired using only

one layer of CFRP wrap in order to evaluate the effect of number of CFRP layers as far as

confinement is concerned. Furthemore, the amount of expansion and the rate of steel loss of

one and two layer wrapped columns are compared.

Individual column specirnens f?om Table 3.1 are discussed in the remainder of this section.

Table 3.2 surnmarizes the time of casting, beginnuig and end of accelerated corrosion as well

as variations of wetting and drying cycles in attempt of promoting corrosion process; and

tirne of repair of individual column specimens including:

2 and 4 fiom pilot series cast by Lee (1998), the long term monitoring of which has been

continued as a part of the current study;

SI-SI1 cast by Khajehpour (2001) and remained for monitoring as a part of this

experimental study ;

5 12-5 17 cast and monitored as a part of the current study.

Beginning of macro-ceIl measurements and linear polarkation (LP) testing, discussed in

detail in Section 3.4.2, are also presented in Table 3.2.

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Specimen Cast Acc. Corrosion Repair Macm-Cell LP CyclesofWetthgandDrying 2 JuVAug-96 No No 12-Dec-97 11 -Jun-99 Wrapped in burlap and plastic 17-Dec-96

Wet/drv 2,511 30-Am--98

1 22-Dec-99 - present S2 24-Apr-98 10-Sept48 - 8-Jul-99 1 -Dec-99 No No

22-Dec-99 - present S4 1-May-98 10-Sept-98 - 1-Jul-99 1-Dec-99 No No

~ d f tiry/wet 2 . ~ 1 11 -srp-ga WeVdry 2.511 7-Dec-98 Half drylwd 2,511 1 1 -Sep48 Wet/drv 2.5/1 7-Dec-98 Hal f dry/w et 2.5/ 1 1 1 -Sep-98

Half dry1wd 2 3 1 1 1 -Sep-9E Wetldrv 2.91 7-Dec-98

1 S7 1 10 Jul-98 1 22-Dec-99 - presmt 1 No 1 No 1 IWeVdry 2.511 22-Dec-95 S8 S9

SI0

S l l 512

1 517 11 l -NOV-991 22-Dec-99 - present 1 No 1 No 1 lwe~dry 2.5/1 22-~ec-991

J 13 514 J 15 J 16

Table 3.2. History of Column Specimms Treatrnent

10-Jul-98 15-Jul-98 15-Jul-98

3-Dec-98 10-Nov-99 1 1 -Nov-99 Il-Nov-99 10-Nov-99 1 1 -Nov-99

22-Dec-99 - présent 22-Dec-99 - present

10-Sept-98 - 18-Dec-98

No No

22-Dec-99 - present 22-Dec-99 - present 22-Dec-99 - present 22-Dec-99 - present

No No

1 -Dec-99

No No No No No No

No Na

18-May-99

7-Sep-99 29-Dec-99

No No No No

,

18-Aug-98

12-Jan-99 22-Dec-99

Wetldry 2.50 22-Dec-99 Wet/âry 2.511 22-Dec-99 Wetldry 2 .W 22-Dec-99 Wetldry 2.511 22-Dec-99

WeVdry 2.5/1 22-Dec-99 Wet/dry 2,511 22-Dec-99 Wetldry 2.511 16-Jul-98 Half ârylwet 2,511 1 1 -Sv-98 WeUdry 2,511 7-Dec-98 Weüdry 2.511 12-Jan-99 WeUdry 2,511 22-Dec-99

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3.1.2.1 Pilot Series (2,4)

Column specimens fiom this series were cast, rnonitored, repaired and tested by Lee (1 998)

and Khajehpour (200 l), and discussed in greater detail in their theses.

Two coliimns were left for long-tenn natural corrosion monitoring. These columns, denoted

column 2 and column 4, were cast in July 1996 (Table 3.2). Column 2, subjected to naturaz

corrosion testing was under natural corrosion (i.e. no applied electrical potential) since the

thne of casting. Until May 1998 it was covered with wet budap and plastic to achieve 100%

relative humidity as shown in Table 3.2. However, it was f o w d more efficient, in t ems of

promohng corrosion, to use cyclic wetting and drying (lday wetting in 3% NaCl solution and

2.5 days drying in laboratory air). This regime was then used for al1 other column specimens

that required natural corrosion testing.

Column 4, assigned corroded-repaired-namal test regime was under accelerated corrosion

for 343 days until it reached an estimated steel Ioss of 7.8% by mass and a circumferentid

expansion of 0.179% (Lee, 1998). Then it was repaired with two layers of CFW sheets and

since has been subjected to a natural corrosion cycles of 1 day wetting in 3% NaCl solution

and 2.5 days drying in laboratory air.

Column specimens 2 and 4 were cast without a multi-elernent probe. Nevertheless, linear

polarization tests were conducted using the procedure outlined in Section 3.4.2.1. Based on

the results of corrosion monitoring, the performance of naturally corroding column 2 was

compared to the performance of corroded and repaired col- 4.

3.1.2.2 Natural Damage Series (S11, J12)

This series consists of two columns, denoted SI 1 and J12, which undergo natural corrosion

since the tirne of casting. Column S11 was cast in December 1998 with multi-element probe

for corrosion monitoring in order to evaluate the long-term stability of the probe in the

aggressive environment provided by cyclic variation of wetting in 3%NaCl solution and

drymg in laboratory air. Another purpose of this column was to establish a natural corrosion

rate. Column 512 allocated to nuîural corrosion-rnoisture barrier test regime was cast in

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November 1999. It contains a modified multi-element probe for corrosion monitoring

described in Section 3.2.2.2. Column 512 is currently monitored under natural corrosion

regime. M e r the corrosion process is active and stable, column 512 will be wrapped with a

membrane to inhibit moisture penetration into the column and to compare its performance

with carbon fibre reinforced polymer wraps.

3.1.2.3 Moderate Damage Series (SI, S10)

The moderate damage series consists of four colunins that underwent accelerated corrosion

regime until they reached a targeted steel loss of 6.5 %. Two of these columns (S3 and S5)

were tested by Khajehpour (ZOO 1) and resdts are discussed in his thesis. The two remaining

columns, denoted S 1 and S 10, are discussed in this section.

Column S1 subjected to corroded-repaired-accelerated (corrosion) test regkne was cast in

April 1998. It was under an accelerated corrosion for 105 days until it reached a steel loss of

6.75% and circumferential expansion of 0.175% (Khajehpour, 2001). It was repaired with

two Iayers of CFRP sheet in Januafy 1999, after which it took a year for the corrosion

activity to stabilize before it was subjected to accelerated corrosion testing again in order to

evaluate the performance of CFRP wrap under these conditions and to compare it with

performance of other columns subjected to corroded-repaired-accelerated (corrosion) test

regime (see Table 3.1).

Column SI0 subjected to the corroded-repaired-natural (corrosion) test regime was cast in

July 1998 with multi element probe for corrosion monitoring. It was under an accelerated

corrosion for 99 days until it reached a steel loss of 6.93% and circumferential expansion of

0.248% (Khajehpour, 2001). It took about a year for corrosion activity to stabilize, d e r

which column S10 was repaired with two Iayers of CFRP wrap. It is currently subjected to

wetldry cycles without applied potential in order to evaluate the effect of the CFRP wrap on

post repair natural corrosion and to compare its performance with other specimens

undergoing corroded-repaired-natural test regime (see Table 3.1).

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3.1.2.4 Eigh Damage Series (S7-S9,J14)

The high damage senes consists of four columns. Three of which, denoted S7, S8 and S9,

were cast in July 1998 by Khajehpour (200 l), while column J14 was cast in November 1999

as a part of this research program (Table 3.2). All four columns are currently subjected to

accelerated corrosion until they reach a targeted steel loss of 13%.

After column S7, assigned to the cowoded-tested regime, will reach a steel loss of 13%, it

will be tested to failure in compression and its strength and ductility will be compared to that

of columns with different levels of damage subjected to the same testing regime (see Table

3 -1). To evaluate the extent of damage achieved by accelerated corrosion, the performance of

column S7 will also be compared to the performance of control specimens.

After column specimen S8, allocated to the cowoded-repaired-tested regime, will reach a

steel loss of 13%, it will be repaired with two layers of CFRP wrap and tested to failure in

compression. The performance of column 58 will then be compared to the performance of

other column specimens subjected to the same testing procedure but with different levels of

damage and different types of repair. In order to assess the effect of confinement on the

stnictural performance of corroded specimens, the capacity, strength and ductility of column

S8 will also be compared to that of unconfined corroded columns subjected to corroded-

tested regirne (see Table 3.1).

Column specimen S9 subjected to corroded-repaired-accelerated (cornsion) test regime

will be repaired with two layers of CFRP wrap subject to achieving a high level of damage

(13% steel loss). After repair, it will be connected to accelerated corrosion regime again in

order to evaluate the performance of CFW wrap under M e r accelerated corrosion testing.

The amount of expansion and the rate of steel loss before and after repair will be compared to

evaluate the effect of wrap on specimen's corrosion activity. Furthemore, the performance

of the CFRP wrapped column under accelerated corrosion will be compared with the

performance of other columns subjected to corrosion-repaired-accelerafed testing regime to

evaluate the repeatability of results (see Table 3.1).

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Column specimen 514 wiil also be repaired with two layers of CFRP wraps after reaching a

targeted steel loss of 13%. This column, assigned to corroded-repaired-natd (corrosion)

regime was cast with a multi-element probe in order to evaluate natural corrosion activity in

CFRP wrapped column and to compare the natural corrosion rate before and after repair.

Moreover, post repair natural corrosion activity will be compared to that of specimens

repaired using expansive grout or penetrating corrosion inhibitor prior to wrapping.

3.1.2.5 Expansive Grout Series (J13,515,516)

The expansive grout series consists of three colurnns denoted 51 3-51 6, and J15, which were

cast in November 1999 as a part of the current experimental program. They are currently

subjected to an accelerated corrosion regime until they reach a high Level of darnage (target

steel loss of 13%). The reason for these columns to be highly damaged before repair is that

cover could be removed easily to be replaced with an expansive grout to induce active

confinement from the wrap. M e r that, these columns will be wrapped with 2 layers of CFRP

sheets.

Column 513 will be tested to failure in compression in order to evduate the effect of active

confinement by comparing it with the performance of passively confined columns and

unconfined specimens. Columns 515 that contains multi element probe for corrosion

m o n i t o ~ g and column 51 6 will remain for long-term corrosion mûnitoring in order to assess

the repair technique that involves replacing delamuiated concrete with an expansive grout by

comparing the corrosion activity of columns 515 and 51 6 with that of columns repaired only

with CFRP wraps subjected to the same testing regime (see Table 3.1).

3.1.2.6 Corrosion Inhibitor Series (J17)

The corrosion inhibitor series consists of one column that was cast in November 1999. It is

currently subjected to an accelerated corrosion regirne until it will reach a target steel loss of

13%. Concrete cover will be rernoved and penetrating corrosion inhibitor will be applied

before placement of a new concrete to reduce the rate of corrosion after repair. Then column

will be wrapped with two layers of CFRP sheet and will remain for long term monitoring.

The effect of penetrating corrosion inhibitor on corrosion activity will be assessed by

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comparing the natural corrosion rate of JI7 with that of other repaired specimens undergoing

natural corrosion testing (see Tabie 3- 1).

3.1.2.7 One Layer Repair Series (S2, S6)

The one layer repair series consists of two columns cast in May 1998, which underwent

accelerated corrosion- Column S2 reached 1 3 -52% steel loss and circumferential expansion

of 0.348% while column S6 reached 13.53% steel loss and circumferential expansion of

0.752% (Khajehpour, 1 999). M e r half a year of stabilizing they were repaired with one layer

of CFRP sheets. Colunin 6 is left for structural testing which will be conducted together with

specimens 57, S8 and 513 &er these columns will reach targeted steel loss in order to

maintain similar testing set up and thus minimize test variables.

M e r being repaired, column S2 is currently subjected to an accelerated corrosion regime in

order to evaluate the performance of one layer repair under induced corrosion regime and to

compare it with the performance of column specimens repaired with two layers of CFRP

wraps under induced corrosion (see Table 3.1).

3.1.2.8 Special Cases

There are two special specimens rnentioned in Table 3.1. First one, denoted column 1

belongs to the pilot series. The purpose of this specimen was to investigate cycles of wetting

and drying as an alternative accelerated corrosion technique. However, it was found that

corrosion could not be initiated rapidly enough without applying an electricd potential.

Column 1 discussed in detail in earlier thesis (Lee, 1998).

Column specimen designated 54 was connected to accelerated corrosion regime incorrectly,

i-e. rebar cage became a cathode (Khajehpour, 2001). After 50 days, specimen S4 did not

demonstrate any sign of corrosion as opposed to al1 other specimens connected to an

accelerated corrosion regime. The mistake was discovered and connections were corrected on

day 50. Four days later c o h m S4 demonstrated visual signs of corrosion activity and was

corroding rapidly thereafter. The average rate of steel loss for column S4 was four times of

that for al1 other corroding columns. Therefore, it was proposed to further investigate this

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accelerated corrosion technique in terms of becoming an alternative to the procedure used for

d l other columns of the overall research project described in Section 3.4.1, After reaching

44.16% of steel loss and stabilizing corrosion activity, column S4 was repaired with two

layers of CFRP wrap. To evaluate structural performance of this highly corroded specimen

confined with two layers of CFRP wrap, column S4 will be structurally tested together with

columns S 6 , S7, S8 and 513 to maintain similar testing set up and thus minimize test

variables,

3.2 Column Specimens

Specimens used in the overall study were designed to mode1 aging reinforced concrete bridge

columns. In order to simdate chloride contamination of the cover by de-icing salts, two types

of concrete were placed simultaneously in each specimen. To initiate corrosion rapidly, the

cover concrete was cast using chloride-contaminated concrete; while the inner core was cast

using essentidy the same concrete mix but without chlorides (Figure 3.1). To facilitate the

ingress of oxygen and moisture through the cover, a high water-to-cement ratio was used.

3.2.1 Column Specimen Geometry

A total of thirty-one large-scale reinforced concrete columns have been constructed to date.

The overall dimensions and cross-sectional details are shown in Figure 3.1. Al1 specimens

were 305 mm in diarneter and 1016 mm in height. The clear cover to the spiral steel was

20 mm. Each column was reinforced with six 15M longitudinal reinforced bars and D5 spiral

at 44-mm spacing, providing reinforcement ratios of 1.7% (by area) in the longitudinal

direction and 1 .l% @y volume) in the transverse direction. Longitudinal bars were pre-

drilled and tapped at one end in order to accommodate an electrical comection for

accelerated corrosion and macro-ceII measurements. For the pilot series, a seventh 15M bar

was placed longitudinally in the centre of the colurnn to serve as an intemal cathode for the

accelerated corrosion set up. For the rest of the specirnens, a perforated hollow 15-mm

diameter stainless steel pipe was used as an interna1 cathode in order to maintain oxygen

supply at the cathode and to accommodate the ingress of hydroxyl ions to the concrete.

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chloride-fiee concrete 6 - 15M bars

mm D5 spiral @ 44 mm

15M bar intemal cathode chIoride concrete

SECTION

ELEVATION

Figure 3-1. Geornetry of Concrete Column Specimen (Lee, 1998)

A 61 0 mm length of the column at nid-height constituted the effective test region. Ln order to

eliminate end effects, corrosion of steel outside the test region was prevented by painting the

upper and lower 203-mm long sections of the reinforcement cage with epoxy (CP 1047B

supplied by Niagara Paint Inc.) and using uncontamlliated concrete (Le. no chlorides) for

both the cover and the core.

3.2-2 Multi Element Probe W P )

To monitor the corrosion process, six coiumns were cast with embedded commercial multi-

eiement probes: two columns fiom the previous study, and four columns from this portion of

the experimentai study.

The multi element probe (MEP) for corrosion monitoring consisted of a carbon-steel working

electrode, a manganese-dioxide reference electrode and a stainless-steel counter electrode as

s h o w on Figure 3.2. Electrode connections are epoxy encapsulated in a PVC housing and

connected to a multi-wire monitoring cable (Corrosion Service Co. Ltd, 1998).

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1. - PVC Probe Houçing 2. - Stainless steel counter electrode 3. - Mn02 reference electrode 4. - Carbon steel working electrode 5. - Rebar connection wke 6. - Multiwire connection cabte

Figure 3.2. Commercial Multi Element Probe (Corrosion Service Co. Ltd, 1998)

The MEP has following specifications, as stated in the manufacturer's Literature (Corrosion

Service Co. Ltd, 1998):

Probe Dimensions: (L=l6Omm) x (H=100mm) x (W40m.m)

Weight: Probe head ~0.5 kg (2.5 kg c/w 1 Om cable)

Sensors: S tainless steel counter electrode

Carbon steel working electrode

ERE 20 MnOî reference electrode

Comection cable: 6c-Anixter SO HA- 1806 (10m = Typical).

The multi element probe enables measurement of:

* Corrosion potential of rebar, working and counter electrodes

Corrosion rate via linear polarization resistance

Concrete resistivity with qualitative indication of chlondehumidity ingress

Macro-ce11 corrosion curent.

For this experimental study, the nahirai corrosion rate (Le. corrosion rate in the absence of an

applied electrical potential) was estimated using the linear polarization resistance test (see

Section 3 .W. 1).

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3.2.2.1 Prism Specimen

To evaluate the performance of the MEP in tems of stabiIity of the ernbedded Mi102 half-

ce11 in the aggressive environment, one of the probes was embedded into a prism specimen.

The prisrn specimen was constnicted by Khajehpour (2002) and was 280 mm long, 165 mm

hi&, and 165 mm wide. The geometry of the prism is shown in Figure 3.3.

Lonrritudinal Section Cross-Section

Figure 3.3. Geometry of the Pnsm Specimen (Khajehpour, 2001)

The prism specimen was subjected to natural corrosion achieved by cyclic variation of

wetting and drying (2 days wet / 5 days dry) using a 3% NaC1 solution ponded on the top

surface of the specimen. Linear polarization was performed every two weeks at the end of

wetting cycle using four different electrode configurations as described in Table 3.3. The

performance of embedded Mn02 was compared by assessing the stability of its output versus

that of an externally mounted Cu/CuS04 half-ce11 illustrated in Figure 3 -3.

Table 3.3. Electrode Configurations used for LP tests of P r i m

Working Electrode

Probe

10M re-bar 1 stainless steel re-bar 1

Counter Electrode

Probe

Ab breviation

Mn-Pr-cPr

Mn- 1 OM-CS S Cu-Pr-cPr

CU- 1 OM-CS S

probe

Reference HaKCell

Mn02

Mn02

CdCuSO4

C ~ C U S O ~

probe

10M re-bar 1 stainless steel re-bar 1

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The regdar set up for h e a r polarization is illustrated in Figure 3.4. The results of linear

polarization tests performed on the prism can be found in Section 4.1.1.2.

Figure 3.4. Set up for LP Tests for Prism

3.2.2.2 Modified Multi-Element Probe (MMEP)

The working electrode of the multi element probe had clean, rust-free shiny appearance as

opposed to the regular rebars fiom the reinforcement cage. Thus, the concern associated with

the probe was that the probe working electrode was most likely made of a higher quality steel

than the rebar cage, therefore, it might be corroding slower. As a result, the multi element

probe was modified in order to compare linear polarization readings measured using the

carbon steel working electrode of the probe with the linear polarization readings using a

piece of black steel bar as the working electrode. A piece of regular 10M black steel re-bar

was attached so that the distance between the 10M working electrode and the Mn02 reference

half-cell would be equal to the distance between the embedded probe working electrode and

MnOz reference half-cell. The geometry of the probe with 10M working electrode is shown

on Figure 3.5. This modified multi-element probe (MMEP) was installed in columns 512,

514, J15, and 51 7. The installation of the probe in the specirnens is discussed in the next

section.

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2. - MnOz reference elec'trode 3- - Stainless steel counter electrode 4. - 1 OM rebar working elecîrode

Figure 3.5. Modifïed Multi-Element Probe

3.2.3 Column Specimens Fabrication

Specimens were cast in the inverted position. The reuiforcement cage and the intemal

cathode were fixed in predrilled holes in the formwork in order to have access to them fioni

the top of the specimen after casting. All columns were fabricated in 305-mm diameter

sonotubes. Figure 3.6 shows a photograph of six cylinder forms; one sonotube forrn has been

removed to allow the positioning of the steel cage to be observed.

Figure 3.6. Reinforcement Cage in the Formwork

64

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The probe was attached with plastic fasteners to the spiral, on the inner side of the

reîdorcing cage, between two longitudinai bars near mid-height of the column as

schematicdy illustrated in Figure 3.7. In order to prevent electrical continuity with the

spiral, a plastic chair was placed between the spiral and the probe. The Mn02 reference hdf-

cell cover was removed prior to casting. This cover was instdled by manufacturer in order to

protect the ha-cel l against my possible damage. The photo of the installed MEP is shown in

Figure 3.8.

P% , Spiral

Plastic chair

Figure 3.7. Alignment of Probe Details

bars

Figure 3.8. MEP Installation

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Columns were cast in the following sequence. The f i s t layer of chloride-fiee concrete was

placed to a depth of 203 mm and vibrated. In order to keep chloride-fiee and chloride

contaminated concrete separate in the test region, a thui aluminium sleeve (178 mm in

diameter, 4 mm thick) was then placed concentricaily inside the column. Two sleeves have

been used during casting: one was rounded for specimens without the modifïed probe, and

the shape of another similar sleeve was adjusted for the shape of the modified probe. Then

chlonde-fiee concrete was placed inside the sleeve, while chloride-contamuiated concrete

was placed outside the sleeve. The rate of placing was controlled to maintain approxirnately

the same depth inside and outside the sleeve. This procedure was used to place al1 of the

concrete inside the test region. After placing this concrete, the sleeve was removed. Prior to

the removal of the sleeve, both types of concrete were vibrated. Finally, the upper portion of

the sonotube (approximately 203 mm) was filled with chloride-fkee concrete, vibrated and

finished. In order to keep consistency, this procedure was identical while casting control

specimens with no chloride-contaminated concrete (Lee, 1 998; Khajehpour, 200 1).

3.3 Materials

Materials used in fabrication and repair of the specimens consisted of cernent, fine and coarse

aggregate, potable water, sodium chloride, admixtures (air entrainer Micro Air - 1, and water

reducer 25 - XL), reinforcing steel and carbon fibre reinforced plastic sheets.

3.3.1 Concrete Materials

Type 10 (CSA) Portland cernent supplied by St. Lawrence was used in all the concrete

mixes.

The fine aggregate used in the concrete mixes consisted of natural sand supplied by Dunlop

Sand Inc. The coarse aggregate used in the concrete mixes consisted of crushed h e s t o n e

supplied by Dufferin. The maximum particle size of the coarse aggregate used was nominally

10 mm.

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The water used in concrete mixes w s reguiar city water, which was clean and fiee of

deleterious substances in accordance witb OPSS 1302. A water-to-cernent ratio of 0.62 was

used for al1 concrete mixes.

The air-entraining admixture, Micro Air - 1, was used at a dose selected to achieve a target

air content of 7% for al1 mixes. Furtherrnore, a water reducer 25 - XL was used in al1 mixes

to reduce the amount of water required to achieve the desired workability. Master Builders

Inc. supplied both admixtures.

3.3.1.1 Mix Design

Table 3.4 illustrates the concrete mix design for the pilot series of colurnns- Table 3.5 shows

concrete mix designs for all other concrete specirnens.

Table 3.4. Concrete Mix Design for Pilot Series

Table 3.5. Concrete M x Design for Subsequent Series

Constituents (kg/m3) Cernent Water

Coarse Aggregate Fine Aggregate

Water Reducer (ml) Air Entrainer (ml)

NaCl Water-to-Cernent Ratio

Chloride Mix 300.0 186.0 882.7 869.6 700.0 80.0 9.9

Regular Mix 250.0 155.0 870.0 1040.0 630.0 80.0

- 0.62

Constituen ts (kg/m3) Cernent Water

Coarse Aggregate Fine Aggregate

Water Reducer (ml) Air Entrainer (ml)

NaCl 1

Water-to-Cernent Ratio 0.62 0.62 1

Chloride Mix 250.0 155.0 870.0 1 040 .O 630.0 80.0 8.25 0.62

-

Replar Mix 300.0 186.0 882.7 869.6 700.0 80.0

-

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This mix design was modined as needed to account for variations in the aggregate water

absorption. The total aggregate volume and the water content were adjusted in order to

maintain the same water-to-cernent ratio and the mUc volume.

3.3.1.2 Mixing and Casting Procedures

Prior to mixing, al1 materials were weighed and stored in covered buckets. In order to allow

complete dissolution, NaCl powder was added to the water of chloride-contamhated

concrete m.ïx 24 hours prior to casting. Both chloride-f?ee and chlonde-contaminated

concrete were mixed in the University of Toronto laboratory using the medium-size pan

mixer (GE 2036E3)- The slump and air-content for each mix were measured and results are

siimmarized in Table 3 -6.

In order to prevent penetration of cernent paste into the perforated stainless steel pipe (used

as a cathode), a transparent rubber tube was lubricated and inserted into the pipe prior to

casting. Then the pipe was placed into the predrilled hole at the centre of the forrnwork The

rubber tube was removed f i e r the concrete had hardened. Concrete was cured under wet

burlap and plastic sheets for seven days.

3.3.1.3 Compressive Strength Test Results

Twelve standard 100 x 200-mm cylinders were cast for each concrete mix for compressive

strength testing. Concrete was placed in two different layers. Each of the layers was rodded

fïfteen times before placing the next one. Cylinders were cured for twenty-four hours under

wet burlap and plastic. m e r that they were stored in buckets filled with water in the

Iaboratory until test.

The 28-day compressive strength test involved six specimens per concrete mix (three f?om

regdar concrete and three fiom chloride-contaminated concrete). The diameter of cylinders

was measured in five different places at the top and bottom by micrometer. The ends of al1

cylinder specimens were ground to a smooth surface prior to testing. The standard rate of

loading of 1.9 kN/s was used. The average value of 28-day compressive strength of each mix

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is presented in Table 3.6. The large discrepancy in concrete properties of different batches is

due to poor quality control during specimen fabrication and testing.

Table 3.6. Concrete Properties

Chloride 180

Batch

1

1 Chloride 210 6 1 9,12 1 Reguiar 1 220

Chloride 200

Specimens

Cl

- -

Regular 191 Chloride 191 Regular 220 Chloride 215 Regular 175 Chloride 185 Regular 175 Chloride 192 Regular 210 Chloride 210

Concrete

iype Remilar

8 9

10

11

-

18 Prisrn 1 Regular ( 1 60

Slump (mm)

65

C2 SI, S2

S3, S4

S5, S6

Air (%) 8.0

f c (at 28 days) W a )

25 .O

Regular Regular Chloride Regular Chloride Regular Chioride

180 250 240 205 230 254 228

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33.2 Steel Reinforcement

1SM longitudinal bars and DS spiral transverse reinforcement were used in each of the

twenty-four columns. Mechanical properties are summarized in Table 3.7. The stress-strain

curves for the reinforcement are illustrated in Figure 3.9.

Table 3.7. Mechanicd Properties of Steel Reinforcement (Lee, 1998)

. -

700 - 800 -. I 1

œ

100

a 1 O 0.05 O. 1 0.1 5 0.2 0.25

Strain (mmlmm)

(i) 15M Longitudinal Bars

Properfy Yield Strength, MPa

Ultimate Strength, MPa Modulus of Elasticity, MPa

0.00 0.Oi 0.02 0.03 0.04 0.05 0.08 0.07 O. 08

Strain (mmmim)

(ii) D5 Spiral Rcinforcmient

Figure 3.9. Stress-strain Characteristics of Reinforcing Steel (Lee, 1 998)

15M Bar 44 1 626

198 500

D5 Spiral 529 699

192 500

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3.3.3 Repair Materials

Carbon fibre reinforced polymers (CFRP) were used in this project for repair of the corroded

concrete specimens. Unidirectional carbon filaments oriented in the longitudinal direction

were Replark Type 30 sheets manufactured by Kasei Composites Ltd. (Japan) and supplied

by Mitsubishi Canada Ltd. Mechanical properties of the CFRP sheets as stated in the

manufacturer's product manual are summarized in Table 3 -8.

Table 3.8. Mechanical Properties of CFRP Sheets

Fibre Weight, g/mZ Fibre DensiS.,

Design Thickness, mm Tensile Strength, MPa Tensile Modulus, MPa

Elongation, %

Replark, Type 30

300

1.8 0.167 2 936

227 828 1 -4

Two more components were used in the repair of column specimens: primer and epoxy, both

provided by Mitsubishi Chernical Inc. Epoxy consisted of two components: L700S-main

agent BPA epoxy resin and L700S-modified aliphatic polyamine hardener.

3.4 Laboratory Test Procedures

Various laboratory tests were performed on col= specimens and the pnsm specimen.

Accelerated corrosion testing, natural corrosion monitoring as well as repair procedures are

discussed in following subsections.

3.4.1 Accelerated Corrosion Regime

For this experimental study, ten columns were subjected to accelerated corrosion testing, 2

repaired columns (SI and S2), 3 specimens cast by Khajehpour (2001) (S7 - S9), and 6 new-

cast columns (513 - 517) and. Ln order to be consistent with the previous study, the same

accelerated corrosion set up was used. To simulate field conditions, all column specimens

were subjected to wetting and drying cycles (1 day wetting in 3 % NaCl solution and 2.5

days drying in laboratory air) while under accelerated corrosion. Accelerated corrosion was

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created using a galvano-static approach. A fixed 12-V potentid was applied across the

reinforcing cage and the intemal cathode. The voltage was supplied by a power source with

fifteen independently regulated channels. A schematic drawing of the corrosion ce11 is

illustrated in Figure 3.10, where V, represents the applied voltage and Vi is the voltage drop

across the 1-i2 resistor.

1

Figure 3.10. Corrosion Cell

Figure 3.1 1 shows a photograph of corroding columns, the accelerated corrosion system and

power supply dong with the data acquisition system.

Figure 3.11. Accelerated Corrosion System

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The percentage of steel loss was estimated fiorn the measured value of the electric current by

measuring the voltage drop across 1-0 resistor as shown in Figure 3.10. Assuming uniform

corrosion and that al1 of the measured current is associated with the corrosion process, the

estimated amount of steel loss can be calculated using the equation:

where Aw - the incremental steel loss

W, - the atomic weight in gram (for reinforcing steel, 55.85 g/mol)

I - average current in Amperes

At - time increment in seconds

z - metal vaiency (the number of electrons transferred per atom,

z = 2 for ferrous metal)

F - Faraday's constant (96500 Amps s)

The voltage &op, Vi (Figure 3.10) was recorded by a personal computer every 6 hours on

average ushg a Heliotronic Data Acquisition System. This was converted to the current, 1,

and the total steel loss was determined fiom estimating the area under the corrosion current

versus t h e curve by integration:

While specimens were subjected to an accelerated corrosion testing, the circumferential

expansion was monitored in order to determine the extent of damage caused by corrosion.

Circumferential expansion was measured using mechanical expansion collars. The repaired

column S 1 was also instrumented with two fibre optic senson; one of them was placed inside

the wrap at mid-height, while the other one was mounted at the sarne height on top of the

CFRP wrap. A cornparison of readings taken by mechanical expansion collars and by fibre

optic sensors made for column S 1 is presented in Section 4.2.1.2.2.

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3-4.1.1 Mechanical Expansion Coiiar

A mechanical collar, shown in Figure 3.12, was made of a fl2-76-mm wide and 0.85-mm

thick stainless steel. The collar had a stainless steel head at each end. The gap between the

heads was held closed by two stainless steel springs, attached to the top and bottom of the

heads with stainless steel screws. The collar was wrapped acound the colurnn at the mid-

height. In the case of coIumn SI, the collar was placed 50 mm below the mid-height, in order

to avoid interference with the fibre optic sensor.

Figure 3.12. Mecfianical Expansion Collar

Circumferential expansion readings were taken twice a week immediately pnor to the

wetting period; the measurements were made using a micrometer (accurate to 0.01 mm) to

measure the change in the size of the gap between the heads, as iilustrated in Figure 3.13.

Figure 3-13. Expansion Measurements

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3.4.1.2 Fibre Optic Sensors

Fibre optic Bragg pting long-gage strain sensors were wrapped around column specirnen

Si at the mid-height (Khajehpour, 2001).

A one circumference of the column (0.974 rn) sensor was wrapped between the first and

second layer of the CFRP wrap. Prior to the repair procedure, the fibre optic sensor (FOS)

was secured on the d e r side of the CFRP sheet with adhesive tape. The distance between

twc adjacent pieces of tape was 0.15 m. Care was taken in order to prevent placing of the

tape on the &or of FOS. A six circderence of the column (2.875 m) sensor was wrapped

around the repaired column after allowing the epoxy to cure for 7 days. Adhesive tape and an

additional layer of epoxy were used to secure the sensor.

Demodulation system for long-gauge FOS consisted of a mechanical actuator, a motion

controller and a digital oscilloscope as shown in Figure 3.14. Readings were taken every two

weeks in order to compare results with the expansion measured by the mechanical collar. To

account for temperature and relative humidity, readings were also taken for the reference

FOS. A detailed procedure for taking readings using the equipment described above cm be

found in Appendk A.

Figure 3.14. Fibre Optic Sensor Equipment

75

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3.4.2 Natural Corrosion Regïme

NaturaI corrosion was achieved by subjecting column specimens to cyclic variation of

wetting in 3% NaCl solution and drying in air without any applied potential. As found Çom a

previous study by Lee (1998), the most favourable regirne was 1 day wetting and 2.5 days

drying*

Two different methods have been used for monitoring natural corrosion in column specimens

(as well as in the prisrn specimen): a linear polarization resistance technique and macro-ce11

rneasuements.

3.4.2.1 Linear Polarization Resistance Technique

Naturd corrosion in two columns fiom the pilot series (naturdly corroding column 2 and

corroded-repaired column 4, two columns fiom the low-damage senes (S 11 and 512) and one

repaired column fiom the moderate damage series (S10) were monitored using a linear

polarization resistance technique.

Column specimens fiom the pilot series were cast without a rnulti element probe, therefore

linear po larïzation tests were performed using:

Cu/CuS04 extemal reference half-ce11 located in 3% NaCl solution dong the

reinforcement cage as a reference electrode (see Figure 3.1 5 )

15M bar located at the centre of the column (cathode) as a counter electrode

One of the 15M reinfurcing bars (rebar) as a working electrode

The natural corrosion behaviour of column S 1 1 fkom the natural damage senes and S 10 fiom

the moderate damage series was monitored using an embedded multi-element probe. In order

to evaluate the long-term stability of the embedded MnOz reference haif-cell, readings were

also taken using an extemal Cu/CuS04 reference half-ce11 placed as shown in Figure 3.16.

Furthemore, LP readings were taken using one of the 15M bars from the reinforcing cage as

a working electrode (bar closest to the embedded MEP). Al1 three different electrode

configurations are summarized in Table 3.9.

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cathode

Figure 3.15. Experimental Setup for LP Testing

Table 3.9. Electrode Configurations used for LP tests of Column S 10 and SI 1

1 C U - ~ r - c ~ r 1 Cu/CuS04 1 probe I probe I

Abbreviation

Mn-Pr-cPr

1 Mn-15M-cPr 1 &O2 15M rebar probe 1

Column 512 from the naturai damage senes was cast with a modified multi-element probe

(MMEP), therefore, readings were taken using both the embedded probe working electrode

as w e l as the attached piece of 1 OM rebar as a working electrode.

Reference Half-CeH

- 0 2

Linear polarization tests were performed every week after 24 hours of wetting while the

column was subjected to the natural corrosion regime (i.e. no electricd potential was applied

when LP readings were made). n i e equipment for potentio-dynamic linear polarization tests

and the accompanying cornputer software (CMS 100) was supplied by Gamry Instruments.

The general procedure for linear polarization tests is described in Appendbc B.

Working: Electrode

probe

Counter Electrode

probe

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3-4.2.2 Macro-Cell Measurements

A macro-cell was created by installing a resistor between the intemal cathode and the

reinforcing steel. A 100042 resistor was installed on columns 2 and 4 fkom the pilot series,

512 fiom the natural damage series, as well as on column SI0 fkom the moderate damage

series. A 10042 resistor was installed on column SI1 and the pnsm specimen between the

working electrode and the bottom layer of reinforcing steel (cathode).

The voltage drop was measured across the resistor using a high impedance d i - m e t e r

acquisition system. The electncal current was calcdated fiom Ohm's law:

Where 1- electrical current, Amps

V- measured potential, Volts

R - electrical resistance, Ohms

3-43 Repair Procedure

In this experimental study, four column specimens were repaired using pre-impregnated

carbon fibre reinforced polymer sheets; column SI0 fiom the rnoderate damage series and

special column specimen S4 were repaired using two layers of CFRP while columns S 2 and

S6 from one layer repair series were repaired with one layer of CFRP sheet. Al1 columns

were instnunented with 0.974-m fibre optic sensors during repair.

A continuous layer of CFRP sheet was used; for one layer repair the length of the sheet was

one circumference of the column (0.96 m) with 0.153-m overlap, while the length of the

sheet for two layer repair was two column circumferences (1.92 m) with 0.153-m overlap.

Since the CFRP sheets were 0.254-m wide, it was necessary to use three sheets applied edge

to edge in order to cover the test region. Fibre optic sensors were installed in the middle layer

of the CFRP sheet as was described in Section 3.4.1.2. The repair procedure illustrated in

Figure 3.26 is s m a r i z e d betow.

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Figure 3.16. Repair Procedure (Lee, 1998)

Surface Preparation

1 Al1 fixtures and sensors were removed fiom the coliimn.

2. The column surface was sanded with a sanding d i x attached to a rotary Ml; a metal

brush was used to remove rust fkom the cracks.

3. The column sudace was washed with a wet mg to remove al1 dust and the surface was

then left to dry overnight.

Primer Application

4. A two-component primer supplied by Mitsubishi Chernical Inc. was mixed using a resin

to hardener ratio = 2: 1 by m a s

5. The primer was applied on the entire column surface using a hairless paint roller.

Care was taken to ensure that al1 voids are filled.

6. The colurnn was left to dry overnight.

CFRP Wraminq

7. The required length of CFRP sheets was cut (1.1 13 m for one-layer repair, and 2.073 m

for two-layer repair.

8. The epoxy was prepared by mixing resin and hardener in the proportion 2: 1 by mass.

9. The first layer of epoxy was applied on the concrete surface using a hairless paint roller.

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10. The CFRP sheet was applied around one circumference, pressing firmly with a rag in

order to remove air bubbles and insure good bond between concrete and CFRP wrap.

11. The protective layer of paper was removed fiom the CFRP wrap. In the case of the two-

layer repair an overcoat was applied on the first layer to serve as an undercoat for a

second layer.

12. Upon installation of al1 CFRP sheets, an additional layer of epoxy was applied to provide

some protection to the wrap.

13. The wrapped column was left to cure for 7 days, as suggested by manufacturer.

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CILAPTER 4. DISCUSSION OF EXPERIMENTAL RESULTS

The results fiom the laboratory experiments are presented and discussed in this chapter. A

cornparison is made between these results and the results obtained fiom the previous studies

conducted by Lee (1998) and Khajehpour (2001). The discussion of natural corrosion

monitoring in column specirnens is presented including issues associated with multi element

probe (MEP) for corrosion monitoring such as: stability of the MnOz half-cell, evaluated on

the basis of its performance in the pnsm specimen, as well as the performance of modified

MEP. The discussion of results of repaired and non-repaired specimens' response to an

accelerated corrosion testing is also provided.

4.1. Natural Corrosion Testing

In order to evaluate the natural corrosion activity and the effect of wrapping on the corrosion

process, linear polarization tests were performed on five column specimens as well as the

pnsm specimen. Macro-ce11 readings were also made for these specimens to estimate the

corrosion current, which is an indication of the corrosion activity.

4.1.1 Linear Polarization

Linear polarization tests were performed weekly immediately before the drying period on

column specimens 2 and 4 fiom the pilot series, on specimens SI1 and 512 from the natural

damage senes, and on specimen S 10 fkom the moderate damage series. Linear polarization

tests were also performed bi-weekly on the prism specimen. Details of the procedure used are

given in Appendix B. The results of these tests are discussed in this section.

4.1.1.1 Pilot Series (2,4)

Columns 2 and 4 fiom the pilot series were cast by Lee (1998). A detailed description of the

treatment of these columns is presented in Section 3.1.2.1. In order to have a better

understanding of the effect of the CFRP wrap on natural corrosion activity, linear

polarization tests were conducted once a week on both the naturally corroding specimen 2

and the corroded-repaired specimen 4. Both column spechens were cast without a multi-

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element probe; therefore LP tests were performed using the electrode configuration described

in Section 3.4.2.1.

This approach has a limitation Since the spirais electrically connect rebars from the steel

cage, the effective anodic area is not known. Considering this limitation, the following

obsewations can be made comparing the corrosion behaviour of the naturally corroding

column 2 and corroded - repaired specimen 4 (Figures 4.1,4.2). It should be noted that Iinear

polarization tests started 1.5 years after the repair of column 4, which corresponds to the time

zero on both graphs- A potential of -350 mV measured against the Cu/CuS04 hdf-cell

indicates a "high nsk" of corrosion activity.

time O - 1.5 years after repair of column 4 +4 - Corroded-RepairebNahraI -700 -, 1 8 t

O 100 200 300 400 500 600

Time, days

Figure 4.1. Corrosion Potential vs. T h e for Columns 2 and 4

As can be seen from Figure 4.1, the corrosion potential between the reinforcing steel and the

Cu/CuS04 reference half-ce11 shows that the corrosion is active in both specimens (threshold

for CulCuS04 is -350 mV).

The potential is more negative in repaired column 4, which is an indication of a higher risk of

corrosion. The most likely explanation for this behaviour would be a higher chlonde

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concentration around the reinforcing cage resulting fiom the applied potential used during

accelerated corrosion testing which would act to draw chlondes towards the steel cage

(anode).

+ 2 - Natural time O - 1.5 years aRer repair of column 4 -4 - Corroded-Repaired-Natural

, 1 I I I

O 100 200 300 400 500 600

Time, days

Figure 4.2. Corrosion Current vs. Time for Columns 2 and 4

Even though the corrosion potential is more negative in the repaired column, the corrosion

current is about two times higher in the naturally corroding colurnn 2 (Figure 4.2). One of the

reasons for this is a higher electrical resistivity of the corroded and repaired column 4

perhaps as a resuit of lower intemal moisture content.

4.1.1.2 Linear Polarization Specimen (Prism)

Linear polarization readings for the next three column specimens were taken using the rnulti

element probe (commercial device for corrosion monitoring described in Section 3 2.2). One

of the concems associated with the probe was the long-term stability of the embedded Mn02

reference half-ce11 in the aggressive environment created by wetting the specimen in 3%

NaCl solution. This concern rose fiom the fact that the Mn@ reference half-cell cannot be

monitored d e r it is cast in the specimen; therefore its performance was compared with the

extemal Cu/CuS04 reference half-ce11 which can be monitored on the regular basis. P r i m

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specimen was cast to evduate the stability of t h e probe. Linear polarization tests were made

every two weeks just before the drying cycle using four different eIectrode configurations as

descnbed in Seciion 3.2.2.1.

The approach of conducting LP readings usinig 10M rebar as a working electrode has a

limitation discussed in the previous section. Considering the limitation, the following

observations c m be made f?om the examinations of LP results as represented in Figures 4.3 - 4.6. It should be noted that time zero on dl graphs represents the time of casting. A potential

of -455 mV measure against the MnOz half-ceKi is equivalent to -350 rnV rneasured against

the Cu/CuS04 half-cell. These values indicate a "hi& risk" of corrosion activity.

O 1 O0 200 300 400 500 600 700 800 900 Time,:, days

-700 -

-800

Figure 4.3. Corrosion Potential vs. Time for Prism

Tirne O - casting June 1998 8 n 8 1 t t

As c m be seen from corrosion potential graph, it took about a year for readings taken using

the probe working electrode to show that corrosion is active, as opposed to readings taken

using 10M bar working electrode, which shoowed active corrosion within 40 days after

beginning the test. Such a behaviour provided s~ome proof of the concem outlined in Section

3.2.2.2, that the difference in the steel quality oof the probe working electrode and the 1 SM

rebar is believed to be a key factor for such behmviour.

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The potential between the probe working electrode and the embedded Mn02 reference half-

cell differed fiom the potential between the probe working electrode and the external

Cu/CuSOs reference half-cel by about lOOmV during the overail testing period. This

ciifference is expected due to dserent potentials of the standard haE-cell: and it indicates that

the embedded MnOz haif-ce11 is stable.

Tme O - casting June 1998 I

Time, days

Figure 4.4. Corrosion Current vs. Time for Pnsm using Probe

, Tme O - casting June 1998

O 100 200 300 400 500 600 700 800 900

Time, days

Figure 4.5. Corrosion Current vs. Tirne for Prism using 10M bar

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O 100 200 300 400 500 600 700 800 900

Time, days

Figure 4.6. Current Density vs, T h e for Pnsm

The corrosion current rneasured using the probe working electrode increased after about 400

days (Figure 4.4), which corresponds to the decrease in corrosion potential and indicates the

increase in corrosion activity

The corrosion current measured using the 10M rebar as a working electrode (Figure 4.5) is

higher than the current measured using probe working electrode due to the increased anodic

area of the rebar compared to the probe working electrode.

As can be seen f?om current density graph (Figure 4.6), afler about a year of natural

corrosion current density measured using probe working electrode is approximately the same

as current density measured using the 10M rebar working electrode. The smdl difference in

current density c m be attributed to the fact that effective anodic area of the 10M rebar

working electrode is an estimated value of the epoxy-fiee area of the bar.

4.1.1.3 NaturaI Damage Series

In order to evaluate the natural corrosion activity and to address the probe issues, two

specirnens fiom natural damage series were monitored: column SI1 and column 512. Column

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SI1 was cast in December 1998 by Khajehpour (2001). Specimen 512 was cast in November

1999 as a part of the curent study. A detailed description of the treatrnent of these two

colunin specimens is presented in Section 3.1.2.2.

4.1.1-3.1 Column SI1

The naturai corrosion behaviour of column SI1 was monitored fkom the t h e of casting using

an embedded rnulti-element probe (MEP) as described in Section 3.4.2.1. In order to assess

the long-term stability of the embedded Mn02 reference half-cell, readings were also taken

using extemai Cu/CuS04 reference half-cell, placed dong the steel cage, as a reference

electrode. Furthemore, LP readings were taken using one of the 15M bars fiom the

reinforcing cage as a working electrode (the rebar ciosest to the embedded MEP). All three

diEferent electrode configurations are described in Table 3.10,

The approach of conducting LP readings using 15M rebar as a working electrode has a

limitation discussed in Section 4.1.1.1. Considering the limitation, the following obseniations

can be made fiom the examinations of LP resdts as represented in Figures 4.7 - 4.9. It should

be noted that time zero on al1 graphs represents the t h e of casting.

-+- Mn-Pr-cPr Threshold -a- CwPr-cPr

CuCuS04 -350mV Mn02 4 5 5 mV a Mn-15m-cPr

J tirne O - castrng December 1998

-800 , t 1 1 1 8 1

O 100 200 300 400 500 600 700 800

T ime, days

Figure 4.7. Corrosion Potential vs. Time for Column S 1 1

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The potenîial between the probe working electrode and the MnOz reference half-ce11

indicated active corrosion approxuriately after 1 year (Figure 4.7). The data are consistent

with the results using the extemai Cu/CuS04 half-cell.

It took about a year for the probe working electrode to show the active corrosion state as

opposed to the 15M rebar working electrode which appeared to be actively corroding from

the first measurement made at 160 days. These results reflect back on the observation made

in the previous section for the difference in the qualit. of steel of the probe working electrode

and the 15M rebar.

The potential between the probe working electrode and the embedded MnOz reference half-

cell differed fiom the potential between the probe working electrode and the extemal

Cu/CuS04 reference half-cell by about 100 mV during the overall testing period. This

difference is expected, and it confirms the previous finding that the embedded MnOz

reference half-ceIl is stable in the aggressive environment created by wetting column in 3%

NaCl solution.

time O - casting December l998

O 100 200 300 400 500 600 700 800

Time, days

Figure 4.8. Corrosion Current vs. Time for Column S 1 1 using Probe

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time O - casting December 1998

L t Mn-:SM-cPr 0.00 * Ci, * i & I I

O 1 O0 200 300 400 500 600 700 800

Time, days

Figure 4.9. Corrosion Current vs, Tirne for CoIumn S 1 1 using 15M bar

As can be seen fiom Figure 4.8, the corrosion current measured using the probe working

electrode increased after about a year. The timing of the observed increase in current

coincides with the timing of the decrease in the measured corrosion potentiai of the probe.

Because of the increased effective anodic area of the rebar compared to the small working

electrode of the probe the corrosion current measured using the 15M-rebar was much higher

than the current measured using the probe working electrode (Figure 4.9).

4.1.1.3.2 Column 512

As can be seen from the results of pnsm and column S 11 monitoring, it took longer for the

probe working electrode to indicate active corrosion than for the 15M rebar working

elecbode. Therefore, another concern associated with the probe was the difference in steel

quality of the probe working electrode and the reinforcement cage. To address this concern,

coiumn JI2 fiom the natural darnage series was cast with a rnodified multi-element probe

(described in Section 3.2.2.2). A detailed treatment of the column is presented in

Section 3.1.2.2.

Linear polarkation readings were taken using both the probe working electrode (called

"probe" on the graphs) as well as attached piece of the 10M rebar as a working electrode

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(called "rebar" on the graphs). Figure 4.10 illustrates the potential vs. time graph. The

potential between the probe working-electrode and the reference half-ce11 as well as

the potentiai between the 10M rebar and the MnOz reference half-ce11 indicates that corrosion

is in active state.

O time O - casting Threshold November 1999 Mn@ -455 mV

-t probe ++ rebar

O 50 1 00 1 50 200 250 300 350 400

lime, days

Figure 4.10. Corrosion Potential vs. Time for Column J12

Figure 4.1 1 represents the cornparison of readings taken using multi element probe for al1 3

naturally corroding specimens (S 1 1, 51 2 and prism). Time zero on this graph represents the

tirne of commencement of LP tests for each specimen. Potential cuves are similar for al1

three specimens. The drop in potential occurred for colurnn SI 1 and pnsm specimen

indicated active corrosion. Since column 512 was monitored for 300 days only, the potential

drop carmot yet be codhned. Therefore, M e r monitoring is necessary.

Figure 4.12 represents the change of corrosion potential with t h e for d l 3 naturally

corroding specimens. Readings of corrosion potential represented on the graph were made

using rebar cage for column S 1 1, 10M rebar for pnsm specimen, and a piece of 10M rebar

mounted on the probe for column 112 as a working electrode. For all 3 specimens Mn02

reference haif-cell and probe counter electrode were used. Time zero on this graph represents

the tirne of the commencement of LP tests.

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Threshaid -100 1 Mn02 -455 mV

+SI1 probe -+-JI2 probe -+- Prism probe

O 100 200 300 400 500 600 700 8M3

Time, days

Figure 4.11. Corrosion Potential vs. Time for Naturally Corroding Specimens using Probe

O 1 00 200 300 4I30 500 600 700

Tirne, days

O

Figure 4.12. Corrosion Potential vs. Time for Naturally Corroding Specimens using Rebar

-1 -

-200 -

Threshoid + Sl 1 15M rebar cage Mn02 -455 mV -e- J i 2 piece of 10M rebar

-- - Prism 10M rebar

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Potentîd for SI1 and prism specimen indicated active corrosion since the beginning.

However, potentiai of 512 was less negative, thus indicated Iower corrosion activity.

Figure 4- 13 shows the cross section area of the column 512. An aluminium sleeve, adjusted

for the specîmens with modified MEP, was used during casting as described in Section 3.2.3.

During casting, chloride contaminated concrete was placed outside the sleeve, while chloride

fiee concrete was placed inside the sleeve. As a result, attached 10M rebar working electrode

happened to be located on the border of the two concrete mixes, while the re~orcement cage

is located in the chloride-contaminated area of the specimen. Therefore, the concentration of

chlorides around the 10M rebar working electrode is most likely lower compared to rebar

cage. This can result in lower corrosion activity of column JI2 according to the potential

readings taken using 1OM rebar as a working electrode.

Longitudinal bars

Figure 4.13. Cross Section of column J12 with Modified MEP

4.1.1.4 Moderate Damage Series (SPO)

Column SI0 fiom the moderate damage series was cast with an embedded MEP by

Khajehpour (2001). A detailed description of the specimen treatment is presented in

Section 3 -3.3.

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Column SlO was subjected to natural corrosion testing during the first month and LP tests

were conducted weekly. M e r that, the column was under accelerated corrosion for 99 days

during which LP tests could not be conducted- Upon achieving the moderate damage, the

specimen was discomected fiom the accelerated corrosion regime and LP readings

continued.

The corrosion behaviour of this column was monitored using the embedded (non-modified)

multi-element probe (MEP). LP tests were conducted before and after the specimen was

subjected to the accelerated corrosion testing. It was not possible to perform LP readings

during accelerated corrosion regime due to the high potential applied to the reinforcement

cage. The acceIerated corrosion regime appeared to have changed the electrochemical

environment of the column since the potential between the probe working electrode and the

MnOz reference half-ce11 became less negative after the accelerated corrosion was completed

(Figure 4.14), which indicates a decrease in corrosion activity. Therefore it was decided to

allow corrosion activity to stabilize prior to repairing the column.

To assess the stability of the embedded MnOz reference half-cell, readings were also taken

using extemal Cu/CuS04 reference half-cell. Furthemore, LP readings were taken using one

of the bars from the reinforcing cage as a working electrode. Al1 three electrode

configurations are described in TabIe 3.9.

The following observations can be made from the examinations of LP results obtained after

accelerated corrosion was completed as represented in Fiagres 4.14 - 4.16. It shouId be noted

that time zero on al1 graphs represents the time of casting.

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time O - casting July 1998

Threshold CuCuS04 -350mV

Mn02 -455 mV

O 1 00 200 300 400 500 600 2 0 0 800 900

Time, days

Figure 4.14. Corrosion Potential vs. Time for Column S 110

Prior to accelerated corrosion testing the potential of the proabe was between

-500 and -600 mV indicating an active state of corrosion. M e r t h e specimen was

disconnected fiom the accelerated corrosion regime the potential between- the probe working

electrode and the M n 0 2 reference half-cell indicates a passive state. The potential between

the 15M rebar working electrode and Mn02 reference half-ce11 however indicates that

corrosion is active (Figure 4.14). It is possible that the applied potemtial resulted in an

increase of chlonde concentration in the vicinity of the steel and ; a decrease in the

surrounding area of the probe.

M e r removing the applied potential, the working electrode of the probe became steadily

more electronegative with time such that after about 3 months the potential readings

indicated an active state of corrosion (i.e. potential is < -455 mV). Fuahier decreases in the

potentiai of the probe working electrode were observed during the next 3 months until a

stable value in the region of -700 mV was reached.

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The potential between the probe working electrode and the Cu/CuS04 reference half-cell was

100 mV less negative than that between the probe working electrode and the Mn02 reference

half-ce11 before repaÏr- This again confirms the long-term stability of the embedded MnOz

reference half-ce11 in the aggressive environment.

After the specimen was repaired with 2 Iayers of CFRP wrap the corrosion activiq increased,

however, the increase in corrosion activïty was temporary, and after about 2 months, the

corrosion potential graph showed a decreasing trend, which indicated a decrease in corrosion

activity. The following explanation for such behaviour can be provided. When specimen is

unwrapped it has access to moisime and oxygen fluctuation with wetldry cycles. When

column is wrapped, the arnount of moisture and oxygen get trapped inside, representing

temporarïly a higher than average supply for corrosion reaction. After a while corrosion

reaction depletes the moisture and oxygen and since wrapped column is insensitive to

wet/dry cycles, corrosion activity decreases.

The corrosion current had an increasing tendency right after repair (Figure 4.15). However,

d e r approximately 2 months, the corrosion current measured using the probe working

electrode had a decreasing trend, which supports the previous observation and can be

explained by the sealing effect of the wrap. lncrease in corrosion current measured using

probe working electrode corresponded to tirne of decrease in corrosion potential, thus

indicating increase in corrosion activity. Corrosion current measured using 15M bar working

electrode (Figure 4.16) is higher than current rneasured using the probe due to the Iarger

anodic area of the cage as compared to the probe working electrode.

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tirne O - casting July 1998

acc elerated

repaired r

I , natural corrosion

<

0.000 I 1 1 I 1 1' 1 1 I

O 1 00 200 300 400 500 600 700 800 9013

Time, days

Figure 4.15. Corrosion Current vs. Time for Column SI0 using Probe

Time, days

Figure 4.16. Corrosion Current vs. Time for Column S10 using 15M bar

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4.1.2 Macro-CeU Measurements

A macro-cell was created by installing a resistor between the intemal cathode and the

reinforcing steel on colurnns 2 and 4 from the pilot series, as weil as on columns S11 and JI2

fiom the low-damage series and on column SI0 fkom the moderate-damage series.

Furthemore, a resistor was installed on the prism specimen between the working electrode

and the bottom layer of reinforcing steel (cathode). Macro-ce11 measurements were

performed weekly just pnor to the drying period, Corrosion current can be calculated fiom

macro-ce11 measurements as discussed in Section 3.4.2.2.

4.1.2.1 Pilot Series (2 and 4)

Columns 2 and 4 from the pilot series were cast and tleated by Lee (1998). Initially column 2

was covered with wet burlap and plastic to achieve a hi& humidity environment, and after

that it was subjected to wetldry cycles in 3% NaCl solution in an attempt to promote

increased corrosion activity. Column 4 was subjected to accelerated corrosion, repaired and,

since then, it was subjected to cyclic wetting and drying. A detailed description of the

laboratory treatment of these columns is presented in Section 3.1.2.1. In order to have a

better understanding of the effect of CFRP wrap on the natural corrosion activity and to

compare results fi-orn lhear poiarization resistance techniques, macro-ce11 measurements

initiated by Khajehpour (2001) were continued during this experimental study. A resistor was

installed 1.5 years after casting on column 2, and 4 rnonths after repair on coiumn 4. Figure

4.17 illustrates the rnacro-ceil corrosion current vs. tirne. T h e zero on the graph represents 6

months after repair of column 4. It also corresponds to 1.5 years since casting of both

columns.

Gradua1 increase in current c m be observed for naturally corrodîng column 2, indicating

continuhg increase in corrosion rate due to the increased chloride content at the

resorcement cage. As can be seen fiom corrosion current graph for repaired column 4,

CFRP wrap prevents the corrosion rate from increasing.

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0.12

0.1 u E G 008 C

006 O

0134

O 02 Time O - 6 months + 2 - Natural

O O 100 200 300 400 500 600 700 800 900 1000

Time, days

Figure 4.17. Macro-CeLl Corrosion Current vs. Time for Columns 2 and 4

4.1.2.2 Linear Polarization Specimen (Prism)

A small pnsm specimen was constructed by Khajehpour (2001) in order to evaluate the long-

term performance of the probe as discussed in Section 3.2.2.1. A resistor was installed

between the working electrode and bottom layer of reuiforcing steel (cathode) of the prism

specimen. Figure 4.18 represents current vs. t h e graph. Time zero is the tirne of casting the

pnsm specimen. After 200 days, macro-ce11 corrosion current has a gradually increasing

trend, which indicates the continuous increase in corrosion activity of naturally corroding

prism specimen subjected to wetldry cycles without applied potential.

O 100 MO 200 4M 500 600 700 rn 900

Tirne, days

Figure 4.18. Macro-Ce11 Corrosion Current vs. Time for Pnsm Specimen

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4.1.2.3 Natural Damage Series

Macro-cell current of columns SI1 and 512 fiom the natural damage series was measured

using a resistor installed between the cathode and the reinforcement cage. To initiate macro-

cell corrosion current readings, resistor was installed 49 days d e r casting of colurnn 512 and

278 days after casting of column S 1 1. The results of macro-ce11 measurements are presented

on Figure 4.19.

From cornparison of macro-ce11 corrosion current of two natumlly corroding columns SI1

and 512, it can be detected that current of column S I 1 is about 10 times larger than current of

column 512. This merence is due to the differences in concrete strength for columns S 11

and 112. As summarized in Table 3.6, the concrete strength for column 512 is higher than

strength of column S 1 1. Higher strength generdl y correlates with lower permeability, and

since resistivity is inversely proportional to permeability, thus, resistivity of column 512 is

expected to be higher than the resistivity of column S 1 1. Therefore the dif5erences in macro-

ceU corrosion current of two naturally corroding specimens SI1 and J12 can be attributed to

the differences in concrete strength descnbed in Section 3.3.1 -3.

resistor installed -&-SI1

278 days afier -+-JI2 casting S1 7

resistor installed 49 days afier casting J I 2 ?

i- 1 1 I I r

O 100 2W 300 400 500 600 700 800

Time, days

Figure 1.19. Macro-CeIl Corrosion Current vs. Time for Column S 1 1 and JI2

4.1.2.4 Moderate Damage Series (S10)

Column SI0 fiom the moderate-damage series was cast by Khajehpour (2001). A detailed

description of the treatrnent of column S 10 is presented in Section 3.1.2.3. A resistor was

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instaIled 307 days after casting and 188 days before repair of column S10, as indicated in

Figure 4.20. The overall trend of the graph indicates that macro-ceIl corrosion current is

indifferent to the changes in the environment of the column (Le. corrosion current did not

change after repair with CFRP wrap).

0.25

307 days afier casting

Figure 4.20. Macro-Ce11 Corrosion Current vs. T h e for Colurnn S 10

0.05 -

0.m

4.1.3 Circumferential Expansion (S10)

-4- before repair +after repair

I 1 1 I 1

Circumferential expansion of column S10 fiom the moderate darnage series was measured

before and after repair using mechanical collar described in Section 3.4.1.1. Figure 4.21

shows the expansion readings taken twice a week immediately pnor to the wetting period.

307 407 507 607 707 807

Time, days

It c m be observed that column expands rapidly while cracking when subjected to an

acceIerated corrosion. As cracks started to accommodate corrosion products, the rate of

expansion reduced. Column S 10 continued to expand under natural corrosion regime without

applied potential. After repair wîth 2 Iayers of CFRP wrap, the rate of expansion reduced, as

indicated by the dopes of the graph 100 days before and 100 days &er repair. The decrease

in expansion rate was presumably due to restraining effect of the wrap.

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Natural Corrosion

* before repair

+ afier repair

O 100 200 300 400 500 600 700 800 900

Time, days

Figure 4.21. Expansion vs. Time for Column S 10

4.2 Accelerated Corrosion Testing

A total of ten column specimens were subjected to accelerated corrosion testing as discussed

in Section 3.4.1. Two of them (S 1 and S2) assigned to the corroded-repaired-accelerated

testing regime (see Table 3.1) were previously damaged and repaired specimens (Le.

specimens subjected to a second stage of accelerated corrosion a e r the damage fiom the

initial phase had been repaired by CFRP wraps). Eight columns: S7, S8, S9, 514 fYom the

high damage senes, J13,115, J16 fiorn the expansive grout senes, and 317 fiom the corrosion

inhibitor series were subjected to initial stage of accelerated corrosion in order to proceed

with assigned testing regimes (see Table 3.1).

4.2.1 Corroded-Repaired-Accelerated Test Regime (SI and S2)

Colurnns S1 and S2 were subjected to accelerated corrosion before they were repaired.

Column S1 had a steel loss of 6.75% and a circumferential expansion of 0.18% after the

applied potential was removed. As a result of accelerated corrosion, the electrochemical

environment of the column was probably changed and thus afler column S 1 was repaired

with two layers of CFRP wrap, it was left to stabilize for about a year. During this period the

column continued to expand and the total expansion at the time of post repair accelerated

corrosion initiation was 0.22%. Column S2 had a steel ioss of 13.52% and a circumferential

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expansion of 0.35% after the applied potential was removed. During stabilization period

column continued to expand so that the total amount of expansion at the time of repair with

one layer of CFRP wrap was 0.42%. After being repaired, colurnns S 1 and S2 were subjected

to accelerated corrosion again in order to assess the rate of steel loss and the amount of

expansion of CFRP wrapped column under accelerated corrosion by comparing it to that

before repair.

4.2.1.1 Steel Loss Rate

As c m be seen £kom the current vs. time graph (Figure 4.22), columns S1 and S2 initially

experienced a high current and thus hi& steel loss rate f i e r being repaired and subjected to

the same accelerated corrosion regime as before repair. Repaired columns initially experience

high current presumably because as a result of repair, some moisture and oxygen get trapped

inside the wrap and for some tirne it may represent an excessive supply for the corrosion

reaction. This hypothesis is supported by the fact that column S2 experienced higher initial

current than column S l perhaps because c o b S2 underwent wet/dry cycles up to the tirne

of repair as opposed to column S 1, which was lefi to dry out for a month before wrapping. It

is believed that after a while the corrosion reaction consumes moisture m d oxygen inside the

wrap and, since a wrapped column is less sensitive to wet/dry cycles than unwrapped, the

current drops significantly during the first month and continued to decrease as rust is formhg

on the reinforcement cage. As a result of repair, the corrosion current dropped significantly

after the initial increase.

As c m be seen fkom Table 4.1 and 4.2, after the columns were repaired with CFRP sheets,

the average rate of steel loss reduced for both columns.

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-- -- S i disconnected afier SI and S2 have the

same trend of

S2 disconnected afier reaching

Accelerated Corrosion

--

Accelerated Corrosion before Repair

1

Time, days

Figure 4.22. Current vs. Time for Repaired columns S1 and S2

Table 4.1. The Rate of Steel Loss for Repaired Column S 1

m S p e e ï Z e n 1 Time 1 Steel Loss 1 Steel Loss Rate 1 Sl

before repair

Table 4.2. The Rate of Steel Loss for Repaired Column S2

after repair To ta1

days 1 O5

Figure 4.23 supports the previous observation by showing that the gradient of the steel toss

320 425

curves alter repair is slightly less, than the gradient before repair.

O h

6.75

Steel Loss Rate %/day 0.0449 0.03 04 0.0753

%/day 0.0643

9.9 1 16.66

Steel Loss '!!.'O

13 -52 9.73 23.25

Specirnen S2

before repair after repair

Total

0.03 1 O 0.0953

Time days 301 320 62 1

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1 . -./ S2 disconnected after ,/

*' reaching 13.52% of steel loss ,,,--

SI disconnected after 4 reaching 6.75% of steel loss

,/I Accelerated Corrosion after Repair

Accelerated Corrosian - SI bef ore Repair - 52

I I I l I I 1

O 1 O0 200 300 400 500 600 700 800 900

Time, days;

Figure 4.23, Steel Loss vs. Time for Repaired columns S 1 and S2

4.2.1.2 Circumferential Expansion

Expansion readings were performed twice a week just before the wetting penod using a

mechanicd coilar (Section 3 -4.1.1 ). Column S 1 was alsor instnunented with two fibre optic

sensors to compare the readings taken by mechanical expansion collars and by fibre optic

sensors made for column S 1 (Section 3.4.1.2).

4.2.1.2.1 Mechanical Expansion Coilar

Figure 4.24 - 4.26 illustrate the change in expansion with time for columns S 1 and S 2 before

and after repair. It should be noted that time zero on al1 three graphs represents the time of

the commencement of accelerated corrosion (5 rnontths afler casting). The following

observation can be made fiom analysis of these figures.

The change of expansion with time for column SI befo-re repair is airnost identical to the

expansion of column S2 before repair (Figure 4.24). B-oth columns S1 and S2 expanded

rapidly during the first 50 days of accelerated corrosion, which corresponds to the time of

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extensive cracking. This expansion initiation is followed by a 70-day period of 1ittIe or no

expansion, because of the corrosion products accommodation by the cracks.

4

Beginning of Post Repair Accelerated Corrosion

SI disconnected - after reaching

6.75% of steel -

52 disconnected afkr reaching 13.52% of

- f steel loss +SI before repair -2- S2 before repair 6 -+-SI after repair = S2 aRer repair

O 1 O 0 200 300 400 500 600 700 800 900

Time, days

Figure 4.24. Expansion vs. Time for columns S 1 and S2 during Accelerated Corrosion

Before and Afier Repair

After column S1 was corroded to moderate damage (estimated at 6.75% of steeI loss),

accelerated corrosion was removed. Column S 1 was allowed to dry for a month pnor to its

repair with 2 layers of CFRP wrap. Specirnen S1 continued to expand slowly under the

natural corrosion regime (Figure 4.25).

After being subjected to the sarne accelerated corrosion regirne as before repair, column S 1

did not expand significantly during the first 80 days. By comparing corrosion current of

corroded repaired specimen subjected to post repair natural corrosion with corrosion current

of specimen subjected to accelerated corrosion after repair, it c m be approximated that 80

days of accelerated corrosion correspond to about 220 years of natural corrosion. However, it

should be taken into account that accelerated corrosion produces more steel loss and less

damage than natural corrosion. This dormant period is followed by a significant amount of

expansion. Perhaps this dormant period represents the existing cracks being filled with

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corrosion products. Because of the wrap no m e r cracks can be formed and m e r

corrosion results in expansion.

1 +- before repair + after repair

Accelerated Corrosion Natural Corrosion Mer Repair

O 1 00 200 300 400 500 600 700 800 900

Time, days

Figure 4.25. Expansion vs. Time for Repaired column S 1

Column specimen S2 was highly damaged (estimated at 13 -52% of steel loss) when the

accelerated corrosion was rernoved. It was expanding slowly under natural corrosion regime

(Figure 4.26). The sudden hcrease in the expansion at about 380 days can be associated with

sliding of the mechanical collar fiom its original position, since the slope of the curve before

and &ter this jump is the same. CoIumn 52 was subjected to wet/dry cycles up to the t h e of

repair. M e r being repaired with 1 layer of CFRP wrap, specirnen S2 was subjected to the

same accelerated corrosion regime as before repair. Slope of the expansion curve afier repair

is smaller than before repair. This suggests that CFRP wrap somewhat reduced the rate of

expansion presumably due to its restraining effect, however, the wrap does not stop the

expansion of the c o l m .

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1 -- before repair

O 1 O0 200 300 400 500 600 700 800 900 lime, days

Figure 4.26. Expansion vs. Tirne for Repaired colurnn S 1

Accelerated Corrosion after Repair

I 0.1 4

a Accelerated Corrosion rsr. ~1 before Repair

4.2.1.2.2 Fibre Optic Sensors

During the repair procedure, column S 1 was instmented with two fibre optic senson (FOS)

as discussed in Section 3.4.1.2. FOS readings were conducted every two weeks before the

wetting penod. Figure 4.27 illustrates the cornparison of expansion measured using the

mechanical collar with the expansion measured using fibre optic sensors. T h e zero on the

graph corresponds to the beginning of the post-repair accelerated corrosion regime (464 days

total). It should also be noted that 0% expansion on this graph corresponds to the actual

expansion of 0.22% prior to the column being subjected to the accelerated corrosion regime

after repair.

Natural Corrosion

As c m be seen fiom the graph, values of expansion measured using two FOS and a single

mechanical collar were similar during the first 80 days of accelerated corrosion testing.

Akhough good agreement was observed between readings taken using the colla and the

2.875 m long sensor (6 column circumferences, or 6 PD) up to 80 days, a large discrepancy

can be seen between these values thereafter. Since readings taken using 0.974 m long (IpD)

FOS showed sirnilar rates of expansion as the mechanical collar through the accelerated

corrosion-testing penod, it is suggested that the observed discrepancy is due to the 6 pD

I I l b L 0.0 -' I I

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sensor slip fkom its original position. As mentioned in Section 3.4.1.2, the 1pD FOS was

h e d on the inner side of the wrap as opposed to the 6 pD sensor, which was mounted on the

surface of CFRP wrap and secured with an additional layer of epoxy. However, this rnay not

be sufftcient to prevent the sensor fiom sliding when the column expands. Moreover, the

1 pD sensor may be considered to be better protected fiom any type of damage than the 6

pD sensor.

0.2

Beginning of Post-Repair Accelerated Corrosion

+i PiD -6 PiD 4 Collar

O 1 1 1

O 20 40 60 80 100 1 20 140 160

Time, days

Figure 4.27. Cornparison of Expansion Data for Coiumn S 1

4.2.2 High Damage, Expansive Grout, Corrosion Inhibitor Series

Eight newly cast column specimens S7-S9 and 513-517 were subjected to accelerated

corrosion and will be kept under these conditions until they achieve a hi& level of damage

with a target steel loss of 13.5%. Figures 4.28-4.33 represent the results of steel loss and

expansion monitoring for dl eight specimen subjected to accelerated corrosion. These results

are discussed in the rernainder of this section.

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for S7, S8. S9 reduced to 6V

+ S7. S8. S9 have the same trend of voltage

Applied Voitage for S7. S8. S9 reduced ta 3V -

Applied Voltage for ST, S8. S9--

reduced to 1 S V

1 50 200

Time, days

Figure 4.28. Applied Potential vs. Time for columns S7-S9

Applied Voltage for 57. S8. S9 reduced to 6V

Voltage SE. S9

!d tu 3V

S7. S8. S9 have similar trend of corrosion

current

Applied Voitage for S7. S8. S9

reduced to 1 S V

50 100 1 50 200 250

Time, days

Figure 4.29. Current vs. T h e for Columns S7-S9

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OTT

0-0

1'0

2'0

F s-O

3 E* O

P'O "a oc

s'O

9'0

L'O

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N p i i e d AppEed Voltage for 57, 58. S9 for S7. S8. S9 reduced to SV

reduced to 1.5V

O 50 100 1 50 200 250 300 350

Time, days

Figure 4.32. Steel Loss vs. Time for Columns S7-S9 and 513-517

O 2 4 6 8 10 12 14

Steel Loss, %

Figure 4.33. Expansion vs. Steel Loss for Columns S7-S9, JI3417

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Figure 4.31 shows how the expansion changes with time; Figure 4.32 illustrates the rate of

steel loss; Figure 4.33 represents the relationship between the expansion and steel Loss for dl

columns subjected to an accelerated corrosion testing.

Two different patterns can be observed fiom these graphs. The J-series columns (J13-JI 7)

expand gradually. The S-senes columns (S7-S9) initially showed the same expansion as the

J-senes specimens, however, after 50 days the expansion virtually stopped. Evidence of the

initiation of steel loss, such as rust-coloured salt solution and deposits on the surface of the

columns, were observed within a few days for column specimens S7-S9. It took longer to

observe mst leaching on columns 513-517. Withùi a month, it was evident that columns S7-

S9 were losing steel much faster than columns J13-J17, while expanding more slowly. The

reason for this is the fact that columns S7-S9 had a significantly higher water-to-cernent ratio

than J-series of columns because of the poor quality conkol during specimen fabrication.

A few modifications were made in order to accelerate the expansion and to reduce the steel

loss rate of three columo specirnens S7, S8, and S9 in order to be consistent with other

corroding specimens. Oxygen was introduced into the hollow cathode through a small

diameter plastic tube; this was done in an effort to increase the rate of corrosion by increasing

the availability of oxygen at the cathode. Also, an attempt was made to increase the

expansion by reducing the wetting time. In order to slow down the rate of steel loss, the

applied potential for column specimens S7, S8 and S9 was reduced £kst down to 6V, then

down to 3V and afler that down to 0.5V. These modifications as well as the time of their

irnplementations are summarized in Table 4.3, and discussed in detail in the following

subsections.

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Table 4.3. Accelerated Corrosion History for S7, S8, S9

S pecimen Change in Regime Accelerated Corrosion

Insert Bubbler in the Cathode Dry out the Cathode 1 day wet / 6 day dry

hsert Bubbler in the Cathode Dry out the Cathode

1 day wet / 2.5 day dry Switch Potential to 6V Switch Potential to 3V

Switch Potential to 1.5 V Accelerated Corrosion

Insert Bubbler in the Cathode Dry out the Cathode 1 day wet / 6 day dry

Insert Bubbler in the Cathode Dry out the Cathode

1 day wet / 2.5 day dry Switch Potential to 6V Switch Potential to 3V

Left dry for 14 days 1 day wet / 2.5 day dry

Switch Potential to 1.5 V Accelerated Corrosion 1 day wet / 6 day dry

1 day wet / 2-5 day dry Switch Potential to 6V Switch Potential to 3V

Switch Potentiai to 1.5 V

Date 22-Dec-99 13-Jan-O0 4-Feb-O0 7-Feb-O0 14-Feb-00 20-Feb-00 2 1 -Feb-00 24-Feb-00 I O-Mar-O0 24-May-00 22-Dec-99 22-Jan-O0 4-Feb-O0 7-Feb-O0 14-Feb-00 20-Feb-00 2 1-Feb-00 24-Feb-00 10-Mar-00 13 -Apr-O0 27-Apr-00 24-May-00 22-Dec-99 7-Feb-O0

21-Feb-00 24-Feb-00 t 0-Mar-00 24-May-00

4.2.2.1 Applied Potential

An initially constant 12V potential was applied to al1 ten specimens. However, due to the

unexpectedly high rate of steel loss of three column specimens (S7, S8 and S9) compared to

J-series specimens, it was decided to reduce the potential applied to these three c o l m s . A

plot of the applied voltage is s h o w on Figure 4.28. First, the applied potential was reduced

to 6V; however, the decrease in current (and thus the steel loss rate) was negligible.

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Therefore, it was decided to M e r reduce the voltage to 3V. Later, the voltage was brought

down to 1 . 3 7 in order to allow specimens to expand without losing a large amount of steel.

As can be seen fkom the current vs. h e graph for columns S7-S9 (Figure 4-29), the current

dropped fiom 0.35A to 0.20A on average as a result of decreasing applied potential fkom

12V to 6V. However, this effect was omly temporary, since the current tended to rise back up

such that after two weeks the current was 0.30A. The decision was made to M e r decrease

the potential applied to columns S7, S8, and S9 to 3V. As a resdt, the current initidy

dropped to 0.1 A and this t h e it did not rise significantly over time (0.013A increase over 75

days). The voltage was decreased to 1.5V (Iowest possible) in order to vimially stop the steel

loss and to allow specimens to expand without loshg a significant amount of steel. The

change in slope of the steel Ioss vs, time curves can be observed in Figure 4.32. As

illustrated in Figure 4.34, the relations3ip between corrosion current and applied potential is

not linear. Therefore there is an o p t i m m value of applied potential to cause higher current,

after which current might not increase significantly.

O 2 4 6 8 10 12 14

Applied Potential, V

Figure 4.34. Current vs. Applied Potentid for S7-S9

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4.2.2.2 Wetting and Drying Cycles

While Linder accelerated corrosion testing, ail specimens were subjected to cyclic wetting and

drying. The optimal wetting and drying time determined by Lee (1998) was found to be 1

day of wetring and 2.5 days of drying. An attempt was made to increase the expansion of

columns S7, S8 and S9, as shown in Table 4.3, by increasing the dryïng period to 6 days.

Furthemore, column S8 was left to dry for two weeks. However, no significant change in

expansion was observed.

Results fkorn a previous experimental study conducted by Khajehpour (2001) have shown

that pumping air through the perforated hollow cathode can increase the rate expansion. Air

was purnped through the hollow cathode of column S7 and S8; however, the increase in

expansion rate was only temporary.

4.3 Summary of Experimental Results

This summary compares and contrasts the experimental results and observations for the

columns involved in the research project. It also attempts to explain the observed corrosion

process, the similarities and differences in the columris' performance.

4.3.1 Natural Corrosion

As can be seen from corrosion potential vs. time (Figure 4.1, 4.3, 4.7, 4.10, and 4-14),

corrosion is in the active state for al1 column specimens and the prism. Measurements

performed using the probe incorporated in columns SlO, S1 1 and the prism, have indicated

that it takes about a year for the probe working electrode to show the active corrosion state as

opposed to the 15M rebar working electrode, which appeared to be actively corroding within

one month. This is most likely due to dBerences in steel quality used for fabrication of the

probe working electrode and reinforcement cage. In order to investigate this difference, a

modified probe, incorporating of the piece of 10M rebar as a working electrode, was installed

in column 512. Due to the lower chloride concentration around the 10M rebar working

electrode than around the reinforcement cage, the potential between the M n 9 reference half-

ce11 and the 10M rebar working electrode of column 512 is lower than potential between

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Mn02 reference half-ce11 and 15M rebar (reinforcement cage) working electrode of column

Sll (Figure 4-12)

The potential between the probe working electrode and embedded MnOz reference half-ceil

M e r e d fiom the potential between probe working electrode and extemal CuICuS04

reference half-ce11 by about lOOmV for columns S11, SI0 and the prism. This difference was

expected and indicates that the embedded MnOz reference half-ce11 is stable in aggressive

environment created by wetting the specimen in 3% NaCl solution.

M e r repair of column specimen S10, the rate of expansion decreased, as indicated in

Figure 4.21, presumably due to restraining effect of CFRP wrap.

4.3.2 Accelerated Corrosion

Columns SI and S2 experienced a high current thus hi& steel loss rate immediately after

repair (Figure 4.22). This was especially evident with column S2 because of its continued

wet/dry cycles up to the tirne of repair. Column S1 was left to dry for a month before

wrapping. As a result of repair, some moisture and oxygen was most likely trapped inside the

wmp and initially it represented an excessive supply for the corrosion reaction. Once the

oxygedmoisture was consumed in the corrosion reaction and since the impermeable wrap

out the column off from the effect of wetldry cycling, the current dropped significantly

during the fïrst month and continued to decrease as the rust was fomiing on the

reùiforcernent cage.

After repair of columns SI and S2 a dormant period of expansion can be observed under

induced corrosion regime (fïrst 100 days as indicated in Figure 4.24). M e r this period

columns continue to expand presumably because the top and the bottom of the c o l a are

not completely isolated fiom moisture and oxygen and corrosion process continues.

The alteration in the applied voltage of columns S7-S9, fiom 12V to 6V resulted in a

temporary decrease in the corrosion current (Figure 4.29). This decrease may be amibuted to

the polarkation effect. The M e r decrease in applied voltage from 6V to 3V resulted in a

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permanent decrease in the corrosion current. The effect of polarization is probably less

significant at lower range of electrical current.

The rate of steel loss was lower for the newly cast 513 - 517 column specimens as opposed to

the S7 - S9 specimens constructed by Khajehpour (2001) due to the better q d t y concrete as

a resdt of poor qudity control of the specimen fabrication.

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CHAPTER 5. CONCLUSIONS AND RECOMMENDATIONS

This is an ongoing project at the University of Toronto aimed at developing a "smart?' wrap

system for corrosion darnaged reinforced concrete columns.

In order to assess stnictural performance of corroded CFRF' confined columns, the previous

studies conducted by Lee (1998) and Khajehpour (2001) involved stnictural tests. The

developments on the earlier parts of this research project are surnrnarized below.

This part of the overall research project was concentrated mainly on corrosion monitoring in

wrapped columns, to evaluate post repair corrosion activity. Conclusions on this part of the

overall project are also provided in this chapter followed by recommendations.

5.1. Earlier Developments

1. Structural tests have shown loss of strength and considerable loss of ductility due to

corrosion.

2. Extensive-pitting corrosion occurs in spiral at overall steel loss on the order of 10%.

3. Wraps restore colurnn strength and ductility lost due to corrosion.

4. Wrapped columns subjected to considerable post-repair corrosion still outperform

control specimen.

5.2. Conclusions

1. CFRP wraps do not stop corrosion activity in the colunin.

2. Natural corrosion current sliphtly increases right after repair. This penod of higher

corrosion activity is temporary. Afier initial increase corrosion current becomes the

same as before repair or slightly less.

3. Column subjected to post repair natural corrosion regime (without applied potential)

expanded less than before repair.

4. Colurnns subjected to post repair accelerated corrosion (12V applied potential) did

not expand during first 80 days of accelerated corrosion. After this dormant period,

repaired columns expand gradually.

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5.3 Recommendations

1. Fuaher monitoring is necessary to have a better understanding of corrosion after

repair and to check a repeatability of results

2. In order to improve natural corrosion monitoring it is suggested to take macro-ce11

readings during both wet and dry cycles.

3. While conducting linear polarization tests with external CdCuS04 reference half-cell

it is recommended to place the half-ceii at different locations dong the column to

have more data.

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CHAPTER 6. REFERENCES

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Andrade, C. (1988). "Corrosion of Steel in Concrete". Corrosion of Steel in Concrete. Report of Technical Cornmittee 60-CSC RILEM, Edited by Schiessl, P. Chapman and Hall.

Ansari, F. (1997). ''Theory and Applications of Integrated Fibre Optic Sensors in Structures". Intelligent Civil Engineering Materials and Structures. ASCE. 28 pp.

Amp, H, Klinghoffer, 0, and Meietz, J. (1997). "Manganese Dioxide Reference Electrode for Use in Concrete". Corrosion of Reinforcernent in Concrete - Monitoring. Prevention and Rehabilitation. European Federation of Corrosion Publications No. 25. pp. 40-53.

ASTM C876-(1991). "Standard Test Methods for Half-Ce11 Potential of Uncoated Reinforcing Steel in Concrete".

ASTM G3 -89 (1 989, reapproved 1 994). "Standard Practice for Conventions Applicable to EIectrochemical Measurements in Cmrosion Testing".

Baker, A.F. (1986). "Potential Mapping Techniques". Serninar on Corrosion in Concrete - Monitoring-. Surveving-. and Control bv Cathodic Protection. London Press Centre, paper No. 3.

Bakker, R.F.M. (1988). "Initiation Penod". Corrosion of Steel in Concrete. Report of Technical Cornmittee 60-CSC RILEM, Edited by Schiessl, P, Chapman and Hall, New York. 27 PP-

Ballinger, C, Maeda, T, and Hoshijima, T. (1993). "Strengthening of Reinforced Concrete Chunneys, Columns and Beams with Carbon Fibre Reinforced Plastics". SP 138-15, ACI. pp. 223-248.

Ballinger, C.A. (1997). "Strengthening of Engineering Structures with Carbon Fibre Reinforced Plastics - an Overview of History and Current Worldwide Usage". 42nd International SAMPE Symposium, pp. 927-932.

Bentur, A, Diamond, S, and Berke, N.S. (1997). Steel Corrosion in Concrete. E&FN Spon, London.

Berke, N.S, and Weil, T.G. (1992) "World-Wide Review of Corrosion Inhibitors in Concreteyy. Advances in Concrete Technoloey, CANMET, Ottawa. pp. 124-140.

Bovankovich, J.C. (1986). "On-Line Electrochemical Techniques for Corrosion Engineering, Houston. pp. 3 05-3 1 0.

Corrosion M o n i t o ~ g - A Current View. Engineering". National Association of Corrosion

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Bradford S.A. (1993)- Corrosion Control. Van Nostrand Reînhold. New York.

Broomfield, J, P. (1997). Corrosion of Steel in Concrete (understanding, investigation and re~air). E & FN Spon.

Cameron, G.R, and Chiu, AS. (1986). c~Electrochemical Technique for Corrosion Inhibitor Study". Electrochemical Techniques for Corrosion Engineering. National Association of Corrosion Engineering, Houston. pp. 183-192.

Cercone, L, and KorfY J. (1 997). "Putting the Wraps on Quakes". Canadian Journal of Civil Engineering Vol. 67 No. 7. pp. 60-61.

Chandra, S , and Ohama, Y. (1994). Polyners in Concrete. CRC Press, Inc.

Chess, P, and Gronvold, F. (1996). Corrosion Investigation. A Guide to HaIf-ce11 Potentid Mapping. Thomas Telford Services LTD- London.

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Appendix A

Procedure for Taking Readings Using FOS Equipment

1. Motion ControiIer

To clear the signal press CLEAR, then REV; when see the red signal flash press

CLEAR and CLEAR.

Should see O on the screen of the Motion Controller

In order to have slow velocity tuni the handle VELOCITYall the way ccw.

2. Osciiioscope

Adjust to channel 1

There are 2 knobs on the upper right corner called REFERENCE and DIFFERENCE-

Adjust REFERENCE (horizontal solid line on the screen of the oscilloscope) to O.

Should be able to see it in the middle of the screen. Adjust DIFFERENCE (dotted

line) at 1 division below the solid line.

Adjust Volts/Division to 5, using little knob called VOLTS/DrVISION on top of the

bigger one on the left side of the oscilloscope (channel 1).

Adjust Time/Division to 0.5 s, using knob TIMEDIVlS..ON on the right second fiom

the top.

Check that apparatus at DC level (a button on the lower left).

Check that mode is normal (a button on the right side). If the mode is Normal, line is

moving on the screen).

Check source - channel 1

Check coupling - AC

3. Taking Readings

Oscilloscope:

Plug in mirror and reference (do not screw too much in the upper one)

SetDiFFERENCEon 10Volts

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Touch the sensor so it is fitted with the horizontal dotted line (between solid line in

the midde and second dotted line)

Set to AC mode (button on the lower left)

Using BIG VOLTS/DMSION knob set it to 50 mV

Motion Controller:

Press M D

Should be able to see the signal at about 2500 for reference

Once can see big pattern press FWD again to stop, Write down the value and press

REV. Get that big pattern again and write down the value. Take an average of the two

values-

If signal is off the screen (too large) instead of 50mV get to 0.1 V/div or 0.2 V/div

using; BIG VOLTS/DMSION knob.

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Appendix B

Procedure for Linear Polarization Tests

The hardware installed and set up by Gamry Instruments included voltmeter and ammeter. In

order to perform the linear polarization tests, the proper connections between the computer

and specimen were established. The general procedure for linear polarization tests is

described below.

The cables were comected to the electrodes

CMS 100 program was open.

The relevant data (output file name, area of the steel subjected to LP test, etc.) entered

into the dialog box titled "Polarization Resistance".

Tafel constants were entered according to the corrosion conditions: 0.052 VDec if

corrosion is passive, 0.026 VDec if corrosion is active. The threshold used for

Cu/CuS04 reference half-ce11 was -350mV, for MnOz reference half-cell was

45SmV.

Afier open circuit potential was measured, the working electrode was tested as the

potentio-stat polarized fiom -20mV below the initial open circuit potential and

increased in small steps to reach the final working electrode potential, which was

+20mV above the initiai open circuit potential.

While the CMSlOO program was running, electncai current was recorded for each

potential step and plot of log of current vs. potential was displayed.

Upon completion of polarization, data analyses were performed using CMSIOS

program, which run under CMSlOO and uses MS Excel program for drawing graphs

and fitting numerical curve.

The Line fit to the LP cuve was generated f?om least squares fit between -IOmV and

t 1 OmV with respect to initial open circuit potential.

The slope of the fitted line indicated the polarization resistance in Ohms cm2

Rp = AE/N

where dE - change in potential

AI- change in current density.