EPA/600/R-09/055 | June 2009 | www.epa.gov/ord
United States
Environmental Protectio
Agency
              Condition Assessment of Ferrous Water
              Transmission and Distribution Systems
              STATE OF TECHNOLOGY REVIEW REPORT
   Office of Research and Development
   National Risk Management Research Laboratory - Water Supply and Water Resources Division

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SEPA
EPA/600/R-09/055
    June 2009
                 State of Technology Review Report
                                  on
       Condition Assessment of Ferrous Water Transmission
                      and Distribution Systems
                                  by

                             James Thomson
                          Jason Consultants, LLC
                          Washington, B.C. 20006

                                 and

                               Lili Wang
                                Battelle
                           Columbus, OH 43201
                         Contract No. EP-C-05-057
                           Task Order No. 0062

                                  for

                             Michael Royer
                           Task Order Manager

                  Water Supply and Water Resources Division
                National Risk Management Research Laboratory
                     2890 Woodbridge Avenue (MS-104)
                            Edison, NJ 08837
                National Risk Management Research Laboratory
                     Office of Research and Development
                    U.S. Environmental Protection Agency
                          Cincinnati, OH 45268

                              June 8, 2009

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                                        DISCLAIMER
The U.S. Environmental Protection Agency, through its Office of Research and Development, funded and
managed, or partially funded and collaborated in, the research described herein under Task Order (TO)
0062 of Contract No. EP-C-05-057 to Battelle. It has been subjected to the Agency's peer and
administrative review and has been approved for publication. Any opinions expressed in this report are
those of the author (s) and do not necessarily reflect the views of the Agency, therefore, no official
endorsement should be inferred.  Any mention of trade names or commercial  products does not constitute
endorsement or recommendation for use. The quality of secondary data referenced in this document was
not independently evaluated by EPA and Battelle.

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                                         FOREWORD
The U.S. Environmental Protection Agency (EPA) is charged by Congress with protecting the Nation's
land, air, and water resources. Under a mandate of national environmental laws, the Agency strives to
formulate and implement actions leading to a compatible balance between human activities and the ability
of natural systems to support and nurture life. To meet this mandate, EPA's research program is
providing data and technical support for solving environmental problems today and building a science
knowledge base necessary to manage our ecological resources wisely, understand how pollutants affect
our health, and prevent or reduce environmental risks in the future.

The National Risk Management Research Laboratory (NRMRL) is the Agency's center for investigation
of technological and management approaches for preventing and reducing risks from pollution that
threaten human health and the environment.  The focus of the Laboratory's research program is on
methods and their cost-effectiveness for prevention and control of pollution to air, land, water, and
subsurface resources; protection of water quality in public water systems; remediation of contaminated
sites, sediments and groundwater; prevention and control of indoor air pollution; and restoration of
ecosystems.  NRMRL collaborates with both public and private sector partners to foster technologies that
reduce the cost of compliance and to anticipate emerging problems.  NRMRL's research provides
solutions to environmental problems by: developing and promoting technologies that protect and improve
the environment; advancing scientific and engineering information to support regulatory and policy
decisions; and providing the technical support and information transfer to ensure implementation of
environmental regulations and strategies at the national, state, and community levels.

This publication has been produced as part of the Laboratory's strategic long-term research plan.  It is
published and made available by EPA's Office of Research and Development to assist the user
community and to link researchers with their clients.
                                            Sally Gutierrez, Director
                                            National Risk Management Research Laboratory

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                                  ACKNOWLEDGEMENT
The authors wish to extend their sincere appreciation to John Black of Opus Consultants in Australia for
his review and input to this document.  The authors also would like to thank Frank Blaha of the Water
Research Foundation (formerly American Waterworks Association Research Foundation [AwwaRF]),
David Hughes of American Water, and Stewart Burn of the Commonwealth Scientific and Industrial
Research Organization (CSIRO), for providing written review comments. Our sincere appreciation also
extends to those who provided verbal review comments during the project's Technology Forum held on
September 9 and 10, 2008 at Edison, NJ. Both written and verbal comments have been incorporated into
this final document as appropriate.
                                              in

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                                      CONTENTS
DISCLAIMER	i
FOREWORD	ii
ACKNOWLEDGEMENT	iii
APPENDICES	vi
FIGURES	vi
TABLES	vi
ABBREVIATIONS AND ACRONYMS	vii
EXECUTIVE SUMMARY	ix

1.0  CHARACTERIZATION OF WATER NETWORK IN U.S	1
     1.1  Overview of U.S. Water Transmission and Distribution Network	1
     1.2  Types of Ferrous Pipes	2
            .2.1   Cast Iron Pipes	2
            .2.2   Ductile Iron Pipes	3
            .2.3   Steel Pipes	3
            .2.4   Summary of Ferrous Pipes	4
     1.3  Overview of Failure Modes of Ferrous Pipes	5
            .3.1   Corrosion- Internal and External	6
            .3.2   Mechanical Failures	12
     1.4  Main Break Occurrence Factors	14
     1.5  Causes of Failure and Indicators in Ferrous Pipes	14

2.0  STATE-OF-THE-ART CONDITION ASSESSMENT OF WATER MAINS	17
     2.1  Role in Relation to  Asset Management	17
     2.2  Condition Assessment	18
     2.3  Condition Assessment- Risk and Prioritization	19
          2.3.1   Consequences of Failure	19
          2.3.2   Likelihood of Failure - Key Indicators	20
          2.3.3   Likelihood of Failure- Secondary Indicators	23

3.0  TECHNOLOGIES FOR CONDITION ASSESSMENT	27
     3.1  Visual Investigations	27
          3.1.1   External Condition Inspection	27
          3.1.2   Internal Condition Inspection Using CCTV	27
     3.2  Pit Depth Measurements	28
     3.3  Destructive Testing	28
     3.4  Non-Destructive Testing	29
          3.4.1   Sonic/Seismic Technologies	29
          3.4.2   Guided Wave Ultrasonic Testing	30
          3.4.3   Electromagnetic Methods	30
          3.4.4   Radiographic Testing	31
     3.5  Environmental Testing	32
     3.6  Leakage Management	34
          3.6.1   Overview of Leak Management	34
          3.6.2   Leak Detection Technologies	34
     3.7  Summary of Inspection Methods and Applications	36
                                           IV

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4.0 APPROACHES TO CONDITION ASSESSMENT	39
     4.1   Condition Assessment Basics	39
     4.2   Condition Assessment and Likelihood of Failure	40
           4.2.1   Relative Criticality	40
           4.2.2   "Belief Networks"	41
     4.3   Life Cycle Curves	41
     4.4   Residual Life - Life Predictions, Modeling, and Life Expectancy Curves	42
           4.4.1   Life Predictions	42
           4.4.2   Modeling	44
           4.4.3   Life Expectancy Curves	44
           4.4.4   Software Programs	45
     4.5   Current Barriers to Effective Use of Condition Assessment	46
           4.5.1   Database Quality	46
           4.5.2   Regional and Local Variations	46
           4.5.3   Inspection Data Set Requirements	47
           4.5.4   Current Condition Assessment Methodologies	47
           4.5.5   Current Inspection Technologies	47
           4.5.6   Physical Difficulties and Costs of Inspection	49
           4.5.7   Relationship between Information Needed and What Current Technologies
                  Provide	49
           4.5.8   Relationship between Performance and Cost	49

5.0 KEY PERFORMANCE AND COST IMPROVEMENT AREAS	51
     5.1   National Asset and Failure Database Guidelines	51
     5.2   Guidelines for Interpreting Defects and Distress Indicators and Developing Condition
           Ratings	51
     5.3   Guidelines for Utilities on Undertaking Condition Assessment	51
     5.4   Developing User-Friendly Models to Predict Residual Life and Deterioration	52
     5.5   Developing Cost-Effective Inspection Tools and Methodologies	52
     5.6   Determining an Acceptable Relationship between Cost of Inspection and Value of
           Asset	53

6.0 PROSPECTS FOR SHORT- AND LONG-TERM IMPROVEMENTS TO CONDITION
     ASSESSMENT FOR FERROUS WATER MAINS	55
     6.1   Starting Points for Evaluating and Improving Short- and Long-Term Advances in
           Condition Assessment	55
     6.2   Short-Term Improvements to Condition  Assessment	55
           6.2.1   Short-Term Improvements to Use of Existing Information	55
           6.2.2   Short-Term Advances in Inspection Technologies	56
     6.3   Long-Term Improvements to Condition  Assessment	56
           6.3.1   Long-Term Improvements to Use of Existing Information	56
           6.3.2   Long-Term Advances in Inspection Technologies	57
     6.4   Measuring Success	58
     6.5   Accelerating Development- Potential Government Roles	58
           6.5.1   Guaranteed Minimum Work Programs for Internal Inspection	58
           6.5.2   Support for Database Development	59
           6.5.3   Defining Next-Generation Inspection Technology Needs	59
           6.5.4   Funding Technology Innovation Research	59
           6.5.5   Development and Support of Condition Assessment Technology Facilities	59
           6.5.6   Support of Field Demonstrations	60
     6.6   Getting Utilities to Buy-In	60

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7.0 REFERENCES	62


                                        APPENDICES


Appendix A:  Current and Developing Inspection Techologies	A-l
Appendix B:  Forum Summary, Conclusions, and Recommendations	B-l


                                          FIGURES

Figure 1-1. External and Internal Graphitization in a Cut Section of Grey Iron	7
Figure 1-2. External Corrosion of a Grey Iron Pipe	8
Figure 1-3. External Pitting after Shot Blasting	8
Figure 1-4. Deep Corrosion Pits Leading to Perforation	10
Figure 1-5. Tuberculated 6-in. Cast Iron Water Pipe	12
Figure 1-6. Examples of Structural Failure Modes for Water Mains	13
Figure 2-1. Risk: Consequences and Likelihood of Failure	19
Figure 4-1. Overall Belief Network—Likelihood and Consequences	41
Figure 4-2. Life Cycle of Typical Pipeline	42


                                           TABLES

Table 1-1.  Water Network by Pipe Material	1
Table 1-2.  Water Network by Age	2
Table 1-3.  Water Network by Diameter	2
Table 1-4.  Advantages and Limitations of Types of Ferrous Pipes	4
Table 1 -5.  Change in Wall Thickness Specifications for a 3 6-inch Pipe Operating at 15 0 psi	5
Table 1-6.  Percentages of Failures of Iron Pipe  with Different Modes in U.K	14
Table 1-7.  Summary of Factors Leading to Main Break Occurrences	15
Table 1-8.  Main Forms of Failure and Indicators in Ferrous Pipes	15
Table 2-1.  Drivers for Undertaking Condition Assessment	17
Table 2-2.  High Consequence  of Failure	20
Table 2-3.  Number of Different Types of Failure in a U.K. Utility (1991-1997)	22
Table 2-4.  Average Remaining Life Predictions in Years for Ferrous Water Mains Based on
           Period of Installation	23
Table 2-5.  Failure Modes and Indicators	26
Table 3-1.  Indicators and Criticality from Environmental Data	32
Table 3 -2.  Tools and Technologies for Inspecting Structural Integrity Externally	37
Table 3 -3.  Tools and Technologies for Inspecting Structural Integrity Internally	37
Table 3-4.  Tools and Technologies for Leak Inspection	38
Table 4-1.  Structural Condition Ratings for Force Mains (after NYCDEP)	43
Table 4-2.  Tools and Techniques for Condition Assessment Strategic Planning	45
                                              VI

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                        ABBREVIATIONS AND ACRONYMS
AMR        automatic meter reading
AMSA       Association of Metropolitan Sewerage Agencies
ANSI        American National Standards Institute
API          American Petroleum Institute
AC          asbestos cement
AWWA      American Water Works Association
AwwaRF     American Water Works Association Research Foundation
ASME       American Society of Mechanical Engineers
ASTM       American Society for Testing and Materials
AUT         automated ultrasonic testing

BEM         broadband electromagnetic

CCTV       closed circuit television
CI           cast iron
CIP          cast iron pipe
CML         cement mortar lining
CSIRO       Commonwealth Scientific and Industrial Research Organization

DC          direct current
DDM        Design Decision Method
DI           ductile iron
DIP          ductile iron pipe
DIPRA       Ductile Iron Pipe Research Association
DMA        District Metering Areas
DSS         decision-support system

EC          eddy current
ECDA       External Corrosion Direct Assessment
EPA         U.S. Environmental Protection Agency
EPRI         Electric Power Research Institute
EPTA        EPA Edison Pipeline Test Apparatus

ft            foot (feet)

gal          gallon(s)
GASB       Governmental Accounting Standards Board
GCM        Grand Central Model
GIS          Geographic Information System
GPR         Ground Penetrating Radar
GRP         glass reinforced plastic
GTI          Gas Technology Institute
GWRC       Global Water Research Coalition
GWUT       Guided Wave Ultrasonic Testing

hr           hour(s)

ILI          In-Line Inspection
                                             vn

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in.           inch(es)
in2           square inch(es)
IPWEA      Institute of Public Works Engineering Australia
IWA         International Water Association

LPR         Linear Polarization Resistance
LWC        Louisville Water Company
MFL         magnetic flux leakage
MIC         Microbiologically Induced Corrosion
min          minute (s)

NACE       National Association of Corrosion Engineers
NCER       National Center for Environmental Research
NDI         non-destructive inspection
NDT         non-destructive testing
NERC       North American Electric Reliability Corporation
NIST        National Institute of Standards and Technology
NRC         National Research Council of Canada
NRMRL     National Risk Management Research Laboratory
NYCDEP    New York City Department of Environmental Protection

O&M        operations and maintenance

PCCP        prestressed concrete cylinder pipe
PE           polyethylene
PPIC         Pressure Pipe Inspection Company
PTA         Pipeline Test Apparatus
PVC         polyvinyl chloride

RFEC        remote field eddy current
RBI          risk based inspection
RFT         remote field technology

SAM        Strategic Asset Management
SBIR        Small Business Innovation Research
SF           safety factor
SRB         sulfate reducing bacteria
STAR       Science to Achieve Results
STREAMS   Scientific, Technical, Research, Engineering, and Modeling Support

TIP          Technology Innovation Program
TO          task order

UHF         ultra high frequency
UKWIR     United Kingdom Water Industry Research
UT          ultrasonic testing

WERF       Water Environment Research Foundation
WRc         Water Research Centre
WSAA       Water Services Association of Australia
WSSC       Washington Suburban Sanitary Commission
                                             Vlll

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                                   EXECUTIVE SUMMARY
As part of the U.S. Environmental Protection Agency's (EPA's) Aging Water Infrastructure Research
Program, which supports the Sustainable Water Infrastructure Initiative, scientific and engineering
research is being conducted to evaluate and improve promising innovative technologies that can reduce
costs and improve the effectiveness of operation, maintenance, and replacement of aging and failing
drinking water distribution and wastewater conveyance systems (EPA, 2007). Task Order (TO) 62 (EPA
STREAMS Contract No. EP-C-05-057) is being conducted by Battelle, in collaboration with Jason
Consultants, Virginia Tech University, National Research Council of Canada (NRC), and PARS
Environmental, Inc., to identify and characterize the state of the technology for condition assessment of
drinking water transmission and distribution systems. This State of Technology Review Report is one  of
the first deliverables prepared under this project.

Purpose of the State of Technology Review Report

This State of Technology Review Report was developed to serve as the basis for discussion at a
Technology Forum on Condition Assessment of Water Transmission and  Distribution Systems that was
held on September 9 and 10, 2008, at Edison, NJ.  It was distributed to the Forum participants for review
in advance of the meeting.  The Forum and State of Technology Review Report focused on ferrous  water
mains, which represent two thirds of the installed network.  The State of Technology Review Report
covers transmission and distribution pipelines with diameters larger than 4 in., but does not include
appurtenances  or service connections. Comments received have been considered and incorporated, where
applicable, into the final document.

The State of Technology Review Report summarizes the current state of the ferrous pipes in the water
network, their defects and causes of failure, and the state of condition assessment technologies. It also
discusses current barriers to effective use of condition assessment, prospects for short-term and long-term
improvement, key performance and cost improvement areas, approaches for measuring success, potential
roles of government in accelerating development and acceptance of innovative condition assessment
technologies, and approaches for getting utilities to accept effective, innovative technologies and
procedures.

Forum Objectives

The overall goals for the Technology Forum were to describe and discuss  user needs, the state of the
technology, and applied research and demonstration needs and opportunities regarding condition
assessment of ferrous transmission and distribution mains.  The Forum convened national and
international experts in condition assessment to discuss several key issues. In cooperation with these key
stakeholders, the Forum helped identify and characterize specific options  for research to accelerate  and
expand the development and acceptance of innovative, cost-effective water main condition assessment
approaches including technologies, procedures, and databases. Better condition assessment approaches
can provide substantial added value to utilities by enabling: (a) early detection and economical correction
of problem  conditions, which reduce both maintenance costs and catastrophic failures, and (b)
confirmation that high-risk pipelines are in good condition, which reduces premature replacement.

State of Technology Review Report Organization

Section 1 provides an overview and characterization of the U.S. drinking water transmission and
distribution network in terms of miles of various types of pipe installed, pipe diameter, and pipe age. The
focus of this State of Technology Review Report and the Forum is on ferrous pipe types, which make up

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approximately two thirds of the distribution network. The review covers ferrous pipe cast in its various
forms, such as grey cast iron, ductile iron, and steel, together with an overview of failure modes by
corrosion, mechanical causes, and leaks. Section 2 presents the current state of the art in condition
assessment, specifically the key factors that are needed to evaluate both the likelihood and consequences
of failure. Section 3 provides a review of the principal approaches and technologies employed for
condition assessment with a focus on non-destructive inspection.

Section 4 gives an overview of the ways in which information from databases and inspection records is
currently used to arrive at a condition evaluation. Any assessment must be based on a combination of
available production/installation data, experience, and inspection records. Techniques such as belief
networks, life cycles, and the methods to predict remaining service life by means of life predictions,
modeling, and life expectancy curves are discussed. In addition, some of the barriers and limitations of
the techniques are examined, together with the technical and economic problems associated with
obtaining robust information from databases and inspection activities.

The information provided in Sections 5  and 6 was intended to stimulate discussion at the Forum.  Section
5 identifies key performance and cost improvement outputs for consideration.  Section 6 sets down some
observations on the prospects for short-term and long-term improvements.  Section 7 provides a list of
references.

Appendix A provides descriptions of some current and emerging inspection tools to supplement the
review in Section 3. Appendix B provides a summary of presentations, discussions, and key findings
from the  Forum.

Current Barriers to Effective Use of Condition Assessment

A number of barriers to effective use of condition assessment were identified in this State of Technology
Review Report and acknowledged by the Forum participants:

       •  Database Quality.  All condition assessment programs are based on high quality asset and
           failure databases. Lack of robust databases for many water utilities is a major barrier to
           condition assessment in painting a picture of failure patterns for pipes with different ages and
           types in a range of locations. The existing U.S. utility databases are incomplete and/or
           inaccurate. Failure databases are not standardized when kept, and failures are normally not
           recorded or attributed in a uniform manner to allow for any sensible comparison.

       •  Regional and Local Variations. Regional and local variations have not been given
           sufficient consideration in applying condition assessment and management tools.  Some
           existing models and curves  often need to be  modified to reflect local conditions, such as soil
           conditions  and support.  For example, the relationship between corrosion of an unprotected
           cast iron pipe and local soil conditions should be taken into account. Lack of soil  support,
           often coupled with increased external loadings, is another local factor that can alter life
           expectancy curves.

       •  Inspection Data Set Requirements. There is no consensus on what key data sets are needed
           or can be obtained from an inspection for a reliable condition assessment and life prediction.
           Inspection  can only provide a snapshot of current conditions. To make predictions, basic
           pipe information including type, age, and original wall thickness is needed. Additional
           information such as how long corrosion has  been taking place and if it has been uniform is
           also needed.

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       •   Current Condition Assessment Methodologies. There is no consensus on what key
           parameters and what their comparative weighting factors should be used in a prediction
           model. Many models require a high level of technical input, which may be available only in
           large utilities. Level of sophistication of these models and multiplicity of the associated
           approaches often can be daunting to managers and engineers in small to medium size utilities.
           There is a need for improving the situation for utilities to conduct in-house condition
           assessment.

       •   Current Inspection Technologies. Some progress has been made on structural condition
           inspection tools and more developmental work is currently underway.  However, to fully
           meet the  needs of water utilities, there is still a long way to go.

       •   Physical Difficulties and Costs of Inspection. Internal inspection has a significant cost in
           gaining access to the line. Many utilities have reservations about introducing inspection tools
           into operational mains due to concerns of potential contamination. Other internal
           technologies can only operate with the main out of service, emptied and cleaned. For an
           external investigation of a main under a roadway, activities such as excavation, traffic
           control, pavement removal,  reinstatement, and dealing with existing utilities will add
           significant cost to the inspection.

       •   Relationship between Information Needed and What Current Technologies Provide.
           The quality of the information obtained by internal and external inspection technologies is not
           well defined.  Currently, utilities have to adjudge any technology or method based on the
           sales pitch and cost. There is no independent testing and evaluation information to compare
           competing methods for their ability to provide the information needed.

       •   Relationship between Performance and Cost.  The value of pipeline inspection information
           is not well quantified, thereby making cost/benefit decisions about assessment  difficult or
           impossible.
Key Performance and Cost Improvement Areas

The State of Technology Review Report and the Forum together identified the following key performance
and cost improvement areas, which fall into two main categories: 1) improving the consolidation,
organization, analysis, and use of data that already have been, or are being, collected by utilities, and 2)
improving the capability and cost-effectiveness of inspection technologies:

       •   Standardized Asset and Failure Databases.  Adoption of a national standardized asset and
           failure database would be a major step in improving condition assessment.

       •   Condition Assessment Priority-Setting & Implementation Guidelines. User-friendly
           guidelines should be developed for utilities for identifying high risk scenarios, interpreting
           defects and distress indicators,  developing pipe condition rating, and selecting specific
           investigation or monitoring techniques.  Guidelines are also needed for utilities on
           undertaking a two-stage condition assessment after a decision has been made and the goals of
           condition assessment have been established. The first stage is an initial assessment based on
           asset and failure databases, which, in some cases, may be sufficient for a decision to be made
           without investigation.  In other cases it will define and prioritize the second stage, which is a
                                              XI

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           more detailed, specific investigation that will typically involve inspection.

       •   User Friendly Residual Life and Deterioration Models. User-friendly models to predict
           residual life and deterioration are needed that can be used by utilities to assist them in their
           asset management planning and expenditure forecasting.  The prediction models for
           individual water mains need to be tailored to the local characteristics and experience, but not
           too complicated and costly to use. An evaluation of the effectiveness of the existing models
           and their extent of use by utilities will be valuable.

       •   Better Inspection and Condition Forecasting. Cost-effective inspection tools and
           methodologies are needed to provide data  on existing structural condition and prediction of
           future deterioration. A consensus is required on what data need to be collected, over what
           percentage of a pipeline, to what accuracy, and what cost the utilities are willing to pay.

       •   Determining an Acceptable Relationship between Cost of Inspection and Value of Asset.
           Utilities seem prepared to pay the relatively high cost of inspection for large mains as the
           consequences of failure can be very high in terms of damage, loss of service, and repair cost.
           There is value, after cost of investigation is deducted from the benefit, in avoiding a failure.
           More in-depth studies on the value of inspection in relation to asset value for different
           diameter and types of pipes are needed.  This could go hand in hand with alternative ways of
           condition assessment for smaller diameter pipes and justify the use of NDT inspection tools.
Short- and Long-Term Improvements to Condition Assessment for Ferrous Water Mains

The State of Technology Review Report and Forum contributions together provide clear guidance on the
potential short- and long-term improvements to accelerate and expand the development and acceptance of
innovative, cost-effective ferrous water main condition assessment approaches (i.e., technologies,
procedures, and databases).

        •   Short-Term Opportunities to Improve Condition Assessment.
           o   Improved effectiveness of collection, analysis, and use of existing information (i.e.,
               environmental, historical, and operational) for condition assessment offers the best
               opportunity to improve the asset management performance of the water industry. The
               knowledge and understanding of local conditions, defects, and failures reside with the
               utility management, engineers, and operators and should be harnessed.
           o   Recent and emerging advances in leak detection and structural inspection technologies
               show promise of providing relatively low-cost, low-intrusion capability for utilities to
               undertake inspection.

        •   Long-Term Opportunities to Improve Condition Assessment.
           o   Utilities should be provided with better understanding of the behavior of different forms
               of ferrous pipes in the water network. A national database  of assets and failures relating
               breaks and leaks to specific materials and environment can allow utilities to benchmark
               their own experience  and support the decision-making process.
           o   Long-term advances in inspection technologies can be accelerated by developing a
               consensus on cost and performance targets for next-generation inspection and condition
               assessment goals, technologies and procedures.  Advances  in electronics, sensor
               technology, and computer science will enable the emergence of new technologies that
               can be applied to the inspection, monitoring, and assessment of the conditions of water
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       mains. Technologies initially developed for non-water applications should be assessed
       for potential transferability to water main condition assessment.

•   Measuring Success. Measuring success will take a number of forms.  By the nature of the
    utility structure and the measures needed it will take time for the full benefits to flow.  Over
    time, the improved condition assessment activities should result in reduced unforeseen
    failures and catastrophic events as well as the associated direct and indirect costs. Improved
    life prediction curves will provide a sound basis for budgeting for renewals and allow a
    running program to be developed

•   Accelerating Development - Potential Government Roles. In cooperation and
    collaboration with relevant stakeholders, the government can play important roles in
    accelerating technology development. Examples  include:
    o  Support for guaranteed minimum work programs for internal inspection
    o  Support for national database  development
    o  Defining next-generation inspection technology needs
    o  Funding technology innovation research & development
    o  Support of condition assessment technology test facilities, and
    o  Support of field demonstrations.

•   Getting Utilities to Accept Effective, Innovative Technologies.  The benefits  of condition
    assessment and the techniques used in inspection, assessment, and prediction should be
    communicated with utilities more effectively through various channels, including workshops,
    conferences,  webinars, papers, and articles.  By raising awareness and interest, the benefits of
    adopting the methods and technologies will become apparent to the utilities.  They will adopt
    these techniques only if such an action helps them save money, make their work easier, and
    make their customers happier.  Field demonstration will be a key way to show utilities what
    can be done and at what cost.
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1.1
                 1.0 CHARACTERIZATION OF WATER NETWORK IN U.S.
Overview of U.S. Water Transmission and Distribution Network
The basics of the U.S. water transmission and distribution network are profiled in Tables 1-1, 1-2, and 1-3
based on studies and surveys conducted by American Water Works Association (AWWA) and AWWA
Research Foundation (AwwaRF) (AWWA and AwwaRF, 1992; 1996; AWWA, 2004).  Because these
surveys are based on limited responses, there are some variations in percentage breakdowns by pipe
materials.  As shown in Table 1-1, about two thirds of the installed network consists of various forms of
ferrous pipes, including cast iron, ductile iron, and steel pipes. This State of Technology Review Report
and the Forum concentrated on ferrous pipes to allow for a more focused and in-depth evaluation of the
condition assessment and inspection needs.  This focus has the advantage that the causes of deterioration
and the technologies of inspection to identify and quantify defects in ferrous pipes are common.
                          Table 1-1. Water Network by Pipe Material
Source of Data
Utilities Responded/Surveyed
Response Rate
Pipe Material
Cast Iron Unlined
Cast Iron Cement Mortar
Lined
Cast Iron Other
L ining/Unkno wn
Total Cast Iron
Ductile Iron Unlined
Ductile Iron Cement Mortar
Lined
Ductile Iron Other
L ining/Unkno wn
Total Ductile Iron
Steel
Subtotal for Ferrous Pipes
Asbestos Cement
Pre-stressed Concrete
Glass Reinforced Plastic
Polyethylene
Polyvinyl Chloride
Others/Unknown
Subtotal for Non-ferrous
Pipes
Grand Total
Water Industry
Database'50
1,097/3,000
37%
Miles
Installed(d)
153,415
159,284
28,476
341,175
35,916
150,705
2,494
189,115
34,047
564,337
136,196
23,584
665
3,349
114,152
20,169
298,115
862,452
Percent of
Total
17.8
18.5
3.3
39.6
4.2
17.5
0.3
21.9
3.9
65.4
15.8
2.7
0.08
0.4
13.2
2.3
34.6
100
Water://Stats 1996
Distribution Survey(b)
898/3,200
28%
Miles
Installed
NA
NA
NA
155,038
NA
NA
NA
81,119
16,415
252,572
56,360
15,921
422
1,318
42,125
6,719
122,865
375,437
Percent of
Total
NA
NA
NA
41.3
NA
NA
NA
21.6
4.4
67.3
15.0
4.2
0.1
0.4
11.2
1.8
32.7
100
Water://Stats 2002
Distribution Survey'0*
337/3,000
11%
Miles
Installed
37,433
34,039
NA
71,472
9,886
35,118
NA
45,004
7,821
124,297
30,484
4,774
NA
1,377
29,835
11,391
77,861
202,158
Percent of
Total
18.5
16.8
NA
35.4
4.9
17.4
NA
22.3
3.9
61.5
15.1
2.4
NA
0.7
14.8
5.6
38.5
100
     NA = not available
     (a) AWWA and AwwaRF, 1992.
     (b) AWWA and AwwaRF, 1996.
     (c) AWWA, 2004.
     (d) Data represent population-based extrapolations to national totals.

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                                Table 1-2.  Water Network by Age
Age in Years
Oto 10
10 to 25
25 to 50
>50
Total
Miles Installed
245,000
325,000
156,500
137,000
863,000
Percentage
28.4
37.6
18.1
15.9
100
                            Source: AWWA and AwwaRF, 1992.
                             Table 1-3. Water Network by Diameter
Diameter Range (in.)
<6
6 to 10
12 to 16
18 to 24
30 to 48
>48
Total
Miles Installed
107,200
523,200
138,600
29,700
57,700
6,000
863,000
Percentage
12.4
60.6
16.3
3.4
6.7
0.8
100
                          Source: AWWA and AwwaRF, 1992.
Various forms of grey cast iron pipes account for nearly 40 percent of the network and are at least 40
years old with some well over  100 years old. The production of grey cast iron pipes ceased from the
1970s so all the iron pipes laid in the last 30 to 40 years have been ductile iron pipes.  According to the
AWWA 1992 Water Industry Data Base (AWWA and AwwaRF, 1992), 34 percent of the network was
more than 25 years old and 72 percent was installed more than 10 years ago (see Table 1-2). Due to lack
of recent survey data on pipe age, it is estimated that, at the present time (i.e., 17 years from 1992), about
75 percent of the current network is older than 25 years and that about half of the current ferrous pipe
network is older than 50 years.

Water transmission mains usually range in diameter from 12 to 96 in. and greater.  From Table 1-3, it is
noted that over 70 percent of the network was in diameters of 12 in. or less. The smaller diameter pipes
have more frequent failures than larger diameter pipes as a result of a greater installed length of small
pipes and a higher failure rate than the larger pipes.  While most of the failures occur in  smaller
diameters, the risk posed by single failure of a large transmission line can be orders of magnitude higher
due to the significant damage and loss of service that can occur.
1.2
Types of Ferrous Pipes
1.2.1       Cast Iron Pipes. Cast iron usually refers to grey cast iron. Most grey cast iron pipes that are
in service were manufactured by either pit casting or spin casting. The earliest cast iron pipes were
vertically pit-cast grey iron.  In the early nineteenth century, the first pit-cast iron pipes in the U.S. were
imported, but from 1830, local production became more widely established. Pit-cast iron pipes were
manufactured and installed until the 1940s.

Pit-cast iron pipes are characterized by:

       •  High degree of variability in wall thickness, often with an eccentric bore
       •  Casting defects such as blowholes, pinholes, etc.

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        •   Mould parting seams
        •   Poured lead joints
        •   Easily fractured with a sharp impact
        •   Flake graphite form
        •   Unlined pipe.

Spun-cast iron pipes followed in the late 1920s and were extensively installed until the 1970s. Spun-cast
iron pipes are characterized by:

        •   Thinner wall than vertically cast pipes, but uniform thickness
        •   Manufacturing defects, laps, laces, and pinholes
        •   Stress corrosion fissures
        •   Leadite joints and rubber gasket seals
        •   Easily fractured with a sharp impact
        •   Flake graphite form
        •   Unlined pipe.

1.2.2       Ductile Iron Pipes. Ductile iron pipes were commercially introduced in the 1950s and
because of greatly improved characteristics, they replaced spun iron by the late 1960s.  The characteristics
of ductile iron pipes are:

        •   Thinner wall with uniform thickness
        •   Shrinkage porosity (angular pores resulting form non-uniform solidification)
        •   Reverse peen pattern on surface
        •   Not subject to brittle fracture
        •   Rubber gasket seals
        •   Spheroidal or nodular graphite form
        •   Approximately twice the strength of cast iron  (tensile, beam, ring bending, and bursting tests)
        •   Increased use of scrap metal in pipe production changing the microstructure
        •   Generally lined pipe.

1.2.3       Steel Pipes. The level of carbon in the metal is what distinguishes steel from cast iron. Steel
normally has less than 1.2 percent by weight of carbon and its structure is dominated by pearlite. Both
grey and ductile iron pipes have a carbon content of 2 to 5 percent by weight. Various methods are used
to fabricate steel pipes. One early form was Lock-Bar pipes (American Society for Testing and Materials
[ASTM] -137-34), which originated in Australia, where pipes were made by rolling steel plate in two half
cylinders and joining the two edges with a locking bar.  In the early nineteenth century, pipes were
formed by using riveted steel plates.  Such pipes are still in operation in the cities of Toronto and Los
Angeles. Since the 1930s, they have been fabricated as welded pipes.

Diameters up to 20 in. can be manufactured to produce seamless pipes. Larger diameter pipes use "O" or
"U" dies to form plates into the required shapes and the longitudinal seams are welded.  Other methods
take plates and roll them to the required shapes, which are welded together by submerged arc with one or
more circumferential and longitudinal seams.  One technique is spiral fusion welding, in which coiled
strip is formed helically into a pipe and the spiral seam is continuously welded.

Contemporary steel pipes in the water network typically have a diameter of 14 in. or greater.  The
characteristics of steel pipes are:

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        •   Thinner wall than grey cast iron or ductile iron pipes
        •   High strength with ability to deflect without breaking
        •   Shock resistance
        •   Lighter weight than ductile iron pipe
        •   Ease of fabrication of large pipe
        •   Availability of special configurations by welding
        •   Ease of field modification
        •   Protective coating externally; cathodic protection is routinely installed
        •   Generally lined pipe.

1.2.4       Summary of Ferrous Pipes.  A summary of the advantages and limitations of various types
of ferrous pipes is provided in Table 1-4.
                 Table 1-4. Advantages and Limitations of Types of Ferrous Pipes
Advantages
Limitations
Grey (Pit and Spun) Cast Iron Pipes
• Thicker wall than ductile iron or steel
• Similar rate of corrosion to ductile iron and
steel
• Most pipes after 1950 supplied with
cement mortar lining or retrofitted
• No elastic behavior and lower mechanical strength
• Prone to external and internal corrosion in aggressive conditions
• Older pipes having caulked joints with little flexibility
• Often no external protection
• Most pipes unlined before 1960
• Manufacturing defects including variations in wall thickness
• Poor records
Ductile Iron Pipes
• Greater ductility than grey iron
• Greater impact resistance than grey iron
• Greater strength than grey iron
• Lighter and easier to lay than grey iron
• Simplicity of joints
• Joints can accommodate some angular
deflection
• Similar rate of corrosion to grey iron and steel
• Prone to external and internal corrosion
• Internal and external protection systems required
• Limited number of protection systems available in U. S.
• Polyethylene wrappings can be damaged
Steel Pipes with Lining
• High tensile strength
• High compressive strength
• Range of corrosion protection systems
• Wide range of diameters and wall
thickness Welded joints give continuity
• Prone to external corrosion
• Electrolysis prone
• Jointing requires skilled welders
• Internal/external corrosion protection systems add to price
• Coatings and linings can get damaged during installation and by
third parties
The improved characteristics developed over the years allowed a significant reduction in the thickness of
pipe walls permitted under AWWA recommendations, as shown in Table 1-5.

Pipes were, and are, manufactured in a range of pressure classes. The date of manufacture is significant
in any consideration of ductile iron mains.  The first AWWA standard C151/A21.51 was issued in 1965
and revised in 1971, 1976, 1981, and 1986.  These standards were based on a series of seven thickness
classes designated as Class 50 to Class 56.  The wall thickness for a 42-in. pipe could vary from 0.47 in.
at Class 50 to 0.83 in. at Class 56.

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                       Table 1-5. Change in Wall Thickness Specifications
                               for a 36-in. Pipe Operating at 150 psi
Year of
Installation
1908
1952
1957
1965
1976
1991
Material
Cast iron
Cast iron
Cast iron
Ductile iron
Ductile iron
Ductile iron
Wall Thickness (in.)
1.58
1.22
0.94
0.58
0.43
0.38
Every pipe from the standard of the same class has the same d/t ratio.  This links directly to pressure
capability as the hoop stress is equal to Pd/2t, where P is internal pressure, d is internal diameter, and t is
wall thickness.  Therefore, for a given allowable hoop stress, every pipe of the same thickness class would
have the same pressure rating, ignoring external load. In 1991, the standard was changed to a "pressure
class" system and the "thickness class" was no longer standard. However, this change was not
universally accepted and some engineers stayed with "thickness class" specifications. These are still
included in the standards as "Special."

Pressure to keep installed costs as low as possible often  results in selecting the lowest pressure class of
pipe for use. The use of a lower pressure class of pipe with a thinner wall frequently results in a shorter
service life and in most cases, this disadvantage far outweighs any short-term economic advantage.

Ductile pipes normally are lined with cement mortar,  and coatings and plastic sheaths help resist external
corrosion.

Other forms of lining are used, including epoxies and urethanes. Water lines can be rehabilitated in-situ,
with polyethylene (PE) and cure in place being the most widely used material and lining system,
respectively.

Steel pipes used for water mains are normally lined internally and coated externally. Linings include
cement mortar and polyurethane.  Coatings include tape, coal tar enamel, cement mortar, epoxy, and
polyurethane.  Cathodic protection by an impressed current or sacrificial anode system for wrapped or
coated steel lines is generally recommended and widely used.  The continuity of welded joints facilitates
the use of cathodic protection.

Early cast iron pipes were jointed rigidly with metal to metal contact with a bell and spigot.  Lead and
leadite were used for jointing. Semi-rigid joints, with a  packing material such as jute or yarn and caulked
with lead, became the predominant method.

Ductile iron pipes can have a variety of joints; bell and spigot push fit type is used primarily for pipes in
trenches, with an elastomeric seal. Bolted  mechanical and flanged joints are also available.

Steel pipes used for water mains principally have welded or flanged joints.
1.3
Overview of Failure Modes of Ferrous Pipes
The primary research focus of this project is on structural condition of water transmission and distribution
mains as opposed to hydraulic or water quality condition.  It is estimated that there are 300,000 main

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breaks a year for all types of pipe material in the U.S. (Grigg, 2007).  The modes of structural failure for
ferrous pipes have been extensively researched, and this section provides a summary of the literature
search.

Causes of failure can be considered under two categories: corrosion and mechanical failures.  Although
these causes are distinct, they are related in that mechanical failures may result from corrosion such that
the pipe is no longer able to resist applied internal and external forces.

Leakage is an additional category that may or may not be classified as a structural failure depending on its
location and its severity. Corrosion of the pipe wall may lead to perforation and leakage. Leakage can
also occur at joints and contribute to mechanical failures in eroding pipe bedding support. Leakage can
be seen as an indicator of wall penetration by pitting.

1.3.1       Corrosion - Internal and External. Many different mechanisms and parameters are
involved in corrosion and failure of ferrous pipes. This complexity has given rise to controversy and
differences of opinion about the relative performance of different forms of ferrous pipes.

Overview of Corrosion Mechanisms

The criteria essential for corrosion by oxidation include

        •   Oxygen supply
        •   Moisture
        •   Soluble salts
        •   Cathodic and anodic sites.

Conditions may vary widely along the length of a buried pipeline and can result in considerable
variability found when investigating external corrosion.  It is common to find a section of badly corroded
pipe adjacent to a sound section. This situation is emphasized by the observation of corrosion "hot spots"
in which accelerated corrosion can be focused on one location in the pipe exposed to conditions that are
conducive to corrosion.

A more detailed consideration to mechanisms of external corrosion is presented in "Corrosion Control
Measures for Ductile Iron Pipe" (Stroud, 1989).  More in-depth information on the mechanisms of
internal corrosion can be found in "Iron Pipe Corrosion in Distribution Systems" (McNeill and Edwards,
2001).

Graphitization

For iron pipes, graphitization is an important form of corrosion. Graphitization occurs where soil
conditions including pH, dissolved salts, and organic content are favorable to anaerobic bacterial growth.
For grey iron, the metal goes into solution leaving behind a corrosion product that consists of a mass of
residual graphite flakes interspersed with iron oxides. Overtime the wall becomes a composite of grey
cast iron and a graphite matrix with the corrosion product occupying the space previously occupied by the
grey iron.  An example is shown in Figure 1-1. It is difficult to identify graphitization during visual
inspection because there is no apparent wall thickness loss. The graphitized material has some strength,
although possibly greatly reduced, which explains why some extensively graphitized grey cast iron pipes
have continued to function.

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         External
         graphitisation
         Sound metal
                                                                                  Tuberculation
                                                                                  Graphitic
                                                                                  corrosion
                                                                                  product
         Plate 2
Detail of a section through the site of an internal pit
        Source: Dempsey and Manook, 1986.

            Figure 1-1. External and Internal Graphitization in a Cut Section of Grey Iron
Often grey cast iron pipe failure comes from mechanical stress or a hydraulic shock (roadwork, transport
damage, or ground movement) acting on the weakened structure. This is then classified as a mechanical
failure rather than a corrosion failure.

General corrosion can occur in ductile iron in the form of graphitization, but the corrosion material that
forms is weaker and more friable than that in grey iron. The graphite corrosion products are in the form
of discrete nodules that are easily detached, and a structure is not retained.  This can lead to leakage and
break failure occurring more  quickly than in grey cast iron (Vrab, 1992).

The relative merits of the different metallurgical forms of grey cast iron and ductile iron and their
resistance to graphitization have been an area of some disagreement among researchers.

Graphitization does not occur in steel pipes.

Pitting Corrosion

For all types of ferrous pipes, external corrosion in the form of isolated pitting, general corrosion, and
graphitization is the most common form of deterioration, which can lead to leakage or failure.

Pitting corrosion is a concentration of corrosion in one particular area.  The metal goes into solution
preferentially at that spot rather than adjacent areas.  Figure 1-2 shows a pipe corroded externally.

Pitting corrosion is the most common deterioration mechanism for all ferrous pipes.  It can occur
internally, although it is more likely to be found externally. Pitting occurs quite randomly, usually
leading to wall penetration and leaks rather than failures. A group of pits in one area can weaken the wall
sufficiently for the pipe to fail. Figure 1-3 shows external pitting on  a pipe.

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 Plate 6
General corrosion damage over part of external surface
Source: Dempsey andManook, 1986.
                  Figure 1-2. External Corrosion of a Grey Iron Pipe
   Plate 7
 Isolated external pitting (narrow)
Source: Dempsey andManook, 1986.
                    Figure 1-3. External Pitting after Shot Blasting

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The AwwaRF report "The Effect of Corrosion Pitting on Circumferential Failures in Grey Cast Iron
Pipes" gives a detailed presentation on pitting in grey cast iron pipes (Makar, 2005).

The extent and rate of external pitting on an unprotected pipe is governed primarily by the corrosivity of
the environment.  Consequently, various protective measures are installed to counter external corrosion.

The most common form of external protection in North America is polyethylene encasement (AWWA
C105 issued in 1972), and its use has been specified in ASTM D1248 since the  1950s. This is a site
operation where the pipe is wrapped in polyethylene sheet at the time of laying. The objective is to
isolate the pipe from the soil environment.  The Ductile Iron Pipe Research Association (DIPRA) sets out
a strong case for this as the only protection system needed.  However, cases of failure of wrapped ductile
iron pipes have been reported. Damage to the polyethylene wrap during installation or subsequently by
third party activities can allow ingress of groundwater, creating corrosive conditions.  Some utilities base
decisions on the grounds of non-corrosive condition and/or cost reduction and have not followed DIPRA
recommendations. It is thought that as much as 50 percent of ductile iron pipes have been laid without
poly-wrap.

Bonded coatings normally are not recommended on ductile iron pipes, while bonded coatings on steel
pipes are readily supplied. The only AWWA standards for ductile iron cover polyethylene encasement
and the standard asphaltic shop coating.

Lining the ferrous pipe interior with cement mortar maintains water potability.  It also protects the metal
from corrosion by providing a coating of electrically inert material between metal and liquid. High pH of
the conveyed water can be incompatible with cement mortar lining (CML). Deterioration takes the form
of leaching of lime from the cement matrix, causing calcium loss. An on-going Water Research
Foundation project,  "Life Expectancy of Field and Factory Applied Cement Mortar Linings in Ductile
Iron and Cast Iron Water Mains" (Project #3126), will address such issues in more detail.

Leakage

Leakage can occur both  from joints due to poor installation and from the body of the pipe where
perforations occur due to pitting. Leakage through perforations in the pipe  wall is common to all ferrous
pipes. Leakage from joints  is probably most common due to incorrect installation. Another cause is
movement of adjacent pipe lengths. In the case shown in Figure 1-4, the deep corrosion pitting
perforating the pipe wall did not lead to a structural failure.

Often small leakage from water mains goes undetected and therefore continues  without remedial action.
All forms of leakage can in theory lead to erosion of the pipe bedding and to structural failure. In
practical terms most leaks, particularly from joints, are defects rather than failures and do not create
conditions leading to failure. This is not to undervalue the serious costs and problems that arise  from
leakage.

The interaction between a leaking pipe and its surrounding soil is complex (Van Zyl and Clayton, 2005).
The relationship between head loss and flow is not linear, as a result of the interaction of the soil particles
with the orifice, turbulent flow in the soil, the changing geometry of the unconfmed flow regime,
hydraulic fracturing, and piping.  Theoretical considerations suggest that small continuous leaks will drain
away without trace into underlying granular soil.  This cannot be expected to occur in lower permeability
clays and silts, where hydraulic fracture is more likely, with leaks rapidly becoming visible as wet patches
and bursts at the ground surface.

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         Plate 10     Holes (FWG) produced by deep external corrosion pits -
                     spun grey iron pipe from a non-failure site
        Source: Dempsey andManook, 1986.

                       Figure 1-4. Deep Corrosion Pits Leading to Perforation
Microbiologically Influenced Corrosion

Buried ductile iron and grey cast iron pipe can be subject to microbiologically influenced corrosion
(MIC).  There are two forms - anaerobic and aerobic. Anaerobic corrosion is what is often referred to as
hydrogen sulfide corrosion.

Sulfate reducing bacteria (SRB) are a typical example of anaerobic bacteria.  The attack is ascribed to the
bacteria's ability to make the oxygen that is present in sulfates, nitrates, and carbonates available for a
cathodic reaction.  This is significant in that it means that corrosion can occur even in the absence of
dissolved oxygen.  It is calculated that the corrosion rate of iron under anaerobic conditions is nearly 20
times as great as under sterile  conditions.  According to a study in Australia, it is estimated that 50 percent
of their studied failures that occurred on buried metal were due to MIC (Ferguson and Nicholas, 1984).

Galvanic Corrosion

Galvanic corrosion is an electrochemical process that occurs when dissimilar metals are electrically
connected and installed in a uniformly conductive soil, or when a metallic pipe is installed in a soil that
has a non-uniform character.  In both cases, electrical current flows from the anode to the cathode. As the
anode loses electrons, the anode metal is oxidized,  and corrosion results.

Galvanic corrosion can be found where a ferrous pipe is connected to copper service  lines. The  service
piping used in North America is almost exclusively copper, with a small amount of lead and galvanized
steel pipe used in the older areas. When ferrous  and copper pipes are connected, the mixed metal system
may accelerate corrosion where the iron piping acts as the anode of a galvanic corrosion cell and the
copper acts as the cathode.
                                               10

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Corrosion cells develop on a ferrous pipe exposed to different electrolytes (Fitzgerald, 1984). This
situation may occur on a long pipeline that passes through different types of soils, i.e., one portion of the
line might be laid in sandy loam while another in clay.  Substantial natural pipeline currents may occur,
which leads to corrosion cells. In soils of low resistivity, such currents exit from the pipeline, causing the
loss of metal at the exit points by anodic dissolution (corrosion).  Anodes and cathodes may be miles
apart. Similarly, mixtures of soils in the backfill will cause corrosion. Lumps of clay mixed into  a sand
backfill will lead to severe corrosion where the clay contacts the pipe. The same phenomenon causes
corrosion on pipe exposed to soil and concrete or other highly alkaline backfill.

Electrolytic Corrosion

Electrolytic corrosion, also called stray current corrosion, occurs when the pipeline picks up stray
electrical current from a direct current (DC) source. Electrolytic corrosion is similar to galvanic except
that an outside source rather than a chemical reaction drives the cell.  Ferrous pipelines buried in the
ground can offer a better path for conducting earth return currents from electrified transport systems,
electrical installations, and cathodic protection systems. The point of corrosion normally is located at the
point where the positive current exits the pipe and enters the earth.

Pipes that are bell and spigot and jointed with a rubber gasket are not considered as being electrically
continuous. However, several case histories are reported in which cathodic protection has been installed
after experiencing high rates of failure (Rajani and Kleiner, 2007). The City  of Calgary, Canada requires
sacrificial anode cathodic protection for all metal pipe systems. Some grey cast iron pipes had a jointing
system that involved metal to metal contact, which theoretically could provide a continuous electrical
path.  Retrofitting by opportunistic fitting of anodes to pipes when exposed has also been increasingly
used.

Steel pipelines with welded joints offer a continuous electrical path, but are normally protected by an
impressed current or sacrificial anode system.

Both ductile iron and  spun-cast iron pipes can become subjected to corrosive conditions as a consequence
of damage to the annealing oxide scale formed during manufacture.  The action appears to be the
electrochemically more noble thermal oxide scale forming a galvanic cell with any damaged area of bare
iron that becomes the anode.  Because of the relatively large ratio  of cathodic to anodic area, this can
provide conditions for rapid localized corrosion attack.

Crevice corrosion occurs where the surface is flawed by mill scale, scratches, or rust. This is found to be
more prevalent in spun-cast iron pipes.

Tuberculation

Internal corrosion of iron can lead to the formation of loose porous rust, i.e., ferric iron hydroxide
Fe(OH)3, which can transform into a crystallized form called tubercles on the internal unlined surface of a
ferrous pipe. Depending on the pH and other ions present, a variety of precipitates can mix with the iron
oxide forming an internal "lining" of tuberculation. This "lining" can slow corrosion by cutting off the
metal from the water and air supply.  Figure 1-5 shows a tuberculated water pipe.

It has been observed that pitting is often present below the tuberculation.  The removal of tuberculation
will cause the pitting to continue at an accelerated rate until a new coating is formed.  Utilities normally
line a pipe with cement mortar after cleaning, which protects the internal surface.
                                                11

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                       Source: provided by John Black of Opus Consultants in Australia

                       Figure 1-5.  Tuberculated 6-in. Cast Iron Water Pipe
Tuberculation creates problems of flow and water quality.  It also creates a barrier for many internal
inspection tools. Disturbing the tuberculation "lining" without subsequent lining can lead to water quality
problems and further accelerated internal corrosion.  For this reason, cleaning or seriously disturbing the
tuberculation by internal investigation is generally avoided.

Relative Resistance to Corrosion of Cast and Ductile Iron

There have been many published discussions on the relative resistance of cast and ductile iron, and some
organizations suggest that in terms of corrosion resistance, ductile is superior to cast iron. This is
considered to be an optimistic conclusion by De Rosa and Parkinson (1986), who, after reviewing a large
range of investigations and evidence, determined that:

        •   The evidence that ductile iron exhibits superior pitting resistance is not conclusive; for all
           practical purposes, there is no significant difference

        •   External pitting rates depend on the aggressivity of the soil environment

        •   For equal thickness, steel is the best material when buried bare.

The Water Research Foundation study "Long Term Performance of Ductile Iron Pipe" (Project #3036) is
expected to provide valuable information on this contentious topic when it is completed in 2010.

1.3.2       Mechanical Failures. Mechanical failures are more complex to investigate and interpret.
Undoubtedly for a utility operator repairing a failure, it would be very difficult to distinguish between a
corrosion and mechanical failure.  A survey by the National Research Council of Canada (NRC) reported
that 23 out of 25 mechanical failures investigated were associated with corrosion pitting (NRC, 2003).
                                               12

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Figure 1-6 illustrates the most common failure modes of water main breaks, as well as the forces acting
on the pipe that cause breaks to occur (NRC, 2003).
            fwn frosf
   - Bonding stress fron swelNng
    clay
   - Thermal eOTiracteon
   - Longitudinal stress near valves
    and fittings
    Brwfc

- Hoop siress from internal
 wale! pressure
• Ring stress from sal
 cover load
- Hoop stress from freeing
 water
- Rjng slrass from traffic load
                                                        Sp*t Bell
                 Bell Sh«»r


              • "Oer homing* ^^o! in ball
                    :ress
                     Spiral Break

                  - Combination of bendng stre:
                   and hoop stress from
                   internal water pressure
               • Hoop stfess froni mtem^
                waler presstf e
               - Corroscm of steeS preiJTe
                wires in CPP
C^_D
  Th rough Hot«
• Corrosion pi^ng
- Casting Daws
  Source: NRC, 2003.

                Figure 1-6.  Examples of Structural Failure Modes for Water Mains
Exposed fracture surfaces and cracks indicate a mechanical failure.  Six different mechanical failure
modes have been identified for cast iron pipes (Makar, 2001).  These modes are:

        •   Circumferential failures, typically found in smaller diameter pipes and due to longitudinal
            stresses

        •   Longitudinal failures, typically found in larger diameter pipes and caused by internal
            pressure or compressive forces which push spigots into bells

        •   Shearing failures, typically found in large diameter pipes often associated with over forcing
            of spigots into bells

        •   Spiral failures, which have been found in medium diameters of up to 20 in.

        •   Bell splits, normally associated with leadite-sulfur based joint sealant, and caused by
            differing thermal expansion between metal and non-metallic leadite

        •   Perforations, normally created by through-wall pitting. The failure will be leakage rather
            than structural.
The seventh failure mode - rupture/blow-out, mainly occurs in prestressed concrete cylinder pipes
(PCCP) due to prestressed wire failure.  Often what is described as blow-out in ferrous pipes is actually
one of the other six modes.
                                                  13

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Circumferential or circular failures may be caused by one or more of the following:

       •   Thermal contraction

       •   Bending stresses arising from differential soil movements or voids in the bedding,
           which in turn may be caused by leaks

       •   Bad installation practice

       •   Third party impingement

       •   Internal pressure in combination with one of the above.

Longitudinal breaks are caused by transverse stresses, and one or more of the following factors are
involved:

       •   Internal pressure
       •   Hoop stress due to live loads
       •   Increased ring stress due to thermal changes (frost loads).

From a study of 72,000 data records of U.K. ferrous water mains laid in the period between 1880 and
1980, the overall percentage of failure types is shown in Table 1-6 (United Kingdom Water Industry
Research [UKWIR], 2001).


           Table 1-6.  Percentages of Failures of Iron Pipe with Different Modes in U.K.
| Circumferential
| 66.4%
Longitudinal
13.3%
Hole
16.1%
Joint |
4.2% |
The large percentage of circumferential failures was concentrated in the smaller diameters up to 12 in.,
which also represent the greatest length of the network. Longitudinal failures became dominant in the
larger diameters.

Mechanical failure for steel pipe is by longitudinal crack propagation.

1.4        Main Break Occurrence Factors

Table 1-7 summarizes the main break occurrence factors. It is based on Table 1 from an EPA "White
Paper on Improvement of Structural Integrity Monitoring for Drinking Water Mains" (Royer, 2005).

1.5        Causes of Failure and Indicators in Ferrous Pipes

Table 1-8 is a summary of main causes of failure and indicators in ferrous pipes. Break failure refers to
situations where pipe loses its functionality and is no long serviceable; structural failure refers to presence
of cracks, holes, and other defects on serviceable pipes.
                                              14

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          Table 1-7.  Summary of Factors Leading to Main Break Occurrences
Factor
Chemical
stressors
Physical
stressors
Other factors
Description
• Internal and external corrosion caused by factors such as aggressive water or soil,
microbes stray currents, oxygen gradients and bi-metallic connections
• Damage during transport, unloading, storage and installation
• Traffic loads
• Soil loads from differential settlement caused by soil movement
• Point loads (impingement)
• Internal radial loads from internal pressure fluctuation
• Axial loads from seismic activity, soil movement and water hammer
• Thermal stress from temperature differences between water, pipe and soil
• Damage by third parties - dig-ins
• Damage to external coatings or internal linings
• Aging - accumulation over time of chemical and physical stressors
• Pipe flaws - inadequacies in design, raw materials or manufacturing
• Installation defects - incorrect bedding, backfill, jointing, encapsulation and coatings
           Table 1-8. Main Forms of Failure and Indicators in Ferrous Pipes
     Form of Failure
      Causes of Failure
      Indicators of Failure
                                       Cast Iron Pipes
Break failure
Internal pitting and
graphitization corrosion
weakening wall often combined
with induced strain
Lining damage, wall loss from
internal pitting, graphitization,
leaks, external loads, and pressure
variations
Break failure
Break failure

Break failure



Structural failure


Structural failure
(Circumferential cracking
smaller diameters <12 in.)

Structural failure
(Longitudinal cracking
larger diameters >12 in.)
External pitting and
graphitization corrosion
weakening wall often combined
with induced strains

Third party impact damage

Manufacturing defects coupled
with fatigue and/or soil
movements

Movements from thermal,
seismic, external loading

Thermal contraction, poor
support leading to movement,
internal pressure

Internal pressures, external
loadings, thermal stresses
Structural failure (bell splits)  Leadite joints

Leaks (joints)
Loss of soil support and
bending failure
Coating damage, wall loss from
external pits, graphitization (hard to
detect), leaks, external loads, and
pressure variations

Construction activity

Cracks in body or bell
Joint leaks, poor bedding, and pipe
movements

Circumferential cracks, frost
regions, leaks, pipe movements,
and expansive clays

Longitudinal cracks, frost regions,
and changed internal/external loads
Cracking at bell

Leak noise, wet areas, and pressure
variations
                                            15

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Table 1-8. Main Forms of Failure and Indicators in Ferrous Pipes (Continued)
Form of Failure
Causes of Failure
Indicators of Failure
Ductile Iron Pipes
Break failure
Break failure
Break failure
Structural failure
Structural failure
(Circumferential cracking-
smaller diameters <12 in.)
Structural failure
(Longitudinal cracking-
larger diameters >12 in.)
Leaks (wall perforations and
joints)
External pitting and
graphitization corrosion
weakening wall often combined
with induced strains
Internal pitting and
graphitization corrosion
weakening wall often combined
with induced strains
Third party impact damage
Movements from thermal,
seismic, external loading
Thermal contraction, poor
support leading to movement,
internal pressure
Internal pressures, external
loadings, Thermal stresses
Loss of soil support and
bending failure
Damaged protection, wall loss from
external pitting, graphitization
(hard to detect), leaks, external
loads, and pressure variations
Damaged lining, wall loss from
internal pitting, graphitization (hard
to detect), leaks, external loads, and
pressure variations
Construction activity
Joint leaks, poor bedding, and pipe
movements
Circumferential cracks, frost
regions, leaks, pipe movements,
and expansive clays
Longitudinal cracks, frost regions,
and changed internal/external loads
Leak noise and wet area
Steel Pipes with Cement Mortar Lining
Break failure
Longitudinal cracking
Pipe bursts
Pitting corrosion weakening wall
Thinning from general corrosion,
and areas of pitting corrosion
Third party damage
Damage to coating/linings, wall
loss, pitting, and leaks
Graphitization, groups of pitting,
and wall loss
Construction activity
                                16

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2.1
          2.0  STATE-OF-THE-ART CONDITION ASSESSMENT OF WATER MAINS
Role in Relation to Asset Management
Asset management is playing an increasingly important role in utility operations. It is defined in the
International Infrastructure Management Manual (Institute of Public Works Engineering Australia
[IPWEA], 2006) as:

           "Asset management is a combination of management, financial, economic,
           engineering, and other practices applied to (physical) assets with the objective of
           maximizing the value derived from an asset stock over the whole life cycle, within
           the context of delivering appropriate levels of service to customers,  communities
           and the environment and at an acceptable  level of risk. "

Asset condition assessment is an important component of asset management in terms of quantifying and
determining asset performance.  Condition assessment  is used to provide accurate information about
current and likely future conditions of an asset. Table 2-1 is a summary of drivers and areas of focus for
undertaking a condition assessment, based on the Governmental Accounting Standards Board (GASB)
(Marlow and Burn, 2008).
       Table 2-1.  Drivers for Undertaking Condition Assessment (Marlow and Burn, 2008)
Driver
Assessments of renewal budgets and timing
of spending
Prioritization of capital programs
Determination of appropriate intervention
Regulatory requirements
Forensic investigations
Focus of Condition Assessment Program
Provide data for use in budget setting and/or
justifying capital deferment
Target priorities for renewal spending
Determine the level of renovation required;
select the most cost-effective whole life
approach
Comply with regulatory or financial reporting
Understand failure and support litigation
The foundation for asset and condition assessment lies in a comprehensive asset inventory.  The pipe
inventory should ascertain characteristics for each pipe segment: size, material (including lining and
external protection, if any), and age. This covers a great deal more than the pipe network and is outside
the scope of this paper. Numerous publications provide guidance on asset management and development
of asset inventories (Association of Metropolitan Sewerage Agencies [AMSA], 2002; IPWEA, 2006).

To facilitate benchmarking and comparisons, it is necessary to have a robust asset management
framework together with standardized data reporting. In order to undertake robust appraisals within an
asset management framework, some form of national standard for asset inventory would be of
considerable value. Research bodies such as AwwaRF have  undertaken extensive research and published
numerous reports, including "Asset Management Planning and Reporting Options for Water Utilities"
(Matichich et al, 2006), which reviews how utilities handle asset management and defines three options
for utilities to use.
                                             17

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2.2        Condition Assessment

Condition assessment may have a variety of goals including strategic, tactical, and operation and
maintenance (O&M), which determine the condition assessment implementation and affect the type and
accuracy of predictions required.

According to Commonwealth Scientific and Industrial Research Organization (CSIRO), there are two
types of condition assessment:
        •   Assessment of an individual pipe
        •   Assessment of a collection (cohort) of pipes.
An assessment of individual or short sections of the network is usually undertaken when there is a reason
to believe that the particular pipe is in a condition leading to its failure.  An assessment of a cohort of
pipes gives a general overview of the overall condition of a group of pipes and is often used in strategic
decision making. Additional information can then be used to develop the condition assessment to focus
on individual pipes. In either cohort or individual condition assessment, it is implicit that a condition
assessment be based on asset and failure data, which then dictate what procedures and locations will be
critically rated and prioritized for inspection and development of life predictions.

In the EPA's water infrastructure research plan (EPA, 2007), condition assessment is defined as the
collection of data and information through direct and/or indirect methods, followed  by analysis of the data
and information, to make a determination of the current and/or future structural, water quality, and
hydraulic status of the pipeline.  The primary research emphasis in this project is structural condition
assessment, as opposed to hydraulic or water quality condition assessment.

Condition assessment should be a structured and logical process. The need is to determine quantifiable
objectives and understand causes of deterioration, then quantify deterioration in order to reach a sound
understanding of the condition.

A comprehensive assessment can be viewed as a four-stage process:

        •   Stage 1.  Initial identification of physical characteristics of a pipeline in terms of historical,
           environmental, and operational data
           o   From this data identify and prioritize assets for condition inspection based on the
               consequences of failure
           o   Determine what information is required from an inspection program.  "If you don't know
               what you are looking for, you are unlikely to find it."

        •   Stage 2.  Evaluate the possible methods of inspection for their appropriateness and cost
           effectiveness to provide the required type and level of information.  Undertake an inspection
           using an appropriate technology

        •   Stage 3.  Carry out a final condition assessment based on the information from stage 1 and
           inspection to provide an assessment of the likelihood and consequences of failure. Bear in
           mind that inspection provides data, not assessment, and needs to be interpreted.
           Interpretation may include developing life expectancy curves and predictions of time to
           failure

        •   Stage 4.  A final stage should be to measure the success of the undertaking.
                                               18

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2.3
Condition Assessment - Risk and Prioritization
Risk is defined as the consequences of failure times the likelihood of failure. In any program of condition
assessment and prioritization, it is necessary to determine not only the likelihood, but also the
consequences of failure. This Risk Based Inspection (RBI) approach has been successfully used for some
years in the oil and gas industry. This is represented in Figure 2-1, which graphically shows the
combination.

The reality of water utility management, with limited resources, is that when the likelihood of failure may
be high but consequences are low, the cost of investigation may not be justified. For example, with a 4-
in. cast iron main in open ground in a rural area it will be more economical to repair any failure and
replace when an unacceptable level of failure is reached. Any condition assessment should include such a
risk evaluation, because it is a key factor in prioritization of investigation.
                                           Consequence of Failure
                    Figure 2-1.  Risk: Consequences and Likelihood of Failure
2.3.1       Consequences of Failure. The consequences of failure can be evaluated under three main
headings:
       •   Direct costs
       •   Environmental costs
       •   Socio-economic costs.
Each individual main can be assessed on the basis of these headings.  If the assessment to any of these
headings indicates a high impact and cost, then the main would have a high rating in terms of
consequences of failure.

Some of the factors that increase the consequences of failure are set out in Table 2-2.
                                              19

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                             Table 2-2. High Consequence of Failure
      Critical Customers                Critical Locations               Difficult Physical Factors
    Large populations           • Industrial/commercial/residential       • No alternative routes
    Government, defense sites    • Highways, bridges, tunnels, railroads,   • Large diameter lines
    Hospitals                    airports, subways                    • Difficult terrain
    Key industries              • Potential landslips                   • Heavy traffic
    Critical care individuals      • Water courses                      • Remote sites
                              • Areas prone to flooding              • No alternative water supply lines
   	• Major utility crossings	
A program under development by UKWIR called "Failure of Large Diameter Trunk Mains" is expected
to provide a flexible framework tool for utilities estimating this kind of risk.

2.3.2      Likelihood of Failure - Key Indicators.  In this section some of the key and secondary
indicators of likelihood of failure are reviewed. Four key indicators are critical in carrying out a condition
assessment and criticality review.  These are defined as three types of burst or break together with leakage
failure.  There are also secondary indicators that will modify the assessment.

It should be noted that there is no agreed definition of failure terms in the industry.  An on-going Water
Research Foundation/WERF project "Key Asset Data for Water Sector Utilities" (Project #4187) may
help address this problem.

The term "burst" is commonly used internationally for a structural failure, which makes the pipeline no
longer operable. The term "break" is sometimes used in the  same sense as "burst" but it has also been
used for a crack in the pipe where the pipe is still serviceable.

Burst/Break Failures

For all types of ferrous water mains, the most critical data set is the number of failures (or bursts and
breaks), their location, and the nature of the failure. Bursts could be further subdivided according to their
significance, as follows.

        •   Class A Failures have greater operational, environmental, and consequential impact and
           cannot be repaired routinely.  It is particularly important for the utility to carry out, in such
           cases,  as comprehensive an investigation and interpretation as possible.  Undoubtedly, it is
           difficult for a utility operator to distinguish between a corrosion and mechanical failure. In
           many cases both types of failure will be involved.  The larger the diameter of the pipe, the
           more important is the quality of the investigation.

        •   Class B Failures are considered routine pipe breaks and are repaired as they occur, usually
           for smaller diameter pipes and often involving circumferential breaks. Their impact is much
           less in terms of cost and environmental, operational, and consequential damage. It was noted
           earlier that circumferential breaks, predominantly in small pipes, represent a large percentage
           of structural failures.  Such breaks are often caused by excess stress due to factors like soil
           movement, external loading, and lack  of bedding support.

        •   Class C Failures are those that occur  due to third party activities and that fall outside the
           scope of likelihood evaluations. They are not easily predicted, although many Class C
           failures are avoidable if proper procedures are followed by third parties.
                                               20

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This failure information is most readily available from maintenance records and failure databases
developed by the utilities. It should be possible to identify the number, location, and type of breaks, as
well as repairs undertaken. Many utilities take the number of failures per mile as the only factor in
determining the likelihood of failure and the need to replace a pipe. This is a very common approach in
smaller diameters where the cost of structural investigation and assessment may be a significant
percentage of the replacement cost.

Leak Failures

Leak failures may be sub-classified  into:

       •   Joint and fitting leaks
       •   Pipe wall leaks.

Most leaks can be considered as defects as the line remains in service until such time as it is repaired.
Leaks in pipe walls can be important, because they are likely to indicate perforation in the pipe wall,
which in some mains is considered to lead to structural failure.  Stress raisers around the pitting create
high local stress leading to fracture.

An AwwaRF study "Leakage Management Technologies" examines the use of proactive leakage
management techniques in the U.K and assesses the practicality of applying them to North American
utilities (Fanner et al., 2007).  An upcoming Water Research Foundation report by American Water will
examine the application of continuous acoustic monitors placed throughout a distribution system
(Hughes, 2008).

Pipe Wall  Corrosion

Pipe wall corrosion indicators are considered in terms of direct data and by inference from environmental
conditions, particularly soil aggressivity. Knowing the extent of the metal loss will allow calculation of
the current beam and hoop strength and the factor of safety.

Investigation Data. The presence of corrosion in the form of pitting occurring internally and externally is
used as a basis for the likelihood of break and predicted life.  When inspection data on wall thickness,
such as wall thickness loss and pitting depths, are available,  this quantitative information can be used to
predict the  remaining pipe life based on the original pipe wall thickness and the age  of the pipe. A major
problem in the U.S. is that the availability and quality of data from U.S. utilities are  extremely variable,
and there is no common reporting standard, which makes comparison difficult.

The findings of a UKWIR study using data from a large utility set out in Table 2-3 may warrant further
consideration of the assumption for  cast iron pipes that failure will occur when a corrosion pit just
penetrates the pipe wall (UKWIR, 2000). It should be noted that corrosion holes only account for 14.3
percent of failures, and most of these failures are concentrated in smaller diameter pipes.  Some of the
findings of the study were:

       •   Cast iron pipes do not fail when graphitization just penetrates the wall.  It has been found that
           9 to 10 percent of random samples of pipes operating successfully had holes in the walls after
           shot blasting

       •   When penetration is through the pipe wall, a fracture analysis shows that there is insufficient
           stress concentration to cause cracking by internal pressure alone
                                               21

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           Table 2-3.  Number of Different Types of Failure in a U.K. Utility (1991-1997)
Size Range
(in.)
2 to 3
4 to 7
8 to 10
12 to 14
15 to 18
20 to 24
>24
Percent
Failure Type
Hole Fracture
1,022
3,152
156
70
17
3
29
14.3
5,947
17,237
449
226
226
15
88
77.0
(count)
Joint
232
678
53
55
55
5
61
3.7
Other
381
1,136
29
16
29
0
7
5.1
        •   Leakage in cast iron pipes after wall penetration does not always occur as graphitization
           product acts as a plug.

The UKWIR study findings need to be compared to the findings on the main failure mode for ductile iron.
This was identified not as general corrosion or graphitization, but as pitting attack (Rajani and McDonald,
1995). A study of 359 failures on 118 ductile iron water mains in U.K. suggested that pitting was the
primary mode of failure (De Rosa and Parkinson, 1986).  The pitting rate appears to be similar for all
types of ferrous pipe so that the wall thickness and external protection become key issues. An AwwaRF
study "The Effect of Corrosion Pitting on Circumferential Failures in Grey Cast Iron Pipes" focused on
small diameter pipes (Makar, 2005).  Spun cast iron pipes with pits larger than 1.6 in. in diameter were
vulnerable to failure.  Pit-cast iron pipes were vulnerable with pits larger than 0.8 in. in diameter.  The
thinner wall pipes were more prone to circumferential failure than thicker wall pipe. Large changes in
soil support were found to be an important factor producing substantial levels of bending stress.

Environmental Corrosion. Environmental corrosion applies to both external and internal pipe
corrosions. External corrosion is related to environmental conditions, specifically the corrosivity of the
soil.  It is necessary to use this information as a proxy to assess the likelihood of corrosion. It is important
that a utility populate a database with soil conditions in the area of its water mains.  However, natural or
man-made changes to the soil environment can create significant differences over the same pipeline. For
internal corrosion, there are only some broad indicators, such as aggressive water with low pH that may
signify internal corrosive conditions leading to pipe wall loss.  For both external and internal corrosion,
likelihood of failure will be modified by the type  of protection provided, taking into account any defects
or damage.

Soil chemistry is an indicator in screening for the likelihood of failure from external corrosion. Soil
chemistry and its potential for causing corrosion to ferrous material have been known for many decades.
It is recognized in numerous codes  and guides as  a key factor.  Soil chemistry is a particular concern for
pit-cast, spun-cast and some ductile iron mains installed without external protection..

The research  on corrosion to ductile iron pipe and the use of polyethylene wrap dates back to the early
1950s. Even  where corrosive soil is known to exist, the potential  for external pipe corrosion may, to
some extent, be discounted if the utility has taken precautions to protect the pipes from the aggressive soil
conditions. Protection measures include encapsulating in PE, external coatings and wrappings, and
cathodic protection.  In some cases retrospective protection has been provided.
                                               22

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2.3.3       Likelihood of Failure - Secondary Indicators.  Several of the indicators listed below are
not indicators of failure in the narrow sense but important factors in the nature and likelihood of failure.

Pipe Age

Pipe age is often used as a direct basis for making replacement decisions.  However, it needs to be placed
in the context of a rate of deterioration or corrosion in order to have a rational basis for replacement
decisions based on remaining service life.  Undoubtedly, older pipes have had more time to suffer various
forms of corrosion and stress. Older pipes may not have been designed for the stresses being imposed
today.  In addition, they have not been provided with the level of protection required on  more recent
installations.  Thus, if two pipes have been subject to identical environmental and operational conditions,
the younger pipe will have a longer life.  The problem is that identical conditions seldom occur and many
factors need to be considered when using age as an indicator for predicting remaining life.

Predicting failure  purely based on age could be misleading when one considers in detail  the causes and
complexities of failure. Some failures occur in the early life of a pipe due to manufacturing and
installation defects.

The variability in  service life is well illustrated in Table 2-4, which shows average remaining life in years
for ferrous water pipes  for a U.K. water utility for pipe sizes of 6-in. diameter and greater (UKWIR,
2001). These are  predictions from an analysis of condition data taken from pipes adjacent to a burst.
         Table 2-4. Average Remaining Life Predictions in Years for Ferrous Water Mains
                          Based on Period of Installation (UKWIR, 2001)
Diameter 1880 to
(in-) 1899
6
9
12 112
15
18
Avg. 112
RL(a) (yr)
Date Range of Installation
1900 to 1920 to 1940 to
1919 1939 1959
99
95
107


100
71
53
57
150
68
80
59
52
18
62

48
1960 to
1980
57
72
33
73

59
Avg.
RL(a)
(yr)
69
60
91
102
68
78
           (a) Average Remaining Life (Yr)

Certainly age is an indicator that can be taken into account as an adjunct to the key critical factors.  Age
can be a guide to the type of pipe in that dates for the introduction of spun-cast iron and ductile iron pipe
introduction are well established.

Pipe Diameter

As noted in Table 2-3, the number of failures is much larger for the smaller diameter pipes. This is the
result of a combination of greater installed lengths of small pipes, and a higher failure rate than the larger
pipes.  The predominant failure type, regardless of diameter, was found to be fracture failure with a much
higher number of failures at the smaller diameters. While most of the failures occur in smaller diameters,
the risk posed by single failure of a large transmission line can be very high due to the large amount of
damage and loss of service that can occur.
                                               23

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Pipe Thickness

The initial pipe thickness when installed is of importance.  This is taken as the calibration base point from
which loss of metal is calculated. Together with pipe age, this provides a theoretical rate of corrosion.
Variation in wall thickness can be large for cast iron pipe.  Pipe thickness can be found in contemporary
AWWA Standards that are used in procuring the pipe.

Type of Internal Lining

CML is the standard form of lining provided since the 1950s with most spun-cast iron pipes and all
ductile iron pipes.  It will provide internal protection unless damaged or deteriorated.  Pipe lining
rehabilitation methods are available and can extend pipe life if structural integrity is present or restored.

Joints

The type of joint used for ductile iron in trenches is predominantly bell and spigot push fit with an
elastomeric seal. These allow some flexibility for soil movement.

Spun-cast iron pipes also used this form of joint although earlier versions of cast iron pipes  (i.e., pit-cast)
can have lead and leadite joints.  Steel pipes have flanged and welded joints. Welded, lead, and leadite
joints cannot accommodate movement; any movement causes stresses  in the pipe.

Joint leaks occur due to improper installation and soil movement, so the indicator is not the joint but the
installation.  The exception is leadite joints, as  bell splitting has found to be associated with this type of
joints. Leadite is a plasticized sulfur cement compound that was used as an alternative to lead.  It was
found to be an inferior product to lead for two reasons. First, leadite has a different coefficient of thermal
expansion than cast iron and results in additional internal stresses that can ultimately lead to longitudinal
splits in the pipe bell.  Secondly, sulfur in leadite can facilitate pitting corrosion, resulting in
circumferential breaks on the spigot end of the pipe near the leadite joint. The failure rate for a leadite
joint pipe is significantly higher than that for a lead joint pipe even though the pipe may not be as old.
Therefore, for a leadite joint pipe, the indicator is the joint in conjunction with soil movement.

Location

Location and depth of cover can identify external loadings on a pipe. This information should be readily
available. It should include key features such as crossings of roads, rail tracks, waterways, depth of
cover, and other situations. A U.K. study showed that pipes laid under heavily trafficked roads had a very
high rate of failure, particularly in the colder months of November through February, although these are
thought to be circumferential fractures and mainly in smaller diameters (UKWIR, 2001).

Loading on a pipeline in practice is a combination of external loadings and internal pressure.

Installation Defects

A remarkably large number of defects in pipelines originate from the time of installation. Improper
bedding and badly made joints are examples.  Some failures appear shortly after installation but often
show up many years later as a structural failure. External corrosion resulting from improperly installed
polyethylene wrapping may not show for many years.  Experience and records will show up patterns that
build a picture on the good and the bad.
                                               24

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Potential Soil Instabilities

Soil instabilities can arise from various causes, including the soil type. A UKWIR study found that for
pipes in clay soils the annual rate of bursts was nearly twice that of pipes laid in chalk areas (UKWIR,
2001).  The study also concluded that the most likely cause of enhanced seasonal failures was the change
in clay soil volume caused by variations in moisture.

Examples of more extreme causes are seismic movements and locations where a pipeline is on or adjacent
to aslope.

An AwwaRF study of grey cast iron pipes found that changes in soil support were a major contributory
factor to circumferential failures (Makar, 2005).

Soil Temperature

Changing soil temperature is of particular concern in Northern regions where ground frost and the
freeze/thaw cycle can cause movement. Since high temperature can accelerate corrosion rates, it needs to
be considered in conjunction with soil aggressivity.  It should be noted that soil temperature is used as a
surrogate measure of water temperature which may be the actual cause of most breaks (see below).

A UKWIR study showed that circumferential fractures in pipe of smaller diameters (4 to 6 in.)
significantly increased in the months of November through January (UKWIR, 2001). No similar pattern
was present for longitudinal fractures. NRC published a paper on the influence of weather and burial
conditions on break rates and developed an empirical model for correlating break rates with climatic
changes (Kleiner and Rajani, 2002; 2004; 2008).

Groundwater Levels

Seasonal changes of groundwater level and those caused, for example, by tidal variations can contribute
to both soil instability and corrosive conditions. In sensitive clays, seasonal changes can cause heave and
shrinkage, resulting in significant pipe movement.

Pressure Changes

Transient pressure can be a significant cause of failures.  Some authorities consider that this can be the
most important cause of induced stress failures. The original design would be based on an operating
pressure with a maximum test pressure that would allow for surges and other intermittent pressure
variations. In the normal operating life, the pipe should be quite capable of working within this design
range.  However if there are surges or increases in operating pressures beyond those allowed in the
design, or that occur when the pipe has deteriorated, then there is a likelihood of failure.

Water Temperature Changes

Thermal stress due to changes in water temperature in the pipe has been found to be a contributory factor
to failure in some regions. When the water in the pipe becomes colder, especially near the maximum
density of water, it seems that pipes tend to break. This occurs when the water in a reservoir turns over in
the fall, and although soil temperature may still be well above freezing, pipes tend to break. Also, rapid
temperature changes seem to possibly be another secondary factor.

An overall summary of failure modes and indicators is given in  Table 2-5, as an initial attempt to provide
a set of indicators and ranking.
                                              25

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                         Table 2-5. Failure Modes and Indicators
Mode:







Causes of Structural Failures


Internal
Corrosion
(a Direct
Form of
Failure)


External
Corrosion
(a Direct
Form of
Failure)

Induced Stresses
(Often in
Combination with
Internal and
External
Corrosion)
Causes
Wall
Perforations
(Can be a
Subset of
Internal and
External
Corrosion)
of Leak




Joint
Failure
(a Defect)
Key Indicators
Break Failures
Leak Failures
Pipe Wall Corrosion
(Investigation Data)
Pipe Wall Corrosion
(Environmental
Conditions)
VC
NC
VC

c


VC
NC
VC

c


VC
NC
VC

VC


NC
VC
VC

VC


NC
C
NA

NA


Secondary Indicators
Pipe Age
Pipe Diameter
Pipe Thickness
Type of Internal Lining
External Protection
Joints
Location
Installation Defects
Soil Instabilities
Soil Temperature
Groundwater Levels
Pressure Changes
Water Temperature
Changes(d)
c
NC
C
VC
NA
NA
NC
C0»
NC
NC
NC
NC
NC

c
NC
C
NA
C(a)
NA
NC
£(»
NC
C
C
NC
NC

c
NC
NC
NA
NC
C
C
C(o)
VC
c
c
VC
c

c
NC
NC
C
c(a)
NA
NC
C(b)
NC
NC
C
NC
NC

C
NC
NA
NA
NA
VC
C
VC
VC
c
c
c
c

VC = very critical; C = critical; NC = not critical; NA = not applicable
(a)  Can be a positive indicator and reduce failure potential.
(b)  Damaged linings and external protection.
(c)  Defective installation.
(d)  Applying to cold regions only.
                                             26

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                    3.0 TECHNOLOGIES FOR CONDITION ASSESSMENT
Condition assessment methods can be classified as direct and/or indirect methods. Direct assessment
usually requires access to the inside or the outside of the pipe, including visual inspection, destructive
testing, and non-destructive testing (NOT). Indirect methods include the analysis of failure history,
leakage level, hydraulics, and soil properties.  Several AwwaRF reports provide a description of a number
of NOT with trials of prototypes (Dingus et al., 2002; Reed et al., 2004; Lillie et al., 2004). The WERF/
AwwaRF study "Condition Assessment Strategies and Protocols for Water and Wastewater Utility
Assets" lists 85 individual condition assessment tools and techniques (WERF, 2007).  The report "Non-
Destructive Testing of Water Mains for Physical Integrity" (AwwaRF,  1992) is outdated, and thus is less
relevant in view of the developments over the last 30 years.

This section provides the basic technologies and their applications together with observations on their
limitations and potential application to ferrous water mains.  Examples  of commercial technologies are
listed in Appendix A.

3.1         Visual Investigations

3.1.1       External Condition Inspection.  The visual judgment of an experienced utility engineer or
operator can have considerable value. Where pipelines are laid above ground, visual surveys play a more
important role in that the pipeline can be directly observed for evidence of coating damage, leaks, or other
defects. For buried pipelines, these can range from walk-over inspection of the surface along the line to
various forms of aerial surveys.  Aerial surveys are rare in the water industry but have been used in times
of drought to look for water leaks by noting unexpected areas of green vegetation.

The monitoring of a line by walk-over surveys is relatively common practice for many pipelines. It is
valuable in that it can give  a warning of some defect or problem such as leakage or ground movement.
However, as no direct observations of the pipeline can be made, it has limitations.

Opportunistic visual inspections when a pipe is exposed for maintenance or repairs can provide a great
deal of valuable information to an experienced engineer or technician.  Deb (2002a) offered a standard
data form that can be used for opportunistic visual inspection of a pipe when it is exposed for
maintenance or repairs.

3.1.2       Internal Condition Inspection Using CCTV. Closed circuit television (CCTV) is a well
known technique employed in gravity sewer mains.  The current generation of CCTV systems has
features that enable an operator to obtain useful information on the internal condition of a pressure main.
Key components include:

       •   Pan and tilt head
       •   Zoom lens
       •   Sonde
       •   Crawlers/tractors.

A CCTV inspection does not provide any quantitative information on the structural condition of the pipe.
The main purpose of such a survey would be to provide some visual indicators to possible defect
locations. Where a pipe has an internal lining, it will provide some qualitative information on the
condition of the lining.  It may also be possible to identify leaks from inward groundwater infiltration
when the pipe is empty.
                                              27

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In common with many other "internal" technologies, the main barrier in undertaking such inspections is
the need to gain access to the line, which may require temporary by-passing, shut down, dewatering,
cleaning and removal of pipe sections or fittings to allow a camera to be put into the line. The costs
associated with these support requirements will be many times the cost of the CCTV survey. Where a
line has to be closed down and emptied for maintenance or repairs, then the opportunity to carry out a
CCTV survey can be taken.

The Water Research Centre (WRc) in the U.K. has developed a CCTV capability based on the same kind
of launch system used for Sahara® leak detection, which is described in A.3.1 in Appendix A. The
camera is attached to a calibrated umbilical cable through which it transmits data in real time. In water
mains a drogue is attached which propels the camera through the line.  The cable also controls the speed
of movement of the tool and allows its retrieval. Color surveys of live water mains up to 2,500 ft from
the entry point are possible. The location of the camera can be detected from the surface using a
walkover tool so that the operator can mark the surface with the exact location. The operation of a
camera may be incorporated as a supplement to the Sahara® leak detection system

3.2        Pit Depth Measurements

A manual technique is widely used as a basis for obtaining a rate of corrosion by measuring pit depth.
Tools are widely available, portable,  and simple to use.

Although pit depth often is used as a key factor in calculating the remaining life of a water main, there
appears to be no standard method of measurement.  At least five different measurement methods can be
used, ranging from mechanical calipers and depth gauges to ultrasonic and electromagnetic techniques.

In field investigation a section of buried pipe is exposed in an excavation and a selection of pits that are
observed is measured. The number chosen for measurement varies among investigation companies. For
mechanical measurement methods, cleaning and preparation of pipe are required, which may be done in
different ways.

For laboratory testing of samples, the pipe is shot-blasted; in some cases the laboratory may take up to 10
random measurements. Other laboratories will take a given number of the largest pits that can be seen. It
is therefore difficult to interpret and compare utility databases on pit depth measurements, and it is normal
to find a large variation in results.

3.3        Destructive Testing

The most common practice is to retain, inspect, and test coupons of pipe wall in a laboratory; however
this is not routinely done in the U.S. and is highly variable among utilities. Core and coupons can be
taken from a ferrous pipe wall using drilling techniques, including pipes in service using pipe tapping
techniques. Some utilities performing non-structural rehabilitation will collect samples to confirm the
structural integrity of the newly lined pipe.

In addition, sections or length of pipe (cut outs) are removed for laboratory analysis. Gas distribution and
potable water utilities commonly undertake laboratory tests on samples.

The mechanical tests carried out include:

        •   Burst test
        •   Tensile test
        •   Ring test
                                              28

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        •   Fracture toughness test
        •   Four-point bending test.

The metallurgical tests include:

        •   Examination of the metal structure and properties
        •   Examination of fracture surfaces, inclusions and fracture pits
        •   Analysis of fracture surfaces and corrosion pits.

A full description of these mechanical and metallurgical tests can be found in Chapters 2 and 4
respectively of the AwwaRF study "Investigation of Grey Cast Iron Water Mains to Develop a
Methodology for Estimating Service Life" (Rajani, 2000).

3.4        Non-Destructive Testing

3.4.1       Sonic/Seismic Technologies. Sonic and seismic technologies generate mechanical waves in
a medium and measure the time taken for a reflected wave to reach a transceiver. This time can be
correlated to material thickness if the elastic response characteristics of the medium are known.

Ultrasonics measure the propagation time of high-frequency, short-wavelength mechanical waves through
a ferrous pipe wall, and correlate this with the nominal thickness of the material.  The detection of flaws
is based on the reflection of the wave from the interface between materials of different properties, for
instance graphite or a cement mortar lining.  The resolution is such that small areas of wall loss can be
identified, allowing the creation of a map of the wall thickness of a pipe. Ultrasonic waves are at
frequencies greater than 100 kHz, but accurate thickness measurements use frequencies in the order of 10
MHz.

External Applications of Ultrasonics

Ultrasonic measurements are among some of the best-established methods for simple  external testing of
points along a ferrous pipeline wall. The equipment is in the form of hand-held instruments where a
probe is positioned on the metal (see Figure A-l, Appendix A).  The tool is calibrated to provide a direct
thickness reading, which can then be compared with the original wall thickness.  These measurements are
point readings of the depth, and there can be substantial variations that are not detected between the
chosen points.

Ultrasonics performs best on steel and ductile iron, and less well on thicker grey iron.  Most ultrasonic
devices require direct contact with clean metal, which involves removal of coatings, linings,  and
corrosion products.

Because ultrasonic tools are inexpensive, they have become popular in-house inspection tools with some
utilities. However, operators still need to be properly trained and understand how the  tools work,
including their limitations, to avoid generating misleading data.

In-Line Investigation Ultrasonic Pigs

The ultrasonic principle is used in intelligent pigs that have been developed for in-line inspection (ILI) of
oil and gas pipelines. The tools directly measure the wall thickness as they travel through the line. They
are equipped with transducers that emit ultrasonic signals perpendicular to the surface of the  pipe. These
transducers are located in a carrier that covers the internal circumference. Typically the spacing will be
                                               29

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every 8 mm circumferentially and 3 mm longitudinally. An echo is received from the internal and
external pipe surfaces.  By timing these return signals and comparing them to the speed of ultrasound in
steel pipe, the wall thickness can be calculated.

Using ultrasonics in-line requires good contact with the pipe wall to obtain an accurate response.
Typically the contact medium is a liquid.  This contact, or coupling, is usually sufficient for liquid-
carrying pipelines. This method  may be impractical in tuberculated mains and potentially compromised
in lined pipes.

It should be noted that the tools used in the oil and gas industry are not suited technically or economically
to the inspection of water mains.  Various laboratory developments have been reported and prototypes
have been built.  However, a commercial proven tool is not thought to be available.

3.4.2        Guided Wave Ultrasonic Testing.  Guided wave ultrasonic testing (GWUT) has the
potential to inspect portions of pipes with continuity from accessible locations.  GWUT uses the pipe wall
as a conduit for the ultrasonic energy.

Guided wave pipe inspection technology was developed for external remote detection. The concept is to
generate ultrasonic Lamb waves and send them along a pipe using one of several transducer types.
Discontinuities such as corrosion give a differing reflection back to the transducer, which is able to
measure and determine the size of the defect.  A guided wave propagation and reception collar is mounted
on the outer surface of the pipe.  This transmits and receives ultrasonic pulses around the full
circumference of the pipe. Losses of wall thickness can be  identified and mapped. To date tools that are
commercially available have been used in the process, oil, and gas industries on pipes with welded steel
joints that provide the continuity. The diameter ranges from 2 to 48 in.  Typically, the length of pipe that
can be scanned depends on pipe condition, coating, and type of soil with maximum distance  in the order
of 100 ft.  It works for pipes that  are insulated or coated.  It is particularly useful for buried steel pipelines
and road crossings.

Trials of guided wave systems on steel mains are described in an AwwaRF report, "Techniques for
Monitoring Structural Behavior of Pipeline Systems" (Reed et al., 2004).

3.4.3        Electromagnetic Methods. Several technologies are based on electromagnetic  principles,
but all  are variations on two: magnetic flux leakage (MFL)  and eddy currents.  They are applicable to
ferrous pipes, or pipes with a ferrous component.

Magnetic Flux Leakage

When a magnet is placed next to  a pipe wall, most of the flux lines pass through the pipe wall. That is,
the pipe wall is a preferred path for the flux. While most of the flux lines concentrate in the pipe wall, a
few pass through the surrounding media.  Flux leakage at a metal-loss region is caused by a local decrease
in the thickness of the pipe wall.  At a metal-loss region, the flux carried by the thin section is less than
that carried in the full wall. Flux leaks from both surfaces of the pipe.

A sensor positioned on the inside (magnet side) of the pipe  is typically used to measure the magnetic field
adjacent to the pipe wall. At a metal-loss region, a sensor records a higher flux density or magnetic field,
which indicates the presence of an anomaly. In this manner, an MFL tool detects an anomaly that causes
flux to leak. The measured leakage field depends on the radial depth, axial length, circumferential width,
and shape of the anomaly, as well as the magnetic properties of the nearby material. To characterize the
anomaly, the measured leakage field must be analyzed.
                                               30

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MFL is the most commonly used inspection technology for oil and gas pipeline inspection. Numerous
inspection companies provide services, but these tools are not suited to "pigging" of water mains.

MFL tools detect and characterize metal loss from corrosion, one of the most common causes of ferrous
pipeline failures. As currently used, though, MFL tools cannot detect all metal loss or reliably detect
other defects such as axial cracking. High resolution and extra high resolution tools can provide
improved detection capabilities.

Eddy Currents

When an energized coil is brought near the surface of a metal component, eddy currents are induced in
the specimen.  These currents create a magnetic field that tends to oppose the original magnetic field. The
impedance of a coil in close proximity to the specimen is affected by the presence of the induced eddy
currents in the specimen.  When the eddy currents in the specimen are distorted by the presence of flaws
or material variations, the impedance in the coil is altered.  In effect, the eddy currents act as  a shield, and
defects reduce the eddy current shield.

These induced eddy currents are the key to defect detection.  Defects block and distort their preferred
flow patterns.  This change is measured and displayed in a manner that indicates the type of flaw or
material condition. Cracks at right angles to the current path interrupt the  surface eddy current flow and
are detected.  Cracks lying parallel to the current path will not cause any significant interruption and may
not be detected.

Skin effects limit conventional eddy current inspection techniques to inspection of only the surface
nearest to the probe.

One  eddy current technique, the remote field eddy current (RFEC), is capable of inspecting the entire wall
thickness without the need to use ultra low frequency. An  exciter that is sized to nearly the same diameter
as the inside diameter  of the pipe, is driven with a low-frequency sinusoidal current. A small, magnetic
field sensor is positioned some distance away. One portion of the magnetic field generated by the exciter
travels down the inside of the pipe, with the field directly coupled to the sensor.  A second portion of the
alternating magnetic field propagates through the material of the pipe, inducing eddy currents as it goes.
Once the magnetic field penetrates the outside wall of the pipe, it spreads along the surface of the pipe
and re-enters the pipe, again inducing eddy currents to flow in the pipe material. This second path is
referred to as the remote path. The total magnetic field and eddy current flow at any point is  the
combination of directly coupled and remotely coupled fields.

Several RFEC tools are in commercial use for ferrous pipeline inspection.

Eddy current technologies have some inherent limitations:

       •   Frequency - most systems are frequency dependent or have a limited number of frequencies
           in their operating range. This limits the detectability of material thickness variations

       •   Size and shape of sensors - the transmitter and receiver size and shape affect the operational
           frequency, so antenna configuration is not easily altered to suit survey  configurations.

3.4.4      Radiographic Testing. Radiography is a non-destructive test method that can be used on
ferrous pipes.  Radiography shows changes in thickness and density that are associated with corrosion. It
has been used widely in petrochemical processing plants and outside the U.S. on water mains. It has
                                               31

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technical limitations in that pipes of 15 in. inner diameter and greater must be emptied. It also has
considerable health and safety issues.  Radiographic testing is expensive and requires specialist operators.
3.5
Environmental Testing
The soil, water table, and pollutants can create conditions leading to corrosion of unprotected ferrous
pipe. Soil environments are not all corrosive to ferrous pipes, and even in moderately corrosive soils the
rate of corrosion may be such that the pipe will have a service life of more than 100 years. All types of
ferrous pipes can suffer potential damage from contaminated soils.

Due to the lack of better indicators of corrosion, the soil environment evaluation is currently the best
approach to evaluating external corrosion for unprotected pipe. Table 3-1 provides a summary  of
indicators and criticality ratings  for soil environment data.
                   Table 3-1. Indicators and Criticality from Environmental Data
             Indicator
                   Criticality
Comments
        Soil Resistivity             High

        Soil Moisture Content       Low

        Soil pH                    High

        Chloride Ion Content      Medium



        Sulfate and sulfide        Medium


        Redox Potential            High
       Known Corrosive           High
       Environments

       Soil Temperature           Low
        Groundwater Levels       Medium
       Potential Soil             Medium
       Instabilities
                                A function of soil moisture, temperature, and
                                concentrations of ionic soluble salts
                                Soils with moisture content greater than 20% considered
                                more corrosive
                                Likelihood of corrosion increases in acid soils with pH
                                values of 4.5 and less
                                Use of de-icing salts on paved surfaces can lead to high
                                concentrations of chloride ions in trench.  Where
                                concentrations are in the range of 10 to 1,000 ppm there is
                                an increasing potential for corrosion
                                Presence of sulfide in waterlogged soils indicates that
                                bacteria have been promoting reduction of sulfate ions and
                                indicates MIC activity
                                Redox potential is an indicator of degree of aeration in
                                soil.  A high level is an indicator of aerobic soil and
                                increase potential for corrosion.  A low negative redox
                                potential is an indicator of anaerobic conditions and
                                potential for SRB and  MIC forms of corrosion
                                Experience indicates that some soils and site conditions
                                are corrosive regardless of testing. These include polluted
                                sites, cinders, landfills, and peat bogs
                                Changing soil temperature is of particular concern in
                                northern climates where ground frost can cause
                                movement.  High temperatures can accelerate corrosion
                                rates
                                Groundwater levels need to be recorded including
                                seasonal changes. Those caused for example by tidal
                                variations can contribute to both soil instability and
                                corrosive conditions. Constant high groundwater level
                                can create anaerobic conditions
                                Soil instabilities can arise from various causes including,
                                for example, seismic movements and locations where a
                                pipeline is on or adjacent to a slope or subject to man-
                                made vibration, such as subway, rail line, heavy vehicle
                                traffic
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Various researchers have tried to establish a direct correlation between soil properties and corrosion
measurements.  The aim is to predict the size of a corrosion pit over time from the estimated corrosion
rate, the known soil properties, and the size of the pit as measured at inspection. However, this work has
not been conclusive. Although external corrosion is influenced by soil environment, the particular
properties and how they govern this behavior are debatable.

For example, it has been shown that the "average corrosion rate" does not reflect the process as the
maximum pitting rate is high and then falls,  so it is not a constant. Another problem lies in changing
environmental conditions that can change the soil properties.

Although internal water quality has no bearing on external corrosion, there is some evidence that the
treatment of water by chlorination and oxygenation is a potential cause of internal corrosion in unlined
cast iron pipes.

The National Association of Corrosion Engineers (NACE) Corrosion Basics provides a table for soil
resistivity vs. degree of corrosion (NACE, 1984).

American National Standards Institute (ANSI)/AWWA C-105/A21.5 provides a 10-point system for
evaluating the likelihood of corrosion deterioration.

DIPRA has a Design Decision Model (DDM) (DIPRA, 2005), which uses a 10-point system for
likelihood of corrosion and uses the same basis of environmental factors as the ANSI/AWWA Appendix
A.  It is intended for new design, but the same considerations can be applied to evaluation of existing
installations.

A discussion of soil tests and corrosion is presented in "Investigation of Grey Cast Iron Water Mains to
Develop a Methodology for Estimating  Service Life"  (Rajani, 2000).

Some key points that arise from this research are of importance in evaluating likelihood of failure.

       •   The growth of corrosion pits is time dependent and depends to a large degree on the
           surrounding soil and its properties

       •   The rate of pitting is higher early in the life of a pipe and then falls

       •   There is no single dominant soil property that appears to govern corrosion

       •   Low values of saturated soil resistivity appear to be directly related to high rates of corrosion.

The conclusion was that the predicted pit depth was a function of

       •   Time (exposure period)
       •   Pipe diameter
       •   Chloride content
       •   Soil sulfide content
       •   Soil redox potential
       •   Saturated soil resistivity
       •   Liquid limit for soil.

The correlation between pH and pitting  corrosion was shown to be weak and is not included in the
analysis. A mathematical analysis using these factors showed a moderate correlation (mean error 45
percent) between predicted and actual pit depths.  However, American Water observed external corrosion
                                               33

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on polywrapping ductile iron pipes in areas affected by acid mine drainage (causing low pH soil) and
employed polyethylene pipe instead (Hughes, 2008).

3.6        Leakage Management

3.6.1       Overview of Leak Management.  The International Water Association (IWA) has suggested
that there are four key tasks in leakage management:

       •   Pressure Management
       •   Leak Detection
       •   Leak Repair
       •   Pipeline Replacement.

The focus of the Forum was on the first two tasks.

Leakage management in North America has been mainly reactive by responding to identified leaks and
from information obtained from water loss audits.  To date there has been no regulatory pressure, but
drought and limited water resources are increasing political, economic, and environmental concern to
reduce leakage. In some countries, such as the U.K., water utilities are subject to government regulation.
This has provided the incentive to develop pro-active approaches such as leak management and improved
leak detection methods. Leak management based on District Metering Area (DMA) has been used by the
U.K. water utilities as a basic approach for over 10 years and covered most of the national network.  A
DMA is an area of between 500 to 3,000 connections into which water can be measured and analyzed to
determine the level of leakage.

A recently published AwwaRF report titled "Leakage Management Technologies" addresses the use of
leakage management methods  (Fanner et al., 2007). This report has three objectives:

       •   Review proactive management techniques used internationally
       •   Assess the applicability of these techniques to North America
       •   Provide guidance on how to practically and cost effectively apply these techniques.

The report highlights the importance of understanding the nature and extent of their water losses in order
to develop the best water loss management strategy.  The study found that a water audit can provide  the
necessary information on the level of losses.  DMAs are recommended to facilitate the identification of
areas of probable leakage and focus leak detection surveys. Pressure management was identified as  being
important in reducing the flow rate of hidden breaks and short term break frequency.

A more detailed description of flow metering, logging, and analysis of the data is presented in
"Technology and Equipment for Water Loss Management" (Farley, 2007).

Pressure management has been identified  as an important measure for the long-term reduction of real
losses. The principle behind pressure management is quite simple - lower system pressures during
periods of lower demands (when system pressures normally rise) and reduce the flowrate from the
existing background leakage (those small  weeping leaks from fittings and joints). An additional benefit
of pressure  management is the potential reduction in water main break frequencies, which in turn helps to
extend the life of the pipeline.

3.6.2       Leak Detection Technologies.  Leak detection uses a variety of methods including acoustic,
acoustic with correlation, infrared thermography, chemical (using a tracer gas), and mechanical (Smith et
                                              34

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al., 2000). Acoustic leak detection is the most widely used method.  Since the beginning of the 21st
century, a number of new leak detection technologies have been developed, including ground penetrating
radar (GPR), combined acoustic logger and leak noise correlator, digital correlator, and radio-frequency
interferometer (Pilcher, 2003). One of the recent advances is in-line leak detection systems, such as the
Sahara® and SmartBall® acoustic systems. Selected leak detection technologies are described below.

External Leak Detection

External technologies fall into two groups: acoustic and correlators.  The former works on the basis of
directly locating the noise of a leak; in its most effective form, it entails the use of a monitor brought in
contact with the main to listen for leakage noise. Other monitors, called hydrophones, do not come into
direct contact with the pipe, valves, or hydrants but are placed over the location of the pipe. There have
been numerous acoustic and electronic advances to improve the capability of "stick sounding."

Correlators are based on the velocity of sound made by a leak as it travels along the pipe wall between
two hydrophones or similar sensors.  The sensors are situated at convenient locations on the pipe some
distance away from, and on either side of, the leak point. The difference in time taken for the sound to
travel to each sensor allows the difference in path length to be calculated, from which the leak position
can be identified.  It has long been recognized that correlators are not as effective on large-diameter
transmission mains.

A recent advance in external technology is the deployment of monitoring units designed to monitor
acoustic noise over extended time periods including permanent installations. There are several variations
in these systems. Some units provide data by downloading to mobile receivers that stop or pass nearby
the monitors. Others are linked to automatic meter reading (AMR) networks that transmit data to a base
station or website.  Some systems are connected to water service lines while others are connected to the
top of valves.

In-Line Leak Detection

One of the most recent valuable leak detection developments has been "In-Pipe  Technology."  Leaks can
be detected by passing a hydrophone through the interior of the pipe to the point where the leak noise
signal is detected. As the hydrophone travels through the pipe it can only be a maximum of one pipe
diameter away from the leak, so even small leaks can be detected.

Commercially available tools  include Sahara® and SmartBall®. Sahara® is a single hydrophone attached
to a calibrated umbilical cable that can detect and locate leaks, in real time, as it travels through the
interior of the pipe.  SmartBall® is a free-swimming foam ball with an instrument-filled aluminum alloy
core that records acoustic activity to identify leaks as it moves along the pipeline.  Both are described in
Appendix A.

Ground Penetrating Radar

GPR technology has been adapted for leak location. GPR uses electromagnetic wave propagation and
scattering to locate and identify changes in the electrical and magnetic properties in the ground.  It is the
ability to detect differences in the density and water content of soils that allows GPR to be used as a leak
detector.

It is used in South Africa on a daily basis for leak detection. It is used frequently as a rapid
reconnaissance survey tool by attaching an array of antennae to a vehicle and driving the pipeline route.
This kind of survey can cost around $500 per mile for a long transmission line.
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However, as with all GPR investigations there are limitations depending on soil conditions, surface
pavement, and other underground structures in urban areas, and the use and data interpretation require a
high level of skill and experience.

Radio Frequency Interferometry

This technology uses a radio-frequency interferometer that transmits low power, ultra high frequency
(UHF) radio waves into the ground. The signal is reflected from the leaking water back to the antenna.
The signal is amplified and processed by a sensitive interferometer system, which ignores signals that do
not change with time but identifies rapidly changing signals that can be displayed to show strength and
character.

Infra-Red Thermography

Infra-red thermography is used to detect leaks in pipelines and the voids around them. High-resolution
temperature measurements made by infra-red cameras show variations in temperature in a pipe wall.  The
method is frequently used from aircraft over-flying long and remote pipelines; it is fast and provides
instant feedback on-site. The pressure drop at a leak point and the plume of leaking fluid in the
surrounding soil both show measurable temperature changes. It has been used for leak surveys on less
accessible water mains.

3.7        Summary of Inspection Methods and Applications

Tables 3-2 through 3-4 present summaries of the current inspection methods and applications discussed
above. More information on the technologies is provided in Appendix A.

For external technologies, if the pipe is not exposed, it will be necessary to excavate inspection pits.
                                              36

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      Table 3-2.  Tools and Technologies for Inspecting Structural Integrity Externally
Application
Grey Cast Iron
Ductile Iron
Steel
Diameters
Typical Length Scanned
Line in Operation
Scan through
Coatings/Wrappings
Loss of Metal
Pit Depth
Graphitization
Cracks
Mobilization Costs
Scanning/Processing Cost

Suitable for Water Main
Investigations
Pit Depth
Measurement
Yes
Yes
Yes
Any
3-6 ft
Yes
No

No
Yes
No
No
Minimal
Low

Yes

Ultrasonics
Yes
Yes
Yes
Any
3-6 ft
Yes
No

Yes
No
No
No
Low
Medium

Yes

Guided
Wave
Ultrasonics
No
No
Yes
2-48 in.
300ft
Yes
Yes

Yes
No
N/A
Yes
Medium
High

No

MFL
(ECAT)
Yes
Yes
Yes
6 in. and up
3-12 ft
Yes
Yes

Yes
No
Yes
Yes
Medium
Medium

Yes

BEM
Yes
Yes
Yes
2 in. and up
3-12 ft
Yes
Yes

Yes
N
Yes
Yes
Low
Low/Medium
a)
Yes

BEM = Broadband Electromagnetic; ECAT = External Condition Assessment Tool; MFL = magnetic
flux leakage
See Appendix A for more detailed information.
(a) Real time provides immediate structural condition without further processing. Full data processing
   is an additional cost.
      Table 3-3. Tools and Technologies for Inspecting Structural Integrity Internally
Application
Grey Cast Iron
Ductile Iron
Steel
Diameters
Typical Length Scanned
Line in Operation
Scan through Linings
Loss of Metal
Pit Depth
Graphitization
Cracks
Mobilization Costs
Scanning /Processing Cost
Suitable for Water Main
Investigations
In-Line
Ultrasonics
No
No
Yes
Most
Miles
Yes(a)
No
Yes
No
Yes
Yes
Very high
High
No

In-Line
MFL
No
No
Yes
Most
Miles
Yes(a)
No
Yes
No
No
No
Very high
High
No

RFT
"See Snake"
Yes
Yes
Yes
Up to 14 in.
10,000 ft
Possibly
Possibly
Yes
No
Yes
Yes
Medium
Medium
Yes

BEM
In-Line Pig
Yes
Yes
Yes
6 in. and up
3,000 ft
No
Yes
Yes
No
Yes
Yes
Medium
Medium/high
Yes

      BEM = broadband electromagnetic; MFL = magnetic flux leakage; RFT = remote field
      technology
      See Appendix A for more detailed information.
      (a) For oil and gas pipeline.
                                            37

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                  Table 3-4. Tools and Technologies for Leak Inspection
Application
External/Internal
Grey Cast Iron
Ductile Iron
Steel
Diameters
Typical Length
Scanned
Line in Operation
Joint Leaks
Wall Perforation
Leaks
Accuracy for
Locating Small
Leaks
Insertion into Line
Mobilization Costs
Scanning/Processing
Cost
Suitable for Water
Main Investigations
Leak
Correlators
External
Yes
Yes
Yes
Most
300ft
Yes
Yes
Yes

Good

N/A
Low
Low
Yes

Listening
Sticks
External
Yes
Yes
Yes
Most
3ft
Yes
Yes
Yes

Fair
(supplement
with
correlator)
N/A
Low
N/A
Possible

Continuous
Acoustic
Monitoring
External
Yes
Yes
Yes
16 in. and less
300-500 ft
Yes
Yes
Yes

Fair
(supplement
with
correlator)
N/A
Low
Medium
Yes

Sahara®
Internal
Yes
Yes
Yes
from 12 in.
up to 6,000 ft
Yes
Yes
Yes

Excellent

via 2-in
tapping
Medium
Low/Medium
Yes

SmartBalf
Internal
Yes
Yes
Yes
24 in. and up
Several miles
Yes
Yes
Yes

Excellent

via valve or
tapping
Low
Low/Medium
Yes

See Appendix A for more detailed information.
                                          38

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                      4.0 APPROACHES TO CONDITION ASSESSMENT
4.1        Condition Assessment Basics

In condition assessment it is necessary to have a logical and robust basis for estimation of the likelihood
of failure for the range of assets in the network. Where there is a significant amount of data, in particular
break data, the likelihood of failure can be assessed using statistical techniques. Where there is no failure
history, the approach needs to be modified.

Historical, environmental, and operational data can be used to:

       •   Provide an overall screening tool for an evaluation of a water main and focus field
           investigation activities

       •   Predict failure without use of structural integrity investigation.

The key to  screening for likelihood of failure is to have a structured database or inventory that is
constantly updated, can be interrogated, and records the full data on the pipeline, its surroundings, and its
operation.  There are programs of condition assessment developed for water utilities that provide
guidance on developing and operating an appropriate database. If the database can be based on a
Geographic Information System (GIS), it becomes more useful and effective.

Equally important, a likelihood of failure analysis should provide a sound basis on which to develop a
cost-effective investigation program. This allows a utility to focus its site investigation not only in terms
of where but also of how, when, and what to investigate. Such an investigation program needs to
supplement and fill the gaps in the information available from historical, environmental, and operational
data.  Thus, data gaps need to be identified before embarking on an investigation program so that the
investigation is focused on the data required.

In the American Petroleum Institute (API) Recommended Practice for Risk Based Inspection (API, 2002),
an important point is made that is relevant to the development of any program. The document explains
that a risk-based inspection (RBI) can be based on qualitative data, quantitative data, or a mixture of the
two. Quantitative risk analysis requires hard data that can be used to calculate, for example, the
anticipated remaining life of a pipe.  The data set needs to be comprehensive for the line under
consideration and the methods used in the calculation need to provide answers that conform closely to
actual performance. For much of the water network, utilities do not have either the comprehensive data
or performance records that allow them to use quantitative risk approaches.

Therefore, it is necessary to rely heavily on qualitative data, which involves inputs based on engineering
observation, judgment, and experience as the basis for determining likelihood of failure. Where it is
possible to  obtain measurable data such as pitting depth or metal loss in the wall of a pipe, such data will
be a major contributor to that judgment. Likelihood judgments and criticality rating are not given as
mathematical answers, but rather in qualitative terms such as high, moderate, or low or some comparative
numerical value.

A consensus has emerged that RBI that considers the consequences and likelihood of failure is the
preferred approach. Figure 2-1 from Section 2 illustrates this approach. The Global Water Research
Coalition (GWRC) is leading  an international project "Tools for Risk Management" that uses this
approach. This project is one element of Track 4 of the Strategic Asset Management (SAM) initiative, as
described below.
                                               39

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There is a multitude of papers and programs on the subject of condition assessment, including the
following studies published by AwwaRF that cover ferrous pipes:

       •   Risk Management of Large-Diameter Water Transmission Mains (Kleiner et al., 2005)

       •   Assessment and Renewal of Water Distribution Systems (Grigg, 2004)

       •   Prioritizing Water Main Replacement and Rehabilitation (Deb, 2002a)

       •   Investigation of Grey Cast Iron Water Mains to Develop a Methodology for Estimating
           Service Life (Rajani, 2000)

       •   Quantifying Future Rehabilitation and Replacement Needs of Water Mains (Deb, 1998).

A specific and very comprehensive  study running to several hundred pages is the WERF/AwwaRF
"Condition Assessment Strategies and Protocols for Water and Wastewater Utility Assets" (WERF,
2007). This study has now been incorporated along with others into an overall SAM Challenge program
involving WERF, Water Research Foundation, and several international associations and agencies. Three
of the tracks being pursued are of relevance here:

       •   Track 2: SAM Benchmarking and case studies
       •   Track 3: Decision support tools
       •   Track 4: Prediction of remaining asset life.

Each track has several embedded research projects.

4.2         Condition Assessment and Likelihood of Failure

The whole purpose of collecting data from inventories, records, observations, and inspections is to use the
information to make an assessment of the current condition of the asset. The second aspect based on this
assessment is to determine the likelihood of failure and predict the future structural condition and life
expectancy. A third use is to prioritize inspection where additional data are needed.

A key element of effective asset management is a cost-effective approach for assessing condition
assessment and performance.  The demand will differ greatly between utilities according to size and
outcome required.  Many programs  have been developed in order to meet regulatory requirements.

The uses and  needs of utilities for condition assessment vary, and approaches can range from simple in-
house evaluations to sophisticated programs operated by specialists.

4.2.1       Relative Criticality. Determination of the relative criticality of mains and a priority ranking
is undertaken using experienced judgment or some  more structured approach. Criticality should  begin
with water customer considerations  such as interruptions of water supply that are life threatening (e.g.,
kidney dialysis), impact on a large number of customers, industrial or commercial commerce, or
disruption of transportation.  Other ranking considerations can include:

       •   Ranking of sections for inspection
       •   Ranking of structural concern
       •   Ranking of operational  concern
       •   Ranking of critical concern sections.
                                              40

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4.2.2       "Belief Networks".  Bayesian theory defines probabilities as "reasonable degrees of belief."
Probabilities are assigned to propositions based on beliefs gained from observations. The probabilities
are conditional based on the state of the variables.

In reality, it is a structured application of expert knowledge and experience to the available information
and observation. Many engineers and operators use this approach instinctively in making their
assessments.

A sophisticated version of Bayesian "Belief Networks" is "Sewer Cataloguing, Retrieval and
Prioritization System" developed for WERF (WERF, 2004).  This is a computer-based expert system for
identifying pipelines at risk of operational and structural failure, and takes into account consequences of
failure.  Although developed for wastewater, it is relevant and adaptable to potable water and many other
assets.

A simpler version has been developed by Jason Consultants, which is aimed at small to medium utilities
that have need for a tool that can be used by their own staff.  A "Relative Criticality Ranking" of large
diameter water transmission mains was developed for a major U.S.  city using this technique.

The technique is used to provide a rating both for likelihood and consequences of failure.  Supporting
detailed "Belief Networks" are developed to provide the information for this overall network (see
Figure 4-1).
                Figure 4-1. Overall Belief Network - Likelihood and Consequences


4.3        Life Cycle Curves

The "Bathtub Curve" is a widely accepted conceptual representation of a pipeline life cycle.
                                               41

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Figure 4-2 shows such a curve.  There is an early high premature failure due to defective design, material
or workmanship.  This is followed by a long period of low failures and moves into a higher rate of
failures as the pipe reaches its effective service life.

*
Pipeline Design Service Lie
4 Def med cy
* Reliable Product
i

,Pr em store Fa
• Defaces Prod
I* Harsh Environ
* External Load!
\
\
\

*
\
* \
\
N
*m
* Rangs ef Leadings
• Rang^ d" Ervironm0nls
lure
JCt
nen!
9


Plpelkw Bfective
Sorviri: Lfc





OeerationalLinl
OerinMty
* Actual Pressure Load
• Actual &(tsrnaS Load
• Actual Cofro&*Qp Rate

CrSical Section .--V
Bfectiwe Serwice Life ""„
Critical Section t .
DE sign Service Life '.-''












I

1
. End of Life J
• Des^n Uml 1

I

I
1
I

t
/
j
*

                                  Service Life - years
           Source: Wayman, 2003.

                            Figure 4-2. Life Cycle of Typical Pipeline
What is of interest is the effective service life, which can be much greater or sometimes less than the
design life.  It is worth noting the factors that determine the effective service life by operational limit,
which are:

        •   Actual pressure load
        •   Actual external load and other pipe stresses such as thermal stresses
        •   Actual corrosion rate.
4.4
Residual Life - Life Predictions, Modeling, and Life Expectancy Curves
It has long been the aim to find a means to accurately predict when a pipe will fail.  The determination of
residual life depends on many factors; interpreting these to reach a residual life that corresponds with
operational experience is challenging. Predicting future performance is based on past performance and
there are considerable variations in experience between utilities due to different local conditions.

4.4.1       Life Predictions. Pit depth measurement is a widely used method for inferring the residual
life of a ferrous water main.  The rate of corrosion is based on combining maximum external and internal
pit depths together with the pipe age and original thickness.  A linear rate of corrosion is assumed when
the pit or pits will fully penetrate the pipe wall and this is then taken to be the time of failure.  ASME B31
code provides guidance on determining the remaining strength, but not on pit depth measurement
(ASME, 1991).
                                               42

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This approach has several weaknesses:

        •   It can be difficult to determine the true age of the pipeline

        •   It can be difficult to determine the original pipe wall thickness

        •   The way pit depths are measured is not a standard procedure

        •   Pit depth sampling is very random and pitting is very variable along a pipeline so that it is an
           act of faith to assume the pit depths recorded represent the worst case

        •   Internal pitting is very difficult to identify and measure in a pressure main

        •   Pitting in coated pipelines may start after failure of the coating

        •   It has been observed that the rate of pit corrosion is not uniform and tends to slow down over
           time.

Utility experience has shown that such predictions can significantly underestimate or overestimate the
service life.  The reality is that isolated pit penetration which can lead to leakage is not a major cause of
pipe burst failure (UKWIR, 2001).  Only if an area becomes weakened by a group of pits is it likely to be
an important contribution to failure. It has been noted earlier that grey cast iron pipes continue to
function even when full wall penetration has occurred.  However, in ductile iron it becomes a more
frequent cause of failure.

Various attempts to improve the reliability of life  predictions have been developed.  For example, when
the extent and depth of pitting can be compared with a database of various types of pitting in pipes of a
similar age and type, then it becomes more meaningful. CSIRO developed a failure model that takes into
account variations in corrosion rate, the resistance as the pipe corrodes, and the applied service loads.

New York City Department of Environmental Protection (NYCDEP) is currently undertaking non-
destructive evaluation and development of an asset management system for wastewater force mains.
They developed an asset inventory database first,  including a standardized reporting tool.  In order to
develop a structural rating, a detailed finite element analysis was conducted on typical mains. This has
resulted in Table 4-1, which defines the level of defect and action.
            Table 4-1. Structural Condition Ratings for Force Mains (after NYCDEP)
Defects
Cracks, breaks, significant change in cross
section, bending deflection > 4 mm for CI, >
0.06D for DI and 0. ID for lined DI
Greater than 75% loss of wall thickness at any
cross section, noticeable sag or change in
cross section
Wall thickness loss between 50-75%
Wall thickness loss between 25—50%
0—25% wall thickness loss
Condition
Failed; immediate action required
Severe damage; preventive action required
Moderate damage; preventive repair planned
Small damage; preventive repair on basis of
remaining service life
Minimal damage; no immediate action required
Ra
5
4
3
2
1
CI = cast iron; D = diameter; DI = ductile iron
                                               43

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Although this analysis was for force mains, it has a relevance to ferrous pipes in the water network.

4.4.2       Modeling. Modeling is used to assist utilities in a wide range of infrastructure situations.
Models can be used to provide indications of the overall network picture as well as detailed structural
evaluations at a zonal level (McKellar, 2006).  A specific example of this approach is the "Burst
Consequence" model developed by Thames Water.  This identifies where flooding would occur if there
were a burst and the financial consequences (Blakey, 2001).

A paper "Comprehensive Review of Structural Deterioration of Water Mains: Statistical Models"
provides an overview of work carried out in the past 20 years to quantify the structural deterioration of
water mains by analyzing historical performance data (Kleiner and Rajani, 2001). The authors consider
the physical mechanisms that lead to pipe failure often require data that are not readily available and are
costly to obtain. Physical models may currently be justified only for major transmission water mains,
where the cost of failure is significant, whereas statistical models, which can be applied with various
levels of input data, are useful for distribution water mains.  The statistical methods are classified into two
classes, deterministic and probabilistic models. Subclasses are probabilistic multi-variate and
probabilistic single-variate group processing models. The review provides descriptions of the various
models including their governing equations, as well as critiques, comparisons and identification of the
types  of data that are required for implementation.

A current project undertaken by NRC in conjunction with Water Research Foundation is "Dynamic
Influences on the Deterioration Rates  of Individual Water Mains" (Project #3052). The objective is to
develop a model that considers both the static and dynamic factors of individual water mains. The
deterioration process is complex with many static factors like soil, pipe material, size,  and age as well as
dynamic factors like  climate, operation, and protection.  It is expected that the outcome will be a model
and analytical tool that covers dynamic factors for an individual main.

A model to prioritize the replacement of cast iron distribution mains was developed for AwwaRF and
AWWA titled "Decision Support System for Distribution System Piping Renewal" (Deb, 2002b).  It is
based on the relationship between remaining wall thickness and residual strength. External and internal
loads  are used to model the stresses on the pipe, fed into a model and compare them to the current
strength and the current Safety Factor (SF)  is calculated.

A partnership between AwwaRF and NRC  has produced a report titled "Risk Management of Large-
Diameter Water Transmission Mains" that provides a method to translate distress indicators obtained
visually or  from non-destructive evaluation techniques on large water mains into condition ratings
(Kleiner et  al., 2005). The process involves "fuzzy logic", a method for combining scarce condition data
with modeling that predicts the statistical likelihood of deterioration and failure of a given pipe.

4.4.3       Life Expectancy Curves. The concept of determining the economic life of an asset using
statistically developed life expectancy curves has been developed by a number of researchers and
authorities. There is  some disagreement about the value of this approach.

Any pipe material laid in a given year will have an average life, but may not require replacement at the
same time due to a multitude of factors. The basis is that the mains will have a probability of needing
replacement spread on either side of the average. Typically, a life expectancy model combines a series of
normal distribution curves for types of pipes and the year laid. The simplest approach is to decide the life
of the asset and then  using standard deviations (10 to 20 percent) to produce a series of replacement cost
curves.
                                               44

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Some fundamental assumptions like "average life" and standard deviations are made, but they should
correspond with experience to match real life.

4.4.4       Software Programs. Many programs have been developed for residual life prediction as
part of condition assessment strategic planning.  These programs range widely in degree of sophistication.
Many of them are developed as planning models, but all are concerned with making an evaluation of the
life of an asset.

"Condition Assessment Strategies and Protocols for Water and Wastewater Utility Assets" (WERF,
2007) has an extensive table in Chapter 7 that summarizes the tools and techniques available for condition
assessment of both water and wastewater systems that have been developed worldwide.  Table 4-2 was
modified based on this work for condition assessment strategic planning of water systems.
          Table 4-2. Tools and Techniques for Condition Assessment Strategic Planning
Tool or
Technique
FailNet-Stat


WRc Trunk
Main Structural
Condition
CARE-W

KANEW


MRP



FARMS-
PLANNING

PIREP


UtilNets


WARP


Assessment Focus
Failure forecasting


Current condition/
remaining life

Strategic planning
with rehab planning
Strategic tool for
replacing

Decision support
tool for main
renewal

Decision support for
asset renewal

Decision support
system for rehab
planning
Reliability support
system

Long term planning
using asset failure
curves
Data
Needs
High-
asset and
failure data
Moderate


Dependant on
tools used
High-
comprehensive
data
Very High -
asset,
performance
and failure
High-
asset and
failure
High-
asset and
failure
Very high -
asset and
failure
High-
asset and
failure
Skills
Required
High


High


High

High


High



High


High


High


High


Degree of
Sophistication
High


Basic generic
approach

Basic generic
approach
High


High



High


High


High


High


Commercially
Available
No (only research
application in
Europe)
Available as
manual

No (trials in
Europe)
Available from
CH2M Hill

Yes



Yes (in Australia)


No (under
development)

No (prototype
stage)

Yes


Note: many of these programs cover more than pipeline assets.
Updated based on Table 7-6 in WERF, 2007.
The tools and techniques listed in Table 4-2 have the following in common:

       •   All are computer-based
       •   Very high data needs - assets and failures
                                              45

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        •   High professional engineering skills required.

This list is by no means comprehensive and there are a number of other programs and developments
currently under way. It would require an extensive effort to evaluate these programs for their
comparative merits.

An example of one of these programs is "UtilNets." European funding invested a significant sum in this
forecasting model, which is a decision-support system (DSS) for rehabilitation planning and optimization
of the maintenance of underground pipe network of water utilities. The DSS performs reliability-based
life predictions of the pipes and determines the consequences of maintenance and neglect overtime in
order to optimize rehabilitation policy. While admirable in its aims and logic, it was found that the model
requires more data than currently available to make its use worthwhile.

4.5        Current Barriers to Effective Use of Condition Assessment

There are a number of barriers to effective use of condition assessment. The following is not meant to
serve as a comprehensive list.

4.5.1      Database Quality.  In the previous section it was noted that all condition assessment
programs are based on high quality asset and failure databases. The lack of robust databases for many
water utilities is a major barrier to condition assessment in building a picture of the failure patterns for
different ages and types of pipe in a range of locations.

The UKWIR's "Nationally Agreed Failure Data Base and Analysis Methodology for Water Mains" has
provided statistically robust information on mains failure together with basic data on the assets for more
than 95 percent of the U.K. water network (UKWIR, 2004). It has more than 500,000 records and is
increasing the number and quality of records in a staged development.  The data from the utilities was
taken and reformatted to be consistent and comparable. This has provided valuable insights into both
national and regional patterns of failure for all types of pipe material.

Currently, Water Research Foundation is pursuing a project (Project #4195) to try to make use of the
architecture, definitions and structure of the UKWIR database for data on main breaks in the U.S.  This is
being done in parallel with Australian water utilities. At present, Water Research Foundation is
identifying a handful of utilities that have interest in the topic of main breaks and condition assessment to
work on this project and provide some feedback on adaptation of this model to the situation in the U.S.,
while the Water Services Association of Australia (WSAA) follows a similar path in Australia.

In many cases, the existing U.S. utility databases are incomplete and/or inaccurate.  Failure databases are
not standardized when kept, and failures are normally not recorded or attributed in a uniform manner that
could allow any sensible comparison.

The fragmentation and diversity of water utilities in the U.S. would make the development of a national
database a difficult, but valuable task. The U.S. electrical utilities have the North American Electric
Reliability Corporation (NERC) database. It is maintained by the electrical utilities and contains
information on reliability and failure of electrical power systems supplied by vendors.

An AwwaRF paper supports the concept of National Water Main Failure Database and believes that it
would be of great value to water utilities (Gaewski and Blaha, 2007).

4.5.2      Regional and Local Variations. In an attempt to provide all-purpose condition and
management assessment tools applicable to a wide range of clients, the importance of local variations that


                                              46

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can arise from a number of reasons, not just environmental, has not been given sufficient consideration in
the past.  This is now better recognized, and several organizations including NRC, WRc, and UKWIR are
building frameworks that allow individual utilities to model around their own experience and data.

4.5.3       Inspection Data Set Requirements. Although a great deal has been written on both the
asset and failure data, there is not a good consensus on what key data sets are needed or can be obtained
from an inspection to make a reliable condition assessment and life prediction.  This lack of consensus is
likely due to the fact that it is difficult to define the exact and reliable pre-failure conditions leading to
structural failures because of multiple types and magnitudes of loadings and pipe strengths. Furthermore,
for technical and economic reasons, it is often difficult to measure the pipe and loading parameters with
adequate spatial, temporal, and failure mode coverage even though the feasibility of measuring critical
parameters may change as technologies improve and costs decline. For structural condition assessment, a
typical aim is to try to determine the loss of metal by general corrosion, graphitization, and pitting.
Detecting cracks and flaws is also needed, though.

However, external investigations, which can only cover a small percentage of the main, may not represent
the maximum loss of metal or be typical of the line. Internal investigations are costly and disruptive to
the utility operation, and are rarely undertaken.  The quality of the data in terms of identifying pitting is
often poor. General areas of metal loss are more easily identifiable than graphitization or pitting.

At best, inspection can only provide a snapshot of the current condition.  To make predictions, the basic
information on the pipe (type, age, and original wall thickness) is needed. Additional information such as
how long corrosion has been taking place and if it has been uniform is also needed.

The use of soil characteristics to determine the likelihood of corrosion and particularly pitting has
relevance when the pipe is unprotected, but a large part of the ferrous network has been laid with some
sort of protection.  Polyethylene encasements became common, but not universal, in the U.S. in the 1970s
and now installation of ductile iron pipe with polyethylene encasement is considered routine by most
utilities.  However, many unprotected pipes have been and continue to be installed.  Cathodic protection
installed during initial work, retroactively or opportunistically, is another protection method.

In earlier sections of this report some anomalies are highlighted both in the forms of failure and the
relevance of the statistical and inspection data.

Many vendors' reports are prefaced with a wide range of disclaimers as to their accuracy.

4.5.4       Current Condition Assessment Methodologies.  All models and predictions must determine
what key factors leading to failure will be used in a model.  It is apparent that there is no consensus
among researchers on what these factors  are and what their comparative weighting should be. Differing
pipe manufacturers, vintages, and local environmental conditions make it difficult to develop a model to
fit all.

Many programs require a high level of technical input, which is probably only available in larger
organizations or by the consultants promoting the method. The multiplicity of approaches and level of
sophistication of these programs can be daunting to managers and engineers in the small to medium size
utilities.  There is a need for improving the situation for utilities to operate in-house condition assessment.

4.5.5       Current Inspection  Technologies. The technologies currently available are described in
Section 3 and Appendix A. Undoubtedly, progress has been made and there have been valuable
developments that will continue.
                                               47

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However, the reality is that there is a long way to go for an inspection tools for structural condition that
will fully meet the needs of the water utilities.  The typical "wish list" is set out below:
        •  Inspect without disruption of service
        •  Inspect unlined pipe without disturbing tuberculation
        •  Access live mains
        •  No obstruction to flow
        •  Negotiate multiple bends, restrictions and appurtenances
        •  Determine presence of linings and coatings and their condition
        •  Inspect without removal of linings and coatings
        •  Provide comprehensive structural data, including loss of metal through general corrosion,
           graphitization and pitting to an accuracy of 10 percent of the original wall thickness
        •  Provide both internal and external loss of metal
        •  Identify longitudinal and circumferential cracks and flaws
        •  Low mobilization cost
        •  Inspection cost of 3 to 5 percent of the asset value.
Internal Inspection
No commercial internal inspection tools currently available can meet all of the criteria either technically
or economically. Recently, tools have been developed that claim to work in pipe diameters up to 14 in.
with the main  in operation. These are recent innovations and little field experience is available.
Major shortfalls lie in the tool's ability to identify pitting and the high cost of mobilization and inspection.
External Inspection
In terms of the "wish list" above, external investigation comes closer to meeting the criteria. There are
tools that will  closely identify the structural condition for the section of pipe exposed and inspected.
The downside of external inspection lies in the cost of exposing a section of pipe and the reliability of
such investigations as being representative of the whole line. This point is discussed elsewhere.
In undertaking limited external sampling, locations and conditions need to be chosen so as to be fairly
uniform in the section being investigated.
Leak Detection
The developments in in-line leak detection have brought us closer to meeting most of the utilities' "wish
list" for leak investigation. However, mobilization and setting up launch and/or retrieval points can be a
significant cost.  Current in-line leak detection is a snapshot of the current leaks.  It is possible for a leak
to develop immediately after examination and remain undetected until being inspected again.
                                               48

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4.5.6       Physical Difficulties and Costs of Inspection. Major barriers to inspection by utilities are
the physical difficulties and the costs involved in gaining access to the pipe.

For an internal investigation the tools that can be used in an operational main are currently limited by
diameter and quality of the data collected. To gain access for such tools, some form of launch and/or
retrieval facility needs to be retrofitted.  Any tuberculation would need to be removed prior to inspection.
Several of the technologies can inspect the ferrous pipe through lining. Other internal technologies can
only operate with the main out of service, emptied and cleaned.

Many utilities have reservations about introducing inspection tools into operational water mains.  The
possibility of contaminating the water supply is a major concern.

For an external investigation of a main in the  road, the costs of excavations can easily be several times the
cost of the inspection. If these are located in roads, then traffic control, pavement removal, reinstatement,
and dealing with existing utilities add to the cost.

4.5.7       Relationship between Information Needed and What Current Technologies Provide.
The quality of the information that is obtained by external and internal inspection technologies is not well
defined.  Currently, a utility has to adjudge any technology or method on the sales pitch and cost. There
is no independent testing and evaluation information to compare competing methods for their ability to
give the information needed.

A number of inspection technologies produce a great deal of data that after processing is presented to the
client in relatively simplistic plots. However, the interpretation of the data lays in the hands of the vendor
whose understanding of electronics and data processing may be greater than his understanding of pipes.
There have been a number of inspections that have not identified or quantified key defects.

4.5.8       Relationship between Performance and Cost. A paper "Economic Assessment of
Inspection - The Inspection Value Method" sets out the concept of a performance-based economic model
of inspection based on cash values (Wall and  Wedgewood, 1998). It defines value of inspection as the
benefit less the cost of inspection (Value = Benefit - Cost).  For cost, it uses three elements:

       •   Fixed cost
       •   Time and speed-dependent cost
       •   Cost depending on reliability.

These can be readily expressed in cash terms.

To estimate the benefit in cash terms is more subjective. Avoidance of costs associated with breaks might
be considered to be a major benefit. It could also be considered as the benefit gained from avoiding
renewal for a longer period.

Grand Central Model (GCM) was  developed as a standard Microsoft" Excel spreadsheet to assist utilities
to  calculate the cost of failure (Cromwell et al., 2002).  The AwwaRF paper "Analysis of Total Cost of
Large Diameter Pipe Failures" continued this work (Gaewski and Blaha, 2007). It was recognized in the
later work that it was unlikely that water utility managers would use the original model to develop the
extensive data inputs as needed. A simplified data collection sheet was developed that made certain
assumptions on behalf of the utility.  The approach and assumptions are detailed in the paper.
                                              49

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Direct costs of the majority of failures are relatively low. A recent AwwaRF paper estimated that for
diameters of 20 in. and less, there are 300,000 breaks per year, with the average direct cost of a break
being $5,000 and with societal cost accounting for another $5,000 (Grigg, 2007). The paper estimated
that for diameters over 20 in. there was approximately 500 breaks a year and from a range of records
calculated that the geometric mean of all costs was $500,000. Again the breakdown is 50 percent direct
cost and 50 percent societal cost. Societal costs are paid by the utility sometimes or only partially.

It cannot be assumed that inspection will directly identify a pending structural failure.  This reality is well
understood by many utility managers who find it more cost-effective to fix breaks than anticipating them.

In terms of the benefit, it will be difficult to show value  for smaller diameters taking into account all of
the costs of inspection.

An AwwaRF study "Performance and Cost Targets for Water Pipeline Inspection Technologies" (Project
#3065), still to be published, addresses the issue of value of inspection. The interim findings state that for
many situations neither the performance nor the cost of many water inspection technologies is acceptable.
It proposes that quantitative cost and performance targets for technologies be identified. The point is
made that value of pipeline inspection information is not well quantified, thereby making cost/benefit
decisions about assessment difficult or impossible.

It is noted that the cost of inspecting just 0.2 percent of aline externally will involve pits every 3,000 ft
(this is based on exposing a 6-ft length).  Statistically this is a small sample. The cost of pits in a highway
can easily be in the range of $20,000 to $50,000.  The actual cost of the inspection element and reporting
could be in the order of $3,000 to $5,000 at each excavation.  Improving the quality of the data by
conducting more inspections in excavations will add significant cost.

Internal inspection should be able to provide more comprehensive information, but has a significant cost
in gaining access to the line. Therefore, the inspection company's high cost associated with equipment
mobilization, data collection,  and data processing can be a significant percentage of the asset value.

There is a strong economic case for not inspecting smaller diameters as the cost of any inspection will be
a significant percentage of the replacement or rehabilitation cost.

The AwwaRF study also discussed the "acceptable" costs to utilities of collecting investigation
information.  Generally, utilities considered the cost too high, even for large mains. For cases in which
they were prepared to offer a percentage relationship, there were two schools. One considered something
between 2 and 5 percent of the pipeline value; the other  was willing to pay less than 1 percent.  For a
comprehensive survey even the upper levels will be difficult to achieve because, based on the costs of the
current technologies, it is likely to be 10 percent or even higher.

Undoubtedly, cost of investigation is a major barrier to greater use of inspection devices. For many in-
line technologies the scope for reducing cost appears to be limited because of the following factors:
        •   High development and production cost of intelligent pigs
        •   High cost of mobilization
        •   Significant cost in providing launch and recovery facilities
        •   Large amount of data collected which has to be processed.
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               5.0 KEY PERFORMANCE AND COST IMPROVEMENT AREAS
The Technology Forum brought the experience and expertise of a wide range of people to bear on the
issue of improving performance and cost of structural condition assessment for ferrous water transmission
and distribution pipes.  The following subsections provide brief descriptions of six key, potential research
products that the authors recommended for consideration and discussion by the Forum attendees. The
products fall into two main categories:  (1) improving the consolidation, organization, analysis, and use of
data that already have been, or are being, collected by utilities, and (2) improving the capability and cost-
effectiveness of inspection technologies.

5.1        National Asset and Failure Database Guidelines

The adoption of a national standardized asset and failure database would be a major step in improving
condition assessment.

AWWA has recognized that such a database would provide considerable benefit and they could make a
valuable contribution by pursuing this initiative. In keeping with this sentiment, Water Research
Foundation is currently pursuing a project (Project #4195) to try to make use of the architecture,
definitions, and structure of the UKWIR database for main breaks in the U.S. This is being done in
parallel with Australian water utilities.  At present, Water Research Foundation is identifying a handful of
utilities that have interest in participating in this project and providing feedback on adaptation of this
model to the situation in the U.S., while the WSAA follows a similar path in Australia.

5.2        Guidelines for Interpreting Defects and Distress Indicators and Developing
           Condition Ratings

Progressive utility managers and operators have a significant body of knowledge and experience in
interpreting defects and distress indicators  for their own networks. Less experienced managers and
operators could benefit if guidelines are developed, based on input from leading utilities, on interpreting
distress indicators and defects and determining their significance. In addition, guidance on rating pipe
condition and on specific investigation or monitoring techniques would be of great help to utilities in
interpreting and allocating defects and distress indicators to the correct cause. This in turn will mean
more accurate inputs into condition rating and life expectancy predictions.

This guidance will also assist utilities to implement the suggestion in Subsection 5.4 that, for models and
life prediction curves to be useful, they need to be modified to take into account local experience.

A great deal of literature addresses this subject, and it should be possible to synthesize it to develop user
friendly guidelines for utilities and their operators.

5.3        Guidelines for Utilities on Undertaking Condition Assessment

These guidelines would address actions to be taken after a decision has been made to do condition
assessment, and the goals of the condition assessment have been established. The guidelines should
present condition assessment as a two-stage process. The first stage is an initial assessment based on
asset and failure databases. This will in some cases be sufficient for a decision to be made without
investigation. In other cases it will define and prioritize the second stage, which is a more detailed,
specific investigation that will typically involve inspection.
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The initial condition assessment should define what additional information, if any, is required from an
inspection to complete the assessment. A feature of the initial assessment should be a definition of type,
quality, and quantity of additional data needed, which in turn defines the inspection approach.

The guidelines should emphasize actions and approaches to ensure that the information obtained through
inspection is not an end in itself, which is not an uncommon approach. Rather, it should be emphasized
that database and inspection information needs is a complementary and integral part of a final condition
assessment and life prediction.

 5.4         Developing User-Friendly Models to Predict Residual Life and
            Deterioration

The current approaches are discussed in Section 4. A good deal of work has been undertaken on the
prediction of residual life. Some form of evaluation of the effectiveness  of these models, and their extent
of use by utilities, would be valuable.

The need is to develop user-friendly techniques that can be used by a wide range of utilities to assist them
in their asset management planning and expenditure forecasting.  Some earlier prediction and life cycle
tools did not correspond well with utility experience, which created some distrust.

The prediction models for individual water mains need to be tailored to the local characteristics and
experience.  However, the process to customize these models to local conditions and provide reliable
results could be complex.  Some programs are building in this facility but the more complex and
structured the model, the more difficult and costly they are to  support data requirements and operate.

5.5          Developing Cost-Effective Inspection Tools and Methodologies

Development of cost-effective inspection tools and/or methodologies to provide data on existing
structural condition and prediction of future deterioration is the most challenging task of all.

A consensus is required on what data need to be collected, over what percentage of a pipeline, to what
accuracy, and at what cost so that the utilities are willing to pay.  Questions that should be considered
include the following:

        •    Can external inspection of a small percentage of the pipeline provide sufficient data to be able
            to draw conclusions on the whole line?

        •    Can limited external  inspection be combined with other condition assessment techniques to
            reach conclusions on the whole line? This appears to be possible, for instance, for an
            unprotected cast iron pipe where  external corrosion is a key factor and soil aggressivity can
            be defined.

        •    Can the circumstances be determined under which a full internal inspection is needed  for
            metal loss or for leakage?

        •    Can tools be developed that can be used with a main in operation? Leakage tools like  Sahara®
            and SmartBall® using appropriate launch and retrieval measures are able to do this. For
            structural investigation diameters above 14 in. require the main to be taken out of service,
            cleaned and emptied. It may be possible for some technologies to work in mains that  are out
            of service but not emptied.

        •    Can acoustic or other technologies be developed for internal investigation that can provide
            the required level of information  on structural condition? For example, can the Sahara® or
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           SmartBall  technologies be developed to carry sensors which collect data on the structural
           condition?

        •   Can the method of installing a wire or fiber optic cable in a pipe to collect acoustic emissions
           or other data on leaks and wire breaks in PCCP be adopted to collect information on
           structural condition of ferrous pipes?

        •   Are "Smart Pipes" a viable option?  The concept of "Smart Pipes" has been promoted for
           many years and has never made many inroads although technically possible. The cost and
           practical difficulties have all discouraged utilities.

        •   How much are utilities willing to pay for inspection to prevent failures for critical high risk or
           high interest scenarios?

5.6        Determining an Acceptable Relationship between Cost of Inspection and
           Value of Asset

For any vendor or developer of inspection tools to achieve success, they need to understand the potential
market and the cost that the market will bear.

The potential market is very large, but in reality the current market is very small because of the barriers
discussed.  Even basic, relatively inexpensive technologies like ultrasonic tools find few applications.
Several vendors have withdrawn from the market. Currently, the cost that the market will apparently bear
may discourage commercial companies in investing substantial sums in development. In addition, the
data collection and processing require a good deal of manual input and is a significant cost element of
inspection.

This can be compared to the oil and gas transmission industries where there is a wide array of available
tools to serve a very large market that will pay for inspection.  The even greater volume of data collected
is analyzed automatically using specially developed software.  It is often suggested that some of these
tools might be adapted to use in ferrous water transmission pipes, but there are considerable differences
that will make the transition difficult:

        •   The value of oil and gas is high. A large transmission line can easily be carrying a million
           dollars of product a day.
           The value of water is low.

        •   Leaks from oil and gas lines  are highly dangerous  to life and property.
           Leaks from water lines occur all the time and are rarely dangerous.

        •   Federal regulations impose a strict set of rules for oil and gas inspection performance and
           frequency.
           There are no similar requirements for the water industry.

        •   Most oil and gas transmission lines investigations  are on very long and straight lines.
           Most water transmission mains are relatively short and have linings, bends, tees, valves
           which create obstructions and limit the use of intelligent pigs.

        •   The very high cost of mobilization becomes acceptable when spread over an inspection of
           many miles.
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            Water utilities do not have the funds or the need to carry out very large inspection programs.

        •   Oil and gas transmission lines use steel pipe with welded joints giving continuity.
           Most water pipes are bell and spigot jointed.

        •   Oil and gas transmission lines are externally wrapped for corrosion protection and methods
            are available to check discontinuities of coatings and potential corrosion spots.
            Where water pipes are externally protected it is with polyethylene baggies andno methodis
            available for checking condition. Cathodic protection indicators (accessible sacrificial
            anodes) are available but seldom employed.

        •   Oil and gas transmission lines do not have internal coatings so that inspection methods can be
            in direct contact with the metal.
           A large percentage of water lines are lined internally with cement mortar linings or other
            materials.  Where no linings have been installed then many older water lines are
            tuberculated.

        •   Oil and gas transmission lines are constructed with launch and recovery facilities for
            intelligent pigs.
           Most water lines would require retrofitting with launch and recovery traps to use intelligent
           pigs.

For the inspection of prestressed concrete water pipes, the water industry has accepted that inspection is
required to determine the structural condition of pipes.  PCCP has been used  mainly for large
transmission lines where there have been a  number of catastrophic failures. It is possible to identify the
mains at most risk, but without inspection, it is not possible to determine the  structural condition.

Utilities seem prepared to pay the relatively high cost of inspection as the consequences of failure can be
very high in terms of damage, loss of service, and repair cost, especially after a utility has experienced  a
catastrophic failure or knows someone with a similar system who  has.  This squares with the report on  the
costs associated with failures of large mains.  There is value, after cost of investigation is deducted from
the benefit, in avoiding a failure.
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          6.0 PROSPECTS FOR SHORT- AND LONG-TERM IMPROVEMENTS TO
                 CONDITION ASSESSMENT FOR FERROUS WATER MAINS
The objective of this Forum was to bring the experience and expertise of a wide range of people to
discuss how both short- and long-term improvements can be made to condition assessment for ferrous
transmission and distribution mains. The following potential improvements were set out to stimulate
discussion and identify additional improvements.

6.1        Starting Points for Evaluating and Improving Short- and Long-Term
           Advances in Condition Assessment

The "EPA Water Infrastructure Research Plan" (EPA, 2007) spelled out the following questions that, if
addressed, will lead to a better understanding of the capabilities and limitations of condition assessment
for ferrous transmission and distribution mains, and a clear recognition of opportunities for short- and
long-term improvements of condition assessment.

       •   What is water main condition assessment?
       •   What are the goals?
       •   What outputs are required?
       •   What is the minimum precision and accuracy needed to meet the goals?
       •   What data, calculations and criteria are required to produce the outputs?
       •   What conceptual, preliminary and physical tasks are involved in obtaining the data?
       •   Do suitable methods exist to collect the data?
       •   How does one determine the value of condition assessment?
       •   What are the limits of condition assessment?

6.2        Short-Term Improvements to Condition Assessment

6.2.1       Short-Term Improvements to Use of Existing Information. Within the short-term, the use
of existing information for condition assessment could offer the best opportunity to improve the asset
management performance of the water industry.

There is a wealth of environmental, historical, and  operational information that has been or can be
developed into an asset database. Operational records should provide information on failures and repairs.

A great deal of literature has been published on asset management and condition assessment programs.
Many of the programs require very good quality data and high levels of expertise to operate.  Some of
these programs have been developed to meet the needs of very large water companies to satisfy regulator
demands for data and expenditure justification. Because of their size they are able to have specialists
allocated to operate such tools.  Such specialized expertise is not normally available except in a few large
U.S. utilities and/or through consultants.

The knowledge and understanding of the network of the management, engineers, and operators should be
harnessed, because they are in the best position to understand local conditions, defects, and failures.

Providing a logical framework on recording the assets and the failures, using this information along with
developed life expectancy curves or models, and then applying their own observations and local
knowledge could lead to significant improvements  in condition assessment. It would enable practitioners
to prioritize both investigation and planned investment.
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Some guidance should be developed for identifying the high risk scenarios, which requires characterizing
both likelihood and consequences of failure. With limited funds, it is necessary for utilities to focus on
the highest risk situations.

The role of government in this area should be through coordination with and support of organizations
such as Water Research Foundation and WERF.

6.2.2      Short-Term Advances in Inspection Technologies.  The various barriers to short-term
advances in inspection technologies were discussed earlier in this State of Technology Review Report.

Regarding internal inspection technologies and tools, because the current technologies cannot meet
technical and economic requirements and because there is no regulatory driver for utilities to inspect
water mains, the limited current market for inspection becomes a major deterrent to potential vendors,
particularly for smaller diameter ferrous pipes.

However, progress has been made in developments of in-line leak detection/location/characterization and
pressure management to reduce water loss and prevent small water main breaks.  Adopting novel
approaches for proactive maintenance of low-risk mains may have the potential to be  economically viable
for some applications.

Sahara® and SmartBall® also offer platforms for carrying sensors to assess the pipe wall conditions in a
live main. For example, the Sahara® Video carries a camera for CCTV inspection of in-service water
mains, such as the overall condition of the internal cement mortal lining.  The Sahara®- and SmartBall®-
based tools are being developed to assess the changes in the pipe wall thickness by measuring either the
speed of sound or the pipe stiffness at certain intervals along the pipe as the tool travels through the pipe.

External inspection, if, as suggested earlier, used in conjunction with other tools, can provide the level of
information needed to support water infrastructure managers, then there are opportunities for short-term
improvements to current external inspection methods. For example, Gas Technology Institute (GTI) has a
program of developing inspection tools that will work from keyhole excavations. A combination of open
and keyhole excavations/inspections could provide a better level of inspection while keeping the cost of
pipe exposure to a reasonable level.

6.3        Long-Term Improvements to Condition Assessment

6.3.1      Long-Term Improvements to Use of Existing Information.  There is considerable
potential for utilities to be provided with a better understanding of the behavior of different forms of
ferrous pipes  in the water network.  There is a wealth of information available from a large body of
research and reports. However, the various research generated can be abstract, sometimes offer
information contradictory to each other, and may have limited applicability. Where contradictions and
anomalies occur, they need to be understood and resolved. The information should be synthesized into
practical guidelines for operators. For instance, it would be possible to develop a range of more specific
life expectancy curves and models that relate not just to a pipe material but to various periods in the pipe
manufacture that have different failure expectancies.  It is commonly accepted that some ferrous pipes of
later vintage have a reduced life expectancy compared to earlier vintage.

Such curves and models need to be  changed to reflect local conditions such as soil parameters and
support.  For  example, the relationship of local soil conditions and the corrosion of unprotected cast iron
should be taken into account. Lack of soil support, often coupled with increased external loadings, may
be another local factor that can modify life expectancy curves.
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Taking a wider range of historical factors and experience into account along with specific local conditions
for a utility could provide more realistic life expectancy predictions.  This should help identify the most
vulnerable pipes and reduce failures. It will also allow improved asset management and allocation of
funds in a long-term program of replacement or rehabilitation.

If a national database of assets and failures were available relating breaks and leaks to specific materials
and environment, this would support the decision-making process of utilities, allowing them to
benchmark their own experience.

6.3.2       Long-Term Advances in Inspection Technologies. A staged approach is needed for long-
term advances in inspection technologies.  Initially the objective should be to reach agreement and define
technical and cost performance targets for both internal and external tools.

One means of obtaining inputs from all sides would be to organize workshops with attendees from
utilities, consultants, developers, and manufacturers.  The objective would be to determine if there is
consensus on effective approaches and ideas on how the objectives can be achieved cost-effectively.

For internal investigations a number of prototypes and trials are under way that could lead to longer-
term improvements. Fundamental characteristics and limitations to the basic technologies employed in
in-line tools need to be understood, along with their cost implications, for any development of internal
inspection in operational water mains.

The New York trials with non-contact ultrasonic tools, the Super-Pig, and Russell Technologies' new
tools, "See Snake", are described in Appendix A. Technically they appear to  have potentials for effective
internal inspection of water networks. However, the tools will require launch and recovery features to be
retrofitted.  These tools are sophisticated and likely to be costly to produce, mobilize, and operate.

In the case of the Super-Pig, its diameter range is limited so that a series of tools will  be required to cover
the size spectrum. Although the prototype performed well, this tool remains at the developmental stage.
The cost of development compared to the potential market and the rates the market would bear is likely to
limit its use to the larger diameters.

One apparently easy approach is to undertake continuous monitoring of pipes for indicators of
deterioration, such as corrosion, wall loss, acoustic emissions (e.g., from leakage, cracking, or
impingement), or strain. An embedded sensor system would be required for continuous monitoring. The
initial cost of an  embedded sensor system  is potentially offset by reduction in mobilization and
demobilization costs, and better spatial and temporal  coverage of the pipe network. Continuous
monitoring is already done for corrosion in some industries, and some of the current commercial tools can
be adapted relatively easily.  For example, fiber optic sensors are developed to measure pipe wall
thickness directly by measuring the change of strain on the pipe outside surface. However, it seems to
have limitations  for monitoring corrosion in the water network.  Only a small number of locations can be
monitored, and the rate of deterioration is  slow and would require years of data collection to yield any
useful data.

The advances in  electronics, sensor technology, information science, electrical and computer engineering
promote the emergence of new technologies that can  be applied to the inspection, monitoring, and
assessment of the conditions of water mains.  Some technologies are initially developed for non-water
applications. The opportunities of technology transfer to the water main condition assessment should be
evaluated.
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A major need is to have some independent test facilities where tools can be tested for their abilities to
identify and quantify defects in varying types of pipes. Tools could then be given an initial classification
based on the results from the test bed.  It should include evaluation of mobilization, launch, parameter
measurement capability (e.g., type and number of parameters measured, precision, accuracy, speed,
effects of interferences), and operational and reporting costs.  Such independent tests would allow
engineers and utilities to have some basis for choosing an inspection vendor.  Currently, there are no
benchmarks or comparisons among different methods and tools.

6.4        Measuring Success

Measuring success will take a number of forms. By the nature of the utility structure and the measures
needed it will take time for the full benefits to  flow. Initially it would require the following activities:

        •   Adoption by utilities of a standardized form of asset database and reporting together with a
           standardized failure database and reporting

        •   Adoption of guidelines with a standard approach to interpreting data and carrying out
           condition assessments to allow comparisons and benchmarking

        •   Getting utilities to use life prediction charts tailored to their type  of pipes and local conditions

        •   Using risk-based assessment approaches in determining priorities for renewal and inspection

        •   Encouraging utilities to allocate funds to investigation of critical  lines.

Over a period of time, these activities should result in reduced unforeseen failures and catastrophic
events.  This will  reduce direct and indirect costs associated with unforeseen  failures. Improved life
prediction curves  will provide a sound basis for budgeting for renewals and allow a running program to
be developed.

If inspection methods and technologies can be developed that improve the quality of the information
collected and reduce the current high cost, this in itself will be a significant success, as it will lay the
foundation for better temporal, spatial, and failure mode inspection coverage  of the pipe network, which
will enable better assessment of pipe condition, and more appropriate, timely, and economical inspection,
repair, rehabilitation, and replacement programs.

6.5        Accelerating Development - Potential Government Roles

The potential government roles cited below are understood to be undertaken in  cooperation and
collaboration with relevant stakeholders.

6.5.1       Guaranteed Minimum Work Programs for Internal Inspection. Currently the
development of cost-effective inspection tools, with the exception of in-line leak detection,  faces a
"chicken and egg" situation, where the lack of market discourages developers from developing better and
more economical  technologies, and the lack of cost effective inspection methods discourages utilities
from inspecting. Also,  some of the more sophisticated and expensive technologies may only be cost-
effective for larger diameter, high risk lines.

If some form of guaranteed minimum work program for inspection of ferrous pipes were established with
a number of utilities, this could be attractive for vendors to spend money on developing tools to meet the
program's technical goals and cost targets.  This approach could apply to both external and  internal
inspection, and should initially focus on the larger diameters, for which the value and willingness to pay
for inspection will be greater. Vendors would have to meet performance specifications. In  the case of
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external inspection, they would need to set out what other support methods would be used to ensure that
the external inspections were representative of the whole line.

6.5.2       Support for Database Development. Transmission and distribution systems are
"laboratories" that produce large amounts of valuable data.  However, it can be difficult and costly to
collect, organize, analyze, and disseminate the results. Government support, in cooperation with the
user/expert communities, can help accelerate and expand collection and use of valuable data, e.g., failure
statistics, deterioration rates, failure cause analysis, failure consequences, inspection technology
performance, decision support system performance, etc. that will help improve asset management
decision-making.

6.5.3       Defining Next-Generation Inspection Technology Needs.  If target performance and cost
specifications can be developed for "next-generation", as opposed to ideal inspection technologies, this
could be invaluable for focusing intellect, energy and resources toward developing the desired inspection
capability.

6.5.4       Funding Technology Innovation Research. Although full government funding of advanced
inspection technologies for ferrous water mains is unlikely, the U.S. government does have programs in
place that can accelerate improvement of technology at various points in the development process. For
example, The National Institute  of Standards and Technology (NIST) Technology Innovation Program
(TIP)  issued a large solicitation in July 2008 for advanced sensing technologies for infrastructure,
including roads, highways, bridges, and water systems. The EPA National Risk Management Research
Laboratory (NRMRL) recently (2007) initiated an Aging Water Infrastructure applied research program
that includes  evaluation, improvement, controlled-condition testing, demonstration, verification, and
decision-support for condition assessment technology research.  The program will be conducted by a
combination of in-house, contractor, and assistance agreement efforts. The EPA National Center for
Environmental Research's (NCER) Small Business Innovation Research (SBIR) program, included water
infrastructure inspection in their recent call for proposals. NCER's Science to Achieve Results (STAR)
Program issued a large solicitation to non-profit research organizations for innovation and research for
water infrastructure and water infrastructure sustainability. Also, the oil and gas sector and the U.S.
government place a high value on inspection of oil and gas infrastructure, and the U.S. government
supports this  research through the Department of Transportation. So, even though there are many
technical and economic obstacles to transferring technology from oil and gas pipe inspection to water
pipe inspection, this is an area of research activity that must be periodically examined for potential
technology transfer opportunities.

6.5.5       Development and Support of Condition Assessment Technology Facilities.  Providing test
facilities for conducting independent testing and evaluations would be of considerable value. This could
include laboratory testing of "breadboard" developments. Establishing a dedicated test site would be
most useful for evaluating existing and prototype tools for their ability to detect, identify, and accurately
characterize various forms of defects that typically occur in various types of water pipe.

There should also be some evaluation of the support work required and costs associated with an
inspection. It will be very important to plan the test pipe and flaws  carefully. Inputs from utilities and
specialists will be needed as to what are considered to be the benchmarks laid down. The test facility
should focus  on structural defects and not leakage.

It will be important to assess the capabilities of existing test facilities as part of the planning process.  For
example, Battelle  has a pipeline facility that was designed for testing and evaluating inspection tools for
the oil and gas industry.  Organizations like the Electric Power Research Institute (EPRI) also operate a
similar test bed for evaluating investigation tools. One of the  advantages these controlled-condition
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simulation/test sites offer the vendor is helping to define the strengths and weaknesses of a tool under
various conditions, and/or in comparisons with other tools, giving direction for making necessary
improvements.  Other advantages of a test site include the reduced cost, complexity, time, risk, and
variability from field conditions, and the ability to characterize, control, vary, and repeat conditions of
interest. An advantage for both the utility and the industry is that they can obtain a basic independent
evaluation of tools as well as guidance on which tools might cost effectively meet specific needs.

EPA also has experience operating test facilities, including Test and Evaluation Facility, Cincinnati, OH;
Leaking Underground Storage Tank Test Apparatus, Edison, NJ;  Pipeline Test Apparatus (PTA), Edison,
NJ; Oil and Hazardous Materials Simulated Environmental Test Tank, Leonardo, NJ.  Upgrades of the
PTA in Edison, NJ are being planned.  These research programs expect to generate products that can
reduce cost and increase benefits to utilities in the condition assessment process and condition inspection.
An EPA-developed test apparatus can be utilized by EPA and its contractors or by others under an outside
user agreement.  Usage costs for non-profits may be waived or substantially reduced.

6.5.6       Support of Field Demonstrations.  The government can also support proper field trials of
various types of tools.  These should be real life situations - monitored,  recorded, and reported.  They do
not serve just as vendors' demonstrations.  Competing vendors could inspect the same pipeline where
practical to allow a direct comparison to be made.

Some utilities may be prepared to pay or make a contribution for high-quality inspection information that
has direct use in their condition assessment work. Recent experience indicates that utilities are cutting
back on inspection because of lack of funds.  Some technology vendors  may be prepared to subsidize the
costs of investigations but may not be able to cover everything, and would expect to be paid for good
quality data.

Bringing both clients and vendors together on relatively unproven technologies can be difficult. Federal
support would facilitate this work. It could take the form of a partnership with a group of utilities,
vendors, and research organizations with the aim of developing a structured program.  Some funding
would be required for the work involved in developing the program, monitoring, recording, and reporting
the trials. It may be necessary to provide some subsidy, for instance, when two technologies are tested on
the same line.

Federal support in these areas will:

       •   Provide the potential users and the developers with understanding of the advantages and
           limitations of the technologies and the tools

       •   Accelerate acceptance and use of inspection tools and methods.

6.6        Getting Utilities to Buy-In

Several studies have shown that the benefits of condition assessment and the techniques used in
inspection, assessment, and prediction are not well understood in  the industry. Some predictions from
earlier models and curves were costly to produce and did not tie in well  with operational experience,
resulting in a loss of credibility.

After credible analysis of the cost-benefit trade-offs, it will be equally necessary to communicate the
benefits through various channels, including workshops, teleconferences, papers, and articles. By raising
awareness and interest, the benefits of adopting the methods and technologies will become apparent to the
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utilities.  They will adopt these techniques only if such an action helps them save money, make their work
easier, and make their customers happier.

As suggested in Section 6.5.5 and 6.5.6, field trials will be a key way to show utilities what can be done
and at what cost.
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                                     7.0 REFERENCES
AMSA. 2002. "Managing Public Infrastructure Assets." Association of Metropolitan Sewerage
       Agencies.
API. 2002 . Risk Based Inspection. API Recommended Practice 580. API Publishing Services,
       Washington, B.C.
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                                             65

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                                        APPENDIX A
               CURRENT AND DEVELOPING INSPECTION TECHNOLOGIES
It should be noted that much of the information in this appendix was obtained from the vendors or
developers and is provided on that basis. A critical evaluation would require extensive testing under
controlled and field conditions.
A.I    Overview of Fielded and Demonstrated Inspection Technologies
A.1.1
Hand Held Ultrasonics
Many similar hand held tools are available for purchase.  Figure A-l shows views of two tools being used
in the field. The following are some examples.

                        Figure A-l. Hand Held Ultrasonic Testing Tool
A more sophisticated tool that can scan the wall of a pipeline has been developed by GE Inspection
Technologies (GEI), a leading inspection group.  The IAS50 consists of a high performance, five-channel
ultrasonic test kit coupled with a two-axis motion controller and data acquisition system.  It can scan on
flat or curved surfaces and has the capability to map flaws and thickness, and internal and external
corrosion loss. It contains built-in remaining strength analysis software.  The IAS tool scanning the
external wall of a pipe is shown at Figure A-2.

Ultrasonics is also the basis for a range of intelligent pigs developed for the oil and gas industry.  Such
tools are based on direct contact with the pipe wall.
                                               A-l

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                  Reprinted with permission of GE Inspection Technologies.

                       Figure A-2.  IAS50 Ultrasonic Scanning Tool (GEI)
A.1.2
Automated Ultrasonic Testing
The ultrasonic thickness measurement process has been automated to increase inspection speed and
repeatability. Fully automated, turnkey ultrasonic inspection systems are available to perform high-speed
ultrasonic thickness imaging, referred to as automated ultrasonic testing (AUT), of large structures such
as plate stock, pressure vessels, storage tanks, pipelines, and ship hulls.

Figure A-3 shows a typical system configured to inspect a 12-in. diameter pipe for internal corrosion.
The sensor moves back and forth along the axis of the pipe. A water source provides the necessary
coupling fluid to transmit the ultrasound into the pipe to obtain the thickness measurements.
           Figure A-3. Water Column-Based Automated Ultrasonic (AUT) Scanner for
                                   Measuring Wall Thickness
                                                A-2

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Magnetic wheels hold the unit to the pipe and are indexed to attain measurements in successive scan lines
around the pipe circumference.  About 10 min is required to cover a swath 18 in. wide around the full
pipe circumference. These systems produce maps of wall thickness, shown in Figure  A-4, which are easy
to interpret using standard personal computers. Local inspection service providers have ultrasonic
inspection equipment readily available and typically provide a complete inspection service for about
$2,400 per day. This fee includes the cost of operating the equipment, the personnel to perform the
inspection, and an inspection report.
0
3
6
9
12
15
18
                 The nominal thickness is 0.365 (green), the weld is added material (blue), and the
                 corrosion pits appear in yellow, red, and magenta.

                         Figure A-4. AUT Output of Pipe Wall Thickness
A.1.3
C-Scan
This tool shown in Figure A-5, developed by Body cote UK, maps an area of pipe wall and identifies
external and internal pits. It requires the pipe to be exposed externally and external coatings to be
removed from a minimum strip of 300 mm around the circumference. It takes thousands of readings on a
2 to 3 mm grid. The close grid setting and number of readings should provide an accurate definition of
metal loss. This tool is not currently available in North America but similar tools are available from U.S.
vendors.
A.1.4
Guided Wave Ultrasonic Systems
Teletest is an example of a tool available commercially.  It is used on steel pipe with welded joints that
provide the continuity (Figure A-6). The diameter range  is from 2 to 48 in.  The transducer is mounted on
an exposed section of pipe about 18 in. long. Typically the length of pipe that can be scanned is
approximately 100 ft. It works for pipes that are insulated or coated and it is particularly useful for buried
pipelines and road crossings.

Another example, based on the guided wave principle, is  the Long Range Ultrasonic Testing tool, which
claims to be able to inspect insulated welded steel pipelines over long lengths while the line  remains in
service. It can detect both internal and external corrosion.
                                                 A-3

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Reprinted with permission of Body cote PDL.





                 Figure A-5. C-Scan from Bodycote
Reprinted with permission of TWI Technology Centre.




Figure A-6. The Teletest Remote Detection Tool Showing Transducer
                                  A-4

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A.1.5
Magnetic Flux Leakage Tool for External Investigation
A tool based on this principle has been developed by a U.K. company (AES Ltd.) for water, wastewater
and gas ferrous pipes investigation.  The AES 519 has been extensively used in the U.K. and also in
Europe and Australia. One version used for pipe diameters of 3 to 12 in. is an external full
circumferential wall inspection tool  (Figure A-7). For diameters up to 6 in., the exciter and sensor ring
wrap around the pipe and the tool moves along the pipe. For diameters of 8 in. or more, pipe inspection is
by segments.

ECAT (External Condition Assessment Tool) is designed for non-intrusive assessment of larger diameter
ferrous pipe wall conditions. This tool, which uses the same basic technology, carries out a series
(Figure A-7) of inspection sweeps using a carrier mounted on guide rails.  It is designed to work  in
diameters of 12 in. and greater. The data can be displayed in both 3-D graphical and numeric form.
    Reprinted with permission of AES Ltd.

                  Figure A-7. AES S19 and AES ECAT Pipe Wall Inspection Tools
Magnetic flux leakage (MFL) is the most commonly used inspection technology for ferrous pipelines
today, holding over 80 percent of the oil and gas inspection market. Numerous inspection companies
provide the service.  Figure A-8 illustrates an MFL type of pig.
A.1.6
Remote Field Eddy Current
A number of remote field technology (RFT) tools are in commercial use for ferrous pipeline inspection.
A major advantage is that RFT does not require close contact with the pipe wall and tools are designed
with a minimum clearance of 0.25 in.  This allows the tool to pass local diameter reductions and deposits.
It also allows scanning of ferrous pipes with internal linings including cement mortar, epoxy and PE.
RFT technologies have some inherent limitations:

       •   Frequency: most systems are frequency dependent or have a limited number of frequencies to
           operate at. This limits the material thickness variations that are detectable.

       •   Size and shape of sensors: the transmitter and receiver size and shape affect the operational
           frequency, so antenna configuration is not easily altered to suit survey configurations.
                                               A-5

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                 Reprinted with permission of GTI

                             Figure A-8.  An MFL In-Line Inspection Pig
Russell Technologies of Canada has been involved in the development of a number of RFT tools mainly
for oil and gas applications.  They were closely associated with the development of the Hydroscope tool.
The Hydroscope Company is currently no longer offering inspection services.

A.l.6.1    "See Snake". The current main range of tools is based around the name "See Snake" which
operates in diameters from 2 to 14 in., although the company states they intend building larger versions.
The "See Snake" tool modules, illustrated in Figure A-9, allow for a large degree of flexibility with a
capability of negotiating 90 degree bends.  The spacers center the tool and direct contact with the pipe
wall is not required.  The tool can be free swimming or tethered on a wire line. Lengths up to 3,000 ft can
be inspected from one launch point when wire line tethered.  The free swimming version can inspect
lengths up to 15,000 ft from the launch point. A "T" or "Y"  piece needs to be retrofitted into the line to
provide a launch trap. The tool is propelled through the  line  by the product flow or compressed air while
the line is in operation.
        access module   battery module
spacer
module
detector electronic
module 1
                                                                             detector module
                                electronic module    exciter
                                               module
                           detector electronic
                           module 2
Reprinted with permission of Russell Technologies

                          Figure A-9.  "See Snake" Modules and Spacers
                                                 A-6

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To date the tool has been used in lengths up to about two miles from the launch point. Russell
Technologies claim that they can identify and measure internal and external pitting and remaining wall
thickness to an accuracy of 20 percent. The "See Snake" cannot distinguish between internal and external
defects. The "See Snake" is powered by internal batteries and the collected data are stored onboard and
downloaded by USB or Bluetooth connections.

Reported "See Snake" specifications are:

       •   Run time: minimum 5 hr
       •   Speed: approx. 10 ft/min
       •   Pipe thickness: up to 0.5 in. steel;  1 in. for cast iron
       •   Pipe diameters: 2 to 14 in.
       •   Clearance is 0.25 to 1 in. around tool
       •   Tool length is approximately 20 times diameter
       •   Can negotiate some bends.

The limitations on thickness of 0.5 in. for steel and 1 in. for cast and ductile iron should not be a problem
for diameters up to 14 in.

Russell Technologies has also adapted a tool used for inspection of well casings and ferrous pipelines
with or without internal linings and of diameters greater than 24 in. The line needs to be closed down and
dewatered to allow an operator to "walk" the tool through the line collect data.  The tool is shown in
Figure A-10.
                           Reprinted with permission of Russell Technologies

                      Figure A-10.  Russell Technology Internal RFET Tool
                                                A-7

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A. 1.6.2    Mainscan. This is an RFT tool that has been developed in Australia by Earth Tech
Engineering.  It uses the response of a single frequency in the remote field region to determine the
thickness of remaining metal. The equipment consists of a 16 channel CPU unit, a laptop computer and a
scanning head.  The probe module houses two differential and two absolute coils.  The differential coils
used with an X-Y display detect and display absolute defects such as pits.  The absolute coils are used to
detect and quantify general wall loss.  Data are gathered and saved for analysis as the scanning head is
moved across the pipe surface (Vickridge et al., 2006).

A.l.6.3    Broadband Electromagnetic. A series of tools have been developed and patented by Rock
Solid Pty. Ltd., an Australian company. BEM is one application of electromagnetic or eddy current
systems. The technique works by inducing eddy currents to flow in close proximity to a transmitter.  In a
ferrous pipe these eddy currents migrate with time allowing a complete profile of the ferrous pipe to be
obtained.

By assessing the primary and secondary induced currents it is possible to gauge the thickness of the metal
and to evaluate the metallurgical changes such as graphitization.

If a fracture exists, the scanned area of the fracture acts as a short circuit for the primary induced current
and perturbs the shape of the possible primary induced current. This perturbation is easily detected.

Typically, eddy current (EC) tools have either one or a limited number of signal frequencies at which they
can operate. BEM differs from other EC tools by being frequency independent. This means that the
frequency at which it operates can be altered or modified to suit the material and site conditions.

Various sizes of sensors are used, with the standard having a 2-in2 footprint. The sensor measures the
thickness of metal under the footprint and provides an average thickness over that area. Thus individual
pits will not be identified except as a general loss of material. It is claimed that metal loss can be
identified to 10% of the wall thickness in the area under the sensor. Any wall thickness can be scanned.

An available 1-in2. sensor provides a higher degree of accuracy when needed as the footprint is only 1 in2
rather than  4 in2. Sensors are made up into antennae with anywhere between 1 and 6 sensors.

The data are seen in real time on the computer screen as a traffic light display but can be fully processed
by the vendor and displayed as a contour plot although this adds to the cost. See Figure A-11 which
shows the comparison between the real time results and the same data analyzed and processed.

A major advantage is that BEM does not require close contact with the metal as the depth of penetration
of the magnetic flux is around 2.5 times the transmitter diameter. This capability allows BEM to scan
through coatings, linings and insulation.

One disadvantage when scanning pipelines internally, compared to other technologies, is that the process
is not continuous and therefore it takes more time to survey a pipeline.

A typical external scanning operation is shown in Figure A-12.

The costs of external scans are comparable to ultrasonic costs with the cost of exposing the pipe under
roads being the major cost.
                                                A-8

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            Distance along Pipe
                                                             Distance along Pipe
                                                  a
                                                  •s
            Real-Time Display
                                         %nc
                                                       D    IDG  33D   30D
                                                               Processed Data
Reprinted with permission of Rock Solid Pty


        Figure A-ll. Post-Survey Data Processing, Analysis, and Plotting
  Reprinted with permission of Rock Solid Pty.


   Figure A-12.  A BEM Hand Held Tool Being Used to Scan a Gray Iron Pipe
                                         A-9

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For internal scanning the antennae are made up into an in-line inspection pig.  Pipes of 4 in. in diameter
and more can be scanned with an internal tool.  Access to the line is required and it must be out of service,
emptied and cleaned of loose deposits.

The pig can be moved by hydraulics or by push or pull rod devices. Normally, the pig is designed to fire
off each 6-sensor antenna successively so that the pig travels for 12 in., takes a reading, and moves on.
This is relatively slow and means that a line has to be out of service for several days as well as being

dewatered and a section removed to gain entry. A BEM pig for a 24-in. diameter internal scan is shown
in Figure A-13. Because of the large number of readings, the cost becomes significant.

Other tools have been developed using the same basic EM principals.  These include a hand held tool that
takes corrosion pit readings without the need for cleaning and measuring required with traditional
approaches.

The company also has a modification that will operate an antenna on a rod attachment to take scans on
top of pipes exposed in keyhole (vacuum) excavations. This has the potential to provide information
about pipe condition (wall thickness) without disrupting service or involving the heavy cost of full access
excavations.

A.I.7      Soil Investigation Technologies

Some tools for field testing provide a direct approach to capturing the data.

A.l.7.1     NovaProbe.  Russell Technologies of Canada has developed the NovaProbe which
simultaneously acquires soil related properties at the pipe depth and surrounds (Figure A-14).  The
properties that it acquires are:

        •   Resistivity
        •   Pipe to soil potential
        •   Soil redox potential
        •   Soil temperature
        •   pH.

It does not collect data on chlorides and sulfides.

A.I.7.2    Linear Polarization Resistance.  This technology is available from Earth Technology,
Australia. Essentially this evaluates external corrosion in the form of pitting based on soil aggressivity.
This is not a new concept but Earth Tech has refined the approach. LPR soil testing is an electrochemical
soil testing technique using soil samples taken from pipe depth to obtain a quantitative measure of soil
corrosivity (see Figure A-15). This approach provides a corrosion rate that can be applied for
extrapolation to quantitative time to failure calculate.

The process involves the use of a specially developed cell that provides a measure of the combined effects
of several soil parameters.  The assessment and time to failure calculation takes into account the pipe
class, age, length of main and type and life of coating.
                                                A-10

-------
       ,^«
/i&-&?3
     Reprinted with permission of Rock Solid Pty.

              Figure A-13. A 24-in. BEM In-Line Intelligent Pig
           Figure A-14.  The NovaProbe from Russell Technologies
                                              external DC
                                              power supply
         working
         electrode
Soil
-  reference
   electrode

     "inert"
     counter
     electrode
                 Figure A-15. LPR Ferguson-Nicholas Cell
                                    A-ll

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A.2  Overview of Developing Technologies for Ferrous Pipe Investigation

For the sake of completeness a number of technologies that are under development or being tested are
noted.  At this time it is not thought that any are commercially available.
A.2.1
Super-Pig
Three UK water utilities developed the Super-Pig, the field testing being undertaken by Thames Water.
This tool is designed to provide a comprehensive condition assessment of a water line. The prototype was
developed for mains in the range of 200 to 300 mm (8 to 12 in.) and will identify wall thickness loss to  1
mm, longitudinal and circumferential cracks, damage to linings, and leaks (Figure A-16).
                 Reprinted with permission of Thames Water pic.

                           Figure A-16.  Ultrasonic Super-pig Modules


The pig is based on an electronic transducer array.  These arrays are battery powered and miniaturized
and designed to collect and store data over several miles of inspection. For example, it generates 30 GB
of data for three miles of survey. It uses water as the contact medium and transducers are not in direct
contact with the pipe wall. It can see through thin internal linings that are fully bonded to the pipe wall,

but it is reported that close fit polyethylene linings and thicker linings such as cement mortar present
difficulties.  The pig can operate with a water main in service but needs special launch and recovery
facilities which need to be retrofitted to the line.

To date it has been used on proving trials and is stated to have performed well.

A.2.2      EMAT - Electro Magnetic Acoustic Transducer

EMAT is based on a coil in a magnetic field at the surface of the pipe internal wall. Alternating current
through the coil induces a current in the pipe wall causing Lorentz forces which in turn generate
                                                A-12

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ultrasound. Lorentz forces are forces acting on moving charges in magnetic field.  The type and
configuration of the transducer defines the types and modes of generated ultrasound and the
characteristics of propagation through the pipe wall.

The advantage of such a tool is that it does not need a couplant.  EMAT is dry coupled and suited to gas
pipelines. It is capable of identifying a wide range of defects including internal and external metal loss
and cracking. The disadvantage is that it needs to be very close (1 mm) to the pipe surface. The
transmitted low frequency ultrasonic energy is a limitation on resolution.

 A.2.3     "No Pig"

This is another tool that was developed for non-piggable oil and gas lines. The above-ground tool detects
and measures corrosion in lines that are not suited to in-line inspection.  It uses an applied signal of
various frequencies at two points along the pipeline up to 1 km apart.  The magnetic field at these
frequencies is measured  at inspection points along the line.

Calculations are made to determine a cross-sectional position of an equivalent current line. Due to the
skin effect, a variation of this position with frequency indicates a local wall thickness reduction. This
dependence is evaluated quantitatively to give the percentage of the metal wall loss.
This technique has not been commercialized.

A.2.4      Non-Contact Ultrasonics

The New York City Department of Environmental Protection  (NYCDEP) commissioned research on non-
destructive investigation offeree mains.  The cumulative effort of all the research into available
technologies concluded that in 2006 an ultrasonic based crawler developed jointly by Inspector Systems
GmbH (Rodermark, Germany) and the RTD Group (Rotterdam, NL), was the most fitting technology for
internal inspection offeree mains (see Figure A-17). The technology has been verified for internal
inspection of pipes and is commercially available.
                  Reprinted with permission of NYCDEP

                              Figure A-17.  The Ultrasonic Crawler
                                                A-13

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The ultrasonic crawler system consists of a video inspection system robot with a ring of ultrasonic
transducers at the back of the crawler.  Main features of this system are highlighted below.

Crawler System. The Video Inspection crawler has the ability to climb/descent vertically while moving
both forwards and backwards and to negotiate all standard bends >1.5 D.

RCCTV: The pan and tilt camera allows to rotate 360° and to sweep 135° up and down. Together with
the integrated zoom, focus and high intensity light source, it is possible to have a direct view to each point
inside the pipe. The accuracy of the video inspection crawler including the high resolution camera is
better than 1 mm (length and width) in a pipe with diameter < approximately 23.6 in. (600 mm).

Non-contact Ultrasonics: The ring of ultrasonic sensors can be seen in Figure A-18. They scan the pipe
continuously and transmit data to the control which analyzes the data and generates a profile of the pipe
wall.

Crawler Connectivity. The crawler is connected to a special fiber optic cable for remote control and video
transmission.

Inspection/Scan Length: The crawler can travel at the speed of 200 m/h (660 ft/hr) and can inspect pipes
up to 500 m (1,650 ft in length).

Pilot Testing: A pilot testing of a steel pipe of 18 in. in diameter and 100 ft in length was carried out in
Rotterdam by RTD. The pipe had hidden damages that were to be detected by the crawler.  It was
demonstrated during the pilot testing that the crawler could detect loss in pipe thickness of steel pipes
successfully.

Information is awaited on full-scale trials that the NYCDEP is proposing to undertake later in 2008 in the
field on force mains.
                   Reprinted with permission of NYCDEP

                    Figure A-18. Ring of Ultrasonic Sensors Marked by Arrow
                                                A-14

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A.2.5
Acoustic Based Technology for Non-Destructive Testing Condition
A Canadian company based in Toronto, Echologics Engineering Inc., has entered into a collaborative
research agreement with NRC of Canada to develop and commercialize this technology. It is based on
utilizing the propagation and characteristics of acoustic signals (Hunaidi, 2006).

The technology works by measuring how quickly acoustic signals are transmitted along a section of pipe.
Acoustic signals are induced in pipes by releasing water at fire hydrants in a controlled manner.  Then,
they are measured using acoustic sensors positioned at two longitudinally separated points on a pipe. The
sensors are attached at easy-to-access points, such as fire hydrants and control valves, or directly on pipes
in existing access manholes.  A schematic of the measurement setup is shown in Figure A-19.  The
acoustic propagation velocity is calculated based on the sensor spacing and time delay between the
measured acoustic  signals. Average wall thickness of the pipe section between the acoustic sensors is
then back calculated from a theoretical model of its relationship with the acoustic velocity, the pipe's
internal diameter and Young's modulus of its wall, and the bulk modulus of elasticity of water, all of
which are usually known or easily determined.
                                          PC-based correlator
                                     /^^Z*
                                           "V
                                      LI

 Figure A-19. Measurement of Acoustical Propagation Velocity Using: (a) an Out-of-Bracket Noise
                             Source; (b) an In-Bracket Noise Source

    (a)  Wave propagation velocity (v) = D / AT, where AT is time delay between signals 1 and 2
    (b)  Arrival time of signal 1 = TI = LI / v, where v is sound propagation velocity in pipe
        Arrival time of signal 2 = T2 = L2 / v
        Time lag between signals 1 and 2 = AT = T2 - Tj = (L2 - Lj) / v
        v = (L2-L1)/AT
The length of the pipe section over which the acoustic velocity is measured can be arbitrarily chosen.
Initially, a section 100 to 200 meters long, which is the usual distance between fire hydrants or valves in
urban areas, may be chosen.  Subsequently, if a higher resolution is needed where there are concerns
about a particular section, the resolution can be increased by moving the acoustic sensors closer together.

Velocity measurement can be performed with hardware normally used for locating pipe leaks using the
cross-correlation equipment, as shown in Figure A-20. However, measurement of the velocity tends to be
                                                A-15

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more technical than the usually straightforward leak correlation. Velocity measurement and wall
thickness calculations are made in real time using specially developed software, trademarked as
"ThicknessfinderRT". Recent research and development have led to a refined theoretical model for non-
uniform pipe sections, an optimal procedure for acoustic velocity measurement, and a method for
inspecting the quality of the measurements.
                                                                      Cable Drum
                                                   Hi  Processing Unrt  (With Chloros Bath)
                                                 | (Audio 8t video Output)
                   Reprinted with permission of WRc

                      Figure A-20. Schematic View of Sahara® in Operation
Remaining pipe wall thickness predicted by NRC's acoustic technology represents an "effective" value
from a mechanics of materials point of view and subsequently it reflects general structural deterioration of
the pipe. Therefore, ferrous pipes in corroded condition may be significantly worse condition locally than
the average thickness indicates. This is not a limiting aspect for some pipe types such as asbestos cement
(AC) as generally such pipes will have a more-or-less uniform thickness profile. The developers
acknowledge that this is a limiting factor for ferrous pipes as average thickness between two sensors is
not the key concern.  Echologics is conducting further research and development on this issue.

Pilot tests have been undertaken on 10 sites on the water distribution system of the City of Toronto.  Pipes
were all pit- or spun-cast iron with diameters up to 20 in. The results coincided with independent testing
of samples for average thickness loss. Echologics has undertaken condition assessment in a number of
other sites. At Maple Ridge, British Columbia, 21 sections were  surveyed. Pipes were ductile iron, cast
iron, and AC in diameters from 100 mm to 200 mm (4 to 8 in.). In Las Vegas, two sections of 150 mm
(6-in.) AC pipe were assessed and found to be in good condition with thickness greater than the records
(probably due to a higher class of pipe being installed than recorded).
A.2.6
Robotic Arm with Sensors
A current project of NRC and the University of Regina is to develop a robotic arm capable of
manipulating sensors in water mains. A robotic articulated arm would be mounted on an inspection robot
that would travel through a pipeline. Sensors mounted on the arm would be moved into position to take
readings on the pipe wall.  Sensors could be of various types including ultrasonic.
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A.2.7      Autonomous Underwater Vehicle

NRC also has an ongoing project to develop a torpedo like vehicle to inspect large water mains. It is
envisaged that a number of NDT techniques could be mounted and manipulated from such a platform.
These could include ultrasonic testing, laser profiling and a multi-camera vision system.
A.3     Leak Detection Technologies
A.3.1      Sahara®

The Sahara® tool is a single, 1-in. diameter hydrophone attached to a calibrated umbilical cable through
which data is transmitted in real time (Figure A-20).  In water mains a drogue is attached which propels
the tool through the line. The cable also controls the tool's speed and allows its retrieval. Sahara® can be
inserted into a line through any standard 2-in. tapping, such as an air valve in a water main, and can
survey up to 6,000 ft from the insertion point.  The location of the sensor can be detected from the
surface, using a walkover tool, so that the operator can mark the surface with the exact location of any
leak.  It operates on the principle that leaks cause turbulence, which in turn causes noise, and it detects
this noise.

Sahara® operates in any pipe material, in pipes 300 mm (12 in.) or greater diameter. Operating pressures
between 0.5 and 16 bar (7 to 230 psi) and flow velocities between 0.3 and 1.5 m/s (1 to 5 ft/s) define the
operating range of Sahara®. It has proven capable of locating leaks as small as 0.25 gal/hr with a high
degree of accuracy.

The cost of setting up an insertion point can be significant but the survey costs vary, depending on
amount to be  surveyed, but range from $2/ft for several miles to $4/ft for shorter runs.

The Pressure  Pipe Inspection Co.,  Mississauga, Ontario, is the licensee of Sahara® from WRc for North
America and  offers a leak inspection service.

A.3.2      SmartBall®

SmartBall®, developed by Pure Technologies Ltd, is  another example of an in-line detector. This is an
acoustic acquisition device complete with power supply contained within an aluminum casing and then
placed inside  a foam ball. The system can operate for up to 15 hr and is free swimming and capable of
investigating  pipes of diameter greater than 10 in. although it operates most effectively in diameters of 24
in. and greater.  SmartBall® can  be inserted and retrieved from an operational pipeline. It can be inserted
through a 4-in. open port valve or 3.5-in. air valve.

Prior to insertion a number of transponders will be  connected to existing appurtenances. These generate a
pulse  that is detected by the SmartBall® providing synchronization with known points.
                                                A-17

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Reprinted with permission of Pure Technologies Ltd.





         Figure A-21. SmartBall® Inspection Method - Insertion, Travelling, and Removal
                                                A-18

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                                        APPENDIX B
             FORUM SUMMARY, CONCLUSIONS, AND RECOMMENDATIONS
Approximately 34 technical experts and representatives from utilities, technology and service providers,
academia, research organizations, consultants, and EPA attended the two-day Technology Forum held in
Edison, NJ on September 9 and 10, 2008. The Forum consisted of a State of Technology Review Report
feedback session followed by six breakout sessions. A companion EPA report titled "Draft Forum Report
on Condition Assessment of Ferrous Water Transmission and Distribution Systems" has been prepared to
fully document the Forum presentations and discussions (Thomson and Wang, 2008). Presentations and
discussions from each session and major conclusions and recommendations are summarized below.

B.I        State of Technology  Review Report Review

The Forum attendees suggested some changes/corrections to the draft State of Technology Review
Report, but there were no major disagreements with the overall sense of the State of Technology Review
Report. The key points which arose from the open discussion are highlighted below.

One attendee suggested that more emphasis should be given to potential technology transfer from other
federal agency research developments. Some attendees expressed reservations because of the economic
and technical difficulties of transfer.

The relative benefits of inspection in terms of cost to asset value for small and large pipes were raised by
several attendees. There were two counter views. One considered that the total cost of the larger number
of small-diameter pipe failures was higher; therefore, reducing these failures would be more cost effective
than reducing the smaller number of large-diameter pipe failures. The counter view was that it was not
cost effective to inspect small diameter pipes.  The "fail and fix" approach or condition assessment based
on pipeline asset and failure data was cost effective for small-diameter pipes.

The definition of condition assessment was raised and its role in asset management. Current condition
assessment is based on individual pipe sections rather than a cohort approach. The current approach is
needed because  of the lack of homogeneity and the wide variations that occur in a set of pipes.

The lack of agreed rigorous definitions used commonly in the water industry was a key issue. One
example was the definition of failure. Some attendees considered that any event that would require
remedial action, including repairing a leaking joint, constituted a failure. The counter view was  that
failure should be defined as when the pipe no longer was operating and serviceable. Leaks should be
defined as defects that needed to be fixed but did not stop a  pipe from being serviceable.  The term "Pipe
Life" was another term that was not rigorously defined.  The "Design life" was not thought to be a useful
concept and an alternative of "Economic Life" was suggested where the cost of maintaining the  line in
service became excessive.

Written comments were received from the project stakeholders and have been incorporated into  the Final
State of the Technology.

B.2        Large-Diameter Cast Iron  Pipes

Presentations included an overview by Yehuda Kleiner, NRC of failure modes and mechanisms  of ferrous
pipes and case studies on large-diameter  cast iron pipe failures experienced by the City of Cleveland and
Washington Suburban Sanitary Commission (WSSC).
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The overview of failure modes for cast iron pipes emphasized the need to understand failure modes and
mechanisms. Some key points that have arisen out of NRC work were:

        •   Pipe age is generally not a good indicator of pipe condition

        •   For small-diameter distribution water mains, the strategy should be to manage failure
           frequency. For large-diameter transmission mains, the strategy should be to prevent failures
           because of the potential of high consequences

        •   There are highly variable properties in cast iron pipes

        •   Variable delivery and installation practices could lead to built-in defects.


Large-diameter CIP and DIP are identified as high-risk and high-interest pipe scenarios for which better,
cost-effective condition assessment capabilities are recognized by the user community as valuable,  but
not attainable with available condition assessment tools (e.g., databases, inspection technologies, and
deterioration and failure models). Many different mechanisms and parameters are involved in corrosion
and failure of ferrous pipes. CIP can fail due to the rigid nature of joints, the lack of tensile strength, and
weakening due to graphitization.

An ongoing Water Research Foundation/NRC study revealed that the large-diameter CIP failures
experienced at Cleveland were likely caused by longitudinal and bell cracks, which may originate from
defects or damages caused by manufacturing, delivery, or installation practices. The low rate of failure
(0.07%) did not justify any replacement program and inspection of the bells to find growing cracks is
technically difficult because of the complex geometry.  This case study generated a lot of interest and
discussions as to whether potential technologies, such as the RFT and BEM, might be possible to detect
the bell cracks, whether similar failures were occurring elsewhere, and whether this high-risk scenario
would offer an opportunity to improve condition assessment capabilities.

Potential difficulties in internal inspection due to fittings, tuberculation, etc. were reported. Utilities like
WSSC placed emphasis and value on data mining using extensive field records, GIS, and "Google Earth"
to help survey the pipeline and assess the condition of their large-diameter CIP. Field records should be
consistently updated when the opportunity occurs during excavations and new installations.

B.3        Large-Diameter Ductile Iron Pipes

This session focused on the corrosion issues with DIP and case studies provided by WSSC and Louisville
Water Company (LWC).

Mike Woodcock of WSCC emphasized that like all materials DI had limitations and it was important that
users understood these. He did not agree with the State of Technology Review Report where it was stated
that most DI was polyethylene wrapped.  Much of WSSC's DIPs were not wrapped but laid bare.
However, larger diameters were protected cathodically. He considered that a typical life for DIP in
WSSC was 30 years.  He pointed out that the thinner wall for DIP meant failure earlier when corrosion
was present.

He discussed and illustrated the changes  in DIP and coatings over the years. Originally DI was produced
from nearly pure iron, but the much greater use of scrap metal has resulted in a differing metallurgical
structure that has the same strength properties, but may not have the same corrosion resistance. He also
had concerns that some manufacturers were not heat treating pipe to the same extent because of high
energy costs.
                                                B-2

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Greg Home of DIPRA presented on "Ductile Iron Pipe Failure Modes and Condition Assessment
Practices". He accepted that deterioration can occur but the problem lay in how to decide which pipes
need to be fixed. He did not consider that current inspection tools could provide this information cost
effectively. He recommended that condition assessment based on records was needed. He showed a
series of slides to illustrate this approach which included asset databases, customer complaints, and break
and leak records. He reiterated that CIP could fail due to its rigid nature and that DIP fails usually due to
corrosion. As corrosion was the potential problem for DIP he recommended that areas of potential soil
corrosion be identified by soil testing and use of the DIPRA "Design Decision Model" using
consequences and likelihood of failure ratings.

Dale Lindemuth of CORRPRO presented on "External Corrosion Condition Assessment Procedures".
The thrust of the presentation was the possible application of External Corrosion Direct Assessment
(ECDA) methods, which were developed for the oil and gas industry, to the water industry. These
methods are used for the condition assessment of pipelines that cannot be inspected by direct inspection
technologies. There are four stages involved in the ECDA:

        •   Stage 1. Pre-assessment data gathering and planning

        •   Stage 2. Indirect inspection with a number of different approaches. The outcome of this stage
           is to integrate and analyze all data and develop rankings to select the most likely sites for
           direct examination

        •   Stage 3. Direct examination involving excavations to expose the pipe and taking direct
           readings and measurements

        •   Stage 4. Post assessment with the main activity being to calculate remaining life by different
           methods.
Cathodic protection was recommended as being a viable method.

The final presentation was by Keith Coombs of the LWC "Case Studies from Louisville Water
Company". The overall goals of the company were the reduction of breaks to 600 per year, the
elimination of unlined CIP and the replacement of two vintages of CI mains showing a much higher break
frequency. Vintages of 1862 to  1865 and 1926 to 1931  had high break frequency and would be replaced
and upsized where necessary.  Pipes of the 1866 to 1925 vintage had minimal maintenance history and
were adequately sized so they could be rehabilitated.

The discussion that followed on  Sessions 1 and 2 emphasized a number of key issues. Several speakers
expanded on the multiplicity of defects and their causes in ferrous pipe and the need to understand "What
you were looking for," and then  use the appropriate technology to find it.

In responding to a question about whether possible limitations to condition assessment arose from the
hardware or the signal processing, one of the leading technology developers pointed out that the real
limitations lay in the basic physics, which cannot be changed.

One university delegate suggested that in view of the costs and disruption involved in internal
investigations, multisensory platforms should be used to collect all possible data at one pass. The
response from a utility delegate was that this resulted in data overload and delays in getting key results
which needed to be immediately available to determine remedial works while the pipe was out of service.

The problems of access and disruption that are involved in internal inspection suggested that greater
consideration be given to developing external non-intrusive inspection and combining limited direct
inspection with asset, soil and coating data. Some inspection companies were developing this approach.
                                                B-3

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A broader issue was the utilities' approach to the value of inspection. A leading inspection vendor of
ferrous pipes said that direct inspection costs were around 4 to 5% of the asset value but with a further 4
to 5% of indirect support cost. This was well above the highest figure of 5% of asset value that utilities
felt that they were prepared to pay according to an AwwaRF study. A leading utility representative stated
that he felt that utilities were aware of the technologies but needed to understand the value of inspection
in reducing failures before they would begin using them.  Another speaker felt that, as with PCCP, the
critical need that condition assessment should address is to reduce catastrophic failures where the
consequential cost is high.

In conclusion a speaker pointed out that a utility inspection only told you that you had a problem.
However,  it did not solve the problem.

B.4        Leakage Management

Mark LeChevallier of American Water opened with "American Water Leak Detection Technology
Update". He described their experience with AMR and how it became cost effective by coupling with
water leak detection. A number of permanent and semi-permanent water leak devices based on acoustic
monitoring tools were described.  The data could also be mined to relate leaks to temperature changes and
patterns that repeat annually and revealed that the maximum number of leaks seemed to occur in the fall.
Conclusions to date  include:

       •   Acoustic monitoring works and may reduce leakage about 30  to 50% mainly on low-medium
           leaks

       •   Early detection and repair reduces operational cost

       •   Leaks increase with water temperature drop.  Large temperature drop trigger larger main
           failure

       •   Many leaks start in the fall

       •   Acoustic monitoring does not find all leaks because of background noise

       •   Acoustic monitoring and area metering can work effectively together

       •   Acoustic monitoring and area metering analysis  and decoders can identify metered leaks.

The second presentation "Optimizing Water Pressure Management to Sustain Distribution Infrastructure"
was presented by George Kunkel of Philadelphia Department of Water. In opening, he emphasized the
need to find ways to activate utilities to take action on water leakage as most utilities do not have any pro-
active approach. He described three components of leakage - reported, unreported, and background
leakage. Philadelphia had reduced leakage by about one third. He then described appropriate approaches
to intervention. This was  followed by a representation of the four components of managing real loss to an
economic  level:

       •   Active leakage control
       •   Pressure management
       •   Improved system maintenance, replacement and rehabilitation
       •   Improved response time to leak repair.

The second part of his presentation described Philadelphia's  DMA project.
                                                B-4

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Brian Mergelas of Pressure Pipe Inspection Company (PPIC) presented "Recent Advances in Leak
Detection Technologies" based on the Sahara® system licensed internationally from WRc the developer.
Sahara® in-line leak detection is able to identify small leaks of less than 1 gal/hr in operational lines due to
the proximity of the acoustic sensor as it passes a leak.  It is suitable for diameters of 12 in. and greater.
Up to 6,000 ft can be surveyed from one insertion point and one to two miles of line can be surveyed in a
day. It is inserted by means of a 2-in. tap. All leaks were not created equal, and many leaks were found
that had not appeared at the surface.

The returns from a Sahara program were illustrated by reference to five projects.  The client cost per mile
in line preparation was about $25,000 and the Sahara® survey cost $25,000 per mile. Using the number
of leaks detected and the cost of repair a total cost was determined. The savings from break avoidance in
terms of value of water recovered at 50% of retail price was calculated and the comparison of net benefits
against cost showed rates of return on the investment all in excess of 1,000%.

PPIC have recently introduced a video camera which can be inserted into an operational main through the
launch point.  He showed examples of the pictures obtained of the inside condition of the pipe including
air pockets.

The final presentation was by Michael Higgins of Pure Technologies "Leak Detection Ball for Large
Diameter Pipes and Future Leak Detection Technologies"

He set out the following goals of inspection:

        •   Reliability of detecting defects
        •   Pipe remains in service
        •   Non-intrusive
        •   Direct test for long pipelines
        •   Inexpensive to deploy.

To his knowledge, currently there were no tools that met all these criteria. One of the tools that Pure has
developed is Smartball®.  The ball is free swimming and propelled through the line at near flow velocity.
An acoustic ping is emitted every three seconds which allows tracking equipment to follow the ball.  It
follows the dominant water flow and passes around bends and fittings.  It can record data up to 12 hr so is
able to monitor many miles from one insertion. The tool requires a 4-in. port for insertion and removal.

A future approach to  permanent leak detection was based on the use of acoustically sensitive fiber optic
cable which could be up to 25 miles long.  This was seen as being a tool that would be installed in key
trunk mains and provide continuous permanent monitoring.

The key points which arose from the open discussion on leakage management are highlighted below.

On the question of how to convince utilities of the technical and economic feasibility and value of
reducing leakage, there was a variety of responses. It was pointed out that unlike countries, which had
achieved significant leakage reduction, there were no real drivers in the U.S. One vendor said his
experience was that there were a whole range of clients from pro-active to reactive. So some utilities did
not need convincing.

The representative from Philadelphia Water pointed out that there were many low tech utilities doing
nothing  and using low tech designs.  He cited utilities who could not isolate areas because they either did
not have valves that were operational or, in some cases, did not know where the valves were.
                                                B-5

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Another speaker pointed out that he had problems of convincing utilities and particularly operators of the
value of inspection because they did not wish to have anything which might disturb the day-to-day
operations.

Steve McKellar referenced the U.K. experience with DMAs and suggested that it would be insane not to
use this approach. He pointed out that all the major U.K. water utilities had been using DMAs now for 10
years and there is 75 to 90% coverage of the network. It is almost mandatory now that UK utilities use
DMAs because of the leakage reduction that could be achieved.

It was questioned if leak monitoring combined with other data could provide information on condition
and if additional tools could be added to provide information on structural condition.

WSSC believed from their experience that the data collected by Sahara® and SmartBall® contained a great
deal of additional information which could be extracted by improved signal analysis. For example, the
individual key pipelines could have each pipe tagged so that as the tool passed it could be identified. It
was thought that more could be done to closely identify defects and their locations.

A suggestion was made that a common system was needed to describe the different forms of leaks that
were found and repaired.  As illustrated in the literature, a wide range of leaks occur. Leaks could be
from joints, fittings, perforation, and breaks. These failure data would be invaluable in understanding the
nature and causes of leaks and the collection of the data should be undertaken by utilities in conjunction
with the vendors.

B.5        Prediction Models and Databases

The session opened by Yehuda Kleiner of NRC who presented "Small Distribution Mains Breakage
Frequency Modelling".

His understanding of what utilities wanted to know included:

       •   Remaining service life
       •   Criteria for replace or rehabilitate
       •   Optimal timing for renewal/inspection
       •   Allocations for future budgets.

Rather than demonstrating the models, he discussed the development and results of the models.  He
showed derived curves for small and large diameter pipes taking into account cost  of renewal and failure
risk giving a total expected cost. He showed how the bottom of this curve was the most cost effective
time of renewal. The time to renewal for large mains was much shorter on this basis because the failure
risk curve was much steeper. He believed that this was  the basis for managing small mains which was to
accept a higher failure frequency than for large mains where it is much more important to identify
impending failures.

Yehuda Kleiner commented on the pros and cons of modelling based on statistical  and physical
information. Statistical models are simpler and data are  more readily available. He  listed the data
requirements and the trade off between group size and homogeneity. The benefits  of opportunistic fitting
of CP anodes and retroactive systematic fitting were graphically illustrated. His final comments were
recommendations directed towards the need for robustness and simplicity in modelling.
                                                B-6

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This presentation was followed by Steve McKellar who outlined the "UKWIR Sewers and Water Mains
National Failure Database". Steve Mackellar pointed out that there were a number of differences between
the U.K. and the U.S. practices that needed to be taken into account. Operating pressures were higher in
the U.S; there was much greater use of PE for potable water in U.K. Probably the biggest difference was
the smaller number of large utilities in U.K. who were responsible for over 90% of the system and were
monitored for performance by a government appointed regulator. The regulator determined, from the
capital spending budgets and plans, the rate increases that would be allowed.

The initiative for development of National Failure Database was from UKWIR who wanted to:

        •   Create a repository for failure data
        •   Make data provision easy
        •   Make data use easy
        •   Manage data and keep secure
        •   Respond to changing needs.

Participation in the database is voluntary and the operation is financed by subscription.  Currently
participation is greater than 90%. The water database has now been operational for some years and is
proving to be highly beneficial to utilities in that they are able to compare their own experience with
failures and pipe materials against national experience.  The sewer database will come on line shortly.

In conclusion he showed a wide range of analysis that was possible. A range of data sets were shown of
different pipe types, failures, leakage and assets and how they could be used to undertake forecast
modelling and mains replacement.

Sunil Sinha of Virginia Tech presented "Condition Curves State-of-the-Technology" and
"Predictability/Preventability Indices" and his role in TO 62. Prediction deterioration models can be
grouped into five major categories:

        •   Deterministic
        •   Statistical
        •   Probabilistic
        •   Advanced mathematical
        •   Heuristic.

Water Research Foundation has  identified six concepts for modelling. Five of these were listed below:

        •   Main age of failure
        •   Total failures over time
        •   Breaks as functions  of single causative factors
        •   Break probability in next time period
        •   Aggregate data.

Sunil Sinha emphasized that sound  data had to be the basis of all modelling. It was not just taking data
from utilities which came in many forms. Virginia Tech on their other projects were taking the data from
utilities and interpreting it into their own format, which is termed "data cleansing". He emphasized that
they were not developing curves but looking into what might be possible.

He continued with his work on exploring the feasibility and  value of developing procedures for
calculating predictability and preventability indices.
                                                B-7

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        •   The predictability index will indicate the inherent, theoretical predictability of various types
           of pipe failure

        •   The preventability index will indicate the technical and economic feasibility of preventing
           pipe failure.

The predictability index was graphically shown in terms of five stages:

        •   Type of failure
        •   Failure mode and mechanism
        •   Variables that predict failure
        •   Develop scoring system for variables
        •   Pipe failure preventability index.

The development of a preventability index was shown in five stages:

        •   Identify water pipe technologies
        •   Evaluate technical feasibility
        •   Evaluate economic feasibility
        •   Develop rating system
        •   Preventability index.

The presentations in this session created significant comments and suggestions throughout the discussion.

One university delegate pointed out that in statistical modelling the stability of the model is essential.  In
this type of modelling it is necessary to create a population of individuals which remain stable. However
in real life the "pipe" individuals  change because of new works, repairs, and replacements. No longer is it
possible to accurately assign failures.  This was illustrated by another speaker who provided an example
where a utility had replaced a lot  of failing PVC with PE but the model attributed the earlier PVC failures
toPE.

She also commented that the data cleansing that Virginia Tech was proposing required a great deal of
effort. The representative  from NRC emphasized this point and pointed out the difficulties of obtaining
data to populate models. He also sounded a warning note on data cleansing and the momentous task
involved.  One set of 140,000 pipe records from one utility had proved to be unusable because of the way
they had been recorded. He considered that data recording had to be at utility level and involve operators
who had in-depth knowledge of the system.

Steve McKellar explained that the UKWIR database was based on two separate records. A higher level
geospatial database presented a picture of long term requirements and investment in the system. The
second was an asset database which provided the information at the operational level on pipe behaviour
and which to replace. This removed some of the difficulties discussed.  It was essential to have a
snapshot of changes and in U.K. the changes were recorded every year.  Since only 1% of the system was
replaced annually it was thought to an acceptable compromise.

On the use of curves or models, Mike Woodcock said that WSSC did not use such methods.  He felt that
the modellers were making things complicated. Using a GIS system, WSSC knew where their assets
were, the maintenance records, and where failures had occurred. There was no need to model; from this
information they could  analyze to prioritize their selection of where to replace or inspect. Models  don't
                                                B-8

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take into account extraneous considerations, which can be most important. It was suggested that Mike
Woodcock was actually modelling.

A speaker pointed out that the description of the parameters in Sunil's model did not include leakage,
which could be a valuable indicator of pipe condition.  This was accepted as being a valid comment. It
was pointed out that the factors used for predictability and preventability were the same.  The value of the
preventability index was questioned. Another comment was that the predictability of failure seemed to be
the same as the current models which used the term "the likelihood of failure".
One university delegate said that his concern in modelling was "Garbage In and Garbage Out".  There are
so many parameters in a model that you can make a model produce any desirable output. His advice was
to keep it simple.

B.6        Emerging Technologies

The session was opened by Marc Bracken of Echologics with "Condition Assessment of Water Pipes".
The basic concept of using acoustic technology to calculate the remaining wall thickness was developed
by NRC and is being further developed and commercialized by Echologics.

The method is based on how quickly low frequency acoustic signals are transmitted along a section of
pipe. Using this relationship between velocity of signal and pipe wall thickness it is possible to back
calculate thickness.  Varying pipe thickness around the circumference can be calculated as being uniform
or linearly variable.  The calculated pipe thickness was the average along the section being  inspected,
which was typically 100 meters long. Examples of inspections and findings on pilot tests on CI and AC
pipe were presented. The results of the inspections and the exhumed pipes were provided.

Krish Ramalingham of CCNY presented "Non-destructive Evaluation of Force Mains in New York".
The technologies being proposed for the evaluation of New York ferrous force mains has direct
application to the evaluation of ferrous water main condition. Initially asset information was collected
and a comprehensive database, standards for structural rating, and condition assessment framework were
developed. The tool that has been chosen for trialling is the Ultrasonic Crawler developed by Inspection
Systems GMBH. The tool is capable of meeting the criteria and can also  provide high resolution digital
video of internal condition.  It can be applied to different diameters and work through 1.5 diameter bends
and climb and ascend vertically. It can scan lengths up to 3,300 ft. The intention is to undertake field
trials in New York in early 2009.

Dave Russell of Russell Technologies presented "In-Line Inspection Tools (Intelligent Pigging) for Water
Mains". Russell Technologies have a range of in-line inspection tools based  on RFT, including wire line,
free swimming, walk through  and collapsible  tools. He estimated, based on replacement cost of $150/ft,
the inspection cost was 10% of replacement. This included the clients cost with the investigation portion
accounting for 40%  of the ILI  cost which equated to 4% of replacement.  The tool averaged some 1,800 ft
a day of inspection with access to the operating mains through hydrants.

Some of the concerns and the  solutions were:

        •   Internal pipe scale - solved by use of a soft foam pig
        •   Red water - solved by a 20 min flush after using tool
        •   Plugged customers filters - not a problem if customers did not use water during inspection
        •   Lost/stuck tools - very occasional and had to be dug up to recover.

Some unexpected findings were:
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        •   Pipelines with graphitized through-holes that had not leaked

        •   DIP had commonly a band of corrosion 3 ft back from bell end which was traced to poor
           coating adherence during manufacture

        •   Corrosion hot spots were found near un-insulated copper services

        •   Long lengths of CI and DI scheduled for replacement with almost no visible corrosion.

Dave Russell wound up by confirming that tools and technologies were available for ILL The "See
Snake" is a remote RFT tool for diameters up to 14" with potential for larger diameters if there is a
demand.

The final presentation was by Edgar Smith  of USAGE Engineering Research Development Center
"Sensor Enabled Water Quality and Corrosion Degradation Assessment Systems for Water Distribution
Networks". His presentation focussed on detection of water quality and corrosion monitoring by the use
of wireless sensors. These included corrosion rate sensors,  HACK Pipe-Sonde water quality sensors. The
use of dynamic modelling and the integration of sensors and models  in support of water distribution
networks were discussed.  The use of permanently installed leak detection systems was illustrated. The
vision was that tying these tools together could provide a "smart" utility network.

Discussion on emerging technologies brought a variety of points.

One  speaker believed that there were plenty of tools that a  utility can use in inspecting its mains. However
the increase in use is very small compared to what it should be.  The  limitations are not due to the lack of
technology but the lack of incentive for utilities. He suggested that the barriers were institutional because
of the way utilities are organized, operated, and regulated.  The utilities needed to look at the rates they
are setting as the income is insufficient to cover the basic level of service.

One  vendor continued the theme from his experience working in two different markets - U.S. and U.K.
In U.K. he had found great interest from utilities who he termed "technology adaptors" as they were
seeking technical solutions in their work. In the U.S., the level of interest is very specific to individual
utilities. His company found that utilities will carry out leak detection so by coupling condition
assessment they are carrying out projects where almost the condition information is  seen as an add-on
thrown in.

One  speaker considered that one potentially exciting development was the use of fibre optics in the pipe
and the potential to provide both the condition of the pipe and the stress in the pipe.

There are fundamental characteristics and limitations to the basic technologies employed in in-line tools
which need to be understood for any development together with cost implications for internal inspection
in operational water mains. It was also recognized that there were both economic and technical barriers to
inspection, not only in the ability of tools to detect cracks and corrosion but also the cost and difficulties
associated with both internal and external inspections.

The group discussed ideas for motivating the utilities to improve their inspection practices, including
possibly bringing together a group of utilities to develop a  guaranteed minimum work program for
condition assessment and condition inspection. One of the problems of U.S. water utilities is the
fragmentation so that very few have the length of pipeline to justify the high mobilization cost for
condition inspection. Such a minimum program of inspection would be attractive to the vendors due to  a
steady flow of work over an extended period and would offer cost-benefit to the participating utilities.
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The point was made that inspection technologies are most effective on pipelines with good records on
construction, maintenance, failure and repair. This information will focus inspection and lead to the
greatest cost-benefit.

The cost of an inspection must be kept low, an acceptable fraction of the replacement cost.  Otherwise,
utilities will consider it to be more cost effective to execute a scheduled replacement program.  Utilities
that do not keep detailed records  often find this to be the most effective approach.

B.7        Technology Demonstration

Bruce Nestleroth of Battelle opened the session with "EPA Technology Field Demonstrations:
Protocols/Metrics/Site Selection." He laid out a framework with possible types and goals of the EPA
technology demonstrations, including both controlled-condition and field demonstrations of established
and new technologies.  He highlighted the pros and cons of controlled demonstrations and field
demonstrations. Controlled demonstrations assess performance of inspection technologies on a full range
of anomaly types and sizes. Field demonstrations assess implementation variables and evaluate a few
anomalies that happen to be present. He then talked about the needs which included input and
contribution from stakeholder groups, water utilities, and inspection vendors.

The final paper was by Rob Pennington of COM with "Controlled Condition Assessment Needs." Under
Task Order 64 CDM had the task of looking at "Controlled - Condition Research on Wastewater
Collection and Drinking Water Distribution Systems." The scope included evaluating EPA's Edison
Pipeline Test Apparatus (EPTA)  facility in Edison, New Jersey, and preparing a design basis and
preliminary designs of controlled-condition testing needs. This was to cover all types of gravity and
pressure pipe assessment and also pipe rehabilitation.  Eleven pipe assessment situations along with four
pipe rehabilitation needs for both pressure and gravity pipe were identified.

During the discussion, comments came from all sides of the floor and particularly vendors that it was
important to simulate real life defects.  Experience was that simulated defects in test facilities were not
representative of real life defects  and would not be found by technologies which were structured to find
actual defects.

There was concern on the range of defects, conditions, and inspection technologies. It would be very
difficult to cover the whole range in a control testing facility or at best would be exorbitantly expensive.
It was pointed out that a loop format was not suitable for leak detecting technologies.

It was also pointed out that vendors already have substantial experience and validation of inspection
findings. They didn't feel that they had to prove their technologies by doing tests in a simulated facility.
They felt that it would be more beneficial to find ways to validate their technologies on real pipes.

Utility representatives were lukewarm on the value of controlled testing. They suggested that it would
not make much difference to utilities in changing their demand for inspection. In their view,
demonstrations that are conducted on real pipes that have similarities to their own are more likely to
stimulate interest and provide more benefit.

The involvement of utilities is a key to the success of technology demonstration. A survey should be
conducted to determine the level  of interest of the utilities. One suggestion was for EPA to subsidize
utilities' pilot studies by collecting supplementary data.
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LWC offered a 2,450-ft long, 24-in. 1933 cast iron main for use by the EPA technology demonstration.
Competing vendors could inspect the same pipeline where practical to allow a direct comparison to be
made.

B.8        Recommendations - "Top 10 Findings" from TO 62 Forum

        1.  Leakage management. Leak detection and mitigation provides the biggest bang for the
           buck. With the reported six billion gallons of water loss out of 40 billion gallons extracted
           daily, even a 20 percent reduction would achieve massive environmental benefits and cost
           savings. Recent advances in leak detection and location technologies provide utilities with
           tools and methods to reduce leakage. However, without regulatory pressure, there is little
           incentive for many utilities to implement leak reduction programs. EPA should consider: (a)
           if there is any existing requirement that can be utilized to audit utility performance; and (b)
           setting rules with specific leakage targets. For example, Washington's Water Use Efficiency
           Rule requires all municipal water suppliers to maintain their distribution system leakage at or
           below 10 percent of their production (http://www.doh.wa.gov/ehp/dw/Programs/wue.htm).
           EPA could also undertake programs to demonstrate the technical and economic feasibility
           and value of reducing leakage.

        2.  Data collection and management. A general  consensus among the participants is that there
           is insufficient data collection and management by utilities.  For example, few water utilities
           collect data on main breaks/burst/failure/repair events and there are no standardized protocols
           for documenting, storing, and managing the data. Since the UKWIR mains break database
           has been proven useful and workable in the U.K., the adoption of this database by the U.S.
           will provide considerable value to water utilities and the researchers by improving
           understanding of the type and distribution of failure modes  and mechanisms, and this
           information can be used to support better decisions regarding pipe selection, installation,
           inspection, service-life prediction, and technology development.  Water Research Foundation
           is currently assessing the adaptability of the UKWIR database to the U.S. utilities.  EPA
           should consider supporting this initiative.

        3.  Barriers to effective condition assessment. From the utilities' perspective, there are plenty
           of effective tools in  providing the level of information required. It is not unusual to find that
           a utility will use an  ineffective method because it is low cost.  There is some slight increase  of
           interest and usage for condition assessment.  However, the real incentives are not there for the
           utilities to conduct condition assessment.  The limitations are not due to lack of technologies.
           The limitations are institutional, which is the real barrier. Water rates need to reflect cost of
           production and delivery.

        4.  Technology demonstration. There is a strong desire for EPA to subsidize field trials of
           inspection technologies.  LWC offers an immediate opportunity: a 2,450-ft long, 24-in. 1933
           vintage cast iron main will be removed and replaced in August 2009. This section of main
           can be used for testing of multiple leak detection and inspection technologies.  At the time of
           finalizing this State  of Technology Review Report, EPA has provided funding  to plan, setup,
           monitoring, verifying, and reporting such field  tests. For large-scale demonstrations at
           multiple locations, a questionnaire should be sent to major cities to solicit their interest in
           participation. The survey should be developed to reflect utility concerns and reasons why
           they should participate and any potential benefits from participation.

        5.  Controlled-condition testing. Water utilities and vendors were generally unconvinced that a
           controlled-condition testing facility for condition assessment technologies would provide
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    substantial benefits.  A key limitation is that controlled-condition testing is not equivalent to
    real-world, field demonstration.  Field demonstrations also have limitations, e.g., cost, risk,
    complexity, and repeatability.  However, should a controlled-condition test facility be
    determined viable, utilities are willing to provide pipe samples for testing.  Further evaluation
    of potential controlled-condition testing needs was recommended.  Another function for the
    EPA PTA facility in Edison, NJ would be to keep an inventory of pipe samples, perform
    forensic examinations of various pipe failures for all pipe types, and maintain a database of
    forensic analysis.

6.   Predictive models.  Much work has been done on the prediction of residual life. An
    extensive evaluation of the effectiveness of these models and their extent of use by utilities,
    engineers, and consultants, would be valuable. Some existing curves and models need to be
    changed to reflect local conditions such as soil parameters and support. For example, the
    relationship of local  soil conditions and the corrosion of unprotected CIP should be taken into
    account.  Lack of soil support, often coupled with increased external loadings, may be
    another local factor that can modify life expectancy curves. A general consensus is that any
    index or model development should be simple to understand, transparent to the users, and
    easy to implement.

7.   Definition of terms. There is lack of proper definitions in the water industry for terms like
    leak, break, failure, condition curves, condition assessment, etc.  A consensus needs to be
    reached among research organizations such as Water Research Foundation, WERF, EPA,
    NRC, UKWIR and others so that there is a common vocabulary and understanding of
    alternative terms for the same thing.

8.   Emerging technologies.  Condition assessment and inspection technologies for existing pipe
    are important, but emerging technologies should also be considered for enabling condition
    assessment for future pipe design and installation (for example, embedded sensor,  micro-
    chip, wireless technologies, etc.).

9.   Value of inspection. More in-depth studies should be conducted on the value of inspection
    in relation to asset value for different diameter and types of pipes. This could go hand in
    hand with alternative ways of condition assessment for smaller diameter pipes and justify the
    use of NDT inspection tools.

10. Need for condition  assessment  guidance.  Provide utilities a basic synthesis of the extensive
    knowledge on pipe failures - cause and symptoms, the means to detect them, and basic
    information about leak detection, condition inspection, and prediction methods.  Some efforts
    (e.g., WERF et al., SAM Challenge program) are underway to address this need. It will be
    necessary to update the guidance as improvements occur in micro-  and macro- level
    understanding of pipe failure; pipe materials, liners, and coatings; and data collection and
    analysis methods.
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